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Home My WebLink About20171731COLORADO Department of Public Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150O St PO Box 758 Greeley, CO 80632 June 1, 2017 Dear Sir or Madam: RECEIVED JUN 05 2017 WELD Y COMMISSIONERS On June 8, 2017, the Air Pollution Control Division will begin a 30 -day public notice period for Bonanza Creek Energy Operating Company LLC - Whitetail CPF. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health a Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickentooper, Governor ( Larry Wolk, MD, MSPH, Executive Director and Chief Medical Officer R.) 1/4he RLve.w CC PLCmrYl/1p), HLcPe.) C0/10`7/!-7 P JCERICH/Jrn/C K) 2017-1731 Air Pollution Control Division Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company LLC - Whitetail CPF - Weld County Notice Period Begins: June 8, 2017 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: Whitetail CPF Well Production Facility Lot 3 SEC 4 T6N R62W Weld County The proposed project or activity is as follows: Applicant proposes a new synthetic minor well production facility in the non -attainment area. This facility will have a permitted glycol dehydration unit, Condensate and Produced water tanks, loading operations, oil/gas/water separators. 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 and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 16WE1052 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: Christopher Kester 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 • �,.:.n.. Colorado Air Permitting Project Project Details Review Engineer: Package #: Received Date: Review Start Date: Section 01- Facility Information Christopher Kester 353850 9/27/2016 3/20/2017 Company Name: County AIRS ID: Plant AIRS ID: Facility Name: Physical Address/Location: Type of Facility: What industry segment? Bonanza Creek Energy Operating Company, LLC 123 9EE5 Whitetail CPF A-4 Lot 3 of Section 4, Township 6N, Range 62W, in Weld County, Colorado n & Production Wei Pad al. Gas, Production & Processing Is this facility located in a NAAQS non -attainment area? Yes If yes, for what pollutant? Carbon Monoxide (CO) [particulate Matter (PM) Weld Section 02 - Emissions Units In Permit Application Quadrant Section Township Range Ozone (NOx & VOC) AIRs Point # Emissions Source Type Equipment Name Emissions Control? Permit # Issuance # Self Cert Required? Action Engineering Remarks 001 TEGDehydrator.' DEHY-1 Yes 16WE1052 1 Yes. Permit Initial Issuance, 002 Condensate Tank .. CNDTK-01 Yes 16WE1052 1 Yes Permit Initial Issuance 003 Producedth aterTank PWT-01 Yes 16WE1052 1 Yes , Permit"itial ; Issuan> e 004 Condensate Tank SLOP -01 Yes 16WE1052 1 Yes ,-""''" Permit: Initial Issuance 005 Hydrocarbon Liquid Loading, L-01 Yes 16WE1052 ? 1 Yes Permit Initial Issuance. 006 Sep Separator Venting LPG FL Yes 16WE1052 1 Yes Permit Initial Issuance Section 03 - Description of Project This is an application fora newly proposed, synthetic minor, exploration and production facility. At the time of the application, the permit request was well in advance of the anticipated potential startup of the facility. There are no wellheads on location or contiguous with this centralized production facility. Section 04 - Public Comment Requirements Is Public Comment Required? If yes, why? eater than 25 tons per year in Non -Attainment' Area Section 05 - Ambient Air Impact Analysis Requirements Colorado Air Permitting Project Was a quantitative modeling analysis required? Na „ If yes, for what pollutants? If yes, attach a copy of Technical Services Unit modeling results summary. Section 06 - Facility -Wide Stationary Source Classification Is this stationary source a true minor? Is this stationary source a synthetic minor? If yes, indicate programs and which pollutants: Prevention of Significant Deterioration (PSD) Title V Operating Permits (OP) Non -Attainment New Source Review (NANSR) Is this stationary source a major source? If yes, explain what programs and which pollutants here: Prevention of Significant Deterioration (PSD) Title V Operating Permits (OP) Non -Attainment New Source Review (NANSR) No SO2 NOx CO VOC PM2.5 PM10 TSP HAPs ❑ ❑ O ❑ ❑ ❑ ❑ LI SO2 NOx ❑ ❑ ❑ ❑ CO VOC PM2.5 PM10 TSP HAPs ❑ ❑ ❑ ❑ ❑ ❑ ❑ ❑ ❑ El Glycol Dehydrator Emissions Inventory Section 01- Administrative Intonnatlon Facility AIRs ID: 123 County SEES Plant 001 Point Section 02 - Equipment Description Details Dehydrator Information Dehydrator Type: Make: Model: Serial Number: Design Capacity: Recirculation Pump Information Number of Pumps Pump Type Make: Model: Design/Max Recirculation Rate: Dehydrator Equipment Flash Tank Reboiler Burner Stripping Gas Dehydrator Equipment Description flash tank, and reboiler burner One (1)Triethylene glycol (TEG) natural gas dehydration unit (Make: TBD, Model: TBD, Serial Number. TBD) with a design capacity of 12 MMscf per day. This emissions unit is equipped with 2 (Make: Kimray, Model: 21015) gas driven glycol pump with a design capacity of 3.5 gallons per minute. This dehydration unit is equipped with a still vent, flash tank, and rehoiler burner. Emissions from the still vent art routed to an air-cooled condenser, and then to the Enclosed Flare. Emissions from the Emission Control Device Description: flash tank are routed directly to the closed -loop system. Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Dehydrator Still Vent and Flash Tank (if present) Requested Permit Limit Throughput = 4,3804: MMscf per year Potential to Emit (PTE) Throughput = 4,380 MMscf per year Secondary Emissions - Combustion Device(s) for Air Pollution Control Still Vent Control Condenser: Condenser emission reduction claimed: Primary control device: Primary control device operation: Secondary control device: Secondary control device operation: Still Vent Gas Heating Value: Still Vent Waste Gas Vent Rate: Flash tank Control Primary control devise: Primary control device operation: Secondary control device: Secondary control device operation: Flash Tank Gas Heating Value flash Tank Waste Gas Vent Rate: Section 04- Emissions Factors & Methodologies Dehydrator Wet Gas Processed: Still Vent Primary Control: 4,380.0 MMscf/yr Still Vent Secondary Control: 0.0 MMscf/yr Waste Gas Combusted: Still Vent Primary Control: 1.7 MMscf/yr Still Vent Secondary Control: 0.0 MMscf/yr Wet Gas Processed: Flash Tank Primary Control: 4,380.0 MMscf/yr Flash Tank Secondary Control: 0.0 MMscf/yr Waste Gas Combusted: Flash Tank Primary Control: 0.0 MMscf/yr Flash Tank Secondary Control: 0.0 MMscf/yr Thesource used.GRtGlytak a.0:to-estimate emissloie. Wet gas compositton, pressure, and temperature era hosed on a weigheda extended gas analyses collected front the Antelope 1421 facility on 9(27/2015 Themodel was based mtthe parameters below: Input Parameters Inlet Gas Pressure Inlet Gas Temperature Requested Glycol Recirculate Rate 800 psig 120 deg F 3.5: gpm STILL VENT Control Scenario Prenary Secondary Pollutant Uncontrolled (lb/hr) Controlled (Ibkir) Controlled (Ibrhr) VOC - 21.9713 1.038565:: :23:9713 nonzero ;::2.9729 0.148845.. :29729 Toluene : 4.1261 0.206305-. 4.1261 Ethylbenzene : :1.8261 0.081305: 1.6261 Xylenes ,::4.2363 0.211815:: '4.2363 n -Hexane ::0.3778 0-01869 '.:: ..0.3778 224-TMP ::0.0385 9.001925... .,0.0385 FLASH TANK Control Scenario Primary Secondary Pollutant Uncontrolled (Ibi r) Controlled (lb/hr) Controlled (Ibthr) VOC ;- 32.5541 0 32:5541 Benzene ;:0.2378 0 0.2378 Toluene ::0.2286 0 :0.2268 Ethylbenzene 0.0562 0 0.0562 Xylenes : 0.1026 0 0.1026 n -Hexane 0.77 0 :0.77 224-TMP :: 0.0804 0 f- 0.0809 Emission Factors Glycol Dehydrator Emission Factor Source Pollutant Uncontrolled Controlled (Ile/MMscf) (lb/MMscf) (Wet Gas Throughput) (Wet Gas Throughput) VOC 109.05 2.20 , Crs - - i y' jy" Benzene 6.4214 0.29729 Toluene 8.7094 0.41261 Ethylbenzens 3.3646 0.16261 xylene 8.6778 0.42363 n -Hexane 2.2956 0.03778 224 TMP 0.2388 0.00385 Pollutant Still Vent Primary Control Device Emission Factor Source Uncontrolled Uncontrolled llb/MMBtu) (lb/MMscf) Glycol Dehydrator -Emissions Inventory Section 05- Emissions Inventory Did operator request a buffer? Requested Buffer (%), Pollutant Pollutant Pollutant (Waste Heat Combusted) (Waste Gas Combusted) Still Vent Secondary Control Device Uncontrolled (Ib/MMBtu) (Waste Heat Combusted) Uncontrolled (lb/MMscf) (Waste Gas Combusted( Hash Tank Primary Control Device Uncontrolled (Ib/MM Btu( (Waste Heat Combusted) Uncontrolled (Ib/MMscf) (Waste Gas Combusted) Flash Tank Secondary Control Device Uncontrolled (Ib/MMBtu( (Waste Heat Combusted) Uncontrolled (Ib/MMsd( (Waste Gas Combusted) Emission Factor Source Emission Factor Source Emission Factor Source Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 Nov CO VOC 0.0 0.0 0.0 0.0 '0.0 0.0 0.0 0.0 0.0 0.0 0.1 0.1 0.1 0.1 0.1 0.6 0.6 0.6 0.6 0.6 238.8 238.8 4.8 238.8 4.8 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled `Controlled (lb/yr) (Ib/yr) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 IMP 14.06 19.06 0.65 14.06 0.65 28126 1302 19.07 19.07 0.90 19.07 0.90 38147 1807 7.37 7.37 0.36 7.37 0.36 14737 712 19.00 19.00 0.93 19.00 0.93 38009 1855 5.03 5.03 0.08 5.03 0.08 10055 165 0.52 0.52 0.01 0.52 0.01 1046 17 Section 06 -Re Wotan, Summary Analysis Regulation 3, Parts A, B Regulation 7, Section XVII.B,D Regulation 7, Section XVII.8.2.e Regulation 7, Section XII.H Regulation 8, Part E, MACT Subpart HH (Area) Regulation 8, Part E, MACT Subpart HH (Major) Regulation 8, Part E, MACT Subpart HHH (See regulatory applicability worksheet for detailed analysis) Source requires a permit Dehydrator is subject to Regulation 7, Section XVII, 6, D.3 The control device for this dehydrator is subject to Regulation 7, Section XVII.B.2.a Dehydrator Is subject to Regulation 7, Section 011.8 The dehy unit meets the benzene exemption and is not subject You have indicated that this facility is not subject to Major Source requirements of t You have indicated that rho facility Is not subject to MACT HHH. Section 07 - Initial and Periodic Sampling end Testing Requirements Was the extended wet gas sample used in the GlyCalc model/Process model site -specific and collected within a year of application submittal? If no, the permit will contain an "Initial Compliance" testing requirement to demonstrate compliance with emission limits Does the company request a control device efficiency greater than 95%for a flare or combustion device? WILSISTI If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 - Technical Anelyeb Notes The operator inmxily inducted condenser control as the requested control of the still vent. On 4/27/20174 contacted the operator to request compliance demonstration that would be involved with very little on -paper reductions(`05 tpy VOC).. Operator crigMalhydid: not include the flash tank emissions In the emtssloncproflle since R was controlled 100%. On 5/2/2017 the operator. profile. Since this stream is controlled 100%, this only increased this uncontrolled emission profile AIRS Point 4 001 Process 0 SCC Code 01 to Include the flash tank emissions in tone.. Pollutant PM10 PM2.5 NOx VOC CO Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP Section 09 - Inventory SCC Codine and Emissions Factors Uncontrolled Emissions Factor Control % *PIV/0i 0.0% 9DIV/O1 0.0% 0.060 109.1 0.272 6.421 8.709 3.365 8.678 2.2% 0.239 0.0% 9798.5% 0.0% 9537.0% 9526.2% 9516.7% 9511.8% 9835.4% 9838.8% Units b/MMscf b/MMsd b/MMsd b/MMsd b/MMsd b/MMsd b/MMscf b/MMscf b/MMscf b/MMscf b/MMscf Dehydrator Colorado Regul ATTAINMENT 1. Are uncont 2. Are total fa NON-ATTAINM 1. Are uncont 2. Are total fa Colorado Regul 1. Is this glycc 2. Is this glycc 3. Is the sum 4. Are actual t Section XII. MACT Ana IN 1. Is the dehyl a. b. 2. Is the dehyl 40 CFR, Part 63 Area Sourc 1. Is the dehyi Exemption: 2a. 2b. 3. Is the unit I Major Sour 1. Does the fa Small or La 2a. 2b. Small Dehv 3. 4. 40 CFR, Part 63 1 Is the facilit Small or La 2a. 2b. Small Dehy 3. 4. Colorado Regul 1. Is the dehyi 2. Is this dehy 3. Is this deh 4. Was this gl' 4a. 5. If construct Section XVI Section XVI Alternative 6. Regulatory Analysis Worksheet ation 3 Parts A and B - APEN and Permit Requirements You have indicated that source is in the Non -Attainment Area rolled actual emissions from any criteria pollutants from this individual source greater than 2 TPY (Regulation 3, Pa cility uncontrolled VOC emissions greater than 5 TPY, NOx greater than 10 TPY or CO emissions greater than 10 TF You have indicated that source is in the Non -Attainment Area ENT rolled emissions from any criteria pollutants from this individual source greater than 1 TPY (Regulation 3, Part A, 5 cility uncontrolled VOC emissions from the greater than 2 TPY, NOx greater than 5 TPY or CO emissions greater th; Source requires a permit ation 7, Section XII.H natural gas dehydrator located in the 8 -hr ozone control area or any ozone non -attainment area or attainment/r natural gas dehydrator located at an oil and gas exploration and production operation', natural gas compressor of actual uncontrolled emissions of VOC from any single dehydrator or group of dehydrators at a single stationary uncontrolled emissions of VOC from the individual glycol natural gas dehydrator equal to or greater than 1 tpy (Re IDehydrator is subject to Regulation 7, Section XII.H H — Emission Reductions from glycol natural gas dehydrators rsis drator located at an oil and natural gas production facility that meets either of the following criteria: A facility that processes, upgrades or stores hydrocarbon liquids' (63.760(a)(2)); OR A facility that processes, upgrades or stores natural gas prior to the point at which natural gas enters the natural gas transmission and storage source category or is delivered to a final end user2 (63.760(a)(3))? drator located at a facility that is a major source for HAPs? Go to MACT HH Area Source Requirement section to determine MACT HH applicability , Subpart MACT HH, Oil and Gas Production Facilities e Requirements drator a triethylene glycol (TEG) dehydration unit (63.760(b)(2))? s Is the actual annual average flowrate of natural gas to the glycol dehydration unit less than 3.001747 MMscf per c Are actual annual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere ocated inside of a UA plus offset and UC boundary area? The dehy unit meets the benzene exemption and is not subject Subpart A, General provisions per §63.764 (a) Table 2 §63.765 - Emissions Control Standards Do Not Apply §63.773 - Monitoring Standards Do Not Apply §63.774 - Recordkeeping §63.775 - Reporting Standards Do Not Apply .ce Requirements Icility have a facility -wide actual annual average natural gas throughput less than 0.65 MMscf/day AND a facility- rge Dehy Determination Is the actual annual average flowrate of natural gas to the glycol dehydration unit less than 3.001747 MMscf per c Are actual annual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere Requirements Did construction of the small glycol dehydration unit commence on or before August 23, 2011 (63.760(b)(1)(i)(B) For this small dehy, is a control device required to meet the BTEX emission limit (standard?) given by the applicabl 'You have indicated that this facility is not subject to Major Source requirements of MACT HH. Subpart A, General provisions per §63.764 (a) Table 2 §63.765 - Emissions Control Standards §63.773 - Monitoring §63.774 - Recordkeeping §63.775 - Reporting , Subpart MACT HHH, Natural Gas Transmission and Storage Facilities :y wide actual annual average natural gas throughput less than 0.9994051 MMscf/day and glycol dehydrators the c rge Deily Determination Is the actual annual average flowrate of natural gas to the glycol dehydration unit less than 9.994051 MMscf per c Are actual annual average emissions of benzene from the glycol dehydration unit process vent to the atmosphere Requirements Did construction of the small glycol dehydration unit commence on or before August 23, 2011 (63.1270(b)(2) and For this small dehy, is a control device required to meet the BTEX emission limit (standard?) given by the applicabl You have indicated that this facility is not subject to MACT HHH. Subpart A, General provisions per §63.1274 (a) Table 2 §63.1275 - Emissions Control Standards §63.1281 -Control Equipment Standards §63.1283 - Inspection and Monitoring §63.1284 - Recordkeeping §63.1285 - Reporting ation 7, Section XVII.D drator subject to an emissions control requirement under MACT HH or HHH (Regulation 7, Section XVII.B.5)? drator located at a transmission/storage facility? ydrator located at an oil and gas exploration and production operation , natural gas compressor station c /col natural gas dehydrator constructed before May 1, 2015 (Reg 7 Section XVII.D.4.b)? equal to or greater than 6 tons per year VOC or 2 tpy VOC if the dehydrator is located within 1,320 feet of a building unit or designated outside activity area (Reg 7, Section XVII.D.4.b)? ed on or after May 1, 2015, are uncontrolled actual emissions from a single glycol natural gas dehydrator equal to Dehydrator is subject to Regulation 7, Section XVII, B, D.3 II.B — General Provisions for Air Pollution Control Equipment and Prevention of Emissions II.D.3 - Emissions Reduction Provisions Emissions Control (Optional Section) Is this glycol natural gas dehydrator controlled by a back-up or alternate combustion device (i.e., not the primary The control device for this dehydrator is subject to Regulation 7, Section XVII.B.2.e Section XVII.B.2.e — Alternative emissions control equipment Disclaimer Act, its implementing regulations, and Air Quality Control Commission regulations. This document is not a rule or regulation, and the analysis it contains may not apply to a particular situation based upon the individual facts and circumstances. This document does not change or substitute for any law, regulation, or any other legally binding requirement and is not legally enforceable. In the event of any conflict between the language of this document and the language of the Clean Air Act„ its implementing regulations, and Air Quality Control Commission regulations, the language of the statute or regulation will control. The use of non -mandatory language such as "recommend," "may," "should," and "can, " is intended to describe APCD interpretations and recommendations. Mandatory terminology Yes Yes Source Requires an APEN. Go to the next question Source Requires a permit Continue - You have indicated the attainment status on the Project Summary Sheet. Continue - You have indicated the facility type on the Project Summary Sheet. Go to the next question Dehydrator is subject to Regulation 7, Section XII.H Continue - Source is subject to MACT HH requirements. You have indicated the source category on t Go to MACT HH Area source applicability section Continue - You have indicated the dehydrator type on the dehydrator inventory sheet. go to the next question The dehy unit meets the benzene exemption and is not subject Go to the next question go to question 2b The dehy unit is a large dehy and subject to control standard 63.765(b)(1)(i) or (ii) Continue - You have previously indicated this in the MACT section Continue - You have previously indicated this in the beginning of the MACT section Continue - You have previously indicated this in the Reg 7, Section XII determination Go to question 5 Source is subject he Project Summary Sheet. Condensate Storage Tank(s) Emissions Inventory Section 01- Administrative Information Facility AIRs ID: 123 County 9EE5 Plant 002 Point Section 02 - EOuipment Description Details Detailed Emissions Unit Up to Eighteen (18).500: bbl aboveground fixed roofcOndgtnate storage tanks. Description: Emission Control Device Enclosed Flares 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 = 0 Barrels (bbl) per year Actual Condensate Throughput While Emissions Controls Operating = 1;000 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 = 4.08'. scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = 0 MMBTU per year 25,385 MMBTU per year Potential to Emit (PTE) heat content of waste gas routed to combustion device = 25,385 MMBTU per year Section 04- Emissions Factors & Methodologies 4.1 Will this storage tank emit flash emissions? Pollutant MEM Pollutant Uncontrolled Controlled (Ib/bbl) (Ib/bbl) (Condensate Throughput) 0:48022' 0.00263' 0.00236 _.:0:00031 0.00073...... 0.01786__.... 0.00200 (Condensate Throughput) 0.02401 0.00013 0.00012 0.00002 0.00004 0.00089 0.00010 Control Device Uncontrolled Uncontrolled llb/MMBtu) (waste heat combusted) :,.. 0:0680'+... (Ib/bbl) 0.3100 (Condensate Throughput) 0.0008 0.0036 Emission Factor Source Emission Factor Source Section 05 - Emissions Inventory Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) VOC NOx CO 525.8 0.0 0.0 525.8 26.3 0.9 0.0 0.0 0.86 0.86 3.9 0.0 0.0 3.93 3.93 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (Ibs/year) (lbs/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 2.8777 0.0000 0.0000 2.8777 0.1439 5755.3200 287.7660 2.5862 0.0000 0.0000 2.5862 0.1293 5172.3420 258.6171 0.3343 0.0000 0.0000 0.3343 0.0167 668.6070 33.4304 0.8005 0.0000 0.0000 0.8005 0.0400 1601.0389 80.0519 19.5600 0.0000 0.0000 19.5600 0.9780 39119.9700 1955.9985 2.1938 0.0000 0.0000 2.1938 0.1097 4387,6650 219.3833 Section 06 - Regulatory Summary Analysis Regulation 3, Parts A, B You have indicated that source is in the Non -Attainment Area Regulation 7, Section XII.C, D, E, F Storage tank is subject to Regulation 7, Section XII.C-F, as provided 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, 0, 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, NIPS Subpart Kb . Storage Tank is not subject to NIPS Kb Regulation 6, Part A, NIPS Subpart 0000 Storage Tank is not subject to NIPS 0000 Regulation 8, Part E, MACT Subpart HH Storage Tank is not subject to MACF HH 18 of 34 K:\PA\2016\16 W E1052.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory (See regulatory applicability worksheet for detailed analysis) 19 of 34 K:\PA\2016\ 16WE1052.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 07 - Initial and Periodic Sampling and Testing Reouirements 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? 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 emissions 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 requirementto develop a site specific emissions factor based on gu Does the company request a control device efficiency greater than 95% for a flare or combustion device? If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 - Technical Analysis Notes The operator used Promax to estimate emissions. from this source. They used a gasanpressurized liquids -analysis from -a nearby facility. I n the promax model, the combined these two samples with a water stream at the beginning of the processto simulate the comingledwater/oil/gas streamthat would comedirectly from the well. The.pramax model then re -separated the streams and-ranthem through the rest of the processequipment at this facility. After going through a. production separator, a heater -treater, and then a WIT, the condensate stream hat about 2psig and flashes into the. storagetank. Because this model was not developed with site specific samples, site specific sampling willbe required through thepermitting action. Section 09 - Inventory SCC Coding and Emissions Factors AIRS Point # 002 Process # SCC Code 01 Uncontrolled Emissions Pollutant Factor Control % Units PM10 #REF! 0 lb/1,000 gallons condensate throughput PM2.5 #REFI 0 lb/1,000 gallons condensate throughput NOx 0.02 0 lb/1,000 gallons condensate throughput VOC 11.4 95 lb/1,000 gallons condensate throughput CO 0.09 0 lb/1,000 gallons condensate throughput Benzene 0.06 95 lb/1,000 gallons condensate throughput Toluene 0.06 95 lb/1,000 gallons condensate throughput Ethylbenzene 0.01 95 lb/1,000 gallons condensate throughput Xylene 0.02 95 lb/1,000 gallons condensate throughput n -Hexane 0.43 95 lb/1,000 gallons condensate throughput 224 TMP 0.05 95 lb/1,000 gallons condensate throughput 20 of 34 K:\PA\2016\ 16WE1052.CP1.xlsm E Regulatory Analysis Worksheet oject summary she a7, ui subject to NSVS OOOO per bility determined Os both criteria, then review RACT re Produced Water Storage Tank(s) Emissions Inventory Section 01- Administrative Information Facility AIRs ID: 123 County SEES 003 Plant Pomt Section 02- Eauioment Description Details Detailed Emissions Unit Description: Emission Control Device Description: Requested Overall VOC & HAP Control Efficiency %: Three (3);SOO bbl fixed roof above grounds produced water storage tan Enclosed flare 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 .: r produced = Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = 405,980 Barrels (bbl) per year Actual Produced Water Throughput While Emissions Controls Operating = Barrels (bbl) per year 1,405,980 Barrels (bbl) per year 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? 0 MMBTU per year 1,573 MMBTU per year 1,573 MMBTU per year Pollutant Pollutant immranom Produced Water Tank Uncontrolled Controlled (lb/bbl) (lb/bbl) (Produced Water Throughput) '_. 0.01019532 0.00000000 0.00000000 0.000001% ". 0.00000000": 0.00036279 0.00000000 (Produced Water Throughput) 0.0005098 0.0000000 0.0000000 0.0000001 0.0000000 0.0000181 0.0000000 Control Device Uncontrolled Uncontrolled (Ib/MMBtu) (Ib/bbl) (waste heat combusted) 0.0030' 0.3100::.;;, (Produced Water Throughput) 0.0000 0.0000 0.00008 0.00035 Emission Factor Source Emission Factor Source Section 05- Emissions Inventory Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) VOC PM10 PM2.5 NOx CO 7.2 0.0 0.0 7.2 0.4 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 01 0.0 0.0 0.1 0.1 0.2 0.0 0.0 0.2 0.2 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (lbs/year) (Ibs/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 00014 0.0000 0.0000 0.0014 0.0001 2.7570 0.1379 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.2550 0.0000 0.0000 0.2550 0.0128 510.0740 25.5037 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Section 06 - Regulatory Summary Analysis Regulation 3, Parts A, B Regulation 7, Section XVI I. B, C.1, C.3 Regulation 7, Section XVII.C.2 Source requires a permit Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3, a Storage tank is subject to Regulation 7, Section XVII.C.2, as provide 23 of 34 K:\PA\2016\16 W E1052.CP1.xlsm Produced Water Storage Tank(s) Emissions Inventory Regulation 6, Part A, NSPS Subpart 0000 'Storage Tank is not subject to NSPS 0000 (See regulatory applicability worksheet for detailed analysis) Section 07 - Initial and Periodic Sampling and Testing Requirements Does the company use a site specific emissions 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 P emo 14-03, Questions 5.9 and 5-12 for additional guidance on testing. Does the company request a control device efficiency greater than 95%for a flare or combustion device? If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 -Technical Analysis Note{, Operator used flash liberation analysis from State Antelope CPFO-1 collected and analyzed in April 2016 to estimate these emissions. A site specific sample will be required. The flash liberation analysis is documented in the next tab of this workbook. - - - - Section 09 • Inventory 5CC Coding and Emissions Factors AIRS Point it 003 Process It 5CC Code 01 4-04-003-15 Fixed Roof Tank, Produced Water, working+breathing+flashing losses Uncontrolled Emissions Pollutant Factor Control % Units PM10 0.00 0 lb/1,000 gallons liquid throughput PM2.5 0.00 0 lb/1,000 gallons liquid throughput NOx 0.00 0 lb/1,000 gallons liquid throughput VOC 0.2 95 lb/1,000 gallons liquid throughput CO 0.01 0 lb/1,000 gallons liquid throughput Benzene 0.00 95 lb/1,000 gallons liquid throughput Toluene 0.00 95 Ib/1,000 gallons liquid throughput Ethylbenzene 0.00 95 lb/1,000 gallons liquid throughput Xylene 0.00 95 lb/1,000 gallons liquid throughput n -Hexane 0.01 95 lb/1,000 gallons liquid throughput 224 TMP 0.00 95 lb/1,000 gallons liquid throughput 24 of 34 K:\PA\2016\ 16WE1052.CP1.xlsm 003 This is the emission factor calculation based on the produced water flash liberation analysis. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3) Ex=0*MW*Xx/C Ex = emissions of pollutant x Q = Volumetric flow rate/volume of gas processed MW = Molecular weight of gas = SG of gas MW of air Xx = mass fraction of x in gas C = molar volume of ideal gas (379 scf/Ib-mol) at 60F and 1 atm Liquid Throughput 1405980 bbl Flash Factor 0.5 sct/bbl Throughput (0) MW 0.70299 MMscf/yr 33.4842 Ib/Ib-mol 80.25 0.001926 scf/hr MMscf/d mole % MW Ibx/Ibmol mass fraction lb/hr Ib/yr tpy Helium 0.00 0.00 0.00 0.00 C02 31.28 44.01 13.764 0.41107 2.91 25531.03 12.77 N2 4.39 28.01 1.228 0.03669 0.26 2278.58 1.14 methane 29.14 16.04 4.674 0.13960 0.99 8670.29 4.34 ethane 20.25 30.07 6.089 0.18184 1.29 11294.03 5.65 propane 9.95 44.10 4.387 0.13103 0.93 8137.87 4.07 isobutane 1.08 58.12 0.630 0.01881 0.13 1168.38 0.58 n -butane 2.15 58.12 1.252 0.03740 0.27 2322.86 1.16 isopentane 0.28 72.15 0.199 0.00593 0.04 368.56 0.18 n -pentane 0.34 72.15 0.245 0.00732 0.05 454.61 0.23 cyclopentane 0.22 70.10 0.154 0.00460 0.03 285.67 0.14 n -Hexane 0.32 86.18 0.275 0.00821 0.06 510.07 0.26 cyclohexane 0.02 84.16 0.016 0.00047 0.00 29.04 0.01 Other hexanes 0.35 86.18 0.300 0.00896 0.06 556.28 0.28 heptanes 0.01 100.21 0.008 0.00023 0.00 14.50 0.01 methylcyclohexane 0.02 98.19 0.020 0.00060 0.00 36.97 0.02 224-TMP 0.00 Benzene 0.00 Toluene 0.00 Ethylbenzene 0.00 106.17 0.001 0.00004 0.00 2.76 0.00 Xylenes 0.00 C8-« Heavies 0.21 114.23 0.241 0.00719 0.05 446.86 0.22 VOC mass frao', 0.230797 Notes Mole %, MW, and mass fractions from a non site specific sample at a nearby facility. Flaring Information Equipment Description Gas Heating Value Throughput 2237 Btu/scf 1572.58863 MMBtu/yr !Overall Control 95.00% Combustion emission factor source: 0.068 IIb NOX/MMBtu Emissions Summary Table AP -42: Chapter 13.5 0.310 Ilb CO/MMBtu Total VOC (Uncontrolled) 7.17 Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 20391 lb/MMscf 1019.53 lb/MMscf 7.17 tpy 0.36 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.05 tpy 0.05 tpy AP -42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 0.24 tpy 0.24 tpy AP -42 Benzene 0.00 lb/MMscf 0.00 lb/MMscf 0 lb/yr 0 lb/yr Gas Analysis n -Hexane 725.58 Ib/MMscf 36.2789 lb/MMscf 510 lb/yr 26 lb/yr Gas Analysis Toluene 0.000 lb/MMscf 0.0000 lb/MMscf 0 lb/yr 0 Ib/yr Gas Analysis Xylenes 0.000 lb/MMscf 0.0000 lb/MMscf 0 lb/yr 0 lb/yr Gas Analysis Ethylbenzene 3.922 lb/MMscf 0.1961 lb/MMscf 3 lb/yr 0 lb/yr Gas Analysis 16WE1052.CP1.xlsm Produced Water Storage Tank Regulatory Analysis Worksheet Please note that NSPS Kb might be might be applicable for certain tanks at water management and injection facilities. If the tanks you are reviewing are at one of these facilities, please review NSPS Kb. E z O M c 0 ATTAINMENT N ni ¢ is in the Non-Attaim NON -ATTAINMENT ulation 7. Section XVII Colorado Re 0 r natural gas pro 0 `0 E O 00 8. 0 c rvj 0 0 a a 3 O a O 0 0 a 0 O 0. v O > 0 0 1.1 Source is sl lion 7, Section XVII.C,2, as provided below Storage Tanks fitted with Air Pollution Control Equipment Transmission and Distribution Standards of Performance for Crude Oil and Natural Gas Production O O O O t 40 CFR. Part 60. Sub 8 F- O NSPS OOOO +mot issions above 6 tons per year VOC on the applicability determination date, it should remain subject to NSPS OOOO per 60.53651e)(2) 0 O 0 O N m v 0 E E v v v a a, `m v v v m ¢ . c °c° a - a M d O t2 v v c v c g y C s0 m o `O 2 w£ > v E ,v. 'O C « Q d a a v o d MN C N K d O m u m J 0 3= v j `0 5 9 O N J O d C 0 o z o 2= c u N £ a` c '�° an d> 0 20 O m ` z > 0 C .u3i .5 A 7 H 0 N U q q en a M a a " , v� vl IA 1 di '= a 0 0 0 0 0 o as 3 VD lD Z3 £ J 0- 3 17, C L .0 0 C E z" C 2 Q a O 0 N O V O 00 E CI A 3 d 3 m E g QV E . .7k.E 0 k-2 g /((j{ E 0C C) 82)%I fa;2 3§�IC. \]�ik� 0 -9- k I—: 0' ®�2f m2 ca; [r {k/«i 0) $ ! \\>S z ■2 a) 00 E:R. `22/0 0§a)- )§ ((\\ 3\\/$f \\\\\- !:w`2f I]k!§; {\k\t ;/ } #a ]�e.13 76 \t\\2 2#\7) 0zu- ($§72] )){)%/ &7»®\ %? \ -/ \k3+ ` \ 2 \)\ ,T) 1-3 TOO {$/{} 2®�f®! )kr§® )\e.E Condensate Storage Tank(s) Emissions Inventory Section 01- Administrative Information 'Facility AIRs ID: 123 9EE5 004 County Plant Point Section 02 - Eauioment Description Details Detailed Emissions Unit Description: One (1)500 bbl above ground fixed: roof slop tank :fez the storage of compressor condensate dropout.'. Emission Control Device Enclosed Flare 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 = Secondary Emissions - Combustion Device(s) Heat content of waste gas= Volume of waste gas emitted per BBL of liquids produced = 617.45': scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = 0 Barrels (bbl) per year Actual Condensate Throughput While Emissions Controls Operating = Barrels (bbl) per year 535 Barrels (bbl) per year 2762.08 Btu/scf 0 MMBTU per year 912 MMBTU per year Potential to Emit )PTE) heat content of waste gas routed to combustion device = 912 MMBTU per year Section 04 - Emissions Factors & Methodologies Will this storage tank emit flash emissions? Pollutant Pollutant Uncontrolled Controlled (Ib/bbl) (Ib/bbl) (Condensate Throughput) 70.27 _.;.. 0.049 0.054 0.015 0:032 :r 0.2031 (Condensate Throughput) Control Device Uncontrolled Uncontrolled (Ib/MMBtu) (waste heat combusted) (Ib/bb0 0.0000 0:0680:':. 0,3100 (Condensate Throughput) Emission Factor Source Emission Factor Source Section 05 - Emissions Inventory Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) VOC PM10 PM2.5 NOx CO 18.8 0.0 0.0 18.8 0.9 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.031 0.031 0.1 0.0 0.0 0.141 0.141 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Requested Permit Limits Uncontrolled Controlled (lbs/year) (lbs/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 IMP 0.0132 0.0000 0.0000 0.0132 0.0007 26 1 0.0146 0.0000 0.0000 0.0146 0.0007 29 1 0.0041 0.0000 0.0000 0.0041 0.0002 8 0 0.0085 0.0000 0.0000 0.0085 0.0004 17 1 0.1082 0.0000 0.0000 0.1082 0.0054 216 11 0.0544 0.0000 0.0000 0.0544 0.0027 109 5 Section 06- Regulatory Summary Analysis Regulation 3, Parts A, B You have indicated that source is in the Non -Attainment Area Regulation 7, Section XII.C, D, E, F Storage tank is subject to Regulation 7, Section XII.C-F, as provided 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, 6, C.1 & C.3, a 28 of 34 K:\PA\2016\16W E1052.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Regulation 7, Section XVII.C.2 Regulation 6, Part A, NSPS Subpart Kb Regulation 6, Part A, NSPS Subpart OOOO Regulation 8, Part E, MACT Subpart HH (See regulatory applicability worksheet for detailed analysis) Storage tank is subject to Regulation 7, Section XVII.C.2, as provide Storage Tank is not subject to NSPS Kb Storage Tank is not subject to NSPS OOOO Storage Tank is not subject to MACT HH 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? 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 emissions 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 initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 -Technical Analysis Notes Source has not built this facility yet. While emissions factors were developed, these are not AIRS Point # Process # SCC Code 004 01 facility. Site specif: is sampling am! emissions factors must be developed, Section 09 - Inventory SCC Coding and Emissions Factors Uncontrolled Emissions Pollutant Factor Control % Units PM10 0.00 0 Ib/1,000 gallons condensate throughput PM2.5 0.00 0 lb/1,000 gallons condensate throughput NOx 2.76 0 lb/1,000 gallons condensate throughput VOC 1673.2 95 Ib/1,000 gallons condensate throughput CO 12.59 0 lb/1,000 gallons condensate throughput Benzene 1.17 95 lb/1,000 gallons condensate throughput Toluene 1.30 95 lb/1,000 gallons condensate throughput Ethylbenzene 0.36 95 lb/1,000 gallons condensate throughput Xylene 0.76 95 lb/1,000 gallons condensate throughput n -Hexane 9.63 95 lb/1,000 gallons condensate throughput 224 TMP 4.84 95 lb/1,000 gallons condensate throughput 29 of 34 K:\PA\2016\16WE1052.CP1.xlsm Supplemental Calculation for blowcase emissions (motive gas to blowdown compressor liquids) associated with 004 slop tank Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3) Ex=O' MW' Xx/C Ex = emissions of pollutant x O = Volumetric flow rateNolume of gas processed MW = Molecular weight of gas = SG of gas' MW of air Xx = mass fraction of x in gas C = molar volume of ideal gas (379 scf/Ib-mol) at 60F and 1 atm Throughput (0) MW 0.764 23.6 MMscf/yr lb/lb-mot 87.21461187 0.002093151 scf/hr MMscf/d mole % MW IbxObmol mass fraction lb/hr Ib/yr tpy Helium 0.0000 4.W26 0.000 0.000 0.00 0.00 0.00 CO2 27378 44.01 1.205 0.051 0.28 2428.89 1.21 N2 0.8525 28013 0239 0.010 0.05 481.40 0.24 methane 70.4864 16041 11.307 0.479 2.60 22792.45 11.40 ethane 122607 30.063 3.686 0.156 0.85 7430.22 3.72 propane 8.1076 44.092 3.575 0.151 0.82 7206.20 360 isobutane 0.9003 58.118 0.523 0.022 0.12 1054.76 0.53 n -butane 2.7467 58.118 1.596 0.068 0.37 3217.93 1.61 isopentane 0.5296 72.114 0.382 0.016 0.09 76988 0.38 n -pentane 0.6816 72.114 0.492 0.021 0.11 99084 0.50 oydopentane 0.0684 70.13 0.048 0.002 0.01 96.70 0.05 n -Hexane 0.1605 86.18 0.138 0.006 0.03 278.83 0.14 cydohexane 0.0646 84.16 0.054 0.002 0.01 109.60 0.05 Other hexanes 0.2134 86.18 0.184 0.008 0.04 37073 0.19 heptanas 0.0404 100.21 0.040 0.002 0.01 81.61 0.04 methylcydohexane 0.0362 98.19 0.036 0.002 0.01 71.65 0.04 224-TMP 0.0161 114.23 0.018 0.001 0.W 37.07 0.02 Benzene 0.0227 78.12 0.018 0.001 0.00 35.75 0.02 Toluene 0.0187 92.15 0.017 0.001 0.00 34.74 0.02 Ethylbenzene 0.0043 106.17 0.005 0.000 0.00 9.20 0.00 Xylenes 0.0077 106.17 0.008 0.000 0.00 1648 0.01 Coo Heavies 0.0156 186.6978846 0.029 0.001 0.01 5871 0.03 VOC mass frac 0304 Total VOC (Uncontrolled) 7.22 Notes Mole %, MW, and mass fractions from Whitetail F-4 gas analysis collected 6/9/2015. An actual site specific gas sample will be required to develop site specific emission factors. Flaring Information Equipment Description Gas Heating Value Throughput 1337 1021.468 Overall Control I 95.00% Btu/scf MMBtu/yr Combustion emission factor source: AP -42: Chapter 13.5 0.07 IIb NOX/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18901.391b/MMscf 945.07 lb/MMscf 7.22 tpy 0.36 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.03 tpy 0.03 tpy AP -42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 0.16 tpy 0.16 tpy AP -42 Benzene 46.7916/MMscf 2.34 Ib/MMscf 36 lb/yr 2 lb/yr Gas Analysis n -Hexane 364.9616/MMscf 18.25 Ib/MMscf 279 Ib/yr 14 lb/yr Gas Analysis Toluene 45.47 lb/MMscf 2.27 Ib/MMscf 35 lb/yr 2 lb/yr Gas Analysis Xylenes 21.57 lb/MMscf 1.081b/MMscf 16 Ib/yr 1 lb/yr Gas Analysis Ethylbenzene 1205 lb/MMscf 0.60 lb/MMscf 9 lb/yr 0 lb/yr Gas Analysis 0.31 IIb CO/MMBtu 16WE1052.CP1.xlsm i Condensate Tank Regulatory A re no MACT HH req hould remain subject to NSP5 OOOO per 60 per year VOC on the applicability de ia, then review RAC' req S 2 B 005 Hydrocarbon Loadout to Tanker Trucks Calculations L = 12.46*S*P*M/T (AP -42: Chapter 5.2, Equation 1) L = loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 1 AP -42 P True Vapor Pressure 2.61 psia Sales Oil Analysis M Molecular Weight o 33.45 lb/lb-mole T Liquid Temperature 524 deg. R Field Data L 0.637224 Wt fraction VOC 1.32 lb/10^3 gal 5.56E-02 lb/bbl Annual requested Throughput Annual requested VOC emissions Control: Flare Efficiency: 93.70% NCRPs 2190280 BBL/yr 91991760 gal/yr 121693 lb/yr 60.85 tpy This value is derived from a collection efficiency of 98.7% and flare control efficiency of 95%. The collection efficiency is from certified trucks per AP -42 Page 5.2-6 Component Mass Fraction oh HAP to VOC Benzene 0.0050 n -hexane 0.0724 Toluene 0.0041 Xylenes 0.0011 224 TMP 0.0055 Source: Stable Sales Oil Analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.05556 lb/bbl 60.8 tpy 3.8 tpy AP -42 Benzene 0.00028 lb/bbl 613.2 lb/yr 38.6 lb/yr AP -42 n -Hexane 0.00402 lb/bbl 8815 lb/yr 555 lb/yr AP -42 Toluene 0.00023 lb/bbl 500 lb/yr 32 lb/yr AP -42 Xylenes 0.00006 lb/bbl 134 lb/yr 8 lb/yr AP -42 224TMP 0.00030 lb/bbl 666 lb/yr 42 lb/yr AP -43 Regulatory Review Regulation 3 - APEN and Permitting Requirements Is this site considered an exploration and production location (e.g. well pad)? If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons (238 BBLs) per day of crude oil on an annual average basis? If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1 Yes No Low pressure gas from the heater treaters and vapor recovery towers controlled by enclosed flares during gas 006 compression downtime Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3) Ex = Q• MW• Xx/C Ex = emissions of pollutant x Q = Volumetric flow rate/volume of gas processed MW = Molecular weight of gas = SG of gas • MW of air Xx = mass fraction of x in gas C = molar volume of ideal gas (379 scf/Ib-mol) at 60F and 1 atm Maximum Vent Rate Throughput ID) MW 1645 scf/hr 1441 MMscf/yr 40.3 Ibfb-mol 1644.9771691 scf/hr 0.039479452 MMscf/d mole% MW Ibxfbmol m frac tion ction Rolle IbNr tpy Helium 0.00 4.0026 0.000 0.00000 0.00 0.00 0.00 CO2 2.37 44.01 1.043 0.02648 4.63 40577.06 20.29 N2 0.13 28.013 0.036 0.00092 0.16 1414.27 0.71 methane 28.15 16.041 4.516 0.11465 20.05 175664.88 87.83 ethane 20.16 30.063 6.062 0.15389 26.92 235799.59 117.90 propane 24.52 44.092 10.813 0.27449 48.01 420587.48 210.29 isobutane 3.27 58.118 1.902 0.04828 8.44 73974.00 36.99 n -butane 10.66 58.118 6.193 0.15722 27.50 240900.45 120.45 isopentane 2.05 72.114 1.476 0.03747 6.55 57413.43 28.71 n -pentane 2.62 72.114 1.892 0.04803 8.40 73589.40 36.79 cyclopentane 047 70.13 0.332 0.00843 1.47 12916.87 6.46 n -Hexane 1.15 86.18 0.991 0.02515 4.40 38529.98 19.26 cyclohexane 0.39 84.16 0.332 0.00843 1.48 12923.00 6.46 Other hexanes 2.04 86.18 1.756 0.04458 7.80 68303.14 34.15 heptanes 0.66 100.21 0.662 0.01682 2.94 25766.33 12.88 methylcyclohexane 0.30 98.19 0.292 0.00740 1.29 11338.65 5.67 224-TMP 0.09 114.23 0.104 0.00265 0.46 4062.00 2.03 Benzene 0.19 78.12 0.145 0.00369 0.65 5657.07 2.83 Toluene 0.14 92.15 0.130 0.00331 0.58 5073.28 2.54 Ethybenzene 0.02 106.17 0.017 0.00043 0.08 657.34 0.33 X`Aenes 0.04 106.17 0.040 0.00103 0.18 1572.09 0.79 C8+ Heavies 0.57 114.23 0.656 0.01666 2.91 25527 30 12.76 VOC mass frac 0.704057 Total VOC (Uncontrolled) Notes Mole %, MW, and mass fractions from weighted average of 21ow pressure gas samples at similar facilities Site specific sampling wilt be required. Flaring Information Equipment Description 'Gas Heating Value Throughput 2237 Btu/scf 32235.171 MMBtu/yr Overall Control 05.00%1 Combustion emission factor source: 0.068 lb NOX/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 74864.11 Ib/MMscf 3743.21 Ib/MMscf 539.40 tpy 27.0 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 1.096 tpy 1.096 tpy AP -42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 4.996 tpy 4.996 tpy AP -42 Benzene 392.581b/MMscf 19.631b/MMscf 5657 lb/yr 283 lb/yr Gas Analysis n -Hexane 2673.8416/MMscf 133.691816/MMscf 38530 lb/yr 5926 lb/yr Gas Analysis Toluene 352.067 1b/MMscf 17.6039 ib/MMscf 5073 lb/yr 254 lb/yr Gas Analysis xylenes 109.0971b/MMscf 5.45491b/MMscf 1572 lb/yr 79 lb/yr Gas Analysis Ethylbenzene 45.617 Ib/MMscf 2.26081b/MMscf 657 lb/yr 33 lb/yr Gas Analysis AP -42: Chapter 13.5 0.310 I lb CO/MMBtu 539.40 Regulatory Applicability AQCC Reoulation 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 LA applies to all emission sources. "No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air." - AQCC Regulation 7 Was the well newly constructed, hydraulically fractured, or recompleted on or after August 1, 2014? No This separator is not subject to Reg 7 Section XVII.G 16WE1052.CP1.xlsm Permit number: Date issued: Issued to: rol Division ltn & Environment CONSTRUCTION PERMIT 16WE1052 Facility Name: Plant AIRS ID: Physical Location: County: General Description: Issuance: 1 Bonanza Creek Energy Operating Company, LLC Whitetail CPF A-4 123/9EE5 Lot 3 of SEC 4 T6N R62W Weld County Well Production Facility Equipment or activity subject to this permit: Facility Equipment ID AIRS Point Equipment Description Emissions Control Description DEHY-1 001 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 21015 glycol pumps with a design capacity of 3.5 gallons per minute. This unit is equipped with a flash tank, reboiler and still vent. Emissions from the still vent are routed to an air-cooled condenser and then to an enclosed flare. Emissions from the flash tank are routed to the sales gas line and the fuel system as a backup. CNDTK-01 002 Eighteen (18) 500 barrel fixed roof storage vessels used to store condensate. Enclosed Flare PWT-01 003 Three (3) 500 barrel fixed roof storage vessels used to store produced water. Enclosed Flare SLOP -01 004 One (1) 500 barrel fixed roof storage vessel used to store compressor condensate dropout. Additionally, sales gas is used to push compressor dropout in the slop tank and is emitted in the process. Enclosed Flare COLORADO Air Pollution Control Division Page 1 of 17 tre Enclosed Flare apor re R -u towers Enclosed flare during VRU downtime This permit is granted subject to all rules and regulations of the Colorado Air Quality Control Commission and the Colorado Air Pollution Prevention and Control Act (C. R.S. 25-7-101 et seq), to 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. Point 006: 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 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. • The dehydrator manufacturer name, model number and serial number • The glycol circulation pump manufacturer name and model number This information shalt be included with the Notice of Startup submitted for the equipment. (Reference: Regulation Number 3, Part B, III.E.) COLORADO Air Pollution Control Division Page 2 of 17 7. EMIS zation letter issued by the Division, after rent construction permit. This construction operation of this source. 8. Emissions of air pollutants shall not exceed the following limitations. (Regulation Number 3, Part B, Section II.A.4.) ) Monthly Limits: Facility Equipment ID AIRS Point Process Pounds per Month Emission Type N0X V0C CO DEHY-1 001 --- --- 833 --- Point CNDTK-01 002 --- --- 4,468 680 Point PWT-01 003 --- --- 68 --- Point SL0P-01 004 1 - Tank Liquids --- 153 --- Point 2 - Blowcase Gas --- 68 --- L-01 005 --- --- 646 --- Point LPGFL 006 --- 187 4,587 850 Point Note: Monthly limits are based on a 31 -day month. The owner or operator shall calculate monthly emissions based on the calendar month. Facility -wide emissions of each individual hazardous air pollutant shall not exceed 1,359 pounds per month. Facility -wide emissions of total hazardous air pollutants shall not exceed 3,398 pounds per month. The facility -wide emissions limitation for hazardous air pollutants shall apply to all permitted emission units at this facility. COLORADO Mr Pollution Control Division :f+r l: Page 3 of 17 imi ilit •m ID 001 IRS :3 in roc Tons per Year VOC CO Emission Type DEHY-1 4.9 Point CNDTK-01 002 26.3 4.0 Point PWT-01 003 0.4 Point SLOP -01 004 1 - Tank Liquids 0.9 2 - Blowcase Gas 0.4 Point L-01 005 3.8 Point LPGFL 006 1.1 27.0 5.0 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. During the first twelve (12) months of operation, compliance with both the monthly and annual emission limitations is required. After the first twelve (12) months of operation, compliance with only the annual limitation is required. Compliance with the annual limits, for 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. 9. Point 001: Compliance with the emission limits in this permit shall be demonstrated by running the GRI GlyCalc model version 4.0 or higher on a monthly basis using the most recent extended wet gas analysis and recorded operational values, including: gas throughput, lean glycol recirculation rate, condenser temperature, flash tank closed loop system downtime, flash tank temperature and pressure, wet gas inlet temperature, and wet gas inlet pressure. 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. 10. The owner or operator shall operate and maintain the emission points in the table below with the emissions control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit. The owner or operator shall operate this dehydration unit so as to prevent any emissions directly to the atmosphere. (Regulation Number 3, Part B, Section III.E.) COLORADO Air Pollution Control Division Page 4 of 17 F ili y Equi e I' , AIRS Point y Co of Device Pollutants Controlled il EH Still Vent: Enclosed Flare VOC and HAP CNDTK-01 002 Enclosed Combustors VOC and HAP PWT-01 003 Enclosed Combustors VOC and HAP SLOP -01 004 Enclosed Combustors VOC and HAP L-01 005 Enclosed Combustors VOC and HAP LPGFL 006 Enclosed Combustors VOC and HAP 11. 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 Point Emissions Recycling Description Pollutants Recovered DEHY-1 001 Flash Tank: Routed to sales gas line or recycled to fuel gas system as a backup VOC and HAP PROCESS LIMITATIONS AND RECORDS 12. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Regulation Number 3, Part B, II.A.4.) Process Limits Facility Equipment ID AIRS Point Process Parameter Annual Limit Monthly Limit (31 days) DEHY-1 001 Natural Gas Throughput 4,380 MMscf 372 MMscf CNDTK-01 002 Condensate Throughput 2,190,000 barrels 186,000 barrels PWT-01 003 Produced Water Throughput 1,405,980 barrels 119,412 barrels SLOP -01 004 Condensate Throughput 535 barrels 45.5 barrels Natural Gas Throughput 0.8 MMscf 0.1 MMscf L-01 005 Condensate Throughput 2,190,000 barrels 186,000 barrels LPGFL 006 Natural Gas Throughput 14.5 MMscf 1.2 MMscf COLORADO Air Pollution Control Division Page 5 of 17 hly pr. -ss rates based on the calendar month. The by g. meter or by assuming the maximum design cf/d. thetw6) mratio pliance with both the monthly and annual throughput limitations is required. After the first twelve (12) months of operation, compliance with only the annual limitation is required. Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 13. 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 site and made available to the Division for inspection upon request. Glycol recirculation rate shall be monitored by one of the following methods: assuming maximum design pump rate, using glycol flow meter(s), or recording strokes per minute and converting to circulation rate. This maximum glycol circulation rate does not preclude compliance with the optimal glycol circulation rate (Lops) provisions under MACT HH. (Reference: Regulation Number 3, Part B, II.A.4) 14. Point 001: On a monthly basis, the owner or operator shall monitor and record operational values including: flash tank closed loop system downtime, flash tank temperature and pressure, wet gas inlet temperature and pressure. These records shall be maintained for a period of five years. 15. Point 006: Upon installation of the flow meter, the owner or operator shall continuously monitor and record the volumetric flow rate of natural gas vented from the separator(s) 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. STATE AND FEDERAL REGULATORY REQUIREMENTS 16. Point 001, 002, 003, 004, a 006: 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) 17. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 18. 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 truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 19. 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. COLORADO Air Pollution Control Division O,0,rt,Itnt s �E W.$ z..J Page 6 of 17 20. oint •1 I°`vurce l iect t• _�- lation lumber 7, Section XII.H. The operator shall Sectio II and, specifically, shall: ping, m toring, reporting and emission control rib m,•ve �,:•lyc s, as deh .rs; and • Ensure 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.) 21. Points 002 & 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) 22. Points 001, 002, 003, 004, Et 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: • All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto -igniter 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. 23. Points 002, 003, 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. 24. Points 002, 003, 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. 25. Point 001: The glycol dehydration unit covered by this permit is subject to the emission control requirements in Regulation Number 7, Section XVII.D.3. Beginning May 1, 2015, still vents and vents from any flash separator or flash tank on a glycol natural gas dehydrator located at an oil and gas exploration and production operation, natural gas compressor station, or gas -processing plant subject to control requirements pursuant to Section XVII.D.4., shall reduce uncontrolled COLORADO Air Pollution Control Division Page 7 of 17 t 95% o a rolling twelve-month basis through the use pment. 26. 'oint6: - seratocove by s permit is bject to Regulation 7, Section XVII.G. (State , 2ing of arator, 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. 27. Point 001: The glycol dehydration unit at this facility is subject to National Emissions Standards for Hazardous Air Pollutants for Source Categories from Oil and Natural Gas Production Facilities, Subpart HH. This facility shall be subject to applicable area source provisions of this regulation, as stated in 40 C.F.R Part 63, Subpart A and HH. (Regulation Number 8, Part E, Subpart A and HH) COLORADO Air Pollution Control Division Page 8 of 17 MAHH A Iic quire en rea Source -nzenmissions exemption 563.764 - General Standards §63 64 (e ) owner or erator is exempt from the requirements of aph ection " 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). §63.772(b)(2) - The determination of actual average benzene emissions from a glycol dehydration unit 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-GLYCaIc TM, Version 3.0 or higher, and the procedures presented in the associated GRI-GLYCaIc TM Technical Reference Manual. Inputs to the model shalt 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 563.7(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)(ii) - The actual average benzene emissions (in terms of benzene emissions per year) as determined in accordance with §63.772(b)(2). 28. Point 005: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. OPERATING Et MAINTENANCE REQUIREMENTS 29. Points 001, 002, 003, 004, 005, Et 006: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to the OM plan are subject to Division approval prior to implementation. (Regulation Number 3, Part B, Section III.G.7.) COLORADO Air Pollution Control Division Page 9 of 17 30. � •' '' 1 `e o er oper r s!A l complete he initial extended wet gas analysis within one hundre• and eig y •ays :I o e latter o 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 Number 3, Part B, Section III.E.) 31. Points 002, 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 within one hundred and eighty days (180) after commencement of operation or issuance of this permit, whichever comes later. 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 these emissions points. 32. Point 003: The owner or operator shall complete site specific sampling including a compositional analysis of the pre -flash pressurized produced water routed to these storage tanks. Testing shall be in accordance with the guidance contained in PS Memo 14-03 within one hundred and eighty days (180) after commencement of operation or issuance of this permit, whichever comes later. 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 these emissions points. 33. 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 34. 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 35. 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: COLORADO Air Pollution Control Division Page 10 of 17 r year, a change in actual emissions of five orted on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOr) in ozone nonattainment areas emitting less than 100 tons of VOC or NO. per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non -criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. • 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. 36. The exhaust stack(s) for the following emission point(s) shall vent emissions at a point greater than or equal to the height specified in the table below: 37. The requirements of Colorado Regulation Number 3, Part D shall apply at such time that any stationary source or modification becomes a major stationary source or major modification solely by virtue of a relaxation in any enforceable limitation that was established after August 7, 1980, on the capacity of the source or modification to otherwise emit a pollutant such as a restriction on hours of operation (Reference: Regulation Number 3, Part D, V.A.7.B). GENERAL TERMS AND CONDITIONS 38. 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. 39. 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. 40. 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, COLORADO Air Pollution Control Division Page 11 of 17 , in ordance with this information and with ator o wner or operator's agents. It is valid only for y specific y identified on the permit. 41. spe thenera pecific 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. 42. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self -certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 43. 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. 44. 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: Christopher Kester Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC ,COLORADO Air Pollution Control Division Page 12 of 17 of (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.govipacific/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. ing time for this permit. An invoice for these t holder shall pay the invoice within 30 days will result in revocation of this permit. Facility Equipment ID AIRS Point Pollutant CAS # Uncontrolled Emissions (tPY) Controlled Emissions (tPY) DEHY-1 001 Benzene 71432 14.06 0.65 Toluene 108883 19.07 0.90 Ethylbenzene 100414 7.37 0.36 Xylenes 1330207 19.00 0.93 n -Hexane 110543 5.03 0.08 2,2,4- Trimethylpentane 540841 0.52 0.01 CNDTK-01 002 Benzene 71432 2.88 0.14 Toluene 108883 2.59 0.13 Ethylbenzene 100414 0.33 0.02 Xylenes 1330207 0.80 0.04 n -Hexane 110543 19.56 0.98 2,2,4- Trimethylpentane 540841 2.19 0.11 PWT-01 003 n -Hexane 110543 0.26 0.01 SLOP -01 (Process 1) 004 n -Hexane 110543 0.11 0.01 SLOP -01 (Process 2) n -Hexane 110543 0.14 0.01 L-01 005 Benzene 71432 0.31 0.02 Toluene 108883 0.25 0.02 COLORADO Air Pollution Control Division Page 13 of 17 Toluene 108883 LPGFL 006 ,4- rimet 1pe ne B 54 1 4.41 0.28 0.33 0.02 2.83 0.14 2.54 0.13 Ethylbenzene 100414 0.33 0.02 Xylenes 1330207 0.79 0.04 n -Hexane 110543 19.26 0.96 2,2,4- Trimethylpentane 540841 2.03 0.01 Note: All non -criteria reportable pollutants in the table above with uncontrolled emission rates above 0.125 tons per year (tpy) 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 information provided in the application and the GRI GlyCalc 4.0 model. Controlled emissions are based on a flare control efficiency of 95%. 6) The emission levels contained in this permit are based on the following emission factors: Point 002: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source N0x 0.00078 0.00078 AP 42 Chapter 13.5 (Back calculated to lb/bbl) CO 0.0036 0.0036 V0C 0.48022 0.02401 Promax Simulation 71432 Benzene 0.00263 0.00013 108883 Toluene 0.00236 0.00012 100414 Ethylbenzene 0.00031 0.00002 1330207 Xylene 0.00073 0.00004 110543 n -Hexane 0.01786 0.00089 540841 2,2,4 Trimethylpentane 0.00200 0.00010 Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. Point 003: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source V0C 0.010195 0.00051 Flash Liberation Analysis 110543 n -Hexane 0.000363 0.0000181 Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. COLORADO Air Pollution Control Division Page 14 of 17 AS # '; -- ` P uta yam..•/bbl otrolled Em s ion Facto Controlled Emission Factors lb/bbl Source V0C 70.27 3.51 Promax Simulation 110543 n -Hexane 0.404 0.020 Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. Point 004 (Process 2): CAS # Pollutant Uncontrolled Emission Factors lb/MMscf Controlled Emission Factors lb/MMscf Source V0C 18901.39 945.07 Gas Analysis and Engineering Calculation 110543 n -Hexane 364.96 18.25 Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. Point 005: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source V0C 0.05556 0.00350 AP -42 Chapter 5.2 Equation 1 71432 Benzene 0.00028 0.000018 108883 Toluene 0.00023 0.000014 110543 n -Hexane 0.00402 0.000254 540841 2,2,4 Trimethylpentane 0.00030 0.000019 The uncontrolled VOC emission factor was calculated using AP -42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L = 12.46*S*P*M/T S = 1 (Submerged loading) P (true vapor pressure) = 2.61 psia M (vapor molecular weight) = 33.45 lb/lb-mot T (temperature of liquid loaded) = 524 °R The uncontrolled non -criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors by the VOC emission factor. Controlled emission factors are based on a flare efficiency of 95% and a collection efficiency of 98.7% for an overall control efficiency of 93.7%. COLORADO Air Pollution Control Division Page 15 of 17 Po P•₹i tan U <• n oiled Emi on Factor ...,.� SCF) Controlled Emission Factors (lb/MMSCF) Source NOx 152.1 152.1 CO 693.4 693.4 AP -42 Chapter 13.5 (Back calculated to lb/MMscf) VOC 74864.1 3743.2 71432 Benzene 392.4 19.6 108883 Toluene 352.1 17.6 100414 Ethylbenzene 45.6 2.3 1330207 Xylene 109.1 5.5 110543 n -Hexane 2673.8 133.7 540841 2,2,4- Trimethylpentane 281.9 14.1 Gas Analysis and Engineering Calculation Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. 7) 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. 8) This permit fulfills the requirement to hold a valid permit reflecting the glycol dehydration unit and associated control device per the Colorado Oil and Gas Conservation Commission rule 805b(2)(B) when applicable. 9) This facility is classified as follows: Applicable Requirement Status Operating Permit Synthetic Minor/Major Source of: VOC and HAP NANSR Synthetic Minor/Major Source of: VOC MACT HH Area Source Requirements: Applicable 10) 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/ COLORADO Air Pollution Control Division Page 16 of 17 60 -En Part 63: National Emission xes SubrtA - Sub ix A - rt KKKK dix I 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 Page 17 of 17 O rO� O 1.4 atss a O z 52 ci) �J 0 4-4 aJ a z 2 4, M N Emission Sourc Facility Equipment ID: Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information Request for NEW permit or newly reported emission source N N CC E ro C C A E U 00 r0 E a F 0 Off, 0 0 0. U O E 0 oD es s U ❑ ❑ Lot 3, Sec 4, T6N, R62W Source Location: CC CC 'cf C E .0 4, 4, V L 4, d 4, L w 3 0 d 0 0 Mailing Address: y O N o o H VI .5 C ,E a. .0 4, Ca aEi C) a o 0 c) 0 O 'Co U .0 0 3 u b z z v W O 'w 0 y a Q O (4 4) .- o.o> g z o 'S 'rei m"t a'>•00 a) o" ❑ 0 0 0 0 L a A Person To Contact: This unit will be equipped with a condenser but it's not being claimed Section 03 — General Information NN 5 N In .14 3 y v N N C O do e p o O G 2 0 O 0 cei 4, o C) D7 ` 0 o d 1 �x x O 0 wz C c Don't know 3 3 5 0 A A ❑ ❑ ❑ 0 0 0 z zz ❑ ❑® C 0 T d en 0 0 •E cu O J 0 0.• CC I 0 O 5 0 Q x N 0 z o CC C d do .41 rze 0 Al O c 0 Ew O a) C (1 EW 4) aD 0 7 v •5 o O\ a) .Y ed •0 0 cn N y CC /attainmaintain.html) he.state.co.us/a '0 CC a) E C 4 CC 0 C 0' z CC C v C) a) .D iu 8 a s H v, C 0 Is this unit located at a stationary source that is considered a Major Source of Hazardous Air Pollutant o ,0 co CL C bp a) Q c0 C) 0 o fir• E.. C O GOC o N .. 6 3 C) ars t > .O d o Q T 0 •b o O > 0 0 ^. O • U 0 y C CO s a 5 E. a) 0 A'00 N V1 — v. .1 N rn Cl.) M g NI NI QNi O" O\ c� .0 .� r .. C0 O T.T1 eel O O 0 rn rn 3 0 -0 CO ..r -2 '5 8 Q i •y o Q U " C O .5 0 0 a� he.state.co.us/a '0 APEN forms: h O co CO 0, he.state.co.us/a •0 Application status: h A F 0 z C) 0 Manufacturer: In Reboiler Rating: O U U a) v y W ❑ 0 E— a) W 'O h 0 0 CC ca U 0 O A E a a 0 Rump Make & Mode v2 M V a) G CC M Glycol recirculation rate (gal/min): ed V N Design Capacity: Dchy. Gas Throughput: U o 4 o Z Z ❑ ED N in •0 2 0 NN rl 00 00 •w d a` 3 4, Water Content: CO a N N 2 0. C t% z N CI cD O CD U) in ca O. CO .O ea c a 0. N 0 O a3 0 z� O. 00 C cn a a� U vii 0 O U 0 ce R. 0 0 ` 0 0. C as O O 0 Q 0 0 0� .0 .0 ENE 2 d 0 O y `° a cki •y s0. 5 II C y (C 0 -a 0o V c 3 CO U 73 1 en O `0.• U 0 L 0 Q Q Q O ERE Form APCD-202 Glycol Dehydrator APEN_JD T 0 FORM APCD-202 i H 0 C ICI 3 a 40 © V d O a3 in § .0 A a> Q o r, y o s o a 0 M 0 ' C O ate.{67 Q O i1 tJ L Ltt O 6 U .° it .a Loavl 0 O O 0 Uu Cm ri) W W a W w H A ON 2 rJ 2 3 W O E O 2_ a G a O a a Z o O CO a 2 5 a w O4 vi O O trz CV M jo o N U U O U N O (.) [e) M 0O _ZO. Z N a9 rd xz ao Q z 0 C O u. v V' > a O Q ° 00 04 V U Direction of stack outlet (check one): Other: Length (inches) = 0 00 Circular: Inner Diameter (inches) = H 0 i CS 3- 0,) O 'S; et cn yb Cr, U C 0.4 L 15 r Ol Section 08 — Emissions Inventory Information & Emission Control Information Estimation Method or Emission Factor Source AP -42 GRI-GlyCalc 4.0 AP -42 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 Mr Pollutant Addendum form to report pollutants not listed above. Permitted Actual Calendar Year Emissions Requested Emissionsons3 0 0 V __jj ,•.� o op of to o b 0 g 0 AD\ 0 0 Controlled I Uncontrolled ons/Year Tons/Year) N/A 238.82 -- d Z ‘ o \ o o' 1 rte) n 1 = oN 0 ,6 Uncontrolled (Tons/Year) Emission Factor Units g4 wn gel Le it it Et CA Uncontrolled Basis co Op c) tr) t" 0.310 6.42 — .0 3.36 coo 00 M N 1/11111 year WI a Control Efficiency (% Reduction) Identify in Section 07 Factor uocumenrauon arracneu Control Device Description Primary I Secondary X O Z U O > CO Benzene Toluene Rthvlhrnzene U X C) x W C « W 0 O v 0 a CP O t t.; O. ti)' H O U c. O 0 Y .2 C a a a) ea 4) ea w i+ 0 4 a cu 00 5 O Q O a) 0 0 C e.O., E 3 5 A o �mg O ›.+ N CO y ccoo O O ti Z N 6, 00 A 0) O 151 O u 0 w _ o in G C4 CO 4. V G L d .O G O 1% Form APCD-202 Glycol Dehydrator APEN_JD 2 v o cr w o 0 0 W ZE Qo U ^^ O J " J a O ao cc 43 QN W > m a O LLI cc 3 a U) W I- U 0 Z AIRS ID Number: Permit Number: 0 J J A C R) Cl E O 0 O C O 0 a a) C W a) 0 CO N C C O CO a) Cu z C ns 0- 0 N N O CO ai O U N a) C O U N Q' z co a) Cl) 0 J U- 0 a) .C Plant Location: JDismukes@BonazaCrk.com E-mail Address: Uncontrolled Controlled Actual Actual Emissions Emissions (Ibs/year) llbs/vearl . 1047 Emission Factor Source GRI-GlyCalc 4.0 Emission Factor (Include Units) 0.239 lb/MMscf Control Equipment / Reduction (%) in O) Chemical Name 2,2,4-Trimethylpentai Chemical Abstract Service (CAS) Number 4 co 6 ,:t - Lo Calendar Ye a v 1 O) C a) a) 0) C W C W O) C E a) a O N a) N C 9- O O) Cr) Jerry Dismukes ca 0 0. O O N 0 >. ca C) a) J C O N IT) 0- 0 a) Name of Person Legally Authorized to Supply Data (Please print) Form Revision Da O Emission Source AIRS ID: it # & AIRS ID] [Leave blank unless APCD has already assigned a p [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.] CNDTK-01 uested Action (Check applicable request boxes) Section 02 — Re 0 E 0 Ts e� d I F co E ^5❑ E o .. a a ou 0 w C aa❑ Change company name 0 Transfer of ownership ❑❑ Change process or equipment E 00 ed ❑❑ for Permit Exempt/Grandfathered source APEN Submitta APEN Submittal for update only (Please note blank APEN's will not be accepted) d . O q � p O O a7 - O oa) T a at m co oa A E 0) R. A p 0" 0 .E fl iU. ...0 a . CO O F y A C ❑ ❑ ❑ ❑ d ® o z7) 3 C) N 00 00 00 0 0 U N O U a A Section 03 — General Information O N •.r .14 0 m col DEI CO •y m ^d O 0 173 (4 12 N al a) .O p id A al 0) .0 .5 coA ® 'b U 0 0 °il 45 AI E A 0 ° p•E fiOO a) . 0 0 - CO 6) 0 0 0 OO 0.CI CO . bi v 0 O t, 0 0 C) f a c' °�,.Q I Er) 0 ¢ b al •� o bCOk�0y CO CO© t.• En U = co ❑ 0 wPa3.5 ovs w �,.o w a m AtG- W a,' CO 0'1)7'1 tiH.I O ° 0. D\ dp N r' IQ a. y, a,e iL. i a .54 eg yio 04 2 b N 6 N i ^A F. A I- 0 �0)y V '' Coved CO y0)i W a) U V a0 y w 'U" y fZ� b0 N C� U .V. e a 0 y�¢'0 tea°° a °o 0 cn 0. co a) a a) "" 'O p, i, M a^ 5 U, 3^0°4 a Av' o 0 = C top W A•o 64 a E EZ++ 0)— -. cc A a Wd � ,o -c-)w.) Ian � �pU ,ao .... •• I- � ..74 d v; ,a op, Es >, 0. av: oEl Up�o a UQ�t. aEi "wc= wUd�A • Qa y E a) A 0 ya 0 • 5 U o A Y 3 0 •� 0 0 O 0 U 6) 2.a go -6 7,4 a) C •0 U O O CO 0 0 U APEN forms: httn:// Application status: h C- E." CO O O . A o .y o 0 o w E O ti o w"0.0 A ^w 0 �, w 0 ' z-�. o N CO cn a es O O `n +•' zz� 0 DIE 8 0 0a, 0 A� o o o. .2 Al y h y a y . 5 .O .0 a O v) 0O •m v > - 0 ❑ El 8 A in r-. CO ° 00 0 U o 0 C6 0 U 0 a CO .' 0 Diz A 4,?., O 0 a o 0 0 .o O o a-) c...) co U N o ��›. o to O O 0 0 .- CO ,O O cis o) Requested Permit Limit: z z 0 0 CO 0 z 00 RVP of Sales Oil a) 0 External Floating Roof: 0 Fixed Roof: a 0 •o CO 4 w w O CO a Y au A 4.0 U CO C �. w 0 C) o y .O a)5. C A 0 0 o >c) as CO en 02 o co, y H h O4 C) o o F ou o 6 F 00 'U o C cet F 6 p. CO 0 "4 O. 0 18- 500 bbl od O A F 2 a 0 H, es pa a CO L 0 CO CO C 0 ID d 0 y w d 3 z Name of Well See Attached APEN Addendum Emission S � ger M W M Permit Number: dla Form APCD-205-Condensate-Tanks-APEN N 0 a) at FORM APCn-2(15 AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Condensate Stora Location (Datum & either Lat/Long or UTM) Source, if no combustion Section 06 —Stack 64 co O • • 8 eU v 0 0 00 OO O O ��••rr U V IG 1� U U O U 0 00 tu V o N N N v; 0 8 mV �p u v re) 0 u e O v eVq N 0 O > Q . 1V A.a 5 .140 .m o �x5 co 0 • N V d W Y 00 00 A U O O O O O II V U • C 04 .1 -CO O O CO ® V 1" d 0 O V V 0 4. O CO v • N s; Cn C.) ') a 0 cd O C4 U CO .E y 0 w C4 o 0 O U Cf A W Section 07 — Control Devic E 174 CO z Cl) A CO C) 00 C 0 O o a V 71 ca O a3 V O CA N 0 Z CO °) CO ❑ U V C, C) V U L4su cc c::: a o A 0 a a o °� E g E U 'E 0 o U E• > U Pilot burner ratine: O ion Device used for c Enclosed Flare is V O Describe An O V 0.0 V] V So 0 �t �a FI,'J ..L!' it .. I. l o g' CO U U V 0w E V W CO 0 -O a c O y gi V F,' o - 0) CO a .. CO CO d (emissions vented): c0 O O N O •C o U A O rR� 00 O a 0 ow V V 00 &P Sites Onl Information aration Technolo 00 •0. O6 y CO o a CO o V O 0 V O O .) U "O. CO o 0 3 Q, cn 0 cct CV V OO V C3 CI] CO 'V� w `a o C V �) V • CO a w a) V Cb V c cum C7 O a y V y V u C C4 V C.) O V V G7 Cq O O E O CO O U CO O C, CO 0 CO as 5 H O V C". y CO iA a O cam) V 07 AP42 Tb1 13.5-1 II Promax Model AP42 Tbl 13.5-1 Promax Model Promax Model Promax Model Promax Model 11 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 O ` N N 1 O 7 t H O \ H O 1 O O 1\ O O V= O I' O d Z 525.84 — d 'z 1 o N 1 N \ eq 0) \ o G ` ,��` ire \ o� N Actual Calendar Year Emission Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor I Units a a w .o Uncontrolled Basis \ 00 0 O , 00 1 O . ",y . O \ M © co \ NH N O O t C G V 1 0 O CC O O 1 (4 N 0 O .? a°, xOM H VOC CO Benzene V ? E° V y 6 w Xylenes V X Z 'fr V g CO C E N N C C a C c a F E ai L CO 'C v CO u V O d CO O O V .O V CO O O O CO E CO u A L a0+ V O y:. W C) y6., '- CO s W 0 V _rd 'O "rd CI A CO V _ I V a a) a c E S u y„ r V a) w o V1 E- CO V a. O ig ¢+ o 6) oE� H N 40 O o N �" N 0 CO b O .O ❑ y V 0 y d b .x a 3 '° CO �C, � o .g i--1 .� w a q o c e TC h Z ,G a) ,n o E o b ^ O O 0 1 V a 41 0 N N o Q 0 H 64 V V 5 /03 o = A cet V 'N cc QO .:l ..C. N 4>' cd W c,'", C a ,0 a) A u V CP L; Cn CL) i� O Z CCO ~ N a O CO b as O gm -2 V V 'n @'gV a oo C O eol 0 O 0 as G 0 •O N rat ❑a) O U ti CC O. aa)) V O. <d .s7 0 N 0 0 a 0 .yea a 0 O macn w dla Form APCD-205-Condensate-Tanks-APEN FORM APCD-205 E&P Storage Tank Air Pollutant Emissions Notice (APEN) Addendum Forml Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: Whitetail CPF A-4, CNDTK-01 Emissions Source AIRS ID2: 123 4 6i 002 Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well - TBD - Whitetail 11-4-9XRLNB ►4 - TBD - Whitetail 21-4-9XRLC ►� 05 -123 - 41166 Whitetail 21-4-9XRLNB A - TBD - Whitetail F21-4-9XRLC ►4 - TBD - Whitetail F-4-9XRLC ►� - TBD - Whitetail F-4-9XRLNB ►� - TBD - Whitetail K-4-9XRLNB ❑ - TBD - Whitetail Federal 31-4-9XRLNB ii - TBD - Whitetail Federal 41-4-9XRLNB ►I - TBD - Whitetail Federal P-4-9XRLNB 4 - TBD - Whitetail Federal U-4-9XRLNB ►� - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - - - ❑ - - ❑ Footnotes: ' Attach this addendum to associated APEN form when needed to report additional wells. 2 If this is a newly report source that has not been assigned an AIRS ID by the APCD, enter N/A Form APCD-212 dl a Form APCD-212-EP-StorageTank-APEN-Addendum CNDTK.docx 0 Q N 4.13 u � o N Ri T:s C.) O a it a 0 • C.) 4.0 0 04 `.V U H O W � Fi O 0 Emission Source AIRS ID: [Leave blank unless APCD has already assigned a permit # & Section 02 — Re Section 01— Administrative Information 0 0 01 0 x CD i. a+ 0 cu a. Tz' g cc 0 a . CO CO .W 76a W w) a) 4 0 DI 14 o 0 o . O Fl 3 w h W o �" a d d 0 0 0 as❑a❑❑ 0 0 zv) 3 Change company name Iu 0 Transfer of ownership ❑ ❑ Change process or equipment N 00 of o W Change permit limit N O N O CO C) 0 0 U N APEN Submittal for Permit Exempt/Grandfathered source O U C u d u u ca 0 0 z 0 00 CO .0 0 O cu u CO CO O C) CO Lo. E 0 a o 'O C7 O CO E CO Cr 0 0 V) O N 3 8zzzzz N I❑®❑®❑ ti 0 a 0 O C�� CO"u N Doom Q CO0 CO' a 0 b oNFri a) o y 'EP C 0. b 0 y CO. Icoiu o• p o ot o o c 6 o w en e W cn U en N E O I. � 6O 0 z •E cn C 0 i.. o o w w 0 w O 0 z3 V) 0 vi Up 0 2 0 en 0, uen C7 ❑. �,c A•- 0121 a A 0 Gil E b 0I alio CO p 0 L t p, p 0 .-00.:0 0 U '�, CO 0 CO a) a u ❑ ❑ g U O 0 o U 0„i rz i.. C0 .n o .0 c• •Cj 'b „o �C. co ai0 E 2 2cn C 0 r. 0 CO c•5E0„ u o o ; . H ,o '8 >, o F O2 U ? O C a CO Cd o U o ..? 0CCC8 odd 0 0 Eu oa o o ,,o N o k° W z,1 .0 1 E,, C W o c +C' y Cd C ®ou ..i".. V i•. 3 3 o Al 2 ed „O 0 b pq 0 •C 0 0 0 0 0 "C boo Cn y O. o b Cd „0 0 C o 0 a° a.o" o N o C) O t0, 0 0 a 2 E i i a .o ° 0 F" a, ° E , • 0 go C) 0 U ��Aa�� b N o '0 .k � O y pw3 3 c7 eg 0 °C4 ° 0 4. 0 a) d i. ac �� w >, O �O 0 cb u zoo u �CVrnz a� CO tC •o W CO CO g' %0 Vo No W F 0. C4. 0 O 0 u.... I. :0•.•C) 0 N Ncf)'= Acs• 000 0 15a • o b o .0fr, A: 0 „0 O. 0 W i1 ^ a+ "0 vl i, N C7y ¢ U wA i. CO it .'769 .�'. Q XI 71 cd '� w y A CO m v oC 4 Al a .. ,-: ,x E 0 0 u CO v, .4 -3, CO W 00 N 0 u u '� 0 z to cA 7 0 a di u y 7 C7 O ~G. 0 O A15 Is S gT 3 0� O >o CC) '≥ cui y LFn o Ay4-0 Q 0a'� E ° - W au E A4 3 •y aai 0 0 C E i z a0+ ^ U oo O U A A° cn ,� ",o y a° A O `0' 0 90 cn 0 ..., o ' U 0:0oCOOE$E�i,z U� 1:9°C) 7F5 oq •U 0 o &' . a o o? o p., y 0 E Ud� r M4 C". r.U•erA w acn APEN a C 'O CO 0 0 Application status: h Information x C7 C7 H a? Section 04 — Stora z Actual While Controls Operational: 76 .O 8 .0 N O 00 a O Requested Permit Limit: z CO COt o to 00 o 0 0 C co O id O C) A H Date Of First Production (Month/Year) A F Installation Date of most recent storage vessel in storage tank (Month/Year) A F Total Volume of Storage Tank (bbl) O O an 4 # of Liquid Manifold Storage Vessels in Storage Tank 0 .0 0 an ri Storage Tank ID 0 5 a O O O Name of Well See attached Addendum API Number 0 C) 00 P, OO M M FORM APCD-207 COI eet Emission Source AIRS ID: Permit Number: Lat/Long or UTM) on (Datum & eithe Stack (Source, if no combu C7 0 0 .3 00 y b N Z C, C� E N N f7 0-1 o 0 N M H Cr' OO z O y • C C)0 H to 0 cO O 0 nns 1,1 co U 5 Section 07 — Control Devic ca A 00 i •a C, cal a W a al o 0 0 CA 0 O N y °o, ) o 0.C� O U N a) C, U C) ra C Enclosed Flare U N U U U 0 Waste gas heat content: C, CC Pilot burner O z a 0 CC 0 U -45 C!1 on 0 Ir :. r1 o C o -oo N ti C C U N Cn 0 0 0 b C) co C, a O E 41) W N o. U U 04 ow > N Nal -el O•' r CC U of of the stora op system used for con C) a, O U C7 C e C, a 'C O b a C, O a •�M U d y C) 0 L � It) N 03 k d C) ° ,0 a'i 00 CA 0 h 0, C) 0 0 el 0 0 a eo N o U .y o 0 O. y F > 0/3 O C) ee O. 1) o U o o C yw O y p� 000 F. s] 6 v — O y O CC E 0 4- O U C C, w O CC E w sue. 4- CJ C, w O 4- v C) 00 Estimation Method or Emission Factor Source CDPHE Memo Promax CDPHE Memo Promax Il Promax II IIPlease use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions Controlled (Tons/Year) O o M O . k 0 Uncontrolled (Tons/Year) N/A . rt: i Y/hi 0 ,„ fJ 0 Actual Calendar Year Emission Controlled (Tons/Year) Uncontrolled (To s/Year) Emission Factor . . . a .., . a ',70- Uncontrolled Basis ., o O o O co q O t Pollutant XON U > II CO Benzene 0 O F",. C C, cu W C y —5-.'Z X kC, a•a U 4 N N 4- aCi 00 O C? b CC 0 r E t4 y V1 O CC 5 a as b +14 U -, cc cc r-i cc C) 4 - CC S a� a a 0 Pr b N Ya. iw C 6 C, w a.)74 y O CO (3ab _O O Cf tiZ C) C 0 0. O • -• a 0 0 O U a U A 0 N a O O T O U U C 0 o �1 /-r rda U ,E 03 U g N C... 0 o O0 b J ti U coi T U gw •° .on U 3 r " 0 o 00 .E O3 6 b O a s N pA 0 N W O N OO CC FORM APCD-207 E&P Storage Tank Air Pollutant Emissions Notice (APEN) Addendum Forml Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: Whitetail CPF A-4, PWT-01 Emissions Source AIRS ID2: 123 PEF5/ Ma Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well - TBD - Whitetail 11-4-9XRLNB ►� - TBD - Whitetail 21-4-9XRLC I 05 - 123 - 41166 Whitetail 21-4-9XRLNB /1 - TBD - Whitetail F21-4-9XRLC O - TBD - Whitetail F-4-9XRLC ►I - TBD - Whitetail F-4-9XRLNB O - TBD - Whitetail K-4-9XRLNB ❑ - TBD - Whitetail Federal 31-4-9XRLNB r - TBD - Whitetail Federal 41-4-9XRLNB @ - TBD - Whitetail Federal P-4-9XRLNB @ - TBD - Whitetail Federal U-4-9XRLNB /1 - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ Footnotes: 1 Attach this addendum to associated APEN form when needed to report additional wells. 2 If this is a newly report source that has not been assigned an AIRS ID by the APCD, enter N/A :1 C Form APCD-212 dl a Form APCD-212-EP-StorageTank-APEN-Addendum PWT.docx AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Condensate Stora 0 Emission Source AIRS ID: [Leave blank unless APCD has already assigned a permit # & AIRS ID] [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 ® ❑ O Change company name C O Transfer of ownership ❑ ❑ Change process or equipment Change permit limit ❑ ❑ N 00 APEN Submittal for Permit Exempt/Grandfathered source •0 .0 0 .01 a) U 0 z a 0 O as a) a) 0 as a E a W ❑ ❑ v 0 U a Nta Mailing Address: _ y b [ o z Section 03 — General Information N 0 3z CO flA I❑ Z ❑❑ H o o ifs -0 3 N In 0 et 0 i -Ob te I® r N 'W :74' 0) 0 a.+ m al cMI oD vi a ' ^o (0y0 -7'- A es 0 O1 g 00 O O Q .0 W o 17) I O 0 h o 0 io O 0 In E 0 0 i. zzo0 Cr o ❑❑0, s Normal Hours of Source Operation: 0 0 A:� 0�o u Oi o g o /\I O b4 u7 In 0 .O +O+ -oI 7`O In In In Cr /r li >" " U 0 a. w0 a� O 0 veto i0.` 4 y 0 c.:-.) C.) 0 .0.0 0 ' a.— 6 0 eel c0 p "d C irl ,o•. 00+ p cd 0 F ,-•. a) u O O '- a 'tl •co Al O 0 0 a o 0 o V o a,, 0 a c.CA o v� oU o ��: o �. Z.o 5' WW a 0 >, CO 0 0 0 ®cd c� p N 0 +' 3 Al b T ti b4 ) O o =woo. 0 ..Xa) 0 o g 0 0 H a•g y >.,a) a, g a) a) h va a) .E In 0 433al El El a) 0 w Dos 0 a y O 00 41 w >,o o 0.a �'-t� 72 CD ; t- .0 W C M q ONi Z ,0 ,0 W 5 .v O 0 � ," 0 t" O O O 7,,5'tcA .O O W G o�. p r -n ¢, O\ O °O F- 0 p r..1 t, I(. fJ ��... �'Ti yq r.N 'vim A w C 6 ao V A �."4" �; ' y �O pWy at�t.� y to -c, 7 O7,,' 'r 0 V y a a O P, 0 0 0 A, U 0 a o = w) E •° a. o 3 y U i. M E 0 a0 0 0 0 0 0 C \ a Q �� w yWp� aA�'L.p v p se i ea , 0E-=wv. C0 t c- ❑❑❑ h � QI C i. ^ O� O w i .; O U M d p Ud� v Wt«. wL -r' w Q� U 0 APEN forms: h Application sta a 0 O a C. 0 a) � 0. co 0 0 0 cat 0 O .a I aJ '1' "0 O 0 En .0a, Actual While Controls Operational: CO 2 Requested Permit Limit: as 2 6 to a o U z RVP of Sales Oil External Floating Roof: Internal Floating Roof: o® a) 0 O t a) Fixed Roof: Installation Date of most recent O.1 a) a O 0 COD o C i f%2 r 0 a H 4- 0 0,3 a 44 L 35 '0 u d 3 a) 0 O. z Name of Well dl Form APCD-205-Slop Tanks-APEN FORM A PCn-205 AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Emission Source AIRS ID: Permit Number: O ,c .5 ' bbce o e ao O td 0 Q C7 Is o o ,o . b� U0 U U O Ir N N N 0 boy Cto ) e Ir 0 et 5 A 0 O II en C • '0 0 Horizontal ❑ Down 0 Other: Length (inches) = nner Diameter (inches) = 0 O O o O o N • as O n 07 — Control Devic bo C4 cn x F ,b W O oy .0 w 0 0 E;13d W 60 0 Ij ay o o z U y O4-,i Or 6 rn 00 r c••.: 0 t •c C) U, 0 0) 't) ti n r:4 a Y 6 id j a O N r, p C'"• G •N[ y C ,S y y .p O . w N 0 y O d) O h w U 'O 0 0 ,. 3 a) w m CD O .0) 0 En 111 y U rCn O >7.I cA CG 0 rn y 1p O w N 0 a) CO O y N y I.'C ycn y CO 'O 0 cri 0) a ) Information aration Technolo Section 08 — Gas/Li L bu CO ^O G CO CO 4 I- d 0 y U, a7 U O Y b y U CO as y O CC O O O U, 0 CO 5 U 161 `41 C O U CID N Promax Model AP42 Tb1 13.5-1 Promax Model Promax Model Promax Model Promax Model Promax Model Promax Model II Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. C ....�7..� 1n ♦__n_—� -. --- - vv .1. 1 1\/A Requested Permitted Emissions Uncontrolled (Tons/Year) I Controlled (Tons/Year) 0.03 M „-I „". O 0 Ov 0 . 0 O 0 V 0 0 0 0 \ N N V/u \ M O O \ M co o 1 H O 0 \ N o co; \ N O 0.07 I Actual Calendar Year Emission Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor Units CO a lb/MMBtu I lgq/gl a a 21 Uncontrolled Basis 00 O O 97.22 H `. O N - O 0 H •O 0.032 M O O a O 0.272 Pollutant xON VOC CO Benzene Toluene o C 0 W Xylenes n -Hexane as y y 0.I .c 0 a E. v N., C C C c C C C a 2 E d CO u 7 CO ,1�•I Y d f. El W s. a., q O W u Cd A s. a? a) w a a 0 H c0 a) a) H es U a a y o e ». o .0 hi 2 0, 00 h p O 0 •N •I' S N O 'er ° 0 y i. Q a .n y 'O .S x bq V CO Q N p N .° y CC . a n y A o 0 , cn 1. CU s. 2 .5 .y E .0 tiZc cu cn c,1 Cad O Q y q 0 V O z. T ct O 0 O a) O 0 y• ef=1as b 0 o +.. •ti 0 rn 7 ad W G L., AQy2 U _ e 6) V) w N IC O z N b W O ig O .b O z O °, _ co .2 O y oi)a) y w bn 0 Q U .9 . y... 5 w -[ ,a) I O 5 a ~ L, O 7 co 0 6 0 O 6 cs T1 023 o. .2 El dl Form APCD-205-Slop Tanks-APEN N 0 04 Qi FORM APCD-2(15 O U O it 123 / ae55005 0 J O' Z 04 a w Section 02 — Requested Action (Check applicable request boxes) Section 01— Administrative Information General Permit GP07 Individual Permit El Action Applies To: Bonanza Creek Energy Operating Company, LLC Lot 3, Sec 4, T6N, R62W Source Location: O ❑ Change company name a) U b �I a) CO ate") .65 to t ti Transfer of ownership 4) w N CO CO or N O N O CO 0 0 tal U N Denver, Colorado JDismukes@bonanzacrk.com E-mail Address: Fax Number: 720-305-0802 Addl. Info. & Notes: C O 44 8 O a) 44 L v a) r. O u u days/week 52 Normal Hours of Source Operation: ti O N O C O Loading of condensate into tanker trucks a a A A A ❑ ❑ 000 O O zzz a a a trA O O o O N a gel h .14 w ad O ca a r• O • O a) 0 >. U o 0 a `n N 0 O °eo a O O O 2 O O Cl) H 0 N .O. o b 04 0 8 0 « q '� 000 u-) d a� a �� S z'„ Y d MMM W b0 I., �to� 1:1 0p o.• a, o W V a) D 0 00C an SH N w = p 0 � 6R 0 r w ' O 2 t) L z p, 'm 0 'N a wo R °� w al 55{o. 613x40 Idx 0 S L O V O 4."" O ..--,..--,O r0 a ^' Li O M {rr •� V a) •O a aGi o > 0 3 a, > 3 is o C M a O H N w' • dpi-• a a)8 de O -5 -4 A>� r �.N Od tg a u R U O 0 N 'OO p o 4-, u a. o0 O O O �' a u o .5 0 0 407 a" v,woC%� a�iU •� D. O O :+a 'O cn, .O b oU p m .r R w A U d al o a 0 a ga c p., O d. .. d O O O E •o 0 N N U w 0 0 C > O p, g !s o A. o .E R o o g 0 w u w 4) Ia— U oO NR O)) NL d Y U 2 O N This product is loaded from w u w d E .O R a R 44 R o O u 7 J R ...yi u a) wa, • Co S en a (7 CC, 0 O ea a O N 42/ch05/index.ht O 0 ? a d e4 s�o rr .. O d :JAI - E e O o d o O u Ir O 6 q C Oa. °ee? iii! a u i o u 0o�oa, u t :E. PA w..C. b Q W e ■ a Cy. O 11. VT! u w . e: .4o "G w d y e ar 0 a�. CS u w • t:44v' a�E'�o a;QE > u a .O Cl . a tiay . Y Cl Y 3 302Y1^� FORM APCD-208 FonnAPCD-208-HydrocarbonLiquidLoadingAPEN-Ver.4-14-2014 (1).docx O bI R a oo O, o O N too d C W CN O S° N aw E 5N N U U (9 O U N N O co O M 0 T CO ❑ II CO N U C •E CO C.) Inner Diameter (inches) = 48 Section 07 — Control Device Information Describe Any Other (Including VRU) VOC & HAP Control Efficiency: used for control of the loadout emissions. Combustion Devic oIo Make/Model/Serial #: Enclosed Combustors Q) Manufacturer Guaranteed: 98 O Cr) V N W O C O U CD O CD - o E V L 0 0 o o m A 00 a+ rr 3a. a) N C C. w u C) U O E u z C 0 C 0 w )al L O C 0 hal h C CO E W 00 C O V 0 0 co 0 N C yM1� O 0 0 C N N T m 0 O Ci C C 'o C O U n O O O CN z C CO 0 0 O C) C. N N 0 O 0 a C U r 0 0 .a O Ci a) C C a .0 CD C 0 .0 O .O CO E d L CC d L C 'C C 0) R u R C C L Wo L C d CO CO L w O CO E as u u a? C. 4- C C d .0 u C C O 4- r C as E C 0 0 a+ u CO W E W Actual Calendar Year Emissions Requested Permitted Estimation Emissions Method or Uncontrolled Controlled Uncontrolled Controlled Emission (Tons/Year) (Tons/Year) (Tons/Year) {Tons/Year) Factor Source AP -42 Tables 13.5-18,2 AP 42 Chap 5.2 AP -42 Tables 13.5-1&2 AP 42 Chap 5.2 AP 42 Chap 5.2 I 1 Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. You may be chareed an additional APF.N fee fnr APF.N ra-cnbrn:ate1 0.144 70 co in (O.a14 4 O 6 N/A 60.77 - N/A �c. nJAY T O T Emission Factor Uncontrolled Basis Units Ib/MMBtu lb/1,000 gal lb/MMBtu lb/1,000 gal To co 0 a co .- O .,-- CO CV O CO O CO M O O O — O O O Control Efficiency (% Reduction) Identify in Section 07' Control Device Description Secondary Primary Pollutant xON U Benzene n -Hexane O > Y V u L V L rfl O u cm E o a a E U C w C ea O C L' 0 R 0 C V � y ^C Y r+ y E a E cE 3 O O u 6 W o C ca 3 'C C a d aa)) .0 co b d 0 C 0 C ≥ O Coo C i E a ai w 0 C _ I Y 'Q oCSC - w v NW L d d u • y a CS .C ar o 1 H 7 L 'C G o° — o. V L w h as aaU y a) 0 L C d 2 a O a, o .0 o U 1 de C L c 0 C C a) o a CO i .0 W w>a CC) L Y .0 i w N O d, L 'O C C d to - C La) 0 u L Wo O) C C o w et E -. 5 O y c w m rrt _ C c 1 E T 0. W 0 CO a) C. C 0 Jerry Dismukes 0 a>> ea C N O N C a 2 z W Q W V I 0 z Z 0 Permit Number: 0 J J A Co O_ E O 0 rn Co aL) a. O rn a) w a) a) U c) N C (6 C 0 CO Company Name: a) O U n. N Whitetail CPF A-4, Lot 3, Sec 4, T6N, R62W Plant Location: JDismukes@BonazaCrk.com E-mail Address: Controlled Actual Emissions Ibs/ ear s M Uncontrolled Actual Emissions (lbs/year) Q ) lt7 s S Emission Factor Source AP -42 N V� a Q Emission Factor (Include Units) 0.0046 lb/1,000-gal 0.0035 lb/1,000-gal Confro1Equipment / Reduction (%) Lo rn Lo Chemical Name gil coo a a) a 5, s a, m E I- 4 (.4 N Toluene Chemical Abstract Service (CAS) Number 0540-84-1 co co c? co O ual Data Applies: N/A 4 - SCE a 0 nY C ca a) C (0 U U) rn C a) m C C w C w rn C E N O U) a) cp a3 Q- 0 co rson Legally Authorized to Supply Data Jerry Dismukes a) a) O 0- 0. U) O a) N O > a) rn a) J C O a) a a) H Name of Person Legally Authorized to Supply Data (Please print) ril 14. 2014 Form Revision Date: A d M N Emission Source AIRS ID: [Leave blank unless APCD has already assigned a permit # & AIRS ID] z w . a 6 E3 0) © e ,;c2 GO GO CO Cr OO ) y 0) CI) ,,0 •O LZ .d g74 O a CO co x � p 10 a o o 10 a co coo ea z U O N a V Section 01— Administrative Information 'U N 0 CO CO 0 a� a 0 co v ❑ Change company name Change fuel or equipment b 3 0 O Transfer of ownership Change permit limit VD 00 'Cr w E.* 4.) O 0) CO d L 0) L a) fm; col s O T CO O C.' a a 0 H 0•4,4 R 0. 0 - O.,-,-3 ett r g O. .tea 0 0 w o CO O0 .O• O CO G 0 U .0 c o .0 6 .y u co 0 v 0 a. 0 w ��0 CO:- •0 . a O >;' Z 0 vn 0 .. 0. 0 y x ) U O Cr a ❑ ❑ ❑ ❑ N N OO 00 O U O) 720-305-0802 Section 03 — General Information N NN 0 d 0 •O 4) CO L O y H a? s. a e V y CO 00 d a d 0 d 0 a ..0 0 15 0 U co U O a v 0 as N a V CO 10 d gt 3 L � O b � d I� E L W y v a� a 0 N 0 O 0,0 ca CO CO ft c0 U c 0 O O ti O °k H O z 0 d O a 4. O a eqi Oq Wy "J MOi y y e at 00 W • s. eon 004 A- e �v m o C U ,- 00 F A0 LO co O "00.0 LqU d o U c a o IsUoi ��A 0 00h 'I$ N M M M N N N CO CT CT VD'O'' O 0 a 0 g -0° to y C o0 O .d Op 2 F v a 0 C) Q 0 A g 3 0 •CO 0 o¢ o U ti UCO 0 0 ° b 90 to a0 0 H e w aV) APEN forms:h Application sta o O 0 O O z act g CO 0 O 00 a co O O 0 z C)a 'b z 'a3 0 ecO C) ^C Ea) Iii s -a cr 00 'Do 0 b CO O N a 0 O .O U 0 c • -O CO o 6) 3� uipment Information Section 04 — Processin y 0 U CO Jo O U 00 ki 0 C 0 t co :c a U r t ab 0 Oes O c4.7: o 4•+ 0 .C .0 h O N N COx� v 6 o .c 3c;wU as 0 co co A ❑IE❑❑❑ O 75 2 C 1 N N r. H Process Paramet oa F 5 "Cr N O 0 ti a N r, a as U 0 1 00 N n 8 Si O Vented Gas Properties: ai C) U U •`,1 a 0 0 4-4 .C ... -, LI I d3 •o 0 0 0 0 U U 0 0 O O Op .O N U U ®® Requested level shall be a "not to e d7 Form APCD-211 Natural Gas Venting APEN_LPGFL N w O FORM APCD-211 N Emission Source AIRS ID: a) Permit Number: en [— o O N en M M M ti M 00 P. C 0 00 C U O •3 U Diameter (inches) = U O O ai d ❑ t o a) •N U _v 0 o � O. o cip U bA i C O 0° L .C W iection 07 — Control Device Information P4 Low Pressure Gas F y z A .11 bD Make/Model/Serial #: Enclosed Combustors 00 a a) 0 U N M N N O Orn ›" U Q, U y 4.1 °' U O :a' O 401 U CP. 0 0 C C Y O C F > U O VRU used for control of: Make/Model: N c y a) N C O N N a) (n C 0 • 7, ai '45 C T 0 5 a) C O iU O z w H W o og b YL. 0 c c n - C 14O O C �0 b ICI H a. y U 0 U en co C En W . 0 I 04 >p, O cd C .O 0 U Q Cl.. V) Estimation Method or Emission Factor Source Mass Balance n Cn_ v? E L Mass tsaiance ) p ro Ya 0] C) 4 00 C) C) C) 0 II n -hexane r..-•LI i - -- Pleace lice the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. yr. emissions oeiow oc uic uugupua au , _ Actual Calendar Year a Emissions Emission Factor 3 Requested Permitted Emissions Uncontrolled Units Uncontrolled Controlled Uncontrolled Controlled Basis (Tons/Year) (Tons/Year) (Tons/Year) (Tons/Year) o_ J— o 111 N �- O M O f e•JQ O l o p tk, o.,. O a.: 0.068 lb/MMbtu N/A 0.310 — lb/MMbtu N/A ‘4 e4 cJ 1 O o ?i I I lb/MMbtu O H d7 Form APCD-211 Natural Gas Venting APEN_LPGFL w O VC N CC. O Z N a) egally Authorized to Supply D 1w FORM APCD-211 Permit Number: U J J a) Q 0 U C) C a) a) 0 0 0) a) C w a) a) U ca N C () C 0 m Company Name: N 0 N O co W 0 U N a) 0 0 (Ni co z I- U a) cv 0 J LL a U a) a) -CC Plant Location: JDismukes@BonazaCrk.com E-mail Address: Uncontrolled Controlled Actual Actual Emissions Emissions (Ibs/year) (Ibs/year) M .9 0 'J Emission Factor Source AP -42 Emission Factor (Include Units) 281.9 Ib/MMscf Control Equipment / Reduction (%) 95 Chemical Name VI MI C N Q >, s a) E F- 4 N N Chemical Abstract Service (CAS) Number 540-84-1 z a) 0 0 c) as 0 a) O L 0 L c� a) a) a U O C •L a) a) C .C) C w W a) C r E a 0 U) a) aa)) ca 0- 0 (B C) a) -J C 0 Cl) a) a 0 a) m C 0) (n a3 4- c) 0 0. 0 V/ 0 a) N 0 N C) a) J C 0 cn a) a 0 a) 1- Name of Person Legally Authorized to Supply Data (Please print) v 0 N L Form Revision Date: A Hello