The URL can be used to link to this page

Browse Search

Home My WebLink About20151694.tiff A COPHE COLORADO CO m Department of Public Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 11500 St PO Box 758 Greeley, CO 80632 CCE j 11 Y June 2, 2015 C JUN 082015 WELD COUNTY Dear Sir or Madam: COMMISSIONERS On June 3, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company, LLC - Pronghorn 11-14-12HZ. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health a Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, — Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure R 4 U(tOZ5 44 t1t kli 2015-1694 .• . .- . ,(_;;,,-,:‘ ..„..,. : -'4•‘ 4300 Cherry Creek Drive S., Denver, Co 80246.1530 P 303-692-2000 www.colorado.govicdphe I r c John W. Hickenlooper. Governor j Larry Wolk, MD,MSPH, Executive Director and Chief Medical Officer , A CDPHE Air Pollution Control Division CO Notice of a Proposed Project or Activity Warranting Public ' Comment Website Title: Bonanza Creek Energy Operating Company, LLC - Pronghorn 11-14-12HZ - Weld County Notice Period Begins: June 3. 2015 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company, LLC Facility: Pronghorn 11-14-12HZ Oil and gas exploration and production facility NWNW Sec 12 T5N R61W Weld County The proposed project or activity is as follows: Source proposes to operate a new oil and gas exploration and production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 12WE2454.CP3 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division wilt receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1 I AV 7..R4'C v s STATE OF COLORADO t pF Cp COLORA 6 DEP RTM NT OF PU LIC HEALTH AND ENVIRONMENT ra AIR POLLUTION CONTROL DIVISION ° TELEPHONE: (303)692-3150 1896 CONSTRUCTION PERMIT PERMIT NO: 1 2WE24554 Issuance 3 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 Pronghorn 11-14-12HZ Production Facility, located in the NWNW Section 12, Township 5N, Range 61W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Paint Description ID Five (5)400 bbl above ground atmospheric condensate CNDTK-1 001 storage tanks controlled by two enclosed flares. Each flare has a minimum control efficiency of 95%. One (1)400 bbl above ground produced water storage tank PW 002 controlled by two enclosed flares. Each flare has a minimum control efficiency of 95%. One (1)Arrow, Model A-62, Serial Number 6B11H015959, natural gas-fired, naturally aspirated, 4SRB reciprocating El 003 internal combustion engine, site rated at 80 horsepower at 1800 RPM. This engine shall be equipped with a non- selective catalytic reduction (NSCR) system and air-fuel ratio control. This emission unit is used for a pump jack Hydrocarbon Loadout to Tanker Trucks. Loadout is controlled by using dedicated vapor balance service and two enclosed TLO 004 flares. Collection system is 70% efficient and each flare has a minimum control efficiency of 95%. Overall control efficiency is 66.5%. One (1) pneumatic water transfer pump, rated at 600 scf/hr P-1 006 (Sandpiper, Model G1F, Serial number 19811466). The pneumatic pump is controlled by two enclosed flares. Each flare has a minimum control efficiency of 95%. AIRS ID: 123/99E1 Page 1 of 24 olor Depa en P li ealth and Environment it Pollution Control Division Facility AIRS Equipment Point Description ID One (1) pneumatic heat trace pump, rated at 600 scf/hr P-2 007 (Sandpiper, Model G1F, Serial number 19811470). The pneumatic pump is controlled by two enclosed flares. Each flare has a minimum control efficiency of 95%. SEP-1 & Two low-pressure separators controlled by two enclosed SEP-2 011 flares during VRU downtime. Each flare has a minimum control efficiency of 95%. One emergency flare used to combust separator gas during FL-2 013 emergencies or when the pipeline is not available. Flare has a minimum control efficiency of 95%. The flare is not enclosed. Point 003: This engine may be replaced with another engine in accordance with the temporary engine replacement provision or with another Arrow A-62 engine in accordance with the permanent replacement provision of the Alternate Operating Scenario (AOS), included in this permit as Attachment A. Points 006 and 007: Each pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et sec)), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. AIRS Point 013: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. AIRS Point 013: The following information shall be provided to the Division within fifteen (15) days after commencement of operation. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 3. AIRS Point 013: Within one hundred and eighty days (180) after commencement of operation, 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). AIRS ID: 123/99E1 Page 2 of 24 1'. 'olor • 4:Depa • eni T P .li " ealth and Environment rre. it Pollution Control Division sdtc SiNe� 4. AIRS Points 0f1 0a"' Yana T notie Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, I submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 5. AIRS Points 001, 002, 004, and 011: 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). 6. 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, Ill.F.4.) 7. AIRS Point 011: Within one hundred and eighty (180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from the low pressure separators. 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 one hundred and eighty (180) days after issuance of this permit. 8. 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.) 9. 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 10. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type x Equipment ID Point NO VOC CO CNDTK-1 001 --- 10.4 2.0 Point PW 002 0.5 Point El 003 2.2 3.7 Point TLO 004 0.7 Point AIRS ID: 123/99E1 Page 3 of 24 olor ;Depa en . P .li ealth and Environment A it Pollution Control Division P-1 .. �06 :` '....... '.. ' .4 Point P-2 007 --- 2.9 1.4 Point SEP-1 &SEP-2 011 --- 2.1 --- Point FL-2 013 --- 5.5 2.6 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. 11. 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 CNDTK-1 001 Enclosed Flare VOC PW 002 Enclosed Flare VOC El 003 Non-selective catalytic reduction (NSCR)system NOx and CO and air-fuel ratio control. TLO 004 Vapor balance and Enclosed Flare VOC P-1 006 Enclosed Flare VOC P-2 007 Enclosed Flare VOC SSEP 2 011 Enclosed Flare VOC FL-2 013 Open Rare VOC PROCESS LIMITATIONS AND RECORDS 12. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) AIRS ID: 123/99E1 Page 4 of 24 a w olora Depa en P li Health and Environment it Pollution Control Division Process/Con �r:n °r. a au Facility AIRS Equipment Point Process Parameter Annual Limit ID CNDTK-1 001 Condensate Throughput 74,460 BBL PW 002 Produced Water Throughput 78,840 BBL El 003 Consumption of natural gas as a fuel 6.31 MMscf/yr TLO 004 Condensate Loaded 74,460 BBL P-1 006 Natural Gas Consumed 5.3 MMSCF P-2 007 Natural Gas Consumed 5.3 MMSCF SEP-1 & Total Gas Vented from All High/Low- 1.4 MMSCF SEP-2 011 Pressure Separators during VRU Downtime FL-2 013 Total Gas Vented from All Separators to 10.0 MMSCF Emergency Flare 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. 13. AIRS Point 011: Upon installation of the flow meter required under Condition 7, The owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from all low pressure separators during VRU downtime using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented to the enclosed flares from all low-pressure separators during VRU downtime. The owner or operator shall use monthly throughput records and calculation methods detailed in the O&M Plan to demonstrate compliance with the limits specified in Condition 12 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 14. 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) 15. Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.2.b shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 5.) 16. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 17. AIRS Point 001: 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: 123/99E1 Page 5 of 24 0lorlDepa en P eli ealth and Environment .ik -it Pollution Control Division 18. AIRS Point 0' r,:: _`so is t ter= - rdke =. monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 19. AIRS Point 001: 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. 20. AIRS Points 001, 002, and 011: The flare(s) covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: XVII.B.2.b If a combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. XVII.B.2.d Auto-igniters: All combustion devices used to control emissions of hydrocarbons must be equipped with and operate an auto-igniter as follows: XVII.B.2.d.(i)All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device. 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. 21. AIRS Points 001 and 002: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. XVII.C.1.b.(i)(a) Control requirements of Section XVII.C.1.b. must be achieved within ninety (90) days of the date that the storage tank commences operation. XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section XVII.C.1.b.(i), whichever comes later, owners or operators of storage tanks subject to Section XVII.C.1. must conduct audio, visual, olfactory ("AVO") and additional visual inspections of the storage tank and any associated equipment (e.g. separator, air pollution control equipment, or other pressure reducing AIRS ID: 123/99E1 Page 6 of 24 Eyehl ,qy t'Rs�x 'i A Pn PPolor Depa en P .lic°iHealth and Environment air Pollution Control Division I sag • �s equip =a'F"the e a tency #ts- as ds ar -ded out from the storage tank. These inspections are not required more frequently than every seven (7) days but must be conducted at least every thirty one (31) days. Monitoring is not required for storage tanks or associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i) Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; XVII.C.1.d.(ii) Visual inspection or monitoring of the air pollution control equipment to ensure that it is operating, including that the pilot light is lit on combustion devices used as air pollution control equipment; XVII.C.1.d.(iii) If a combustion device is used, visual inspection of the auto-igniter and valves for piping of gas to the pilot light to ensure they are functioning properly; XVII.C.1.d.(iv) Visual inspection of the air pollution control equipment to ensure that the valves for the piping from the storage tank to the air pollution control equipment are open; and XVII.C.1.d.(v) If a combustion device is used, inspection of the device for the presence or absence of smoke. If smoke is observed, either the equipment must be immediately shut-in to investigate the potential cause for smoke and perform repairs, as necessary, or EPA Method 22 must be conducted to determine whether visible emissions are present for a period of at least one (1) minute in fifteen (15) minutes. XVII.C.1.e. If storage tanks or associated equipment is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor such equipment until it becomes feasible to do so. XVII.C.2. Capture and monitoring requirements for storage tanks that are fitted with air pollution control equipment as required by Sections XII.D. or XVI I.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. AIRS ID: 123/99E1 Page 7 of 24 olor Depa en . PMI•li ealth and Environment •it Pollution Control Division XVII.C _, , - T ' lud d co __::: technologies, monitoring practices, operational practices, and/or other strategies; procedures for evaluating ongoing storage tank emission capture performance; and monitoring in accordance with approved instrument monitoring methods following the applicable schedule in Section XVII.C.2.b.(ii) and Inspection Frequency in Table 1. XVII.C.2.b.(ii) Owners or operators must achieve the requirements of Sections XVII.C.2.a. and XVII.C.2.b. and begin implementing the required approved instrument monitoring method in accordance with the following schedule: XVII.C.2.b.(ii)(a) A storage tank constructed on or after May 1, 2014, must comply with the requirements of Section XVII.C.2.a. by the date the storage tank commences operation. The storage tank must comply with Section XVII.C.2.b. and implement the approved instrument monitoring method inspections within ninety (90) days of the date that the storage tank commences operation. XVII.C.2.b.(ii)(d) Following the first approved instrument monitoring method inspection, owners or operators must continue conducting approved instrument monitoring method inspections in accordance with the Inspection Frequency in Table 1. Table 1 —Storage Tank Inspections Threshold: Storage Tank Approved Instrument Phase-In 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 AIRS ID: 123/99E1 Page 8 of 24 a., olor rEDepar en of P. li ealth and Environment it Pollution Control Division mainta , "s !an . red g andAlinake them available to the Division upon request, including: XVII.C.3.a. The AIRS ID for the storage tank. XVII.C.3.b. The date and duration of any period where the thief hatch, pressure relief device, or other access point are found to be venting hydrocarbon emissions, except for venting that is reasonably required for maintenance, gauging, or safety of personnel and equipment. XVII.C.3.c. The date and duration of any period where the air pollution control equipment is not operating. XVII.C.3.d. Where a combustion device is being used, the date and result of any EPA Method 22 test or investigation pursuant to Section XVII.C.1.d.(v). XVII.C.3.e. The timing of and efforts made to eliminate venting, restore operation of air pollution control equipment, and mitigate visible emissions. XVII.C.3.f. A list of equipment associated with the storage tank that is designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.C.1.e., an explanation stating why the equipment is so designated, and the plan for monitoring such equipment. 22. 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) 23. 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 23 (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. 24. 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. 25. AIRS Points 011 and 013: The separation equipment, including low pressure separators, covered by this permit is subject to Regulation 7, Section XVII.G emission control requirements (State Only). On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. AIRS ID: 123/99E1 Page 9 of 24 olor Depa en P li ealth and Environment it Pollution Control Division 26. AIRS Point 0 e n ives om the separators during emergencies, is an approved alternative emissions control equipment per Regulation No. 7, Section XVII.B.2.e. The emergency flare shall comply with all applicable requirements in Regulation No. 7, Section XVII.B General Provisions (State only enforceable), except the flare is not required to be enclosed. OPERATING & MAINTENANCE REQUIREMENTS 27. Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) 28. AIRS Point 004: The owner or operator of a loadout at which vapor balancing is used to control emissions shall: a. Install and operate the vapor collection and return equipment to collect vapors during loading of tank compartments of outbound transport trucks and return these vapors to the stationary source storage tanks. b. Include devices to prevent the release of vapor from vapor recovery hoses not in use. c. Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. d. Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. e. Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. f. Inspect pressure relief devices (PRD) annually for proper operation and replace as necessary. PRDs shall be set to release at a pressure that will ensure flashing, working and breathing losses are routed to the control device under normal operating conditions. g. Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. COMPLIANCE TESTING AND SAMPLING Periodic Testing Requirements 29. AIRS Point 003: This engine is subject to the periodic testing requirements as specified in the operating and maintenance (O&M) plan as approved by the Division. Revisions to your O&M plan are subject to Division approval. Replacements of this unit completed as Alternative Operating Scenarios may be subject to additional testing requirements as specified in Attachment A. ALTERNATE OPERATING SCENARIOS 30. AIRS Points 006 and 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. AIRS ID: 123/99E1 Page 10 of 24 «-v arsav 1 Itolor Depa endf Pli ealth and Environment e qir Pollution Control Division i aR 31. AIRS Points 0 00 , h paa r shaltatain 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. 32. AIRS Points 006 and 007: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 33. All previous versions of this permit are cancelled upon issuance of this permit. 34. This permit replaces the following permits and/or points, which are cancelled upon issuance of this permit. Existing Existing Permit No. Emission Point New Permit No. GP01 123/99E1/001 12WE2454 Issuance 3 GP05 123/99E1/002 12WE2454 Issuance 3 35. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30`" whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (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. f. Within 14 calendar days of commencing operation of a permanent replacement engine under the alternative operating scenario outlined in this permit as AIRS ID: 123/99E1 Page 11 of 24 olor epa en P t.li ealth and Environment •it Pollution Control Division ;r Attach , . T P II - e sp L manufacturer, model and serial number and horsepower of the permanent replacement engine, the appropriate APEN filing fee and a cover letter explaining that the owner or operator is exercising an alternative-operating scenario and is installing a permanent replacement engine. 36. Federal regulatory program requirements (i.e. PSD, NANSR)shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 37. 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. 38. 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. 39. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 40. 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. 41. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. AIRS ID: 123/99E1 Page 12 of 24 • �1 olora$ Depar`aent'6f PpliSHealth and Environment i \ir Pollution Control Division 1b as 42. Section 25-7-14!& 42. a),,—t S TMq fres urces•c, sired 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. 43. 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 I Description Issuance 3 This Issuance I Modification to convert AIRS Point 001 from GP01 to this permit. Also added tanks, increased throughput and emissions. Modification to convert Point 002 from GP05 to this permit. Also add tank, increase throughput, and increase emissions. Modification to Point 004 to increase throughput and emissions and to add control. Cancellation of Point 005. Modification to Points 006 and 007 to increase emissions. Adding new points 011 and 013. Issuance 2 8/20/2014 Add pneumatic pumps (006 and 007)to permit. Issuance 1 4/11/2013 Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/99E1 Page 13 of 24 • IIolor ,rDepa en . P »li ealth and Environment °f •it Pollution Control Division s Notes to Permit Holder ' -' me o ` ' .e ' ' '" a '-. 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Mai n%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 3,871 Yes 194 n-Hexane 110543 21,765 Yes 1,088 Toluene 108883 3,296 Yes 165 001 Ethylbenzene 100414 495 Yes 25 Xylenes 1330207 1,305 Yes 65 2,2,4- 540841 2,084 Yes 104 trimethylpentane Benzene 71432 552 Yes 28 002 n-Hexane 110543 1,735 Yes 87 Formaldehyde 5000 119 No 119 Methanol 67561 18 No 18 Acetaldehyde 75070 16 No 16 003 Acrolein 107028 15 No 15 Benzene 71432 9 No 9 1,3-Butadiene 106990 4 No 4 Toluene 108883 3 No 3 Benzene 71432 39 No 13 004 n-Hexane 110543 391 Yes 131 AIRS ID: 123/99E1 Page 14 of 24 . olora: Depart enru-f Ptolic-Health and Environment _ �l � . �„ 1 g it Pollution Control Division jiilin+ I Rrtl �l tiro x ' y g Tole Yky=m``::> "f# 8 P4 'slat 'Mlw 12 Xylenes 1330207 7 No 2 Benzene 71432 235 No 12 n-Hexane 110543 1,725 Yes 86 Toluene 108883 210 No 11 006 Ethylbenzene 100414 55 No 3 Xylenes 1330207 92 No 5 2,2,4- 540841 223 No 11 trimethylpentane Benzene 71432 235 No 12 n-Hexane 110543 1,725 Yes 86 Toluene 108883 210 No 11 007 Ethylbenzene 100414 55 No I3 Xylenes 1330207 92 No 5 2,2,4- 540841 223 No 11 trimethylpentane Benzene I 71432 291 Yes 15 n-Hexane 110543 2,071 Yes 104 Toluene 108883 291 Yes 15 011 Ethylbenzene 100414 105 No 5 Xylenes 1330207 169 No 8 2,2,4- 540841 329 Yes 16 trimethylpentane Benzene 71432 447 Yes 22 I n-Hexane 110543 3,281 Yes 164 Toluene 108883 400 Yes 20 013 Ethylbenzene 100414 105 No 5 Xylenes Ali 1330207 175 No 9 2,2,4- 540841 424 Yes 21 trimethylpentane 5) The emission levels contained in this permit are based on the following emission factors: Point 001: Uncontrolled Controlled Ib/BBL lb/BBL Condensate Condensate Pollutant Throughput Throughput Source VOC 5.6052 0.2803 Promax n-Hexane 0.2923 0.0146 Promax Benzene 0.0520 0.0026 Promax AIRS ID: 123/99E1 Page 15 of 24 „t olor .Depa en . P .II ealth and Environment ' I it Pollution Control Division a' lb/BBL Ib/BBL . Condensate Condensate Pollutant Throughput Throughput Source Toluene 0.0443 0.0022 Promax Ethylbenzene 0.0066 0.0003 Promax Xylenes 0.0175 0.0009 Promax 2,2,4- 0.0280 0.0014 Promax trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. A HHV of 2,691 BTU/scf was used for combustion calculations. Point 002: Uncontrolled Controlled lb/BBL Produced lb/BBL Produced Pollutant Water Throughput Water Throughput Source VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 003: Emission Factors- Emission Factors— Uncontrolled Controlled CAS Pollutant lb/MMBtu g/bhp-hr lb/MMBtu g/bhp-hr NOx 3.9197 14.7000 0.7447 2.7930 CO 1.5465 5.8000 1.2836 4.8140 VOC 0.0107 0.0400 NA NA 71432 Benzene 0.0016 0.0059 NA NA Emission factors are based on a Brake-Specific Fuel Consumption Factor of 8268 Btu/hp-hr, a site-rated horsepower value of 80, and a fuel heat value of 918 Btu/scf. Emission Factor Sources: CAS Pollutant Uncontrolled EFSource Controlled EF Source NOx Manufacturer NSCR CO Manufacturer NSCR VOC Manufacturer No Control 5000 Formaldehyde AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 67561 Methanol AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 75070 Acetaldehyde AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 107028 Acrolein AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 71432 Benzene AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 106990 1,3-Butadiene AP-42; Table 3.2-3 No Control (7/2000); Natural Gas 108883 Toluene AP-42; Table 3.2-3 No Control (7/2000); Natural Gas AIRS ID: 123/99E1 Page 16 of 24 �r 1 tolora ! Depari en IIi P ealth and Environment ff L Air Pollution Control Division 52 �`— , itLa,-1,,, *ttR Au,,,,,h di a "A 1 3.. Point 004: sea Uncontrolled Controlled Pollutant Ib/BBL loaded Ib/BBL loaded Source VOC 0.0550 0.0184 AP-42 Benzene 0.0005 0.0002 AP-42 n-Hexane 0.0053 0.0018 AP-42 Toluene 0.0005 0.0002 AP-42 Xylenes 0.0001 0.00003 AP-42 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 = 1 (Submerged loading: dedicated vapor balance service) P (true vapor pressure)=0.89 psia M (vapor molecular weight) =64.52 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. Points 006 and 007: Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO (Ib/MMBTU) 0.37 0.37 AP-42 VOC 22,100 1,105.0 Gas Analysis Benzene 44.680 2.2340 Gas Analysis n-Hexane 328.12 16.406 Gas Analysis Toluene 40.013 2.0006 Gas Analysis Ethylbenzene 10.501 0.5250 Gas Analysis Xylenes 17.515 0.8757 Gas Analysis 2,2,4- 42.417 2.1209 Gas Analysis trimethylpentane 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 1,403 BTU/scf was used for combustion calculations. Point 011: Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas (°/0) Uncontrolled Controlled lb/MMscf lb/MMscf _ - NOx(lb/MMBTU) --- 0.068 0.068 AP-42 CO (Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 63.6 58,653 2,932.6 Gas Analysis Benzene 0.23 208.18 10.409 Gas Analysis Toluene 0.23 208.13 10.406 Gas Analysis Ethylbenzene 0.08 75.075 3.7538 Gas Analysis Xylenes 0.13 120.46 6.0228 Gas Analysis AIRS ID: 123/99E1 Page 17 of 24 ll olor DDepa en . P »li " ealth and Environment •Ir Pollution Control Division h Pollutant Fraction Factors Factors Source of Gas(°/0) Uncontrolled Controlled lb/MMscf lb/MMscf n-hexane 1.61 1,480.3 74.015 Gas Analysis 2,2,4- 0.26 235.39 11.770 trimethylpentane Gas Analysis Note: The uncontrolled VOC and HAP emissions were calculated based on low pressure separator gas sample collected 10/7/2014 from Pronghorn K-O-12HNB to estimate the VOC and HAP content of the stream. Stream flow is based on a Promax model and applying 20% safety factor. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,975 BTU/scf was used for calculations. Point 013: Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx(lb/MMBTU) --- 0.068 0.068 AP-42 CO (Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 33.9 22,099 1,105.0 Gas Analysis Benzene 0.07 44.685 2.2343 Gas Analysis Toluene 0.06 40.017 2.0009 Gas Analysis Ethylbenzene 0.02 10.501 0.5250 Gas Analysis Xylenes 0.03 17.515 0.8757 Gas Analysis n-hexane 0.50 328.12 16.406 Gas Analysis 2,2,4- 0.07 42.421 2.1210 Gas Analysis trimethylpentane Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,403 BTU/scf was used for 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) Point 003: This engine is subject to 40 CFR, Part 60, Subpart JJJJ—Standards of Performance for Stationary Spark Ignition Internal Combustion Engines (See January 18, 2008 Federal Register posting —effective March 18, 2008). This rule has not yet been incorporated into Colorado Air Quality Control Commission's Regulation No. 6. A copy of the complete subpart is available on the EPA website at: http://www.epa.gov/ttn/atw/area/fr18ia08.pdf 8) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC, n-hexane AIRS ID: 123/99E1 Page 18 of 24 5 olora t Depaijien!if P licfiealth and Environment a� ir Pollution Control Division i 4, r s NANSR u<,a:�eyntf, tica Mt Fu Urceu n gab* m `sw VOC 9) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 163.1-63.599 I Subpart A—Subpart Z MACT 63.600-63.1199 I 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 10) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/99E1 Page 19 of 24 olor Depa en PE.li ' ealth and Environment •it Pollution Control Division ATTACHMENT A: ALTERNATIVE OPERATING SCENARIOS RECIPROCATING INTERNAL COMBUSTION ENGINES October 12, 2012 2.Alternative Operating Scenarios The following Alternative Operating Scenario (AOS) for the temporary and permanent replacement of natural gas fired reciprocating internal combustion engines has been reviewed in accordance with the requirements of Regulation No. 3., Part A, Section IV.A, Operational Flexibility-Alternative Operating Scenarios, Regulation No. 3, Part B, Construction Permits, and Regulation No. 3, Part D, Major Stationary Source New Source Review and Prevention of Significant Deterioration, and it has been found to meet all applicable substantive and procedural requirements. This permit incorporates and shall be considered a Construction Permit for any engine replacement performed in accordance with this AOS, and the owner or operator shall be allowed to perform such engine replacement without applying for a revision to this permit or obtaining a new Construction Permit. 2.1 Engine Replacement The following AOS is incorporated into this permit in order to deal with a compressor engine breakdown or periodic routine maintenance and repair of an existing onsite engine that requires the use of either a temporary or permanent replacement engine. "Temporary" is defined as in the same service for 90 operating days or less in any 12 month period. "Permanent" is defined as in the same service for more than 90 operating days in any 12 month period. The 90 days is the total number of days that the engine is in operation. If the engine operates only part of a day, that day shall count as a single day towards the 90 day total. The compliance demonstrations and any periodic monitoring required by this AOS are in addition to any compliance demonstrations or periodic monitoring required by this permit. All replacement engines are subject to all federally applicable and state-only requirements set forth in this permit(including monitoring and record keeping). The results of all tests and the associated calculations required by this AOS shall be submitted to the Division within 30 calendar days of the test or within 60 days of the test if such testing is required to demonstrate compliance with NSPS or MACT requirements. Results of all tests shall be kept on site for five(5)years and made available to the Division upon request. The owner or operator shall maintain a log on-site and contemporaneously record the start and stop date of any engine replacement, the manufacturer, date of manufacture, model number, horsepower, and serial number of the engine(s) that are replaced during the term of this permit, and the manufacturer, model number, horsepower, and serial number of the replacement engine. In addition to the log, the owner or operator shall maintain a copy of all Applicability Reports required under section 2.1.2 and make them available to the Division upon request. 2.1.1 The owner or operator may temporarily replace an existing compressor engine that is subject to the emission limits set forth in this permit with an engine that is of the same manufacturer, model, and horsepower or a different manufacturer, model, or horsepower as the existing engine without modifying this permit, so long as the temporary replacement engine complies with all permit limitations and other requirements applicable to the existing engine. Measurement of emissions from the temporary replacement engine shall be made as set forth in section 2.2. AIRS ID: 123/99E1 Page 20 of 24 arm, a Fil 4 v oloral'.Depaitnent of PI lic ealth and Environment it Pollution Control Division Nlii mziantr ,_y *a aim say waive 2.1.2 The owner or operator may permanently replace the existing compressor engine with another engine with the same manufacturer, model, and horsepower engines without modifying this permit so long as the permanent replacement engine complies with all permit limitations and other requirements applicable to the existing engine as well as any new applicable requirements for the replacement engine. Measurement of emissions from the permanent replacement engine and compliance with the applicable emission limitations shall be made as set forth in section 2.2. An Air Pollutant Emissions Notice (APEN) that includes the specific manufacturer, model and serial number and horsepower of the permanent replacement engine shall be filed with the Division for the permanent replacement engine within 14 calendar days of commencing operation of the replacement engine. The APEN shall be accompanied by the appropriate APEN filing fee, a cover letter explaining that the owner or operator is exercising an alternative operating scenario and is installing a permanent replacement engine, and a copy of the relevant Applicability Reports for the replacement engine. Example Applicability Reports can be found at http://www.cdphe.state.co.us/ap/oilgaspermitting.html. This submittal shall be accompanied by a certification from the Responsible Official indicating that"based on the information and belief formed after reasonable inquiry, the statements and information included in the submittal are true, accurate and complete". This AOS cannot be used for permanent engine replacement of a grandfathered or permit exempt engine or an engine that is not subject to emission limits. The owner or operator shall agree to pay fees based on the normal permit processing rate for review of information submitted to the Division in regard to any permanent engine replacement. 2.2 Portable Analyzer Testing Note: In some cases there may be conflicting and/or duplicative testing requirements due to overlapping Applicable Requirements. In those instances, please contact the Division Field Services Unit to discuss streamlining the testing requirements. Note that the testing required by this Condition may be used to satisfy the periodic testing requirements specified by the permit for the relevant time period (i.e. if the permit requires quarterly portable analyzer testing, this test conducted under the AOS will serve as the quarterly test and an additional portable analyzer test is not required for another three months). The owner or operator may conduct a reference method test, in lieu of the portable analyzer test required by this Condition, if approved in advance by the Division. The owner or operator shall measure nitrogen oxide (NOX) and carbon monoxide (CO) emissions in the exhaust from the replacement engine using a portable flue gas analyzer within seven (7) calendar days of commencing operation of the replacement engine. All portable analyzer testing required by this permit shall be conducted using the Division's Portable Analyzer Monitoring Protocol (ver March 2006 or newer)as found on the Division's web site at: http://www.colorado.qov/cs/Satellite/C D PH E-AP/CBON/1251596520270. Results of the portable analyzer tests shall be used to monitor the compliance status of this unit. For comparison with an annual (tons/year)or short term (lbs/unit of time) emission limit, the results of the tests shall be converted to a lb/hr basis and multiplied by the allowable operating hours in the month or year(whichever applies) in order to monitor compliance. If a source is not limited in its hours of operation • AIRS ID: 123/99E1 Page 21 of 24 olor Depa en P .li `' ealth and Environment •it Pollution Control Division the test results will be .,. „i syti •.x — • m;,h _ in th :e_thor year(8760), whichever applies. For comparison with a short-term limit that is either input based (lb/mmBtu), output based (g/hp-hr) or concentration based (ppmvd @ 15% O2) that the existing unit is currently subject to or the replacement engine will be subject to, the results of the test shall be converted to the appropriate units as described in the above-mentioned Portable Analyzer Monitoring Protocol document. If the portable analyzer results indicate compliance with both the NOX and CO emission limitations, in the absence of credible evidence to the contrary, the source may certify that the engine is in compliance with both the NOX and CO emission limitations for the relevant time period. Subject to the provisions of C.R.S. 25-7-123.1 and in the absence of credible evidence to the contrary, if the portable analyzer results fail to demonstrate compliance with either the NOX or CO emission limitations, the engine will be considered to be out of compliance from the date of the portable analyzer test until a portable analyzer test indicates compliance with both the NOX and CO emission limitations or until the engine is taken offline. 2.3 Applicable Regulations for Permanent Engine Replacements 2.3.1 Reasonably Available Control Technology(RACT): Reg 3, Part B § II.D.2 All permanent replacement engines that are located in an area that is classified as attainment/maintenance or nonattainment must apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is attainment/maintenance or nonattainment. Note that both VOC and NOX are precursors for ozone. RACT shall be applied for any level of emissions of the pollutant for which the area is in attainment/maintenance or nonattainment, except as follows: In the Denver Metropolitan PM10 attainment/maintenance area, RACT applies to PM10 at any level of emissions and to NOX and SO2, as precursors to PM10, if the potential to emit of NOX or SO2 exceeds 40 tons/yr. For purposes of this AOS, the following shall be considered RACT for natural gas fired reciprocating internal combustion engines: VOC: The emission limitations in NSPS JJJJ CO:The emission limitations in NSPS JJJJ NOX: The emission limitations in NSPS JJJJ SO2: Use of natural gas as fuel PM10: Use of natural gas as fuel As defined in 40 CFR Part 60 Subparts GG (§60.331) and 40 CFR Part 72 (§72.2), natural gas contains 20.0 grains or less of total sulfur per 100 standard cubic feet. 2.3.2 Control Requirements and Emission Standards: Regulation No. 7, Sections XVI. and XVII.E (State- Only conditions). Control Requirements: Section XVI Any permanent replacement engine located within the boundaries of an ozone nonattainment area is subject to the applicable control requirements specified in Regulation No. 7, section XVI, as specified below: Rich burn engines with a manufacturer's design rate greater than 500 hp shall use a non- selective catalyst and air fuel controller to reduce emission. AIRS ID: 123/99E1 Page 22 of 24 r� a joloravDepar' en &f Pt li ealth and Environment ° f � ir Pollution Control Division s'-1 iA R A" :7 T. Er ••v'1�'"' .mss r'ic- 3 ora vats nav Lean burn engines with a manufacturer's design rate greater than 500 hp shall use an oxidation catalyst to reduce emissions. The above emission control equipment shall be appropriately sized for the engine and shall be operated and maintained according to manufacturer specifications. The source shall submit copies of the relevant Applicability Reports required under Condition 2.1.2. Emission Standards: Section XVII.E—State-only requirements Any permanent engine that is either constructed or relocated to the state of Colorado from another state, after the date listed in the table below shall operate and maintain each engine according to the manufacturer's written instructions or procedures to the extent practicable and consistent with technological limitations and good engineering and maintenance practices over the entire life of the engine so that it achieves the emission standards required in the table below: Construction or Emission Standards in G/hp-hr Max Engine HP Relocation Date ! NOx CO I VOC January 1, 2008 12.0 4.0 1.0 100<Hp<500 January 1, 2011 1.0 2.0 10.7 July 1, 2007 i 2.0 4.0 1.0 500<Hp July 1, 2010 1.0 2.0 0.7 The source shall submit copies of the relevant Applicability Reports required under Condition 2.1.2. 2.3.3 NSPS for stationary spark ignition internal combustion engines: 40 CFR Part 60, Subpart JJJJ A permanent replacement engine that is manufactured on or after 7/1/09 for emergency engines greater than 25 hp, 7/1/2008 for engines less than 500 hp, 7/1/2007 for engines greater than or equal to 500 hp except for lean burn engines greater than or equal to 500 hp and less than 1,350 hp, and 1/1/2008 for lean burn engines greater than or equal to 500 hp and less than 1,350 hp are subject to the requirements of 40 CFR Part 60, Subpart JJJJ. An analysis of applicable monitoring, recordkeeping, and reporting requirements for the permanent engine replacement shall be included in the Applicability Reports required under Condition 2.1.2. Any testing required by the NSPS is in addition to that required by this AOS. Note that the initial test required by NSPS Subpart JJJJ can serve as the testing required by this AOS under Condition 2.2, if approved in advance by the Division, provided that such test is conducted within the time frame specified in Condition 2.2. Note that under the provisions of Regulation No. 6. Part B, section I.B. that Relocation of a source from outside of the State of Colorado into the State of Colorado is considered to be a new source, subject to the requirements of Regulation No. 6 (i.e., the date that the source is first relocated to Colorado becomes equivalent to the manufacture date for purposes of determining the applicability of NSPS JJJJ requirements). However, as of October 1, 2011 the Division has not yet adopted NSPS JJJJ. Until such time as it does, any engine subject to NSPS will be subject only under Federal law. Once the Division adopts NSPS JJJJ, there will be an additional step added to the determination of the NSPS. Under the provisions of Regulation No. 6, Part B, § I.B (which is referenced in Part A), any engine relocated from outside of the State of Colorado into the State of Colorado is considered to be a new source, subject to the requirements of NSPS JJJJ. 2.3.4 Reciprocating internal combustion engine (RICE) MACT: 40 CFR Part 63, Subpart ZZZZ AIRS ID: 123/99E1 Page 23 of 24 olor Aepa en P .li ealth and Environment it Pollution Control Division A permanent replacement engine located at either an area or major source is subject to the requirements in 40 CFR Part 63, Subpart 777Z. An analysis of the applicable monitoring, recordkeeping, and reporting requirements for the permanent engine replacement shall be included in the Applicability Reports required under Condition 2.1.2. Any testing required by the MACT is in addition to that required by this AOS. Note that the initial test required by the MACT can serve as the testing required by this AOS under Condition 2.2, if approved in advance by the Division, provided that such test is conducted within the time frame specified in Condition 2.2. 2.4 Additional Sources The replacement of an existing engine with a new engine is viewed by the Division as the installation of a new emissions unit, not "routine replacement" of an existing unit. The AOS is therefore essentially an advanced construction permit review. The AOS cannot be used for additional new emission points for any site; an engine that is being installed as an entirely new emission point and not as part of an AOS- approved replacement of an existing onsite engine has to go through the appropriate Construction/Operating permitting process prior to installation. AIRS ID: 123/99E1 Page 24 of 24 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 04/16/2015 Application Date: 12/15/2014 Facility Identifiers Permit No. 12WE2454 Potentially located in ozone nonattainment area AIRS County!! 123 Weld Facility U 99E1 Facility Type: exploration and production facility 1 2 Located in the 8-hour non-attainment area' 0 True Minor *Synthetic Minor for: l VOC NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Pronghorn 11-14-12HZ Production Facility Source Location: NWNW Section 12, Township 5N, Range 61W 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: 3 Source Description: Oil and gas exploration and production facility known as the Pronghorn 11-14-12HZ Production Facility,located in the NWNW Section 12,Township 5N,Range 61W,Weld County,Colorado. Point Name Type Control Action Cancelling GP01 and adding to facility-wide 001 CNDTK-1 Condensate Tanks Flare permit. Increasing number of tanks, Cancelling GP05 and adding to facility-wide 002 PW Water Tanks Flare permit. Increasing number of tanks. throughput and emissions 004 TLO Loadout Flare Modifying by increasing throughput and adding control Existing point-In 12/2014 application, source requested to increase counts and emission 005 FUG Fugitives None limit from 4.4 to 11.9 tpy. On 4/28/2015, source requested to cancel fugitives since subject to Reg 7 and now APEN-exempt 006 P-1 Pump Flare Modifying by increasing emission limit based on updated gas analysis Modifying by increasing emission limit based 007 P-2 Pump Flare on updated gas analysis 011 SEP-1 & Separator Venting Flare New point SEP-2 013 FL-2 Separator Venting Flare New point-emergency flare 'Pt 003 is an engine covered by Permit 12WE2454 but point is not beingmodified *Pt 008 is a permit exempt engine *Pts 009 and 010 are engines covered by GP02 Five(5)400 bbl above ground atmospheric condensate storage tanks controlled by two 001 enclosed flares. Each flare has a minimum control efficiency of 95%. Requsted Throughput 74460 bbl Control Flare Efficiency 95.00%j Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 5.6052 lb/bbl 208.7 tpy 10.4 tpy Promax Benzene 0.0520 lb/bbl 3,871 Ib/yr 194 lb/yr Promax n-Hexane 0.2923 lb/bbl 21,765 lb/yr 1,088 lb/yr Promax Toluene 0.0443 lb/bbl 3296 lb/yr 165 lb/yr Promax Ethylbenze 0.0066 lb/bbl 495 lb/yr 25 lb/yr Promax Xylenes 0.0175 lb/bbl 1305 lb/yr 65 lb/yr Promax 224-TMP 0.0280 lb/bbl 2084 lb/yr 104 lb/yr Promax Nox 0.068 lb/Mmbtu 0.4 tpy 0.4 tpy AP-42 Table 1 CO 0.37 lb/Mmbtu 2.0 tpy 2.0 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. Regulation 2—Odor Section I.A-No person,wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons(471 bbl) NSPS OOOO:for storage vessels in the natural gas production,transmission, and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. Regulation 7—Volatile Organic Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS Applicant is subject to the emission control requirements for condensate tanks since it is located in the nonattainment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject to this requirement since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions are greater than 6 tpy.The tank is considered a new tank since it was constructed after 5/1/2014. 12WE2454.CP3 123/99E1 One (1)400 bbl above ground produced water storage tank controlled by two 002 enclosed flares. Each flare has a minimum control efficiency of 95%. Emissions Calculations Requsted Throughput 78840 bbl Control Flare • Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.262 lb/bbl 10.3 tpy 0.5 tpy CDPHE Benzene 0.007 lb/bbl 552 lb/yr 28 lb/yr CDPHE n-Hexane 0.022 lb/bbl 1734 lb/yr 87 lb/yr CDPHE Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20%opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes.The approved reference test method for visible emissions measurement is EPA Method 9(40 CFR, Part 60,Appendix A(July, 1992))in all subsections of Section II. A and B of this regulation. Regulation 2—Odor Section I.A-No person,wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air. Regulation 7—Volatile Organic Compounds XVII.C.1.b Applicant is subject since actual uncontrolled emissions are greater than 6 tpy. The tanks are considered new since they were constructed/modified after 5/1/2014 12WE2454.CP3 E2454.CP3 123/99E1 Hydrocarbon Loadout to Tanker Trucks.Loadout is controlled by using dedicated vapor balance service and two enclosed flares.Collection system is 70%efficient and each flare has a minimum 004 control efficiency of 95%.Overall control efficiency is 66.5% 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 5 Saturation Factor 1 AP-42 factor for submerged loading,dedicated vat P True Vapor Pressure 0.89 psis Calculated TVP of liquid based on oil analysis and M Molecular Weight of Vap 64.52 lb/lb-mole Calculated MW of liquid based on oil analysis and T Liquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver,CO L 1.31 lb/10^3 gal 5.50E-02 lb/bbl Annual requested Throughput 74460 BBL/yr 3127320 gal/yr Annual requested VOC emissions 4097 lb/yr 2.05 tpy Control: Flare Efficiency: 66.50% Source assumes 95%control efficiency and 70%collection efficiency NCRPs Component Mass Fraction VOC 0.9588 Benzene 0.0095 n-hexane 0.0955 Toluene 0.0091 Xylenes 0.0016 Source: Sales oil composition and Eq 1-22 of AP-42 Ch 7 Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.0550 lb/bbl 2.0 tpy 0.7 tpy AP-42 Benzene 0.0005 lb/bbl 39 lb/yr 13 lb/yr AP-42 n-Hexane 0.0053 lb/bbl 391 lb/yr 131 Ib/yr AP-42 Toluene 0.0005 Ib/bhl 37 lb/yr 12 Ih/yr AP-42 Xylenes 0.0001 lb/bbl 7 lb/yr 2Ib/yr AP-42 Regulatory Review (Regulation 3-APEN and Permitting Requirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes,review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(me aeLsi per day of crude oil on an annual average basis? No If yes,this emissions paint is categorically exempt from permit requirements per Regulation 3,Part B.Section 11.0.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B.Section 11.0.1.1 12WE2454.CP3 123/99E1 005 Fugitive equipment leaks AS OF 1/1/2015,THIS SITE IS SUBJECT TO REG 7,XVII.F.UNDER REG TXVII.F,SOURCE CAN USE TABLE 2A EMISSION FACTORS. WITH TABLE 2.8,FUGITIVE EMISSIONS ARE NOW APEN-EXEMPT.SOURCE REQUESTED TO CANCEL APEN RegulAlon 7 information Operating Hours: 8760 hourslyear Emission Factor Source Screenng EFs-EPA-453R-95-017 Table 2-8 Control Efficiency Source. None Calculations Emission Factor(kglh. Emissions Service Component Type Count source) Control old Pollutant Mass Fraction ttpyl Table 24 Table 2-8 Reg.3 Connectors 1604 200E-04 103E-05 0 VOC 0.3389 0.1281198 Flanges 94 3.90E-04 570E-06 00% Oscars 0.0007 0O002646 Open-Ended Lines 52 100E-03 150E-05 0 ue 0% Tolne 0.0006 S 0002268 Gas Pump Seals 8 140E-03 150E{N 0.0% Ethpbenzene 90002 7.561E-05 Valves 227 4.50E-03 2.50E-05 0 Xylenes 00003 0.0001134 Other 111 8.80E-03 120E-04 0 n-Hexane 0 095 S 0018902 Connectors 0 )100-06 7.50E-06 0.0% VOC 1 0 Flanges 0 3.90E-07 3.90E-07 00% Benzene 0 open-Ended Lines 0 1.40E-0a 7. E-06 0 Toluene Heavy 01 0 Pump Seals 4 0 0 00E+00 930000 90% Ethytbenzene o Valves 0 9.40E-06 040E-06 00% Xylenes 0 Other 0 3.20E-05 3.20E-05 0 0% n-Hexane 0 Connectors 013 2.10E-04 9.70E-06 0 VOC 00966 0.0892141 i Flanges 14 110E-04 2a0E-06 00% Benzene 0.0052 0.0002832 Open-Ended Lines 5 140E-03 140E-05 00% ' Toluene 0 0 0082 0007258 Light Oil Pump Seals 0 130E-02 s20E{U 0 Ethybenzene 90031 0.0002744 Valves 93 2.50E-03 1.90E-05 0 Xylenes 00097 0.0008586 Other 14 7.50E-03 1.10E-04 0 n-Hexane 00166 0.0014693 Connectors 1.10E-04 100E-05 0 VOC 1 O Flanges 2.90E-06 2.90E-06 0 Benzene 0 e Water/Oil O"r nLIMBnded LIMB 2.50E-04 3.50E-06 0 0% Toluene 0 Pump Seals 240E-05 2a0E-05 0 0% EPNlanzens 0 Valves 9.80E.05 9.70E-06 0 0% Xylenes 0 Other 1.40E-02 590E-05 00% n-Hexane 0 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source I Ipy VOC 0.21py 0.21py Screening EFs-EPA-45YR-95017 Table 2-e Benzene 11b'yr I lb/yr Screening EFs-EPA-453/R-95017 Table 2- 000 Toluene 21b/yr 21Wyr Screening EFs-EPA-453/R-95-017 Table 2- 000 Elhylbenzene t lb/yr I lb/yr Screening EFs-EPA453/R-95-017 Table 2- 000 Xylenes 2 lb/yr 2 lbyr Screening EFs-EPA453/R-95-017 Table 2- 0.00 n-Hexane 7 lb/yr 71b/yr Screening EFs-EPA-453/R-95017 Table 2- 0.00 Regulatory Applloblllry Reg.3 Review Regulation 3.Pad B,Section 111.0 2 to determine is RACT is required? Yes Review40 CFR,Pact 50.Subpart KKK todetermine it applicable to this source? No Rag.5 Review40 CFR,Part 60,Subpart 0000 to determine 1160.5380 and/or 40.5385:5 applicable? No Reg.7 Review Secvton XVII.F to determine l5 LDAR is applicable? Yes One(1)pneumatic water transfer puma rated at 600 scf/hr(Sandpiper, Model G1 F.Serial number 19811466).The pneumatic pump is controlled by 006 two enclosed flares-Each flare has a minimum control efficiency of 95%. Pump Information Manufactur Sandpiper Model Number:Gil Serial Pump Number: 19811466 Information Pump __capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consu mptio Control Flare 95.00%Efficiency Calculations EPA Emission Inventory Improvement Program Publication:Volume a,Chapter le-Displacement Equation 110.4-3) Ex=Q'MW*Xx/C Ex=emissions of pollutant x CI=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=$6 of gas"MW of air Xx=mass fraction of a in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 6OF and 1 atm O sop scf/hr MW 2472 lb/Ib-met Hours of 3760600aryr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr Ib/yr tpy Helium 0 4 0.00000 Helium 0.000 0.000 0.000 CO2 2740536733 44 0.0489 CO2 1.915 16777.909 8.389 nitrogen a83060237e 28 0.0071 nitrogen 0.280 2448.980 1.224 methane as 600]6673 1604 04262 methane 16.681 146125 352 73.063 ethane 1470261329 30.07 0.1788 ethane 6.999 61311.831 30.656 propane to aa9aaoo2 44.09 0.1864 propane 7.294 63894.850 31.947 isobutane 990241778 58.12 0-0212 isabutane 0-830 7273.600 3-637 n-butane 3033309647 58.12 0.0713 n-butane 2.791 24448.854 12.224 isopentane a.528588225 72.15 0.0154 isopentane 0.604 5289.957 2.645 n-pentane a 663794238 72.15 0.0194 n-pentane 0.758 6641.803 3.321 cyclopentane 9365070302 70.15 0.0018 cyclopentane 0.072 633-034 0-317 n-hexane 014420002 86.18 0.0050 n-hexane 0.197 1724.591 0.862 cyclohexane 005947018 84.18 00019 cyclohexane 0.074 650.808 0.325 Other hexanes 0211850581 86.18 0.0074 Other hexane 0.289 2532.053 1.266 I heptanes 3550270624 100.21 0-0020 heptanes 0-080 698.704 0.349 methylcyclohexa o 53459976 98.19 0.0014 methylcycloh¢ 0.054 471.087 0.236 I 224-TMP 3 314074654 114.22 0.0007 224-TMP 0.025 222.944 0.111 Benzene 0027670206 78.11 0.0007 Benzene 0.027 234.836 0.117 Toluene 0417400x54 92.14 0.0006 Toluene 0.024 210.307 0.105 Ethylbenzene 0003740588 106.17 0.0002 Ethylbenzene 0.006 55.193 0.028 Xylenes a058252105 106.17 0.0003 Xylenes 0.011 92 057 0.046 CS+Heavies 0024022281 325 0.0032 08+Heavies 0.124 1082.714 0.541 Mass Fraction VOC 0.3388 Total VOC 58.079 Heating Value I was BTII/scf combustion emission factor source AP-42:Chapter 13.5 007 I lb NoX4MMBIu 0 37 lb CO/MMetu 12WE2454.CP3 123/9951 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1 F,Serial number 19811466).The pneumatic pump is controlled by 006 two enclosed flares.Each flare has a minimum control efficiency of 95%. soles Mole%,MW,and mass fractions are based on weighted average of sales gas samples collected from Pronghorn K-O-12 HNB on 10/7/2014 and fron Emissions are based on 8760 hours of operation per year. Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 22100 lb/MMscf 1105.0 lb/MMscf 58.1 tpy 2.9 tpy Gas Analysis Nos 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.3 tpy 0.3 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 1.4 spy 1.4 tpy AP-42 Benzene 44.680 lb/MMscf 2.2340 lb/MMscf 235 lb/yr 12 lb/yr Gas Analysis n-Hexane 328.12 lb/MMscf 16.406 lb/MMscf 1725 Ib/yr 8616/yr Gas Analysis Toluene 40.013 lb/MMscf 2.0006 lb/MMscf 210 lb/yr 111b/yr Gas Analysis Ethylbenzene 10.501 lb/MMscf 0.5250 lb/MMscf 55 lb/yr 3 lb/yr Gas Analysis Xylenes 17.515 lb/MMscf 0.8757 lb/MMscf 92 lb/yr 5 lb/yr Gas Analysis 224-TMP 42.417 lb/MMscf 2.1209 lb/MMscf 223 lb/yr 11 lb/yr Gas Analysis • 12WE2454.CP3 123/9951 One(1)pneumatic heat trace pump,rated at 600 scf,'hr(Sandpiper,Model G1 F,Serial number 19811470).Tne pneumatic pump is controlled by two 007 enciosed flares.Each flare has a minimum control efficiency of 95%. Pump Information Manufactur Sandpiper Model Number GIF Serial Pump Number 19811470 Information Pump capacity 9.1 gallons per minute pumped natural gas 000 scf/hour used mnsum ptia Control Flare 95.00%Efficiency Calculations EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-31 Ex=QaMW"Xx/C Ex=emissions of pollutant x Q=Volumetric flaw rate/volume of gas processed MW=Molecular weight of gas=$6 of gas*MW of air Xx=mass fraction of a in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Q nos sdf/hr MW 24 72 lb/Ib-mol Hours of op. 6760 boersryr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr to,/ CO2 na59673i 44 0.0489 CO2 1.915 16777.909 8.389 nitrogen a 43052976 28 0.0071 nitrogen 0.280 2448.980 1.224 methane s5 aepec573 16.04 0.4262 methane 16.681 146125352 73.063 ethane i 14792419x8 30.07 0.1788 ethane 6.999 61311.831 30.656 propane io 4,-96:522 4409 0.1864 propane 7294 63894.850 31.947 isobutane 0202417's 58.12 0.0212 isobutane 0.830 7273.600 3.637 n-butane 565;U:a7 58.12 0.0713 n-butane 2.791 24448.854 12.224 isopentane 5528681.22n 72.15 0.0154 isopentane 0.604 5289.957 2.645 n-pentane o 842794210 72.15 0.0194 n-pentane 0.758 6641.803 3.321 cyclopentane 096s0TJ92 70.15 0.0018 cyclopentane 0.072 633.034 0.317 n-hexane 21445422 86.18 0.0050 n-hexane 0.197 1724.591 0.862 cyclohexane 20,6747816 84.18 00019 cyclohexane 0.074 650808 0.325 Other hexanes anlsarse3 86.18 0.0074 Other hexane 0.289 2532.053 1.266 heptanes i555nm2a 100.21 0.0020 heptanes 0.080 698.704 0.349 methylcyclohexa o 0345`527E 98.19 0.0014 methylcycloht 0.054 471.087 0.236 224-TMP 001407464 114.22 0.0007 224-TMP 0.025 222.944 0.111 Benzene 0521579544 78.11 0.0007 Benzene 0.027 234.836 0.117 Toluene a 51e45545-u 92.14 0.0006 Toluene 0.024 210.307 0.105 Ethylbenzene acm74558s 106.17 0.0002 Ethylbenzene 0.006 55.193 0.028 Xylenes 1096252105 106.17 0.0003 Xylenes 0.011 92.057 0.046 CS+Heavies 5524022281 325 0.0032 CS+Heavies 0.124 1082.714 0.541 Mass Fraction VOC: 0.3388 Total VOC 58.079 Heating Value I 1401 BTU/scf combuslion emission factor source. AP-42:Chapter 13.5 007 Ilb NoX/MMew 807 is co/MMelu 12WE2454.CP3 123/99E1 One(1)pneumatic heat trace pump.rated at 600 sof/hr(Sandpiper.Model G1 F,Serial number 19811470).The pneumatic pump is controlled by two 007 enclosed flares.Each flare has a minimum control efficiency of 95%. Notes Mole%,MW.and mass fractions are based on weighted average of sales gas samples collected from Pronghorn K-0-12 HNB on 10/7/2014 and fron Emissions are based on 8760 hours of operation per year. Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 22100 lb/MMscf 1105.0 lb/MMscf 58.1 tpy 2.9 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.3 tpy 0.3 tpy AP-42 CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 1.4 tpy 1.4 tpy AP-42 Benzene 44.6801b/MMsd 2.2340 lb/MMscf 2351b/yr 121b/yr Gas Analysis n-Hexane 328.12 lb/MMscf 16.406 lb/MMscf 1725 lb/yr 861b/yr Gas Analysis Toluene 40.013 lb/MMscf 2.0006 lb/MMscf 2101b/yr 111b/yr Gas Analysis Ethylbenzene 10.501 lb/MMsd 0.5250 lb/MMscf 55 lb/yr 31b/yr Gas Analysis Xylenes 17.515 lb/MMscf 0.8757 lb/MMscf 92lb/yr 5lb/yr Gas Analysis 224-TMP 42.417 lb/MMscf 2.1209 lb/MMscf 223 lb/yr 11 lb/yr Gas Analysis 12WE2454.CP3 123/99E1 Two low-pressure separators controlled by Iwo enclosed flares during VRU downtime.Each flare has a 011 minimum control efficiency of 95%. Equipment Description This source vents natural gas from: low-pressure separators during VRU downtime Emissions from this source are. routed to a flare [Natural gas venting from low-pressure separators during VRU downtime.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=C'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/Ib-mol)at 60F and 1 atm Throughput(O) 1,AC MMscf/yr 159.6942 so'/hr MW 34.926 Ibllbmol 0.003832661 MMscf/d mole N MW Ibx/Ibmol mass fraction lb/Fr Ib/yr toy Helium 0.00 4.0026 0400 0000 0.00 0.00 0.00 CO2 231 44.01 1.016 0029 0.43 375133 1.88 N2 038 28.013 0.108 0003 0.05 397.36 0.20 methane 3924 16.041 6.295 0.180 2.65 23234.02 1162 ethane '758 30.063 5.278 0.151 2.22 19481.36 974 propane 2025 44.092 8.933 0256 3.76 32971.30 16.49 isobutane 2 79 58.118 1221 0.046 0.68 5984.85 2.99 n-butane 973 58.118 5256 0.162 2.38 20876.72 10.44 isopentane 2.26 72.114 1.483 0.042 0.63 5475.03 2/4 r-pentane 273 72.114 1.970 0.056 0.83 7269.88 3.63 cyclopentane 030 70.13 0.209 0.006 0.09 77021 0.39 n-Hexane 0.65 86.18 0.561 0.0161 0.24 2070.82 1.04 cyclopexane 0._28 84.16 0.237 0.007 0.10 874.46 044 Other hexanes 0.89 86.18 0.771 0.022 0.32 2844.43 142 heptanes 0.19 10021 0.193 0.006 0.08 713.88 0.36 methylcyclohexane 0.17 98.19 0.165 0.005 0.07 607.79 0.30 224-TMP 0.08 11423 0.089 0.0026 0.04 329.30 0.16 Benzene 070 78.2 0.079 0.0023 003 291.23 0.15 Toluene 0.09 9275 0079 0.0023 0.03 291.15 0.15 Ethylbenzene 003 106.17 0.028 0.0008 0.01 105.02 0.05 Xvlenes 0.04 106.17 0046 0.0013 0.02 168.51 0.08 C8a Heavies 0.08 135.5495203 0.110 0.003 0.05 405.76 0.20 VOC mass frac 0.636 Total VOC(Uncontrolled) 41.03 Notes Mole%.MW,and mass fractions are based on VRU inlet gas analysis collected 10/7/2014 at Pronghorn K-0-12 HNB Flomrate'is based on predicted flowrate in Promax model.assuming 15%VRU downtime and applying a 20%safety factor I calculated the average MW of 081 based on the average MW an the analysts far the gas. 12WE2454.CP3 123/99E1 Two low-pressure separators controlled by two enclosed flares during VRU downtime.Each flare has a 011 minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Abutec Model 48" Serial Number Gas Heating Value 1975 Btu/scf _ Throughput 2762.869354 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress low-pressure separator gas to sales line.The VRU is considered part of the process and not included as an air pollution control devio 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 lib NOX/MMBtu 0.37 lib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 5865316/MMscf 2932.616/MMscf 41.0 tpy 2.1 toy Gas Analysis Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 0.1 toy 0.1 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 0.5 toy 0.5 spy AP-42 Benzene 208.18 lb/MMscf 10.409 lb/MMscf 291 lb/yr 15 lb/yr Gas Analysis n-Hexane 1480.3 Ib/MMscf 74.015 Ib/MMscf 2071 lb/yr 104 lb/yr Gas Analysis Toluene 208.13 lb/MMscf 10.40616/MMscf 291 lb/yr 15 lb/yr Gas Analysis Ethylbenzena 75.075 lb/MMscf 3.7538 lb/MMscf 105 lb/yr 5 lb/yr Gas Analysis Xylenes 120.46 lb/MMscf 6.0228 lb/MMscf 169 lb/yr 8 lb/yr Gas Analysis 224-TMP 235.39 lb/MMscf 11.770 lb/MMscf 329 lb/yr 16 lb/yr Gas Analysis Regulatory Applicability AOCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yea This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 12WE2454.CP3 123/99E1 One emergency flare used to combust separator gas during emergencies or when the pipeline is not 013 available.Flare has a minimum control efficiency of 95%. The flare is not enclosed. Equipment Description This source vents natural gas from: a well head separator when the sales gas pipeline is not available or during emergencies Emissions from this source are: routed to a flare INatural gas venting from a well head separator when the sales gas pipeline is not available or during emergencies.Emissions from this source are routed tc Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II.Chapter 10-Displacement Equation(10.4-3) Ex=O•MW•Xx/C Ex=emissions of pollutant x 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 o=molar volume of ideal gas(379 scf/Ib-mol)at 60F and I atm Throughput(01 10 MMscf/yr 1141.552511 scf/hr MW 24.72 Ib/Ib-mol 0.02739726 MMsct/d mole% MW Ibx/Ibmol mass fraction lb/hr Ib/yr tpy Helium 0 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 27R.e713 44.01 1.210 0049 3.64 3192869 1596 N2 1630652976 28.013 D.177 0007 553 466156 233 methane 5559095673 16.041 10.537 0426 3174 27803398 13902 ethane '.4/0261528 30.063 4.420 0-179 1331 11682397 58.31 propane -044983922 44.092 4.608 0.186 13.88 12157106 8079 isobutane 0902vtP5 58.118 0.524 0.021 1.58 13838.18 8.92 n-butane 3.033355677 58.118 1.783 0.071 5.31 46514.48 23.26 itopentane 4.725555225 72.114 0.381 0.015 1.15 10059.58 5.03 n-pentane 2563794238 72.114 0.479 0.019 1.44 12630.31 832 cyctopentane 3465070392 70.13 0.046 0.002 0.14 1204-06 0.60 n-Hexane 3.14429902 86.18 0.124 0.0050 0.37 328118 1.64 cyclohexane 3/55'4-7815 84.16 0.047 0.002 0.14 1237.93 0.82 Other hexanes ?211550753 86.18 0.183 0.007 0.55 481745 2.41 heptanes 3062276624 100.21 0.050 0002 0.15 1329.35 066 methylcyclohexane 4.0545595376 98.19 0.034 0.001 0.10 896.28 0.45 224-TMP ?01407404 114.23 0.016 0.0007 0.05 42421 021 Benzene a0b570098 78.12 0.017 0.0007 0.05 '446.85 0.22 Toluene )915459454 9215 0.015 0.0006 005 40017 0.20 Ethylbenzsne 0333748500 106.17 0.004 0.0002 0.01 105.01 0.05 Xylenes 37052/2305 106.17 0.007 00003 0.02 17515 009 08+Heavies 2224022281 325 0-078 0.003 024 2059.96 1-03 VOC mass frac 0.3388 Total VOC(Uncontrolled) 110.50 Notes Mole 59,MW,and mass fractions are based on weighted average of sales gas samples collected from Pronghorn IC-0-12 HNB on 10/7:2014 and from Pronghorn 11-14-12h • 12W52454.CP3 123/98E3 One emergency flare used to combust separator gas during emergencies or when the pipeline is not 013 available.Flare has a minimum control efficiency of 95%. The flare is not enclosed. Flaring Information Equipment Description Flare to combust separator gas when ipeline is not available or during emergencies. Manufacturer TBD Model TBD Serial Number TED Gas Heating Value 1403 Btu/scf Throughput 14030 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup Flare (Overall Control I 95.00%I Combustion emission factor source: AP-42:Chapter 13.5 0.07 lIb NOX/MMBtu 0.37 jib CO/MMBW Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 22099 lb/MMscf 1105.0 lb/MMscf 110.5 tpy 5.5 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.5 tpy 0.5 tpy AP-42 CO 0.3716/MMBTU 0.37 lb/MMBTU 2.6 tpy 2.6 tpy AP-42 Benzene 44.685 lb/MMscf 2.2343 lb/MMscf 447 lb/yr 22 lb/vr Gas Analysis n-Hexane 328.1216/MMscf 16,406 lb/MMscf 3281 lb/yr 164 lb/yr Gas Analysis Toluene 40.017 lb/MMscf 2.0009 lb/MMscf 400 lb/yr 20 lb/Yr Gas Analysis Ethylbenzene 10.50116/MMscf 0.5250 lb/MMscf 105 lb/yr 5 lb/yr Gas Analysis Xylenes 17.515 lb/MMscf 0.8757 Ib/MMscf 175 Ib/Yr 9 lb/yr Gas Analysis 224-TMP 42.421 lb/MMscf 2.1210 lb/MMscf 424 lb/yr 21 lb/yr Gas Analysis Regulatory Applicability AOCC 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.' AOCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section)NIL82 However,since this flare is used for emergency purposes,not used routinely,and must control high pressure,high volume flow intermittently,the emergency flare will be approved as an altemative control device per Reg 7,Sec XVII.B2.e.The flare will have to meet Reg 7,Sec XV11.8 except that it is not required to be enclosed 12WE2454,CP3 123/99E1 AIRS(County/Plant)123/99E1 Permit No.121A/92454 Date 4/16/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions reportable Point ft SCC Pollutant or CAS Factor Enosson Factor Source (thy' (tpy1' PTE(Ipyp Ctb.ER%P VOC 133.46 lb/1000 gallc Promax 8.7 104 208.7 95% Yes NOx 0.068 lblMmbtu AP-42 Table 13.5 0.3 04 04 0% No CO 0.37 lb/Mmbtu AP-42 Table 13.5 1.7 2.0 2.0 0% Yes Benzene 12378 Ib11000 gallc Promax 161 194 3.871 95% Yes 001 40400311 n-Hexane 6.9597 lb/1000 galls Promax 907 1,088 21,765 95% Yes Toluene 1.0541 lb/1000 gallc Promax 137 185 3,296 95% Yes Ethylbenzene 0.1581 lb/1000 gallc Promax 21 25 495 95% Yes Xylenes I O4174 IbIl 000 galISPromax 54 65 1305 95% Yes 224-tnmets Ipentane 0.6665 lb/1000 gallc'lomax • 81 104 2,084 95% Yes VOC 6.238 lb/1000 galls CDPHE 0.5 10.3 95% Yes 002 40400315 Benzene 0 167 I6/1000 italic COPSE 28 552 95% Yes n-Hexane 0.5241bil 000 italic COPSE 87 1,735 95% Yes VOC 1.3100 IbIl 000(Into AP-42 0.7 2.0 66.5% Yes Benzene 0.0124lb/1000 gallc AP-42 13 39 66.5% No 004 40600132 n-Hexane 0.1251 lb/1000 gallc AP-42 131 391 66.5% Yes Toluene 0.0119 lb/1000 galls AP-42 12 37 66.5% No Xylenes 0.0021 lb/1000 gallc AP-42 2 7 66.5% No VOC 221001b/MMecf Gas Analysis 2.9 58.195% Yes NOx 0.0681b/MMBTU AP-42 0.3 0.3 0% No CO 0.37 lb/MMBTU AP-42 1.4 to 0% Yes Benzene 328.12 lb/MMscf Gas Analysis 12 235 95% No 006 31000299 n-Hexane 328.12 lb/MMscf Gas Analysis 86 1725 95% Yes Toluene 013 lb/MMscf Gas Analysis 1t 210 95% No Etbylbenzene 10.5010 lb/MMscf Gas Analysis 3 55 95% No Xylenes I 17.515 7 lb/MMscf Gas Analysis 5 92 95% No 224-Gmetn,loentanc 42491bIMMscf Gas Analysis 11 223 95% No VOC 22100 IRMMscf Gas Analysts 2.9 58.1 95% Yes NOx 00681b/MMATBTU AP-42 0.3 0.3 0% No CO 0.370 b/MMBTU AP-42 1.4 1.4 0% Yes Benzene 344.68028.12 lb/MMscf l Gas Analysis 12 235 95% No 007 31000299 n-Hexane 328.12 lb/MMscf Gas Analysis 86 1725 95% Yes Toluene 40.013 lb/MMsof Gas Analysts tl 210 95% No Etttebenzen0 10.5010 lb/MMscf Gas Analysis 3 55 95% No Xylenes I 17.51 lb/MMscf Gas Analysts 5 92 95% No 224-t meth loentane 42.417 IbtMMscf Gas Analysis 11 223 95% No VOC 586531bIMMscf Gas Analysts 2.1 410 95% Yes NOx 0068 IMIAMBTU AP-42 0.1 0.1 0% No AIRS(County/Plant)123/99E1 Permit No.1207 E2454 Date 4/16/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions reportable Point# SCC Pollutant or GAS Factor Emisison Factor Source (ipy)- ppy)- PTE(toy)*Cut.Eff%? CO 0.370.O/MMEITU AP-42 0.5 0.5 0% No Benzene 208.181WMMsof Gas Analysis 15 291 95% Ves __ 11 31000205 n-Hexane 1480.31WMMscf Gas Analysis 104 2071 95% Yes Toluene 208.131b/MMsct Gas Analysis 15 291 95% Yes Etbylbenzene 75.0751WMMscf Gas Analysis 5 105 95% No Xylenes I 120.46 tb/MMscf Gas Analysis 8 169 95% No 224-Innmeth'pentane 235.391b/MMscf Gas Analysis 16 329 95% Yes _. __._ ._____ VOO 220991WMMscf Gas Analysis 5.5 110.5 95% Yes NOx OO681b/MMBTU AP-42 0.5 0.5 0% No CO 0.380 b/MMBTU AP-42 2.6 2.6 0% Yes Benzene 44.685(b/MMsc Gas Analysis 22 447 95% Yes 13 31000205 n-Hexane 328.12 b/MMscf Gas Analysis 164 3281 95% Yes l Toluene 40.010 b/MMscf Gas Analysis 20 400 95% Yes Et1Ylbenzene 10.5010 Ib/MMsct Gas Analysis 5 105 95% No XNenes f 17.515 4blMMscf Gas Analysis 9 175 95% _No 224-Gmetbylpentane 42 42021 21 lb/MMscf Gas Analysis 21 424 95% Yes K - 4 i _ g ° oo § o , o �7 r "Q` v G. T z z z l.7 a. p O s0.n z 0 %LI9 of 1. ca. Via . <y : D w . Nriso _ u v ` ` eMv r� m ,iC d O C 074 •p C Y lg. " n .0 es 0 0 0 ,.....- •a : a a . i ≥ bI �; i2 �� a E cen en en fa 7 F € € zZ DE: :r nab , z ;;Al N 0u a 8 O m a ~ y � ~ .is d Q W � 1 � _ �„ ` N5 O a p a `. p Y Li ide, F rR v 8 ■ .o.e V ' 5 p G rya • V E >s p s n€0 L w e i p 44 w , pW. Q m i m r I 1 '6 4 0 " a R : a; r E. a b d o 1 6 W a. 0y. m •-, o m S a sC ,E a b .. W V M OO+ : �le ,+ r G 'C yy y a m up.. 0- N d Is O 17 is C W D 1R a g O 0. � �.. se s - 62,c oo a Te pB. U ✓ P I. C Q . O v•t L t v4 p c q �^ r �. u m O 9 ot,J Q— A ,.tv9- , qOA LU `8 E c g o O - o50, a aa.. � s, ..;,:-, il u 5 --d, s'p Z 4ii.) .2 w 2 ° a ' ` o v Cy p W V u d d O "� C .O p qE $ 3 -� yvi y ..i.,..' 7IA O „ L L (Y. ��y a ?v ) L Cx a fi ~ a obi ❑ 0gG ® ® Q o .. u = a �+ o S © ® © ❑ ❑ �' (� a ao a n ❑ 8Eor m '>. a i i ypp 1 O O y, i C , ` ry sa zz � o o �. yQ I _• 4 O w C . 4 w O -. p — .. E �`' ❑® 3 Er. E " !- G �L .r'n G O + O ° ° . a a P. COS V en 7,1 e Z d ° " sr 444 Of ee o u41'a o u 'i ° .°g a r' n= u u o s 2:3 p p� vj o �4>' >^ U Est. v W U O U L. C ,- ,� G r 2 t rilL 73 ►. W E 4 x ti r•-•' w N E "' ❑ ®❑ s Q O r ra r Y U 5 " z z - 7 pr3 - 4 d "1Aii eTy VE .CIO a a s r Oy J7 i al 04 id e O u Er n p � it. CI' n7ls�g 4� � o R. C _ I Il war a e c ° n • M ail 2 y £ C. ' I 0 in B �b c -� p 8 r , p.. il .~. • o ¢1 T a g ~ G y 1�r g�,, CCr w o a• INK a .� 3 at m t . � � 8sgs0e � € $ " o I- ~ a O Q CAI ., 9 it k a N G y T a ` Ca►.i P.U a Z 6. 6. , P. a e6 d �" x ,. ID r �. I kw0 e .. 0 liii! ii 1 r' p A I 7 Z_ n N Q Q T < U < g w Q U a A .> n z w 9 _ ° a om S5dd� 9a " o w F o a gg -M v 0. w Flis 2g 3 ' 6 C F h HI g 3 11 :41� � a e I CE) 1 oil gi 'b'18 (� of r 0 A < a. aE. 4 a. 0. 0. 0. 0 SS d .33.1 $ D N M G 9 .ea se gE r p . V .. � ° 8E o 0O oe 355535553 ds 11 d il• id t iem4 Yea; U ,Z3 r 30' iG El 0 O 3 E .L S a CE 33 ❑ y e a o W le G X Of 2 g N 3; N r r O O r e a o I _ • e a s a 7 Li 353355Ia a en s Oyu S A e 4d a_ 7 .°p,1•qu i 0 a e ' 'C� yy y .. o N a a a .T�. L� O to C2 aE. 21 w y E u o .3 - 2 K e E ✓ n. b a • �} S 0 l .o g g.8 0 t O q o f a o a y. d w u ON ML.OV 3 7-1 C da.... 5 4• 4 ae I F 9 O ,!. r, 0 0 O �O � a O= 0a a Bov o b o S. g S of 00 OOO i +aI 0 a .� L . o '6 lg� O 3 U fi o W P w o° 3 O402 =-Al.o > N Tel S .. _a a„ W e 'Fa 6� 3 :al g C) o a ,... 0e_r3 oo q a g e .01 _ v °> £ c� 4 _ a ..... M COC`ONU,, OCO S s ;es 2 — ® ❑ ` U i r rrcd6 01 §: 9 � u _ o = fir3 w 41 ; s * * ii e : s z , = E-1 ^ a .g. F e « E 8 o a olc.35 a a 22' . ❑ 5 • r. Ey. °o . z a. E �CIp ...- 0 Z a. 2 y •• a S v • L ggg a e pa .a a pa Sao 42 {tyy Aga r4 2 y 9�_4 " b a 'ei U $ a o g 9 w L a 3 d a 3 3 3 . E G7 u c'2 i �� > ❑ � 1 oa Sao ; _ NVI- WNCO : at'1;1, zkm� W m a H o f a s a e 1 CO 0000N0J $u a s ems . Mom ❑ a = 4 u o f g a` 6 is vs O O O O O O d , -1 p, 2111 om a o. s ea'n-- ; " ^ B ° Ea al. id e 1 3 paMQ B J o a �' U o • c d 'a- �l a � • �0 f3 Si 0 c o > 2 5 a =1"8 A] C pp Z 4 1111S•] 8 s. a I. m p un Es II. 19 1EL II p. 3 l ID$ .0 .p .. e e > . 0„ 0 ¢ o . �.@_ a $ S c Qg 8 0 G `0. Ti y L E $ • 6480 ; 3111h V 1 Ii .h A. ' 4 a Vl r4 O U 0..r Fe a q a 1 0 1 1 zi > V 6 O - T iixii bm O ^-g w�7 .. e e S a• w a ° $ o $ e = ao m E- X ee g fix yfi0>; i n wiz) v " W ° ry al m >. 1 CC 0 sa m o 0 0 0 o d 3 e « z N u 0 a 3 ≥.z ZZZX. c c s0 .°. E / 0 to 0. u T 0 C CMint 4 e tm ❑ Y y r2 > > z $ u CA C.1 rq C, c" - F .' .0 L E y �`. o pW.ia °Y Cill .c �o �° _ Le .0 W r a C p y V N V e 01 0 •� O G t N i C 0 en 0 ¢ 3 O al as cn K C m y w 9 3 G� G 5 O L �. C C \ y F o T p`vp Y / .Q °. C °'-' O W 4.. o E co i °a 3 W .°. r I®❑®❑®l\ w F 0 d v' u 1n °a Lzp Cy r V d Cu Eo 4. sn ¢ �°. .: q1. es' 2 e ss s. yQ 0:i o O M C F Y 0 9 a 2 .Y �' Y . u.J 2 9 a Pti 9 q N z p -_ a a.L ` d r. a q L C = d Q d L°' •0 C �V P Wyy pp y = y .L. .V d. ' Q I-00 W W U F 9 O C Y 8 O n G 6 Y tt O O 6 C 0 3 CA A a C C in y N m m 0 T. = F b L i n o d § e n 4 "O a C E a72.1 '4 .4 a j °-1 Li t. On �� a 4C `S papa °E a O „2, g C m � a o a & L.; n a a 9 .o c o •� .2. E .S p; C W Y 3 o q o =� u u E ° o m E e m a d o C e 9 d ,o ° 5 V1 .. 7 d d ^7 Z. "K v u >, e a a q id r e . .. . E .- Y i ry c y - 0 o c U C� C ep 'W o : da `°a pU., h u o D c z' E ht z ° °.^, U cc ° U - `" i 6. p P.L. = Q p`. y -E — 0 ` . O d ¢ S Q step z d a •• 'W e a F? �'O a o S c 0.i o '° O �" o O d .. u a o 8 ` 'E 0 .4 3 a :? o '� u U 4 A, ea,a. u e c F y .g 4 C Z w co s w°. 3 80 „ 02 — __G-1.-. 2 = Q40` L E 4 o - W 2 w z 7 c.. a U V ' ` u ` aai Cipo o E y e a v Q. ,° > •v O PUi aci p 'c cV 0047, ., FS. a i. E R .d+ 3 > .�W. E T. y v v y .N t L U Q .-« d W V U if-7 = z ¢ vn ¢ ¢ d wit e a s .. .. « e 2 g E y F V O w C = I. Pm in O m eo a E ;W c �° t 6 d y y e m g i i o3 0 * e `m s w v h z � � c r = E e • y o a o z z `o E m u .`� e 3 2.00000 V Q 'P' d ®❑ ® ❑ ❑ Q ea w 0. = C k. E tee' a V 4- m i O - ,' i w 3 o 0 ° U 'e '0 Y z N ° Y z U " CO m o O a L v C7 e m .S O c Q — E p�J• .0 o M .. O d 3 y' C T C 0 w al .� 2 ^�. en Q O t0 .y O W 0. n i, 0. rl.. t o, N N O t rep ,° u 0 E C O ��yy a e m 4 N ` W o d E 2 w - Al 3 S/ E. N N ^ C 0. > U N C C d V. ZA Ili z o c 'A 0 .. .. .N-. � J' w C .9 g = ° uE. r a°i .e. k4 44 U U o > c s d = E o ` W u y U Y w = d c 3 ;: ° a e m 'dl W N N ° wE s a t N ti z rep 9 6 ❑ ❑ e c o ❑ ❑ o e r- ,„_,.., a rc n S �_. C O e u W ' 9 v g - .. U 2, 3 ¢ 0 > a c.. V o 0 w r o v o 'e c.:: 9 a F .. O > � d 4A U O 9 d d m y a w e O cQ u 9 .ri " m d — 0 E .O . S z ee m z d o W c C d E 0 o a t t n r ° ° U o d v o E u t t ° — m E E CO O et e g ° s o _ O. A. 11 .W i r C .82 > 8 ° L15 O 1-'8 . o ' .. 1. Vl 6 . m d t O C - E d e Cr ,— ' . a 6. 3 0 0. C C ° U ',—o, po c E _ V) L! a Ir O 0. `a o 9 °f' c E " E r, r e F = ZS ^�. 0ca c v .. e Cl., .o $ a W o bE '.C Z d 3 ° .� d n = v u ? r .. > a 'r ,_ e et Y N V) :" Y N to -Fr.) .R C A e , x E* Ill ,a C ^ 'n F' o a 8 a. 3 v S o y E - o v' C Till; t O 42 iLE-0 Ge W U E x rep m o L® E -0 . 0 0 0 .. c .., a o ? 4/ 3 • N m oU L e CP o '° 3 � 3 Al E 9 rL = z a O r o ^U7 0U 0 o u m i '" A ® ad - Y c C C c v wF 0 C QI m .7 4 ... Q ❑ Pd. 6 ,p i. 0 ° 9 R 9 y d O N w 9 > V T op N I0 .0 E d d c .n t e.o C 0 0 0 0 C p P CO e e E m n0. 6 E .a Q z zA a` c .do N azu _' o o' oe � z � a = F T " h - '� W o 'S m o ¢ C P. A R v d ° d ` ,� 0 9 c. :To a i o o P y>-' c a o S .S c E o .y o .o y - c m a pp a B .E u U 0ci h w 'o 0 H � L 1 1 1 1 c 'e.o a cs c C . 03. C Cr w m w rep w° F a° 3 C7 v) a F H to F ❑ C0 _ _ o C z as 5 w A_ E O 0 0 0 `o w P .y Eg 3 2 k tw u o G 0 d ai -� c V .80 AO a m o ° ° S L: O V 2 F m A O F yN a a a L 0E A h ° U t r gypp° 'E ❑ ❑ ❑ u e 3 w w $.3 N I u .O .y W O O O 7 n v c t n Ho O-• u N C u o O co y i s .•. Q W _, m '0 • 0 o i E* o c ao c°, , C u € € ro L O m .. ^ a < E ° 'i V N e W y ry 4 `o y m 0 2 m E ' E u7 e e > o. c p ..• •.... E m °' v a A y o 'E c c o e e o, m [� m m L T ❑ C �'° N 5g u C d C ; O 'O U " O 0 0 v. _ R V = Of 0 z� ° o .. s ea m e. y o o w a o ° .1. r .o O 3 E a c y e d Q W r 9 53 V E u v e o N N y :t 7 M ❑ •°o ' m o c o o d �' o o c o o 0. d //��O m C.o a N u pi n V .. u u a = H 'O ^ R VI Y a V a '°.F� F " `o a c .-t ''5 ti-- o Way o o ,...Hi euo h 0 t. El a D S .o.. o -O i '9 Ctir QSI V r r v t. P u ai a' ea E 'aa'. c cI. i u^ u o W u ❑ oe rvc c c t .0 0 0 ° V0 N N `v c co,° ao H U F.v ° .° ° =5. q ... O s O ri o, >' e e E < 9 W y. O Y ° O c ` e W - m . o •: o EH o w ° Co u E E _ hot u L W m h ❑ w �'T" O n C. L an d 9 9 ° v v L au O O HN3 y w O O m n V , d G ` ca' N G `° ❑ C U O. " O O F. U 9 C A A m O O u x�. a e ppyy E 3 >q. O A e A ,� c s .y E N '.'. cn . I y ._ W a 0 E O = L A N �' E u u 4 ° c 61 N .° G R c ° a3 ° 0 o f 3 d $ ° ° a o "m a P..a E a U -G, C y V) W C [.°- a y .A w .o c V 9 L c n. fir. .9 U H > 2 u A _ `•' 0 o o d ° € _y ° 2 ® ❑ c � A °o aov � � T p s E a y = '° U w u L • y cr.; a z ° ,E.- d m G — ° CI) i. a Ca �+' m y m v a V 2 E ° 01 x 3S ° L a Zs iii > E e e W H . a- - q a ,40 W y ❑ ,Y C « - •R• y O O C o y m N a m e - a a s o - „ > v F o o m V 'E a a e e ea c E, = m ° W ° y c " z c xu. ❑ E °0 = 0 ° O O C ¢ O �' O L .'GV. y - Oo i O"y Z y w .c. z .. c a y 4 s W u `� . - E.=—-Ce) a c n., t' ° > .i°. o o 3 p A m u T ?`m o `u iI„' W L ve_ > ❑ o o c y e a z o .� y a�,y a 7 F co "n s m c a W m L z v v ° W N X ❑ u o o 'o E o F > ; Le a a 0. `�\ y0 ° o u EI r L m>v e O Q o O p V C a b N N n\ \ b m n y O 2 O Y E y W 'O O 0 F L O N O O �\ c u FQy' L SiQ '�' ^y o a': cO " O W C G O O O y�. -� O M 0 g 1 F . Oe O. c w O V G r� G G ° a % o .e+ w c°i ;`.�y,T ; Q a .°'. �._ p ° .. o a. u ° G °C G; c a a = 01s e E x o ° m �" U .0 ,° a+ m a y e A � d o E s . y W O p E 'Li Tv- ❑ I� Z .V.. 5g Y 'E O L m y = c...)<---o$12- c _ ceq P.� E .c. o a m p eq > E o go 0 O g n a '$W °e I m u Mtn e ° i O . h °. u r, o c e QI „W„ `.° o v m 0 u > V 6 0 R h $ E W u V v V _& a y .c.- E Q rn m°') y .E U a' 'c E $ o U' .°. °' W e .� x U c c H° a >' -AQ' W .� in ° p n Lo .. a i .a oo s a o ... OU o o a. x E I o ' m — O `o � �, O 06 O G O V O . •Q O E O. PI F .G 'k C e ` O c C e �� z '` > v, c4 Z. y e w W • 0 a. >. L ' C S. F id o N C 9 P d Q Q ❑ W 8 ❑ V - O. V ❑ N d m- 6 C U) I CA UJ V? _ U) U) A a. Z T o 0 0 0 o -5 e. Eii r e ten v° ..-- ‘I• a. `v Q p, U .o a - E Z v ? Q114 ed,1- ,°i en nt -1- o .E ah. 0 e 3 0 0 0 0 0 � E v Lu C- ch e e r a ❑ ❑ ❑ ❑ ❑ .7. ..v $ � � a E '�i Mom ❑ OO El n DO El W U a e o00 e C Y V N C E: P ` ^ T. E t C J W • y b v ❑ e 1 ❑ oo❑ o xo Nv � sl! a lg O ° u u E �°. .E .. 9 s m 3 0 Lu L. x �_ E • u. N u ° ,ill ° .m aVi `v u E ay a <a °o ', c a a 'E • o v m o >o c a Y Oy C .,, DD c— .a. u v v ca v 0 U v N. 'E .0 L e a a C 0 °P C, e 4 E =Yu 0 E a s > > > > > °e v E 4P1 a 0. Q, Ea a, v° s 0 p u o U r V _. tui 9 Y :: > :: g 3 Te a e v > a .`°. s Q - .", r a .. U F' L c ❑ ❑❑D ❑ E e °= ° m L tee, = a _ _ R VJ a L E e a E e 'y a e �... e e Y — u U a Y V "J e L Y M T dA4 .� T 0 a .Q E V O O N T 0 o Y 9. u ep.3 0. ❑❑ i, .E .o C L .a .� i e t c ¢ cn Po C a E Y C L L 4 C ` W �. T e �. > °� 'a0 E a 6 ti f"� W 0 U N 1}� ? u E U o a > 4 m ? a a � o o v pY OO �'O o 0 W y A' m i V e Fi u .v� L V c a vt 09 e y Y U C € N 0 I c O 8(AR = ti T o z o z 1O z C U c 2 ; .. e m g v u o - z _ O >. " e z O z y e c - a c i° an o v o 0 eat a W C o EdoL _g, 4,4 _ 3d F � � � � °� ao � ¢ � a w { v ' .% 7 : aFa a F ° Ow �.. Ow 4 lo E d u E C W tai ° 'E s a d .oi c r+ c w E Y a y a c C E z m o -a v .s v a F 3 �� t 0c 4 a v o o € r •� - N Z Ci 0 C OYO 00 A t° 00 s a `°' G .+ `� a a Y - m E C o Ye e " `e •C .C a re a 5 Y ° p y d o a oe S e 0" U U Y Y O T Y o a ° f0 0 u a K C 3 Eis 0 = - .o 'e C V t V O N G OO = pO v w R 0 O. V 1.") L Y tO ❑ O �" y a w a O O a ° C eik o c _ Ci E a a GI o c = W `° `= a of 0 o 4 o o TI ea d m v Z O d s' a 5 a LO — aL e` 0. c.d o `� a s No N o € n A v°i 3 m 0. c ; d `°_ �' kZl v 0 _.0) a a, z y G❑ ol ? LE U .4 o s T °e- a C4 _ E > O a0 N 9 j e=e -E P. 2 .` 1O JC °o Y ak .. 1� CC c a O 9 � = r '00 Z v Y a a co 0 s u L F. .? s 'c o ,a y'' o a n it d i° Q v t�0 m a E 0 z w e O W v5 0 0 m UL. ° O 0 m ti = ° 0 tilt •-•'„ Q z v) w N E N c 76, O E Q m e E p W 0 " w O a e a 'di = a ' --r. e 9 U 1n xx' y C. �_ w L E C d 1. 1=-- I. OE-I a a c a O c o 2 v .o°. e3 _ 0 u e m v _ t° v tilt e C l w s 8 m 0 N U u ° O C u O -6 „ O 9 C a a . E v = ' '° �-. sY, n a U o .o o v o f 2 4 a F .- Q c m a '° ° °y CQ Zi S o O m o 0 a A ro m 144 c `t z U i° - .0 q3 4. n J O v m r 0 9r� ...-0 c d U ` ~ ° a ° a r m P. U N. J C 9 O 'O a O Q e, .j tN N LL O O ° E. ' u Y W- ° b E O I: e ≥. = t ❑ e 355 a ° O O 0 0 d > m w ° i4 z O K o `o a c Q t '� a - y+, 4 E d T 2 E a E. [� 0 a- 2 Z m o n y0 x La� gia ° z n. 0 9 .. _ e a w x szi'°+ °e• ; F-1 0 cD CL LO C N F =co Uco 9 p. Y y p0 ._ v .0 L 941 t'a' L L ` O L/yl, c G w_go, N L' 16• 00 O ly^. a " C a q a y y .e. y 0 A to r N G O p C C M -o 9 F ^^ ' .O .E € y > 0' w: > Z 8 6 a w d OU c o tc c v c v s 'o m c a m 7e � 2,* a a o m `o m.�9 a � a i o 'o v u�°. E 0 a `„ a '' V '„ 0 h o Y 9 a.a^ ° �O L W ac . Z > > ≥ ^ o .' N Q- 0 v on ^G P E Y 1. s °e ILA^ 0 0O q Q O m a Z 7 ❑ a. o. N V o oY. 941 0 , C CO y 5 'y 941 9 - 'L m y 04 a °a m 11 N ' .. w .. c .. 0 0 m V v • 7 L v u O a•°. L Sry Y 0 v ai C C m = o u ? pa e° ,n 0 n °a `e Q L E 7 E c C I. Y Y .E o f v ❑ o - a a w a ,4 ,..•E mE p Uy E ,a Q a .� -0 c a E U c .°' Y. v o o v y v 4-1 Y a `o Z .. .. :q ° p E I Z Z v 7 0 v a l e a >, m e y _, o l c, g y 9 m y, N O c°a i Z W o c ` -°a a 0 00 c Q Z en v $ Lo q _ °' C o Q o 0 4 > T c E g 0 > c = E ° c o `� $ z o = $ n a . rn F a '- '9 " L . O 0 o a o a v 4O' a >= a k a it, 0:E t .2 u U w u v c J u g = m a a p' e W d CO Y L Y i° Y Y e = O O Y a L 5 0.4 w ce a co ❑ U ♦ ♦ ♦ ♦ a 4 a ♦ Q ♦ a a - - - . N N C(1 N N ° M ui a_ w° m = a s o o c o n a o. a n 0 w m o co r t — v c Ejt v .C o 2 m H 0 m m — - U U V U O 9 c c L v H .�-1 U E g N N N NN o N W V V e e c o• q ° W w Q Q Q Q Q n d en o — 0 0 .. co > R o f ', O o o ^° m ° t O 0 n• O O O Wn,, a 0 0 a s m o o OV O O O O o c c U R .E .. II 9 e O o a. " o O 0 0. '3 o °' .0 ^ v 0 o c.J > i a m m yo v = S u u u e W v N O J D o o a 01 cu > a x x c g a O N W C o u Po O Co - co v x x a s u o N O O u U m R .0 E o 0` 3 0 S, c c e P O •E. c 'P. . U N C a .Uc. c 6 9 u `O 'C 2 i • .a ❑ .E 5 r u c a a L U c `j E- y a N o a d fG a s °a .y d _ 'ayi 3 Fi ° 0 u • a w w ; y o tt .o . a 0 0 iq ,V q pp dip t et ' run =a E'm`o v 3 II c .c a a W (° 0 e o-e c € i < E W c m to o Q o E m "�.-b o E c, d' o 3:, O u 0 U =e u = = `N' a L u v . Y .a ... d d p 'a O n a� G ar N Oc �% • n co A U o o '' 0i 0 ° p, - s "C u .2 c 0 EFoo '� ❑ > co i' CI ° E $ 3 s 5 L U 7 y .% O 5 N N n d - - C a k (.. •o ." < Y a g y a r t Q a E o a Y 0 Oo O d W [A E eQ o } u m m To E E 00_ m V o I A¢v 'S. ❑ 0.1 u u .C. c• C d E r-a o w oa a -t z.;:,' c c w '� . .. a B a q 'r o 0 O c WI O ❑ 07 . o u a 0 O y o S N. 3 rn was a a' a E e v_ O n L O L ... >CD 0 ✓ W T .Z •O - Y W w E 0 z N R m = .E i' `o ° •o con .� o V ' G. 6 a O y C 'E no fE a 'a 0 a .. bb ca a a c0 °L' 0 CR CO a � � 3 ^ 5 .E w O o '� 9m m •m v O N N dy y o � oa a. e v II a m .°'. 'S az e 8 O CO . M O ' ° e s A a a E _ c ° V «E m U 'e r E C W C o O o o O d Z E , .0 o y 0 w o 08 E 3 W h _ S Q N - 0 C , O• m ° .4 _ l0 V y C _ N u u o 3 oee 'E $ e 0. A Vm F O N U e ,a o q' v Q H 8 ^ > d si e a $ c E C " m2 a z '_ a d s c m 0- Z 1 • 3 U I I o `. U' m ° o q t a W = w E V)ca E m E m a o Q E n °2' m v t z r U U a a ct u Lo Y 0 U 5 o n 0 0 .= o cC n 3 $ i ti ct . W • a... Y E m• v m a E - c e C q o. e . L 0. rr c E v. >t) El :: '. m Z0 0 `e ,o U v _O e < O. t, a ` 0 �.. .O F " 0.. II in Ho" 0 Oft L �+ r°°, _ L'.. Vi • cn dW o E L d E A�'` O A V4 E W L C C Q 0 V IT.' • Z O °m .�' 0 u C C. p .2 d IY u Q vi C .t O Q a E E �'Tv z � a ma = Wr CO `o O 9 9a ogu'�, a u., o y o �' °' c u ° m y w` q m9 " 'a Id y >w W k O u C CT) E 'e m 'o S 4.T.. U c L CC `�▪ 0.- r; L V1 i5I co h .E V e 0 w a W E e 6 C E- x C 0., I I c a I 0 2 as E 2 I YUU ',"n _ v c 'ee a d o 0 In c o o n E o, U 'E c = c E x U ° r a t a m Lam. o ° '4 O a u H ° v o m l w = o o v d = d0 O m z v °y g E G Z > U x t 0 i A a m p E i a. w c U $ c OD OW oo � > � L. � gb S 8 o z ;r.■ Y].Y V . .� _ _ 0 C Z� 00 N N Nq O y 7 W ,� 'ti L.0 6 Fj 4. V b °b� O, a 3 G G. .A V �^. rei NI M .. aft i �' c .. I R e+� ea .. o I Dip ov e Y .8 a o a = e O L. I .8 L. ^ ' ..y p Y Q _ .0 o i a. 30 .. w A ^ °0 vl Wp� a S, qa r `esl •w .O w s +� ``�' i et CC�' Y 'JY' G O O O m 03 Y �" Y ..4.. oa Q G C O .2 s a0 `7, A A Z a g v . Y C 1 Lii e r E ,Q H 1p .p ¢ =S ll Y ° e " Y 01++ 1. 8 N O .a 6 r ❑ ❑ Y u O V C i If7 s g i ti.1 $' A 00 4 r,' r v i - rp,3 2 $ 3 - v at e d �°Qa. # g c ae 1 s. In u ■ .a, a aI oa. ♦c a,,Ue� o V .13 .o rx. S° .r z. o �o p go �'O 8 e °F° o C) u t� co)O O Z a.. r ' O. ch s" -.=" C O Al A N a gill, as t o a s ..1 V O o m 'y U U �« -.F 3 �. . Y V V �"� Y r. ,G V @ .� li.8 .Qi H < A. f: n °' w v .• ICE ° . a o a s a ag ® ® a w ❑ ❑ � y a 4- - r+ ov.: - S 3 4, N J1.1 a a o Ks 01 o. ti _ — G 3 w Z 03 10. > ` 0 �1`' $� .7 0'1 jf vii 7Y ❑ C ba -- ---t '� O i "�1 ferry Cl" �D a. ~ m. �. T O ..a ! !V 1 N i Q U 1^ IDGX D r A^ Q 1 i ~ U, n 9 co •7 .� 2 E. �y Ca n o uii i Y W vt. U U . ≥ a u. m ,,, "! 8 $ d Y ° y x a. • w zy w N § 6 c r-I� rn a a 4 CD Y d 8 1 K Y V -o a Z � a, +� v u a r, o a Z e A. w -- i3 o ea X a • I ,o O 'VI p o �0 NI � y i • j 1 4 a B C i w F $�� e 0 bC z� Y w Y 'd = Y 4 .—Y. v a r., �" . a �. at 2 I �.y � 4 " >1n R ^' E. a w Z Y u t a < a w CI a o �y . Pc 5 I S' E 2 2 s�E o I B S ►° y rrj LJ o a -° a Zi o �° Z .. M V h Y ® 4r ° $ g. phi 0 la a W C G _�- .4 N on s n O«a E Q ' V r w a. O •Q, a i. • 00 s 4 •j1,•' i E 6 (m,.r LL oM G R1 1.7 0. U a A. A« o 1 4a.. Y °P a 8 .0 Sea S v S# Q L C xiiI VEE Y C h m Y04 3 I 28 la 4 C7 a. 4. a -v a a. c/a• 6.v44 D -3 I X Z I .0 o b I $ •� u 8 f a g. 7d, a v4 ;; A. 3 • f 2 o w F. oQ II e 'Sils .p M Y 3 .I E A ' N N N O 1 C ■ gd II.o 8 P �i �., fp y 9 T 4 T • ■ ■ v 4 2 �e v u O c2 `a an P m A ."e 4 < i i i i' f f E. is o to U3$ 5 n O C n 4 $ 3 U g 7 7 C o met e a' Po ..2 co 2 $if al ° d �. t„ e m C7 e 5 a 3 N �' 0. u ' b e. .x I^ a te E e d v m 6. F n 55 9 , � X2i. z $ o ,p O 0 G7 0 111' 3 C .9 < i go 4 b � { N •— � O a . a < a3 e � it 00 00 '0 °e r• 0 _� eye 2I ' 1 I m e ... 3 ijj 0 0. 7 0 ., a u I Rgr.' E b "t g u a n'• eri FS 341 _ a - e rZ 3 11wgg II S o n• C e ELs I Ya ' ■ . .•.st . 3 0 is t I. N u gyp[• .^� C O �ygy > ® • C''s p[• p m ✓ oba • O 'Q Ti ❑ 1 r G1 aO 6 a �. i 9 C 5 a .a 1_y v.• b a Q3 O• u Q d = 0 i 2 1 -; 1 a a kv. E � a �t8 d fi & . r, s _€ o a ti W g 3 E a a �- O 'e � a m g s rd S 3 z i hO � LOn 4 S P. W 1 e -, > z o 1 el 1 0 7 v d d , CNICr) a ,i I 1F 2 W 5 '� W0 _ ar aatl1 N ^E' gV 3 i °a ri1q F, 1� - CSR e _•' 8 > S v! 1A V1 v1 P P O 1, A O ❑ �. e G P P N P X. y 4 E W § Q Sad eldagt € £d ILI Q aU 3 - �Sco S o S e e E a ei ° = > ® o g 9• „ate u ''77 u 3 • i o QQ20 - S d • .• u @ W C N Si ; 0`44 7.4 C� y u w '5 '2 e a. a v & g•v 'Q7Q�7iij i 70© a� ij C 3 Y S 9 E Is E 6 E `�' U ,-4 • q yy Y c C 1 « d 0. 0 t a s■ ■ a a a R .7 N g $ G3 $ � � � ° • " S ' 11 ' 9 a " 2° Q V pp a a'F$� > • 2 C U U U U U U � ' V qav n ^J ] 7 ' • - -' ,� a u > ≥ G • 5 g A 421 m 0 0 a ® °' m F is if a fat V] y 8 L E `o a ry 0 G .. o. a ...) an a ai C p a. a C LI a fi Z a mm � E ' a s a 5 ¢: ey u n ry 8 ran+ $ ,�, vie 9 a u g_ pp _ o a . u fi C p C _ s e o oc. `o a C : e >. G Y .o E .w. m g e�i �a ao o 'p a € a s t. a_ ... s.12 11 n" z a0. C� 3 a, �! 0 O i 8 `o E 7 E F "p^_� : r a ,co a-3 a 'g Qa on t m 4@ 1 of F 2 Y m m a t o f 'a a s 3 �3 -e: $ _ 0 0 al rE. • b y 'e a 4 u B .Y. = a a a. 8 .'s it Y Y a v e o I .' Y K ❑ ❑ Y V 9 C a Q = T 2 E a O hQ K K d _ e qq pp e '5. . L L O Y • v C .a.. S1 O Q i w 9 6 y p^ U� N e U ^�{ L L L t�] p7 & u Y a I a Y 'O .y. O ee La'G m E. e V O. qq . U . Ti Oj •L a = O W z re U p 8 ° la. �• O a U C a 1 t ° 5 i O -E M '1c '� o 'Fay,at • 3 9• p a L 02 ,??a, ` _ C n 5 < ` s a' 4 ; R g U cEE -- ou .1gU$ ii We g W 3 1 z t= m m 2 W „ . pp GG u I. Y o r t a n .ti c Y 2 o V � o . aI U €J � `a E "n ii Y in > F O u E I a o a. °v = o .. y5 9 E p a pG ® ® e,e a" ❑ ❑ a g _ A x a o $ ❑ ® O o `.t a z° 0- ~ " igg p, a n T 2 w a IV J 8 '� z a e > $ ?� e o 0. a a uIP e19 rv( ❑ U O a c -.77 �. 4 I o el m R a Y \ 3 mi P e ry r au °E y it- -... a Z" 55T i A 3 V W I N Y i• a A '§ p �V t. g. e ^ n a ge o f I I 14 a R O� cryy u o a u a. a 32 W aY -' E X $ '! _- U 4 G U o S 4 £ a a _ N 6 a Zm f:t N Z �.�' r rIC7 y : F1 e 9 1 Z T .k% I. Z.s s C a z. O a I.7 is as �` T Fn 5 4 O S F d d 4 p 3 ; i .p C O S 6 9 r�r NE. .. .. > •� v O F I a In .7 O 4 Z 2 V F v e a Q x W X93 >15 _ F' yE .e E a E a E f. 41 a l r w w EA m s O 'o a z d "V - a g a 3 E.$ 0 5 • n 8 C p m a m _ `� E s _ e , o r 1 N V " `e la I. $r m a ,a ,T., 9 R° mi a; Pr U •Q A 4 P. 8. w a m " 9 • Ea �' S 'E Y S"i C1. E fri v 0 °Ell g $ a � Ng a a € pay S IIt' z z 3 9 3 s I S g '�, .3 8 I . 4 a' E o o fa. i E o �j+ Z °a p a . ` . I-° "g mg C ., S a . e 3 a a U m 8 s o vo,3.,Z W t o (..) m a r5 a z 1 & 38 m A ❑❑®❑❑ ❑ >" ® w p. c m ad. ixW o ° I § i egeea I a 11 1u m I E $ : e• e a gal a e 0 .J i `o R r7 0' n' �' < roc' E .� 6o °� e �m U s < Y b o a E It cr) 2 9 i :. 5 m = § N y` E .. II �■ e r. v ul✓ • C - G. G e u > a'a a .�y i s a M . 0 e 3 o a on F G7 tell I 68 na 9 < m a` N r f�CO Z e .g C w p" e $ N r g r (Dm Z- W W E ' a 3 0.yin - 1 o r, B d 3 0 Y -,1 CS 4 ' O _ a, a E — °' ° e .. Tr, e, — a i 5 �. • a s 8o e up u �+. co 's a g • o 11 a 6 e. 7 e ' fix ; z _� e 2• 8 w 8 —� 4.9 . E .c ° ° t3 r `�', •� rY ap $�j. a _ �)• N •• qi g 7 �i• S� S C O II E i7 T ✓• i u 1 0 4 u Y ® 30 a F S ■ O Ea a co, ' a<m - ❑ wti - W a $ e r r v G 6 # , .1 ,3 gg - w C E S� o p U. E _? c " • at 3 1 I A z N Ch W g o W < 9 . e 0 d- a q E ° Q 9 w �' EE a a 'R O) = u E u m 4C e 8 .. (-) it — a ' i4 $oe • VO OicN .'� ala q 'Q+ aGA oat l Gel E-. q • 'me o = dt9 � S" at C L B w n C O O O �C `� ate. .v. is X' X' X' z L 7 s Yi et a '4 Vii i a . - 8 V ; - en W E a., B � °a ° 4T Et D W • u C $ c4chi 2 8 8 8 8 8 is R 5 W N u� E.-1 >z En t " > C 9 :11A o igvt. eBa ii- tatF"IIHb ® Q I u %` e e a. Vr H p IF p8 IV ae °O I " o�o +�P.' ga p6p LI V 2 a .� m "e w 41 S i t Y , U n C O ii i y i,, a _ o — — i w t a• a B 4 _ f,gii o ° 2 a a E a E : B E e d N m�'A y $ vci o O 'a t el V p' ee 6 S a e a .°� £ A a' 'u gg vg > E et a w` U S u u u 3 7i a `C U vIi an $ I E . a a I C� 1 9h 2 0.y A. -C C 8 r= N ° i > o = a F` ❑ C a a ; Z u 9 0 @ 2 �0 a, u ❑ ❑ • a ® a. m F `m x m rik m^ =u o v v v° q U 1 O O C4 0 aO a - o oc in u m eaL >. E 2 ua _ _ .r'. nit r-- u 4. y O e C O _ N N N m y .n e a— e g 0- c Ca m 4., E u g u . W E o. W v `o Gd U a — E ` oM n on a s o o 9 5u. j 01 Y N' G t .� ... C C �. v or ice. a _ 2. �. C C E L >0 U C = E 3 .c O i° 'C .E 00.. ° u?C O '0 p ' � = 0 a 0. 9 O e .. ED u N W .. u C € Z O y u 0. ° .. c. .. 'e i E ' c .�', °g v a. a o a 0. D., E E �. E m " 'p y_ 6 rui 0 0 z, vi py Q 0 00 G O Q ' N O o w 00u PI E u u `u °i .= u c' u ® u A Cr u ° 1 u 6 N' ¢ m > ° .a .a o0 y y 'w u e0 y 2 o o m h .� c y r m E e0 L " L c .. d 3 '— 9 .`. `n 3 u w .�. t g om 0 0 c 1 E .2 'm 3 0 go a u a. c >, E oat: s u v o >. >. > y 9 O F e y ,a a e U V ° M."E u a o = c o CN ° O. 0 i co .u. E `a e y o o c E' 0 w P. on c '° °- o Z d o A c ❑ ❑ L s a"i eo o m c o G C en in ° Q u c. v v Z >, y a s >. C3 a s u a .a ..., _ E w e o E y z o 0 CI u w c W s .o C u c A 'm > w W L N c o Q 0 0 0 ry IC INC V C" C U c .may C .v, t u 0 d > C:. c E G . U W ° U L ° L 2 V E a o O c z a s. ?' m Z u 3 w '- `o ° 0 p` A? �'O o o .c c c u u ¢0. L Vl ... �C ) < o O E c ° '`� o o c — h e cn u c..) u c o u u d c E 3 e 0 d o u .o 'n t v_ = a t .0 E — o >°. u u F u .q^ P. a o 0 w 0 °c d .. g q U u c o _ z 9 U U u°, O v. E 9 O. U v .C x a o E u "‘° s K E ° 0 0. aci p 0.` E W a ®® i E g i '3 Y ,E Ca „ o c s u _ F u U d w G a Q v, d W v Z A ou0 m E W ° a .. 0.. O c c = a. .H ro t° c d C d X .. - U U Q a o E E C c y = u _ E E. m g — a. V O c o 0 0• i v - 3 o o m m .Tu. O c4 a o a a ❑ ❑ a a ❑ ❑ o � a o � rd 22 d o Q d ` Z ❑ ❑ ❑ a -z v O ❑ xE 3 v u o ii >. .M. .N. a o D. 3 ` z u eaco m .. > - X v 01 o - A d 0 as �y 9 vN, e ❑ U a !e� o `y A r21 - 0 en en en •--! M I. E G 9 G ti > 0 Q r u d a a. v 0 V. T O W _ v T oo S N ° >, u > v. 'J to 70 O ` o. .oi N 3 0 _ d W o s0 .P O 9 C 0 .Q N n n CO ® .. ° a s u CI []] Vl 0 0 ", 0 9 y it y 0. 0 L' U Q d- U U v y m .m c W. ti u a F v u. 2 7 W N E y o r l i r, zt o r y > O 5 v Z E N o. F o Z t a ,z' E o cc! ei u CI TA I-I m >, O Hz. F O > y ya4 _ N C ^ . CID 6 = NI E 11 CM U a H W e � r N F 'Zn 0 U Ca - 3 A s o F m C .A > V o u nee ;o o E °c E .. A E X o o I. '� o O a .v'. U 0 d .2 0 y PG U M) W ea i x v' E, Q u _ .. .. . > 3 o. o *4 N � E 7...2 y v' c o o a Z a " w E � ; `a o g y °° U. C d m >. a _E O ? 0. 4 t a t c c m m c m z E x c u c 9 u es. 0o u 0 .E m • ,1 2 o a m c g !.0. N i O c`o U 33 z V E C) Di v 9 ..c ° eo c c •a oi°o C. a i. O m COJ C .n. j P. C YO E 6 6 O 'Q W Y E .M o .1 d y n e o c u u u .? .. A v e o O 3 o u eo o .. O E a> O o m A •c m i V C� e G C. N.' R a ` ,0 v u°,o y u c i° a o g 7.0 aci E ' N C c v y o ° � v° u E `� a E ° (° :% `w ` g 3 A aE E u E m v y ` ` o 0 .c. so. no U V) a., o 0 E o 2 '� E z z v v o v CI c E. a U a o v 0 0 i a. m ,r >, ` .a Q U Q en 0 ` c o z ._ E a c° .. N ` Z W o ao o — o c� a. p ._ — c 3 E 3 a� r7 E _ t. C o. o .C F E C a G E. C7 0. U P7 O 0 0 y O K o u E u le w n c.c.') vi o n ° z 0 3L e ca ❑ ® ❑ ❑ ❑ ❑ ° >a ® G.. T ems' a Co y Ykn In Vl Y co Y Y Y = 9 o o ,y v — �, V m .E•L ' `o m g Co' N m 9 m i- v Y G N N N u v U m 9 �' Wo. W o A ye y e y e h y It y h o w C V4 O W 2 Q Q Q 2 2 2 2 E o d3 .°a 8 'K. V �` .. 9 Vol w a A — O — C ~ ry �' o R ° o Z. .C .5 " 03 00 C7 aai S .E c c a _ 4. C ` W y a e E o c to o e v: y .. O b o O O p pj o W a i 98 I. y I,�. `Y m v e�i o e V V C u to c y E m E v o m °' = g av, F co a C Y .4 v h s a = r a fi0 C7 rz9 N = a m _ 04cll 'CI > L O $� u .1. Q q O W a Y at i �' C .......@\ F'++ u 'T ,3 R o O ty e O - VC a+ a E O 3 F . C F., e a N ^ ^ h m e q ? co u e e v, 0 0 0 0 m E z .. Y o v v Pa Y a, I, cE q v In 7: >-, ` a ¢ I.y ,O W'C c .. I^ ` cc a ?i a C n LTA/ 4. Lam. rq N OO Zs Y e. A o o f Z 9^a v Iga•v 3 N N O o E 2 e 1 •• — v - C. . T. p. - F i.. ^" 41 04MI o d o o - W = v a.y to E � a I. E00 " Ti m �,° Q o a .°. $,., �' a o 'aN� u �- o ..o e Q U• d cn .. =° s o �. H E y o o O S Y i a J 0 " V N C V� Q O m .T, ❑ ' `w W L v, c+ a a a u u Y C.4 Y p 0 -- 6. `n ' i; a el 3z ti ❑ °i w. o m N. o .E 7' 79a ' ° O 0eq > 01 4 O 9 a7 •O v u •y a N c", 3 w o e0 a d a = e i E w ° `o¢ g 3 U a - ,y m c a a a a a a a a a — 0, R R R 0 ✓ ' a W R 3 5 a C1 'Z N W cn co. ` E'' a o v`°i 'O "P. �. -- . "' d m .� a E - `�a .� _oo' er_ '' ti Jic Go, o € 9 P. ciii$ e o. H a c • W C a V` �I ": T r 4 E t E `�. y^ ,g V F > U C 'E $ FC ' m = .i. b e vn ea „ d c .R. pQyl 2 2 ® R Vmi O O O N• O h .�i o C ci cU "J 5 v° W a c 0.C C •o H ^. �d 3 Y .e. •as Y E u c ;`14a y m� y Y c >a C e = ow d = . , --q °' ai a o o a U r. W W' u o E' C z L y. 9 e C O W a T a Q z a u R c4 ci _ co II • 3 V ,3 q a -' o v V d F is rnrn 'O 0 w¢ 7 .. E E `ca � 11 .2 a L'0 >, --4 1- N 2 a a 0 > = v Q V '.' R y W O O O O O O O u N Y' R (V iO U �y O O U W O O O O O L 'N, , Q 6.-, M V y > C O y . • N o °“'-. NI $o�''' ... a Y N '3 r re" e N L z" it c y E g ,. .g U A G H 3 ® •• O Y E 0 L 0 P. a ' �n e y a a ?' 10 01 EO Mt 0 m > > O a /-. O ti E .2 c., Y u d W 8 U r °.1' ^ .. Y 6 W d .y v `a v V] ',a coc p ►a 26 vY o o •y t a p O 0 , `o O 7 E C1'eb 0 c LY ^ c .' o r a � a E u ` 's Q.,, Z .� '. Y v y U a 00 d o `C v Y ' W U 9 .4. a • E s ct > o C yr, E Ca `a ^ ' . r , iy •E L. . v w N e o ,j c m m tL w : 4; € U b0 ,• • y ` q a i3 > > i C R O C 2 u 9 9 0 9 9 a \N At �" .N^ s L., ,..,0 v U R U C '� C U C, _ o o e e e y 9 m .1 = N u ae .. Y ° O z • T T 9 `e a C a C C E u ``\Y\ ° '� R >w Y m e o > v CG.' m 00 W 00 00 00 00 Y ur V v] th' '']'� V y 'C U •9 'y C_" W 'E p SC 0 a Ic Ya 0 is- a' T M v v m u ¢�c o '�IrV• o a t o „`�, N c E' ,cm y o E E ,g U x x v _ E v o ti -.-. cm - W 0 .v. K o S 'v� wY' a F+ G p � -p > 2 O O Ito F s X '$ C FOB' i O CI W m ❑ ❑ v ¢ ® cv ° y ?D �i VJ i co Vi - V] Vi To co co ) cn rte O c. o \ V O OD 73 E 0) 0a `Ch N R \ _ 0 ) « - { J w \ ) / — » Q. (13 o E CD (0 c3) � k � 3 ® f 2 @ ` / 2 in f ) § •� ) } o � < — § » CO r ) \ / s { ) ` � f 2J k a - E I— \ ) 2 ` .) g -I \ u } \ \ o & / c / a8 - � \ ( / { « ; o J - m ; w ! 2 § E \ § f \ - © + 3 2 \ a \ E \) \ a D. j 00 � = Ce § ) 0 / ) \ . ) 0_ CD IL \ CO / = re CD I al ! ® y13 o« Q / { _ \ Z { - 3 N - § § » « ) ® ] Q\ / \ l \ [ cn \ r { - # # 2 2 = ) I a § j - ~ % \ § } Z fa. ) •§I k § ) / as } \ k Z E # _ ) 2I f \ ? a Z » a J e eE % »/ e 2 \ : 7 t2 : _ / / 2 ; m ) . ( \ ) ( ° { k \ C E 0_ O O 0_ W 6 \ 0 $ 3 Z ) u jr-. I r r , v V S O 0. : mp r ° ,n omv, o El U L C M C p h r • G'., t.,u N N N 7 m A �` d E a I �E . �i 1:7 b'.O 1Q E '2 2 E ,p-.-, es?+ .11 7 O o. 9.� -o ` W a C m•• O O YR p p w' W c ` o f u c n o a e 9 o rr qq . 2 E. E. 6 o P- > • _ _ S� » w w _+ p w w •p . a o y r5 A cy 'p M w • Y 8 ° • b uC y%P. o a o ° • < o > V Y .L. 6. • oa a 2 .O .aU w a b u Q �� a .'+s Al 9 w T •� 2 w v 'v 7— u "� a o 0 0 a G e Q 54 jifl : V pMi go a x E ° 01 °° n ` 2A fb ‘21 gti `� r I tl _9 T w _ ° n c A .m L • L E r a EL 8 o X EC `. s 0. y - .P"' z A. v a E '4 a 2 �o p Xi Do 8 o .9 G . u.o�^ C E O u -? w Y dCa iIIiIHil • �oi : in ! 1llO ' r. -. < ®® i• VV pA pC• � •�V""--- U ZJ GL r7 Y E 0 O 7 Y�� 4 O • a V Y d 'a U x go V P! P S or S �I C un O C w m C y w U ,J ,-_,•••\. Q Q 7 q a "- "A 4 ' C7 cv 2 C w ,J, V w G w a V g 23 G Yl u ti M 6 • 9. � Q N ry V I5 OM Y o s Z `� 0 ti v >' co4. > J"' G d W • G 3 I f co N V fl V I� U 1 3 4 A E v5.3 A Q a — L., U CJ o > U I .0 I2 td c� U F _ _ I C ° ; Z ; L z • '7 w I .. u^ s y A 7 C i .r L a L 4 • 0a A O to t{X _ ..d Li. 6 u I p 7 aa4 ' ti0 2 > . x �� at -7 i _ U 'aj •b 'C I U e + ( o O C Q C1• k Er • z 3 4 4 R • 8 C GE a c, 0 V: ,.' i 4 u a -F- - T. a a -.4 y . W E ° .T � � N is ^w _ 0 > c w ° a � m _ ° va• O 113 c Aca) • -� a.to " '5 'r- o p og0 a .... 'C7 4 $o c t° L' a 5 ° o ^�. `p! i G7 m op� e0 C? 0 m e ° - "3" - R . j 1 ~ ! IiIi �•�° u yi 1ttLHh1ti ° k 7 I 00 ►w.Z7 C o Q U Q s s ` ` e g g p o a D o o v) 9 a g a u •a t :S o 3 L7 0. 0 O Q o _ O O▪ 5• u a .. z 3 ❑ ® ❑ ❑ ❑ ❑ '' ® Gz+ g � � -� ° 2� 1r. � = 555 § s om : gic m g E € m' m A m m• e G 1 ea i Mzrail41141iiii r CI g U $ o u a V erg• ¢ =i cep u "pg Mitt hi i• I l a t es ! o o cs — re 5 u -C o • a fi Q B Sun r-4" m . At g °• o Ig { 00 OCAN � S 'IS: z a : .a: ; : ; I B p a W E Ft X � o N e d d e m q a ii �_ I esw O 7 .. B: E et yy a El • r I 1 B o a y a Ct € II • a V g o as e' �.7 e w a ,2 � � ,z a �ag �' sj .O p a 9 .3 .� c C. 3 v g -. S.❑ � Wig ❑ � Y $ t 3 O e Q 33w aS C c. Uri o 'S.:, p O - • i o ,-. E LI C 2hq x ❑ 'O 1S .e .5 a r 3 W :2 i 8 C a E `u `Y ,i•3 u .t. °u $ .-; a.' e Apia ❑ g ° t s` JaJaz € . 2214 .;g i w d (� a C .a e a i� aa m F P. e fi 8 'g • B - vooICN ` a i4 _ c d f- > I U JI Igo �fQR�p} •o o .- fry{ m e .E.A m W 2 TI lI Ii ® • C i. a O 4 R O M i CC1CC s 2 a O tl7g O $ . ° o Y uw c? • ? Z _ > h h m a — a E ° a 9e fi(:. CM V d1W a e o a o o a - m as G W y. , ac. n d t 5 °e $ ; la a [r N c It, > ® o• r e .Lgg X7 ' ` 0 0 13▪ a a i:141_, a �+• o 2 .14 8 S— 8� , ai z • fro` : °° C r. M 5 =A.= a qY q Y u Q • • S 0 m V' :\ . o Ih ! 1 ( - ttoff ri�i > a G �c M al G s 0.CCC N 0v u U 'J° 1 O iCg &.p8 >> m O OOSOO "X 0 l I r- S 5 3 � g7 c i �` m • g 9 5 I ° axo r = � > a6' � G oil U >sOx _ x p c a '• IV w e S O a a O zUrngo I- $ k a W _ m rA ,ST3 CO -6 w ❑ N ¢ O to C. -a •- a a >, a. ,�� aco c W EE cn 0 _ CDC O 17 Ch .r (j c` - l coN cm Wcn 0 Q to O Cl N _o ° O e- m (13 a Q L III E m m a m co - C w Q CO - V E CO N id C j - t•-•- `) ad J P Z D ¢ N C C m 0 o 0 CI as W a Q m m @ m e m t Z Z Fri m � xx BCD m x E CO W .c o u°. w ° F.. CD . n_ a a Q a h- o asE .J I'D V J = U c @ CO J O J to = 2 ,- 0 •N U C a' p Q Z', LU `� N iZ vl- i 0O LL 0 Wm U = � � o 01 ° E o �, to I Q. SD a o O Q % m 2 E LL! .0 m N Q O U _ � O EL 0 Q N a d7 o 92 O c='t (j O p a Cl) CL , w � . � 1 . a N W - r @ W 'C . I.L e� C E m 0 N O CO a +. i Q ro Z 1 Q - R.LLJ W C a) > c E c Q a Q Tr CD @ - C OTr N i CO a s a O c\i o -� ro o CV _ C 0 Q .� CJ J m z U @ N cQ cl3 cfl a O Jr) mE 0 O N v, Q ` a) — 0 z g z U -8 ays� ° a �, z ° J a Q Ez 4 a t E m E E L � o or cp € a 0 a d w C O c5 o z u- Hello