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Home My WebLink About20141680.tiff STATE OF COLORADO John W.Hickenlooper,Governor Lany Wolk,MD,MSPH �ovco Executive Director and Chief Medical Officer N4 Dedicated to protecting and improving the health and environment of the people of Colorado *' ii �• 4300 Cherry Creek Dr.S. Laboratory Services Division •rare• Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Deparunent Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Weld County-Clerk to the Board 1150 O St PO Box 758 Greeley,CO 80632 e June 3,2014 • Dear Sir or Madam: On June 7,2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—State Seventy Holes F-8 and Pronghorn P-17, in the The Greeley Tribune.A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty(30)days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept.of Public Health&Environment APCD-SS-B 1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention:Clara Gonzales Regards, 2- - L7k3CcLicii Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure �IR 1EtiD CC PLIPIAA) Pw(c 2,C41,Sµ)Hi(to) lfi- 11-aoly 2014-1680 STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH cor cato Executive Director and Chief Medical Officer t Dedicated to protecting and improving the health and environment of the people of Colorado . x 4300 Cherry Creek Dr.S. Laboratory Services Division r len Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692.3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy Operating Company LLC—State Seventy Holes F-8 and Pronghorn P-17— Weld County Released To: The Greeley Tribune On: June3,2014 Published: June 7,2014 PUBLIC NOTICE OF A PROPOSED PROJECT OR ACTIVITY WARRANTING PUBLIC COMMENT Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company LLC Facility: State Seventy Holes F-8 and Pronghorn P-17 Two oil and gas production facilities NWNW Sec 8 T4N R62W and NWNE Sec 17 T5N R61 W Weld County The proposed project or activity is as follows: The application proposes to operate two new oil and gas production facilities. 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.I.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 14WE0008 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at www.colorado.gov/cdphe/AirPublicNotices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in'writing to the following addressee: Carissa Money Colorado Department of Pub .Health and Environment 4300 Cherry Creek Drive SOS APCD-SS-B 1 Denver,Colorado 802401$#0' cdphe.commentsapcd®9tate.co.us F DRAFT STATE OF COLORADO COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT w� AIR POLLUTION CONTROL DIVISION o "� ,� TELEPHONE:(303)692-3150 :'l! *1896' CONSTRUCTION PERMIT PERMIT NO: 1 4W E000$ Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State Seventy Holes F-8 Production Facility, located in the NWNW Section 8, Township 4N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID TL 005 Truck Condensate Loadout FUG 006 Fugitive VOC equipment leak emissions HLP Sep-1 007 One low-pressure separator controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One (1)pneumatic water transfer pump, rated at 600 scf/hr P-1 008 (Sandpiper, Model G1 F, Serial number 2076870)controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One emergency flare with a minimum combustion efficiency of FL-1 009 95%. The flare is not enclosed. The emergency flare is used during periods when the sales gas cannot be routed to the pipeline. Point 008: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario(AOS)in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et sec), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. AIRS Point 009: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be AIRS ID: 123/9BCC Page 1 of 14 • • : • ,. • 1 ealth and Environment 'r Pollution Control Division downloaded • e s u- u ul. Failure to notify the Division of startup rmitted sou a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, SoCtion III.G.1 and can result in the revocation of the permit. 2. AIRS Point 009: The tenoning information shall be provided to the Division within fifteen(15)days after comencement of operation. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference:Regulation No,3; Part B, III.E.) 3. AIRS Point 009: Wltimlin,i ne hundred and eight/ days (180) after commencement of operation, compliance(4th the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operas respdnsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No.3, Part B, III.G.2). 4. AIRS Points 005 — 00SP VOU MUST notify the Alr Pollution Control Division (the Division) no later thanSuen days after Issuance of this permit, Dv suamiaina Notice of Startuo foZto the Division. The Notice of Startup form may be downloaded online atalohe.stateco.us/ao!SQwnloadforms.html. Failure to notify the Division of startup,of Vie permitted source IS a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B. Section II1.G.1 and can result in the revocation of the permit. 5. MRS Points 005 —'00M iWithin one hundred and eighty days (180) after issuance of this permit, compliarice`,With the conditions contained in this permit shall be demonstrated to the Clivtioit It is the owner or Operator's responsibility to self-certify compliance with the coridirlis. Failure to demonstrate compliance within 180"days may result in revocation of thepermit.(Reference:Regyprtion No.3, Part B, 6. This permit shall expire if the owner or operator ofihe source for which this permit was issued: (i) does not commence consfruction/modtflcation or operation of this source within 18 months after either,the date of issuance of this construction permit or the date on which such constfuctim n or activity was scheduled to commence as set forth In the permit application associatedwith this permit; (if),;dlscontinues construction for a period of eighteen months or more; (Iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No.3, Part B, III.F.4.b: (Reference: Regulation No. 3, Part B, III.F.4.) 7. AIRS Point 007: Within nihety(90)days after issuance of this permit, the operator shall Install a flow meter to miinitor and record volumetric flowrate of natural gas vented from the low pressure seitd[or. The operator shall use the gas flow rate listed in the application for actual flow'rate until the lbw meter is Installed, not to exceed ninety(90) days after issuance of this permit 8. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) AIRS ID: 123/9BCC Page 2 of 14 olor Depa en P li ealth and Environment it Pollution Control Division 9. The operator in e ' I n le ued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 10. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO VOC CO Emission Type TL 005 11.9 Point FUG 006 9.4 Fugitive HLP Sep-1 007 -- 5.8 1.7 Point P-1 008 -- 2.2 1.3 Point FL-1 009 1.0 9.5 5.5 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant.emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 11. AIRS Point 006: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas extended analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 12. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID HLP Sep-1 007 Enclosed Flare VOC P-1 008 Enclosed Flare VOC FL-1 009 Open Flare VOC AIRS ID: 123/9BCC Page 3 of 14 II ealth and Environment r Pollution Control Division a5 13. This source sh be ' • to the following maximum processing rates as listed below. Monthly records of the **al processing rates shall be maintained by the owner or operator and made enable to the Division for inspection upon request. (Reference: Regulation 3, Part f},5,A,4) Process/Consuttlptbrt Limits Faculty awe Equipment ;rat Process Parameter Annual Limit ID TL Condensate 91,980 BBL HLP Sep-1 Gas Vented from Low •Separator 5.1 MMSCF P-1 000 ' :' Natural Gas ' 5.3 MMSCF FL-I • 009 Gas Vented from SeflNFetor 22.5 MMSCF Compliance with the annual throughput limits shell be determined on a rolling twelve (12) month total. By the and of each month a new twelve-month total is calculated based on the previous twelvemonths' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with Ste responsibility,for Division review. 14. AIRS Point 007: Upon installation of the flow meter required under Condition 7, the owner or operator shag .continuously monitor and record the volumetric flowrate of natural gas vented from isath low pressure separator using a flow meter.The flow meter shall continuously mUaai$ flowrate and record total volumetric flow vented from each separator. The owner or operator shall use monthly throughput records to demonstrate compliance with the flmjts specified in Condition 13 and to calculate emissions as described in this Permit STATE AND FEDER .pEG3il,ATORY REQUIREMENTS 15. AIRS Point 005,007,008 and 009:The permit number and AIRS ID point number(e.g. 123/4567/890) shall:be marked on the subject equipment for ease of Identification. (Reference: Ftegulationtiumber 3, Part B, III.E.)(State only enforceable) 18. Visible emissions shill i of exceed twenty percent(20%)opacity during normal operation of the source. Duringlieriods of startup, process modification, or adjustment of control equipment visible stnimAnit shall not exceed 30%opacity for more than six minutes in any sixty consicutil*fflinutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or A(1d1.B.1.c shall have no visible emissions. (Reference: Regulation No. 1,Section IIA.1.:$r4.) 17. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 18. - This source is subjectttt Regulation No. 7, Section XII.C General Provisions(State only enforceable). All ooredonsate collection, storage, processing and handling operations, regardless of size„ eh.<be designed, operated and maintained so as to minimize leakage of volatile *trio compounds to the atmosphere to the maximum extent practicable.The opera shall comply with all applicable requirements of Section XII. 19. AIRS Point 005: Tsource is located in an ozone non-attainment or attainment- maintenance area arid Is subject to the Reasonably Available Control Technology AIRS ID: 123/9BCC Page 4 of 14 Depa en P li ealth and Environment it Pollution Control Division (RACY) requirDolor I m B, II .a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 20. AIRS 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.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 20 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. AIRS 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. 22. AIRS Point 006: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection must be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: AIRS ID: 123/9BCC Page 5 of 14 ...a 3 YET j`:yti earth and Environment ' r Pollution Control Division AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, sucpi( tut repairs, repair delays, and post- repair screenings. vi. Leaks shell be repaired as soca as practicable, but no later than 15 calendar days after detection!ilettes it is technically or operationally infeasible to make the repa*'within 15 calendar days. Records documenting the rationale shag.be maintained if ft is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING+MAINTEN4,4E REQUIREMENTS 23. AIRS Points 006, 00?,008, and 009: Upon'(startup of these points, the owner or operator shall follow the most recent operating nce(O&M)plan and record keeping format approved by the Division, in tb demonstrate compliance on an ongoing basis with the requirements of this pent* ;Revisions to your OW plan are subject to Division approval prior to implementation. (Reference: Regulation No.3, Part B,Section III.G.7.) COMPLIANCE TESTING A( {SAMPLING • Initial Testina Reouiramants 24. AIRS Point 006:Within one hundred and eighty days(180)after issuance of this permit, the operator shall complete"a hard count of con*** at the source and establish the number of components Mat are operated in "hear/liquid service", light liquid service', "water/oil service" and `gas service". The opener shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 25. AIRS Point 009: Within 180 days after commencement of operation, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference:Regtitalion No. 1,Section II.A.1 &4) Periodic Jesting Rea alj inents 26. AIRS Point 006: On an"annual basis,the owner or operator shall complete an extended gas analysis of gas sariples that are representdthte of volatile organic compounds (VOC) and hazardous *pollutants (HAP).that may be released as fugitive emissions. This extended gas analysts shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit ALTERNATE OPERATING{> QENARIOS 27. AIRS Point 008: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section MA and without applying for a revision to this permit'ot obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. • AIRS ID: 123/9BCC Page 6 of 14 Depa en P li it Pollutionealthand Control DivisionEnvironment 28. AIRS PointDolor or ' tain on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 29. AIRS Point 008: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 30. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five(5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO.) in ozone nonattainment areas emitting less than 100 tons of VOC or NO. per year, a change in annual actual emissions of one (1)ton per year or more or five percent, whichever is greater, above the level reported on the last APEN;or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, . above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified;or e. No later than 30 days before the existing APEN expires. 31. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 32. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. AIRS ID: 123/9BCC Page 7 of 14 , i ealth and Environment 'r Pollution Control Division 33. If this permit been granted, then the remainder of this creifillitifils not applicable the issuance of this construction permit does not prov de lnal authority for adielly or operation of this source. Final authorization of the permit must be secured from the APCD in wilting in accordance with the provisions of 20-7 14.5(12)(a)C.R.S. and Regulation No. 3, Part B, Section III.G. Final auihoriza 1 Cannot be granted tat the operation or activity commences and has been verified byte APCD as confonnklg.in all respects with the conditions of the permit. Once self-Certification of all points het been reviewed and approved by the Division, it will provids, n documentation of final authorization. Details for obtaining final au( en to operate are In the Requirements to Self- Certify for Final Authefipidlon section of this penult. 34. This permit is issued fri'relfance upon the and completeness of information supplied by the owner ' operator and is aNt�c�led upon conduct of the activity, or construction, installation 8nd-operation of the sou nit In ac cordance with this information and with representationtMedil by the owner or 4orator or owner or operator's agents. It is valid only for the en{and operations Or activity specifically identified on the permit. I 35. Unless specifically se, the general Mkt Specific conditions contained in this permit have been v; by the APCD to be'nacessary to assure compliance with the provisions of 25-7-114.5(7)(a), C.R.S. 36. Each and every of this permit is a I part hereof and is not severable. Any challenge to dr of:a condition hereof constitute a rejection of the entire permit and upon suCh 0trumunce, this permit be deemed denied ab initio. This i. permit may be revoked,atanyitime prior to self-certification and final authorization by the Air Pollution Control MOW(APCD) on groundti ad forth in the Colorado Air Quality Control Act and of the Air Quality Control Commission (AQCC), including failure to meet any term or condition of pernit. If the Division denies a permit, conditions a permit are by the owner or operator, or the Division revokes a pthe owner or operator a source may request a hearing • before the AQCC for reviser of the Division's action, 37. Section 25-7-114.7(2Xa),"C..R.S. requires that all iicfr►ces required to file an Air Pollution Emission Notice ( must pay an annual tte lb cover the costs of inspections and administration. If a c*or activity is to be continued, the owner must notify the Division in writing fig a cancellation of the permit. Upon notification, annual fee billing will terminate. - 38. Violation of the tern*•ci a permit or of the provisions of the Colorado Air Pollution Prevention and Cottri Act or the regulations of MeAQCC may result in administrative, civil or criminal enfprsil nt actions under ltecgons 25-7-115 (enforcement), -121 (Injunctions),-122(di Al -122.1 (criminal penalties),C.R.S. By: Carissa Money Permit Engineer AIRS ID: 123/9BCC Page 8 of 14 olor Depa en P li ealth and Environment it Pollution Control Division Permit Histo Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BCC Page 9 of 14 I i earth and Environment r Pollution Control Division i Notes to Permit Holder 1) The permit holder is • to pay fees for the time for this permit.An invoice for these fees will be issued ,permit is issued.The shell pry the invoice within 30 days of receipt of the invoice.ripe to pay the invoice wilt ` 'frevocation of this permit (Reference: Regulation No. 3, Pest A,Ssolion VI.B.) 2) The production or raw,material processing limits and emission limits contained in this permit,are based on the consumptInn rates requested in the pinitit applcation. These limits may be sued upon request of the inister or operator providing % accedence of any specific emission control regulation or any alt blentair quality standard air pollution emission notice(APEN) and complete applicado tm1 must be submitted with i►. ' for a permit revision. 3) This source is subject tp.4M Common Provisions Pert II,Subpart E, Affirmative= Provision for Excess Einlations During Malfunctions. or operator shall notify the of any malfunction canton which causes a violation ,emission limit or limits stated 1s permit as soon as poplins/hot no later than noon of wgrldng day,followed by written mite to the Division addresUig poll of the criteria set II.E.1 of the Common Proololope Regulation. See: httb: .colorado.cov/cs/Sat nt C&childoaoename=C Main%2FDocument C1r% ONAddLinkView&cid=1 1&oaoename=CBONWraoper 4) The following emissions 0?non-criteria reportable air sr'e estimated based upon the , limits as indicated in This information is the operator of the Division% ' of the specific com .emitted if the sources) permitted limitations. Un Are the Comrolted a- 1 AIRS s 1,,,,„ emissions Emission Rate :, . Point Pollutant CM I (Ibfylt .4 f ,reportable? (IMyr) Benzene 71432 320 . 'r Yes 320 n-Hexane 110543 1694 , Yes 1694 005 Toluene , 108883 675 • Yes 675 Xylem* 1330207 445 ''; Yes , 445 Benzene 71432 102 ". No 102 n-Hexane 110543 525 r- Yes 525 . 006 Toluene 108883 183 .t., No 183 Ethylb�sne 100414 42 -.` No 42 Xylenes ' 1330207 116 . No t16 Benzene 71432 472£ Yes 24 007 n-Hexane ' 110543 2750 ° Yes 138 , Toluene 108883 287, Yes 14 Benzene 71432 171 No 9 a n-Hexane 110543 979 Yes 49 008 Toluene. 108883 119 No 6 Ethylbenagp 100414 16 No 1 AIRS ID: 123/9BCC Page 10 of 14 olor Depa en P li ealth and Environment it Pollution Control Division Xyl 0 2 Benzene 71432 731 Yes 37 Toluene 108883 508 Yes 25 009 Ethylbenzene 100414 69 No 3 - Xylenes 1330207 138 No 7 n-Hexane 110543 4181 Yes 209 5) The emission levels contained in this permit are based on the following emission factors: Point 005: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.259 AP-42 Benzene 0.0035 AP-42 Toluene 0.0073 AP-42 Xylenes 0.0048 AP-42 n-Hexane 0.0184 AP-42 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95)using the following values: L=12.46*S*P*M/T S=0.6(Submerged loading: dedicated normal service) P(true vapor pressure)=6.37 psia M (vapor molecular weight)=67.76 Ib/Ib-mol T(temperature of liquid loaded)=524 R The uncontrolled non-criteria reportable air pollutant (NCRP)emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 006: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 1076 417 297 Flanges 56 10 12 Open-ended Lines 34 3 1 Pump Seals 4 0 1 Valves 153 57 35 Other* 74 10 12 VOC Content(wt. 0.2789 1.0 0.9968 1.0 fraction) Benzene Content(wt. 0.00054 0.0134 0.0012 fraction) Toluene Content(wt. 0.00037 0.0283 0.0003 fraction) Ethylbenzene(wt. 0.00005 0.0066 0.0001 fraction) AIRS ID: 123/9BCC Page 11 of 14 m and Environment Pollution Control Division Xy/enes Content( 0187 0.0001 fraction) n-hexane Content(wt. 0.00308 0.0712 0.0001 fraction) 141) 'Other equipment type Includes compressors, pressure relief valves, relief valves, diaphragms, drains,dump arms,hatches,instrument meters,polish rods and.vents TOC Emission Factors(kg/hr-componenty Component Gas Service Heavy Oil Ught Oil Water/Service l Connectors 2.11E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2,0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4;5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7,5E-03 1.4E-02 Source: EPA-453/R95-017 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts,multiplied by the VOC content from the most recent gas anafys's. Point 007: Weight. , Emission Emisalen Pollutant Fraction of Factors Factors- Source Gas(%) Uncontrolled Contra*, NOx 0.068 0.068 AP-42,Table 13.5-1 Ib/MMBtu CO 0S AP-42,Table 13.5-1 0.371b/MMBtu Ib/MMBtu- VOC 9 45,332 2,266.6 Engineering lb/mmscf Ib/mmscf, Calculation Benzene 0.11 92.1363 4.6068'•'!; Engineering lb/mmscf lb/mined Calculation Toluene 0.07 55.9222 2.7961- Engineering lb/mmscf lb/mmscf Calculation Ethylbenzene 0.01 6.1629 0.3081 " Engineering lb/mmscf lb/mmscf Calculation Xylenes 0.01 10.9251 0.5463' Engineering lb/mmscf lb/mmscf ,, Calculation n-hexane 0.64 536.8627 26.8431 Engineering Ib/mmscf Ib/mmscf Calculation Note: •The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 10/1/2013 of the gas vented frbm the low pressure separator tit State Seventy Holes F-J-8HNB to estimate the VOC and HAP content of the stream and a Promos model to estimate stream flow. Emission factors for CO and NOx are based on AP-42 Table 13.6-1. A HHV of 1,827 BTU/scf was used for calculations AIRS ID: 123/9BCC - Page 12 of 14 R: AePFltJl olluti Health and Environment t on Control Division Point 008: Emission Emission Factors- Factors- Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NO, 0.068 Ib/MMBTU AP-42 Table 13.5-1 CO 0.37 lb/MMBTU AP-42 Table 13.5-1 VOC 16,884 844.19 All emission factors Benzene 32.567 1.6284 are based on the Toluene 22.612 1.1306 stated consumption Ethylbenzene 3.0815 0.1541 and sales gas Xylenes 6.1629 0.3081 analysis collected 10/1/2013 from n-Hexane 186.23 9.3115 State Seventy Holes F-J-8HNB The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II,Chapter 10-Displacement Equation(10.4-3)." Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,328 BTU/scf was used for calculations. Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled NOx 0.068 0.068 AP-42,Table 13.5-1 lb/MMBtu lb/MMBtu CO 0.37 AP-42,Table 13.5-1 0.37 lb/MMBtu lb/MMBtu VOC 27 9 16,884 844.19 Engineering lb/mmscf lb/mmscf Calculation Benzene 0.05 32.567 1.6284 Engineering lb/mmscf lb/mmscf Calculation Toluene 0.04 22.612 1.1306 Engineering lb/mmscf lb/mmscf Calculation Ethylbenzene 0.005 3.0815 0.1541 Engineering lb/mmscf lb/mmscf Calculation Xylenes 0.01 6.1629 0.3081 Engineering lb/mmscf lb/mmscf Calculation n-hexane 0.31 186.23 9.3115 Engineering lb/mmscf lb/mmscf Calculation Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,328 BTU/scf was used for calculations. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: AIRS ID: 123/9BCC Page 13 of 14 dor:� " • i ee@h and Environment Pollution Control Division Applicable Requirement Operating Permit c Minor Source • NANSR *c Minor Source qk MALT HH misty Source Require - Applicable Source R .ui . W,• L,bie 8) Full text of the Tolle 4C ? on of Environment : is Code of Federal Regulations can be found at the website Nerd Ei4lpw: http://ecfr.gpoaccess.29y/ Part 60:Standardsnce for New S Sources 14'; NSPS 60.1-End SubpartA—S NSPS Part 60,Applietilites Appendix A— 1 Part 63: National 94 400 Standards for Hasa : Pollutants for Source Categories MACT 63.1-63.690, Subpart A—S MACT 63.600-63.1100 : Subpart M DOD MACT -63.120063.139. Subpart EEE P?P MACT 63.144043 , , • Subpart 000 T VYYY MACT 63.658 Subpart ZZZZ- MMMMM MACT 63.8980-End'' Subpart NNNNI4 XXXXXX 9) An Oil and Gas Indusbrponstruction Permit Self lOn Form is included with this permit packet. Please use 1MR:fo to complete the self-ce requirements as specified in the permit conditions. Further guidanon on self-certification can on our website at www.Colorado.00v/cdWke/Fflpesoermits • • AIRS ID: 123/9BCC Page 14 of 14 Division Information Engineer: Carissa Money Control Engineer: Chris Laplante Review Date: 04/24/2014 Application Date: 11/08/2013 Facility Identifiers Permit No. 14WE0008 E0008 AIRS County k 123 Weld Facility i1 9BCC Facility Type: exploration and production facility ID located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: f7 VOC r NOx r Co Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Seventy Holes F-8 Production Facility Source Location: NWNW Section 8,Township 4N, Range 62W SIC: 1311 Mailing Address 1: Bonanza Creek Energy Operating Company LLC Address Address 2: 410 17th Street,Suite 1500 /,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pvoung@bonanzacrk.com 'Section 02: Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Seventy Holes F-8 Production Facility, located in the NWNW Section 8,Township 4N,Range 62W,Weld County,Colorado. Point Name Type Control 005 TL Loadout None 006 FUG Fugitives None 007 HLP Sep-1 Separator Venting Flare 008 P-1 Pump Flare 009 FL-1 Separator Venting Flare This is an emergency flare for when pipeline n 1005 'Truck Condensate Loadout Calculations AP-42:Chapter 5.2 Equation 1 L=12.46•S•P•M/T L=loading losses in lb per 1000 gallons loaded S=Saturation Factor P=true vapor pressure of liquid loaded[psia] M=molecular weight of vapors[lb/lb-mole] T=temperature of bulk liquid loaded[deg.R] 1 degree Fahrenheit=460.67 degree Rankine Source S 0.6 Submerged loading:dedAP42 • P 6.37 psia Sales Oil Analysis documenting RVP 8.5 and AP-42 M 67.76 lb/lb-mole Sales oil analysis documenting RVP 8.5 and interpo T 523.67 deg.R EPA Tanks Met Data for Denver,CO L 6.16 lb/10^3 gal 2.59E-01 lb/bbl Annual requested Throughput 91980 BBL/yr 3863160 gal/yr Annual requested VOC emissions 23805 lb/yr 11.90 tpy Regulatory Considerations I his hid*is not condisdered a terminal(In Reg.7)because average daily throughput will be _. below 20,000 gallons at 10,584 gallons per day. This facility is not considered a bulk plant(in Reg.7)because it does not distribute gasoline. NCRPs Co111�ponent. Mass Frac. lb/yr Emission Factor lb/1000 gal Bsazeie 0.01345 320.18 0.0035lb/bbl 0.0829 n-hexane 0.07117 1694.20 0.0184 lblbbl 0.4386 Toluene 0.02834 674.63 0.0073 ib/bbl 0.1746 Xylene 0.01871 445.39 0.0048 lblbbl 0.1153 14WE0008.CP1 123/9BCC qo ... me oeoo ,] .,go . �$ on ."'.•: : x 6 �� ri 4006666 0 006 �,'�' 5;m o - < m 0oo00T . o . g, g ; gom .. . f. c1 � No 0 o00adosE d "E DE N o o m. o 6 0 6 6 0 0 o n 45 Ulo:1e .. qe - m 00000000on s' c dd ,^�dr oddd � _ eeeem .. 00.q g .S e e e o o o u o o e o 6 d d d d e e e „ o o m l ..m o o0 0 0 0 0 m.. o o m q g R ooaeeo� d tiddd 00000 o. o ; o . �.q ..m 0 0 q m o o 0 0 0 0« o e g�j $N o d g q0o0000000 ! — E ggqwTo.�� eeogmoogil g5 06 v - 0 0 d g v 0 N d. o o d 0 d .. o o d d � 5¢ oan. m .. o 00oo ..om. moo. em 'b�, g n "m .�e e '„j� d � � d .. o o m 6 e u g e e mee"� o� m otr: mna 0000 .! gg 0 0`�Q d w ,^'.�o : d 6 0 o a o d n 6 6 6 e g e $ 6 a o 0 3 ,�� om� ooeee m o " q o 0 0, e e 0 o o m m o o^j a 388888 .: o ti o 0 o - 0 0 0 d d d d e .. e o d m 466666 F g^ 000 oo 0000 oo0a2agmaa : '{ cant o .. d6d .�66 do 666 .. 000m w roceeo 1 1Z5556556565556. .5555555555 ga 0 "v "vm $ p $$4 $43 $4 ,W04 $ 4444 1 � e ,c2 1 ,IsmI F $ i _ g. _ I ; 8e i m 32 < Enmo R :, e : e,0 00002 - : A2 - - a a u 6 _ 0 goo _ ,_ r F. E n 9yC Y na cep FCq n .C4L I n n q y{ m _ _ p Al1 § IHI r C gSI Eib8co ≥ 8 _sea3ab .4LLo≥ ellu (f I t mt3Ji3 a I § ILL W o 1 i ; I 3 I II I F I ! ' F I i 4 11 i ! II I II 1 e i L II ! d • 007 One low-pressure separator controlled by two enclosed flares.Each flare has a minimum combustion efficiency of 95%. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW`Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=5G of gas•MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scffb-mol)at 60F and 1 atm Throughput(O) 5.1 MMaM/yr 584.8 scf/hr 0.44 MMscf/mo MW 31.900 lb/lb-mot 0.014 MMscf/d mole% MW Ibx/Ibmol masa fraction E lb/hr Iblyr tpy Hakim 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.57 44.01 1.131 0.035 CO2 1.7 15289 7.64 N2 Oil 28.013 0.031 0.001 N2 0.0 417 0.21 methane 40.06 16.041 6.426 0.201 methane 9.9 86862 43.43 ethane 23.7325 30.063 7.135 0.224 ethane 11.0 96441 48.22 propane 21.3662 44.082 9.4208 0.295 propane 14.5 127342 63.87 isobutane 2.1637 58.118 1.2575 0.039 isobutane 1.9 16998 8.50 n-butane 6.4499 58.118 3.7486 0.118 n-butane 5.8 50870 25.33 isopentane 1.0602 72.114 0.7646 0.024 isopentane 1.2 10335 5.17 n-pentane 1.2901 72.114 0.9303 0.029 n-pentane 1.4 12576 6.29 cyclopentane 0.0975 70.13 0.0684 0.002 cyclopentane 0.1 924 0.46 n-Hexane 0.2361 86.18 0.2035 0.0064 n-Hexane 0.3 2750 1.38 cyclobexane 0.0609 84.16 0.0513 0.002 cyclohexane 0.1 693 0.35 Other hexane. 0.4158 88.18 0.3583 0.011 Other hexanes 0.6 4844 2.42 heptanes 0.1791 100.21 0.1795 0.006 heptanes 0.3 2426 1.21 methylcyclohexane 0.044 98.19 0.0432 0.001 methylcydohexane 0.1 584 0.29 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 2 0.00 Benzene 0.0447 78.12 0.0349 0.0011 Benzene 0.1 472 0.24 Toluene 0.023 92.15 0.0212 0.0007 Toluene 0.0 286 0.14 Ethylbenzene 0.0022 106.17 0.0023 0.0001 Ethylbenzene 0.0 32 0.02 Xylenes 0.0039 106.17 0.0041 0.0001 Xylenes 0.0 56 0.03 C8+Heavies 0.0794 116.000 0.0921 0.0029 C8+Heavies 0.1 1245 0.62 VOC mass traction: 0.5386 Total VOC Emissions(Uncontrolled) 116.12 31.903 Mu Mole%and MW are based on analysis of VRU gas from Slate Seventy Holes F-J-BHNB collected 10/1/2013 Emissions are based on 8760 hours o1 operation per year. I calculated the average MW of C8+based on the average MW on the analysts for the gas at 111.9 Ib/lbmol and uncontrolled emissions at 116.09. Since minimal difference,used source's values. Flaring information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0100 Serial Number 21283 and 21284 Gas Heating Value 1827 Btu/scf Throughput 9359.721 MMBh.r/Yr VRU Information Not applicable Equipment Description Make Model Requested Control Efficiency 14WE0008.CP1 123/9BCC • 007 One tswprwws aeprabret=So0ed by two enciceed flares.Each bare lies a niobium combustion efficiency of95%. Anneal 6,Peee Time Beckon Flare IDIOMS CO ma 95.00% . coma.0dnalrbdmrebr.or.e �1P�i�¢ 0.07 b rwxMMekt I 6L�YIBABW 0.32 b 1.73 y NOX *CO Emissions Summery 0.3 ,by NOX Uncontrolled/ME 1.7, mpyy CO 116.1 - bY'1Oc Controlled 6.6 1PWVOC uneenrba0ed Caeee0e0 Total Beaten. - 412"" VS. V' a9ea 286 _ Yee -.14 • E99bentrts 32 No 2 Mend se NO 3 rt4teeane .2160 .. Yee 138 224-lW ' 2 No 0 Rogulatery . RerYri -1 Flit source is subject to the opacity requirements for%Se in Section llA5:'No owner or operator dal e0 eta some..¶1b pele0ntN4beY rloeatsd,slits on..aralbw the recomment Pudic Comment Required isgradvaa required? 124.236 IMAMS ' ' 675.99 . Idkeded .. 46331.6624 bfrAfAsof 92.1383. M*4S Toki oe 56.9222 b„64ed E3iylbnmen. 8.1829 h%*Ied Xylem 10.9251 RIPSAW nHrrrr 630.8827 bic4ed 224-TMP 0.3014 baled alcalltil NOX 124.238 addled CO • 670.99 VOC `2280.5776 Ind tone4.8088 tMMd 27961 tBMled 0.3081 baled 0.5463 Iblabcf 28.8431 MJMd 2a71.P 0.0151 lb/MOW duniti00t.cP1 123/9901: -� - . One(1)water transfer pump, rated at 600 scf/hr(Sandpiper, Model G1F, 008 Serial number 2076870). Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2076870 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled c Flare Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4- 3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas• MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Q 600 scf/hr MW 22.s Ib/Ib-mol Hours of op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy CO2 2.19 44 0.0421 CO2 1.525 13363.276 6.682 nitrogen 0.72 28 0.0088 nitrogen 0.319 2795.804 1.398 methane 71.46268 16.04 0.5006 methane 18.147 158964.376 79.482 ethane 13.0232 30.07 0.1710 ethane 6.200 54308.435 27.154 propane 8.3022 44.09 0.1598 propane 5.795 50763.252 25.382 isobutane 0.7737 58.12 0.0196 isobutane 0.712 6236.118 3.118 n-butane 2.2672 58.12 0.0575 n-butane 2.086 18273.914 9.137 isopentane 0.3668 72.15 0.0116 isopentane 0.419 3670.133 1.835 n-pentane 0.4465 72.15 0.0141 n-pentane 0.510 4467.597 2.234 cyclopentane 0.0336 72.15 0.0011 n-pentane 0.038 336.195 0.168 n-hexane 0.0819 86.18 0.0031 n-hexane 0.112 978.828 0.489 cyclohexane 0.0214 84.18 0.0008 cyclohexane 0.029 249.827 0.125 Other hexanes 0.145 86.18 0.0055 Other hexanes 0.198 1732:968 0.866 heptanes 0.065 100.21 0.0028 heptanes 0.103 903.318 0.452 methylcyclohexa 0.0163 98.19 0.0007 methylcyclohe 0.025 221.958 0.111 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 14WE0008.CP1 123/9BCC One(1)waterArensfer pump,rated at 600 sd/hr(Sandpiper,Model G1 F, 008 Serial number 2076870. Benzene o.oise 78 1 00005 Benzene 0.020 171.151 0.086 Toluene 0.0093 92.14 0.0004 Tahiti, t, t#014 118.836 0.059 Ethylbenzene 0.0011 "106:17 0.0001 Ethtlikonvene 0.002 16.196 0.008 *planes 0.0o22 106.17 0.0001 Xylener r . 0.004 32.392 0.016 C8+Heavies 0.036 116 0.0018 C8+Reale 0.066 579.131 0.290 Mass Fraction VOC: 0.2795 Total 44.377 Heating Value I 1328 BTU/sd Combusllon emission factor source: AP•4t Chapter 13.5 0.07 I lb NOXIMLIBtu 0.37 ' lb COIMMBtu tt41$4 Mole%,MW,and mass fractions from: sales gas analysis at State Seventy Holes F.l$NNB,collected 10/1/2013 Emissions Summary Uncontrolle 0.2 tpy NOX d/PTE 1.3 tpy CO 44.4, tpy VOC Controlled 2.2 tpy VOC Reportable Controlled CAS* Total(Ib/yr) 9 ° - Total 110543 978.8 Yes 49 2 540841 1.6 No 0 derizenit 71432 171.2 No ' 9 Tolue%ie 108883 118,8 NO ; 6 E-eslzhts 100414. 16.2 No ;'. 1 Xylenes 1330207 32.4 No ;- 2 Resultant Emission Fads VOC 16886.111 Ib/MMsd natural gas used Benzene 32.563 ib/MMsd natural gas used n-hexane 186.231 Ib/MMsd natural gas used Toluene 22.610 Ib/MMsd natural gas used tSaren. 3.0815 lb/MMscf natural gas used Mimes 6.1629 lb/MMscf natural gas used 224 TMP 0.301 lb/MMscf natural gas used • 14WE0008.CP1 123/98CC 009 One emergency flare with a minimum combustion efficiency of 95%. The flare is not enclosed. Equipment Description This source vents natural gas from: a well head separator when pipeline not available Emissions from this source am: routed to a flare I Natural gas venting from a well head separator when pipeline not available.Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=O'MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rateNolume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of z in gas C=molar volume of ideal gas(379 scfflb-mol)at 60F and 1 atm _ Throughput(O) 22.5 MMscf/yr 2562.8 scf/flr 1.91 MMscf/mo MW 22.900 Ib/Ib-mol 0.062 MMscfid mole% MW Ibs/Ibmol mass traction E Ib/hr Ib/yr tpy Helium 0.01 4.0026 0.000 0.000 Helium 0.0 24 0.01 CO2 2.19 44.01 0.964 0.042 CO2 6.5 57092 28.55 N2 0.72 28.013 0.202 0.009 N2 1.4 11947 5.97 methane 71.46266 16.041 11.463 0.501 methane 77.5 679028 339.51 ethane 13.0232 30.063 3.915 0.171 ethane 26.5 231914 115.96 propane 53022 44.092 3.8606 0.160 propane 24.8 218635 108.42 Isobutane 0.7737 58.118 0.4497 0.020 isobutane 3.0 28635 13.32 n-butane 22072 58.118 1.3177 0.058 n-butane 8.9 78051 39.03 isopenlene 0.3568 72.114 0.2645 0.012 isopentane 1.8 15668 7.83 rryentane 0.0465 72.114 0.3220 0.014 n-pentane 2.2 19073 9.54 cyclopentane 00336 70.13 0.0236 0.001 cyclopentane 0.2 1396 0.70 n-Hexane 0.0819 86.18 0.0706 0.00308 n-Hexane 0.5 4181 2.09 cyclohexane 0.0214 84.16 0.0180 0.001 cyclohexane 0.1 1067 0.53 Other texanes 0.145 86.18 0.1250 0.005 Other hexanes 0.8 7402 3.70 heptares 0.065 100.21 0.0651 0.003 heptanes 0.4 3858 1.93 methylcyclohexane 0.0163 98.19 0.0160 0.001 methylcyclohexane 0.1 948 0.47 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 7 0.00 Benzene 0.0158 78.12 0.0123 0.000539 Benzene 0.1 731 0.37 Toluene 0.0093 92.15 0.0086 0.000374 Toluene 0.1 508 0.25 Ethylbenzene anon 108.17 0.0012 0.000051 Ethylbenzene 0.0 89 0.03 Xylenes 0.0022 106.17 0.0023 0.000102 Xylenes 0.0 138 0.07 C8+Heavies 0.036 116.000 0.0418 0.001824 CB+Heavies 0.3 2474 1.24 V0C mass fraction: 0.2794 Total VOC Emissions(Uncontrolled) 189.52 22.943 Notes Mole%.MW.and mass fractions are based on sales gas analysis from State Seventy Holes FJ-8HNB collected 10/1/2013 Emissions are based on 8760 hours of operation per year. Typically I would calculate Ilia average MW of C8+based on the average MW on the analysis for the gas. Since Bonanza used 116 as MW and this results in minimal difference in emissions.I used 116 lbllbmol Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0007 Serial Number 21169 Gas Heating Value 1328 Btu/scf Throughput 29813.6 MMBluryr 14WE0008.CP1 123/9BCC 006 Ono emayrtay lore with a nsntmm ambrrlbn efficiency of 96%.TM Sant Isnoten closed. VRU Information•Not spplledbie Egdpnwa DaerbOon Maio- Model Required Control Vasa Anma Sass Time - Backup Ram Overall Control 95.00% Combustion emission factor source: AP-42;CSpte 13.6 0.07 I b NOXta eI,i 0.37 I lb COSUNSIu 1.01 My NOX 562 toyCO Emissions Summary 1.0 tP1'NOX Uncontrolled/PTE 5.5 tpy CO 169.5 IMy VOC Controlled 9:5 tgyVOC.. Uncontrolled Ce.Yallsd1*pl Total lap) R.patsble? Styr) Banana 731 V4 9S' Toluene 508 Vat ESyWnzans ..69 No 8. Vanes 136 N0 7 n4resne 4181 Yes - - 209 224-IMP 7 No 0 : .� A paten Applicability b the opacity requirements for flares M seam IlA.5:'No owner or operator oral toil emission sowers."No person.Mama bated.slim'err or elm the Public Comment Regired/Publlc Comment not required required? NOX 00.304 lb/UAW CO 491.36 IbAaid VOC 16683.8208 IIMAMad Seams 32.5872 bMIMd Toluene 22.8120 SYM6Md E9aeeru to 3.0515 SYMeMcf. 6.1629 bitted 188.2307 IbttAWMd 0.3014 IbAMsd .. ''®' 0 MMEIM=MIN V'."' ®' MillE:MMI=I= Vii•«��«�;��n..;� r'.:.` '®'. rrr tl 7.... �NSMIwes Tr_ INIUMMONIa 14WE0006.CP1 123/9BCC m II a a2 y a y 888 0 8 0 0 0 0 0 N o O O z @c•-• > Y » z > Zzz » > z z z esees eeesee seeese Sea e e e m tL00000 OOOOOO S00LaN0 0) 0 0 0) 0) o U w o• N g • " (O " alai ON W 1- � 9a N n NI ; 0 .- A co ca V N O 9 Q a N 2 2 "! Ng ^ in TrN N N. l0 cD m1� N N t+) CD O) Q m .y � co (0co4 0) O )N COO r 1- r )OOr °I V) I.I. N 0 r OD It) o am' W o..- .- 9 C a o S m um) . m C O •- a 2 O ¢ wg ' 2' Im H o 0 0 oco U x y x N = U ONNNNN f: CIE 03 co � � Op = = y 7 .et6 CI? M- CD ` N 1.6 � � mp y 76 �� N t aa"a as mason (?) c a s c c c a a c C m c al m m . m m ix ym t0 m m m y N )p .. p O CO m m O Op m O 0 m o U U U U UUI U U U U c� cg' m �.` YZ U U or y` m or ' i. N O N c1/4i fV N N q m N N co coma_ Fmi fV fV q c �') y c a Eaaaaaaao. ooaa.2 = m aa - mmm > _ - waaaaa w l 1 1 l I oaaaoo 2 8 a a m (O8 2 8 2 m m m m m ` a a O1OO) t 'G 3t $ '� '�) 2 y i 'y3 o § § § S " M22222 : f 2 f 0 22222 2 Z U 2 2 2 w 33233IIIIII3aaa3a 3p as a as -O r 1 M r r M M 00). tO+) BC{Dp N I OCr: COCD g m mi Ov7r N .j O) O 0000 vNtnoNcO+) N a M N 6 a .- N St 7 � NMI 0 U ic m v p m co c.) o m m m m CO S N c c c m c C C m c g c e m co i) wv ? U 2 m J m 8 c m 5S, mUx c 05 x c 3S` Na 00 = os, Om = o5S, OoOm ? o 0o m oa a > toe )- x > mchwX > ZUnici- > zO 0 )- it N _m Z O N atE NNNNN OOOOOO NN 1Ou) NM Oi S Oi S S S -2. ` M �q � ��NNN 5N� NN 00000 N NN N5N5�� 5oNQ�) NNQ ON) N NO R. r Ua U 2525 c8 SSS25gg 5000025 25 25 0 O COv v vv V 0) c') 0) ch 0) Cr) Cr) 0) Cr) 0) Cr) M M M 0) c+) TO; N K a o § N- 0 0 O O O a IJ!IlIP!! glEglisuLiiiiii tiiiiiE: i 7 ?iiIbO iii6—ii. i-, 11 .., L . l ; E Li w 'sir_ :0 1 ru:rr : i xy R ' i ' h ' Jill ill i II irrillpirsurilri ., ,i ., . gm ....., i diem_ • . „, et:4 , 2 :4 , ., ,. . . ,. ;.,„ § i inn,. , cc a E § 8 DRAFT STATE OF COLORADO COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION TELEPHONE:(303)692-3150 .IA• 0, A sI7.4 CONSTRUCTION PERMIT PERMIT NO: 14W E001 1 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the Pronghom P-17 Production Facility, located in the NWNE Section 17, Township 5N, Range 61W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID TL 004 Truck Condensate Loadout FUG 005 Fugitive VOC equipment leak emissions HLP Sep-1 006 One low-pressure separator controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One(1)pneumatic water transfer pump, rated at 600 scf/hr P 1 007 (Sandpiper, Model G1 F, Serial number 2027733)controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One emergency flare with a minimum combustion efficiency of FL-1 OOg 95%. The flare is not enclosed.The emergency flare is used during periods when the sales gas cannot be routed to the pipeline. Point 007: This pump may be replaced with another pump in accordance with the provisions of the Altemate Operating Scenario(AOS)in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. AIRS Point 008: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submittina a Notice of Startup form to the Division. The Notice of Startup form may be AIRS ID: 123/981E Page 1 0114 ® • • • earth and Environment A 1 Pollution Control Division . downloaded . '" "7C^ u= ❑ u . Failure to notify the Division of stet 9f-t$ta.permitted source itt_"'.violidion of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section lII.G.1 and can result in the revocation of the permit 2. AIRS Point 000: The fadowklg information shall be provided to the Division within fifteen(15)days after ixirf(it epcement of operation. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment (Reference: Regulation$Q,.3i Part B, III.E.) 3. AIRS Point 008: Within, hundred and eighty days (180) after commencement of operation, compliance WNh Conditions contained In this permit shall be demonstrated to the Division. It is the is or operator's responsibility to self-certify compliance with the conditions. Failure:to,demonstrate compIBnce a4thin 180 days may; result in revocation of the permit(Reference:Regulation No.3, Part B, III.G.2). 4. AIRS Points 004—007; YOU MUST notify the AIr,Polludon Control Division (the Division) no later tharyt>l tart days after issuance 9f this permit, by submitting a The Notice of Startup form may be downloaded online at .state.Co.us/earddownloadforms.htmt Failure to notify the Division of startup.,'Of.., permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the pemit 5. AIRS Points 004 —007: Within one hundred and eighty days (180) after issuance of this permit, compliarige rtliff the conditions contained in this permit shall be demonstrated to the D It is the owner or opotetor's responsibility to self-certify compliance with the LFailure to demonstrate:compliance within 180 days may result in revocation of the permit.(Reference: Regulation No. 3, Part B, III.G.2). 6. This permit shall expire If the owner or operator of theltource 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 constructlan 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 Divisign may grant extensions of the deadline per Regulation No. 3, Part B, lll.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 7. AIRS Point 006: Within ninety(90)days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric floNrrate of natural gas vented from the low pressure separator. The operator shall use the gas flow rate listed in the application for actual flow rate until the flow meter is installed, not to exceed ninety(90) days after issuance of this permit 8. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No.3,Part B, Section III.E.) . AIRS ID: 123/981 E Page 2 of 14 olor Depa en P li Health and Environment it Pollution Control Division 9. The operator in e ' I ' n le ued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 10. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type Equipment ID Point NOx VOC CO TL 004 10.0 Point FUG 005 6.0 Fugitive HLP Sep-1 006 --- 14.0 3.7 Point P-1 007 -- 1.7 1.2 Point FL-1 008 1.0 7.2 5.2 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 11. AIRS Point 005: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent extended gas analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 12. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID HLP Sep-1 006 Enclosed Flare VOC AIRS ID: 123/9B1 E Page 3 of 14 of ealth and Environment Trlution Control Division P-1 E VOC FL-1 008 Open Flare VOC PROCESS (,.IMITATIONS AND RECORDS 13. This source shall be limited to the following Maximum processing rates as listed below. Monthly records of the actual processing t getsihell be maintained by the owner or operator and made available to the Divislo l fOr b$pection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility mot Equipment Point Process Pareritir Annual Limn ID TL 004 Condensate Load 74,460 BBL HLP Sep-1 006 Gas Vented from Low Separator 10.4 MMSCF P-1 007 Natural Gas 5.3 MMSCF FL-1 008 Gas Vented fmatifittstor 22.2 MMSCF i i. 4 em( Compliance with the annual throughput limits , De determined on a rolling twelve(12) month total. By the end of each month a onth total is calculated based on the previous twelve months' data. The shall calculate throughput each month and keep a compliance record oft s(laf.or at a local field office with site responsibility,for Division review. 14. AIRS Point 006: Upon installation of the fleet."; required under Condition 7, the owner or operator shall continuously m record the volumetric flowrate of natural gas vented from each low pressure using a flow meter.The flow meter shall continuously measure flowrate and r volumetric flow vented from each separator. The owner or operator shall u throughput records to demonstrate compliance with the limits specified in 13 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY RE TS 15. MRS Points 004, 006, 007, and 008: The number and AIRS ID point number (e.g. 123/4567/890)shall be marked on the `equipment for ease of identification. (Reference: Regulation Number 3, Part B, II , ) } only enforceable) 16. Visible emissions shall not exceed twenty %)opacity during normal operation of the source. During periods of startup, Modification, or adjustment of control equipment visible emissions shall not ex opacity for more than six minutes in any sixty consecutive minutes. Emission Weird devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no 1!leiisle.emissions. (Reference: Regulation No. 1,Section II.A.1.&4.) 17. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) AIRS ID: 123/9B1 E Page 4 of 14 olor epa en P li ealth and Environment it Pollution Control Division 18. This source i JJ I . 7 XII.C ral Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable.The operator shall comply with all applicable requirements of Section XII. 19. AIRS Point 004: This source is located in an ozone non-attainment or attainment- maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 20. AIRS Point 004: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: . Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 20(a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. AIRS Point 004: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 22. AIRS Point 005: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis.The first AVO inspection must be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. AIRS ID: 123/9B1E Page 5 of 14 ® •I Awo. pollutionD Control ivision , . to be repaired will be closed if practicable,minimizing the volume released. iv. Repaired components shall be re-screened using AV0 to determine if the leak is repaired. v. The following records shall be maintained fora period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to mace the repair within 15 calendar days. OPERATING&MAINTENANCE REQUIREMENTS 23. AIRS Points 006, 007, and 008: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M)plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Tastina Reaulrements 24. AIRS PoInt 005:Within one hundred and eighty days(180)after Issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in 'heavy liquid service', 'light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 25. AIRS Point 008: Within 180 days after commencement of operation, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference:Regulation No. 1,Section IIA1 &4) Periodic Testina Reaulrements 28. AIRS Point 005: On an annual basis,the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic cofnpbundb (VOC) and hazardous air pollutants (HAP) that may be-released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit AIRS ID: 123/9B1 E Page 6 of 14 :. olor epa en li ealth and Environment it Pollution Control Division ALTERNATE OPE S 27. AIRS Point 007: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section IV.A and without applying for a revision to this permit or obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. 28. AIRS Point 007: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 29. AIRS Point 007: All pump replacements installed and operated per the altemate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 30. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30'" whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO„) in ozone nonattainment areas emitting less than 100 tons of VOC or NO■ per year, a change in annual actual emissions of one(1)ton per year or more or five percent, whichever is greater, above the level reported on the last APEN;or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified;or e. No later than 30 days before the existing APEN expires. 31. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). AIRS ID: 123/9B1 E Page 7 of 14 III Polluti earth and Environment on Control DMsion GENERAL TERMS 32. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 33. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise,the issuance of this construction permit does not provide*final"authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in vatting in accordance with the provisions of 25.7-114.5(12Xa)C.R.S. and AQCC Regulation No. 3, Part B, Section • III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located In the Requirements to Self- Certify for Final Authorization section of this permit. 34. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction,installation and operation of the source, in accordance with this information and with representations made by the owner or operator of owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 35. Unless specifically stated otherwise, the general and specific conditions contained in this permit have been determined by the APCD to be necessary to assure compliance with the provisions of Section 25-7-114.5(7)(a), C.R.S. 38. Each and every condition of this permit is a ma :;part hereof and is not severable. My challenge'to or appeal of a condition hereof constitute a rejection of the entire permit and upon such occurrence, this permit shell deemed denied ab init/o. This permit may be revoked at any time prior to self- and final authorization by the Air Pollution Control Division (APCD) on grounds'set forth hi the Colorado Air Quality Control Act and' regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit,conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 37. Section 25-7-114.7(2)(a), C.R.S. requires that all spumes required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 38. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal' enforcement actions under Sections 25-7-115 (enforcement), -121 (Injunctions),-122(civil penalties),-122.1 (criminal penalties),C.R.S. AIRS ID: 123/9B1E Page 8 of 14 olor epa en P li ealth and Environment it Pollution Control Division By: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9B1E Page 9 of 14 iiPtIgal , III • •• :A P t i ealth and Environment DPollution Control Division lit Notes to Permit Holder :. 1) The permit holder is required to pay fees for the processing time for this permit.An invoice for these fees will be issued after the permit is Issued.The permit holder shall pay the invoice within 30 days of r. receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No.3,Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates repuested in the permit application These limits may be revised upon request of the owner or.. providing there is no ecceedance of any specific emission control regulation or any amblerN�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: htto://www.Colorado.cov/cs/Satellite?c=Document C&childpaaename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=125159$389641&panename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit This information is listed to inform the operator of the Division's analysis • of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled • Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CM if (lb/yr) reportable? (Ib/yr) Benzene 71432 237 r No 237 n-Hexane 110543 1292 Yes 1292 004 Toluene 108883 520 Yes 520 - Xylenes 1330207 363 Yes 363 Benzene 71432 59 No 59 n-Hexane 110543 307 Yes 307 005 Toluene 108883 109 No 109 Ethylbenzene 100414• 20 No 20 Xylenes 1330207 73 No 73 Benzene 71432 1256 Yes 63 n-Hexane 110543 • 7713 Yes 386 006 Toluene 108883 797 Yes 40 Ethylbenzene • 100414 113 No 6 Xylenes 1330207 174 No 9 Benzene 71432 122 No 6 007 n-Hexane 110543 765 Yes 38 • AIRS ID: 123/9B1 E Page 10 of 14 olor epa en P li ealth and Environment it Pollution Control Division Tol 8 5 Ethylbenzene 100414 12 No 1 Xylenes 1330207 32 No 2 Benzene 71432 518 Yes 26 n-Hexane 110543 3236 Yes 162 008 Toluene 108883 378 Yes 19 Ethylbenzene 100414 50 No 3 Xylenes 1330207 137 No 7 5) The emission levels contained in this permit are based on the following emission factors: Point 004: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.270 AP-42 Benzene 0.0032 AP-42 Toluene 0.0070 AP-42 Xylenes 0.0049 AP-42 n-Hexane 0.0174 AP-42 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95)using the following values: L= 12.46*S*P"M/T S=0.6(Submerged loading: dedicated normal service) P(true vapor pressure)=6.67 psia M(vapor molecular weight)=67.41 Ib/Ib-mol T(temperature of liquid loaded)=524 R The uncontrolled non-criteria reportable air pollutant (NCRP)emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 005: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 714 303 267 Flanges 34 8 10 Open-ended Lines 22 3 1 Pump Seals 2 0 1 Valves 101 39 29 Other* 50 5 10 VOC Content(wt. 0.2261 1.0 0.9934 1.0 fraction) Benzene Content(wt. 0.0004 0.0118 0.0012 fraction) Toluene Content(wt. 0.0003 0.0259 0.0003 AIRS ID: 123/9B1E Page 11 of 14 DRAT.. 11Iliealth and Environment r Pollution Control Division fraction) • Ethylbenzene(wt 0.001104 0.0047 0.0001 fradion) Xyl9nes Content(wt 0.0001 0.0180 0.0001 fraction) n-hexane Content(wt 0.0025 0.0643 0.0001 fraction) 'Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains,dump arms,hatches,instrument meters,polish rods and vents ' . TOC Emission Factors(kg/hr-component): Component Gas Service Heavy Oil Light Oil Wrvice l Seervice; Connectors 2.1E-04 7.5E-08 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA • 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R95-017 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts,multiplied by the VOC content from the most recent gas analysis. Point 006: Weight Omission Emission Pollutant Fraction of tractors Factors Gas(%) Uncontrolled Controlled Source NOx 0.068 0.068 AP-42 _ lb/MMBtu Ib/MMBtu . CO 0.37 AP-42 - 0.37 lb/MMBtu Ib/MMBtu VOC 80.17 53,899 2,695.0 Engineering Ib/mmsd lb/mmscf "Calculation Benzene 0.14 121.20 6.0600 Engineering Iblmmed 'Dimmed Calculation Toluene 0.09 76.832 3.8416 Engineering ,, Ib/mmad lbimmscf Calculation Ethylbernzene 0.01 10.925 0.5463 Engineering {`4. Ib/mmsd Ib/mmscf Calculation Xylenea 0.02 16.808 0.8404 Engineering ib/mmscf Ib/mmscf Calculation n tnexans 0.83 744.01 37.201 Engineering ib/mmsd lb/mmscf Calculation Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 9/19/2013 of the gas vented from the low pressure separator at Pronghorn P,T-22HNB to estimate • AIRS ID: 123/9B1E Page 12 of 14 ol Depa P li Health and Environment it Pollution Control Division the VOC and HA ofR_2FOd stimate stream flow. The controlled VOC and HAP emissions factors for point 006 are based on the flare control efficiency of 95%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,938 BTU/scf was used for calculations. Point 007: Emission Factors Emission Factors -Uncontrolled -Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NO„ 0.068 lb/MMBTU AP-42 Table 13.5-1 CO 0.37 lb/MMBTU AP-42 Table 13.5-1 VOC 13,007 650.34 All emission factors Toluene 17.020 0.8510 are based on the Xylenes 6.1629 0.3081 stated consumption n-Hexane 145.53 7.2764 and sales gas analysis from Pronghorn P-T-17- Benzene 23.292 1.1646 HNB collected 9/19/2013 The displacement equation can found in"EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10-Displacement Equation(10.4-3)." Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,258 BTU/scf was used for calculations. Point 008: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled NOx 0.068 0.068 AP-42 Table 13.5-1 lb/MMBtu Ib/MMBtu CO 0.37 AP 42 Table 13.5-1 0.37 lb/MMBtu lb/MMBtu VOC 22.61 13,007 650.34 Engineering lb/mmscf lb/mmscf Calculation Benzene 0.04 23.292 1.1646 Engineering lb/mmscf lb/mmscf Calculation Toluene 0.03 17.020 0.8510 Engineering lb/mmscf lb/mmscf Calculation Ethylbenzene 0.01 2.2411 0.1121 Engineering lb/mmscf lb/mmscf Calculation Xylenes 0.01 6.1629 • 0.3081 Engineering lb/mmscf lb/mmscf Calculation n-hexane 0.25 145.53 7.2764 Engineering lb/mmscf lb/mmscf Calculation Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,258 BTU/scf was used for calculations. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the AIRS ID: 123/9B1E Page 13 of 14 oI Ith and Environment r Pollution Control Division most recent a for each emissions point • associated with this permit For any questions regarding a specific exxpirafon date cal the Division at 303 � )-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Squres of: VOC and n-hexane NANSR Synthetic Minor Source of: MACT NH S�Requirements: Not Applicable Arep`Source Requlrettfrints: Not Applicable 8) Full text of the Title 40, ProjeCtion of Environment Electronic Code of Federal Regulations can be found at the website listed below: htto://ecfr,snoccess.gov/ Part 60:Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart IOW - NSPS Part 60,Appendixes Appendix A—Appendix I Part 83: National Emission Standards for Hazardous Mr Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart M—Subpart DDD MACT 63.1200-63.1439 Subpart EEE-Subpart PpP MACT 63.1440-63.6175 Subpart QQQ..Support YYYY MACT 63.6580-63.8830 Subpart 2222 Subpart MMMMM MACT 63.8980-End Subpart NNNNN=Subpart XXXXXX 9) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado.gov/cdohe/oiloasvermits AIRS ID: 123/9B1E Page 14 of 14 Division Information Engineer: Carissa Money Control Engineer: Chris Laplante Review Date: 05/01/2014 Application Date: 11108/2013 Facility Identifiers Permit No. 14W E0011 AIRs County 123 Weld Facility If 9B1E Facility Type: exploration and production facility 9 Located in the 8-hotr non-attainment area? 0 True Minor O Synthetic Minor for: r voc r NOx r co Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Pronghorn P-17 Production Facility Source Location: NWNE Section 17,Township 5N, Range 61W SIC: 1311 Mailing Address 1: Bonanza Creek Energy Operating Company LLC Address Address 2: 410 17th Street,Suite 1500 f,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pvoung@bonanzacrk.com Section 02: Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Pronghorn P-17 Production Facility,located in the NWNE Section 17,Township 5N,Range 61W,Weld County.Colorado. Point Name Type Control 004 TL Loadout None 005 FUG Fugitives None 006 HLP Sep-1 Separator Venting Flare 007 P-1 Pump Flare 008 FL-1 Separator Venting Flare This is an emergency flare used when pipeline 1004 (Truck Condensate Loadout Calculations AP-42:Chapter 5.2 Equation 1 L=12.46'S•P=M/T I.=loading losses in lb per 1000 gallons loaded S=Saturation Factor P=true vapor pressure of liquid loaded[psia] M=molecular weight of vapors[lb/lb-mole] 7=temperature of bulk liquid loaded[deg.RI 1 degree Fahrenheit=460.67 degree Rankine Source S 0.6 Submerged loading:dedAP-42 P 6.67 psia Sales Oil Analysis documenting RVP 8.8 and AP-42 M 67.41 lb/lb-mole Sales oil analysis for RVP 8.8 and interpolating valu T 523.67 deg.R EPA Tanks Met Data for Denver,CO L 6.42 lb/10"3 gal 2.70E-01. lb/bbl Annual requested Throughput 74460 BBL/yr 3127320 pl/yr Annual requested V0C emissions 20074 lb/yr 10.04 tpy Regulatory Considerations • I his facility is not condisdered a terminal On Reg.7)because average daily thoughput will be below 20,000 gallons at 8566 gallons per day. This facility is not considered a bulk plant(in Reg.7)because it does not distribute gasoline. NCRPs Component Mass Frac. lb/yr Emission Factor lb/1000gal Benzene 0.011821 237.29 0.0032 ibibbl 0.07588 n-henna 0.06437 1292.16 0.0174 lblbbl 0.41319 Touene 0.025914 520.20 0.0070Iblbbl 0.16634 Xylenes 0.018061 362.56 0.0049Ib/bbl 0.11593 14WE0011.CP1 123/981E C Es 3_ e p 0 � o ; Ei0eg . .0 . 0000 . 000va e 4 n n O On •-. O '. p n o 0 00 0 0 0 0 n0 0 00 0 .0° a s a ,A. ° It00 ° 0 ' " ° " 0000o ° ° o0et a ? € m ry " -� K i° O ° OOOae = ry 0000000vea ` an 0000 m .. .. 000000000 e . I000o0ogom :00 % ovov000000e _ it l tl m0 G C C G C m C m m C C o C o O o o o C G o o o i ti v _ ZseOr4000Vo � mo « o 00000000' . "s_ s $ I 8PmOrvoo 3 1— soV t 3 N o « 0 0 0 c 0 „ ,^., o « 0 0 0 0 0 0 0 0 0 0 0 $ 'e O $ _ N $$$ m o m o o ry . . . . . . ,... ,.. . . g .m a o a o o " ti 0 o r 0 m w 0 0 o 0 0 o 0 o n 6 o o e 8 �'£ oocc00n0c°' og ; a y888 � 8 fr3Mom .. o " 300000 FE.': 'o .': oaod 'o '00000 0000000 .'; 000„ m 88888 500000 _ $ x e > €_.00000000000 °o o8 8888mo8m °rv° 88e a Sobog B'0i I F . 0 = = .:, . ... . . . .. m a o 6 0 0 _ 12 i IZ000000000066 6000006666 I Mil �oO 'O O p o . 00'0000 _ O moo = ,u •' g 4 4 '4144 2244' 44 22 22244444 '44 i LI I ! t s8 "1" ww8a88M 8M W 8 svg v o ,., mmmm N. mmarv . rvry tg s > E Iii24442W44W4444 4224442424 w r: a E' uu : uu 4 2 — rc 8388 0 '0 8orv9 � X '� °m' n n 000 � � g ^�,g - a -« 088 a o a s o g III in w L i I O V N 2 v „ v „ E° p r. > 6 f - r a - a e o r _ C x R n iii c n e ° _ — s g ' et .' c i � me H vt 6 �' z: 'x rocOr Or g E o ° o 2 23 8 § ° €ai6 icI 3uEE 8 & NE Egc $$ t ;9 o ^ 8.t.; ed9LLo >" db8 o'>" a' b8c' o'> zsa o~ � 1 $ °' .i3 4 8 '^ a ; 3 N11 8 8 1 o x 3 W 3 I II I a I 9 I a 1 I a iii 6� l 6 f 111 I 006 One low-pressure separator controlled by two enclosed flares.Each flare has a minimum combustion efficiency of 95%. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II.Chapter 10-Displacement Equation(10.4-3) Ex=0*MW'Xx/C Ex=emissions of pollutant x Q=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/lb-mol)at 60F and 1 atm Throughput(O) 10.4 MMscf/yr 1183.4 scf/hr 0.88 MMscf/mo MW 33.950 lb/lb-mot 0.028 MMscf/d mole% MW lbx/Ibmol mass traction E Ib/hr Ib/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 C02 2.58 44.01 1.135 0.033 CO2 3.5 31058 15.53 N2 0.14 28.013 0.039 0.001 N2 0.1 1073 0.54 methane 36.2348 16.041 5.812 0.171 methane 18.1 158984 79.49 ethane 21,724 30.063 8.531 0.192 ethane 20.4 178636 89.32 propane 24.0702 44.092 10.6130 0.313 propane 33.1 290293 145.15 Isobutane 2.5189 58.118 1.4639 0.043 isobutane 4.6 40042 20.02 n-butane 8.0091 58.118 4.6547 0.137 n-butane 14.5 127318 63.66 isopentane 1.3574 72.114 0.9789 0.029 isopentane 3.1 26775 13.39 n-pentane 1.8714 72.114 1.2053 0.036 n-pentane 3.8 32968 18.48 cyclopentane 0,1315 70.13 0.0922 0.003 cyclopentane 0.3 2522 1.26 n-Hexane 0.3272 86.18 0.2820 0.0083 n-Hexane 0.9 7713 3.88 cyclohexane 0.0815 84.16 0.0686 0.002 n.Aaiexane 0.2 1876 0.94 Other hexanes 0.5785 86.18 0.4968 0.015 Other hexanes 1.6 13569 6.79 heptanes 0.264 100.21 0.2648 0.008 heptares 0.8 7236 3.62 methylcyclohexare 0.061 98.19 0.0599 0.002 methylcyGMexene 0.2 1638 0.82 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 3 0.00 Benzene 0O588 78.12 0.0459 0.00135 Benzene 0.1 1258 0.63 Toluene 0.0316 92.15 0.0291 0.00086 Toluene 0.1 796 0.40 Ethylbenzene 0.0039 106.17 0.0041 0.00012 Ethylbenzene 0.0 113 0.06 Xylenes 0.006 106.17 0.0064 0.00019 Xylenes 0.0 174 0.09 C.B.Heavies 0.1398 116.000 0.1622 0.00478 C8+Heavies 0.5 4438 2.22 VOC mass fraction: 0.6017 Total VOC Emissions(Uncontrolled) 279.4 33.946 Notes Mole%.MW,and mass fractions from analysis of LP gas collected 9/19/2013 from Pronghorn P,7-22HNB. Emissions are based on 8760 hours of operation per year. Typically I would calculate the average MW of C8+based on the average MW on the analysis for the gas, Since Bonanza used 116 as MW and this results in minimal difference in emissions,I used 116 Ib/Ibmol Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Lead Model L-30-010 and HOC-48 Serial Number 21455 and 18677 Gas Heating Value 1938 Bturscf Throughput 20090.43979 MMBtu/yr 14WE0011.CP1 123/981E ... ... •.` a'-• ..,Q. .. • VRU Information-Not applicable Equipment Description Make ,Modal Requested Control Efficiency Annual Bypass Time Baclap Flare Overall Control 85.00% Combustion emission factor sgxce: ,AP-42:Chapter 13.5 0.07 lb NOX/%0A8tu 0.37 lb CORAMBlu 0.68 tpy NOX 3.72 tpy CO Emissions Summary 0.7' tpy NOX UncontroledIPTE 3.7 tpy CO 219.4 tpy VOC Controlled 14.0 tpy VOC Uncontrolled Controlled Total Total(Rlyr) Reportable? • llayr) Benzene 1256 Yes 63 Toluene 798 Yes 40 _Ethylbenzene 113 No 6 Xytenes 174 No .. ' 9 - n-hexane 7713 Yes 388 224-TMP 3 No 0 Regulstory ,r�,up��p�lic�sbiifty 1""` Y�..e�Is subject to the opacity requirements for flares in Section IIA.5:No owner ar9gpor°f el l applies to ell emission sources."No person,wherever located,scull muse oraltuir the emission comment Public Comment Required - required? Factors for Perla IIMIIINV7t 131.784 Ibf Q4scf CD 717.06 It11AM4tscf • VOC 13899.2132 lb/haled penxscts 121.1994 IbIf,MAsd • ToluMfe 76.8322 IbdMMedf • • 10.9251 IhlMMec( 16.8079 IlsIMMed 744.0131 IWMM.cf 0.3014 lM 4Mscf ' R NO X 131.784 lbvt4Mscf , CO 717.06 Ibl MMAacf VOC 2894.9807 IWMMicf lissom 6.0600 IbIMMecf ToAune 3.8416 IM. 4scf • • Ethllberr>7ens 0.5483 IbTMAAsc f )(lief.' '0.8404 IbfldAiscf twHeaane 37.2007 IblMMscf 224.TMP 0.0151 IWAMMsof . 14WE0o11.cP1 123/961E One (1)water transfer pump, rated at 600 scf/hr(Sandpiper, Model G1F, 007 Serial number 2027733). Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump , Number: 2027733 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled ®Flare Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4- 3) Ex=Q* MW*Xx Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas* MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Q soo scf/hr MW 21.8 lb/lb-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy CO2 2.36 44 0.0476 CO2 1.644 14400.608 7.200 nitrogen 0.86 28 0.0110 nitrogen 0.381 3339.432 1.670 methane 75.37707 16.04 0.5546 methane 19.141 167671.698 83.836 ethane 11.6264 30.07 0.1604 ethane 5.536 48491.938 24.246 propane 6.654 44.09 0.1346 propane 4.644 40685.442 20.343 isobutane 0.5528 58.12 0.0147 isobutane 0.509 4455.637 2.228 n-butane 1.6262 58.12 0.0434 n-butane 1.496 13107.375 6.554 isopentane 0.2588 72.15 0.0086 isopentane 0.296 2589.505 1.295 n-pentane 0.3158 72.15 0.0105 n-pentane 0.361 3159.836 1.580 cyclopentane 0.0244 72.15 0.0008 n-pentane 0.028 244.142 0.122 n-hexane 0.064 86.18 0.0025 n-hexane 0.087 764.896 0.382 14WE0011.CP1 123/981E cyclohexane o.otee 84.18 0.0006 cydohexane 0.022 193.791 0.097 Other hustles 0.1137 Sias 0.0045 Other hexane 0.155 1358.886 0.679 heptanes 0.o5e9 200.2.1 0.0026 heptanes 0.090 790.750 0.395 methylcydohexa 0.0143 98.19 0.0006 methylcyclohe 0.022 194.724 0.097 224-IMP 0 114.23 0.0000 224-IMP 0.000 0.000 0.000 Benzene 0.0113 78:11 0.0004 Benzene 0,014 122.406 0.061 Toluene 0.007 .V.2.4 0.0003 Toluene 0.010 89.446 0.045 _Ethylbenzene 0.0008 10317' ' ' 0.0000 Ethylbenzene 0.001 11.779 0.006 Xylenes 0.0022 198.17 0.0001 Xylenes 0.004 32.392 0.016 C8+Heavies 0.035s lire 0.0019 C8+Heavies 0.065 571.087 0.286 Mass Fraction VOC: 0.2262 Total 34.186 • Heating Value I 1zse 8111/sd Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOXIMMBW 0.37 ' I lb COIMMetu Notes Mole%,MW,and mass fractions from: sales gas analysis collected 9/19/2013 at Pronghorn P-T-17HNB Emissions Summary Uncontrolle 0.2" 'tpy NOX d/PTE 1.2' tpy CO 34.2 tpy VOC Controlled 1.7 tpy VOC Reportable Controlled cake Total(Ib/yr) 7 Total n-hexane 110643 764.9 Yes 38 224-TMP 540841 0.0 No 0 Benzene _ 71432 .122:4 No 6 Toluene) 108883 89.4 No 4 E-Benzene 100414 11.8 No 1 Xylenes 1330207 32A No 2 Uncontrolled Emission Factors Controlled Emission Factors VOC 13008.390 Ib/MMsd 650.4194763 lb/MMscf Benzene 23.289 lb/MMscf 1.164436675Ib/MMscf n-hexane 145.528 lb/MMscf 7.276411609 lb/MMscf Toluene 17.018 Ib/MMsd 0.850897098 lb/MMscf E•80nzene 2.241 Ito/MMscf 0.11205277 lb/MMscf Xylenes 6.163 lb/MMscf 0.308145119 lb/MMsd 224-IMP 0.000 lb/MMscf 0 lb/MMsd 14WE0011.CP1 123/981E One emergency flare with a minimum combustion efficiency of 95%. The flare is not enclosed.The emergency flare is used 008 when the pipeline is not available. Equipment Description This source vents natural gas from: a well head separator when pipeline not available Emissions from this source are: routed to a flare Natural gas venting from a well head separator when pipeline not available.Emissions from this source are routed to a flare. fmission 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 Q=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/lb-mol)at 60F and 1 atm Throughput(Q) 22.2 MMscf/yr 2538.0 scf/hr 1.89 MMsd/mo MW 21.800 IMb-mol 0.061 MMscf/d mole% MW Ibx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 0.01 4.0028 0.000 0.000 Helium 0.0 23 0.01 CO2 2.36 44.01 1.039 0.048 CO2 7.0 60928 30.46 N2 0.86 28.013 0.241 0.011 N2 1.6 14132 7.07 methane 1531707 16.041 12.091 0.555 methane 81.0 709296 354.85 ethane 11.6284 30.083 3.496 0.160 ethane 23.4 205073 102.54 propane 6654 44.092 2.9339 0.135 propane 19.6 172107 88.05 isobutane 0.5526 58.118 0.3213 0.015 isobutane 2.2 18847 9.42 n-butane 16262 58.118 0.9451 0.043 n-butane 8.3 55442 27.72 Isopentane 02586 72.114 0.1666 0.009 isopentane 1.2 10948 5.47 n-pentane 0.3156 72.114 0.2277 0.010 n-pentane 1.5 13359 6.88 cyclopentane 0.0244 70.13 0.0171 0.001 cyclopentene 0.1 1004 0.50 n-Hexane 0.064 86.18 0.0552 0.0025 n-Hexane 0.4 3236 1.62 cyclohexane 0.0166 84.16 0.0140 0.001 cyclohexane 0.1 820 0.41 Other hexanes 0.1137 88.18 0.0980 0.004 Other Scenes 0.7 5748 2.87 heptanes 00569 100.21 0.0570 0.003 heptanes 0.4 3345 1.67 methykydohexene 00143 98.19 0.0140 0.001 methylcyclohexane 0.1 824 0.41 224-TMP 0 114.23 0.0000 0.000 224-TMP 0.0 0 0.00 Benzene 0 0113 78.12 0.0088 0.00040 Benzene 0.1 518 0.28 Toluene 0.007 92.15 0.0085 0.00030 Toluene 0.0 378 0.19 Ethylbenzeee 0.0008 106.17 0.0008 0.00004 Ethylbenzene 0.0 50 0.02 Xylenes 00022 106.17 0.0023 0.00011 Xylenes 0.0 137 0.07 C8*Heavies 0.0355 116.000 0.0412 0.00189 C8+Heavies 0.3 2416 1.21 VOC mass fraction: 0.2261 Total VOC Emissions(Uncontrolled) 144.6 21.797 Notes Mole 16,MW.and mass fractions are based on sales gas analysis collected 9/19/2013 at Pronghorn P-T-17HNB Emissions are based on 8760 hours of operation per year. Typically I would calculate the average MW of C8.based on the average MW on the analysis for the gas. Since Bonanza used 116 as MW and this results in minimal difference in emissions,I used 116 Ib/Ibmol Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1258 Bh1/sc( Throughput 27968.96304 MMBtu/yr 14WE0011.CP1 123/981E VRU Information-not applicable Equipment Description MS Model Requested.Control Efficiency Annual Bypass This Rap Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chpptpr 13.5 0.07 m NOXaaAeb 0.37 lb CODAMBlu 8.95 toy NOX 5.17 WY CO Emissions Summary 1.0 Ipy NOX Uncontrolled/PIE 5.2 toy CO 144.8 lay VOC • Controlled \ 72 ley VOC Uncontrolled Controlled Total Total(Rryr) Reportable? (Ibrye) Benzene 518 - Yes -2e Toluene 378 Yes 19 Eorylbentane 50 No 2 . .. )(Oconee 137 .. . No 7. . n-hexane 3238 Yes 162 224-1MP 0 No 0 ItoWlatsrY Ajplleabllfly tee zest tto the opacity requirements for flares in Section liA.5:'No owner or operator ofe Sae to al emission sources.'No person,wherever roosted,stall cause or allow the emissions Public Comment Required required? lealaainfastaleammil • 85.5K. Idbplaol CO 485:48 Btfated VOC 13008.7755 SAS? Berens 23.2917 IblABAscf ToAwrs 17.0198 IblLUeecf Eerylberiens 22411 lb/MMecf Xylenee 6.1629 IblAlAlscf Mims 145.5252 145.5282 IMAPAsd 224-TMP 0.0000 lMllAsd c» tl NOX 85.544 IbIMMed CO 485.48 b.Ied VOC 850.3388 lb/MtAsef • -'N Benzene 1.1848 IIMIAMeof toluene 0.8510 iti/MIAsof Eul�st....ela•ne 0.1121 ItallAscf ^isOee 0.3081 IbIt*4ecf n4lenne - 7.2764 Ibft Aacf 22-TMP 0.0000 WBAMscf 14VE0011.01 123/981E m II a a@ w s. 00) 00) 0 0 0 0 0 00000 0 0 0 0 zea z > r > z > zzz > r > zz zzzz r,; 00000 0 0 0 0 0 0 �00 � � �� aoo mrnmrn 0w I gpM St NNtMO CO N O O a ^ OIAA N OAl �A N N N ' W ' 0) W � N IOM M NOai N n A - - �i Ci i- aD M I— a. 9. m m � N N N M O N 0 , N A p •co co N V l0 a) N 0 - t0 41 .- N O m 'y e 3 10 $„7, U K W & _ C C c d c 2 2 2. 0 a a 0 0. 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