Loading...
The URL can be used to link to this page
Your browser does not support the video tag.
Browse
Search
Address Info: 1150 O Street, P.O. Box 758, Greeley, CO 80632 | Phone:
(970) 400-4225
| Fax: (970) 336-7233 | Email:
egesick@weld.gov
| Official: Esther Gesick -
Clerk to the Board
Privacy Statement and Disclaimer
|
Accessibility and ADA Information
|
Social Media Commenting Policy
Home
My WebLink
About
20151424.tiff
4 CDPHE • COLORADO CI CO Department of Public Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board RECEIVED 1150 0 St PO Box 758 Greeley, CO 80632 MAY 1 8 2015 May 14, 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On May 20, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company, LLC - Antelope 21-17 Production Pad. 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, „. / /' l .r'44.,-4_,, • —.,:-7",.--.4,- -i Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 5 " gl- 15 C `LPL-,PWj 1_ 5tis 2015-1424 o A,'; 4300 Cherry Creek Drive S., Denver, CO 80246.1530 P 303-692-2000 www.colorado.gov/cdphe I F. ' is John W. Hickenlooper, Governor Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer , . t,t ., I `,.1876 .. CDP1HE Air Pollution Control Division 16 CO Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - Antelope 21-17 Production Pad - Weld County Notice Period Begins: May 20, 2015 Notice is hereby giver 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: Antelope 21-17 Production Pad Oil and Gas Exploration and Production Facility NENW of Section 17, Township 5N, Range 62W Weld County The proposed project or activity is as follows: The applicant proposes to permit equipment associated with an oil and gas exploration and production facility. This permit covers hydrocarbon loadout from storage tanks to tanker trucks, and three (3) natural gas driven pneumatic pumps. 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 13WE1497 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Harrison Slaughter 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 �V COLORADO STATE OF COLORADO of.cO4O COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT Q� AIR POLLUTION CONTROL DIVISION TELEPHONE: (303) 692-3150 w lai6� CONSTRUCTION PERMIT PERMIT NO: 13WE1497 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company, LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility, known as the Antelope 21-17 Production Pad, located in the NENW of Section 17, Township 5N, Range 62W, in Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Truck Truck loadout of condensate and produced water. Emissions from Loadout 004 the loadout are not controlled. Pneumatic 006 One (1) GIF natural gas driven pnuematic pump for heat trace Pump P1 circulation and water transfer. Pump rated at 600 scf/hr. Pneumatic 007 One (1) GIF natural gas driven pnuematic pump for heat trace Pump P2 circulation and water transfer. Pump rated at 600 scf/hr. Pneumatic One (1) GIF natural gas driven pnuematic pump for heat trace Pump P3 008 circulation and water transfer. Pump rated at 600 scf/hr. These pumps may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days of the latter of commencement of operation or issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at https://www.colorado.gov/pacific/cdphe/other-air- AIRS ID: 123/9398 Page 1 of 12 Pneumatic pump SM/M Version 2012-1 i II A Colorado Department of Public Health and Environment Air Pollution Control Division permitting-notices. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, I I I.F.4.) 4. Point 006, 007, and 008: 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.) 5. Point 006, 007, and 008: The following information shall be provided to the Division within fifteen (15) days after issuance of permit. • 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.) 6. The operator shall retain the permit final authorization letter issued by the Division after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 7. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type Equipment ID Point NO, VOC CO Truck Loadout 004 --- 16.6 --- Point AIRS ID: 123/9398 Page 2 of 12 i! 1-41 f I Colorado Department of Public Health and Environment tsz6 tea; , Air Pollution Control Division Pneumatic 006 0.3 2.4 1.3 Point Pump P1 Pneumatic 007 0.3 2.4 1.3 Point Pump P2 Pneumatic 008 0.3 2.4 1.3 Point Pump P3 See "Notes to Permit Holder" for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 8. 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 Pneumatic 006 48" Enclosed Combustor VOC, HAPs Pump P1 Pneumatic 007 48" Enclosed Combustor VOC, HAPs Pump P2 Pneumatic 008 48" Enclosed Combustor VOC, HAPs Pump P3 PROCESS LIMITATIONS AND RECORDS 9. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rate shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits AIRS ID: 123/9398 Page 3 of 12 Colorado Department of Public Health and Environment Air Pollution Control Division Facility AIRS Equipment Point Process Parameter Annual Limit ID Truck Condensate and Produced Water 004 200,750 bbl/ ear Loadout Loading Pneumatic Venting of natural gas used to drive 006 5.3 MMscf/yr Pump P1 pneumatic pump Pneumatic Venting of natural gas used to drive 007 5.3 MMscf/yr Pump P2 pneumatic pump Pneumatic Venting of natural gas used to drive 008 5.3 MMscf/yr Pump P3 pneumatic pump The owner or operator shall calculate monthly process rates based on the calendar month. Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 10. Point 004: Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) STATE AND FEDERAL REGULATORY REQUIREMENTS 11. Point 006, 007, and 008: The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 12. Point 006, 007, and 008: No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 13. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 14. 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) 15. 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): AIRS ID: 123/9398 Page 4 of 12 ein ail i 9 y , i . T l 1 Colorado Department of Public Health and Environment Air Pollution Control Division 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 onsite at the time of inspections to monitor compliance with Condition 15 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 16. 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. OPERATING & MAINTENANCE REQUIREMENTS 17. Point 006, 007, and 008: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING 18. This source is not required to comply with any testing and sampling requirements. ALTERNATE OPERATING SCENARIOS 19. Point 006, 007, and 008: 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. 20. Point 006, 007, and 008: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 21. Point 006, 007, and 008: 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 22. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: AIRS ID: 123/9398 Page 5 of 12 Colorado Department of Public Health and Environment Air Pollution Control Division 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. 23. 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 24. 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. 25. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. AIRS ID: 123/9398 Page 6 of 12 Ei 'HP • EA Ni Al M To Colorado Department of Public Health and Environment • `,, c q ss, Air Pollution Control Division 26. 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. 27. 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. 28. 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. 29. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 30. 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: Harrison Slaughter Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC Permit For: Truck loadout of condensate and three (3) pneumatic pumps used for heat trace AIRS ID: 123/9398 Page 7 of 12 Colorado Department of Public Health and Environment Air Pollution Control Division circulation and water transfer. One additional well was added to the facility. AIRS ID: 123/9398 Page 8 of 12 .i.r,,,. ..4144 m i A 7. wil,R arm °t1. a Colorado Department of Public Health and Environment a"isme> IthFsan ,14§mat a unit,w era Air Pollution Control Division Notes to Permit Holder at the time of this permit issuance: 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (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: https://www.colorado.gov/pacific/cdphe/aqcc-reqs 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 I Are the Controlled AIRS Emission Rate emissions Emission Rate Point CAS# Pollutant (Ib/yr) reportable? (Ib/yr) 71432 Benzene 460 Yes N/A 108883 Toluene 920 Yes N/A 1330207 Xylenes 729 Yes N/A 004 110543 n-Hexane 2,269 Yes N/A • 100414 Ethylbenzene 205 No N/A 540841 2,2,4-TMP 231 No N/A 71432 Benzene 291 Yes 15 108883 Toluene 208 No 11 006 1330207 Xylenes 58 No 3 110543 n-Hexane 1,796 Yes 90 100414 Ethylbenzene 20 No 1 71432 Benzene 291 Yes 15 108883 Toluene 208 No 11 007 1330207 Xylenes 58 No 3 110543 n-Hexane 1,796 Yes 90 100414 Ethylbenzene 20 No 1 71432 Benzene 291 Yes 15 008 108883 Toluene 208 No 11 AIRS ID: 123/9398 Page 9 of 12 Colorado Department of Public Health and Environment Air Pollution Control Division 1330207 Xylenes 58 No 3 110543 n-Hexane 1,796 Yes 90 100414 Ethylbenzene 20 No 1 5) The emission levels contained in this permit are based on the following emission factors: Point 004: Emission Factors - AIRS Uncontrolled Point CAS# Pollutant lb/BBL Loaded Source VOC 0.165 AP-42 71432 Benzene 0.00229 Engineering Calculation 108883 Toluene 0.00458 Engineering Calculation 004 100414 Ethylbenzene 0.00102 Engineering Calculation 1330207 Xylenes 0.00363 Engineering Calculation 110543 n-Hexane 0.0113 Engineering Calculation 540841 2,2,4-TMP 0.00115 Engineering Calculation The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46*S*P*M/T S = 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) = 4.05 psia M (vapor molecular weight) = 68 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 extended liquid analysis for Antelope FJ-17HZ by the VOC emission factor. Point 006: Emission Emission Factors - Factors - AIRS Uncontrolled Controlled Point CAS# Pollutant lb/MMscf vented Ib/MMscf vented Source NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 17,930 896.52 All emission factors 108883 Toluene 39.63 1.98 are based on the 006 1330207 Xylenes 11.21 0.56 displacement 110543 n-Hexane 341.76 17.09 equation and the extended natural 71432 Benzene 55.44 2.77 gas analysis for Antelope FJ-17 HZ 100414 Ethylbenzene 3.64 0.18 The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4-3)." AIRS ID: 123/9398 Page 10 of 12 1,1 V 2 1:t 9 i 3 4,11 'T ajj Colorado Department of Public Health and Environment aStal Air Pollution Control Division Point 007: Emission Emission Factors - Factors - AIRS Uncontrolled Controlled Point CAS # Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO 0.37 lb/MMBtu 0.371b/MMBtu AP-42 VOC 17,930 896.52 All emission factors 108883 Toluene 39.63 1.98 are based on the 007 1330207 Xylenes 11.21 0.56 displacement 110543 n-Hexane 341.76 17.09 equation and the extended natural 71432 Benzene 55.44 2.77 gas analysis for Antelope FJ-17 HZ 100414 Ethylbenzene 3.64 0.18 The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4-3)." Point 008: Emission Emission Factors - Factors - AIRS Uncontrolled Controlled Point CAS # Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 17,930 896.52 All emission factors 108883 Toluene 39.63 1.98 are based on the 008 1330207 Xylenes 11.21 0.56 displacement 110543 n-Hexane 341.76 17.09 equation and the extended natural 71432 Benzene 55.44 2.77 gas analysis for Antelope FJ-17 HZ 100414 Ethylbenzene 3.64 0.18 The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3)." 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN)associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC, n-Hexane NANSR Synthetic Minor Source of: VOC, n-Hexane 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: AIRS ID: 123/9398 Page 11 of 12 Colorado Department of Public Health and Environment Air Pollution Control Division http://ecfr g poaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/9398 Page 12 of 12 Division Information Engineer. Harrison Slaughter Control Engineer: Christopher Laplante Review Dale: 04/08/2015 Application Date: 02/25/2013 Facility Identifiers Permit No. 13WE1497 County# AIRs Facility# 9398 Point# 004 Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Antelope 21-17 Production Pad(COGCC#404901) NENW Section 17.Township 5N,Range 62W Source Location'. SIC: 1311 Elevation(feet) 4690 Portable Source? No Portable Source Homebase N/A Mailing Address 1: Bonanza Creek Energy Operating Company LLC Address 2: 410 17th Street,Suite 1500 Address City.State Zip: Denver,CO 80202 Name. Peg young Person To Phone. 720-440-6133 Contact Fax: 720-729-2331 Email. pyoungaabonanzacrkcom Section 02-Emissions Inventory Analysis AP-42:Chapter 5.2 The table of inputs below enables you to Equation 1 L=12.46'S-P'M/T calculate the loading loss emissions factor L=loading losses in lb per 1000 gallons loaded "L". If you choose to use a state default S=Saturation Factor emissions factor,you may enter is directly P=true vapor pressure of liquid loaded[psial into cell 650 in units Ib/1,000 gallons which M=molecular weight of vapors[Ib/Ib-mole] will overwrite the formula. T=temperature of bulk liquid loaded[deg.R] 1 degree Fahrenheit=460.67 degree Rankine Criteria Pollutants Variables S 0.6 Submerged loading:dedicated normal service P 4.05 psis M 68 lb/lb-mole T 524 deg.R L 3.93 lb/10"3 gal White values with black background are 1.65E-01 lb/bbl Annual requested Throughput 8 431,500 Gallons per Year Annual requested VOC emissions 33,12 Pounds per Year 16.6 Tons VOC per Year Non-Criteria Reportable Air Pollutants/Hazardous Air Pollutants Mass Ratio Company (pounds Are Company HAP VOC E.F. HAP/pound Emissions Emissions Com.onent E.F.(lb/BBL lb/BBL VOC lb r Reportable? Benzene 0.00229 0.165 0.0139 460 Yes n-hexane 0.0113 0.165 0.0685 2,269 Yes 2,2,4-TMP 4-TMP 0.00115 0.165 0.0070 231 No Toluene 0.00458 0.165 0.0278 920 Yes Ethylbenzne 0.00102 0.165 0.0062 205 No Xylene 0.00363 0.165 0.0220 729 Yes There are two(2)primary methods to estimate HAP emissions. The first,is based on site specific analysis looking at HAP sped ation provided by the operator. If the operator does not provide a HAP analysis,you may do a more generic analysis based on the State default emissions factors for condensate and crude oil tanks. 1.If the operator provides speciation and of HAPs and you approve the HAP and VOC emissions factors provided, you should calculate a Mass Ratio and emissions by entering above the lb/bbl HAP and VOC emissions factors provided by the operator in lieu of the state default factors. 2.If the operator does not provide HAP speciation and emissions on the APEN,one generic approach to use is to generate a mass ratio of(pound HAP/Pound VOC)using the appropriate state default emissions factors for HAP and VOC for the location of the operation. These factors may be found in PS Memo 14-03. Section 03-Regulatory Considerations Is this site considered an exploration and production location(e.g.well pad)? Yes If yes,review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day on an annual average basis? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.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 II.D.1.1 Is this site located in an ozone non-attainment area? Yes If yes,this source is subject to Reasonably Available Control Technology(RACT)requirements under Regulation 3,Part B Section III.D.2.a. This requirement may be met using"submerged fill"and/or vapor balance with emissions routed to an emissions control device. Is this facility classified as a major source of HAPs? No If yes,evaluate if 40 CFR,Part 63,Subpart EEEE"Organic Liquids Distribution"MACT provisions apply Does this facility involve the loading of refined crude/condensate in the form of"gasoline"? No If yes,proceed to evaluate the following: Is this facility classified as a"Terminar as defined per Regulation 7,Section VI.C.2.a? No If yes,the provisions of Regulation 7,Section VI.C.2 may apply Is this facility classified as a"Bulk Plant"as defined per Regulation 7,Section VI.C.3.a? No If yes,the provisions of Regulation 7,Section VI.C.3 may apply Section 04-SCC Coding Emissions Factor Pollutant (lb/1,000 gallons) VOC 3.93 b/1,000 gallons Benzene 0.0545 b/1,000 gallons n-hexane 0.268 b/1,000 gallons 2,2,4-TMP 0.0275 b/1,000 gallons Toluene 0.109 b/1,000 gallons E-Benzene 0.0244 b/1,000 gallons Xylene 0.0865 b/1,000 gallons 40600132:Crude Oil:Submerged Loading(Normal Service) Use if S=0.6 Please select one SCC codes above based on the design and operation of your site, For these codes "Crude Oil"is a generic term that includes both condensate and crude oils. Delete SCC codes not used. Notes: APEN Updates: 1. The MW reported on the APEN was deemed to be low compared to what is expected. The operator was contacted about this and the value was recalculated using an RVP of 7.4. This RVP was obtained using a weighted average of the RVP values provided in the application. The calculation is as follows: Given: RVP Antelope G17,1-17,21-17,22-17=12.2;RVP Antelope Fl-17HZ=6.4;%Production Antelope FJ-17HZ=82.6%;%Production Antelope G17,1-17,21-17,22-17=17.4%. Calculation: Average RVP=)12.2*0.174)+(6.4*0.826)=7.4 The MW and TVP were then interpolated from AP-42 Table 7.1-2 at 64 degrees F. 2. The emission factors for the HAPs were updated so they were in units of Ib/1000gallons. 3. The emission for the HAPs were calculated by multiplying the mass fraction of each component by the annual requested VOC emissions for tank loadout. The mass fraction used for the calculation was obtained from the extended liquid analysis from the Antelope 13-17HZ well. An example calculation is as follows: HAP Emissions(tpy)=((HAP wt%in extended liquid analysis)/(100))*(VOC emissions,spy) Benzene Emissions=(1.3877/100)*(16.6 tpy)=1.13 tpy A similar calculation was performed for the other HAPs.It should be noted that the weight percents used in the calculation were obtained from the extended liquid analysis for the Antelope FJ-17H7 well. The weight percents that were used in the calculation are as follow: b. n-Hexane: 6.8334% c. 2,2,4-TMP: 0.6995% d. Toluene: 2.7727% e. Ethylbenzene: 0.6205% f. Xylenes: 2.2021% Permit Information/Updates: 1. The operator was provided with a draft permit to review. They reviewed the draft permits and expressed that they did not have any comments or requests. Division Information Engineer: Harrison Slaughter Control Engineer: Chris Laplante Review Date: 03/31/2015 Application Date: 02/25/2013 Facility Identifiers Permit No. 13WE1497 Potentially Located within EAC - determine attainment County# 123 Weld Attainment Status AIRs Facility# 9398 PM10 Attainment Point# 006 PM2.5 Attainment Facility Equipment ID Pneumatic Pump P1 SOx Attainment Nonattainme NOx nt Nonattainme VOC nt CO Attainment Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: Antelope 21-17 Production Pad E i NNW Section 17, Township 5N, Range 62W Source Location: SIC: 1311 Elevation (feet) 4690 Address 1: Bonanza Creek Energy Operating Company, LLC Mailing Address Address 2: 410 17th Street, Suite 1500 State Zip: Denver, CO, 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@bonanzacrk.com Section 02: Requested Action X New permit/newly reported emission source Request Mod-Change fuel/equipment Request Mod -Change permit limit Request Mod -Change company name Request Mod -Transfer of ownership Request Mod -Other 'Request to limit HAPs with federally enforceable limits Issuance Number: 1 Add'I Info and notes: Section 03: General Facility Information For existing sources,operation began on: 11/24/2012 For New/recon sources, projected startup date: N/A Normal hours of operation: 24 hrs/day 7 days/wk 52 weeks/yr General description of One (1) GIF natural gas driven pneumatic pumps for equipment purpose: heat trace circulation and water transfer Will this equipment be operated in any nonattainment area?' Yes • Section 04: Pump Information Manufactur Sandpiper Model Number: GIF Serial Pump Number: TBD Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control Flare 95.00% efficiency Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex=O.* MW * Xx 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 Q 600 scf/hr MW 23.3 lb/lb-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy nitrogen 0.56 28 0.0067 nitrogen 0.248 2174.514 1.087 CO2 2.35 44 0.0444 nitrogen 1.637 14339.588 7.170 methane 70.9278 16.04 0.4883 methane 18.011 157774.568 78.887 ethane 13.2341 30.07 0.1708 ethane 6.300 55187.915 27.594 propane 7.798 44.09 0.1476 propane 5.443 47680.355 23.840 isobutane 0.8083 58.12 0.0202 isobutane 0.744 6514.999 3.257 n-butane 2.4705 58.12 0.0616 n-butane 2.273 19912.538 9.956 isopentane 0.4744 72.15 0.0147 isopentane 0.542 4746.759 2.373 n-pentane 0.6223 72.15 0.0193 n-pentane 0.711 6226.619 3.113 cyclopentane 0.0489 72.15 0.0015 n-pentane 0.056 489.284 0.245 n-hexane 0.1503 86.18 0.0056 n-hexane 0.205 1796.311 0.898 cyclohexane 0.0382 84.18 0.0014 cyclohexane 0.051 445.952 0.223 Other hexanes 0.2439 86.18 0.0090 Other hexanes 0.333 2914.972 1.457 heptanes 0.1214 100.21 0.0052 heptanes 0.193 1687.120 0.844 methylcyclohexa 0.0289 98.19 0.0012 methylcyclohe 0.045 393.533 0.197 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 Benzene 0.0269 78.11 0.0009 Benzene 0.033 291.390 0.146 Toluene 0.0163 92.14 0.0006 Toluene 0.024 208.282 0.104 Ethylbenzene 0.0013 106.17 0.0001 Ethylbenzene 0.002 19.141 0.010 Xylenes 0.004 106.17 0.0002 Xylenes 0.007 58.895 0.029 C8+ Heavies 0.0531 116 0.0026 C8+ Heavies 0.098 854.218 0.427 Mass Fraction VOC: 0.2917 Total 47.1 VOC mol % 12.9068 'Total Uncontrollc 47.1 tpy VOC Total Controlled 2.4 tpy VOC Notes Mole %, MW, and mass fractions from Antelope FJ-17 HZ gas analysis collected 02/23/2013. Emissions are based on 8760 hours of operation per year. 1161b/lb-mol was used as the average MW of C8+. Uncontrolle Controlled Scenario A CAS# d (Ib/yr) (Ib/yr) Reportable? n-hexane 110543 1796 90 Yes 224-TMP 540841 2 0 No Benzene 71432 291 15 Yes Toluene 108883 208 10 No E-Benzene 100414 19 1 No Xylenes 1330207 59 3 No Uncontrolled Emission Factors VOC 17930 lb/MMscf natural gas used Benzene 55.440 lb/MMscf natural gas used n-hexane 341.764 lb/MMscf natural gas used Toluene 39.627 lb/MMscf natural gas used E-Benzene 3.642 lb/MMscf natural gas used Xylenes 11.205 lb/MMscf natural gas used 224-TMP 0.301 Ib/MMscf natural gas used Controlled Emission Factors VOC 896.52 lb/MMscf natural gas used Benzene 2.772 lb/MMscf natural gas used n-hexane 17.088 lb/MMscf natural gas used Toluene 1.981 lb/MMscf natural gas used E-Benzene 0.182 lb/MMscf natural gas used Xylenes 0.560 lb/MMscf natural gas used 224-TMP 0.015 lb/MMscf natural gas used Notes: 1. Since the pnuematic pump is controlled by an enclosed combustor,the resulting NOx and CO emissions were included on the APEN and subsequently the permit. The emission factors used to calculate the NOx and CO emissions were obtained from AP-42 Table 13.5-1 and are as follow: a. NOx=0.068 lb/MMBtu b. CO=0.37Ib/MMBtu These emission factors,along with an estimated gas higher heating value(HHV) of 1255 Btu/scf,were used to calculate the NOx and CO emissions. The calculation is as follows: a. Hourly emission rate=(emission factor, lb/MMBtu)*(Heat input, MMBtu/hr) b. Heat Input=(HHV, Btu/scf)*(Gas consumption,scf/hr)*(1MMBtu/1000000Btu) Example Calculation:' NOx emissions=(0.068Ib/MMbtu)*(0.753 MMBtu/hr) =0.0512 lb/hr* 8760hr/year* lton/20001bs= 0.224tpy APEN Updates: 1. Values for maximum vent rate, requested volume and vent gas heating value were added to the APEN since they were initially left blank. 2. The waste gas heat content was corrected to reflect a value of 1255 Btu/scf rather than 1225 Btu/scf(this III/MC a ict a tunn nn the APrNI VVO typto Lin Luc rrLIN). 3. The uncontrolled emission factors were updated to have units of lb/MMscf rather than wt%. Permit Information/Updates: 2. The operator was provided with draft permits to review. They expressed that they did not have any comments on the drafts after their review. status of NOx and VOC Division Information Engineer: Harrison Slaughter Control Engineer: Chris Laplante Review Date: 03/31/2015 Application Date: 02/25/2013 Facility Identifiers Permit No. 13WE1497 Potentially Located within EAC - determine attainment County# 123 Weld Attainment Status AIRs Facility# 9398 PM10 Attainment Point# 007 PM2.5 Attainment Facility Equipment ID Pneumatic Pump P2 SOx Attainment Nonattainme NOx nt Nonattainme VOC nt CO Attainment Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: Antelope 21-17 Production Pad NENW Section 17, Township 5N, Range 62W Source Location: SIC: 1311 Elevation (feet) 4690 Address 1: Bonanza Creek Energy Operating Company, LLC Mailing Address 2: 410 17th Street, Suite 1500 Address r,State Zip: Denver, CO, 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@bonanzacrk.com • Section 02: Requested Action X New permit/newly reported emission source Request Mod-Change fuel/equipment Request Mod -Change permit limit Request Mod -Change company name Request Mod -Transfer of ownership Request Mod-Other 'Request to limit HAPs with federally enforceable limits Issuance Number: 1 Add'I Info and notes: Section 03: General Facility Information For existing sources,operation began on: 11/24/2012 For New/recon sources, projected startup date: N/A Normal hours of operation: 24 hrs/day 7 days/wk 52 weeks/yr General description of One (1) GIF natural gas driven pneumatic pumps for equipment purpose: heat trace circulation and water transfer Will this equipment be operated in any nonattainment area?' Yes Section 04: Pump Information Manufactur Sandpiper Model Number: GIF Serial Pump Number: TBD Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control Flare 95.00% efficiency Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex =Q* MW * Xx/C Ex =emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW= Molecular weight of gas=SG of gas * MW of air Xx= mass fraction of x in gas C= molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm Q 600 scf/hr MW 23.3 lb/lb-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy nitrogen 0.56 28 0.0067 nitrogen 0.248 2174.514 1.087 CO2 2.35 44 0.0444 nitrogen 1.637 14339.588 7.170 methane 70.9278 16.04 0.4883 methane 18.011 157774.568 78.887 ethane 13.2341 30.07 0.1708 ethane 6.300 55187.915 27.594 propane 7.798 44.09 0.1476 propane 5.443 47680.355 23.840 isobutane 0.8083 58.12 0.0202 isobutane _ 0.744 6514.999 3.257 n-butane 2.4705 58.12 0.0616 n-butane 2.273 19912.538 9.956 isopentane 0.4744 72.15 0.0147 isopentane 0.542 4746.759 2.373 n-pentane 0.6223 72.15 0.0193 n-pentane 0.711 6226.619 3.113 cyclopentane 0.0489 72.15 0.0015 n-pentane 0.056 489.284 0.245 n-hexane 0.1503 86.18 0.0056 n-hexane 0.205 1796.311 0.898 cyclohexane 0.0382 84.18 0.0014 cyclohexane 0.051 445.952 0.223 Other hexanes 0.2439 86.18 0.0090 Other hexane≤ 0.333 2914.972 1.457 heptanes 0.1214 100.21 0.0052 heptanes 0.193 1687.120 0.844 methylcyclohexa 0.0289 98.19 0.0012 methylcyclohe 0.045 393.533 0.197 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 Benzene 0.0269 78.11 0.0009 Benzene 0.033 291.390 0.146 Toluene 0.0163 92.14 0.0006 Toluene 0.024 208.282 0.104 Ethylbenzene 0.0013 106.17 0.0001 Ethylbenzene 0.002 19.141 0.010 Xylenes 0.004 106.17 0.0002 Xylenes 0.007 58.895 0.029 C8+ Heavies 0.0531 116 0.0026 C8+ Heavies 0.098 854.218 0.427 Mass Fraction VOC: 0.2917 Total 47.1 VOC mol % 12.9068 'Total Uncontrolle 47.1 tpy VOC Total Controlled 2.4 tpy VOC Notes Mole %, MW, and mass fractions from Antelope FJ-17 HZ gas analysis collected 02/23/2013. Emissions are based on 8760 hours of operation per year. 1161b/lb-mol was used as the average MW of C8+. Uncontrolle Controlled Scenario A cnsu d (Ib/yr) (Ib/yr) Reportable? n-hexane 110543 1796 90 Yes 224-TMP 540841 2 0 No Benzene 71432 291 15 Yes Toluene 108883 208 10 No E-Benzene 100414 19 1 No Xylenes 1330207 59 3 No Uncontrolled Emission Factors VOC 17930 lb/MMscf natural gas used Benzene 55.440 lb/MMscf natural gas used n-hexane 341.764 lb/MMscf natural gas used Toluene 39.627 lb/MMscf natural gas used E-Benzene 3.642 lb/MMscf natural gas used Xylenes 11.205 lb/MMscf natural gas used 224-IMP 0.301 lb/MMscf natural gas used Controlled Emission Factors VOC 896.52 lb/MMscf natural gas used Benzene 2.772 lb/MMscf natural gas used n-hexane 17.088 lb/MMscf natural gas used Toluene 1.981 lb/MMscf natural gas used E-Benzene 0.182 lb/MMscf natural gas used Xylenes 0.560 lb/MMscf natural gas used 224-IMP 0.015 lb/MMscf natural gas used Notes: 1. Since the pnuematic pump is controlled by an enclosed combustor,the resulting NOx and CO emissions were included on the APEN and subsequently the permit. The emission factors used to calculate the NOx and CO emissions were obtained from AP-42-Table 13.5-1 and are as follow: a. NOx=0.0681b/MMBtu b. CO=0.37 lb/MMBtu These emission factors,along with an estimated gas higher heating value(HHV) of 1255 Btu/scf,were used to calculate the NOx and CO emissions. The calculation is as follows: a. Hourly emission rate=(emission factor, lb/MMBtu)*(Heat input, MMBtu/hr) b. Heat Input=(HHV, Btu/scf)*(Gas consumption,scf/hr)*(1MMBtu/1000000Btu) Example Calculation: NOx emissions=(0.068 lb/MMbtu)*(0.753 MMBtu/hr)=0.0512 lb/hr*8760hr/year* lton/2000lbs= 0.224tpy APEN Updates: 1. Values for maximum vent rate, requested volume and vent gas heating value were added to the APEN since they were initially left blank. 2. The waste gas heat content was corrected to reflect a value of 1255 Btu/scf rather than 1225 Btu/scf(this was just a typo on the APEN). 3. The uncontrolled emission factors were updated to have units of lb/MMscf rather than wt%. Permit Information/Updates: 1. The operator was provided with draft permits to review. They expressed that they did not have any comments on the drafts after their review. Division Information Engineer: Harrison Slaughter Control Engineer: Chris Laplante Review Date: 03/31/2015 Application Date: 02/25/2013 Facility Identifiers Permit No. 13WE1497 Potentially Located within EAC- determine attainment County# 123 weld Attainment Status AIRs Facility# 9398 PM10 Attainment Point# 008 PM2.5 Attainment Facility Equipment ID Pneumatic Pump P3 SOx Attainment Nonattainme NOx nt Nonattainme VOC nt CO Attainment Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: Antelope 21-17 Production Pad NENW Section 17, Township 5N, Range 62W Source Location: SIC: 1311 Elevation (feet) 4690 Address 1: Bonanza Creek Energy Operating Company, LLC Mailing Address 2: 410 17th Street, Suite 1500 Address f,State Zip: Denver, CO, 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@bonanzacrk.com Section 02: Requested Action X New permit/newly reported emission source Request Mod-Change fuel/equipment Request Mod-Change permit limit Request Mod -Change company name Request Mod -Transfer of ownership Request Mod-Other 'Request to limit HAPs with federally enforceable limits Issuance Number: 1 Add! Info and notes: Section 03: General Facility Information For existing sources,operation began on: 11/24/2012 For New/recon sources, projected startup date: N/A Normal hours of operation: 24 hrs/day 7 days/wk 52 weeks/yr General description of One (1) GIF natural gas driven pneumatic pumps for equipment purpose: heat trace circulation and water transfer Will this equipment be operated in any nonattainment area?1 Yes Section 04: Pump Information Manufactur Sandpiper Model Number: GIF Serial Pump Number: TBD Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control Flare 95.00% efficiency Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex =Q* MW * Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW= Molecular weight of gas=SG of gas * MW of air Xx= mass fraction of x in gas C=molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm Q 600 scf/hr MW 23.3 Ib/Ib-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy nitrogen 0.56 28 0.0067 nitrogen 0.248 2174.514 1.087 CO2 2.35 44 0.0444 nitrogen 1.637 14339.588 7.170 methane 70.9278 16.04 0.4883 methane 18.011 157774.568 78.887 ethane 13.2341 30.07 0.1708 ethane 6.300 55187.915 27.594 propane 7.798 44.09 0.1476 propane 5.443 47680.355 23.840 isobutane 0.8083 58.12 0.0202 isobutane 0.744 6514.999 3.257 n-butane 2.4705 58.12 0.0616 n-butane 2.273 19912.538 9.956 isopentane 0.4744 72.15 0.0147 isopentane 0.542 4746.759 2.373 n-pentane 0.6223 72.15 0.0193 n-pentane 0.711 6226.619 3.113 cyclopentane 0.0489 72.15 0.0015 n-pentane 0.056 489.284 0.245 n-hexane 0.1503 86.18 0.0056 n-hexane 0.205 1796.311 0.898 cyclohexane 0.0382 84.18 0.0014 cyclohexane 0.051 445.952 0.223 Other hexanes 0.2439 86.18 0.0090 Other hexanes 0.333 2914.972 1.457 heptanes 0.1214 100.21 0.0052 heptanes 0.193 1687.120 0.844 methylcyclohexa 0.0289 98.19 0.0012 methylcyclohe 0.045 393.533 0.197 224-TMP (.0001 114.22 0.0000 224-IMP 0.000 1.584 0.001 Benzene 0.0269 78.11 0.0009 Benzene 0.033 291.390 0.146 Toluene 0.0163 92.14 0.0006 Toluene 0.024 208.282 0.104 Ethylbenzene 0.0013 106.17 0.0001 Ethylbenzene 0.002 19.141 0.010 Xylenes 0.004 106.17 0.0002 Xylenes 0.007 58.895 0.029 C8+ Heavies 0.0531 116 0.0026 C8+ Heavies 0.098 854.218 0.427 Mass Fraction VOC: 0.2917 Total 47.1 VOC mol % 12.9068 (Total Uncontrolle 47.1 tpy VOC Total Controlled 2.4 tpy VOC Notes Mole %, MW, and mass fractions from Antelope FJ-17 HZ gas analysis collected 02/23/2013. Emissions are based on 8760 hours of operation per year. 1161b/lb-mol was used as the average MW of C8+. Uncontrolle Controlled Scenario A CAs# d (Ib/yr) (Ib/yr) Reportable? n-hexane 110543 1796 90 Yes 224-TMP 540841 2 0 No Benzene 71432 291 15 Yes Toluene 108883 208 10 No _ E-Benzene 100414 19 1 No — Xylenes 1330207 59 3 No Uncontrolled Emission Factors VOC 17930 lb/MMscf natural gas used Benzene 55.440 lb/MMscf natural gas used n-hexane 341.764 lb/MMscf natural gas used Toluene 39.627 lb/MMscf natural gas used E-Benzene 3.642 lb/MMscf natural gas used Xylenes 11.205 lb/MMscf natural gas used 224-TMP 0.301 lb/MMscf natural gas used Controlled Emission Factors VOC 896.52 lb/MMscf natural gas used Benzene 2.772 lb/MMscf natural gas used n-hexane 17.088 lb/MMscf natural gas used Toluene 1.981 lb/MMscf natural gas used E-Benzene 0.182 lb/MMscf natural gas used Xylenes 0.560 lb/MMscf natural gas used 224-TMP 0.015 lb/MMscf natural gas used Notes: _._ __. _.... _... _._ ..... 1. Since the pnuematic pump is controlled by an enclosed combustor,the resulting NOx and CO emissions were included on the APEN and subsequently the permit. The emission factors used to calculate the NOx and CO emissions were obtained from AP-42 Table 13.5-1 and are as follow: a. NOx=0.068 lb/MMBtu b. CO=0.37 lb/MMBtu These emission factors, along with an estimated gas higher heating value (HHV) of 1255 Btu/scf,were used to calculate the NOx and CO emissions. The calculation is as follows: a. Hourly emission rate=(emission factor,lb/MMBtu)*(Heat input, MMBtu/hr) b. Heat Input= (HHV, Btu/scf)*(Gas consumption,scf/hr)*(1MMBtu/1000000Btu) Example Calculation: NOx emissions=(0.068 lb/MMbtu)*(0.753 MMBtu/hr) =0.0512Ib/hr*8760hr/year* lton/2000lbs= 0.224tpy APEN Updates: 1. Values for maximum vent rate, requested volume and vent gas heating value were added to the APEN since they were initially left blank. 2. The waste gas heat content was corrected to reflect a value of 1255 Btu/scf rather than 1225 Btu/scf(this was just a typo on the APEN). 3. The uncontrolled emission factors were updated to have units of lb/MMscf rather than wt%. Permit Information/Updates: 1. The operator was provided with draft permits to review. They expressed that they did not have any comments on the drafts after their review. 9 0 N ..... r c o 0 0 0 .° E c r 6 o 5 5 .2 5 5 a O S. Oca M M m e T O 0 O O O 0 cWc�� CO N Ln N N N 0 E.4- 9 a ❑ O O 01 0 0 a - Q ad 1 N a, 0, a, a c. o v co . o a ❑ ❑ ❑ ❑❑ W U0. .-' v y e -0-‘1 '0"-?,C? _ c d x c :a H,0. .. ,'c_ « o 0 0 o o y e `° c 'E o^ e w '2.. ccc 0 o u ° >, v O = c .E Z z 2 2 z 7,3 2 " m vc z c2 z `n con ` p A O. O a „, 7.• \ ❑ ® ®❑ ® 'S Q y C V L L Q W = 9 C1 o c °v ° .E m E € .= - r° ^ N x d 7 N Q, e u v d va a .`. 3 ° Y .. _ _ Wo L h L w 8 vi a LP `N 0. E" N E d ._.. r c .ol N C R 'T O >' 0 6 L 00 U G .0 E = U H Y u o = r Yv r >- Yv o c--) v a. A o on a ? a 71 -' a o r.Q w !o y z `c a E o .0 W v o .y d ¢ W Len SJ 'n/ o, al u OD ❑ ❑ _ Z L y A O w T C an Y ^ O .y N O g c L E `e .^ n0.' ,° O 9 E u v o .. L o Y T "v, d Y .---0 v Od L .e .° a L ` N r o y •o ° d s u u °c' cam a =: r s v ea > w9 E a.. Ua�o o c; m rz ° y y Z ° O m U c p_ a. c .`; € °' a °3 m m 'u ° a S V W 46 ten 6 0 5 p c u oocj o e p Z v �' u W 0 `° ' ^ o v q m L U .o t ` o y .c •,..2 .. 0 m .3 m p� c y C o o s. U Lo o GC d p . E• F, 0 6 0 .° v c U y d O > go a 2 .E E �2 . m — .. 2 ?± c v 'E. o .W _ cage �o WW a a �' m E a Q ° Q a z 0., ." `o' v��v F m '� ° go `^ `o E 6 6 z U v T. _ . UQaA w Qrn a E �' d �j�]7 w o € .. a ''i °E' E i o .o o m W Z O m o. m 'E W .y m C 13 . m ° C �+. p € a j v o el o. `p 2 c d V G e 2 Q v a s y 0 o o L - FC �. .. U a .. .. a' D °_' g r a = - L t°° I u i u w c m a m = a s ^ c a o a - O 0 0 O O = — ee -1 .E . a , N N 9, 3 rJ - u c C C4 a ❑ ❑ CC C ❑ ❑ ,^, a r H oM = "L a c a O • `o V e b - '$ o O C al v w ® D ❑ ❑ Q @1 c �` n a. m o ° o a ao a µI111 % E ,-4 n F r L d N 9 L ` ;fl, N C X y T' W - N C o € ; .. 3 c n 2 'o = cE € O o t 9 r o C2 N 6 L O 0.— V e v - a 'O a Q 23 =tog, d W0 = — ° Y T 9 o O O - td G N o N .M. n c. o m a a. = m e eOW„ •a •Ed 0" > 1E A. .111 a Q T q 440 m r T N o e, ''al OD ❑l ej o ` 6.a .� Q o °� �C 'O ..a 1 .. Tii `L 0 0 3 , m 0. a m i` L. - FG a u se - 'I i Z o r '� `o ii c o a. = c° i.Q L. .a-o 0. 2 L. .2 o 44. a' a E e �I > o .v. e 754 Its N Va r UV a U ^' 4 T -. 0 ya';° .. .o Q o u > m > c y -P. Q U U — L L N d c y ea N V 6 V 00 C = s u W u _u ri 2 ti W N 2 2 h a v a c Q U el E E '3 eo '� -a ° V _a € a m Z V - m�'�. c a -Sc F �y E '- c c F4 Q O Lx. r T _ O o P- U O r 61 3✓ ,� d b. N 9 V .= O W 0. .1 P '� N 9 0 2 ad a (y '' r eaa N T > C 'e '�° le CG S �i r n x, e la' v u°- m o u ,a° ° .°1. Y U 0o a Q 5 y E Y, . Cou ° e . ° 'c E o o n e a �. m a w p �_J Zes et O u E U Y 6— 4.. cat...y r'n 9 0. ^e r' c .-J Ct m U 0 o N F 'CS 71 ° O 8 °) rn ° ° 6 h 0 a . CC � °' c co I- °c ° "cC 9 .. ` o E Q �,° [fit yy 9 3 O O m N Vl S' O O L O y O ra0\ p G 8 1 N C E A O 2.o 7. O > 4 V � N v „' . G Gza ^ ee e a e gin o v a. .. Q -Coal c T 6 E r w j, .° c.? O .4 T IS E O e Z .°.'. o a 2 °�' oQ c.ao0 " v = apgz i° 9 is in a RI ° w m .� >,Z c o ° m .v. 1r '0 o N e' i° .. ..w w y i L E '.°. s, Ld 3 O E a` a c CO a co.�' A L o v o & 0 e O r a a 2 =_ E A E* cp. d et e e O e 9 9 '° C y L j O C 9 F g T W n '�`O 0 M = d U N en V] U G t R m co n o O C V O 73 Las-C co ° e a 1° o tr" a", . O F d ue a Co E ° ca ed a ° e E E ..' „? ,L° d d -o o � et ? e c. a y o - v 8 E :: a - `e W r u O E m y c m a ° a i.e. o 0. .a et . - F v° N W G C co d z Q .ri a C� i O F a',1 L e 9 G O y h y'y C .° cat, u v Y O' e O .� . .. .. y .. d c O 0 p 0 ° V .. .n v. V .D v {b n o ` 04.O v .. .n P. 0 U d d E v v ° G u V ,, o ° .a° O .a a o cc, e ._ a ea• c E N o ' c. d c c „ .a c v` C"J p y sr, o c g., y ',,,c, 'y m.a ti m W v o v W —c, m E I Z Z -° o v I o°, 'y ° TT o y .N Y TS 1 cr a ,° P, J e at. a T ° o Z, W c .' a o Q e c o o y L y z �m o 0 o Q o o y v ° C C a o c c H •A e ), .0 .. .� .•L ^ v a C 5 v y ° a E = o c c y c o ° v 3 A ° E 'c d 4.4 o v ao W 0. Ga 0. U r v W d o € °°' w ° 002 0 0 a v° W 2 C7 ♦ ♦ ♦ ♦ ti a PZZ ♦ ac' rt, h ♦ .? `1 L Y 4 V y� 9 w d e t o `o 0 o v e . 5 's f w o EC 3 3 n O 'y r0 ri o a. 0 m -.`2° ' u v 'E o N ., u n 5 r o .A- m '�' 9 w" X' W m L ryi it, r m 4. 0 U O ° w Q £ f CI� r O o a s e C s oo. ( 5 "C .T ° o`c., v y :7 19 75 t . d T re to ,G� to ' o C T-21. o 7 -.E. m 22 T 4 9 0 9 0 .r. 0 0 i*4 en E E E r o 0 1 `o ,T3 m II a v 0. .� �,� y`:. W E c 6 E '..7i s E v .E d v 9 ai 7y' O ,ti rh a > !- o C Q z.- a a scc c al _ G O 7PP' e ti L p 5 `.) a °2 o " 0e: a chi o r 9 O e 4 > C 40 F s C irc co` '- R E o 3 3 r. H. n C N i �- a d � 'O o O u e o • 0 9 v = °�n A. o ` ee c m " o c ., 0 v- cur•�i N _ N E a 00 °, o v O E m t P.O c, 0 48 0 C" L .. 0 �x yo v L o a C N G ^ 0➢ d G O z v. A O v pOy. v� Er. Y V] ' u •- v G C U c . E 1.1 o L O E E2 V o p Too` `"� O a ❑ eE. AN' O C tin a y t ♦L" m •�' c s ` n m yep Q '� � v c 27 p >. y - pp }� _ V W m ❑ ° o v J^ L 1 b E o o '0 E d `o o o� � o w ❑ °� 9 D 1 9 'g a9 a a o CQ tu ° o _o^ " c o z t" ° ? i F F a = con are R �p C E u SaZ� " U a =n o U ,o a 3 o 0J C "1� Z, N m o, e y T. E •,., oq ti. a .� X o �, E U. S .`o_ a LA. C.o L .. `' E ; r c . Q m E �, U A .y rr in 6' t O e4 0.- d v � g "y ryzj N^ .E O T O O O .E ° 1Q toy ad odzE7 0 L7 Q�yl y '`"'qKX ��pp a yC VJ u t .i = R �O . T N Y N j n V T WP y c y — G R � ' �.c 3 " cc 'C a y E m c •t an 7, O n C O C d y 6 fp k7 N "' .� to o „ to W (] V 'd ❑ w ° ' o r U .. o rw 0 v W o _ m > c v U 'Z.. n >, o r.m w 0 w t4. .c o`A, ❑ ° E o d v z a 0 re w .. o a, c c f7 r _ �" a 3 U m a m :° 'v ° U o. i Z v E u°.a— o .E A IC a a yam' m ° v W Ca W a d c U a V1 i X m U V °'� t 4.) r, A d Q 3 A � y_ � "' a a.. o u c c � c ` i, y c E a,. >2 111 o o c re a c 4 U t G w n. E F o T E A C m u W = v .'N' .. E c N u A e L O L 7 ❑ " o co Z �C 5 0o �—Y o C 9 �' 5.-.) 0 c G c c. .a `C tea `' "' v E U u Y .. E y W a O u 'ou. a h o C 'w. 7 y6.ov T. m o o u ay O Zo O m '= o .`. ra ("� o °�; v '°" u OV `I' C _-E 40 a E A N S O Y V U A e E v ?. 9 a O 0. o s O w 'e C . C h q C �3 `� V `_c`�o ai N0 G r' yy > _ L a r o .E o p v L. m.? � o 6 V U u 0 y t o c`. ya y m G u > co ° c Lt. a. �n o a r o v :.- 'oJ w p v v N v V ., a q J tu o c o c d c c a ° y of ° x U O N m E _ o .°'. c l u Z° o Fe o > fn C Q > Q o L." o z O U m o X x ? a J O 2 q .�°. K •u ® c" W F W c .V CIO o2 o Ilit a. A 0 = q o a O > c E wo off ^tri 0 0- A '^ 4 ❑ a C W CO N - N N N v. "vii 53 ra F P. $ Q d _v 47 0-, 01`, .. .c o d M ^ K0 0 4 C G 0 v s .. o Q d S € o 0 0 a Cl. O G o : ;it, > ° e y E' s ° " 6u eoa ,Nn W i..L s >.Errk € nprc� aocavy �. .. d F _ aS Wo, OasZCa y E e = C. S F `° u v' t. m 9 en 0: _M o c o o a o0. • U p' `n `o a " > b •`"0 9 "'N. Pwemwom o .ci.. m t6 ° w 0 h r v H t m m a �°. 'o t A 3 0 CC E ° 0 0 `o tii 17] 73 40 i s c °tp. o o a a� m E U O. C. �. ems¢ v E U [- .,o, x h s A o V V Q' ° p a •o c: c v • �: .a © �' a' � o °�' E w a m y ° n o � c 0 3 Z dl.. ^ `d c ❑ ❑ $ A s a"i oo r c o o ❑ m q ^ Ca '� 3 £., E Y a, y 0 3 0 '• a 0. a >, c o p w e o o '„ 3 s o 0 al+ i -c °' c fi r a�i E C] 'a`-I ro > v `m ` o c o y ° 0 0 • O v c o o a u, c :: c. ,po ti :-°° 'oc E aai a,'c v c v s i L s E C o G 0 z E.. -• r >, o Z 0 'a ° .� as Ca �' O c o .m a°i 0L m -E o W o `o ° y o m U ny O c .E O cr E .� o 0. E c o 'o °' ..s. 9 s b = 0.=1 v°. U ULh co a, u `uF v 0.0. mBo d o o m V c CO V > m ° Z o y r 9 O. V � Q 6 n vm ° s K.5 7 o V n v p 0.` E G a 0 2 IC 3 as , o - e - m Fes . � .aec2av, dd Q W . v Z (QC. 0 0 E W o E 8 W c b O y L 0 e I- O = = O. N o c '0 F b o p V.. v2 N W C s L' 2 a V a. U v C y N_ y LL .• U U 4 'a P E.m E a d o 0 c 0 0 0 -c 3 m A > Y °' 0 0 Z' o �' m Oa e.r n 3 O o 0 °° 0 m�« Y. E in C ch 5 C 0L 4 ❑ ❑ 0'i a ❑ ❑ c c t Q Y c4 'A ° c •• o o tt ® ❑ ❑ ❑ aa2z° T a `; � w 0 Rc .$ v a c u < N u o na ° o v ° Xfi c 0., a .c 3 .5 z '� O. n a, v E A 0 a) W N ri N ❑ U N qN to ?U 'O M - 0. rl `V0) [88 a r 0 J N _v Z A C1 ":".' e o e r li -0 v 0.Q1 w J y. o o ro W E 3 e w •n N 0 >' H 0 cn $! c aN N 3 W ,may W O U A 'E O m ,.' CO ti n P F m ® O ,7 J En g 0 ie u) E. U W 0U W O-i U O j c m m 0. N v • O T. V Zoo U N E .. N kz. •V] a a o° 2 a �--� o a`.) N F e o' o N v p; ,n N CJ O Q p !O U 0 0 , � 0 a �'1 >a a 0. N - L r. E O 41- N a N c ��.. O @S) CC iG k" N "j N J & O N a' m CO 0 LE; C171 P C F W OA U N O 'o C '�' U u H u W a O 0h0 2 r. a a 3 e E c € a m s r. O E NA 9 Zr d E C o a x - Y 0) a , ° x c � cr ui: iiu .�`= 0.O a n eo c m E E 9 E Pr C U NI V m e A m o z ° c o '� N cc3 In m a �" a a 0 3 > Fo F c v a ° W Y ? a o .-i - pppp�4,,,, U G T u Q y p r W e v d �' `° O Cv 0 o c y m .. y m E a N C co d Z e Q A. A. ` 4 .°. w o y .c 4 o a) v tt y 3 /� y . O L 0 d c. E o (r u r , y N E N U G w 'vi C m c. F C A 0 o U(Dug, 0.C. E O 0.' ti ≥ U A E Q m m .9 P. .0. E C'J E m c. E o 0.. W m t `5 oy 3 i P'i "> Lsc 7 '= I Z Z o 9 U E � 'a a iF kC ._oc) ? E 4 '� .. 0. n •. c 9-' �'�i' Z c` at c a o ¢ e c 0 a Q 3 0 '° v v E o A © p l c o E I ≥ 0 E o ' _ in A '.0. ---- 0 'a 3 a ct w U cc c e ri o z O 0 0 P., ht. z o. m wzo 3E`, z I — L ` ^ C F U 1 ' y.- C� O L5 A 0 w F T o g e2 m o yN - c r can 3 Es_, . - 'C 0 m a L L p pp G W A r a a s Q- - G 3- S� , ¢ L OD eLL u �-1 a ry ` N a .. 'O O m c v V eV c T ° ro C a a m ° v m u 01 `° u L W O F 0 0 0 0 e �r 0 Z a n o y �' Qt o Mm 11 y'� N V V V V O 41 W .-' N C oY .N t .C C. CI 9 a a G D. Q o Z o q m m to _ m u J Z m e ❑ «? ii $ o € c .-1 . 1 O u e z '.-E. 0 y G .iii > O 0. — - e o 3 3 ' r V C ? G Fy .e-i N N O R C N OA R O CO. O o CC " e N el O O 0 c �. , a e 0 V 0 0 0 0 0 Y o a+ To. rn O v m o S m O .52 `o no 0 .o `m o m co h a _ v t h L 0 2'0 e c 0 c 0 ,s„ Ow M E " g ° a c - = o P o }., o o a _ C � 0 2 v c O .c U .o z v c U F, U E ❑ .5 A .. _ ro ,. °0, P. o o ❑ -0 u Q � s c ^ U E '$ ^ e 0 +' N h a o o 'j o a 0 u yp]�'' ? 7 c ... N N .. m '�" a O a Tea m C ❑ V c r E �. > E F u. Q. L.. `'+' E ms' 0 3 ea g c 04 O V] m 0 S ❑ w v n y .c. J? .c. ! c.° o �' ,19 W a mi p��.I a C O ➢ V' ❑ Q p 0 C• o c G G 'O y f Q E. b Z z0 U 6 m - 3 c y a0 E° c X z . G W A c c y Y T _ f" c u ro m �° o a O F o p W c ro �n to re - Y a .g 5 v c r7. •-• F U [- > U 0 '� o T 4 m o o ('n u a 'R M [� a 'o II O ❑ .c n o dQ .qp eh y�? o A CO j ® E € >`, '=; 0 0 4 4 4 P e �' .o c W Z c W i >, E Y.ea ' I o E N. U $ d U ' w c I-I 0 -Z r� U a O 8 ppJ L S'.E N O �' ; ._. U E o L ? c U 'N !' w S o q m o Q c 0 a W U is m Z '� U C e o h in to 0' to 0' 0 Cr, 7 o p r c, O. P O. 0. 0, ° N . p ? c2 ❑ 5` E d z a= m T C T ❑ r O Vl fr 7 J2, Q = .E E ,a n � Ca U q coo ? Y m C.3 �' E ❑ O o E; 2 0 0 0 0 o a °6 L q W ,_ E °Z a U W v c.r, en v > c 0" h E'5 >, 0. oK:iLE] U 0.4 _ U r., c 7 ® O xUi N N o GL O 0 0 .0 4' m 0" i' O FI L P 0 °' +. c v W .f. a .a C 0. o y �' a m o ,4 ` h Q ti v in d u 0 O " 2 e P '° - O c C L c W N c V ► F y E O 0 $ d y ` E W E Ny vJ . 0 C" ti m E' L a L a L L a y T �L o` ¢'7 v o x S E ` o o c, .°. 0 0 0 0 0 c U A '. a Vl U p pp 'y Pr ,/e, § E ^ = A A E e. > = -a o u o .E a .0 a a a a .N a, ° °4j eV Y m u a o s L o U F T O '7 c P. U P" E E E E E E c c A C., x > a `) a U >. 0 0 0 0 0 0 E y = a ea �- a ._.e m c w > 0 E E �, U U U U U U n a 'CI Pm Is h W v c E U o .7 W E _ a cr 0 0. I o v m 1 >. .y m c V E O QI In c C c 7 E F cq 0 `U' c ro •E C e c u 4 — tr c - z c m C > h C Q F C] C W o pout,OU O4 v o T >. .53 0 � RIy'i d pa.' U 0 W a� ❑ ❑ avi Q ® 0.. S F 04 'K C '.0 ❑ m o U s b v p o a 0 a . • - N 'n -e � c y a a d t° a z o . =r n m m = 70 Q tC ❑ p W 0 h. C Y as N N N "Cr Cs 01 2 y vi O e0 3 S a u .o ‘.0 ,C) € € 0 c 0 o 0 0. C 0 0ann 0 © CO 0 0 0 0 a o 0 a, a E .a FW. 0 o a '> m a� • `n ._'..— = °' . .c el .-, x c y P. 5 c d E emu- :IE v °° .ca s 10 C7X W L T ki C 2 = E Z C E e W w o 'OO Vray • $ LIi E uo. E A " € = x S `° u, aW. Q 0 om n �a Z ›. M. I' O o y 0 O v L' 0. O 'J Q E U y0 R Q m p 9 .p ; N el " z ^ d t c n 3 w ° '0 t `m 3 v O s n o 0 0 0 C7 d e s A. o Too. s •- 0 aa 00 A 3 as Q.I. L .fl U F ` .0 N m `o U ^ '7 O C G O O o 0 0 a. CO i...ii chi m p x " v " C " `� W E .:1 R' O 3 0. .. +' FG,. G n m ❑ ❑ _ m ^� o E v '3 " en g 'CJ V 3 0. Q ce rr a °' a n .0 A z v m � — `m ❑ c q '^ 3 .. E .c. Z .¢ o = c ha z. 3 E E n d o o f d e o ° 3 I u .N a"i 3 'R 0 d `m € a a °' .. :to E. c .. ry t = y x x m m c cr. t u E Q m u ,y o = o F 0 0 ��i n V 'goo °' m .u. "-' a q Q y W 9 e a.. UT oo U r :9 a s L V] O C G z �' .f S C v W y .6 L - 0 6 �p A L O C .E 'E 0 " a� 7 ° .. E ct o 4 = o 'o o `-' c8 ,0 y " .00 do t(2s' U u. a = 0 0 .cc a O u v C °' p; A 4 o c U 0 ? o p Ue °> = ao _ z .2 U U p 'h d a o Q 9 n i° .y a c 2 .2t. U A 04 -E, O El N 3 o 3 W .2 a : a 0 E m F a._-_. c o a M d c ` E a n zUd or Cg a Qco Q Q V G '� y Z p O o E Z 0 0 '0 2 Lu : L. O m c - W ," e C pc '5' Gi L L i y a o o d w 0 O ..+ C Ca' U U .. n' 'a E 0 E 'a R If E y e 0 Cl o g - > a�i u en 00 00 � on xe c o ;a o u -c 'E 9 e d L m ❑ .. x . 0 r -0 6 O u e co v € o 0 0 2' °' 0 k o c o .� a c 3 'm Z 0 cc. E > - e .-,v CL v `L' w d m ,..0 0 II 0 d a ill N O ❑ U rl 0 ttl '� n n a ro $ v - C. o� c _ >9 O N 7 N O 0 ? ^, S y 0 C 4 '8N p V Q -01 0 N N �" 0 gp.O O V T a 5-' 0 N 7 \ '.y.l' " co W u A E- " py Co eo .. 'B i '• W o u z 0 `O ni 2` c E t- N ro m N ° 2 in 0 o w 0 O Q 9 W 1 ? U U U 0 Z 2 0 ci 0 V en n /� U ¢ Q �? W �i r' .. N r r vI a O O b a .0 In Z rn N E Eo. O § 78 u z N o z g o a e = z - T v o CO 7 .8 L - e c x o L m E o T a W 50 w m- o .. N Q .7 u O o N x w W CCTi CC 0 U m 0 o o 0 I X = o O N O 'm o ' ' ' U = m o u a m m a, F PN a e 3 o a $ o e Z e = _ _ z 8 Q ^ 2 w o a 3 L W y E c c a >. d A m 6- E u Hi E "' u .r. v 0 o 0 n c n -m E 7 7 x 4, 0C g O 0 U t ern E c °_' r ° c c 7 7 N m r a 0. N a 3 d ° c uc. o m g m a cal y 3 = 2 e .�0 a e e m OEn. n > e o m ._ .. 'n d d E z o C Z a A 0. Pte. © (9" .u. v m _o c E G. a v .. G m o, = N �i. c g= d .. .. d o c -o u E m a a° Qco d „ a m A Y 0 ,D 0 ni E y " Y al `n o O .o. 0 0 U cn 0. E o e V U L E E E ° E a m © =yo .... .22i-o y 6. a .a ° o c E r E > 0. Q. d m m 9 = 9 o a n o o v = 3 .. W ° .a d o- .w e. v o e U 'c-0 eel E , E u c x .? E a -°o .. a a a o y z �' o E ri> > c c E o w -2 s 3 0 .� 3 0 a U W 0 c d y o „z" �. E o A y e O a w t a w n z v 3L ca ❑ ❑ ® ❑ ❑ ❑ ° > ® w . .. . . _ . . . . a. Om _ c 3 Si. ° o o g i r J ; O. u I m ty m E o re a v e s ; ' w O. y en a W W m �s P. P. W i t ,r 0 y m o U o5 ° W�.- Q < Q d . I.i '- 0 oo `o e a .a n in0 O > d N `m tic N o '. o y 0 a ° z 0 ° E e _ _ ^ ^ a ce a+ .� ❑ ` W o o40 o 0 o e e 7-4 G C3 0 9 O F ,y o .�.^ G N V V V V O y N v ^ s w r @ E F �/ Q O Q ..r CC O to 52 _ V i o HZid e r a w 3 Ht .,- i •c H.R. ‘o e o 0 R \ V E O 3 .1. o N p ti _ 0 0 OQG w Q ^ co CC �i cm a �' .� V C) Ci C) G C 'v - 'C� F _ 0. ,�i 0 m °� !gym, q i = V E.a R = p' N N te �° ` i a a a7 E = o c v o Ii = o 0 >'„ o o `° r. � � e z m C C .7 V 1 III . O -0 'o .F y u c 3 `v E E a a S 4 _ p '2 z e a) U n, o c U {rEj '°' '7.'m a L H °i a 0 ° o �u a r a= o C oo = F o o "] 0 > d Q O c o m O 7 I 0 N N O r O Q COG 0 i. v Y v ' ° O o m °' ® a = F I a�i. µ`t .`f ,N e ` ° A t? >, �.c. 7 .`�. ❑ .o '° 'e ° R £ rt e c c E E ,)) as o CI) o x ❑ 9 _ f8 P. E o o " ,. V O V1 C ¢ ° W .o a°c Pi �e 1� h d v t w cri y = o 03 S o a .7 S g. i Q ill E ��-. m io d E Ca " `Z. , U 0, O c o i- L W x Z i y x a y °'07\14 ' ne CO a` `.. o E y U e E o 8 Q 'S L. .E y r., on o 0 a O = o y as c ,a 1' a t�1 ^ t4 ¢ G ,./1 W ° e u II O F > U c E o ern o �+p�',` 'tpp' C C tyin? Z 61 o °o G l„ u. 2 = y _ �.. ° L V` a y 0 V A W 0 W d a o . To U 8 a 3 2 � � ° E 1 o to N = j 0 E o1 Ft `° o " 'a4 r w° Q v 0 0 o a U W ix �j A O D m - 0 c o Z -o 0 R V' ❑ o ¢ = v =°E r. a° v 4 A T V1 r E u. `" ° :CIA E o = > 0 ° Q as ' is 7 v �' c °�64 a O U W o 0 0 o e o z _y ¢ y G u > W U. "v, 0.r, en C > = o y o b T p, ft a cc 0E0 N > ® 0 a w y i d o C F v C o E o 9 o m esi .t t p 2. ct F •. .0 ° ® V m E to 0 2O L0 .m a C. 0 a o� w a ie U g$ E W F •°° w ° a o c o 7 G Q ¢ q�: '1,', C c a E 9 m ' . a'N 'o = W z o _ ° 5 '5 = � Q 6:.C 2 v v ° > 0 ° c o L Qw a. R . 0 u = Q ,::. pUp..,, E > 0 i 3- t >, '" a '� ° Q y - E t Z` � 0 0 0 0 0 0V-.) U o ."C = L E N 0 ti A 3 0 r ° U A o Q m = „2 U -^�� E E E E E E .-,$ q A Y m ° ° &, O - >, = °_ 0 0 0 0 0 0 0 % .1 t.S e" o oo c 2 > 0 E c E .y 4z U U U U U U c ��, U V] h W a 'o U o 0 'a 5 0 W v N C Q a. u.. a I a t wo c 9 Y o a o - O CL .� m S ° = .0 W 00 ° 0 N V ° e E ^ K 3 ` o E z fi ` A p > ri Q F c y o > Z U v o X 2' c 0❑ Q o as n O U C] W i ❑ ❑ y Q ® °' 0.1 H W c y 5, w U] I cc , m VJ v, • r o a o O V� �' O o f c 'o 0 9 a �` d 0' = e� � � � c u a ❑ C W bop moo. _ V7 . r� . c w D Q o m e I:" C-1 c ai c `b rn � a 4 .. 4 a .9 o c a a A d " E �4�i ^(0 n € € o o co 0 y �n 9 0 O O o E. a Q7 .0 E a FW. v �c W 0. > m c "".1`^ 'C 'C 3 0. .. E .. c a ° s " m a a s V t9 ^ > u � vr € m 0e 0 O• >, 0 0 E R ... 0" E a 0 ,.o. .0 C L a o O � c v g go . z s a o c Wc� a a s Z 0 a.. • E E h 1 z = c n m wL. 6 ¢ a m �,.�.. u s o o yn E u C. O c .. co- o E. N., 7 o u u u 0 b V a o = u w m y yr O a 'o ry m .t....01 aPi g t" en y a I'' o o y s c s 'S bo t°. �.. �.. ❑ cC v .E v L• V I `J m a y c v 3 E d u t u m .a c �. �. a y > COO �r il .p O F e N m o U ^ p Op Z " = 2o , e o 0 3 0 .0 Qe L u :61 m `� A o u ❑ . .c a m E 'c7 a o 3 0 wVVjj o a E g a appp c > E 3 `o > o o .'> 8 " 3 m m u. ai v on ❑ ❑ �' uo L O 4. 0 '3 '> m0 0 E 0 o'eC „'. C • 6. `m Sy .a0i 00 l' C y O 00 y l: y L' EE '� y '. 9 3 ,e u i, 3 a .a as -o _ y5 ue 0 E .y s o 0 QC) h u u i c ko. s' .o € u E G 0.1 a ro > G w m 6 e c o ¢ h e o 0 4. Li e a e o m e .-. a P3 .0 a o > �. 9 a.. U m o U " s h E h 00 py G, .=c >- A W �E. - , ^ o E o octal w, "O 0 o .E p❑ c o 0 o O O ❑ _ •5 O 0. co 0 N a o u m O b �.J 0 p 0 O 'O^ L L o >, u E F or!- E .o. ¢ 4 o m Cj c a 8 a , to U `0 T. o m Z 2 U U C .7 I Q a V € C o m � .y a y .. .a 8, =0 L) 0, m w 'm qWc, n.c. ®® �. E 3 W F; ,E a 5 o C N u o 0 H o '.c-. le U b e = o.. 6 rn 6 6 Q W aai v Z Q coo m .E W ,o u oai 1.L°) 6 <4) c ,. O c c o ." m t c 6 V "' 0 y C. t .c r Q >o �. 6 0 0 C y 0 .A o GS U U V .o. E 0 E y O o 0 C o o ca c c 0 " 3 m >O Yom' en V e o m m m a�i w co o o COw 00 x c o i v, 9 C a a' ❑ ❑ C fY, ❑ ❑ o c F' O Y v) E c 8 ... o c a o = 'a .. o m 'n o L ® ❑ El El 9Q e Z T E L\ m 0 0 ea 0 '$ Y a = = e U 3 a0i o O L' N t' T o O N r 3 '2 z A > x a o 0 a E a Y G c a = c c 0 o o en` y0 NI en C "E •p) 1p� Q. .0 O N b N O o ? ^ M O O C FZ a E 3 e o e 0 oo "' O - > s $9 c 'm R m e N u AV w uc c r n To a°y' �c+, Ws W o u Q t P 0 9 G .� 9 e` r n N ® 0 g j v ❑ W VJ O O m O a O 3t h g y L+ V Q -c Q U U S 4 p z o N ;le. a '� .N-. 0 O 41 .�. 0 [~-I o u. Z W N o H tl o 0 O c-., 7 .. O G.. V 0 O N ''Ci' v E U z, c `c .. .. > m � pa h o c CO Ct o O C a0 no a , °� U O z c co 6 .. W CM W aU.� N O 'm C U m _ 9 9 O O = c A.en d a 3 <0, 9 o ev .o. y > g ._ Zr- a. c ,° o °u rc E a `° 2 c S C fY, ^ A• S C o 05 i QO'' 60 y = . 5 Z . F Q'" tr. a '. .o in 0 O Q aFOi ~ E. > > f v W _ a e^ c p W a .r. top J ce C oS o a >, 0 v Fs' E ri m m a s `-h < � z. 0 = ,C. u ,� v t O �° m m e c c E A E. F.e °' a cj e� m U c @) E L ° c al E '�+ 9 0 e° 2 E. ��y/ r^ 0 'O OD L A 0 a .L c C L eel b0 2 6 I�I a R 0 O .-. > O 4. G O. 6 9 W O N '' i E ,..I • a m o .0. W O v d �• N O P O O C .. M O L � .. y rl 0 C Z e it a a ep a O 0 b0 .N -u c ro E. a v 'I 1;. Z m is c '= GO a v ° o o L .00 .� a ET q u `v - u a:4, u 0 9 6 6 c y ; y d 0 v' g v E v o U u 0 a., ,, o o e = V '� aj z Z `° q O 'a~o m 0 .� a o F o v A . o 04 n 0. a 'o '> 0^ >, u o ¢ U n = y c 3 e o S, .Q' E a a .. m co o o 4, W e c o .- o _ o 0 0 u c c c a 3 I - E u �y o E `0' .° [- 0 e 'S a = 3 e 'C 3 C7 ae U W O e0' 4 0 c /ayi E — = E O K " °I'v 0 Lb: aE o a c: w z U 0 w m DE zo 0 3g v`. A ❑ ❑ ® ❑ ❑ ❑ L i C) 0 w a 'fi E 9 .N p i' r. r ❑ G Cfl 0. 0 z F c° m A 1 'a 0 E I. C^e c e a Y . > 0 cam. = °'.m �" a m W ^� n P, C. On Pr Dui w 00 `o -6 mo e, w Q Q Q Q t I- 01 'g ❑' o O g o O ❑ .4 NI U G v o N y ? 9 a n :? . N 70 v G 0, v O('J N O N � W U E c c a C Lu. ee^o C7 [ ... ., a a` o w' c 6. 0.1 0 0 �❑ o 0 o e e 'Z. m m m o 0 U m o o "I": 6°- 0 ^� u — O t:. ^ �' �. r.+ N V V V V O y QI +�+ ry ira E m u 'C a) m J d 7 E-' ❑ �A I c .c5 �o m -o x € E a. UU .I r1 O L � q p Y E mCO co o � a ov h.", e A Y u w I In g 45 o ° o a e e o m o 0 ro e o 3 � F � � � o � ° o o � W •et o k z OD r a V o 0 0 0 o d =7114 a rn o ❑ ro o y�... y d O ea'',%) d00 Q '0 m o kL n tY L \ 7 029 e ❑ Q L a 0 O� C CD • L° 5 „,m n 3 II o J' o o f wi Pr 01 N o c O ° ',Z, `n"' O F C r u 7 J °' o C v a 0 c Z a, o o E 77 ❑ .c Yv .. y a, . u a' c e 0 0 6 .G I;i� J O ‘0Th:o "'1 ` v >' 6 Q O y.c O V H O g �I O 7 NN '• :: Y O yo a 4, 0 SI 41 Y O Y : E ® a° Y u ` d E m U T s. yOJ, v E ,.`o .Y c£c i E `o v E G of0a it O N m ❑ .2 ❑ 9 ,4".. v c uTL 9 v.g O ,..1 o �D ❑ zm v o ff' o - '� ,�" W" Ty 8 9p 5 y'°a' a 'el o v y c Eo3 ❑ d . o � .. .;€. ° a W 9 t Q . G L 2 w p, •a 'at G �, O E 0.., E o 0 y c .0 "r�i ;Z CV = O. W 0. •a° U a e .o �, o L m c c2' x J c a .m d Es T 3. 9 y° o°_2 7 0. Z — m `o° 0 40 c o pa c n I.i e An Mr cal','R' 6 p ^ c V F J U o .E c P 4e `o er o d. 1 .« A i u Y c 0 �7 0 ▪ II y a o n o O 4 P. o w gq G rilmS �- .g m ® e € ,, w o a a 4 4 P .. 'o u • �' r 8 ,� `m - o '3 a" a �(»0 0 \ W ..= a W C C O -Ae4 O O ^Y y '3 rdi A u o o o a .O m 1 q ❑• 0 .5 -.YE N. 5 F N Y Y Y O L J- O E c Y. •L ❑ O aJ .- - O Q 0 w '•'• > `Y V o „ a a a Q 0 a o s CC c o 0 c z -0Y CA .5 E ¢ 16 8 E w t 2 2 P. m 2 ❑ ,T FFSS.. io 773 o U .. c O U W a e e o 0 0 y 0 u o �] �, > 0 o E i, ' c E u. H > ® -To c o e. LA a I 10 � d E °N0 v— c a �,' t, .Y. 0 .C o o04 0 „ `" o > ,�i, o w c E a ,On v d '0 C H a U mB, V V E W •aoi ,0 t" ' a t a y o 'o Q v V) , O O L p � ❑ e Q Y, a: 5 S O Ca N y; E > E u Y y 'a \�\\v T .Nr E '' 0 i •> c a ► ' E O t. `o' `0 `0 0 0 0 v — c J o is py a c 5 a to 1 .1 e=1 73 o °� > v a o o ❑ o E a 2 2 2 2 a' a•@ • ul N Y cl 135 O, O N ` Y 02 T O y lei `• U 0. O O O O O O ❑ d o t..., x v v e v °o o v9 u .Y. E � a U U U U U U o „ U 00 eh' C), y .o U W v ° ^� � K w a v m t. g Y aF 3�e G t in go e ot j v� KO Q F O c o 00 W ? O O ° O E 5 �, v e a o ,@, S Z 0 t,- n o o A o > Z Y o >, X S �° O is .0'2 s C. W F ”5. c u c Vi [ O U q w ❑ �❑ d ® u ii W
Hello