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Home My WebLink About20163568.tiffCOLORADO 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 1150O St PO Box 758 Greeley, CO 80632 November 15, 2016 Dear Sir or Madam: RECEIVED NOV 1 8 2016 WELD COUNTY C ad Ulf 4 H 1 �� --**..yy t � L-- 1 fzsa V-/y�L/1-"i �.r l7 On November 17, 2016, the Air Pollution Control Division will begin a 30 -day public notice period for Bonanza Creek Energy Operating Company, LLC - Seventy Holes CPF B-5. 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 Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe PLAoi iG John W. Hickenlooper, Governor I Larry Wolk, MD, MSPH, Executive Director and Chief Medical Officer CC- PL.Cmm/ TP), HL. C P(3), Rview I/ UM/CK) I l a3/ it t / Q9-/ ICo 2016-3568 Air Pollution Control Division Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - Seventy Holes CPF B-5 - Weld County Notice Period Begins: November 17, 2016 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: Seventy Holes CPF B-5 Well production facility SWNW Section 5 T4N R62W Weld County The proposed project or activity is as follows: The applicant proposes to operate a centralized production facility without any wellheads on location or contiguous with the production equipment. The facility collects EEtP hydrocarbons prior to custody transfer and upstream of a processing plant. The facility includes separators, condensate storage, produced water storage, hydrocarbon loadout, and TEG dehydration 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 III.C.1.a (25 tpy in a non -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 16WE1063 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: Andy Gruel Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us COLORADO 1 I ��.R�, Colorado Air Permitting Project Version No. 1.00 Project Details Review Engineer: Package #: Received Date: Review Start Date: Section 01- Facility Information Company Name: Bonanza Creek Energy Operating Company, LLC County AIRS ID: 123 Plant AIRS ID: 9EE7 Facility Name: Seventy Holes CPF B- Physical Address/Location: SWNWSection 5T4N R62W Type of Facility: i xpiorattan &Produ tionWe F What industry segment? OW l3 rat Production Sr Is this facility located in a NAAQS non -attainment area? If yes, for what pollutant? ❑ Carbon Monoxide (CO) Andy Gruel 353859 9/27/2016 10/27/2016 Section 02 - Emissions Units In Permit Application ❑� Ozone (NOx & VOC) ❑ Particulate Matter (PM) AIRs Point # Emissions Source Type Emissions Control? Permit # Issuance # Self Cert Required? Action Engineering Remarks 001 TE w�Dehydratr .,. CP1 3 `' .. , �\ o s uanc ...' 002 Condensate 5torageTank Yes, 16WE1063 003 Produced-WaterStorag&'Eat; 004 g ; Condensate Storage Tangy" 005 C t lrecarbort Liquid LoaLoading 006 ' ;. Separator Section 03 - Description of Project This is a centralized production facility without any wellheads on location or contiguous with the production equipment. The facility collects E&P hydrocarbons prior to a processing plant, and is considered an E&P site for Reg 7 Section XVII purposes. Section 04 - Public Comment Requirments Is Public Comment Required? If yes, why?' Requesting;Synthe t l j€r�c,Pe Section 05 - Ambient Air Impact Analysis Requirements Was a quantitative modeling analysis required?2 Section 06 - Facility -Wide Stationary Source Classification Is this stationary source a true minor? Is this stationary source a synthetic minor? If yes, explain what programs and which pollutants here: Title V Operating. Permits (OP)-: VOC, HAPs (total, and benzene, toluene, xylenes, and n- hexane) Non -Attainment New Source Review (NANSR): VOC Is this stationary source a major source? If yes, explain what programs and which pollutants here: Construction Permit Application Preliminary Analysis Summary Section 1 — Applicant Information Company Name: Bonanza Creek Energy Operating Company, LLC Permit Number: 16WE1063 Source Location: SWNW Section 5 T4N R62W Equipment Description: TEG dehydration unit (see Section 4 for details) AIRS ID: 123-9EE7-001 Date: 10/31/2016 Review Engineer: Andy Gruel Control Engineer: Stefanie Rucker Section 2 — Action Completed Grandfathered Modification APEN Required/Permit Exempt X CP1 Transfer of Ownership APEN Exempt/Permit Exempt Section 3 — Applicant Completeness Review Was the correct APEN submitted for this source type? X Yes No Is the APEN signed with an original signature? X Yes No Was the APEN filled out completely? X Yes No Did the applicant submit all required paperwork? X Yes No Did the applicant provide ample information to determine emission rates? X Yes No If you answered "no" to any of the above, when did you mail an Information Request letter to the source? On what date was this application complete? 09/27/2016 Section 4 — Source Description AIRS Point Equipment Description 001 One (1) Triethylene glycol (TEG) natural gas dehydration unit (make, model, serial number: TBD) with a design capacity of 12.0 MMscf per day. This emissions unit is equipped with two (2) Kimray, model 21015 gas -glycol pumps with a design capacity of 3.5 gallons per minute. This unit is equipped with a flash tank, reboiler and still vent. Stripping gas is not used. Emissions from the still vent are routed to an air-cooled condenser and then to the facility's bank of enclosed flares. Emissions from the flash tank are recycled. Is this a portable source? Yes X No Is this location in a non -attainment area for any criteria pollutant? X Yes No If "yes", for what pollutant? PKo CO X Ozone Is this location in an attainment maintenance area for any criteria pollutant? Yes X No If "yes", for what pollutant? (Note: These pollutants are subject to minor source RACT per Regulation 3, Part B, Section III.D.2) PM,o CO Ozone Page 1 Is this source located in the 8 -hour ozone non - attainment region? (Note: If "yes" the provisions of X Yes No Regulation 7, Sections XII and XVII.C may apply) Section 5 — Emission Estimate Information AIRS Point Emission Factor Source 001 GRI Gly-Calc v4.0 (Refer to Section 14 for calculations) Did the applicant provide actual process data for the emission inventory? Yes X No Basis for, Potential to Emit (PTE) AIRS Point Process Consumption/Throughput/Production 001 12.0 MMscf per year, 3.5 gallons per minute glycol circulation rate Basis for Actual Emissions Reported During this APEN Filing (Reported to Inventory) AIRS Point Process Consumption/Throughput/Production Data Year 001 No actual emissions reported — not constructed yet N/A Basis for Permitted Emissions (Permit Limits) AIRS Point Process Consumption/Throughput/Production 001 12.0 MMscf per year, 3.5 gallons per minute glycol circulation rate Does this source use a control device? X Yes No AIRS Point Process Control Device Description % Reduction Granted 001 01 Combustor and condenser 95 for combustor; condenser reduction varies by pollutant (see section 13 for overall reduction) Section 6 — Emission Summary (tons per year) Point NO. VOC CO Single HAP Total HAP PTE: 001 0.13 96.23 0.59 18.55 (xylenes) 58.579 Uncontrolled point source emission rate: 001 0.13 96.23 0.59 18.55 (xylenes) 58.579 Controlled point source emission rate: 001 0.13 3.71 0.59 0.7 (toluene) 2.1 Section 7 — Non -Criteria / Hazardous Air Pollutants Pollutant CAS # Uncontrolled Emission Rate (lb/yr) Are the emissions reportable? Controlled Emission Ib/ r Rate ( Y ) Benzene 71432 26040 Yes 1180 Toluene 108883 36140 Yes 1400 Ethylbenzene 100414 14240 Yes 420 Xylenes 1330207 37100 Yes 1020 n -Hexane 110543 3300 Yes 160 2,2,4-Trimethylpentane 540841 338 Yes 20 Note: Regulation 3, Part A, Section II.B.3.b APEN emission reporting requirements for non -criteria air pollutants are based on potential emissions without credit for reductions achieved by control devices used by the operator. Page 2 Section 8 —Testing Requirements Will testing be required to show compliance with any emission rate or regulatory standard? Yes X No If "yes", complete the information listed below AIRS Point Process Pollutant Regulatory Basis Test Method Section 9 — Source Classification Is this a new previously un-permitted source? X Yes No What is this facility classification? True Minor X Synthetic Minor Major Classification relates to what programs? X Title V PSD X NA NSR MACT Is this a modification to an existing permit? Yes X No If "yes" what kind of modification? Minor Synthetic' Minor Major Section 10 — Public Comment Does this permit require public comment per CAQCC Regulation 3? X Yes No If "yes", for which pollutants? Why? VOC For Reg. 3, Part B, III.C.1.a (emissions increase > 25/50 tpy)? X Yes No For Reg. 3, Part B, III.C.1.c.iii (subject to MACT)? Yes X No For Reg. 3, Part B, III.C.1.d (synthetic minor emission limits)? X Yes No Section 11 — Modeling Is modeling required to demonstrate compliance with National Ambient Air Quality Standards (NAAQS)? If "yes", for which pollutants? Why? Yes X No AIRS Point Section 12 — Regulatory Review Regulation 1 - Particulate, Smoke, Carbon Monoxide and Sulfur Dioxide 001 Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15 -second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A (July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5 - Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2 — Odor 001 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. Page 3 Regulation 3 - APENs, Construction Permits, Operating Permits, PSD 001 Part A-APEN Requirements Applicant is required to file an APEN since emissions exceed 1 ton per year VOC in an a nonattainment area for ozone. 001 Part B — Construction Permit Exemptions Applicant is required to obtain a permit since uncontrolled VOC emissions from this facility are greater than the 2.0 TPY threshold (Reg. 3, Part B, Section II.D.3.a) Regulation 6 - New Source Performance Standards 001 None Regulation 7 — Volatile Organic Compounds 001 The facility is considered an area source with respect to HAPs. Is this source subject to the control requirements of MACT HH? (Regulation 8 -Hazardous Air Pollutants review). No Is this source subject to the exemptions under MACT HH (i.e. throughput exemption less than 3 MMSCFD or benzene exemption of less than 1984 Ib/yr)? Yes, after taking credit for federally enforceable controls Even though this source is subject to some requirements of MACT HH, it is not subject to control requirements. Therefore, it can also be subject to Regulation 7 control requirements. 001 Section XII.H: Is this source located in the non -attainment area? Yes This source is subject to Regulation 7, Section XII.H. Uncontrolled actual emissions of volatile organic compounds from the still vent and vent from any gas -condensate -glycol (GCG) separator (flash separator or flash tank), if present, shall be reduced by at least 90 percent through the use of air pollution control equipment. 001 Section XVII.D (State only enforceable). Applicant is required to reduce VOC emissions from this dehydrator by at least 90% since uncontrolled VOC emissions are greater than the 15.0 TPY threshold. Regulation !8 — Hazardous Air Pollutants 001 1. Is facility a production field facility per 63.761 (Refer to Section 14 for definition)? Yes 2. If facility is defined as a production facility, then is it a major source of HAPS when summing up dehydrator and flash tank emissions? No 3. If facility is NOT a production field facility (i.e. natural gas processing plant), then is it a major source of HAPS when summing all HAP emissions from ALL HAP emitting units? N/A — is a production field facility 4. Is this facility considered MAJOR for HAPS? No 5. Is this source subject to MACT HH? Yes 6. WHY? This facility is an area source of HAP and MACT HH area source requirements apply to this TEG dehydrator. However, since benzene emissions from each unit will be less 1984 Ib/yr, this source is only required to calculate and keep records demonstrating that benzene emissions stay below this level. Page 4 Section 13 — Aerometric Information Retrieval System Coding Information Point Process Process Description Throughput limit Emission Factor Pollutant / CAS # Fugitive (Y/N) Emission Factor Source Control (%) 001 01 Glycol Dehydrator 4380 MMscf per year 43.9426 lb/MMscf VOC No GlyCalc 4.0 96.14 5.9458 lb/MMscf Benzene / 71432 No GlyCalc 4.0 95.47 8.2523 lb/MMscf Toluene / 108883 No GlyCalc 4.0 96.13 3.2521 lb/MMscf Ethylbenzene / 100414 No GlyCalc 4.0 97.05 8.4726 lb/MMscf Xylenes / 1330207 No GlyCalc 4.0 97.25 0.7556 lb/MMscf n -Hexane / 110543 No GlyCalc 4.0 95.15 0.0771 lb/MMscf 224-TMP / 540841 No GlyCalc 4.0 95 SCC 31000227: Glycol Dehydrator: reboiler still stack Page 5 Section 14 — Miscellaneous Application Notes AIRS Point 001 Glycol Dehydrator In order to determine emissions, the operator used GRI GIyCALC 4.0. The source assumed the inlet gas temperature of 120°F and pressure of 800 psig. The permitted glycol recirculation rate is 3.5 gallons per minute, which is the same as the pump maximum. The gas stream to be dehydrated is the sales gas stream after separation. The GlyCalc model was based off of a Promax model of the sales gas concentration, which was ultimately based on gas and liquid samples taken from nearby Bonanza Creek facilities. An updated extended gas analysis will be required because this source is a new source and an actual sample was not available for emission calculations. MACT HH includes requirements for both major and area sources of HAPs. The definition of major source for MACT HH (63.761) states: (3) For facilities that are production field facilities, only HAP emissions from glycol dehydration units and storage vessels with the potential for flash emissions shall be aggregated for a major source determination. For facilities that are not production field facilities, HAP emissions from all HAP emission units shall be aggregated for a major source determination. The following definitions from 63.761 are also needed to determine major source applicability: Production field facilities means those facilities located prior to the point of custody transfer Custody transfer means the transfer of hydrocarbon liquids or natural gas: after processing and/or treatment in the producing operations, or from storage vessels or automatic transfer facilities or other such equipment, including product loading racks, to pipelines or any other forms of transportation. For the purposes of this subpart, the point at which such liquids or natural gas enters a natural gas processing plant is a point of custody transfer. Natural gas processing plant (gas plant) means any processing site engaged in the extraction of natural gas liquids from field gas, or the fractionation of mixed NGL to natural gas products, or a combination of both. Based on the definitions above, this source qualifies as a production field facility. The facility has federally enforceable limits and requirements which bring HAP emissions to below major source levels. Does this dehydrator have a reboiler? Yes If Yes, what is the reboiler rated? 0.50 mmbtu/hr Reboiler is APEN-exempt because of a design rate less than 5 MMBtu/hr. Page 6 Condensate Storage Tank(s) Emissions Inventory Section 01- Adminstrative Information Facility AIRs ID: County 9E1 7 Plant Point Section 02 - Equipment Description Details Detailed Emissions Unit Eighteen (18) fixed•roof atmosphericstr Description: Emission Control Device Enclosed flares with minimum control efficiency of 959 Description. Requested Overall VOC & HAP Control Efficiency %: Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Condensate Throughput = Requested Permit Limit Throughput = Potential to Emit (PTE) Condensate Throughput = storage of condea Barrels (bbl) per year Barrels (bbl) per year Barrels (bbl) per year Secondary Emissions - Combustion Device(s) Heat content of waste gas= 2841'. Btu/scf Volume of waste gas emitted per BBL of liquids produced = A.14& scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = Potential to Emit (PTE) heat content of waste gas routed to combustion device = Section 04- Emissions Factors & Methodologies will this storage tank emit flash emissions? Actual Condensate Throughput While Emissions Controls Operating = Barrels (bbl) per year based on tank flowrate 1019.3 scf/hr, and pilot 16.8 sd/hr 0 MM BTU per year 25,796 MMBTU per year 25,796 MMBTU per year Pollutant PM2.5 Condensate Storage Tanks Uncontrolled E.F. (Ibs/bbl Condensate Throughput) Controlled E.F. (Ibs/bbl Condensate Throughput) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (Ibs/bbl Condensate Throughput) 0.0000 0.0000 0.0008 IIIIIIIIIIMEIM0.48;. '!- 0.0240 \ NVIII ALN. Lt I:kM1111`lkiNNX\'" 0.003 0.00013 ►1VN 0.002 0.00012 ' \ •- - - 0.0003 0.00002 \ 0.001 0.00004 \ \ \-1k\ \\ B.O18 0.00089 \N0 • 0.002 0.00010 ` 1.XX: 0.0037 Emissions Factor Source Citation Section 05 - Emissions Inventory Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM1O PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.9 0.9 0.88 0.0 0.0 525.8 525.8 26.29 0.0 0.0 4.0 4.0 4.00 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 2.9E+00 2.9E+00 1.4E-01 0.0E+00 0.0E+00 2.6E+00 2.6E+00 1.3E-01 0.0E+00 0.0E+00 3.3E-01 3.3E-01 1.7E-02 0.0E+00 0.0E+00 8.0E-01 8.0E-01 4.0E-02 0.0E+00 0.0E+00 2.0E+01 2.0E+01 9.8E-01 0.0E+00 0.0E+00 2.2E+00 2.2E+00 1.1E-01 0.0E+00 0.0E+00 Section 06- Regulatory Summar/ Analysis Regulation 3, Parts A, B Source requires a permit Regulation 7, Section XII.C, D, E, F Storage tank is subject to Regulation 7, Section XII, as provided bel Regulation 7, Section XII.G, C Storage Tank is not subject to Regulation 7, Section XII.G Regulation 7, Section XVII.B, C.1, C.3 Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3, a Regulation 7, Section XVII.C.2 Storage tank is subject to Regulation 7, Section XVII.C.2, as provide Regulation 6, Part A, NSPS Subpart Kb Storage Tank is not subject to NSPS Kb Regulation 6, Part A, NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 Regulation 8, Part E, MACT Subpart HH Storage Tank is not subject to MAR HH (See regulatory applicability worksheet for detailed analysis) Controlled PTE Uncontrolled PTE (lb/yr) (lb/yr) 5754 288 5172 259 669 33 1601 80 39120 1956 4388 219 1 of 11 K:\PA\2016\ 16WE1063.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 07 - Initial and Periodic Sampling and Testing Requirements Does the company use the state default emissions factors to estimate emissions? ��r If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? ; _ fi If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use an older site -specific sample. If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company request a control device efficiency greater than 95% for a flare or combustion device? If yes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 -Technical Analysis Notes Applicant modeledflash and vrarldng/breaihing losses using Promaz model, based on an annual model throughput of 5000 bbf/day. The modeled results -.(mass flow) were divided : by this model throughputto arniveatthe emission factors Nsted above, which match the APEN- The model is based on a pressurized liquid analysis from the Whitetail F-4 21-4-9 XRLNB collected 6/9/15. The subject facility has not been: construaedye„ ..-.., this sampleisacceptable for preconstrucbon permitting purposes. The permit will require a site•speoflcsampleto recalculate actual site -specific emLssidn factor Section 09 - Inventory 5CC Coding and Emissions Factors AIRS Point # 002 Process # 01 5CC Code Pollutant PM10 PM2.5 NOx VOC CO Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP Uncontrolled Emissions Factor 0.00 0.00 0.02 11.4 0.09 0.06 0.06 0.01 0.02 0.43 0.05 Control % Units O lb/1,000 gallons condensate throughput O Ib/1,000 gallons condensate throughput O lb/1,000 gallons condensate throughput 95 lb/1,000 gallons condensate throughput O 16/1,000 gallons condensate throughput 95 Ib/1,000 gallons condensate throughput 95 lb/1,000 gallons condensate throughput 95 lb/1,000 gallons condensate throughput 95 lb/1,000 gallons condensate throughput 95 Ib/1,000 gallons condensate throughput 95 Ib/1,000 gallons condensate throughput 2 of 11 K:\PA\2016\16W E1063.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Issuance Date: December 30, 2015 Section 01- Adminstrative Information Facility AIRS ID: 123 PEE? 003 County Plant Point Section 02 - Equipment Description Details Detailed Emissions Unit Three (3)500rbbi produced water storage vessels. Description: Emission Control Device En -dined flares with minimum control efficiency.. 95%. Description: Requested Overall VOC & HAP Control Efficiency %: 95 Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Produced Water Throughput = Requested Permit Limit Throughput = Potential to Emit (PTE) Produced Water Throughput= Secondary Emissions - Combustion Device(s) Heat content of waste gas= Volume of waste gas emitted per BBL of liquids produced = 0.15acf/bbl Actual heat content of waste gas routed to combustion device Request heat content of waste gas routed to combustion device = Barrels (bbl) per year Actual Produced Water Throughput While Emissions Controls Operating = Barrels (bbl) per year Barrels (bbl) per year 2841'. Btu/scf 0 MMBTU per year 583 MMBTU per year Potential to Emit (PTE) heat content of waste gas routed to combustion device = 583 MMBTU per year Section 04- Emissions Factors & Methodologies Will this storage tank emit flash emissions? Pollutant PM2.5 Produced Water Storage Tanks Uncontrolled E.F. (Ibs/bbl Produced Water Throughput) Controlled E.F. (Ibs/bbl Produced Water Throughput) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (Ibs/bbl Produced Water Throughput) 0.0000 Emissions Factor Source Citation 0.0000 0.0000 0.0164 0.00082 Wilis7444.7%7 1•Wi IIMENNIMINWIIIVIIIINVICIIIO1 IIIIIIEMEMME 0.00032 0.000016 \ \ .IV IMIIIIMEEMMI 0.00028 0.000014' ' ►:1 Mil 0.00008 00007 0.000001 0.000003 0.000006 0.0000001 0.0001 Section 05 - Emissions InventOry Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOR VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.02 0.0 0-0 11.5 11.5 0.58 0.0 0.0 0.1 0.1 0.09 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 2.2E-01 2.2E-01 1.1E-02 0.0E+00 0.0E+00 2.0E-01 2.0E-01 9.8E-03 0.0E+00 0.0E+00 1.9E-02 1.9E-02 9.3E-04 0.0E+00 0.0E+00 4.9E-02 4.9E-02 2.4E-03 0.0E+00 0.0E+00 8.8E-02 8.8E-02 a.aE-03 0.0E+00 0.0E+00 1.7E-03 1.7E-03 8.7E-05 0.0E+00 0.0E+00 Section 06- Regulatory Summary Analysis Regulation 3, Parts A, B Source requires a permit Regulation 7, Section XVII.B, 0.1, C.3 Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3, a Regulation 7, Section XVII.C.2 Storage tank is subject to Regulation 7, Section XVII.C.2, as provide Regulation 6, Part A, NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 (See regulatory applicability worksheet for detailed analysis) Uncontrolled PTE (lb/yr) 445 391 37 98 176 3 Controlled PTE (lb/yr) 22 20 2 5 9 0 3 of 11 K:\PA\2016\16 W E1063. CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Issuance Date: December 30, 2015 Section 07 - Initial and Periodic Sampling and Testing Requirements Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid water sample drawn at the facility being permitted and analyzed using flash liberation analysis? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use an older site -specific sample. If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor. See PS Memo 14-03, Questions 5.9 and 5.12 for additional guidance on testing. 4,4 Does the company request a control device efficiency greater than 95% for a flare or combustion device? If yes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08- Technical Analysis Notes Applicant used Promax model to model flash/ working/breathing emissions, based on a model throughput of 3210 bbl/d; The modeled emissions were divided by this model throughput to VOC and NAP emission factors listed above. The original APEN reed 9/27/16appeared to have errors In VOC and HAP emission factors, and Toluene was not reported. IemaikMJerry Dismabes on 10/28/1.6 to inquire; he agreed and sent me a revised APEN and tale sheet on 10/31/16. Section 09 - Inventory SCC Coding and Emissions Factors AIRS Point 6 003 Process A SCC Code 01 4-04-003-15 Fixed Roof Tank, Produced Water, working+breathing+Flashing losses Uncontrolled Emissions Pollutant Factor Control % Units NOx 0.00067 0 lb/1,000 gallons liquid throughput VOC 0.39078 95 lb/1,000 gallons liquid throughput CO 0.00306 0 lb/1,000 gallons liquid throughput Benzene 0.00753 95 lb/1,000 gallons liquid throughput Toluene 0.00662 95 lb/1,000 gallons liquid throughput Ethylbenzene 0.00063 95 lb/1,000 gallons liquid throughput Xylene 0.00166 95 lb/1,000 gallons liquid throughput n -Hexane 0.00298 95 lb/1,000 gallons liquid throughput 224 TMP 0.00006 95 lb/1,000 gallons liquid throughput 4 of 11 K:\PA\2016\16W E1063.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 01- Adminstrative Information Facility AIRs ID: 123 County 8EE7 Plant 004 Point Section 02 - Equipment Description Details Detailed Emissions Unit One (1)500 -bbl !hied -roof atmospheric slop tank for storage of compressor condensate dropout before being hauled"'. Description: away by tanker trucks. Emission Control Device Enclosed flares with minimur Description: Requested Overall VOC & HAP Control Efficiency 96: Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Condensate Throughput = Requested Permit Limit Throughput = Potential to Emit (PTE) Condensate Throughput= +'. Barrels (bbl) per year Actual Condensate Throughput While Emissions Controls Operating = 535 Barrels (bbl) per year 535.; Barrels (bbl) per year Secondary Emissions - Combustion Device(s) Heat content of waste gas= 2762. Btu/scf Volume of waste gas emitted per BBL of liquids produced = 316.322scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = based on 0.33 MMscf/yr tank vent gas 0 MMBTU per year 911 MMBTU per year Potential to Emit (PTE) heat content of waste gas routed to combustion device = 911 MMBTU per year Section 04- Emissions Factors & Methodologies Will this storage tank emit flash emissions? COMBINED Pollutant Condensate Storage Tanks Uncontrolled E.F. (Ibs/bbl Condensate Throughput) Controlled E.F. (Ibs/bbl Condensate Throughput) IIIIIIIIMEMINNVIIINIIIINglilINNIN MIIIIIIIMMINVIIILlill MM. ..,t 87.22 ':' INICIlikW W ',aa IIMIECIMENIVIIIINVVOIXWIA PM2.5 Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (Ibs/bbl Condensate Throughput) Emissions Factor Source Citation 0..12 063 0:272.......... 0.0056 0.0060 0.0016 0.0031 0.0000 0.0000 Section 05 - Emissions Inventory Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.03 0.0 0.0 26.0 26.0 1.30 0.0 0.0 0.1 0.1 0.14 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 3.0E-02 3.0E-02 1.5E-03 0.0E+00 0.0E+00 3.2E-02 3.2E-02 1.6E-03 0.0E+00 • 0.0E+00 8.7E-03 8.7E-03 4.3E-04 0.0E+00 0.0E+00 1.7E-02 1.7E-02 8.4E-04 0.0E+00 0.0E+00 2.5E-01 2.5E-01 1.2E-02 0.0E+00 0.0E+00 7.3E-02 7.3E-02 3.6E-03 0.0E+00 0.0E+00 Section 06 - Regulatory Summary Analysis Regulation 3, Parts A, B Source requires a permit Regulation 7, Section XII.C, D, E, F Storage tank is subject to Regulation 7, Section XII, as provided bet Regulation 7, Section XII.G, C Storage Tank is not subject to Regulation 7, Section XII.G Regulation 7, Section XVII.B, C.1, C.3 Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3, a Regulation 7, Section XVII.C.2 Storage tank is subject to Regulation 7, Section XVII.C.2, as provide Regulation 6, Part A, NSPS Subpart Kb Storage Tank is not subject to NSPS Kb Regulation 6, Part A, NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 Regulation 8, Part E, MAC Subpart HH Storage Tank is not subject to MAR HH (See regulatory applicability worksheet for detailed analysis) Controlled PTE Uncontrolled PTE (Ib/yr) (lb/yr) 60 3 64 3 17 1 33 2 495 25 146 7 Barrels )bbl) per year 5 of 11 K:\PA\2016\16 W E1063.CP1.xism Condensate Storage Tank(s) Emissions Inventory Section 07 - Initial and Periodic Sampling and Testing Requirements Does the company use the state default emissions factors to estimate emissions? If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? _ 4 If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use an older site -specific sample. If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company request a control device efficiency greater than 95% for a flare or combustion device? If yes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 - Technical Analysis Notes Slop tank emissions include emissions associated with storage of theslopliquids (flash/working/breathing), andalso biowcase emissions (motive gas toblawdown compressor liquids.) ` -- - Applicant modeled flash and w/b emissions from the strop tank using:Promax model based on slop tank liquids throughput of 178.5 bbi/yr. The VOC and HAP emission factors were confirmed as follows: VOC: 70.2724- lb/bbl" Benzene: - 0.04481b/bbl - - Toluene: 0.0544-Ib/bbl- - EthyBienzene: 0.0153 lb/bbl Xylenes:. 0.0318 lb/bbl n -Hexane: 0.4044lb/bbI 222-TMP: 0.2032lb/bbF, ionfactors calculated above are.added to the emission factors from the blowcaseemissions, whichare calculated bas ed on the 1.3.Ib/MMscfi Benzene: 46:9 lb/MMsd Toluene: 45.57h/MMscf €thyl ietizene:.-12.0-Ib/MMscf Xylenes:: 21.5 lb/MMscf -n-Hexane:. 365.216/MMscf 222-TMP: :-485lb/MMscf les gas analysis (weight %}: as follows: The calculated PTb emissions (in Ib/yr) based on a biowdown venting of 764 Mscf/yr are calculated below, and then converted to a lb/bbl: format based anthe requested 535 bbl/yrthroughput :o sloptanks: VOC: 14425.3 lb/yr; 26.9632 lb/bbl - - - Benzene 35.8 lb/yr;: 0.066975 lb/bb) Toluene:. 34.8 Ib/yr;. 0.064976 lb/bbl Ethyibenzene: 9.2 lb/yr; 0.01714 lb/bbl Xylenes:. 16.5 l6/yr; 0.039703 tb/bbl - - - - - - n -Hexane: 279.0 Ib/yr,. 0.52152 Ib/bbl:: 222-TMP: 37.1 lb/yr; 0.06926 Ib/6bl::- These lb/bbl amounts are ".added :to theflash/w/b Efs:calculated above, and are enteredmanuallyinto the emission factor table in Section 04 above,_ which match the APEN: Section 09 - Inventory SCC Coding and Emissions Factors - AIRS Point # Process # SCC Code 004 01 Uncontrolled Emissions Pollutant Factor Control % Units NOx 2.76 0 lb/1,000 gallons condensate throughput VOC 2314.8 95 lb/1,000 gallons condensate throughput CO 12.57 0 lb/1,000 gallons condensate throughput Benzene 2.66 95 lb/1,000 gallons condensate throughput Toluene 2.84 95 lb/1,000 gallons condensate throughput Ethylbenzene 0.77 95 lb/1,000 gallons condensate throughput Xylene 1.49 95 lb/1,000 gallons condensate throughput n -Hexane 22.05 95 lb/1,000 gallons condensate throughput 224 TMP 6.49 95 lb/1,000 gallons condensate throughput 6 of 11 K:\PA\2016\16W E1063.CP1.xlsm 123-9EE7-004 Continued 16WE1063 CP1 Emissions from point 004 include slop tank emissions (modeled as a typical storage tank) and venting from blowdown events. The caics below are for the blowdown events, which are added to the slop tank caics on the previous page to arrive at an overall emission factor for VOC and HAPs. Blowcase Emission: Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3) Ex=Q*MW* Xx/C Ex = emissions of pollutant x Q = Volumetric flow rate/volume of gas processed MW = Molecular weight of gas = SG of gas * MW of air Xx = mass fraction of x in gas C = molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm Throughput (Q) MW 0.764 MMscf/yr 87.2 scf/hr 0.06 MMscf/mo 23.6 Ib/Ib-mol 0.000 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 2.7382 44.01 1.205 0.051 CO2 0.3 2429 1.21 N2 0.8527 28.013 0.239 0.010 N2 0.1 482 0.24 methane 70.5053 16.041 11.310 0.479 methane 2.6 22799 11.40 ethane 12.2653 30.063 3.687 0.156 ethane 0.8 7433 3.72 propane 8.1097 44.092 3.5757 0.152 propane 0.8 7208 3.60 isobutane 0.9006 58.118 0.5234 0.022 isobutane 0.1 1055 0.53 n -butane 2.7475 58.118 1.5968 0.068 n -butane 0.4 3219 1.61 isopentane 0.53 72.114 0.3822 0.016 isopentane 0.1 770 0.39 n -pentane 0.682 72.114 0.4918 0.021 n -pentane 0.1 991 0.50 cyclopentane 0.0685 70.13 0.0480 0.002 cyclopenta 0.0 97 0.05 n -Hexane 0.1606 86.18 0.1384 0.006 n -Hexane 0.0 279 0.14 cyclohexane 0.0646 84.16 0.0544 0.002 cyclohexan 0.0 110 0.05 Other hexanes 0.2134 86.18 0.1839 0.008 Other hexa 0.0 371 0.19 heptanes 0.0404 100.21 0.0405 0.002 heptanes 0.0 82 0.04 methylcyclohexani 0.0362 98.19 0.0355 0.002 methylcycl4 0.0 72 0.04 224-TMP 0.0161 114.23 0.0184 0.001 224-TMP 0.0 37 0.02 Benzene 0.0227 78.12 0.0177 0.001 Benzene 0.0 36 0.02 Toluene 0.0187 92.15 0.0172 0.001 Toluene 0.0 35 0.02 Ethylbenzene 0.0043 106.17 0.0046 0.000 Ethylbenze 0.0 9 0.00 Xylenes 0.0077 106.17 0.0082 0.000 Xylenes 0.0 16 0.01 C8+ Heavies 0.0156 142.178 0.0222 0.001 C8+ Heavie 0.0 45 0.02 VOC mass I 0.3033 otal VOC Emissions (Uncontrolled) 7.2 23.600 annual limit assuming 95% control 0.4 Notes Mole %, MW, and mass fractions from sales gas analysis from Whitetail F-4 21-4-9XRLNB collected 6/9/15. Emissions are based on 8760 hours of operation per year. Average MW of C8+ is assumed. The results of these calculations are incorporated into the overall point 004 emission factors on the previous page. 123-9EE7-005 16WE1063 CP1 APEN rec'd 9/27/16 (Condensate loadout to tank trucks. Emissions are controlled by vapor balance and enclosed flares. Emissions Inventory Analysis AP -42: Chapter 5.2 Equation/ L = 12.46'C'S'P'M/T L = loading losses in lb per 1000 gallons loaded C = vapor VOC content S = Saturation Factor Criteria Pollutants 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 = 46067 degree Rankine Variables C S P M T L 0.6372 from sales oil composition 1 Submerged loading: dedicated normal service 2,61 psia 33.45 lb/lb-mole 525 deg. R 1.32 0.05549 b/10"3 gal b/bbl Annual requested Throughput 91,991.760 Gallons per Year Annual requested uncontrolled VOC emissions 121.538 Pounds per Year Annual requested uncontrolled VOC emissions 60.77 Tons VOC per Year Vapor Balance Collection Efficiency 96.7% Enclosed Flare Control Efficiency 95% Combined Control Efficiency Annual r-• uested CONTROLLED VOC emissions 3.7 • Controlled emissions are based on vapor balance system with 98.7% collection efficiency, and the collected vapors controlled at 95% in the enclosed flares. The 98.7% collection efficiency requires all tanker trucks having NSPS-level annual test (3 inches pressure change), per AP -42 Chapter 5.2 page 5.2-6. NOx and CO Emissions Calculations: NOx and CO are based on the AP -42 Ch 13.5 emission factors of 0.068 lb NOx / MMBtu 0.31 lb CO / MMBtu The gas has an estimated heating value of The requested vent gas flowrate is 246.7 scf/hr 2.161 MMscf/yr NOx: CO: 288.618 lb/yr 1315.759 lb/yr Non -Criteria Reportable Air Pollutants/Hazardous Air Pollutants Uncontrolled Are NCRP Weight VOC Emission NCRP Emission Emissions Emissions Com•onent Fraction Factor lb/bbl Factor Ib/bbl • r Re ortable? Benzene 0.003211 Yes 24 Toluene 0.002619 0.05549 - Yes 20 n -hexane 0.046257 0.05549 Yes 351 224-TMP 0.003487 0.05549 Yes 26 1964 Btu/scf 0.144 tpy 0658 tpy 0.000601 Emission Factor WAD loaded) 0.000132 Controlled Emissions 0.05549 0.0002 390 0.0001 318 0.0026 5.622 0.0002 424 NCRPs were estimated by multiplying the weight fraction of the NCRP in the sales oil (taken from Antelope J-21 on 7/30/14) by the VOC loading loss emission factor calculated above. All other NCRP5 are below reporting threshold of 250 lb/yr. 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) of crude oil per day on an annual average basis? 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 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 "Terminal" 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 Pollutant NOx CO VOC Benzene Toluene n -hexane 2,2, 4-Trimethyl pentane Uncontrolled Emissions Factor Control Controlled Emission Factor (lb/1,000 gallons) Efficiency (lb/1000 gal) N/A 0 0.00314 N/A 0 0.01430 1.32 93.77% 0.08238 0.00424 93.77% 0.00026 0.00346 93.77% 0.00022 0.06111 93.77% 0.00381 0.00461 93.77% 0.00029 40600142: Crude Oil: Submerged Loading (balanced Service) Use if S = 1.00 Produced Natural Gas Venting/Flaring Preliminary Analysis 123-9EE7-006 16WE1063 CP1 APEN recd 9/27/16 Colorado Department of Public Health and Environment Air Pollution Control Division Venting and flaring of low pressure gas from heater -treaters and vapor recovery towers, when VRU compressors are down. Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3) Ex=Q*MW*Xx/C Ex = emissions of pollutant x Q = Volumetric flow rate/volume of gas processed MW = Molecular weight of gas = SG of gas * MW of air Xx = mass fraction of x in gas C = molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm Throughput (Q) 14.41 MMscf/yr 1645.0 scf/hr 1.22 MMscf/mo MW 39.4 Ib/Ib-mol 0.039 MMscf/d 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 2.3703 44.01 1.043 0.026 CO2 4.5 39663 19.83 N2 0.1298 28.01 0.036 0.001 N2 0.2 1382 0.69 methane 28.1532 16.041 4.516 0.11464 methane 19.6 171708 85.85 ethane 20.1644 30.063 6.062 0.154 ethane 26.3 230488 115.24 propane 24.5228 44.092 10.8126 0.274 propane 46.9 411112 205.56 isobutane 3.2722 58.118 1.9017 0.048 isobutane 8.3 72307 36.15 n -butane 10.6562 58.118 6.1932 0.15/ n -butane 26.9 235474 117.74 isopentane 2.0468 72.114 1.4760 0.037 isopentane 6.4 56121 28.06 n -pentane 2.6234 72.114 1.8918 0.048 n -pentane 8.2 71931 35.97 cyclopentane 0.4735 70.13 0.3321 0.008 cyclopentane 1.4 12626 6.31 n -Hexane 1.1495 86.17 0.9905 0.025145 n -Hexane 4.3 37661 18.83 cyclohexane 0.3948 84.16 0.3323 0.008 cyclohexane 1.4 12633 6.32 Other hexanes 2.0375 86.18 1.7559 0.045 Other hexanes 7.6 66763 33.38 heptanes 0.661 100.21 0.6624 0.017 heptanes 2.9 25185 12.59 methylcyclohexane 0.2969 98.19 0.2915 0.007 methylcyclohexane 1.3 11084 5.54 224-TMP 0.0914 114.23 0.1044 0.002650 224-TMP 0.5 3970 1.98 Benzene 0.1861 78.12 0.1454 0.003691 Benzene 0.6 5528 2.76 Toluene 0.1416 92.15 0.1305 0.003312 Toluene 0.6 4961 2.48 Ethylbenzene 0.0159 106.17 0.0169 0.000429 Ethylbenzene 0.1 642 0.32 Xylenes 0.0381 106.17 0.0405 0.001027 Xylenes 0.2 1538 0.77 C8+ Heavies 0.5745 114.23 0.6563 0.017 C8+ Heavies 2.8 24952 12.48 VOC mass fraction: 0.7040 Total VOC Emissions (Uncontrolled) 39.392 annual limit assuming 95% control Notes Flowrate is based on Promax model, plus a 20% safety factor. Mole %, from Promax model, using weighted average of LP separator gas (58.82%) and VRT gas (41.18%). Promax model is based on samples from nearby facilities but are not site -specific. Emissions are based on 8760 hours of operation per year. MW for C8+ is assumed by applicant, and I accepted. 527.2 26.4 Produced Natural Gas Venting/Flaring Preliminary Analysis Colorado Department of Public Health and Environment Air Pollution Control Division Flaring Information Equipment Description Enclosed flares combust low-pressure separator and VRT gas during VRU downtime. Manufacturer Model Serial Number Gas Heating Value Throughput Enclosed Flares TBD TBD 2237 32235.6174 Btu/scf MMBtu/yr Combustion emission factor source: AP -42: Chapter 13.5 0.068 lb NOX/MMBtu tpy NOX 0.31 5.00 lb CO/MMBtu tpy CO 1.10 Emissions Summary My Calculation Uncontrolled/PTE 1.1 tpy NOX tpy CO tpy VOC tpy VOC 5.0 527.2 26.4 Controlled Applicant's Calculation 1.3 6.0 539.2 27.0 tpy NOX tpy CO tpy VOC tpy VOC 123-9EE7-006 16WE1063 CP1 APEN rec'd 9/27/16 My calculations (above) were less than the applicant's calculations by about 2%. The applicant's quantities were higher and more conservative, so I accepted the applicant's calculations. (Applicant's Calculated) Uncontrolled Total (Ib/yr) Scenario A Reportable? Controlled Total (lb/yr) Benzene 5654 Yes 283 Toluene 5072 Yes 254 Ethylbenzene 658 Yes 33 Xylenes 1572 Yes 79 n -hexane 38518 Yes 1926 224-TMP 4060 Yes 203 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 smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity.' AQCC Regulation 2 _ Section I.A applies to all emission sources. "No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air." AQCC Regulation 3 Part B: A permit is required for this source because uncontrolled VOC emissions from this facility exceed two tons per year in a nonattainment area for ozone. This source is subject to Section III.D.2 (Minor Source RACT) because it is located in a nonattainment area. RACT for this source has been determined to be the use of a flare to control emissions. Is public comment required? Public Comment Required AQCC Regulation 7 Was the well newly constructed, hydraulically fractured, or recompleted on or after August 1, 2014? yes This separator is subject to Reg 7, Section XVII.G. and control requirements of Reg 7, XVII.B.2 Produced Natural Gas Venting/Flaring Preliminary Analysis SIC CODING: 31000205 Emission Factors for Permit Uncontrolled NOX 182.4 lb/MMscf natura CO 693.5 lb/MMscf natura VOC 74854.8 lb/MMscf natura Benzene 392.5 lb/MMscf natura Toluene 352.1 lb/MMscf natura Ethylbenzene 45.7 lb/MMscf natura Xylenes 109.1 lb/MMscf natura n -Hexane 2673.6 lb/MMscf natura 224-TMP 281.9 lb/MMscf natura Controlled NOX 182.4 lb/MMscf natura CO 693.5 Ib/MMscf natura VOC 3742.7 lb/MMscf natura Benzene 19.63 lb/MMscf natura Toluene 17.61 lb/MMscf natura Ethylbenzene 2.29 lb/MMscf natura Xylenes 5.46 lb/MMscf natura n -Hexane 133.68 lb/MMscf natura 224-TMP 14.10 lb/MMscf natura gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented gas vented Colorado Department of Public Health and Environment Air Pollution Control Division 123-9EE7-006 16WE1063 CP1 APEN rec'd 9/27/16 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION FACILITY EMISSION SUMMARY Company Name County AIRS ID Plant AIRS ID Facility Name Bonanza Creek Energy Operating Company, LLC 123 SEEP Seventy Holes CPF 8-5 History File Edit Date 10/28/2016 Ozone Status Non -Attainment EMISSIONS - Uncontrol ed (tons per year EMISSIONS With Controls (tons per year POINT AIRS ID PERMIT Description PM10 PM2.5 H2S SO2 NO4 VOC Fug VOC CO Total HAPs PM10 PM2.5 H28 SO2 NOx VOC Fug VOC CO Total HAPs REMARKS Previous FACILITY TOTAL 00 00 00 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 00 00 0.0 0.0 0.0 0.0 0.0 New Facility- No Previous Total Previous Penntted Facility total 00 0.0 0.0 0.0 0.0 0.0 0.0 0.0 O0 TO O0 00 0.0 0.0 0.0 0.0 00 00 001 16WE1063 TEG Deny 2.1 962 3.7 586 0.1 3.7 0.6 2.1 new point 002 16WE1063 Condensate storage, 9000 bbl .29 525.8 4.0 28.4 0.9 263 4.0 1.4 new point 003 16WE1063 Produced water storage, 1500bbl 20 11.5 0.1 0.6 0.0 0.6 0.1 0.0 new point 004 16WE1063 Slop tank 500 -bbl 0.0 26.0 0.1 0.4 0.0 1.3 0.1 0.0 new point 005 16WE1063 Loadout to tank trucks 2.1 608 0.7 3.4 0.1 3.8 0.7 0.2 new point; control efficiency relies on ALL bucks passing the annual NSPS test 006 16WE1063 LP Separator and VRT venting 1.3 539.2 6.0 27.8 1.3 27.0 8.0 1.4 new pout APEN-E empt/Insignificants Heated separators 0.1 0.1 1.5 0.1 1.3 0.0 0.1 0.1 1.5 0.1 1.3 0,0 from Oct 2016 revised Form 102 Pneumatic Devices I 5.7 0.2 5.7 0.2 front Oct2016 revised Form 102 Fugitive Equipment Leaks 0.5 0.0 0.5 0.0 from Oct 2016 revised Form 102 Compressor Slowdown Stack 0.7 00 0.7 0.0 from Oct 2016 revised Form 102 FACILITY TOTAL 0.1 0.1 0.0 0.0 4.0 1,266.1 0.5 15.9 119.3 0.1 0.1 0.0 0.0 4.0 69.2 0.5 12.8 5.4 HOC: Syn Minor (NANSR and OP) NO. Minor (NANSR and OP) CO: Minor (PSD and OP) HAPS: Syn Minor B, T, X, n -hex, & Total HH: Syn Minor o affected Area ZZZZ: Syn Minor Permitted Feciffy Total 0.0 0.0 00 0.0 2.5 1,259.6 0.0 14.6 119.1 0.0 0.0 0.0 0.0 2.5 62,7 0.0 11.5 5.2 Excludes untsexempt frompermds/APENS (A) Change in Pemrted Emissions 0.0 0.0 0.0 0.0 2.5 62.7 0.0 11.5 Puboom required based on new syn minor permit Note 1 Total VOC (4) Change p Total Permitted Facility Emissions (point and fugitive VOC emissions (point and fugi9ve) 69.7 Facility is eligible for GP02 because < 90 toy Project emissions less Man 25/50 toy 62.7 Note 2 Page 1 002 Panted 10/31/2016 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION DIVISION FACILITY EMISSION SUMMARY - HAPs Company Name Bonanza Creek Energy Operating Company, LLC County AIRS ID 123 Plant AIRS ID 9EE7 Facility Name Seventy Holes CPF B-5 Emissions - uncontrolled (lbs per year POINT PERMIT Description Formaldehyde Acetaldehyde Acrolein Benzene Toluene Ethylbenzene Xylenes n -Hexane McOH 224 TMP H2S TOTAL (tpy) Previous FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0 0.0 001 16WE1063 TEG Dehy 26040 36140 14240 37100 3300 338 58.6 002 16WE1063 Condensate storage, 9000 bbl 5754 5172 669 1601 39120 4388 28.4 003 16WE1063 Produced water storage, 1500 bbl 445 391 37 98 176 3 0.6 004 16WE1063 Slop tank, 500 -bbl 60 64 17 33 495 146 0.4 005 16WE1063 Loadout to tank trucks 390 318 5622 424 3.4 006 16WE1063 LP Separator and VRT venting 5654 5072 658 1572 38518 4060 27.8 0.0 APEN-Exempt / Insignificants 0.0 Heated separators 2 54 0.0 Pneumatic Devices I 28 28 7 13 221 29 0.2 Fugitive Equipment Leaks 3 5 2 4 19 4 0.0 Compressor Blowdown Stack 3 3 1 2 26 3 0.0 TOTALrftpy) 0.0 0.0 0.0 19.2 23.6 7.8 20.2 43.8 0.0 4.7 0.0 0.0 119.3 'Total Reportable = all HAPs where uncontrolled emissions > de minimus values Red Text: uncontrolled emissions < de minimus Emissions with controls (lbs per year POINT PERMIT Description Formaldehyde Acetaldehyde Acrolein Benzene Toluene Ethylbenzene Xylenes n -Hexane McOH 224 TMP H2S TOTAL (tpy) IPrevious FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0 0.0 001 16WE1063 TEG Dehy 1180 1400 420 1020 160 20 2.1 002 16WE1063 Condensate storage, 9000 bbl 288 259 33 80 1956 219 1.4 003 16WE1063 Produced water storage, 1500 bbl 22 20 2 5 9 1 0.0 004 16WE1063 Slop tank, 500 -bbl 3 3 1 2 25 7 0.0 005 16WE1063 Loadout to tank trucks 24 20 351 26 0.2 006 16WE1063 LP Separator and VRT venting 283 254 33 79 1926 203 1.4 0.0 APEN-Exempt / Insignificants 0.0 Heated separators 2 54 0.0 Pneumatic Devices I 28 28 7 13 221 29 0.2 Fugitive Equipment Leaks 3 5 2 4 19 4 0.0 Compressor Blowdown Stack 3 3 1 2 26 3 0.0 TOTALltpy) 0.0 0.0 0.0 0.9 1.0 0.2 0.6 2.4 0.0 0.3 0.0 0.0 5.4 2 1239EE7.xlsx 10/31/2016 Permit number: Date issued: Issued to: DO trol Division Department of Public Health & Environment CONSTRUCTION PERMIT 16WE1063 Facility Name: Plant AIRS ID: Physical Location: County: General Description: Issuance: 1 Bonanza Creek Energy Operating Company, LLC Seventy Holes CPF B-5 123/9EE7 SWNW Section 5 T4N R62W Weld County Well Production Facility Equipment or activity subject to this permit: Facility Equipment ID AIRS Point . Equipment Description Emissions Control Description DENY -01 001 One (1) Triethylene glycol (TEG) natural gas dehydration unit (make/model/serial number: TBD) with a design capacity of 12.0 MMscf per day. This emissions unit is equipped with two (2) Kimray model 21015 gas -glycol pumps with a design capacity of 3.5 gallons per minute. This unit is equipped with a flash tank, reboiler, and still vent. Stripping gas is not used. Emissions from the still vent are routed to an air - cooled condenser and then to an enclosed combustor. Emissions from the flash tank are recycled to be used as facility fuel gas. CNDTK-01 002 Eighteen (18) 500 barrel fixed roof storage vessels used to store condensate. Enclosed Combustors PWT 01 003 Three (3) 500 barrel fixed roof storage vessels used to store produced water. Enclosed Combustors SLOP -01 004 One (1) 500 barrel fixed roof storage vessel used to store condensate. Enclosed Combustors L-01 005 Loadout of condensate to tanker trucks. Vapor Balance and Enclosed Combustors LPGFL 006 Heater treaters and vapor recovery towers; vapors are controlled by enclosed combustors when the VRU compressors are down. Enclosed Combustors COLORADO Air Pollution Control Division po snerst v Pubbz hieaKt b c?•rvrzeuv enc Page 1 of 16 This - is r ed sub t all rues and regulations of the Colorado Air Quality Control Co on a e' �`ad lutio "-� -vention and Control Act (C.R.S. 25-7-101 et seq), to the specific 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 for the equipment covered by this permit. The Notice of Startup form may be downloaded online at www.colorado.gov/pacific/cdphe/other-air-permitting- notices. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation Number 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. A self certification form and guidance on how to self -certify compliance as required by this permit may be obtained online at www.colorado.gov/pacific/cdphe/air-permit-self-certification. (Regulation Number 3, Part B, Section 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. (Regulation Number 3, Part B, Section III.F.4.) 4. Within one hundred and eighty days (180) after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flow rate of natural gas vented from each separator covered by this permit. Until the flow meter is installed, the operator shall monitor and record condensate/crude produced through the separator and estimate the gas flow rate based on standard cubic feet (scf) per barrel (bbl) of 6.58 scf/bbl estimated in the permit application. 5. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self -certification process. (Regulation Number 3, Part B, Section III.E.) 6. The following information shall be provided to the Division within fifteen (15) days of the latter of commencement of operation or issuance of this permit: • Point 001: The dehydrator manufacturer name, model number, and serial number. 7. 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 8. Emissions of air pollutants shall not exceed the following limitations. (Regulation Number 3, Part B, Section II.A.4.) COLORADO Air Pollution Control Division Department tar Public Health is 4rrduonrrrsnt Page 2 of 16 Facility Equipment ID AIRS Point Tons Per Year Emission NO. VOC CO Type DEHY-01 001 0.2 3.8 0.6 Point CNDTK-01 002 0.9 26.3 4.0 Point PWT-01 003 0.1 0.6 0.2 Point SLOP -01 004 0.1 1.3 0.2 Point L-01 005 0.2 3.8 0.7 Point LPGFL 006 1.4 27.0 6.0 Point Note: 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 not exceed 8.0 tons per year. Facility -wide emissions of total hazardous air pollutants shall not exceed 20.0 tons per year. The facility -wide emissions limitation for hazardous air pollutants shall apply to all permitted emission units at this facility. Compliance with the annual limits, for both criteria and hazardous air pollutants, 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 actual emissions each month and keep a compliance record on site or at a local field office with site responsibility for Division review. 11. Point 001: Compliance with the emission limits in this permit shall be demonstrated by running the GRI-GLYCaIc model version 4.0 of higher on a monthly basis using the most recent wet gas analysis and recorded operational values, including: gas throughput, lean glycol recirculation rate, condenser temperature, wet gas inlet temperature, wet gas inlet pressure, and any other operational values needed to properly model emissions using GRI-GLYCaIc. Recorded operational values, except for gas throughput, shall be averaged on a monthly basis for input into the model and be provided to the Division upon request. 12. The emission points in the table below shall be operated and maintained with the emissions control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit. (Regulation Number 3, Part B, Section III.E.) Facility Equipment ID AIRS Point Control Device Pollutants Controlled DENY -01 001 Still Vent: Condenser and Enclosed Combustor V0C and HAP CNDTK-01 002 Enclosed Combustors V0C and HAP PWT-01 003 Enclosed Combustors V0C and HAP 'COLORADO Aix Pollution Control Division SA'"paru ie':i:' t Puttr, Health , Emire £VY;eni Page 3 of 16 AIRS Point. SLOP -01 004 Enclosed Combustors Pollutants Controlled VOC and HAP L-01 005 Vapor Balance and Enclosed Combustors VOC and HAP LPGFL 006 Enclosed Combustors during Vapor Recovery Unit (VRU) downtime VOC and HAP 13. The owner or operator shall operate and maintain the emission points in the table below as a closed loop system and shall recycle 100% of emissions as described in the table below. (Regulation Number 3, Part B, Section III.E.) Facility Equipment ID AIRS PointRecovered Emissions Recycling Description Pollutants DEHY-01 001 Flash Tank: Recycled to Facility Fuel Gas System VOC and HAP PROCESS LIMITATIONS AND RECORDS 14. 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. (Regulation Number 3, Part B, II.A.4.) Process Limits Facility Equipment ID AIRS Point Process Parameter Annual Limit DEHY-01 001 Natural gas throughput 4,380 MMscf CNDTK-01 002 Condensate throughput 2,190,000 barrels PWT-01 003 Produced Water throughput 1,405,980 barrels SLOP -01 004 Condensate throughput 535 barrels L-01 005 Condensate loading 2,190,280 barrels LPGFL 006 Natural gas venting 14.41 MMscf The owner or operator shall monitor monthly process rates based on the calendar month. The volume of gas processed shall be measured by gas meter or by assuming the maximum design rate of the dehydrator unit of 12.0 MMscf/d. 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. 15. Point 001: This unit shall be limited to the maximum lean glycol circulation rate of 3.5 gallons per minute. The lean glycol recirculation rate shall be recorded weekly in a log maintained on COLORADO Air Pollution Control Division Et^;urmrf '%f Putik,1.1ee th & Environment Page 4 of 16 for inspection upon request. Glycol recirculation rate owing methods: assuming maximum design pump rate, using glycol flow meter(s), or recording strokes per minute and converting to circulation rate. (Reference: Regulation No. 3, Part B, II.A.4 16. Point 001: On a monthly basis, the owner or operator shall monitor and record operational values including: gas throughput, lean glycol recirculation rate, condenser temperature, wet gas inlet temperature, wet gas inlet pressure, and any other operational values needed to properly model emissions using GRI-GLYCaIc. These records shall be maintained for a period of five years. 17. Point 006: Upon installation of the flow meter, the owner or operator shall continuously monitor and record the volumetric flow rate of low pressure natural gas vented from the heater treater(s) and/or vapor recovery towers to the enclosed combustors using the flow meter. The owner or operator shall use monthly throughput records to demonstrate compliance with the process limits contained in this permit and to calculate emissions as described in this permit. 18. Point 006: The owner or operator shall continuously monitor and record Vapor Recovery Unit (VRU) downtime while emissions are routed to the control device. STATE AND FEDERAL REGULATORY REQUIREMENTS 19. The permit number and ten digit AIRS ID number assigned by the Division (e.g. 123/4567/001) shall be marked on the subject equipment for ease of identification. (Regulation Number 3, Part B, Section III.E.) (State only enforceable) 20. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 21. Point 001: This source is subject to the control requirements under Regulation Number 7, Section XII.H. The operator shall comply with all applicable requirements of Section XII and specifically uncontrolled actual emissions of volatile organic compounds from the still vent and vent from any gas -condensate -glycol (GCG) separator (flash separator or flash tank), if present, shall be reduced by at least 90 percent on a rolling twelve-month basis through the use of a condenser or air pollution control equipment. (Regulation Number 7, Section XII.H.1.) 22. Point 001: This source is subject to the requirements of 40 CFR, Part 63, Subpart HH - National Emission Standards for Hazardous Air Pollutants for Source Categories from Oil and Natural Gas Production Facilities including, but not limited to, the following: §63.764 - General Standards §63.764 (e)(1) -The owner or operator is exempt from the requirements of paragraph (d) of this section if the criteria listed in paragraph (e)(1)(i) or (ii) of this section are met, except that the records of the determination of these criteria must be maintained as required in §63.774(d)(1). §63.764 (e)(1)(ii) - The actual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere are less than 0.90 megagram per year, as determined by the procedures specified in §63.772(b)(2) of this subpart. §63.772 - Test Methods, Compliance Procedures and Compliance Demonstration §63.772(b) - Determination of glycol dehydration unit flowrate or benzene emissions. The procedures of this paragraph shall be used by an owner or operator to determine glycol dehydration unit natural gas flowrate or benzene emissions to meet the criteria for an exemption from control requirements under §63.764(e)(1). COLORADO Air Pollution Control Division a b{C HeaN^ & "e^rwont ni Page 5 of 16 2) - Thetermination of actual average benzene emissions from a ation shall be made using the procedures of either paragraph (b)(2)(i) or (b)(2)(ii) of this section. Emissions shall be determined either uncontrolled, or with federally enforceable controls in place. $63.772(b)(2)(i) - The owner or operator shall determine actual average benzene emissions using the model GRI-GLYCalc TM, Version 3.0 or higher, and the procedures presented in the associated GRI-GLYCalc TM Technical Reference Manual. Inputs to the model shall be representative of actual operating conditions of the glycol dehydration unit and may be determined using the procedures documented in the Gas Research Institute (GRI) report entitled "Atmospheric Rich/Lean Method for Determining Glycol Dehydrator Emissions" (GRI-95/0368.1); or §63.772(b)(2)(ii) - The owner or operator shall determine an average mass rate of benzene emissions in kilograms per hour through direct measurement using the methods in §63.772(a)(1)(i) or (ii), or an alternative method according to §63.7(f). Annual emissions in kilograms per year shall be determined by multiplying the mass rate by the number of hours the unit is operated per year. This result shall be converted to megagrams per year. §63.774 - Recordkeeping Requirements §63.774 (d)(1) - An owner or operator of a glycol dehydration unit that meets the exemption criteria in §63.764(e)(1)(i) or §63.764(e)(1)(ii) shall maintain the records specified in paragraph (d)(1)(i) or paragraph (d)(1)(ii) of this section, as appropriate, for that glycol dehydration unit. §63.774 (d)(1)(i) - The actual annual average natural gas throughput (in terms of natural gas flowrate to the glycol dehydration unit per day) as determined in accordance with §63.772(b)(1), or §63.774 (d)(1)(ii) - The actual average benzene emissions (in terms of benzene emissions per year) as determined in accordance with §63.772(b)(2). 23. Points 002 and 004: This source is subject to Regulation Number 7, Section XII. The operator shall comply with all applicable requirements of Section XII and, specifically, shall: • Comply with the recordkeeping, monitoring, reporting and emission control requirements for condensate storage tanks; and • Ensure that the combustion device controlling emissions from this storage tank 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. (Regulation Number 7, Section XII.C.) (State only enforceable) 24. Points 001, 002, 003, 004, 005, and 006: The combustion device covered by this permit is subject to Regulation Number 7, Section XVII.B.2. General Provisions (State only enforceable). If a flare or other combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed; have no visible emissions during normal operations, as defined under Regulation Number 7, XVII.A.16; and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. This flare must be equipped with an operational auto -igniter according to the following schedule: COLORADO Pollution Control Division ai PULA Page 6 of 16 ces ins led on or after May 1, 2014, must be equipped with an er upon installation of the combustion device; • All combustion devices installed before May 1, 2014, must be equipped with an operational auto -igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 25. Points 002, 003, and 004: The storage tank covered by this permit is subject to the emission control requirements in Regulation Number 7, Section XVII.C.1. The owner or operator shall install and operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons except where the combustion device has been authorized by permit prior to May 1, 2014. The source shall follow the inspection requirements of Regulation Number 7, Section XVII.C.1.d. and maintain records of the inspections for a period of two years, made available to the Division upon request. This control requirement must be met within 90 days of the date that the storage tank commences operation. 26. Points 002, 003, and 004: The storage tanks covered by this permit are subject to the venting and Storage Tank Emission Management System ("STEM") requirements of Regulation Number 7, Section XVII.C.2. 27. Point 005: This source is located in an ozone non -attainment or attainment -maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to tank trucks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 28. Point 005: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.D.2): Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. All compartment hatches at the facility (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. The owner or operator shall inspect onsite loading equipment during loading operations to monitor compliance with above conditions. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 29. Point 005: All trucks that loadout condensate from this facility shall have a current certification of NSPS XX leak testing (completed and passed within the previous 12 months of the loadout event). The owner or operator shall retain positive documentation that all trucks used for loadout at this facility were current with this NSPS XX leak test certification at the time of loadout, and the documentation shall be provided to the Division upon request. The applicable NSPS XX testing is described in 40 CFR Part 60 Subpart XX. The records of truck certification must be retained for five years. 30. Point 006: The separator/heater-treaters covered by this permit are subject to Regulation 7, Section XVII.G. (State Only). On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons OPERATING Et MAINTENANCE REQUIREMENTS 31. Points 001, 002, 003, 004, 005, and 006: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record COLORADO Air Pollution Control Division Dimar,mL.nt Pubiclica€t:^.0 Lnvivururenc Page 7 of 16 the D Sion, in order to demonstrate compliance on an ongoing of th `` `''=rmit. Revisions to the OEtM plan are subject to Division approval prior to implementation. (Regulation Number 3, Part B, Section III.G.7.) 32. Point 001: The condenser outlet temperature shall be recorded as per the frequency required in the approved OEtM Plan. This information shall be maintained in a log on site and made available to the Division upon request. The condenser outlet temperature shall not exceed 160°F on a monthly average basis. 33. Point 005: The owner or operator of a loadout at which vapor balancing is used to control emissions shall: • Install and operate the vapor collection and return equipment to collect vapors during loading of tank compartments of outbound transport trucks and return these vapors to the stationary source storage tanks. • Include devices to prevent the release of vapor from vapor recovery hoses not in use. • Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. • Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. • Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. • Inspect pressure relief devices (PRD) annually for proper operation and replace as necessary. PRDs shall be set to release at a pressure that will ensure flashing, working, and breathing losses are routed to the control device under normal operating conditions. • Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 34. Points 001, 002, 003, 004, 005, 006: The owner or operator shall demonstrate compliance with opacity standards, using EPA Reference Method 22, 40 C.F.R. Part 60, Appendix A, to determine the presence or absence of visible emissions. "Visible Emissions" means observations of smoke for any period or periods of duration greater than or equal to one minute in any fifteen minute period during normal operation. (Regulation Number 7, Sections XII.C, XVII.B.2. and XVII.A.16) 35. Point 001: The owner or operator shall complete an initial extended wet gas analysis within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit. The owner or operator shall use this analysis to calculate actual emissions, as prescribed in the Emission Limitation and Records section of this permit, to verify initial compliance with the emission limits. The owner or operator shall submit the analysis and the emission calculation results to the Division as part of the self -certification process. (Reference: Regulation No. 3, Part B, Section III.E) 36. Point 002: The owner or operator shall complete site specific sampling including a compositional analysis of the pre -flash pressurized condensate routed to these storage tanks and a sales oil analysis to determine RVP and API gravity. Testing shall be in accordance with the guidance contained in PS Memo 05-01. Results of testing shall be used to determine a site - specific emissions factor using Division approved methods. Results of site -specific sampling and analysis shall be submitted to the Division as part of the self -certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. ;COLORADO Aar Pollution Control Division Page 8 of 16 37. oper or shall complete site specific sampling including a omp• `.n .' lys `.`' pre- =�' pressurized water routed to these storage tanks and a flash liberation analysis to determine the gas to water ratio (GWR) in units of scf gas/BBL water. The analysis of the flash gas shall include gas chromatography (GC) to determine total VOC, n -hexane, and benzene content. Testing shall be in accordance with the guidance contained in PS Memo 14-03. Results of testing shall be used to determine a site -specific emissions factor using Division approved methods. Results of site -specific sampling and analysis shall be submitted to the Division as part of the self -certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. 38. Point 004: The owner or operator shall complete site specific sampling including a compositional analysis of the pre -flash pressurized condensate routed to these storage tanks and a sales oil analysis to determine RVP and API gravity. Testing shall be in accordance with the guidance contained in PS Memo 05-01. Results of testing shall be used to determine a site - specific emissions factor using Division approved methods. Results of site -specific sampling and analysis shall be submitted to the Division as part of the self -certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. 39. Point 006: The owner/operator shall complete an initial site specific extended gas analysis ("Analysis") within one hundred and eighty days (180) after commencement of operation or issuance of this permit, whichever comes later, of the natural gas vented from this emissions unit in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n -hexane, and 2,2,4- trimethylpentane content (weight fraction) of this emission stream. Results of the Analysis shall be used to calculate site -specific emission factors for the pollutants referenced in this permit (in units of lb/MMSCF gas vented) using Division approved methods. Results of the Analysis shall be submitted to the Division as part of the self -certification and must demonstrate the emissions factors established through the Analysis are less than or equal to, the emissions factors submitted with the permit application and established herein in the "Notes to Permit Holder" for this emissions point. If any site specific emissions factor developed through this Analysis is greater than the emissions factors submitted with the permit application and established in the "Notes to Permit Holder" the operator shall submit to the Division within 60 days, or in a timeframe as agreed to by the Division, a request for permit modification to address this/these inaccuracy(ies). Periodic Testing Requirements 40. Point 001: The owner or operator shall complete an extended wet gas analysis prior to the inlet of the dehydration unit on an annual basis. Results of the wet gas analysis shall be used to calculate emissions of criteria pollutants and hazardous air pollutants per this permit, and be provided to the Division upon request. ADDITIONAL REQUIREMENTS 41. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Regulation Number 3, Part A, II.C.) • 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 NOX 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 COLORADO Air Pollution Control Division Page 9 of 16 100 t. s per year or more, a change in actual emissions of five yea 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. • Whenever there is a change in the owner or operator of any facility, process, or activity; or • Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or • Whenever a permit limitation must be modified; or • No later than 30 days before the existing APEN expires. 42. MACT Subpart HH - National Emission Standards for Hazardous Air Pollutants From Oil and Natural Gas Production Facilities major stationary source requirements shall apply to this stationary source at any such time that this stationary source becomes major solely by virtue of a relaxation in any permit limitation and shall be subject to all appropriate applicable requirements of Subpart HH. (Reference: Regulation No. 8, Part E) 43. 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 Number 3, Parts C and D). GENERAL TERMS AND CONDITIONS 44. 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 Number 3, Part B, Section II.B. upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 45. 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 Number 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. 46. 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. 47. 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. COLORADO Air Pollution Control Division Depa file^.. %.'. PUt1(a" I-�E'£5C>'f.3' SPe'IIYIr rn, %f Page 10 of 16 48. f this . mit is a material part hereof and is not severable. Any alle - t• • :'.p condi "Whereof 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. 49. 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. 50. 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: Andy Gruel, P.E. Permit Engineer Permit Histo Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC. COLORADO Air Pollution Control Division Depart -mere -of Public' Health b e^^ ve rram Page 11 of 16 No th - x s this it 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. (Regulation Number 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-regs 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. AIRS Point Pollutant CAS. # Uncontrolled Emissions (Ib/yr) Controlled Emissions (Ib/yr) 001 Benzene 71432 26040 1180 Toluene 108883 36140 1400 Ethylbenzene 100414 14240 420 Xylenes 1330207 37100 1020 n -Hexane 110543 3300 160 2,2,4- Trimethylpentane 540841 338 20 002 Benzene 71432 5754 288 Toluene 108883 5172 259 Ethylbenzene 100414 669 33 Xylenes 1330207 1601 80 n -Hexane 110543 39120 1956 2,2,4- Trimethylpentane 540841 4388 219 003 Benzene 71432 445 22 Toluene 108883 391 20 Ethylbenzene 100414 37 2 Xylenes 1330207 98 5 n -Hexane 110543 176 9 COLORADO Aix Pollution Control Division Page 12 of 16 AIRS Point gm Pollutant CAS # Uncontrolled Emissions (lb/yr) Controlled Emissions (Ib/yr) 2,2,4- Trimethylpentane 540841 3 1 004 Benzene 71432 60 3 Toluene 108883 64 3 Ethylbenzene 100414 17 1 Xylenes 1330207 33 2 n -Hexane 110543 495 25 2,2,4- Trimethylpentane 540841 146 7 005 Benzene 71432 390 24 Toluene 108883 318 20 n -Hexane 110543 5622 351 2,2,4- Trimethylpentane 540841 424 26 006 Benzene 71432 5654 283 Toluene 108883 5072 254 Ethylbenzene 100414 658 33 Xylenes 1330207 1572 79 n -Hexane 110543 38518 1926 2,2,4- Trimethylpentane 540841 4060 203 bove Note: All non -criteria reportable pollutants in the table above with uncontrolled emission rates a 250 pc per year (lb/yr) are reportable and may result in annual emission fees based on the most recent Air Pollution Emission Notice. 5) The emission levels contained in this permit are based on the following emission factors: Point 001: CAS # Pollutant Uncontrolled ` Emission Factors lb/MMscf Controlled Emission Factors lb/MMscf Control Efficiency %', Source NOx 0.0596 AP -42 Ch. 13.5 CO --- 0.2716 ---- AP -42 Ch. 13.5 VOC 43.94 1.6962 96.14 GRI-GLYCaIc 4.0 model based on a non -site - specific sales analysis 71432 Benzene 5.95 0.2695 95.47 108883 Toluene 8.25 0.3193 96.13 100414 Ethylbenzene 3.25 0.0959 97.05 1330207 Xylene 8.47 0.2330 97.25 110543 n -Hexane 0.76 0.0369 95.15 540841 2,2,4 -gas Trimethylpentane 0.077 0.00385 95.0 =COLORADO Mr Pollution Control Division Health £J Environment Page 13 of 16 facto for this point are based on the enclosed combustor control f •°' ., ` �" ��: vari �'� ontrol efficiency of the condenser depending on the physical properties of the pollutant. Combustion emissions (NOx and CO) are based on a heating value of 2,235 Btu/scf, a flow rate to the combustor of 196 scf/hr (as modeled by GlyCALC), and AP -42 Chapter 13.5 emission factors for industrial flares. The total NOx and CO emission (lb/yr) was divided by the permit limit 4380 MMscf/yr to arrive at the emission factors listed above in terms of lb/MMscf. Point 002: CAS # Pollutant Uncontrolled ` Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source N0x --- 0.0008 AP -42 Ch. 13.5 CO --- 0.0037 AP -42 Ch. 13.5 V0C 0.48 0.024 Promax model based on a non site specific sample collected 6/9/2015 71432 Benzene 0.003 0.00013 108883 Toluene 0.002 0.00012 100414 Ethylbenzene 0.0003 0.00002 1330207 Xylene 0.001 0.00004 110543 n -Hexane 0.018 0.00089 540841 2'2'4 Trimethylpentane 0.002 0.00010 Note: The controlled emissions factors for this point are based on the enclosed combustor control efficiency of 95%. Point 003: CAS # Pollutant Uncontrolled Emission Factors lb/bbi Controlled Emission Factors lb/bbl Source N0x --- 0.00003 AP -42 Ch. 13.5 CO --- 0.00013 AP -42 Ch. 13.5 V0C 0.0164 0.00082 Promax model based on a non site specific sample collected 71432 Benzene 0.00032 0.000016 108883 Toluene 0.00028 0.000014 100414 Ethylbenzene 0.00003 0.000001 1330207 Xylene 0.00007 0.000003 110543 n -Hexane 0.00013 0.000006 540841 224-6/9/2015 Trimethylpentane 0.000002 0.0000001 Note: The controlled emissions factors for this point are based on the enclosed combustor control efficiency of 95%. Point 004: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors. lb/bbl Source N0x --- 0.1158 AP -42 Ch. 13.5 CO --- 0.5281 AP -42 Ch. 13.5 V0C 97.22 4.86 Promax model, and gas analysis for blowcase motive gas; see below 71432 Benzene 0.112 0.0056 108883 Toluene 0.119 0.0060 100414 Ethylbenzene 0.032 0.0016 1330207 Xylene 0.063 0.0031 110543 n -Hexane 0.926 0.0463 COLORADO Air Pollution Control Division Page 14 of 16 CAS # Pollutant Uncontrolled Emission Factors lblbbl Controlled Emission Factors lb/bbl Source 540841 2'2'4 Trimethylpentane 0.272 0.0136 Note: The controlled emissions factors for this point are based on the enclosed combustor control efficiency of 95%. Emission factors for Point 004 are a sum of the flash and working/breathing emissions from the tank (as modeled by Promax) plus the blowcase emissions (as modeled by the Displacement Equation on a sales gas analysis from a non -site -specific sates gas sample collected 6/9/15, and based on 0.764 MMscf/yr of venting.) Point 005: CAS # Pollutant Uncontrolled Emission Factors lbAbbl loaded Controlled Emission Factors lb/bbl Source N0x --- 0.000132 AP -42 Ch. 13.5 CO --- 0.000601 AP -42 Ch. 13.5 V0C 0.05549 0.003457 AP -42 Ch. 5.2 Eqn 1 71432 Benzene 0.000178 0.0000181 Eng. Calc. 108883 Toluene 0.000145 0.00000964 Eng. Calc. 110543 n -Hexane 0.002567 0.0001702 Eng. Calc. 540841 2'2'4 Trimethylpentane 0.000193 0.00001283 Eng. Calc. Note: The controlled emissions factors for this point are based on a vapor balance collection efficiency of 98.7% (relying on a current annual NSPS )X certification of all trucks), and a enclosed combustor control efficiency of 95%, for an overall control efficiency of 93.77%. The uncontrolled V0C emission factor was calculated using AP -42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L = 12.46*S*P*M/T S = 1.0 (Submerged loading: vapor balanced service) P (true vapor pressure) = 2.61 psia M (vapor molecular weight) = 33.45 lb/lb-mot T (temperature of liquid loaded) = 525 °R The uncontrolled non -criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the sales oil sample (not from a site -specific sample) by the V0C emission factor. Point 006: CAS # Pollutant Uncontrolled Emission Factors lb/MMscf Controlled Emission Factors lb/MMscf Source N0x --- 182.4 CDPHE CO --- 693.5 CDPHE V0C 74854.8 3742.7 Promax 71432 Benzene 392.5 19.63 Promax 108883 Toluene 352.1 17.61 Promax 100414 Ethylbenzene 45.7 2.29 Promax 1330207 Xylene 109.1 5.46 Promax 110543 n -Hexane 2673.6 133.68 Promax COLORADO Air Pollution Control Division 5Del'a rnerit'vt PvIM : 11ezith e^≤rzorirr m Page 15 of 16 CAS # Pollutant Uncontrolled Emission Factors Ib/MMscf . Emission Factors lb/MMscf Source 540841 2,2,4- Trimethylpentane 281.9 14.10 Promax Note: The controlled emissions factors for this point are based on the enclosed combustor control efficiency of 95%. Combustion emissions (NOx and CO) are based on a heat value of 2237 Btu/scf. 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 permit fulfills the requirement to hold a valid permit reflecting the storage tank and associated control device per the Colorado Oil and Gas Conservation Commission rule 805b(2)(A) when applicable. 8) This facility is classified as follows: Applicable Requirement Synthetic Minor Source of: VOC, HAPs (benzene, toluene, xylenes, n - hexane, and total) Operating Permit PSD or NANSR Synthetic Minor Source of: VOC MACT HH Area Source Requirements: Applicable 9) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1 -End Subpart A - Subpart KKKK NSPS Part 60, Appendixes Appendix A - Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 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 COLORADO Air Pollution Control Division 'e: eva rtfr em —.;f I'aenith $ ?E^dPonifY znc Page 16 of 16 Emission Source AIRS ID: t # & AIRS ID] [Leave blank unless APCD has already assigned a p Permit Number: in your organization.] [Provide Facility Equipment ID to identify how this equipment is referenced wi Facility Equipment ID: Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information Request for NEW permit or newly reported emission source h .,.1 o. 0 O A 0h ❑ O O o o, Tie O a Wa) 0 x C h F ^ E •r >, -p o 2 0 .0 ° a .o r. .0 a. O _ 0..7, ° 0 8 y 01 a as a 0 ti 0 3 <° o i_ C C E r. U F" �° 0 •o c x 4 O ❑ ❑ O O 0 o 01) .t7 w C 0 to 0 (7y 41 b .A O Zvi y z.. e�4z 'en 3 0 C.) I7 0 .yy 0 1 't% V F+ v _ O U y a a O in Z O ° 0 O 00 0D AlA w �., O ❑ 0 icy 'O O ccdd cd _ d' d a 6j•' y U U h h ` a a) as 0 0 0 0.a 0 a❑ ® ❑ 0 o 0 "Si U U z0 Bonanza Creek Energy Operating Company, LLC z E 0 Source Name: 3 Source Location: C) 0 In N O O 00 O O as C a) as 0 Mailing Address: O 0 0 O 0 a) C7 as Person To Contact: 720-305-0802 a z Section 03 — General Information O p•O a7 O a)) ICI C) 0� C vi O v) a Ex k O 0 O ° Z O 0 ger C) CO -o en a) 'o en O O Q ° es 0 0 0 ^ O O o A A ❑ 0 z z z ❑ 0 E ® 0 O 0 O CO 0 gn C O U O b fl O 0 A 3 eso X b r 0 d C O o W , H n en as o Al o b° ea r. W o a C O U 0 No z O W o co b0 0 a C b 0 U C cy o 0 U o 2 s� o 0 0 0.4 ) y �• 0 'C 4 c7 h CG C inmaintain.html) hc.state.co.us/a (http://www.cd Will this equipment be operated in any NAAQS nonattainment area? C"-• C C source that is considered a Major Source of Hazardous Air Pollutant Is this unit located at a station C d E 0 • ro A O 0 4s 'd a 6: O 8 L 0 O Al* a Aa 0 0 0 O U 0 -o it 0 O E 0.., N ai C. a) -0 N U b ca— C = a "x �E �� .°� CO apeC00 2 .o a b> o 0 5 d uo 0• 'r, -e-'a > r.) t0" i N 0 di 0 o U N .C) ° a. i4t CO U o.. O 0 aa) ,.0V)�V .0 a O ccd 4 O' V d m O.� ,_, oA0 > n a,0 g k'� OUd'A w° aan O • N .j M M m N N N V, he.state.co.us/a i 3 U U) he.state.co.us/a APEN forms: htt Application status: Section 04 — Dehydration Unit Eauinment Information CO 00 b O Manufacturer: 2pia 0 0 Reboiler Rating: C7 A DiEthylene Glycol C G•1. 0 O O Kimray 21015 Pump Make & Model: 0 O M 7 Design Capacity: Dehy. Gas Throughput: O rl 0 01 Z z t❑® O a A H O O 00 L y N C a) U- CO Water Content: O N tU bmi 0. H H 00 00 U L/) N m a) w Flash Tank: C) m d Cold Separator: z a) 3 "vi b0 b a� ❑ CO ea a 5 O O Z§ o ® 3 O' a) 0 N 0 U C 72) .4 a. O O -o -o 0 0 0 0 U U Cl) U) O O U EZ v O Ii o h CU C4 N 0 it > A. Q co o a' ax acoo) < 00 oU E t, r O O co 'O r N U b0 L)) lii M V w et et ea Q DEEI b O E tx Form APCD-202 G N w 0 a) CO P-i M oo I 44 4 r:4 c.> c.7 z • 0 V 4.4 el Cd fa a " U F M�1 N-1 ew c4 O C T O .0 0 O O CJ CI O A V ID Emission Source AIRS ID: Permit Number: Section 05 — Stack Information (Combustion stacks must be listed here) O 0Cl` E -104.356054 M ry oo A a00 �z�, '§tr.:7;c N3 N 0 z M Ci0 Z CU m 8 O H °v CU Other (Describe): Width (inches) = Horizontal ❑ Down O Other: Length (inches) = El CO E El 0 Circular: Inner Diameter (inches) = El be 0 O U • N C%) C) 00 O 0 device controls the flash tank and/or regenerator emissions) Section 07 — Control Device Information (Indicate if a contro 0 ® Combustion Device used for control of: 0 a Manufacturer Guaranteed: Waste gas heat content: Pilot burner rating: cc liz ❑ U C) Co >, a) a) c.) a) c , U N ,—,•(-) ••L _ • cc C o o o 0 O .. U Co' H • 'a. CoH O U F G) E CO Temperature (°F): ted VOC & HAP Control Efficienc C a+ s 0) Flash vapors are sent to the sales gas line. As a backup the vapors are sent to the fuel system. oe 44 0 Co 0 0 U D O O Requested VOC & HAP Control Efficiency: '0 O a) Section 08 — Emissions Inventory Information & Emission Control Information Estimation Method or Emission Factor Source; AP -42 GRI-GlyCalc 4.0 N GRI-GlyCalc 4.0 GRI-GlyCalc 4.0 GRI-GlyCalc 4.0 GRI-GlyCalc 4.0 GRI-GlyCalc 4.0 Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions3 Controlled (Tons/Year) H O IN M In O V7 O ON O N O 0.51 O co, Uncontrolled (Tons/Year) N/A 96.23 N/A 13.02 18.07 7.12 in CA r. 1.65 Actual Calendar Year Emissions2 Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor lb/INIMBtu u u b/MMscf lb/MMscf u u Uncontrolled Basis 00 O O 43.94 00 M co Ocn bi In 8.25 N• M I 8.47 0.76 Control Efficiency (% Reduction) Identify in Section 07 Control Device Description Secondary C •• .C a Pollutant XON VOC CO Benzene Toluene Ethylbenzene U a) X n -Hexane z N N to .0 reel 7 6 .0 a Co L 0 Co 0 Po W u O u 0) L Tt co 0) A & Env. En ervisor. Permittin i. d CU H N W O N a) CO a z w w U H 0 z 0 Cl) cn H z ✓ J J 0 Na I.L. w J m H cc 0 a w w I ce V 0 z E O rn a) a E O U O a) U t6 0 5 O a) O Cl) a) Co a) a) a) a) U) 123-05-E? 0O I AIRS ID Number: Permit Number: U J J Co Q E O 0 a, Co a) a O a C) Lm w U co N C C O m Company Name: Zip Code: 80202 N C O U Seventy Holes CPF B-5, SWNW Sec 5, T4N, R62W Plant Location: JDismukes@BonazaCrk.com E-mail Address: Controlled Actual Emissions Ibs/ ear 15 Uncontrolled Actual Emissions Ibs/ ear M M Emission Factor Source G I-GlyCalc 4.0 Emission Factor (Include Units) 0.077 lb/MMscf Control Equipment / Reduction (%) 95 Chemical Name 0 C a) _a L_ a) E .` I- 4 N N Chemical Abstract Service (CAS) Number 4— CD O z Actual Data Applies: J rJ e 0 Co >- Co Co 0 f Person Legally Authorized to Supply Data Supervisor, Permitting & Env. Engineering Jerry Dismukes Title of Person Legally Authorized to Supply Data Name of Person Legally Authorized to Supply Data (Please print) Form Revision Date: A CA O O N Emission Source AIRS ID: unless APCD has already Permit Number: [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.] Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information APEN Submittal for update only (Please note blank APEN's will not be accepted) a) 0 a; 4) 4) h O O C.) cle L y ea 2 CD e 0 0 o 4), O ^ u p o , 0 E w a 4F,°D o a) 6 tq „ Qd 4) a O23 y O ®❑ ❑ ❑ ❑ d kz a) 'o o 1.1c N N 3tr3 etr oo O 'b 0 ° 0 vn o p U ZU U U 0 P-' c W N Bonanza Creek Energy Operating Company, LLC z E O U 410 17th Street, Suite 1500 720-305-0802 z Section 03 — General Information r N O 0 to O O O N 0 0 w o 3 > z , eq a) y 0 oo N ® 7 zz atm ❑ Ct E o 0 CCI ZZoo N a Jig T q2 OZ o cn v o = 4 p Al ° el.) 4) 4 a a o a, a 4 17 b O 00 .174 cci b o �v � 618 p o as o a) 0 0 a) �; > 0 o0E 0 Lo b a+ y O CC ,n ai G >. a a o _ G b a) O Sr� N N N S >w p pW„i O ad, CV O 0 'O W A `t ilric o°°; W 14 ,=4�1 .--0° 4)F.., O•p 69 i.N �. et. A `° 0 v3 cry c.) � z by N a, 6, a, 2 .OOP1OOO-rrie. 1". y O c0 co ° oq. o,4 3,flOa o aa) y°, 6 - ❑ bD 0 W a0, 8 a o �u'4_o 4 o s i64O oo, 0 y o ro o U A a) lz1 o U ° hW 4Age W ,., o. 3 a ti ;, o a, U �o • 'E'a8,r �0 'Ua'', 1) 0.0 > -�..y eA0 > as C 0 p., Ud��:3 Fr Wtp Eu or For guidance on how to complete t Air Pollution Control Division: Small Business Assistance Program .0 U > 0 ://www.colorado APEN forms: ht Ct a) G 6) b O O //www.colorado Application status: 1 co 0 .0 .0 N Z Requested Permit Limit: 44 o N H CO RVP of Sales Oil External Floating Roof: Internal Floating Roof: Fixed Roof: Date Of First Production (Month/Year) O B O CO O a b 4) d COR i. O 'a 2 131 Name of Well State Seventy Holes 11-5-17XRLNB State Seventy Holes 21-5-17XRLNB State Seventy Holes F-J-5HNB State Seventy Holes K21-5-17XRLC API Number Emission Source Al Permit Number: 353853 Page 1 oft FORM APCD-2(15 CC et i/) it CC C1 U 4.0 A O it O I-� C4 W AIR POLLUT Section 06 —Stack (Source, if no combustion) Location (Datum & either Lat/Long or UTM) O v • b0 0w0 U • 5 bD g' o' 0 o • yw • v 0 a a M -104.356054 M 00 5 d O 4 o C) O en ) ro 0 > • CO q • CO bp x C.7 Other (Describe): E CO C 0 Width (inches) _ Other: Length (inches) = Vertical ❑ Vertical with obstructing raincap ® Circular: Inner Diameter (inches) = 48 Direction of stack outlet (check one): 2 Qa M C CO ® Combustion Device used for control of Eight (8) ECDs (SNs: TBD) Enclosed Flare O1 Manufacturer Guaranteed: Control Efficiency: w 2 en 0.1 � OO 00 N Waste gas heat content: Pilot burner rating: 0 0 0 5 Section 07 — Control Devi C.) a) A ❑ r control of the stora E&P Sites Onl Information aration Technolo Section 08 — Gas/Liauids Se ‘5.t.„‘) CO a] CO O a) x 0 0 C O C) U, 0 CO CO CO a) 0 U, v a) CO 0 a ...4 0 y a) C C •0 C) s q V Q CQ ✓ O V) W U, 0 0 U a O 6 0 V q HI y 0 V V N ai d v7 CO a a co: a'O+ c C) V i L O d u CO CO m 666 C 'O u CO CO CO O CO n a O u 0 L C u w 0 Emission Factor' Data Source AP42 Tbl 13.5-1 II Promax Model II AP42 Tbl 13.5-1 Promax Model II Promax Model II Promax Model Promax Model II Promax Model Promax Model Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions Uncontrolled (Tons/Year) I Controlled (Tons/Year) 0000 0 26.29 4.0 •- 0 0.13 0.02 o 0 00 0 Il 0 z 525.84 V/AI O\ No• 2.59 M O o V7 .1N ti Actual Calendar Year Emission Uncontrolled (Tons/Year) Controlled (Tons/Year) I Emission Factor I Units a .a n0 ot=1 AM NIM 4:2 Uncontrolled Basis o 0 O 0.31 o 0 o 0 .r • 0 o 0 0 0 0 Pollutant xON VOC CO Benzene Toluene a) C .O W Xylenes n -Hexane C) CO o a. a) 4 N N O O a A V ti O) E-+ 0 o y O a CO an -coa) CO o an O 2 • -o O a)< C -o 0) O O a 4 CO • E z. - CO CO U, CO • O ti rV O .� CO 00 _,n 0 0 • rn CO U CO a O n CO CO t. Q 'to= at CO a00) b w 01) O v •� ti OO . O .5 • a N a a O O 0. a, 0 0 O E p x 8 CO C a O 0 a pCO .23 ar C) N U a G O CO a 0 CO C) a 1." U Q 0 C 0 .0 6 F 0 0 6 O 'C 0 a .2 I 00 W 'CO U N 4- O 01) C) CO a FORM APCn-2n5 .2 CC U C.) OBI est a U 6) ^W^ rQ O coo 1D E— M O N— N T Emission Source AIRS ID: '+O Permit Number: c c n 9) R rb G C 75 m E. 0 sL 9) G, Z. tz: 3-6 r-i c Section 01 — Administrative Information 100 . uu Z c z ces C U SWNW Sec 5, T4N, R62W C C 0 et 00 N 00 410 17th Street, Suite 1400 O C C 720-305-0802 a z E-mail Address: N 0 9) 4) -C C O C U 3 zzzzz ❑®®®❑ N en .. >, o - Cif Z 00C)i) 0 J U MODE CC U ti E) 0 y U C 7a o - ti., L 0 o -f-- -. =� 0;� att o 0 41 •c L. 0 CVI L V1 Li -,CC C L. 0 Z a U v ' O C ❑3 Cr';: �. V c C C p R •C E C C t C A q I-Ui L L, y C 5 z J" rn Q. ' O Ca 3 0 0 > ' u ❑ ❑ w L c3 t) o a 0 0 .. . c L Q �. v .7. T'C y C C) 'C U c n E C v G G J o. c,-, P a. c L C 0 >. .i'C. v g o s a TC r U L O G 0. - c a U d3 ° cc -' ° o 80V) a u E d — • C.) U o cn Q U o-0 J o j1E _. rj m 0 C,:iz in— v> W� =C -LYE 0 — ® U cC c �:, 3 AI A'0 G— CD C. 0 U U -C 0 ? CD° w c ti L C 0 . U V j V L) C C 6) C C- U •ril, y C v-5 oT •. i CD„ c>.. 44 M C U Q O < Q 'C ., 3 > C 0 0 )- ti, L C y Q d > Z o u 4. > 4 . O .. -C 6 Y u ..r C: o .o m T. lf) C rr) C J^ r ` C £R a '> U _ O • L C � U 0, C 'o w K c o \'-C 0 _) v tC y O CO tn e.. r r 5~9 L N .. El ^ t L O V4 C.CJ O h t m C. C 4. = d CQ ; u m w C 2 D v v v C> w 0 b u i C O a =< cC. a c o . v� y y .= 0- `o C" 03 R .o 5 z O. o i cz y yo 4. C C 0 W = 12 '11 .r C y Cq y a C y 7 L 0 = •W CD ' E 4. L rLl N • a ° ."c ..` o:nom, cCGr LO oS' 3 C�9d^ o� t; C.) 0 o r o 5 E v L A a v 5a. >, �_C y cVo > e, _ E•7 4t >•'O C.C d. UQ:2)2, c9- W2 iUdcra C Co .4; .. ,- N rnm m,n CO \—°;4;_' �. z — 9)C .- f_: CSI '.-1 Q Cell— U & O "6:C. . r g `4f f/ ,C S C-. T Q Pfi ..-E 8 C) cc Ti c o 8 'y v > 00 Q m ilt C. •� 0O C Q 1 o . .I C) v C) C U vi u O .C P c r -0 CO w eDF,�, � C. C Q CI) < 7.7 C{ 7-4 C c U O. C. C E C- L :6 T z Actual While Controls Operational: zz C Q External Floating Roof: Fixed Roof: CD y a C ea C C V 4.0 ., w aJ :D C L L G c at c y r u q CC o V) 011 V a Lo C F L M 3 d C Z Name of Well State Seventy Holes 11-5-17XRLNB State Seventy Holes 21-5-17XRLNB State Seventy Holes F-J-5HNB State Seventy Holes K21-5-17XRLC API Number 9) m F a co C C 0 q F Form APCD-207-ProducedWaterTank-APEN.doe is 4rf FORM APC11-2117 ea ea Q Emission Source AIRS ID: 7 O C O C) r s Q CC U .15 C a O O c v u O U C) Cip C) CJ o z 5 C U 7 Cl 7 -104356054 M C O cc. ® Combustion Device us Enclosed Flare 00 a C. o� o 0, C\ C Q z U U T O - U c C) U U L4) .0 E o G < O = E O U F U 0 Ceo C C t (VRU) use L O L C C: Make/Model: N Cl) o c C) O .ro- G L C C ❑ ' C O V C) H C c i, C. C O C) L c L O O C E C O C C) w 1.1 C d a y C) ( rr, C O u C) Estimation Method or Emission Factor Source CDPHE Mcml) Promax CDPHE Memo Pro x co en x t Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutan• ts not listed above. 11 Requested Peonitted Emissions Controlled (Tons/Yearl 7 C Cr" 00 C • CC — C O ,... C. c:.. 7 C Uncontrolled (Tons/Year) Q z Q z 0.22 N o O O Actual Calendar Year Emission2 Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor ,�'.. 1.1 O O .C A — U J O 0 O 7 .C 0 O N C 0 C M C 0 C C- © © O O © O 5 a ....-5 C XON voC Q r...,- Benzene O U C O E- U N y T -cX Lr C) j T m X U .T. — C) C «C+ U 7, y F 7 N e../ 47 C) L. 1. C C, CC La GU i Ana O4 CU O L U O co> co C > O L d0 .... V] H a c D, C) a � .- p., • C g a a Cil a O .ir •y F, E a C _O F. W O .C+ yo Ts r,�I as .�. iC v L C C 00 C2 y = w 3 a O c d R C O C •o .te �zLy C 5 H O U n E E CC E oi L 1.4 C O U C W rC 023 CS' 0. 0 win APCD-207-ProducedWaterTank-APEN-doe N w c N C) C) FORM APCD-207 O Emission Source AIRS ID: 03 unless APCD has already assigned a p .0 U .111 3 [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.] I Pi 00 Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information E as Cu g a A V E «. 0. L. 0 az y w ai C7 a) Z b O a Q 00 3 d w W ° A z� O a o� o o� Change company name Change process or equipment Transfer of ownership Change permit limit APEN Submittal for Permit Exempt/Grandfathered source APEN Submittal for update only (Please note blank APEN's will not be accepted) "J A El El 0 ❑ ❑ ¢ °z Ire 0) et N N 00 O 0 0 A 720-305-0802 Section 03 — General Information NN 0 00 0 0 0 CO 0 v • • C 0 3 Tz z z ❑ Z ❑ ❑ N Normal Hours of Source $2%.,4-. A Are Flash Emissions anti • cid N Ot. a) p 0 Al 0 4.. o 0 0 ro 0 03 o tno 0 o v a 0 00 o U 0 o . a .i o a) b Q. Z a^'a�^O' o W c o >, e' `,. .5a o a.� ° ° Al E p cc - 8 t) .2. a P.= G o , O H o C) -0 cn y 0 0 ml o o. 0 U C) 0 •� •� a p, y >° a. C I U •a G U C) C et m 0 a°i 0 ¢ .d o v, en �� c♦♦ o v 0 O co kr) m m m Q U Z O Tr._.NNN C') W co I P. Q O:CD `� m m m Q N 97 0 W o .14 0 1. N •o pp 0 O - q L 0 EA W > Q Z 00 N 0 d d 'y0 COE a a al caa N U y i O - 00 to QI � q O 7 .y V of 0 C ' •� a. O C) . co8py�uOo�'W 8 �N �� 1 g. g 0 g y o a U o U Q 2 y V W Q O C) C U CA q O g •o .� 0 0 Cl E a in 0 A V d p O Ca >, O.' Cw—a' 0UO p b0 a' ai O L. 0 > .� O O y b. ,- Ua� Ww- i:U�aA w° am APEN forms: httn://www.colorado. ermitstatus 00 00 0 O U 0 ://www.colorado. Application status: ht U L {. 0) 0 a0 a 00 00 0) 00 0 a 1. w 00 O a b a, OO VI 0 a, 00 u s. O 0) E 0 O a) i0. O h 0 h a N 1.1 a) 0 O J, z Actual While Controls Operational: >, .0 -0 N ofin E r b e A b +O+ C) C V d C° >, o 1° 0 b a) s. Tnito,0 Ww Requested Permit Limit: Q z z RVP of Sales Oil External Floating Roof: CO O Q `413 El an 0 0 cO • 0 k w g 0 N a Q .on ' a°D "O AUH E d a 00 a) Fa a) U Ca O a+ i rn 0 00 O L i. O y o eq A On O h o> 00 00 al aw o On y. CO 0 a 0 m Wells Serviced by this Storage Tank or Tank Battery (E&P Sites Only) r Newly Reported Well • ■ ■ ■ ■ Name of Well 1. CU E z 1 II FORM APC11-2O cet 6J R1 y ON N Emission Source AIRS ID: Permit Number: O O 00 O as O1 Ir 67 "G1 as O O O C o 0 00 C o z .71 ° Source. if no combustion Section 06 —Stack ti No 104.356054 Z oo xO N A0 Z N g 3 CJ o Other (Describe) O O Direction of stack outlet (check one): Width (inches) = II i U .O. Exhaust Opening Shape & Size (check one): Section 07 — Control Device Information &P Sites Onl Information aration Technolo ID "d Section 08 — Gas/Li 00 CO H N C) C O m O CJ b�q U cn o. co 0 a� O 0 cn O tO. ti ti 6 U .Y See Attached Process Flow Description and Diagram. O y 00 3 .fl cn cn 0 0. 0 d cn C U N a) a) 0 5 S,a o 151 O U O col O at at 6 w O ;Ti O ON O O U C) z N d d Cn 0 0 .a 00 O 0 .O O O CO C 6� C) C 7 CO C C L d y A 'O d C C 0. 0 5 E A m CO O Emission Factor: Data Source AP42 TbI 13.5-1 Promax Model AP42 Tbl 13.5-1 Promax Model Promax Model Promax Model Promax Model Promax Model Promax Model Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions Uncontrolled (Tons/Year) I Controlled (Tons/Year) ,'• 0.03 1.30 0.14 N O 0 N O 0 rl O 0 N '=. 0= C rl O 0 Q z 26.02 Q z M O o M O O C •O N O 0.25 n O 0 Actual Calendar Year Emission Uncontrolled (Tons/Year) I Controlled (Tons/Year) Emission Factor Uncontrolled Basis I Units CO .0 CO .0 II Please use the APCD 00 0 0 97.22 •-•N '. H 0 O\ rl 0 N O 0 M O 0 �D ON 0 0.272 Pollutant xON VOC CO Benzene Toluene Ethylbenzene Xylenes n -Hexane U `4 N 7-, 0) 9 . ( 4 N N V C) 0 O U 6 CC iw a 0 CO 0 0 V o O C) 7.0 U 0, rtZ CC I) .:� ry.+ O CC W "0 q Yr 6J 1E.1 O O O .C.y C) .t7 q O ca v & Env. En O; O 6 P•� a) .9 y P, '� 0 •w E Ncn a y ,0 O o t7 0 ' .fl C .L1 176 o C) a � N O b. cn as • IC O O o ti 0 b .d Y O C- y 0 N cn 0 O cn ctl • 0 g .CO o. O O 4. I- 0 'O II O o x x O O 8 U U U 10 El y 6 on o g O 5 9 ti .CC 1-5 > o a U O 65 QJ U O O b o y 11 N0 . w. O T ti o 0 o .9 czz '56 ¢ W as 0 ¢¢ LEE Ila1 C, II'i N w O cal N FORM APCI)-205 ' uid Loadin V C) Q M M Permit Number: Facility Equipment ID: Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information General Permit GP07 Individual Permit ❑ Action Applies To: C I- C o a) 41.4 u 4.4 7 O O N y a ❑ ❑ ❑ O "0 U U U Z SWNW Sec 5, T4N, R62W Source Location: Change company name Transfer of ownership ❑ ❑ Change process or equipment . 44 U C 7 d R .0 4. CC '0 1. y C ya 0) •y > �1 W o4. w z O a 0 C w �$d It S d°' CA CA 0 y Q• Q' a a'3 ❑❑❑❑ Mailing Address: 410 17th Street, Suite 1400 d Denver, Colorado N O N O GD O O U N Person To Contact: Jerry Dismukes Fax Number: 720-305-0802 Addl. Info. & Notes: Section 03 — General Information days/week 52 N- 0 N Normal Hours of Source Operation: Loading of condensate into tanker trucks A AAA .0 ❑ -0 .0 Q 0 0 0 0 0 ❑ ❑ ❑❑❑ z 0 z z z CI 0 CI O El < a a O 0 O 0 a) O 000 >. a) a a) Ca m C)) C 0 U 0 oa O Vf rn C) a to Ca ai 0 "0 a 0 0 Ca a° O .0 �. W .0.. O cam. O C. LA Oo'a) u O O T a' p ee 0 0 O E 'b 0 a) 0 °°Lo a�" g 10 ono O a Ca w 0 g O �a0) C .2 = y O O b a> ey O - a 0 o 84 5 is ! y y' c N y 6O ... >> .D O. dB ..O-� O ,� c C .b .b b .E 0 q O 0 c0C O Cy 4.' C)) .5 « R �. E 0 O.,i 0 Ca N. N O V 0 60 �.. U a) d cC ; .C a) O 0 A d . O el 0 ' 5 T.6, U •0 y b a c c.. 0 > y y 6 o a p 70 N yLc 0 C) 0 O 'C o Cc6 5 o E Z N e,MM 0 LL1 COy L. y NNN w c. d .VDT .C A U C E M cr c41 WU y a O; c 000 p > N L d U V1 p W" et 47 E .may C O C _ 0,, c w ' y L 3 'm E a' t '- C co W 0 S O 0 .s." y '_' a, W A `a q u a °' _ Q d - ai eo u y �° X30 0L: E w g r. O a. 0? O O e O O U v .0 airs O v0� CL O I. 0 C ! 0 • p, P. E• y a a) ..i > +d+ 3 R O > O U > U yr^ =6, 0 w et g o y C A y0 Q el 49, B. A., •p CI...,) O R on 8 0 �D O Z'J a.. >). E u i0r ,"" e A O d v0 0 w 'b o v d ^' °° y u d O O o '-' FAW'�,'O C • 0.0 0 Q °' .y. w O rI) d U 5 7 U aro 0 wo EA' U u 0 y V Ca pUp.�� O 0. p. O g tl•° grac..)dgA w° �cn Permit status: www.coloradqgov/cd 'O Ca O 0 U a) 0 U ❑ Condensate Product Loaded: CC .0 .0 C V G Ca O > L.. 0 C d a) Ca y u d 0 d 0 u i. a) F Ca O O u >, CC G u OO I. OD aa) y+ N .0 L O CY R w 'C w d 0" a 3 u o a y L 0 0. E h O CC u u � - C C>~ = s. L W a O d A O N N U a) d Y at w 7 v 0 Y h 7 Ca L. y u C 0 y E a) U 0 Y U a. r O y w H . - I Ca O This product is loaded from 0 1--1 CC) M w ac. Ca CC True Vapor Pressure: Actual Calendar Year: C 42/ch05/index.ht ://www.ena.Eov/ttnichief/a FormAPCD-208-IIydrocarbonLiquidLoadingAPEN-Ver.4-14-2014 (1).docx N w O a) 7 a CD Y oo M FORM APCD-208 .. uid Loadin drocarbon Li M 0 ti G) U - O O 0 C.> o r V O C = 'L Lr .r o Gn G7 E O • a UoL w 0 o • E ed • a 00 44 2 W ' m C C W as Q F a Permit Number: Section 05 — Stack Information (Combustion stacks must be listed here) U U CD 0 U MO ti3 b 000 3 13 -104.356054 N r Other (Describe): Width (inches) = II y U ❑ O M a0 z IC) N a U W Direction of stack outlet (check one): Section 08 — Emissions Inventory Information a PO 0 O) 0< a) x A 444.44. a .o o. O s C7 L W ' C as O. R 0 as 0 O Q Oa T. N U Condensate O hi 0< x x CO co O O O O II d C) a or O 0 U z N N N CiD C4414 O u Q C C6 .O 00 0.1 17) C O s 0 m Q O y CC CC R A R i, R O u W E. E u u w u CO CO C .= Cr1 b 444) CO C O i. aOe C E C 044) A L O CO 1=4 col O Estimation Method or Emission Factor Source AP -42 Tables 13.5-182 AP 42 Chap 5.2 AP -42 Tables 13.5-182 AP 42 Chap 5.2 AP 42 Chap 5.2 Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions Controlled (Tons/Year) 0.144 3.79 CO 9LL'0 ZI.0.0 CO O Uncontrolled (Tons/Year) V/N LL'09 V/N LC) a) e— CO O CV Actual Calendar Year Emissions5 Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor a m m o' a m m p1 To a, a E Z. a a Uncontrolled Basis CO O r CD O C000M O O T- O O O Control Efficiency (% Reduction) Identify in Section 07 Control Device Description Primary Secondary Pollutant NOx VOC CO Benzene n -Hexane a 12 C e CO L C CO o as a p 'fl 4 CO F 74 u Q p CO Supervisor, Permitting & Enviro. Eng. a C) E 5 C) u H zed to Supply Data CD-208-HydrocarbonLiquidLoadingAPEN-Ver.4-14-2014 (1).docx kO. O O N by CO0.4 u'4 z W O w U H 0 Z Z O Vi O co w°' c H ZE QO U r O a) J J Og _ m CLo Q a) m Wa) J CO Q a) �- � e4 0 n. W cL w Li. U z 0 Z 23- qE T- 005 AIRS ID Number: 113 Permit Number: U J J C a) O E O U C) C Co a`) 0 O C) C w a) a) U Company Name: (NI O N O co a) O U Q N a) C 0 U N CD z L U a) z ICi CO U - CL. 0 a) 0 C a) a) Plant Location: Jerry Dismukes Person to Contact: JDismukes@BonazaCrk.com E-mail Address: Controlled Actual Emissions Ibs/ ear 26.42 LO a0 of Uncontrolled Actual Emissions (lbs/year) 423.74 318.31 Emission Factor Source AP -42 AP -42 Emission Factor (Include Units) 0.0046 lb/1,000-gal 0.0035 lb/1,000-gal Control Equipment / Reduction (%) O) O) Chemical Abstract Service (CAS) Chemical Name Number 2,2,4-Trimethylpentaij a) c a) c O I -- 1540-84-1 M 00 U) co c) z tual Data Applies L Co a) >- O C a) a) C .C) C w C w Cr) C 4- a`) a O co a) w a 0 !A erson Legally Authorized to Supply Data O C co a) C U U) ca ca 0 a Q Co 0 a) N 0 L ca a) J C 0 L a) I..L O a) Jerry Dismukes Name of Person Legally Authorized to Supply Data (Please print) 0 N Form Revision Date: A 0 b ri= C, N Emission Source AIRS ID: [Leave blank unless APCD has alrea Permit Number: Facility Equipment ID: nested Action (check applicable request boxes) Section 02 — Re Section 01 — Administrative Information Request for NEW permit or newly reported emission source 0 .O C Change company name ❑ ❑ Change fuel or equipment Change permit limit ❑ ❑ Request to limit HAPs with a Federally enforceable limit on PTE CL ❑ ❑ ® ❑ ❑ ❑ .Q 4) c) O- Q O co C TU .?` O Cj U U c a 0 > U z U a co N Source Name: 410 1714 Street, Suite 1400 0 d c O 4) G a z` 720-305-0802 4) z E a)' c g z g z Section 03 — General Information U 3 T a r- >, C a General description of equipment and purpose O m O d '- [— rn Z y U :,C M M -M 0.= J y, - (-.4 N N .�.'. R O. .- J _ D n'} : C :a O O a) a) v v U. O « «.)� c�j En T cC C a 7. Q ,O _ - O -, U i zs".-- ','. c ca W d9 a C. Q 'O to 7 V2 C 'j a. Q = > 0 c v m 3 4E' ) .. 5 Y cSs 6 L. IHU>' O G. O a) 4D co GOt' II ,- U 4 MoQm G • 3-v. as b O m v; o U >`� E a Ux c n � 0 c o'm 4O c o c o c p hi) O F. c-1, m 0 o O -0- - .m m e L6U a`l 3 0m Z - . a - o U o > >4 a, is L -5 C. X' m o a n v o .- ,E a c H 'd.1 :.7..... c...)-¢ ,44:z Lt. QC5 d Q ment Information Section 04 — Processin 0n 4) H U C/) 5 4) w O - x Blowdowns: 8 a) O o DE❑❑❑ ❑ o v 73 r M N N et z 7 6i a 75',5 N O V off' C) L.) 0 Process Parameters: for to issuance. C' N m O O � 4) U U en 0- est Cr. 3 O � x en o ZZ cd level shall be a "not to e Form APCD-21 I Natural Gas Venting AP EN_LPGFL.doc r"-° .. fsa s � FORM APCD-211 60 M CC it z 5 Qyt M 1••I T a is C U C R, z C7 M 111 Emission Source AIRS ID: Permit Number: F- L O O C a a a a O a E a E a O O U O a a r a .t". 77) a O Ctin U 414 O U a a U N y a I U 4 c .5 v -oo v 15 .•ti ..r .n M M, 00 ' 7 aaa ¢ 7 in 7 0 U C h Do V J o x❑ C. U C NTS 0O C O U 3 L "J 5I U C 7 o O ED c � U N v � J R- O Go a C O O O w Section 07 — Control Device Information a a CaC a a a a Co) a a 473 Gz7 a E a a O a a a Estimation Method or Emission Factor Source Mass Balance ^ D N 7 Q m N R Q G .52 03 crl us us vs Mass Balance Mass Balance II Mass Balance ilss Balance L Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Annual t nvccinn free will I 4. �i t a 7 rr i n __. Requested Permitted Emissions4 Uncontrolled Controlled (Tons/Year) (Tons/Year) NO °• N r • .r C1 • u, r-, O h O O o O O• o O M C. O 539.21 Q _ Z < Z N 00 N M WI N N r") O 00 h O N Actual Calendar Year Emissions3 Uncontrolled Controlled (Tons/Year) (Tons/Year) Emission Factor Uncontrolled. Units Basis c.. V)' = 'C .C = ' VI w ' U V) y 4...4. �. VA CD co 7 n a a f---; O N O f7 N V) f7 I 45.7 I • Q o .. r so N Control Efficiency (% Reduction) V) a' V) a 95 V) a' IS) a' 95 Overall Collection Efficiency O a O H a H a Hi O Control Device Description C ' C O V) •L C_ W w W ECU I W 41 Pollutant VOC xON II I CO YI C'-) N j o C CII o X z fr. • C 'rs 'o E I y 4) d ^_ E C U a ee p a C) az A h C. + 0 O O C. O +4-+ a CE N E 0 gam . .sew G y E a on O G O E ;a A o n C.•-• O L N Fr, ea L o a z ai m •L O a p v G G y � m v u � „ o E - U a � fJ 3 U . › C : O 4 L Q U CJ CL q. ej a Z!] : o C- 0 ) •- a+ O mss'¢ U } 7 hOp v _ Form APCD-21 I Natural Gas Venting APEN LPGFL.doc N w 0 N CU cc2 C. FORM APCD-211 2 z W W U h- 0 Z z rcn D 5/ y W.°' C T) -- z a- Ci o J " J m CL ce a) Q W 2>2 m a 6D H - re 'O1 Q V` w 3 173 ooC AIRS ID Number: Permit Number: U J -J C) Q E O U C, :7- a) n. O a) c LU a) a) U N C4 c 0 CO Company Name: N O N O CO a) O C-) g N Seventy Holes CPF B-5, SWNW Sec 5, T4N, R62W Plant Location: JDismukes@BonazaCrk.com E-mail Address: Controlled Actual Emissions (Ibs/year) O ri O N Uncontrolled Actual Emissions (lbs/year) 0 CO O vi Emission Factor Source AP -42 Emission Factor (Include Units) 281.9 lb/MMscf Control Equipment / Reduction (%) 95 t Chemical Name C a) >. I Nil Chemical Abstract Service (CAS) Number r co Actual Data Applies: N/A erson Legally Authorized to Supply Data O 0) C a) a) C .C) C L13 c LU (a O) C E a) 0 U) L a) n. L! Jerry Dismukes cC C) O a. Q Co 0 a) N 0 (D C, a) J c 0 U) a) a- 0 a) F- Name of Person Legally Authorized to Supply Data (Please print) Form Revision Date: April 14, 2014 Hello