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Home My WebLink About20141753.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD,MSPH c2. to Director and Chief Medical Officer 01 Dedicated to protecting and improving the health and environment of the people of Colorado .�. * 4300 Cherry Creek Dr.S. Laboratory Services Division Denver,Colorado 80246-1530 8100 Lowry Blvd. taus Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Weld County-Clerk to the Board 1150 O St PO Box 758 Greeley, CO 80632 RECEIVED June 4,2014 JUN 0 9 2914 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On June 8, 2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC— State North Platte T-36 Production Facility(COGCC#433300), in the The Greeley Tribune.A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty(30) days from the date the public notice is • published. Please send any comment regarding this public notice to the address below. • Colorado Dept. of Public Health & Environment APCD-SS-Bl 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 ?uktQiL R.CIAJ �� 2014-1753 -I � - Itu - 1� C�- P(��M)PuJLs�,u+,�M�+k.(Pa) V-9- 14 STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD,MSPH .1(a#17 x,v cozo Executive Director and Chief Medical Officer ti i • 4 Dedicated to protecting and improving the health and environment of the people of Colorado ,r.��,��": 4300 Cherry Creek Dr. S. Laboratory Services Division Ie;�s) Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy Operating Company LLC—State North Platte T-36 Production Facility (COGCC#433300)—Weld County Released To: The Greeley Tribune • On: June 4, 2014 Published: June 8, 2014 PUBLIC NOTICE OF A PROPOSED PROJECT OR ACTIVITY WARRANTING PUBLIC COMMENT Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company LLC Facility: State North Platte T-36 Production Facility (COGCC#433300) Exploration and Production Facility SESE, SEC 36, T5N, R63W Weld County The proposed project or activity is as follows: The source proposes to construct a facility that includes 6 condensate storages tanks, 3 produced water storage tanks, truck loadout operation, fugitive equipment leaks, emergency flare, 2 high/low pressure separators, and water transfer pneumatic pump. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. • 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section 1ll.C.l.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application,the Division's analysis, and a draft of Construction Permit 14WE0187 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at www.colorado.gov/cdphe/AirPublicNotices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: David Thompson Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-Bl Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us £ v.. '.' 1 TA STATE OF COLORADO +s3+ of co.„ COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT e`` '�� AIR POLLUTION CONTROL DIVISION * TELEPHONE: (303)692-3150 • ',eta .� •1876. CONSTRUCTION PERMIT PERMIT NO: 14WE0187 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State North Platte T-36 Production Facility (COGCC#433300), located in the SESE, SEC36, T5N, R63W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Condensate Six (6) above ground 500 bbl atmospheric condensate storage Tank 002 tank One (1) above ground 400 bbl and two (2) 60 bbl concrete vaults PW Tanks 003 used to store produced water. Only the 400 bbl tank is controlled by the combustors TL 004 Truck Condensate Loadout FUG 005 Fugitive VOC leak emissions FL-1 006 Separator controlled by a 40' flare stack. Flare has a minimum combustion efficiency of 95%. The flare is not enclosed. Sep-1, 007 Separator controlled by a 40' flare stack. Flare has a minimum Sep-2 combustion efficiency of 95%. The flare is enclosed. P-1 008 One (1) Sandpiper Cl F pneumatic pump used for water transfer Point 008: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION AIRS ID: 123/9BDF Page 1 of 14 olor-A De pa en .f P ,+.li 'Health and Environment f it Pollution Control Division 1. Points 002, +! , + + ', 0+ r +_ +.+ :: Y�i,. T no ' e Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, pi 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. Point 006: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after startup by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 3. Points 002, 003, 004, 005, 007, 008: Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 4. Point 006: Within one hundred and eighty days (180) after startup, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 5. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (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, III.F.4.) 6. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 7. Point 006: The following information shall be provided to the Division within fifteen (15) days after start-up. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) AIRS ID: 123/9BDF Page 2 of 14 olor Depa.' nen f P li Health and Environment it Pollution Control Division 8. The operator stiaikre ain e I o ' n lette ' ued 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 9. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO VOC CO Emission Type Condensate 002 --- 0.2 --- Point Tank PW Tanks 003 --- 0.6 --- Point TL 004 --- 27.5 --- Point FUG 005 --- 12.6 --- Fugitive FL-1 006 1.2 12.9 6.4 Point Sep-1, Sep-2 007 0.7 10.9 3.7 Point P-1 008 0.3 2.8 1.4 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 10. Point 005: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas analysis and liquids analyses, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 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.) AIRS ID: 123/9BDF Page 3 of 14 olor.. Depa en P •Ii "Health and Environment it Pollution Control Division Y.y , s • Facility 0` Equipment ID AIRS Point Control Device Pollutants Controlled Condensate Tank 002 Enclosed Flare VOC, HAPs PW Tanks 003 Enclosed Flare VOC, HAPs (400 bbl tank only) FL-1 006 Open Flare VOC, HAPs Sep-1, Sep-2 007 Enclosed Flare VOC, HAPs P-1 008 Enclosed Flare VOC, HAPs PROCESS LIMITATIONS AND RECORDS 12. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Point Process Parameter Annual Limit Equipment ID Condensate Tank 002 Condensate Throughput 188,340 BBL PW Tanks 003 Produced Water Throughput 78840 BBL TL 004 Oil Loaded 188,340 BBL FL-1 006 Gas Vented from Separator 24 MMSCF Sep-1,Sep-2 007 Gas Vented from Separator 11.9 MMSCF P-1 008 Natural Gas 5.3 MMSCF Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 13. Points 002, 003, 004, 006, 007, 008: The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on all applicable equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 14. Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 4.) 15. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) AIRS ID: 123/9BDF Page 4 of 14 olor. Depa en 'if P ell Health and Environment it Pollution Control Division 16. Point 002: Nod) ne or op ato 41. o es.ai re or o . flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 17. Point 002: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 18. Point 002: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 19. Point 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) 20. 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 18 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. Point 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. 22. Point 005: This source is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. The operator shall comply with all applicable requirements of Section XII. 23. Point 005: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, AIRS ID: 123/9BDF Page 5 of 14 olor #} ,Depa en of P •li Health and Environment A it Pollution Control Division III.D.2.a). Thin n® ea tP, a4•lyfi- C r^ >s - ' :- sat :=• by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection shall be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. Hi. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 24. Points 002, 003, 004, 006, 007, 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 AIRS ID: 123/9BDF Page 6 of 14 olora i Depa en f P lic±lealth and Environment it Pollution Control Division Initial Testing% q eme 25. Point 005: Within one hundred and eighty days (180) after issuance of this permit, the owner or operator shall complete the initial extended gas analysis of gas samples that are representative of volatile organic compound (VOC) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 26. Point 005: Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 27. Point 006: Within one hundred and eighty days (180) after startup, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.1 & 4) 28. Point 008: The owner or operator shall complete an initial extended gas analysis and submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. (Reference: Regulation No. 3, Part B, Section III.E.) Periodic Testing Requirements 29. Point 005: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 1. Point 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. 2. Point 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. 3. Point 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. AIRS ID: 123/9BDF Page 7 of 14 ll olor-1 Depa en o P •Ii" Health and Environment •it Pollution Control Division ADDITIONAL REQI&s E N 30. 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: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOr) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 31. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 32. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 33. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences AIRS ID: 123/9BDF Page 8 of 14 Dolor r Depa 'enem 3f P ilic'1Health and Environment it Pollution Control Division #% and has been ri ' by•th-«• •if s con omits in all ,a=rpects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. 34. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 35. Unless specifically stated otherwise, the general and specific conditions contained in this permit have been determined by the APCD to be necessary to assure compliance with the provisions of Section 25-7-114.5(7)(a), C.R.S. 36. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 37. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 38. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122 (civil penalties), -122.1 (criminal penalties), C.R.S. By: David Thompson Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BDF Page 9 of 14 olor. Depa en • P di Health and Environment °it Pollution Control Division Notes to Permit Holder . " - me o ' .e' an - 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childoagename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&paqename=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# (lb/yr) reportable? (Ib/yr) 002 Benzene 71432 75.3 No 3.8 002 n-Hexane 110543 414.3 Yes 20.7 003 Benzene 71432 551.9 Yes 27.6 003 n-Hexane 110543 1734.5 Yes 86.7 004 Benzene 71432 818 Yes 818 004 n-Hexane 110543 3722 Yes 3722 004 Toluene 108883 1604 Yes 1604 004 Xylenes 1330207 1378 Yes 1378 005 Benzene 71432 135.6 No 135.6 005 n-Hexane 110543 608.9 Yes 608.9 005 Toluene 108883 225.1 No 225.1 • 005 Ethylbenzene 100414 35 No 35 005 Xylenes 1330207 183.6 No 183.6 006 Benzene 71432 925.1 Yes 46.3 006 n-Hexane 110543 5397.3 Yes 269.9 006 Toluene 108883 606.9 Yes 30.3 AIRS ID: 123/9BDF Page 10 of 14 olor Depa en f P li Health and Environment Air Pollution Control Division At 006 Ethl n e JOO4t4ML'1L3J m of 2.7 006 Xylenes 1330207 208.4 No 10.4 007 Benzene 71432 956.6 Yes 47.8 007 n-Hexane 110543 5295.5 Yes 264.8 007 Toluene 108883 674.2 Yes 33.7 007 Ethylbenzene 100414 73.3 No 3.7 007 Xylenes 1330207 156.7 No 7.8 008 Benzene 71432 202.6 No 10.1 008 n-Hexane 110543 1182 Yes 59.1 008 Toluene 108883 132.9 No 6.6 008 Ethylbenzene 100414 11.8 No 0.6 008 Xylenes 1330207 45.6 No 2.3 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput VOC 0.039 0.00195 Source n-Hexane 0.0022 0.00011 Source Benzene 0.0004 0.00002 Source Note: The controlled emissions factors for point 002 are based on the flare control efficiency of 95%. Point 003: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL Produced lb/BBL Source Water Throughput Condensate Throughput VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE Note: The controlled emissions factors for point 003 are based on the flare control efficiency of 95%. Point 004: Emission Factors- Uncontrolled Pollutant lb/BBL loaded I Source AIRS ID: 123/9BDF Page 11 of 14 Iolor- Depa en f P dii "Health and Environment A it Pollution Control Division • n F t. Ea!ibdb2 oiI'at'a + �`•.-x ., Pollutant IbBBL loaded Source VOC 0.292 AP-42 Benzene 0.0043 (tpy)(wt%)/100 n-Hexane 0.0198 (tpy)(wt%)/100 Toluene 0.0085 (tpy)(wt%)/100 Xylenes 0.0073 (tpy)(wt%)/100 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46*S*P*M/T S= 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) = 7.3 psia M (vapor molecular weight) =66.71 Ib/Ib-mol T (temperature of liquid loaded) = 64 °R Point 005: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 1217 571 467 Flanges 51 16 18 Open-ended Lines 37 6 1 Pump Seals 2 0 1 Valves 177 72 50 Other* 86 8 18 VOC Content(wt. fraction) 32.96 99.78 100 Benzene Content(wt. fraction) 0.06 1.49 0.12 Toluene Content(wt. fraction) 0.04 2.92 0.03 Ethylbenzene(wt. fraction) <0.01 0.43 <0.01 Xylenes Content(wt. fraction) 0.01 2.51 <0.01 n-hexane Content(wt. fraction) 0.34 6.77 <0.01 *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors (kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 AIRS ID: 123/9BDF Page 12 of 14 • olor 4-Depa en, f P .IiHealth and Environment it Pollution Control Division Source: EPA-453/ Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 006: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas(%) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 32.96 21503.99 lb/mmscf 1075.20 lb/mmscf Engineering Calculation Benzene 0.0588 38.54 lb/mmscf 1.93 lb/mmscf Engineering Calculation Toluene 0.0386 25.29 lb/mmscf 1.26 lb/mmscf Engineering Calculation Ethylbenzene 0.0034 2.24 lb/mmscf 0.11 lb/mmscf Engineering Calculation Xylenes 0.0133 8.68 lb/mmscf 0.43 lb/mmscf Engineering Calculation n-hexane 0.3431 224.89 lb/mmscf 11.24 lb/mmscf Engineering Calculation Note: the gas heat content of the emergency flare gas is 1,437 Btu/scf Point 007: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (%) NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 46.39 36295.44 lb/mmscf 1814.77 lb/mmscf Engineering Calculation Benzene 0.1024 80.39 lb/mmscf 4.02 lb/mmscf Engineering Calculation Toluene 0.0722 56.65 lb/mmscf 2.83 lb/mmscf Engineering Calculation Ethylbenzene 0.0079 6.16 lb/mmscf 0.31 lb/mmscf Engineering Calculation Xylenes 0.0168 13.17 lb/mmscf 0.66 lb/mmscf Engineering Calculation n-hexane 0.5671 445.00 lb/mmscf 22.25 lb/mmscf Engineering Calculation Note: the gas heat content of the flare gas is 1,697 Btu/scf Point 008: Emission Factors- Emission Factors- Uncontrolled Controlled Pollutant lb/MMscf vented Ib/MMscf vented Source NOx 0.068 lb/MMBtu 0.0681b/MMBtu AP-42 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 All emission factors VOC 21503.06 1075.15 are based on the displacement equation and the n-Hexane 224.89 11.24 State North Platte Y- U-36HC sales Note: the gas heat content of the flare gas is 1,437 Btu/scf AIRS ID: 123/9BDF Page 13 of 14 II olor- Depa en .f P'� li '°Health and Environment it Pollution Control Division 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN)associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC's, HAPs, n-Hexane NANSR Synthetic Minor Source of: VOC's, HAPs, n-Hexane MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfccrpoaccess.eov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado.qov/cdphe/oilgaspermits AIRS ID: 123/9BDF Page 14 of 14 Division Information Engineer: David Thompson Control Engineer: Chris Laplante Review Date: 05/06/2014 Application Date: 11/27/2013 Facility Identifiers Permit No. 14WE0187 AIRS County# 123 Weld Facility# 9BDF Facility Type: exploration and production facility • ❑Located in the 8-hour non-attainment area? O True Minor 0 Synthetic Minor for: t VOC F NOx F CO Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State North Platte T-36 Production Facility (COGCC# Source Location: SESE, SEC36. T5N, R63W 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 !Section 02: Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State North Platte T-36 Production Facility (COGCC#433300), located in the SESE, SEC36, T5N, R63W, Weld County. Colorado. Point Name Type Control 002 Condensate Condensate Tanks Flare Tank 003 PW Tanks Water Tanks Flare 004 TL Loadout Flare 005 FUG Fugitives Flare 006 FL-1 Separator Venting Flare 007 Sep-1, Sep-2 Separator Venting Flare 008 P-1 Pump Flare I 002 Six(6)above ground 500 bbl atmospheric condensate storage tank Emissions Calculations Pollutant E.F. Source VOC 0.039 lb/bbl E&P TANK 0.00195 Benzene 0.0004 lb/bbl E&P TANK 0.00002 n-Hexane 0.0022 lb/bbl E&P TANK 0.00011 Requsted Throughput 188,340 bbl Control 0 No Control 0 Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 3.67263 tpy 0.1836315 tpy Benzene 75.336 lb/yr 3.7668 lb/yr n-Hexane 414.348 lb/yr 20.7174 lb/yr Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II. A and B of this regulation. Section lt.A.5 - Smokeless Hare or Flares for the Combustion Combastien of Waste Gases ses No owner or operator of a smokeless flare or t„er flare for the combustion of s ante gases shall a V „c 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. 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 10,800 gallons (47 1 bbl) NSPS 0000: for storage vessels in the natural gas production,transmission, and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. Regulation 7—Volatile Organic Compounds XII. VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is not subject to the emission control requirements for condensate tanks since it is located in an attainment area.) XVILC STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS_ (Applicant is not currently subject to this since actual uncontrolled emissions are less than 20 tpy of VOC.) 003 One (1)above ground 400 bbl and two(2)60 bbl concrete vaults used to store produced water. Emissions Calculations Pollutant E.F. Source VOC 0.262Ib/bbl CDPHE 0.0131 Benzene 0.007 lb/bbl CDPHE 0.00035 n-Hexane 0.022 lb/bbl CDPHE 0.0011 Requsted Throughput 78840 bbl 17520 Control O No Control ® Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 10.32804 tpy 0.516402 tpy 2.29512 2.811522 Benzene 551.88 lb/yr 27.594 lb/yr 122.64 n-Hexane 1734.48 lb/yr 86.724 lb/yr 385.44 Regulatory Review Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A (July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5 -C iokePeso Hare or Flares tor :he CoronUStipp o. ,N:ste Gases No owner r r opera operatm of a s keiess hiare or other flare for the _, :hisoon of waste gases shall ailow or cause emssio rs into the atmosphere of any a h po lutant which is in excess pi 30',6 opacity fore oehod or periods s aggregating more than six minutes in any sixty consecutive minutes. Regulation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or • commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. 004 Truck Condensate Loadout Calculations AP-42:Chapter 5.2 Equation 1 L= 12.46*S*P*M/T L= loading losses in lb per 1000 gallons loaded 5 =Saturation Factor P=true vapor pressure of liquid loaded [psia] M = molecular weight of vapors [lb/lb-mole] T=temperature of bulk liquid loaded [deg. R] 1 degree Fahrenheit=460.67 degree Rankine Source S 0.6 Submerged loading: ded AP-42 P 7.3 psia Sales Oil Analysis M 66.71 lb/lb-mole AP-42 T 524 deg. R Field Data L 6.95 lb/10^3 gal 2.92E-01 lb/bbl Annual requested Throughput 188340 BBL/yr 7910280 gal/yr Annual requested VOC emissions 54960 lb/yr 27.48 tpy Regulatory Considerations This facility is not condisdered a terminal (in Reg. 7) because average daily throughput will be below 20,000 gallons at 3.956 gallons per day. This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. NCRPs Component Mass Frac. lb/yr Emission Factor Benzene 0.014885 818.07 0.004343601 lb/bbl n-hexane 0.067752 3723.62 0.019770753 lb/bbl Touene 0.029196 1604.60 0.008519703 Ib/bbl Xylenes 0.025081 1378.44 0.007318902 lb/bbl a=, N o oy : reo,, o d `,.° N d d m ,. o• •O •O •O •O •O •O O o w d o oa m, so c os ,nno v .. ^ e m666 .. a n ti .� o O O o a o O O o w 6 J Sm a oa M y ,n - ,�. " 00 wo °co in sa .� 6 ci 6 d o m m 6 d d o o a O O O 0 6 0 6 •6 co D • ° o n v_ 0 0 0 0 0 0 0 O O o m o a .. o .4 o o „ O o 0 0 o d d o o d Odd o n d „q m 'C.' Yi o .+ O O O 0 ° d 6 6 0 6 O O O O O O O 0 g �. _ o n 0 or I a ry oi H o °� n ^o 6664 d aao ,m,., ,a -. eo OOOO oo < o o ry es n C U a lj i v r = °'. - N Sa O !n .. od oo ,'^ ,a o < o OOOOOO .. O o ry d oi pi E o A O n' > O a.. ry n m 6 o n o a o o ~ O O U a C C n o b 4 n o (:,,II w 0 0 O w 6 O m O ,ry m O O o O o O o 6 4 o in ' \ p o O O 0 o m n oca 000000 172 s r o n o O O O O .: o d o O O O O O o n o o 6 0 0 0 0 o 0'v m o — a - = m v o o g r-' O n, 0 0 0 ..-. 0 O .". 0 0 0 0 O 0 0 0 N 0 o '(500. 0. 0. 0 8_, n o0 06 d o 0000coo To 9 m — u ° 5 a vo ,0 g ` $ 'u o— O O O O O O 0 0 0 o a o 0 0 0 0 0 0 0 0 0 0 6 E '^ 6 0 0 0 iII U of v O w o S o 0 o g q o q 8 a. ili v 8= o o m o Lis 0 Lis 0 0 0 o Lb us us us Ls O 0 0 P us A c A In w a _ co C r ,v., m6mn n .. n n .. .. m mdm .+ m n .. ., n n a Tr O x v w Z m ° L x e 0 — x8888888888 E w co 43 W Lit.: Y w mae .$ o m0 LL LL �, ., a ,� rv ., nm .. .� na, .� n ,a �,„ •44 Co_ m w v v n w — `o n w 3 c 0 ,� L" OO O OO v o ; h - 000 E 0 U n O d U 2 no— t yJ C v p T .. T T w _ 0 _ __ __ __ u u. a = m 8a co a ` N a O 8 a _ - 2 - 2 a J J ' •a css a '^ a r r r.a r E 6 0 0 'a, `a o O E a > E a c v i E a a ≥ E r `c 'a > E z ` E r 0 . i- ,2 '� v F ,^; 0 LL o (.1'1? ;' d s 3 c o >' d s 3 2 o;° .7. 53 '- o >' a 53 0 3 H ,3 =a 3 0 0 v - ° ° ilme) m 0 q v 9 3 8 i 0 LL ,`n 3 .w z O F O 8 or z E • 0• 3 s s_. L_ E O O � q p K 006 Separator controlled by a 40'flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: Sales gas routed to a candle stick flare in case of emergency Emissions from this source are: routed to a flare Natural gas venting from Sales gas routed to a candle stick flare in case of emergency. Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q'MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(O) 24 MMscf/yr 2739.7 scf/hr 2.04 MMscf/mo MW 24.800 Ib/lb-mol 0.066 MMscf/o mole% MW Ibx/lbmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.28 44.01 1.003 0.040 CO2 7.3 63542 31.77 N2 0.38 28.013 0.106 0.004 N2 0.8 6741 3.37 methane 63.0611 16.041 10.116 0.408 methane 73.1 640568 320.28 ethane 18.0437 30.063 5.424 0.219 ethane 39.2 343503 171.75 propane 10.9656 44.092 4.8350 0.195 propane 35.0 306171 153.09 isobulane 1.0063 58.118 0.5848 0.024 isobutane 4.2 37035 18.52 n-butane 2.7729 58.118 1.6116 0.065 n-butane 11.6 102051 51.03 isopentane 0.4454 72.114 0.3219 0.013 isopentane 2.3 20385 10.19 n-pentane 0.5252 72.114 0.3795 0.015 n-pentane 2.7 24029 12.01 cyclopentane 0.0377 70.13 0.0264 0.001 cyclopentane 0.2 1674 0.84 n-Hexane 0.0989 86.18 0.0852 0.003 n-Hexane 0.6 5397 2.70 cyclohexane 0.0268 84.16 0.0226 0.001 cyclohexane 0.2 1428 0.71 Other hexanes 0.1746 86.18 0.1505 0.006 Other hexanes 1.1 9528 4.76 heptanes 0.0766 100.21 0.0768 0.003 heptanes 0.6 4861 2.43 methylcyclohexane 0.0219 98.19 0.0215 0.001 methylcyclohexane 0.2 1362 0.68 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 7 0.00 Benzene 0O187 78.12 0.0146 0.001 Benzene 0.1 925 046 Toluene 0.0104 92.15 0.0096 0.000 Toluene 0.1 607 0.30 Ethylbenzene 0.0008 106.17 0.0008 0.000 Ethylbenzene 0.0 54 0.03 Xylenes 0 0031 106.17 0.0033 0.000 Xylenes 0.0 208 0.10 C8+Heavies 0.0376 13033 0.0059 0.000 CB+Heavies 0.0 372 0.19 ' VOC mass fraction'. 0.3286 Total VOC Emissions(Uncontrolled) 258.0 24 800 Notes Mole Ms,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year I calculated the average MW of O8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Candle Stick Flare Model TBD Serial Number TBD Gas Heating Value 1437 Btu/scf Throughput 34488 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 1.17 tpy NOX 6.38 tpy CO Emissions Summary 1.2 tpy NOX Uncontrolled/PTE 6.4 tpy CO 258.0 tpy VOC Controlled 12.9 tpy VOC Uncontrolled Controlled Total Total(Ib/yr) Reportable? (Ib/yr) Benzene 925 Yes • 46 Toluene 607 Yes 30 Ethylbenzene 54 No 3 Xylenes 208 No 10 n-hexane 5397 Yes 270 224-TMP 7 No 0 Regulatory Applicability AQCC Regulation 1 [This source is subject to the opacity requirements for flares in Section II.A.5.'No owner or operator of a AQCC Regulation 2 [Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment ]Public Comment Required required? Emission Factors for Permit Uncontrolled NOX 97.716 b/MMscf CO 531.69 b/MMscf VOC 21503.9948 b/MMscf Benzene 38.5447 b/MMscf Toluene 25.2865 b/MMscf Ethylbenzene 2.2411 b/MMscf Xylenes 8.6841 b/MMscf n-Hexane 224.8866 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 97.716 lb/MMscf CO 531.69 lb/MMscf VOC 1075.1997 lb/MMscf Benzene 1.9272 lb/MMscf Toluene 1.2643 lb/MMscf Ethylbenzene 0.1121 lb/MMscf Xylenes 0.4342 lb/MMscf n-Hexane 11.2443 lb/MMscf 224-TMP 0.0151 lb/MMscf 007 Separator controlled by a 40'flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: gas from low pressure separator Emissions from this source are: routed to a flare Natural gas venting from gas from low pressure separator. Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q'MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(Q) 12 MMscf/yr 13584 scf/hr 1.01 MMscf/mo MW 29.700 Ib/Ib-mol 0.033 MMscf/d mole/ MW Ibx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.91 44.01 1.281 0.043 CO2 4.6 40212 20.11 N2 0.14 28.013 0.039 0.001 N2 0.1 1231 0.62 methane 45.5117 16.041 7.301 0.246 methane 26.2 229225 114.61 ethane 24.3608 30.063 7.324 0.247 ethane 26.2 229949 114.97 propane 17.8141 44.092 7.8546 0.264 propane 28.2 246622 123.31 isobutane 1.672 58.118 0.9717 0.033 isobutane 3.5 30511 15.26 n-butane 4.8334 58.118 2.8091 0.095 n-butane 10.1 88201 44.10 isopentane 0.7784 72.114 0.5613 0.019 isopentane 2.0 17625 8.81 n-pentane 0.9652 72.114 0.6960 0.023 n-pentane 2.5 21855 10.93 cyclopentane 0.0735 70.13 0.0515 0.002 cyclopentane 0.2 1618 0.81 n-Hexane 0.1957 86.18 0.1687 0.006 n-Hexane 0.6 5295 2.65 cyclohexane 0.0531 84.16 0.0447 0.002 cyclohexane 0.2 1403 0.70 Other hexanes 0 3309 86.18 0.2852 0.010 Other hexanes 1.0 8954 4.48 heptanes 0.159 100.21 0.1593 0.005 heptanes 0.6 5003 2.50 methylcyclohexane 00405 98.19 0.0398 0.001 methylcyclohexane 0.1 1249 0.62 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 4 0.00 Benzene 0.039 78.12 0.0305 0.001 Benzene 0.1 957 0.48 Toluene 00233 92.15 0.0215 0.001 Toluene 0.1 674 0.34 Ethylbenzene 0.0022 106.17 0.0023 0.000 Ethylbenzene 0.0 73 0.04 Xylenes 0.0047 106.17 0.0050 0.000 Xylenes 0.0 157 0.08 C8+Heavies 00815 0/060 0.0547 0.002 08+Heavies 0.2 1716 0.86 VOC mass fraction: 0.4632 Total VOC Emissions(Uncontrolled) 216.0 29.700 Notes Mole 3k,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year I calculated the average MW of 08+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0010-000 Serial Number 21242, 21281,21277,21243 Gas Heating Value 1697 Btu/scf Throughput 20194.3 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare Overall Control 95.00% • Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 0.69 tpy NOX 3.74 tpy CO Emissions Summary 0.7 tpy NOX Uncontrolled/PTE 3.7 tpy CO 216.0 tpy VOC Controlled 10.8 tpy VOC Uncontrolled Controlled Total Total(Ib/yr) Reportable? (lb/yr) Benzene 957 Yes 48 Toluene 674 Yes 34 Ethylbenzene 73 No 4 Xylenes 157 No 8 n-hexane 5295 Yes 265 224-TMP 4 No 0 Regulatory Applicability AQCC Regulation 1 [This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a A CC Re ulation 2 Section LA applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled NOX 115.396 b/MMscf CO 627.89 b/MMscf VOC 36295.4398 b/MMscf Benzene 80.3873 b/MMscf Toluene 56.6516 b/MMscf Ethylbenzene 6.1629 b/MMscf Xylenes 13.1662 b/MMscf n-Hexane 444.9980 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 115.396 b/MMscf CO 627.89 b/MMscf VOC 1814.7720 b/MMscf Benzene 4.0194 b/MMscf Toluene 2.8326 b/MMscf Ethylbenzene 0.3081 b/MMscf Xylenes 0.6583 b/MMscf n-Hexane 22.2499 b/MMscf 224-TMP 0.0151 b/MMscf 008 One (1) Sandpiper G1F pneumatic pump used for water transfer Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2091608 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled ®Flare Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex= Q* MW * Xx/C Ex = emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW= Molecular weight of gas =5G of gas * MW of air Xx= mass fraction of x in gas C= molar volume of ideal gas (379 scf/lb-mol) at 601 and 1 atm Q 600 scf/hr MW 24.6 Ib/Ib-mol Hours of Op. 6760 hours/yr Requested Throughput 5.256 MMscf/yr Component Mole% MW mass fraction Component lb/hr lb/yr tpy CO2 2.28 44 0.0405 CO2 1.588 13912.452 6.956 nitrogen 0.38 28 0.0043 nitrogen 0.168 1475.563 0.738 methane 63.0611 16.04 0.4079 methane 16.013 140275.573 70.138 ethane 18.0437 30.07 0.2188 ethane 8.590 75244.571 37.622 propane 10.9656 44.09 0,1949 propane 7.654 67048.435 33.524 isobutane 1.0063 58.12 0.0236 isobutane 0.926 8110.903 4.055 n-butane 2.7729 58.12 0.0650 n-butane 2.551 22349.919 11.175 isopentane 0.4464 72.15 0.0130 isopentane 0.510 4466.596 2.233 n-pentane 0.5262 72.15 0.0153 n-pentane 0.601 5265.060 2.633 cyclopentane 0.0377 72.15 0.0011 n-pentane 0.043 377.219 0.189 n-hexane 0.0989 86.18 0.0034 n-hexane 0.135 1182.004 0.591 cyclohexane 0.0268 84.18 0.0009 cyclohexane 0.036 312.867 0.156 Other hexanes 0.1746 86.18 0.0061 Other hexanes 0.238 2086.733 1.043 heptanes 0.0766 100.21 0.0031 heptanes 0.122 1064.525 0.532 • methylcyclohexa 0.0219 98.19 0.0009 methylcyclohe 0.034 298.214 0.149 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 Benzene 0.0187 78.11 0.0006 Benzene 0.023 202.565 0.101 Toluene 0.0104 92.14 0.0004 Toluene 0.015 132.892 0.066 Ethylbenzene 0.0008 106.17 0.0000 Ethylbenzene 0.001 11.779 0.006 Xylenes 0.0031 106.17 0.0001 Xylenes 0.005 45.644 0.023 C8+Heavies 0.0376 12.1075798 0.0002 C8+ Heavies 0.007 63.134 0.032 Mass Fraction VOC: 0.3286 Total 56.510 Heating Value I loon BTU/scf Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMBtu 0.37 I lb CO/MMBtu Notes Mole%,MW,and mass fractions from: Buffalo Ditch 1-32H facility gas analysis,dated 2/1/2008 Emissions Summary Uncontrolle tpy NOX ncontrolle d/PTE 1.0 tpy CO 56.5 tpy VOC Controlled 2.8 tpy VOC Reportable Controlled • CAB# Total (Ib/yr) ? Total n-hexane 110543 1182.0 Yes 59 224-TMP 540841 1.6 No 0 Benzene 71432 202.6 No 10 Toluene 108883 132.9 No 7 E-Benzene 100414 11.8 No 1 Xylenes 1330207 45.6 No 2 Uncontrolled Emission Factors Controlled Emission Factors VOC 21503.058 lb/MMscf 1075.152898 lb/MMscf Benzene 38.540 lb/MMscf 1.926988127 lb/MMscf n-hexane 224.887 Ib/MMscf 11.24432982 lb/MMscf Toluene 25.284 lb/MMscf 1.264189974 lb/MMscf E-Benzene 2.241 lb/MMscf 0.11205277 lb/MMscf Xylenes 8.684 lb/MMscf 0.434204485 lb/MMscf 224-TMP 0.301 lb/MMscf 0.015068602 lb/MMscf o rn tos c n. 4) Y K < 2 w z o- 0 < c., r t nn < o m Z F 0 K W <,ro I J U m m J 20o 0 U > H o. o Z O w00 < O ix N Z rm�n mU x > < Jto Q o 2 ' 0 orv ,-mm x y H > N N U H 2 a N N N O x -0 0 m O 7 0 O U -n Z • o Z O O c z o o O c Q 2 O u H x a cc ce n o cc Q LL L No O a W J K S.a a O CO o vr- o Q W U O U U O K J 0 0 0 Z co O 0 0 h y Z > U O UO O O r N' O N `n 6 U > JU H >- d x o0 O ct U pp_ Z E U Uw or 4 u C 00.3ci >00 .7z 0 H Z w Pe,0 s o1P y A E C d6V 1 U r a c c v s >> O p w p o c o f Z H U U' y H~ j m N C-0 D N 'O '6 « R CO a G1Ny n a.a n E 413 O 3332 N l/IR 0, wmmrr rr E mmmm I E o O a 3333333rtl << a «« O m I- 01 1 00 <0000 a 0 0 0 0 0 0 0 CO 00 000 OJ CO Nr n,co 6 6 co o c.00 O O r 0 0 0 O 0 o O r fr- O r r 0 6 17 O O O 6 f • 0.-6 O N N 0 0 0 0 Q c N r e]t0 O O 0 0 0 0 f0) O O r 0 0 0 0 0 0 0 N O 017 6 0 0 0 O r 0_ f r r r- O O 4 t7 N N(000 F D-000 (0 0 O N N N M t 0 0 0 O N V 17to NN OOO p n COO m NOJ r(O NOOOO N Ul 1° N°D) m N F Tv nil- 0 4 - 7 r r r N F Fo 0 O O w 4ko ❑ 0 o o O O O 0 O d 2 2 O a o o. O H p- 4 a N N <Of N m N t7 y Oat en N r d h y O r• C 4 CJ N N r N r 01 % 0 10O N N * O r m O m N d x r N N N ' C O co P of to V:^V r- N NC' O N O N to r0 m N d O N 0 -' d X x' - • t. w<. O ,n 0 's d P 0 W < O N N CpN . m O d N'.0 P 0 J d 6Nr00ro M. F- „ F 0 O O O N O O Q Q Nap ty N J . O d N N N 10 t- LO ID CD 0 C CO CO 0. O o3. 0 o O a S z w O Q 0, 0N a co o a 0 u $ -c U a a OO a € a E U S LL r u- c d b E_ I a O q ell 0 0 OIL a o m c Ti o a Oacu =ILz - - dF w m 2Eo o. `m -� - ` c 0`ew o mY » 0 V N O N O 'i • d y v c > B a E ; ) J > off,°v F `-g3 � oE N oNN3 (43S mma' U3 coin a' C o r rrr — NINNNN — lOWOWWWr OW Ommm - www0 0 0°r' 000000 f' in wwwo wwwwwwo 3333333 3333333 sm a a< aaae aaa a a a ae o. do 412 rcr F O• O 2 0 1(0) 01 0 NCO V 01 10 r CO CO 0 r 0 0 0 0 0 0 0 0 - 0 0 0 0 0 0 0 0 -e AIRS (County/Plant) 123/9BDF Permit No. 14WE0187 Date 5/6/2014 Uncontrolled Emission Point# SCC Pollutant or CAS Factor 002 40400311 VOC 0.9286 lb/1000 ga 002 40400311 Benzene 0.0095 lb/1000 ga 002 40400311 n-Hexane 0.0524 lb/1000 ga 003 40400315 VOC 6.2381 lb/1000 ga 003 40400315 Benzene 0.1667 lb/1000 ga 003 40400315 n-Hexane 0.5238 lb/1000 ga 004 40600132 VOC 6.947872 lb/10^3 ga 004 40600132 Benzene 0.0122 lb/1000 ga 004 40600132 n-Hexane 0.1065 lb/1000 ga 004 40600132 Toluene 0.1065 lb/1000 ga 004 40600132 Xylenes 0.1065 lb/1000 ga 005 31000220 VOC --- -- 005 31000220 Benzene --- --- 005 31000220 n-Hexane --- --- 005 31000220 Toluene --- --- 005 31000220 Ethylbenzene --- --- 005 31000220 Xylenes --- --- 006 31000205 VOC 21503.99477 Ib/MMscf 006 31000205 Nox 97.716 lb/MMscf 006 31000205 CO lb/MMscf lb/MMscf 006 31000205 Benzene 38.544697 lb/MMscf 006 31000205 n-Hexane 224.886596 lb/MMscf 6 31000205 Toluene 25.286544 lb/MMscf 6 31000205 Ethylbenzene 2.241055 lb/MMscf 6 31000205 Xylenes 8.68409 lb/MMscf 7 31000205 VOC 36295.4398 lb/MMscf 7 31000205 Nox 115.396 lb/MMscf 7 31000205 CO lb/MMscf lb/MMscf 7 31000205 Benzene 80.387335 lb/MMscf 7 31000205 n-Hexane 444.998047 lb/MMscf 7 31000205 Toluene 56.651583 lb/MMscf 7 31000205 Ethylbenzene 6.162902 lb/MMscf 7 31000205 Xylenes 13.166201 lb/MMscf 8 31000299 VOC 21503.058 lb/MMscf 8 31000299 Nox 0.068 lb NOX/M\ 8 31000299 CO 0.37 lb CO/MMI 8 31000299 Benzene 38.539763 lb/MMscf 8 31000299 Toluene 25.283799 lb/MMscf 8 31000299 EthylBenzene 2.241055 lb/MMscf 8 31000299 Xylenes 8.68409 Ib/MMscf 8 31000299 n-Hexane 224.886596 lb/MMscf Controlled Controlled Actual Requested NCRP = Emissions Emissions Ctrl. reportable Emisison Factor Source (tpy)' (tpy)' PTE (tpy)* Eff% ? E&P TANK 0.2 3.7 95% Yes ' E&P TANK 3.8 75.3 95% No E&P TANK 20.7 414.3 95% Yes CDPHE 0.5 10.3 95% Yes CDPHE 27.6 551.9 95% Yes CDPHE 86.7 1734.5 95% Yes AP-42: Chapter 5.2 27.5 27.5 0% Yes AP-42: Chapter 5.2 96.3 96.3 0% No AP-42: Chapter 5.2 842.4 842.4 0% Yes AP-42: Chapter 5.2 842.4 842.4 0% Yes AP-42: Chapter 5.2 842.4 842.4 0% Yes --- 12.6 12.6 0% Yes --- 135.6 135.6 0% No --- 608.9 608.9 0% Yes --- 225.1 225.1 0% No --- 35 35 0% No --- 183.6 183.6 0% No --- 12.9 258 95% Yes AP-42: Chapter 13.5 1.2 1.2 0% No AP-42: Chapter 13.5 6.4 6.4 0% Yes --- 46.3 925.1 95% Yes _ --- 269.9 5397.3 95% Yes --- 30.3 606.9 0.95 Yes --- 2.7 53.8 0.95 No --- 10.4 208.4 0.95 No --- 10.8 216 0.95 Yes AP-42: Chapter 13.5 0.7 0.7 0 No AP-42: Chapter 13.5 3.7 3.7 0 Yes --- 47.8 956.6 0.95 Yes --- 264.8 5295.5 0.95 Yes --- 33.7 674.2 0.95 Yes --- 3.7 73.3 0.95 No --- 7.8 156.7 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 2.8 56.5 0.95 Yes AP-42: Chapter 13.5 0.2 0.2 0 No AP-42: Chapter 13.5 1 1 0 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 10.1 202.6 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 6.6 132.9 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 0.6 11.8 0.949 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 2.3 45.6 0.95 No Buffalo Ditch 1-321-I facility gas analysis, dated 2/ 59.1 1182 0.95 Yes Air Pollutant Emission Notice (APEN)—and—Application for Construction Permit OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY �.".-\ Current Status(Check all that apply) Reason for APEN Submittal(Check all that apply) V`/- - APEN update only4 / ,.` AIRS ID New or pr vio co 7. ❑❑ P y ® New or previously unreported battery Modification to existing sources ❑ Previously grandfathered battery ❑ Registration for coverage under general permit no.GP01 ❑ Synthetic minor facility &cancellation request for individual permit6: ® Located in the 8-hr Ozone Control Area' ® Application for or Modification of an individual permit ❑ Registered under general permit no.GP01 ❑ Administrative permit amendment° ❑ Permitted under individual permit: 14 W C 01 87 ❑ Other: For individual permit applications,check if you want': ®A copy of the preliminary analysis conducted by the Division ®To review a draft of the permit prior to issuance Company Name': Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address10: 410 17'6 Street,Suite 1500 pyoung®BonanzaCrk.co City: Denver State: CO Zip: 80202 E-mail: m Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name": State North Platte T-36 Production Facility(COGCC#433300) Number of tanks: 6-500 bbl Location'°(QQ Sec.Twp.Range.): SE/SE,Sec 36,T5N,R63W County: Weld Total tank capacity[bbl]: 3,000 Calendar year for which"Actual"data applies': ' 2013 Year(s)tank(s)were placed in service14: 2013 Control Description's: Four(4)Leed L30-0010 SN:21242,21281,21277,21243 Control Efficiency16: 95% Condensate Throughput"[bbllyear] Requested's: 188,340 Maximum for PTE calculation': 188,340 Acmal20: 156,950 While Controls Operational21 156,950 Other equipment at facility22: Heater treaters,produced water tanks,natural gas-fired engines,pneumatic pump,flare Comments: 2-yr APEN update not required Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit ❑ Check if the Division is to calculate emissions. ®Check if site-specific emission factors provided to calculate emissions'. Emission Factor Battery Requested Emissions" Actual Emissions20 Pollutant°° [lb/bbl] PTE25 Uncontrolled26 Controlled' Uncontrolled26 Controlled' VOC[tons/year] 0.039 3.69 3.69 0.18 3.07 0.15 0.02 0.02 0.02 0.02 NOx[tons/year] 0.09 0.09 0.08 0.08 CO[tons/year] Benzene[Ibs/year] 0.0004 81.6 81.6 4.1 68.0 3.4 n-Hexane []bs/year) 0.0022 420.0 420.0 21.0 350.0 17.5 Wells serviced by this tank or tank battery28 API#: 05-123-37577 Name: State North Platte 34-31-36HNB ®Newly Reported Well API#: 05-123-37578 Name: State North Platte Y-U-36HC ®Newly Reported Well API#: Name: ❑Newly Reported Well API#: Name: ❑Newly Reported Well API#; Name ❑Newly Reported Well API#: Name: _.. ❑Newly Reported Well API#: Name: ❑Newly Reported Well The signature below indicates that I have knowledge of the facts herein setforth and that the same are true,accurate,and complete to the best of my knowledge and belief. If this is a regi tion for coverage under general permit GPOI,I further certify that this source is and will be operated in full c iance with eac condition permit GPOI. `,` itth //3 • Signature of Legally A ///z orized Person(not a vendor or consultant) Date David J.Lille Vice President,Rocky Mt.Asset Management Type or Print Name of Person Signing Above Official Title Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-BI (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South 301944 registration to: Denver,CO 80246-1530 FORM APCD-205 Page 1 oft FormAPCD-205-E&PCondensateTanIcAPEN.docx r e u ".- , ' S = z' z ° a NOV27201 , NN 3 e 0 w e °' W e a a. m a - u t E 5- ❑ . 0 3 a ^' 9s a day eo u e Mm ' n " .u. o e D in �. 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