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Home My WebLink About20201461.tiffa COLORADO Department of Public Health & Environment Weld County - Clerk to the Board 1150 O St PO Box 758 Greeley, CO 80632 April 15, 2020 Dear Sir or Madam: RECEIVED APR 2 4 2020 WELD COUNTY COMMISSIONERS On April 16, 2020, the Air Pollution Control Division will begin a 30 -day public notice period for Bonanza Creek Energy Operating Company, LLC - Latham 14-12 Production Facility (COGCC #429825). A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Public Notice Coordinator 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe Jared Polis, Governor I Jill Hunsaker Ryan, MPH, Executive Director Pubr;c Rcv;e'J CG: pt_(Tp), HL(LK), PW(mimicN/cx), oGCsK) 510./O 2020-1461 Air Pollution Control Division Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - Latham 14-12 Production Facility (COGCC #429825) - Weld County Notice Period Begins: April 16, 2020 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: Latham 14-12 Production Facility (COGCC #429825) Exploration and Production Well Pad SWSW T4N Sec 12 R63W Weld County The proposed project or activity is as follows: This facility is updating their facility -wide permit to account for the anticipated increase in throughput due to the addition of a new well, which is anticipated to occur in late spring 2020. Additionally, upon re-evaluation of the facility set-up, it was determined that the low pressure separator gas flaring (point 013) should not be considered a unique emission point and it was subsequently cancelled and removed from this permit. This facility is a synthetic minor facility of VOC and n -hexane. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 13WE1101 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Comments may be submitted using the following options: • Use the web form at https://www.colorado.Rov/pacific/cdphe/air-permit-public-notices. This page also includes guidance for public participation • Send an email to cdphe.commentsapcd@state.co.us • Send comments to our mailing address: Lauraleigh Lakocy Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 its COLORADO Department of Public Health 6 Environment a CDPHE COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado CONSTRUCTION PERMIT Permit number: I3 WE 1101 Date issued: Issued to: Facility Name: Plant AIRS ID: Physical Location: County: Description: Issuance: 5 Bonanza Creek Energy Operating Company, LLC Latham 14-12 Production Facility (COGCC #429825) 123/9AC2 SWSW SEC 12 T4N R63W Weld County Well Production Facility Equipment or activity subject to this permit: Facility Equipment ID AIRS Point Equipment Description Emissions Control Description CNDTK-01 003 Six (6) 400 barrel and three (3) 500 barrel fixed roof storage vessels used to store condensate Enclosed Combustion Device PWT-01 004 One (1) 300 barrel and one (1) 400 barrel fixed roof storage vessels used to store produced water Enclosed Combustion Device L-01 006 Truck loadout of condensate by submerged fill using vapor balance Enclosed Combustion Device This permit is granted subject to all rules and regulations of the Colorado Air Quality Control Commission and the Colorado Air Pollution Prevention and Control Act (C.R.S. 25-7-101 et seq), to the specific general terms and conditions included in this document and the following specific terms and conditions. REQUIREMENTS TO SELF -CERTIFY FOR FINAL AUTHORIZATION 1. Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, compliance with the conditions contained in this permit must be demonstrated to the Division. It is the owner or operator's responsibility to self -certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. A self certification form and guidance on how to self -certify Page 1 of 12 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado compliance as required by this permit may be obtained online at www.colorado.gov/cdphe/air- permit-self-certification. (Regulation Number 3, Part B, Section III.G.2.) 2. The operator must complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self -certification process. (Regulation Number 3, Part B, Section III.E.) 3. The operator must retain the permit final authorization letter issued by the Division, after completion of self -certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 4. Emissions of air pollutants must not exceed the following limitations. (Regulation Number 3, Part B, Section II.A.4.) Annual Limits: Facility Equipment ID AIRS Point Tons per Year Emission Type PM2.5 NO, VOC CO CNDTK-01 003 --- 1.1 33.5 5.2 Point PWT-01 004 --- --- 0.5 --- Point L-01 006 --- --- 0.5 --- Point Note: See "Notes to Permit Holder" for information on emission factors and methods used to calculate limits. Facility -wide emissions of each individual hazardous air pollutant must not exceed 8.0 tons per year. Facility -wide emissions of total hazardous air pollutants must not exceed 20.0 tons per year. The facility -wide emissions limitation for hazardous air pollutants must apply to all permitted emission units at this facility. Compliance with the annual limits, for both criteria and hazardous air pollutants, must be determined on a rolling twelve (12) month total. By the end of each month a new twelve month total is calculated based on the previous twelve months' data. The permit holder must calculate actual emissions each month and keep a compliance record on site or at a local field office with site responsibility for Division review. 5. The owner or operator must use the emission factors found in "Notes to Permit Holder" to calculate emissions and show compliance with the limits. The owner or operator must submit an Air Pollutant Emission Notice (APEN) and receive a modified permit prior to the use of any other method of calculating emissions. 6. The emission points in the table below must be operated and maintained with the emissions control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit. (Regulation Number 3, Part B, Section III.E.) Page 2 of 12 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado Facility Equipment ID AIRS Point Control Device Pollutants Controlled CNDTK-01 003 Enclosed Combustion Device VOC and HAP PWT-01 004 Enclosed Combustion Device VOC and HAP L-01 006 Vapor Balance System to an Enclosed Combustion Device VOC and HAP PROCESS LIMITATIONS AND RECORDS 7. This source must be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates must be maintained by the owner or operator and made available to the Division for inspection upon request. (Regulation Number 3, Part B, II.A.4.) Process Limits Facility Equipment ID AIRS Point Process Parameter Annual Limit CNDTK-01 003 Condensate throughput 78,475 barrels PWT-01 004 Produced Water throughput 78,476 barrels L-01 006 Condensate Loaded 78,475 barrels The owner or operator must monitor monthly process rates based on the calendar month. Compliance with the annual throughput limits must be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder must calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 8. The permit number and ten digit AIRS ID number assigned by the Division (e.g. 123/4567/001) must be marked on the subject equipment for ease of identification. (Regulation Number 3, Part B, Section III.E.) (State only enforceable) 9. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 10. On or before June 30th, 2021 (and on June 30th each year thereafter), the owner or operator of oil and natural gas operations and equipment at or upstream of a natural gas processing plant in Colorado must submit a single annual report that includes actual emissions and specified information in the Division -approved report format. The information included in the annual report must be in accordance with the general reporting requirements of Regulation Number 7, Part D, Section V.B. Beginning July 1, 2020, and each calendar year thereafter, owners or Page 3 of 12 a 4. - COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado operators must maintain the information according to Regulation Number 7, Part D, Section V.C. for inclusion in the annual report. (Regulation Number 7, Part D, Section V) 11. Points 003, 004: The combustion device covered by this permit is subject to Regulation Number 7, Part D, Section II.B.2. General Provisions (State only enforceable). If a flare or other combustion device is used to control emissions of volatile organic compounds to comply with Section II, it must be enclosed; have no visible emissions during normal operations, as defined under Regulation Number 7, Part D, Section II.A.23; and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. This flare must be equipped with an operational auto -igniter according to the schedule in Regulation Number 7, Part D, Section II.B.2.d. 12. Points 003, 004: This source is subject to Regulation Number 7, Part D, Section I. The operator must comply with all applicable requirements of Section I and, specifically, must: • Comply with the recordkeeping, monitoring, reporting and emission control requirements for storage tanks; and • Ensure that the combustion device controlling emissions from this storage tank be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. (Regulation Number 7, Part D, Section I.C.) (State only enforceable) 13. Points 003, 004: The storage tank covered by this permit is subject to the emission control requirements in Regulation Number 7, Part D, Section II.C.1. The owner or operator must install and operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons except where the combustion device has been authorized by permit prior to March 1, 2020. The source must follow the inspection requirements of Regulation Number 7, Part D, Section II.C.1.d. and maintain records of the inspections for a period of two years, made available to the Division upon request. This control requirement must be met within 90 days of the date that the storage tank commences operation. 14. Points 003, 004: The storage tanks covered by this permit are subject to the venting and Storage Tank Emission Management System ("STEM") requirements of Regulation Number 7, Part D, Section II.C.2. 15. Point 006: Hydrocarbon liquids loadout from storage tanks to transport vehicles must be controlled by using (a) submerge fill and (b) a vapor collection and return system and/or air pollution control equipment. Compliance with Section II.C.5. must be achieved in accordance with the following schedule: (Regulation Number 7, Part D, Section II.C.5.a.) • Facilities constructed or modified on or after May 1, 2020, must be in compliance by commencement of operation. • Facilities constructed before May 1, 2020, must be in compliance by May 1, 2021. • Facilities not subject to Sections II.C.5.a.(i)(A) or II.C.5.a.(i)(B) that exceed the hydrocarbon liquids loadout to transport vehicles throughput of greater than or equal to Page 4 of 12 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado 5,000 barrels per year on a rolling 12 -month basis must control emissions from loadout upon exceeding the loadout threshold. 16. Point 006: Storage tanks must operate without venting at all times during loadout. (Regulation Number 7, Part D, Section II.C.5.a.(ii)) 17. Point 006: The owner or operator must, as applicable (Regulation Number 7, Part D, Section II.C.5.a.(iii)): • Install and operate the vapor collection and return equipment to collect vapors during the loadout of hydrocarbon liquids to tank compartments of outbound transport vehicles and to route the vapors to the storage tank or air pollution control equipment. • Include devices to prevent the release of vapor from vapor recovery hoses not in use. • Use operating procedures to ensure that hydrocarbon liquids cannot be transferred to transport vehicles unless the vapor collection and return system is in use. • Operate all recovery and disposal equipment at a back -pressure less than the pressure relief valve setting of transport vehicles. • The owner or operator must inspect onsite loading equipment to ensure that hoses, couplings, and valves are maintained to prevent dripping, leaking, or other liquid or vapor loss during loadout. These inspections must occur at least monthly, unless loadout occurs less frequently, then as often as loadout is occurring. 18. Point 006: The owner or operator must perform the following observations and training (Regulation Number 7, Part D, Section II.C.5.a.(iv)): • The owner or operator must observe loadout to confirm that all storage tanks operate without venting when loadout operations are active. These inspections must occur at least monthly, unless loadout occurs less frequently, then as often as loadout is occurring, • If observation of loadout is not feasible, the owner or operator must document the annual loadout frequency and the reason why observation is not feasible and inspect the facility within 24 hours after loadout to confirm that all storage tank thief hatches (or other access point to the tank) are closed and latched. • The owner or operator must install signage at or near the loadout control system that indicates which loadout control method(s) is used and the appropriate and necessary operating procedures for that system. • The owner or operator must develop and implement an annual training program for employees and/or third parties conducting loadout activities subject to Section II.C.5. that includes, at a minimum, operating procedures for each type of loadout control system. 19. Point 006: The owner or operator must retain the records required by Regulation Number 7, Part D, Section II.C.5.a.(v) for at least two (2) years and make such records available to the Division upon request. • Records of the annual facility hydrocarbon liquids loadout to transport vehicles throughput. Page 5 of 12 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado • Inspections, including a description of any problems found and their resolution, required under Sections II.C.5.a.(iii) and II.C.5.a.(iv) must be documented in a log. • Records of the infeasibility of observation of loadout. • Records of the frequency of loadout. • Records of the annual training program, including the date and names of persons trained. 20. Point 006: Air pollution control equipment used to comply with this Section II.C.5. must comply with Section II.B., be inspected in accordance with Sections II.C.1.d.(ii) through (v), and achieve a hydrocarbon control efficiency of 95%. (Regulation Number 7, Part D, Section II.C.5.a.(vi)) OPERATING £t MAINTENANCE REQUIREMENTS 21. Upon startup of these points, the owner or operator must follow the most recent operating and maintenance (OEM) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to the OftM plan are subject to Division approval prior to implementation. (Regulation Number 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements Point 003: The owner or operator must complete site specific sampling including a compositional analysis of the pre -flash pressurized condensate from the single stage separator processing liquids from the Latham F11-J14-14HNB well (API # 05-123-49899) and the Latham 14-11-12HZ well (API #05-123-35939) routed to these storage tanks and a well -head fluid sample from the Latham O-K-12HNB well (API #05-123-37402). Testing of the pre -flash pressurized condensate must be in accordance with the guidance contained in PS Memo 05-01. Results of testing must be used to determine site -specific emissions factors for VOC and Hazardous Air Pollutants using Division approved methods. Results of site -specific sampling, analysis, and working/breathing calculations must be submitted to the Division as part of the self - certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. Additionally, the operator must submit to the Division within 60 days of sampling, or a timeframe as agreed to by the Division, a request for permit modification to use the site -specific emission factors developed through these analyses to estimate emissions and demonstrate ongoing compliance. Periodic Testing Requirements 22. This source is not required to conduct periodic testing, unless otherwise directed by the Division or other state or federal requirement. ADDITIONAL REQUIREMENTS 23. All previous versions of this permit are cancelled upon issuance of this permit. 24. A revised Air Pollutant Emission Notice (APEN) must be filed: (Regulation Number 3, Part A, II.C.) • Annually by April 30th whenever a significant increase in emissions occurs as follows: Page 6 of 12 a COLORADO Air Pollution Control Division Department of Public Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado 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 (NOX) in ozone nonattainment areas emitting less than 100 tons of VOC or NOX per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non -criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. • Whenever there is a change in the owner or operator of any facility, process, or activity; or • Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or • Whenever a permit limitation must be modified; or • No later than 30 days before the existing APEN expires. 25. Federal regulatory program requirements (i.e. PSD, NANSR) must 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 must not exceed the Federal program threshold until a permit is granted. (Regulation Number 3, Parts C and D). GENERAL TERMS AND CONDITIONS 26. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation Number 3, Part B, Section II.B. upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 27. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7- 114.5(12)(a) C.R.S. and AQCC Regulation Number 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self -certification of all points has been reviewed and approved by the Division, it will provide written documentation Page 7 of 12 a COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado 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. 28. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 29. 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. 30. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof must constitute a rejection of the entire permit and upon such occurrence, this permit must be deemed denied ab initio. This permit may be revoked at any time prior to self -certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 31. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 32. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122 (civil penalties), -122.1 (criminal penalties), C.R.S. By: Lauraleigh Lakocy Permit Engineer Permit History Issuance Date Description Issuance 1 May 13, 2013 Issued to Bonanza Creek Energy Operating Company, LLC Issuance 2 September 23, 2014 Added condensate tanks (003) to permit. The point had previously been covered by GP01. Increased emissions and throughput for loadout Page 8 of 12 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado (006). Increased fugitive emission limit (007). Added new equipment under AIRS Point 011, 012, and 013. Issuance 3 November 13, 2017 Issued as Final Approval - removed self -certification and initial testing requirements. Removed Point 005 - now covered by GP02. Removed Point 007 - cancelled per operator request (emissions are below permit threshold). Removed Point 012 - equipment was never installed. Issuance 4 April 25, 2018 Issued to Bonanza Creek Energy Operating Company, LLC Point 014: Permit heat trace pump (P-02), previously covered under point 008, as a separate point (point 014). Points 008, 011 ft 014: Update emissions based on site -specific gas analysis provided with the application., Issuance 5 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC Points 008, 011, and 014: Removed from permit due to removal from site. Point 003: Updated site -specific emissions factors, throughput, and emissions. Added initial testing requirements- Point 004: Added to permit (previously GP05). Point 006: Updated throughput Et emissions limits. Point 013: Removed point from permit based on cancellation received 4/7/2020. Page 9 of 12 4%0 COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado Notes to Permit Holder at the time of this permit issuance: 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder must pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit. (Regulation Number 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator must notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: https://www.colorado.gov/pacific/cdphe/aqcc-regs 4) The following emissions of non -criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. AIRS Point Pollutant CAS # Uncontrolled Emissions (lb/yr) Controlled Emissions (lb/yr) 003 Benzene 71432 5,152 258 Toluene 108883 3,888 194 Ethylbenzene 100414 488 24 Xylenes 1330207 815 41 n -Hexane 110543 32,128 1,606 2,2,4- Trimethylpentane 540841 145 7 004 Benzene 71432 549 28 n -Hexane 110543 1,727 86 006 Benzene 71432 33 2 n -Hexane 110543 283 15 Note: All non -criteria reportable pollutants in the table above with uncontrolled emission rates above 250 pounds per year (lb/yr) are reportable and may result in annual emission fees based on the most recent Air Pollution Emission Notice. Page 10 of 12 a COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado 5) The emission levels contained in this permit are based on the following emission factors: Point 003: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source N0x 0.0275 0.0275 AP -42, Chapter 13.5 CO 0.1256 0.1256 V0C 17.06 0.853 Site -specific Pressurized liquid sample taken upstream of VRT (10/14/2019) modeled through ProMax for flash, working, and breathing emissions 71432 Benzene 0.0657 3.285E-03 108883 Toluene 0.0495 2.475E-03 100414 Ethylbenzene 0.0062 3.1E-04 1330207 Xylene 0.0104 5.2E-04 110543 n -Hexane 0.4094 2.047E-02 540841 2,2,4- Trimethylpentane 0.0019 9.5E-05 Note: The controlled emissions factors for this point are based on a control efficiency of 95%. Point 004: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source V0C 0.262 0.0131 CDPHE Approved State Emission Factor per PS Memo 14-03 71432 Benzene 0.0070 0.004 110543 n -Hexane 0.0220 0.0011 Note: The controlled emissions factors for this point are based on a control efficiency of 95%. Point 006: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source V0C 0.236 1.18E-02 CDPHE Approved State Condenate io Loadout Emission Factor per PS Memo 14-02 71432 Benzene 4.1E-04 2.05E-05 110543 n -Hexane 3.6E-03 1.80E-04 Note: The controlled emissions factors for this point are based on a control efficiency of 95%. 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 must 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 Page 11 of 12 a _rt. COLORADO Air Pollution Control Division Department of Public Health & Environment Dedicated to protecting and improving the health and environment of the people of Colorado emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This permit fulfills the requirement to hold a valid permit reflecting the storage tank and associated control device per the Colorado Oil and Gas Conservation Commission rule 805b(2)(A) when applicable. 8) This facility is classified as follows: Applicable Requirement Status Operating Permit Synthetic Minor Source of: VOC, n -hexane PSD True Minor Source NANSR Synthetic Minor Source of: VOC 9) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://www.ecfr.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1 -End Subpart A - Subpart UUUU NSPS Part 60, Appendixes Appendix A - Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A - Subpart Z MACT 63.600-63.1199 Subpart AA - Subpart DDD MACT 63.1200-63.1439 Subpart EEE - Subpart PPP MACT 63.1440-63.6175 Subpart QQQ - Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ - Subpart MMMMM MACT 63.8980 -End Subpart NNNNN - Subpart XXXXXX Page 12 of 12 -ke( Condensate Storage Tank(s) APEN 14kr8 Form APCD-205 -° Air Pollutant Emission Notice (APEN) and Application for Construction Permit All sections of this APEN and application must be completed for both new and existing facilities, including APEN updates. Incomplete APENs will be rejected and will require re -submittal. Your APEN will be rejected if it is filled out incorrectly, is missing information, or lacks payment for the filing fee. The re -submittal will require payment for a new filing fee. �hL ree This APEN is to be used for tanks that store condensate associated with oil and gas industry operations. If your emission source does not fall into this category, there may be a more specific APEN available for your source (e.g. crude oil storage tanks, produced water storage tanks, hydrocarbon liquid loading, etc.). In addition, the General APEN (Form APCD-200) is available if the specialty APEN options will not satisfy your reporting needs. A list of alt available APEN forms and associated addendum forms can be found on the Air Pollution Control Division (APCD) website. This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: I3W E 1101 14 AIRS ID Number: 123 / 9AC2 / 003 anc :,._ Section 1 - Administrative information Company Name: Bonanza Creek Energy Operating Company, LLC Site Name: Latham 14-12 Production Facility (COGCC #429825) Site Location: 40.32039, -104.39238 SWSW, T4N, Sec 12, 63W Mailing Address: (Include Zip Code) 410 17th Street, Suite 1400 Denver, CO 80202 Site Location County: Weld NAICS or SIC Code: 1311 Contact Person: Alisson Soehner Phone Number: (303) 803-1752 E -Mail Address2: asoehner@bonanzacrk.com 1 Use the full, legal company name registered with the Colorado Secretary of State. This is the company name that wilt appear on all documents issued by the APCD. Any changes will require additional paperwork. 2 Permits, exemption letters, and any processing invoices will be issued by the APCD via e-mail to the address provided. 424781 aMoinkIC S c0L•at.eiie Noma** innn.aoawat Permit Number: 13WE110114 AIRS ID Number: 123 / 9AC2 / 003 Section 2 - Requested Action O NEW permit OR newly -reported emission source ❑ Request coverage under traditional construction permit ❑ Request coverage under a General Permit ❑ GP01 ❑ GP08 If General Permit coverage is requested, the General Permit registration fee of $312.50 must be submitted along with the APEN filing fee. -OR- Q MODIFICATION to existing permit (check each box below that applies) ID Change in equipment 0 Change company name3 0 Change permit limit ❑ Transfer of ownership4 O Other (describe below) - OR O APEN submittal for update only (Note blank APENs will not be accepted) - ADDITIONAL PERMIT ACTIONS - • APEN submittal for permit exempt/grandfathered source ❑ Limit Hazardous Air Pollutants (HAPs) with a federally -enforceable limit on Potential To Emit (PTE) Additional info ft Notes: updating emission factor, throughput and number of tanks to account for new well 3 For company name change, a completed Company Name Change Certification Form (Form APCD-106) must be submitted. 4 For transfer of ownership, a completed Transfer of Ownership Certification Form (Form APCD-104) must be submitted. Section 3 - General Information General description of equipment and purpose: Company equipment Identification No. (optional): For existing sources, operation began on: Condensate Storage CNDTK-01 DTK-01 8/21/2012 For new or reconstructed sources, the projected start-up date is: Normal Hours of Source Operation: 24 Storage tank(s) located at: hours/day 7 days/week 52 weeks/year 0 Exploration Et Production (E&P) site O Midstream or Downstream (non E&P) site Will this equipment be operated in any NAAQS nonattainment area? 0 Yes ■ No Are Flash Emissions anticipated from these storage tanks? El Yes I No Is the actual annual average hydrocarbon liquid throughput ≥ 500 bbl/day? ■ Yes B No If "yes", identify the stock tank gas -to -oil ratio: m3/ iter Are these storage tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) 805 series rules? If so, submit Form APCD-105. Yes No • 0 Are you requesting ≥ 6 ton/yr VOC emissions (per storage tank), or are uncontrolled actual emissions ≥ 6 ton/yr (per storage tank)? Yes No I O COLORADO -NMN b fnnwn,nen ✓❑ Upward ❑ Horizontal Permit Number: 13WE1101 14 AIRS ID Number: 123 / 9AC2 / 003 Section 4 - Storage Tank(s) Information 1 Condensate Throughput: Actual Annual Amount (bbl/year) 65,396 From what year is the actual annual amount? Projected 2020 Average API gravity of sales oil: 48.07 degrees O Internal floating roof Tank design: ,r❑ Fixed roof Requested Annual Permit Limits (bbUyear) 78,475 RVP of sales oil: 11.25 O External floating roof Storage Tank ID # of Liquid Manifold Storage Vessels in Storage Tank Total Volume of Storage Tank (bbl) Installation Date of Most Recent Storage Vessel in Storage Tank (month/year) Date of First Production (month/year) CNDTK-01 Six {400 bbl) and Three (500 bbl) Tanks 3,900 6/2013 8/2012 Wells Serviced by this Storage Tank or Tank Battery' (E&P Sites Only) API Number Name of Well Newly Reported Well 05 - 123 - 35939 Latham 14-11-12HZ ■ 05 - 123 - 35941 Latham 14-12 ■ 05 - 123 - 37402 Latham O-K-12HNB ■ 05 - 123 - 49899 Latham F11-J14-14HNB O ■ 5 Requested values will become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on alt APENs, including APEN updates. 6 The EEP Storage Tank APEN Addendum (Form APCD-212) should be completed and attached when additional space is needed to report all wells that are serviced by the equipment reported on this APEN form. Section 5 - Geographical/Stack Information Geographical Coordinates (Latitude/Longitude or 0TM) 40.32039, -104.39238 ❑ Check box if the following information is not applicable to the source because emissions will not be emitted from a stack. If this is the case, the rest of this section may remain blank. Operator Stack ID No. Discharge Height Above Ground Level (Feet) Temp. (°F) Flow Rate (ACFM) Velocity (ft/sec) ECD 01-05 25 500 TBD TBD Indicate the direction of the stack outlet: (check one) O Downward ❑ Other (describe): O Upward with obstructing raincap Indicate the stack opening and size: (check one) Q Circular Interior stack diameter (inches): 48 ❑ Square/rectangle Interior stack width (inches): O Other (describe): Interior stack depth (inches): COLORADO 3 NaWtNIYnN nwN Permit Number: 13WE 1101 14 AIRS ID Number: 123 / 9AC2 / 003 Section 6 - Control Device Information ❑ Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. Vapor ❑ Recovery Unit (VRU): Pollutants Controlled: Size: Make/Model: Requested Control Efficiency: % VRU Downtime or Bypassed (emissions vented): ❑ Combustion Device: Pollutants Controlled: VOC, HAPs Rating: 3.62 Type: 4 LEED and 1 Cimarron MMBtu/hr Make/Model: 48" and 48" HVECD Requested Control Efficiency: 95 % Manufacturer Guaranteed Control Efficiency: 99 Minimum Temperature: 500 Waste Gas Heat Content: Constant Pilot Light: 0 Yes ❑ No Pilot Burner Rating: 2,901 0.05 Btu/scf MMBtu/hr ❑ Closed Loop System Description of the closed loop system: ❑ Other: Pollutants Controlled: Description: Control Efficiency Requested: Section 7 Gas/Liquids Separation Technology Information (E&tP Sites Only) What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? ^r50 psig Describe the separation process between the well and the storage tanks: Well head liquid is routed to (2) single stage separators and (1) 2 -stage separators, then directed to tanks COLORADO nro.>�dv. . �. HMNBlnrirormeM Red -lines per attached etnails/ I calculations received 3/10/2020 and 3/19/2020. -LL Permit Number: 13WE 1101 14 E txvx _. _, . APC.-- AIRS ID Number: 123 / 9AC2 J 003 Section 8 - Criteria Pollutant Emissions Information Attach all emissions calculations and emission factor documentation to this APEN form7. Is any emission control equipment or practice used to reduce emissions? 0 Yes ❑ No If yes, describe the control equipment AND state the collection and control efficiencies (report the overall, or combined, values if multiple emission control methods were identified in Section 6): Pollutant Control Equipment Description Collection Efficiency (% of total emissions captured by control equipment) Control Efficiency (% reduction of captured emissions) VOC LCD 100% 95% NOx CO NAPS LCD 10 °!, 95% Other: From what year is the following reported actual annual emissions data? Projected 2020 Use the following table to report the criteria pollutant emissions from source: Pollutant Emission Factor? Actual Annual Emissions Requested Annual Permit Emission Limit(s)5. source Uncontrolled Controlled Uncontrolled Controlled Uncontrolled Basis Units (AP -42, Mfg., etc.) Emissions (tau/yeer) Emissions8 (tons/year) Emissions (tons/year) Emissions (tons/year) VOC 17 0'.;- 17.06 lb/bbl ProMax 557.50 557.83 27:88 27.90 ssaoo- 669.39 33,45 33.47 NO,, 0.068 ib/MMBtu AP -42 0.91 0.91 1_09 1.1 4O8 1.1 CO 0.310 lb/MMBtu AP -42 4.12 4.12 493 5.2 4133 5.2 5 Requested values wilt become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on all APENs, including APEN updates. 7 Attach condensate liquid laboratory analysis, stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. 8 Annual emission fees will be based on actual controlled emissions reported. If source has not yet started operating, provide projected emissions. Section 9 - Non -Criteria Pollutant Emissions Information Does the emissions source have any uncontrolled actual emissions of non -criteria pollutants (e.g. HAP - hazardous air pollutant) equal to or greater than 250 lbs/year? If yes, use the following table to report the non -criteria pollutant (HAP) emissions from source: Chemical Name Chemical Abstract Service (CAS) Number Emission Factor Actual Annual Emissions Uncontrolled Basis Units Source (4P-42, Mfg., etc.) Uncontrolled Emissions (ibs/year) Controlled Emissions8 (lbs/year) Benzene 71432 o 0.657 Iblbbl ProMax 4.292 216 Toluene 108883 0.0495 Ibfibl ProMax 3,239 162 Ethylbenzene 100414 0.0062 Ib/bbl ProMax 407 22 Xylene 1330207 0.0104 Ib/bM ProMax 680 34 n -Hexane 110543 o,401 -0.4094 Ib bbl ProMax 26.754 1.338 2,2,4-Trimethylpentane 540841 0.00180.0019 11>/bbl ProMax 121 8 0 Yes ❑ No 7 Attach condensate liquid laboratory analysis, stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. 8 Annual emission fees will be based on actual controlled emissions reported. if source has not yet started operating, provide projected emissions. 5 e DeptUsent AV. COLORADO Permit Number: 13WE1101 1101 14 AIRS ID Number: 123 /9Ac2/003 Section 10 Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP01 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable General Permit. °2:72-0 Signature of Legally Authorized Person (not a vendor or consultant) Date Alisson Soehner Environmental Engineer, Air Quality Name (print) Title Check the appropriate box to request a copy of the: ❑r Draft permit prior to issuance ID Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Send this form along with $191.13 and the General Permit For more information or assistance call: registration fee of $312.50, if applicable, to: Colorado Department of Public Health and Environment Air Pollution Control Division APCD-SS-B 1 4300 Cherry Creek Drive South Denver, CO 80246-1530 Make check payable to: Colorado Department of Public Health and Environment Small Business Assistance Program (303) 692-3175 OR (303) 692-3148 APCD Main Phone Number (303) 692-3150 COLORADO rY Dro.rtmenla/ua1� V - iswwm q [naimwm 4/7/2020 State.co.us Executive Branch Mail - Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Request STATE OF COLORADO Lakocy - CDPHE, Lauraleigh <Iauraleigh.Iakocy@state.co.us> Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Request Patrick Dilsaver <pdilsaver@slrconsulting.com> Tue, Mar 10 2020 at 2.04 PM. To: "Lakocy - CDPHE, Lauraleigh"<lauraleigh.lakocy@state.co.us>, Patrick Dilsaver <PDilsaver@bonanzacrk.com> Cc: Alisson Soehner <ASoehner@bonanzacrk.com> Hey Lauraleigh, I ran with 500 bbl tanks, attached is the updated ProMax printout, W&B stencil, and updated tank calcs and 102 Form This is! what I would proposeredlining the APEN with. What do you think? We understand the separator venting will need an initial test to demonstrate compliance, thanks. Pat Patrick Dilsaver Associate Scientist 970-494-0805 970-494-0805 307-214-9584 pdilsaver@slrconsulting.com SLR International Corporation 143 Union Blvd, Suite 505, Lakewood, CO 80228 Confidentiality Notice and Disclaimer This communication and any attachment(s) contain information which is confidential and may also be legally privileged. It is intended for the exclusive use of the recipient(s) to whom it is addressed. If you have received this communication in error, please e-mail us by return e-mail and then delete the e-mail from your system together with any copies of it. Any views or opinions are solely those of the author and do not represent those of SLR Management Ltd, or any of its subsidiaries, unless specifically stated. From: Lakocy - CDPHE, Lauraleigh <lauraleigh.lakocy@state.co.us> Sent: March 09, 2020 9:43 AM To: Patrick Dilsaver <PDilsaver@bonanzacrk.com> Cc: Alisson Soehner <ASoehner@bonanzacrk.com>; Patrick Dilsaver <pdilsaver@slrconsulting.com> [Quoted text hidden] [Quoted text hidden] 3 attachments https://mai l.google. com/mail/u/0?ik=44f88835c3&view=pt&search=all&permmsgid=msg-f%3A1660809570710812789&simpl=msg-f%3A16608095707... 1/2 4/7/2020 State.co.us Executive Branch Mail - Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Request W&B 500 bbl tanks.PNG 58K in Latham 14-12_Updated Tanks and 102 Form.pdf 4-4 184K ami Latham 14-12_50 psig_500bbl tanks.rtf 5193K https://mai I.google.com/mail/u/0?ik=44f88835c3&view=pt&search=all&permmsgid=msg-f%3A1660809570710812789&simpl=msg-f%3A16608095707... 2/2 Bonanza Creek Energy Operating Company, LLC. - Latham 14-12 Production Facility (COGCC #429825) Condensate Tank Site Specific Emission Factor Calculations Emission Source: Condensate Tanks Designed Throughput: 179 bbl/day Designed Throughput: 65,396 bbl/yr Requested Throughput: 78,475 bbl/yr Enclosed Flare VOC Control Efficiency: 95% Operating Days per Year. 365 days/yr Total Emissions Emission Pollutant Factors I°l (Ib/bbl) Actual Emissions (tpy) 1"I Requested Emissions (tpy)l° Uncontrolled Controlled Uncontrolled Controlled CO2 0.09 3.05 3.05 3.66 3.66 Methane 0.17 5.45 0.28 6.55 0.33 VOC 17-06s 557.83 27.90 669,39? 33.47; Benzene 0.0657 2.15 0.11 2.58 0.129 Toluene 0.0495 1.62 0.08 1.94 0.098 Ethylbenzene 0.0062 0.20 0.01 0.24 0.013 Xylenes 0.0104 0.34 0.02 0.41 0.021 n -Hexane 0.4094 13.39 0.67 16.06 0.804 224-TMP 0,0019 0.06 0.00 0.07 0.004 Notes: (a) Emission Factor from ProMax run (b) Uncontrolled Emissions (toy) = (Emission Factor, lb/bbl) ' (Actual Throughput, bbl/yr) 1(2,0001 Mon) (c) Requested Emissions (tpy) = (Actual Emissions, tpy) ' 1.2 Bonanza Creek Energy Operating Company, LLC. - Latham 14-12 Production Facility (COGCC #429825) Enclosed Combustion Device (ECD) Emission Calculations for Condensate Tank Battery 1 Emission Source: Condensate Tanks Source Type: ECD Heat Input Requested: 3.63 MMBtu/hr Heat Input Acutal: 3.03 MMBtu/hr Gas Oil Ratio (GOR): 137.80 scf/bbl Tank Vent Gas Flowrate Requested: 1,234.5 scf/hr Tank Vent Gas Flowrate Requested: 10.81 MMscf/yr Tank Vent Gas Flowrate Actual: 1,028.7 scf/hr Tank Vent Gas Flowrate Actual: 9.01 MMscf/yr Pilot Gas Flowrate: 16.8 scf/hr Pilot Gas Flowrate: 0.15 MMscf/yr Total Flowrate to Combustor Including Pilot: 9.16 MMscf/yr Estimated HHV: 2,901 Btu/scf Total VOC Control Efficiency: 95% Sulfur Content of Fuel: 0.0020 gr/scf Operating Hours per Year: 8,760 hr/yr Pollutant Emission Factors or Uncontrolled Emissions (° Actual Emissions Requested Emissions lb/hr (4(cl tpy Ib/hr1"1,tel tpy (dl CO2 116.98 lb/MMBtu 354.77 1,553.89 424.58 1,859.68 N20 0.00030 Ib/MMBtu 0.00 0.01 0.00 0.01 NO x 0.068 Ib/MMBtu 0.21 0.91 0.25 1.09 CO 0.3101b/MMBtu 0.94 4.12 1.13 4.93 SO2 0.00020 lb/MMBtu 0.0006 0.0027 0.0007 0.0032 PM -to 40.0 pg / t 0.0277 0.1212 0.0331 0.1450 PM2.5 40.0 pg /1 0.0277 0.1212 0.0331 0.1450 Notes: (a) Emission factors are from AP -42 Tables 13.5-1 8 2 (Industrial Flares) 40 pg / L is for lightly smoking flare (this is conservative as this unit is smokeless in design). SOc emissions based on AP42, which is based on 100% conversion of sulfur to SO 3 at 2000 grainslElMscf. CO2 and N20 emission factors from 40 CFR Part 98 Table C-1 and C-2 for Natural Gas. (b) Hourly Emission Rate (Ibdrr) except for PM lo = (Emission Factor, lb/MMBtu) ' (Heat Input, MMBtu/hr) (c) (scf CHn/rr) (10.6 set E/sct CH.,) (0.0283 m3/scf E) (40 p PM,o/L E) (1000 Vm3) (5/106 pg) (lb/453.59 g) / (hr/yr) = lb PM,,/ hr (d) Annual Emission Rate (tpy) _ (Hourly Emission Rate, Ib/hr) • (hryr) / (2,000 lb/ton) 3/23/2020 State.co.us Executive Branch Mail - Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 ModificationRequ... STATE OF COLORADO Lakocy - CDPHE, Lauraleigh <Iauraleigh.lakocy@state.co.us> Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Request Patrick Dilsaver <pdilsaver@slrconsulting.com> To: "Lakocy - CDPHE, Lauraleigh"<lauraleigh.lakocy@state.co.us>, Patrick Dilsaver <PDilsaver@bonanzacrk.com> Cc: Alisson Soehner <ASoehner@bonanzacrk.com> Lauraleigh, Successfully beat the storm home and now following back up on emails! Answers below in red, let me know if you want to discuss or have followup questions, I can alter the O&M plan and get that out once we work out the below questions. Thanks, Pat Patrick Dilsaver Associate Scientist O 970-494-0805 O 970-494-0805 -...307-214-9584 • pdilsaver@slrconsulting.com SLR International Corporation 143 Union Blvd, Suite 505, Lakewood, CO 80228 Confidentiality Notice and Disclaimer This communication and any attachment(s) contain information which is confidential and may also be legally privileged. It is intended for the exclusive use of the recipient(s) to whom it is addressed. If you have received this communication in error, please e-mail us by return e-mail and then delete the e-mail from your system together with any copies of it. Any views or opinions are solely those of the author and do not represent those of SLR Management Ltd, or any of its subsidiaries, unless specifically stated. From: Lakocy - CDPHE, Lauraleigh <lauraleigh.lakocy@state.co.us> Sent: March 12, 2020 11:29 AM To: Patrick Dilsaver <PDilsaver@bonanzacrk.com> Cc: Patrick Dilsaver <pdilsaver@slrconsulting.com>; Alisson Soehner <ASoehner@bonanzacrk.com> Subject: Re: FW: [EXTERNAL] Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Request Dear Pat, Thank you for this swift response! https://mail.google.com/mail/u/0?ik=44f88835c3&view=pt&search=all&permmsgid=msg-f%3A16616355387369089078‘simpl=msg-f%3A1661635538... 1/13 3/23/2020 State.co.us Executive Branch Mail - Bonanza Creek Operating - Latham 14-12 Production Facility - Permit 13WE1101 Modification Requ... With regards to the newly submitted O&M plan, I do want to confirm the calculation methodologies that you are requesting to use. There appear to be 3 proposals, which I have annotated with a few notes in blue: 1. Back -calculate the volume of LPGFL from other volumes of gas sent to the enclosed combustor o Condensate GOR: 137.80 or 137.6? This value changed with the newly submitted calculation sheet and I am unclear why, Produced Water GWR: what is the representative GWR used for this facility? Loadout GOR: 1.32 scf/bbl - how was this value calculated? I believe the GOR changed to 137.8 because we ran the new ProMax with larger tanks, which slightly increased the emission factors but also GOR due to more W&B losses. The GWR we use would be the same as Ant F-15, 3.89 scf/bbl which is based on several flash liberation analysis across the field, and in this case is more conservative than the state factor used to permit the water tanks (36 scf/bbl). The Truck Loadout is now using the state factor for emissions calcs, which works out to 1.70 lb/bbl, it looks like we were still calculating the scf/bbl based on a site -specific analysis. I would propose just changing this to the 1.70 as that is what is used for the truck loadout emissions. 1. Calculate the ratio of volume of gas from separator to other sources and multiply by the total volume: Can you elaborate more on this methodology and what you consider a "flash factor"? If this is the emission factor resulting from flash emissions, why would this not also include working/breathing emissions as those vapors go to the combustors as well? Maybe we can have a call on this if I'm not answering this question correctly, but here is an example of how we would calculate the "ratio" of LPGFL to total volume. This is a method we worked out with Carissa Money on another site, I can dig for that email an specific site if helpful. This example isn't specific to this site, but if LPGFL = 100 scf/bbl, CNDTK = 100 scf/bbl, PWT= 50 scf/bbl, and TLO = 50 scf/bbl, then the total "flash" is 300 scf/bbl of oil produced for the various sources contributing to the meter volume. LPGFL works out to 33% of of that, so Bonanza would take 33% of the total volume measured and use that as the LPGFL volume combusted, for that particular month where the previous equations resulted in a negative flow rate. This happens very infrequently where the main equation works out to a negative flow rate on a monthly basis. We have also had some O&M plans that state the equation will be applied on a daily basis if it results in a monthly negative flow rate, if that would be preferable. 2. Use the GOR ratio of the....and there is not a VRU compressor at this site, so for this option are you intending on using the liquid throughput from the separator? I recognize that this option is likely standard language used across multiple plans; however, I would request that the following language is removed as it does not apply to this facility "or the flow meter has not yet been installed or is not required". We can remove that part and resubmit once we work out the rest of the O&M plan. As a kind of "out -there" question, would it be considered to consider all of the vapor going through the flow meter to be from the separator? I do know of a few facilities that do have the "double -counting", conservative emissions estimate, and believe this may have been one of the options in Bonanza's O&M plans previously at other facilities. We have done this at other facilities, however this facility is in a different situation. The new well is not on a 2 -stage separator, so it will not be contributing to any of the flow to LPGFL. It is just one remaining separator for older wells that we are permitting the LPGFL for. Most of the emissions from this facility are expected from the new well and are accounted for in the condensate tank emissions. So if we assumed LPGFL was equal to the entire meter volume at any point, it would be vastly overestimating the LPGFL flow (which is fairly low) and would not at all be representative of the flow rate for that point. If you could let me know about the redlining and additional clarification questions in blue, that would be greatly appreciated. I do realize that this may be getting very in-depth, but I see very few facilities that add new wells that do not have a dedicated flow meter to measure the volume of gas vented, and with the proximity to thresholds, it is important to clearly establish compliance demonstrations and determine what is most appropriate at these types of facilities that are increasing production, but still maintaining original set-ups. Sincerely, Laurateigh Lakocy Oil Et Gas Permit Engineer Stationary Sources Program https://mail.google.com/mail/u/Vik=44f88835c3&view=pt&search=all&permmsgid=msg-f%3A1661635538736908907&simpl=msg-f%3A1661635538... 2/13 Produced Water Storage Tank(s) APEN Form APCD-207 Air Pollutant Emission Notice (APEN) and Application for Construction Permit All sections of this APEN and application must be completed for both new and existing facilities, including APEN updates. Incomplete APENs will be rejected and will require re -submittal. Your APEN will be rejected if it is filled out incorrectly, is missing information, or lacks payment for the filing fee. The re -submittal will require payment for a new filing fee. This APEN is to be used for tanks that store produced water associated with oil and gas industry operations. If your emission source does not fall into this category, there may be a more specific APEN available for your source (e.g. crude oil storage tanks, condensate storage tanks, hydrocarbon liquid loading, etc.). In addition, the General APEN (Form APCD-200) is available if the specialty APEN options will not satisfy your reporting needs. A list of all available APEN forms and associated addendum forms can be found on the Air Pollution Control Division (APCD) website. This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: 13WE1101 1101 14 Dr r AIRS ID Number: 123 / 9AC2 / 004 Section 1 - Administrative Information Company Name: Bonanza Creek Energy Operating Company, LLC Site Name: Latham 14-12 Production Facility (COGCC #429825) Site Location: 40.32039, -104.39238 SWSW, T4N, Sec 12, 63W Mailing Address: (Include zip code) 410 17th Street, Suite 1400 Denver, CO 80202 Site Location County: Weld NAICS or SIC Code: 1311 Contact Person: Alisson Soehner Phone Number: (303) 803-1752 E Mail Address2: asoehner@bonanzacrk.com t Use the full, legal company name registered with the Colorado Secretary of State. This is the company name that will appear on all documents issued by the APCD. Any changes wilt require additional paperwork. 2 Permits, exemption letters, and any processing invoices will be issued by the APCD via e-mail to the address provided. 424782 COLORADO 207ivl7ei rr?te} i ::£flu. Permit Number: 13WE 1101 14 AIRS ID Number: 123 / 9AC2 / 004 Section 2 - Requested Action ❑ NEW permit OR newly -reported emission source ❑ Request coverage under traditional construction permit ❑ Request coverage under a General Permit 0 GP05 0 GP08 If General Permit coverage is requested, the General Permit registration fee of $312.50 must be submitted along with the APEN filing fee. OR ❑ MODIFICATION to existing permit (check each box below that applies) O Change in equipment 0 Change company name3 O Change permit limit ❑ Transfer of ownership4 0 Other (describe below) -OR- ❑ APEN submittal for update only (Note blank APENs will not be accepted) - ADDITIONAL PERMIT ACTIONS - ▪ APEN submittal for permit exempt/grandfathered source ❑ Limit Hazardous Air Pollutants (HAPs) with a federally -enforceable limit on Potential To Emit (PTE) Additional Info & Notes: Updating throughput to account for new well 3 For company name change, a completed. Company Name Change Certification Form (Form APCD-106) must be submitted. 4 For transfer of ownership, a completed Transfer of Ownership Certification Form (Form APCD-104) must be submitted. Section 3 - General Information General description of equipment and purpose: Company equipment Identification No. (optional): For existing sources, operation began on: Produced Water Storage PWT-01 8/21/2012 For new or reconstructed sources, the projected start-up date is: Normal Hours of Source Operation: 24 hours/day Storage tank(s) located at: ❑✓ Exploration & Production (E&P) site days/week 52 weeks/year 0 Midstream or Downstream (non E&P) site Will this equipment be operated in any NAAQS nonattainment area? a Yes ■ No Are Flash Emissions anticipated from these storage tanks? o Yes ■ No Are these storage tanks located at a commercial facility that accepts oil production• wastewater for processing? Yes No a Do these storage tanks contain less than 1% by volume crude oil on an annual average basis? a Yes ■ No Are these storage tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) 805 series rules? If so, submit Form APCD-105. Yes No U a Are you requesting ≥ 6 ton/yr VOC emissions (per storage tank), or are uncontrolled actual• emissions ? 6 ton/yr (per storage tank)? Yes No © COLORADO 2 xwunei�a.n Permit Number: 3WE1 1101 14 AIRS ID Number: 123 I9AG2 1 004 Section 4 - Storage Tank(s) Information Actual Annual Amount (bbllyear) IProduced Water Throughput: From what year is the actual annual amount? Tank design: Fixed roof 65,396 Projected 2020 ❑ Internal floating roof Requested Annual Permit Limits (bbtlyear) 78,476 ❑ External floating roof Storage Tank ID # of Liquid Manifold Storage Vessels in Storage Tank Total Volume of Storage Tank (bbl) installation Date of Most Recent Storage Vessel in Storage Tank (month/year) Date of First Production (month/year) PWT-01 One (300 bbl) and One (400 bbl) Tanks 700 bbl 6/2013 8/2012 Wells Serviced by this Storage Tank or Tank Batteryb (E&P Sites Only) API Number Name of Well Newly Reported Well 05 - 123 - 35939 Latham 14-11-12HZ ■ 05 - 123 - 35941 Latham 14-12 ■ 05 • 123 - 37402 Latham C)-K-12HNB ■ D5 - 123 - 49899 Latham F11-J14-14HNB ■ 5 Requested values will become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on all APENs, including APEN updates. 6The EEtP Storage Tank APEN Addendum (Form APCD-212) should be completed and attached when additional space is needed to report all wells that are serviced by the equipment reported on this APEN form. Section 5 - Geographical/Stack Information Geographical Coordinates (LatitudetLongitude or UTM) 40.32039, -104.39238 ❑ Check box if the following information is not applicable to the source because emissions wilt not be emitted from a stack. If this is the case, the rest of this section may remain blank. Operator Stack ID No. Discharge Height Above Ground Level (Feet) Temp. (°F) Flow Rate (ACFM) Velocity (ft/sec) ECD 01-05 25 500 TBD TBD Indicate the direction of the stack outlet: (check one) El Upward O Horizontal Downward ❑Other (describe): Upward with obstructing raincap Indicate the stack opening and size: (check one) Q✓ Circular Interior stack diameter (inches): 48 0 Square/rectangle Interior stack width (inches): 0 Other (describe): APCD- 211T Interior stack depth (inches): :COLORADO JIMIlt H. Hea.rt.wmaauNw °,atvr*m Permit Number: 13WE 1101 14 AIRS ID Number: 123 I 9AC21004 Section 6 - Control Device Information ❑ Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. Vapor ❑ Recovery Unit (VRU): Pollutants Controlled: Size: Requested Control Efficiency: VRU Downtime or Bypassed (emissions vented): Make/Model: Q Device: Combustion Pollutants Controlled: VOC, HAPs Rating: 0.40 Type: 4 LEED and 1 Cimarron MMBtu/hr Make/Model: 48" and 48" HVECD Requested Control Efficiency: 95 Manufacturer Guaranteed Control Efficiency: 99 Minimum Temperature: 500 Waste Gas. Heat Content: 405 Btu/scf MMBtu/hr Constant Pilot Light: O Yes ❑ No Pilot Burner Rating: NIA O Closed Loop System Description of the closed loop system: O Other: Pollutants Controlled:. Description: Control Efficiency Requested: Section 7 - Gas/Liquids Separation Technology Information (E&P Sites Only) What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? —50 psig Describe the separation process between the well and the storage tanks: Well head liquid is routed to (2) single stage separators and (1) 2 -stage separators, then directed to tanks COLORADO Oepw.fmmtal wwce NISM 42nnfmmmu Permit Number: 13WE1101 1101 14 AIRS ID Number: 123 I 9AC2 / 004 Section 8 - Criteria Pollutant Emissions Information Attach all emissions calculations and emission factor documentation to this APEN form7. Is any emission control equipment or practice used to reduce emissions? D Yes 0 No If yes, describe the control equipment AND state the collection and control efficiencies (report the overall, or combined, values if multiple emission control methods were identified in Section 6): Pollutant Control Equipment Description Collection Efficiency (% of total emissions captured by control equipment) Control Efficiency (% reduction of captured emissions) VOC ECD 100% 95% NOx CO HAPs ECD 100% 95%. Other: From what year is the following reported actual annual emissions data? Projected 2020 Use the following table to report the criteria pollutant emissions from source: Pollutant Emission Factor7 Actual Annual Emissions Requested Annual Permit Emission Limit(s)3 Uncontrolled Basis Units Source (AA 42, Mfg., etc) Uncontrolled Emissions (tons/year) Controlled Emissionsg (tons/year) Uncontrolled Emissions #buns/year) Controlled Emissions (torn/year) VOC 0.282 Ibttibt State Default 8.57 0.43 10.28 0.52 NOX 0.0037 lb/bbl State Default 0.12 0.12 0.14 0.14 CO 0.0167 Ibfbbl State Default 0.55 0.55 0.66 0.66 5 Requested values will become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on all APENs, including APEN updates. 7 Attach produced water laboratory analysis, stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. 8 Annual emission fees will be based on actual controlled emissions reported. if source has not yet started operating, provide projected emissions. Section 9 - Non -Criteria Pollutant Emissions Information Does the emissions source have any uncontrolled actual emissions of non -criteria pollutants (e.g. HAP - hazardous air pollutant) equal to or greater than 250 lbs/year? 0 Yes ❑ No If yes, use the following table to report the non -criteria pollutant (HAP) emissions from source: Chemical Name Chemical Abstract (CAS) ServiceUnits Number Emission Factor' Actual Annual Emissions Uncontrolled Basis Source (AP -42, Mfg., etc.) Uncontrolled Emissions (lbs/year) Controlled Emissions8 (lbs/year) Benzene 71432 0.0070 191051 State Default 456 24 Toluene 108883 NA NA NA NA NA Ethylbenzene 10O414 NA NA NA NA NA Xylene 1330207 NA NA NA NA NA n -Hexane 110543 0.0220 198051 State Default 1,440 72 2,2,4-Trimethylpentane 540841 NA NA NA NA NA 7 Attach produced water laboratory analysis, stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. 8 Annual emission fees wilt be based on actual controlled emissions reported. If source has not yet started operating, provide projected emissions. i ^COLORaA aDO pmnmemwtar .,nq envvme.,x Permit Number: 13 W E 1101 14 AIRS ID Number: 123 / 9AC2 i 004 Section 10 Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP05 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable General Permit. Signature of Legally Authorized Person (not a vendor or consultant) Date Alisson Soehner Environmental Engineer, Air Quality Name (print) Title Check the appropriate box to request a copy of the: El Draft permit prior to issuance Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Send this form along with $191.13 and the General Permit registration fee of $312.50, if applicable, to: Colorado Department of Public Health and Environment Air Pollution Control Division APCD-SS-B1 4300 Cherry Creek. Drive South Denver, CO 80246-1530 Make check payable to: Colorado Department of Public Health and Environment For more information or assistance call: Small Business Assistance Program (303) 692-3175 OR (303) 692-3148 APCD Main Phone Number (303) 692-3150 fir tt 1,4 '.COLORADO Jawaep itMm s w.bh N4YU 6Cnv.tonmfM Hydrocarbon Liquid Loading APED LIVED Form. APCD-208 Air Pollutant Emission Notice (APEN) and AN 2 8 2420 Application for Construction Permit APCD Stationary Alt sections of this APEN and application must be completed for both new and existing facilities, including APEN Bounces updates. Incomplete APENs will be rejected and wilt require re -submittal. Your APEN will be rejected if it is filled out incorrectly, is missing information, or lacks payment for the filing fee. The re -submittal will require payment for a new filing fee. This APEN is to be used for hydrocarbon liquid loading only. If your emission unit does not fall into this category, there may be a more specific APEN for your source (e.g. amine sweetening unit, glycol dehydration unit, condensate storage tanks, etc.). In addition, the General APEN (Form APCD-200) is available if the specialty APEN options will not satisfy your reporting needs. A list of all available APEN forms can be found on the Air Pollution Control Division (APCD) website. This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: 13WE 1101 14 AIRS ID Number: 123 / 9AC2 / 006 I Section 1 - Administrative Information Company Name': Bonanza Creek Energy Operating Company, LLC Site Name: Latham 14-12 Production Facility (COGCC #429825) Site Location: 40.32039, -104.39238 SWSW, T4N, Sec 12, 63W Mailing Address: (Include Zip Code) 410 17th Street, Suite 1400 Denver, CO 80202 Site Location County: Weld NAICS or SIC Code: 1311 Contact Person: Alisson Soehner Phone Number: (303) 803-1752 E -Mail Address: asoehner@bonanzacrk.com 1 Use the full, legal company name registered with the Colorado Secretary of State. This is the company name that will appear on all documents issued by the APCD. Any changes will require additional paperwork. 2 Permits, exemption letters, and any processing invoices will be issued by the APCD via e-mail to the address provided. 424783 COLORADO AMP MrDe urn wuic ,'Ha. 6bnr.wnw.nx Permit Number: 13WE1101 14 AIRS ID Number: APCD 123 /9AC21006 Section 2 - Requested Action ❑ NEW permit OR newly -reported emission source ❑ Request coverage under construction permit O Request coverage under General Permit GPO7 If General Permit coverage is requested, the General Permit registration fee of $312.50 must be submitted along with the APEN filing fee. -OR- 0 MODIFICATION to existing permit (check each box below that applies) ❑ Change fuel or equipment ❑ Change company name3 O Change permit limit ❑ Transfer of ownership' O Other (describe below) -OR - ❑ APEN submittal for update only (Note blank APENs will not be accepted) - ADDITIONAL PERMIT ACTIONS - ❑ Limit Hazardous Air Pollutants (HAPs) with a federally -enforceable limit on Potential To Emit (PTE) Additional Info & Notes: Updating throughput to account for new well 3 For company name change, a completed Company Name Change Certification Form (Form APCD-106) must be submitted. 4 For transfer of ownership, a completed Transfer of Ownership Certification Form (Form APCD-104) must be submitted. Section 3 - General Information General description of equipment and purpose: Return Line for control of Truck Loadout Vapors Company equipment Identification No. (optional): L-01 For existing sources, operation began on: 9/28/2012 For new or reconstructed sources, the projected start-up date is: Will this equipment be operated in any NAAQS nonattainment area? Yes No SI ■ is this equipment located at a stationary source that is considered a Major Source of (HAP) emissions? Yes 0 No • Does this source load gasoline into transport vehicles? Yes 0 No ■ Is this source located at an oil, and gas exploration and production site? 0 Yes No ■ If yes: Does this source load less than 10,000 gallons of crude oil per day on an annual average? Yes No ® ■ Does this source splash fill less than 6,750 bbl of condensate per year? Yes No El ■ Does this source submerge fill less than 16,308 bbl of condensate per year? Yes No ■ p goCOLORADO Permit Number: 13WE1101 I4 AIRS ID Number: 123 / 9AC2 / 006 Section 4 - Process Equipment Information Product Loaded: ❑ Condensate O Crude Oil O Other: If this APEN is being filed for vapors displaced from cargo carrier, complete the following: Requested Volume Loaded5: 78,475 bbl /year Actual Volume Loaded: This product is loaded from tanks at this facility into: tank trucks (e.g. "rail tank cars" or "tank trucks") 78,475 bbl/year If site specific emission factor is used to calculate emissions, complete the following: Saturation Factor:Average N/A temperature of bulk liquid loading: NSA F True Vapor Pressure: N/A Psia ® 60 `F Molecular weight of displaced vapors: NIA lb/lb-mot If this APEN is being filed for vapors displaced from pressurized loading lines, complete the following: Requested Volume Loaded5: bbl /year Actual Volume Loaded: bbl/year Product Density: lb/ft3 Load Line Volume: ft3/truckload Vapor Recovery Line Volume: ft3/truckload 5 Requested values will become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on all APENs, including APEN updates. Section 5 - Geographical/Stack Information Geographical Coordinates (Latitude/Longitude or UTM) 40.32039,-104:39238 ❑ Check box if the following information is not applicable to the source because emissions will not be emitted from a stack. If this is the case, the rest of this section may remain blank. �O,pe aat Disc'rar° H hi. ov f 'lfem Flo jet a elo�rF ECD 01-05 25 500 TBD TBD Indicate the direction of the stack outlet: (check one) Upward ❑ Downward ❑ Horizontal 0 Other (describe): Indicate the stack opening and size:. (check one) ❑✓ Circular ❑ Square/rectangle ❑ Other (describe): 0 Upward with obstructing raincap Interior stack diameter (inches): 48 Interior stack width (inches): Interior stack depth (inches): > COLORADO e,p.w,u ar�K NwIM fi G+imnmmt Permit Number: 13WE 1101 14 AIRS ID Number: 123 t 9AC2 1006 Section 6 - Control Device Information O Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. 0 Loading occurs using a vapor balance system: Requested Control Efficiency: 100 1] Combustion Device: Used for control of: VOC, HAPs Rating: 0.035 MMBtu/hr Type: 4 LEED and 1 Cimarron Make/Model: 48" and 48" HVECD Requested Control Efficiency: 95 Manufacturer Guaranteed Control Efficiency: 99 % Minimum Temperature: 500 'F Waste Gas Heat Content: 3,001 Btu/scf Constant Pilot Light: O Yes 0 No Pilot Burner Rating: N/A MMBtu/hr O Other: Pollutants Controlled: Description: Requested Control Efficiency: Section 7 - Criteria Pollutant Emissions Information Attach all emissions calculations and emission factor documentation to this APEN form. Is any emission control equipment or practice used to reduce emissions? 1] Yes O No If yes, describe the control equipment AND state the collection and control efficiencies (report the overall, or combined, values if multiple emission control methods were identified in Section 6): Pollutant Control Equipment Description Collection Efficiency (% of total emissions captured by control equipment) Control Efficiency (% reduction of captured *missions) PM SOx NOx CO VOC ECD 100% 95% HAPs ECD 100% 95% Other: 1 Using State Emission Factors (Required for GP07) VOC Benzene n -Hexane ❑✓ Condensate 0.236 Lbs/BBL 0.00041 Lbs/BBL 0.0036 Lbs/BBL ❑ Crude 0.104 Lbs/BBL 0.00018 Lbs/BBL 0.0016 Lbs/BBL From what year is the following reported actual annual emissions data? Projected 2020 Use the following table to report the criteria pollutant emissions from source: Pollutant Emission Factor Actual Annual Emissions Requested Annual Permit Emission Limit(s)5 Uncontrolled Basis Units Source (AP -42, Mfg., etc.) Uncontrolled Emissions (tans/year) Controlled Emissions6 (tans/year) Uncontrolled Emissions (tons/year) Controlled Emissions (toeslyear) PM 40 ugh AP -42 <0,01 <0.01. <0.01 <0.01 SOx 0.00019 lb/MMBtu AP -42 <0.01 <0,01 <0.01 <0,01 NO„ 0:068 ib/MMBtu AP -42 0.011 0.011 0.011 0.011 CO 0.310 tb/MMBtu AP -42 0.049 0.049 0.049 0.049 VOC 0.236' lb/bbl State Default 9.26 0.47 9;26 0;47 5 Requested values wilt become permit limitations or will be evaluated for exempt status, as applicable, and should consider future process growth. Requested values are required on all APENs, including APEN updates. 6 Annual emission fees will be based on actual controlled emissions reported. If source has not yet started operating, provide projected emissions. COLORADO : Permee edwaK Es. i' - :<ewmnw�x ec. Permit Number: 13WE1101 14 AIRS ID Number: 123 /9AC2/006 Section 8 - Non -Criteria Pollutant Emissions Information Does the emissions source have any uncontrolled actual emissions of non -criteria pollutants (e.g. HAP - hazardous air pollutant) equal to or greater than 250 tbs/year? rB Yes ❑ No If yes, use the following table to report the non -criteria pollutant ('HAP) emissions from source: Chemical Name Chemical Abstract Service (CAS) Number Emission Factor Actual Annual Emissions Uncontrolled Basis Units Source (AP -42, Mfg., etc.) Uncontrolled Emissions (lbs/year) Controlled Emissions6 (lbs/year) Benzene 71432 0.00041 lb/bbl State Default 33 2 Toluene 108883 N/A N/A N/A NIA N/A Ethylbenzene 100414 N/A N/A NIA N/A N/A Xylene 1330207 N/A N/A N/A N/A N/A n -Hexane 110543 0:0036 lb/bbl State Default 283 15 2,2,4-Trimethyipentane 540841 N/A N/A N/A N/A N/A Other: 6 Annual emission fees will be based on. actual controlled emissions reported. If source has not yet started operating, provide projected emissions. Section 9 - Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP07, I further certify that this source is and will be operated in full compliance with each condition of General Permit GP07. Signature of Legally Authorized Person (not a vendor or consultant) Date Alisson Soehner Environmental Engineer, Air Quality Name (print) Title Check the appropriate box to request a copy of the: [jr Draft permit prior to issuance Q Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5) years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, ILC. for revised APEN requirements. Send this form along with $191.13 and the General Permit registration fee of $312.50, if applicable, to: Colorado Department of Public Health and Environment Air Pollution Control Division APCD-SS-B1 4300 Cherry Creek Drive South Denver, CO 80246-1530 Make check payable to: Colorado Department of Public Health and Environment For more information or assistance call: Small Business Assistance Program (303) 692-3175 OR (303) 692-3148 APCD Main Phone Number (303) 692-3150 100;COLORADO .9.0Intent Pub. >:: Heath Ermtmnnt Colorado Air Permitting Project PRELIMINARY ANALYSIS-PROJECT SUMMARY Project Details For Division Use Only Review Engineer: Tteg a W Package#: liiiiG : is ti Received Date: 1/2 Review Start Date: 2/2S/20?." Section 01-Facility Information Company Name: En+ t CpeBnCompany,LLC Quadrant Section Township Range County AIRS ID: •>',yl - SWsr,fifg r f4 12 63 Plant AIRS ID: m Facility Name: C#429825) Physical Address/Location: SWSW quadrant of Section 4N,Township 12,Range 63W County: Weld County Type of Facility: RiDerration&Product?on Well Pad - ir - What industry segment Oil&Natural Gas Prc,<sductron&Processing =f Is this facility located in a NAAQS non-attainment area? Yes . If yes,for what pollutant? Ozone 41yc x&VtdC} Section 02-Emissions Units In Permit Application Leave Blank-For Division Use Only AIRS Point II Permit ft (Leave blank unless Emissions (Leave blank unless Issuance Self Cert Engineering Emissions Source Type Equipment Name Action APCD has already Control? APCD has already f; Required? Remarks assigned) assigned) Permit Aq1i F •003 o d s e Tarn' '. Yes 'Yes Modification wer' °t . -3,-1;f4•044 v z,r , Point t}eifl " convertedf im Permit initial GF0S to C O04 Produced Water Tank PWT-01 Yes 13WE110]. Yes Issuance coverage �r Permit 006 Liquid Loading - L-01 Yes E 1Q :4''5 Yea Modification See technical i anal ysi n to 013 5peeat� Venting LP FL s ', `tea .� - .tea Canceilitftr4 onpptq, s! Section 03-Description of Project This facility is U.pdatitr f wide permit to account i7,7— ,e S hput due to t a - occur in late spring' Ily,upon re-evaluation ofthe facilityset-vp,it wasatietermined that the low presser''dsf;or a po not be con i , ne tin point and it was subsequently cancelled and removed from this per mit.This facility 7i et c rtts require t go t¢, ub WiRT-TV as the source is newly requesting a federally en#oi ceahe synch t c frr + e fizot ��stU��f�irte7i�dAf. 5t}toy.The facility was prev•rously permitted as a synthetic mrn t st� �r e�z�t{'t�. Sections 04,OS&06-For Division Use Only Section 04-Public Comment Requirements • Is Public Comment Required? _ Yea If yes,why? ,Requesting Synth3 j sr Permit v Section 05-Ambient Air Impact Analysis Requiremer Was a quantitative modeling analysis required? Np If yes,for what pollutants? If yes,attach a copy of Technical Services Unit modeling results summary. Section 06-Facility-Wide Stationary Source Classification Is this stationary source a true minor? P a Is this stationarysource a synthetic minor? If yes,indicate programs and which pollutants: SO2 NOx Co VOC PM2.5 PM10'TSP HAPs Prevention of Significant Deterioration(P5D) 0 0 0 0 0 ❑ Title V Operating Permits(OP) 0 0 ❑ l 0 ❑ ❑ -0 Non-Attainment New Source Review(NANSR) ❑ IS Is this stationary source a major source? If yes,indicate programs and which pollutants: S02 NOx CO VOC PM2.5 PM10 TSP HAPs Prevention of Significant Deterioration(PSD) 0 0 ❑ 0 ❑ . O Title V Operating Permits(OP) ❑ 0 0 0 0 000 Non-Attainment New Source Review(NANSR) ❑ 0 Condensate Storage Tank(s)Emissions Inventory Section 01.-Administrative Information ` Facility Allis ID ,.' • .$AC2 ,,,✓n 303 ,1 County Plant Point Section 02-Equipment Description Details Detailed Emissions Unit 'd+(afiee(St)1}p'htf\af . ue sseaa �F��st�orogn afi euodengsa₹a Pgt,u3ds �' Description: ..\.\\\ \� Emission Control Device / ////� ��\ ///),Z ////// / Description: ';,,r, / / �%/� �.� z�.b'f. Requested Overall VOC&HAP Control Efficiency%: it.:.,.\\Rki:A.Siv/7///7„A 03-Processing Rate Information for Emissions Estimates Primary Emissions-Storage Tank(s) Actual Condensate Throughput= / so Barrels(bbl)per year 'Requested Permit Limit Throughput= s r3.i7 Barrels(bbl)per year Requested Monthly Throughput= 6655,0 - Barrels(bbl)per month Potential to Emit(PTE)Condensate Throughput= 4S Barrels(bbl)per year Secondary Emissions-Combustion Device(s) Heat content of waste gas= 0d;.o Btu/scf Volume of waste gas emitted per BBL of n" liquids produced= 159,6''..scf/bbl Actual heat content of waste gas routed to combustion device= 26,111.$MMBTU per year Requested heat content of waste gas routed to combustion device= 31,334,1 MMBTU per year Potential to Emit(PTE)heat content of waste gas routed to combustion device= 31,334.1 MMBTU per year I Control Device Pilot Fuel Use Rate: / &fs cfh 0.7 MMscf/yr Seonilsustors @ 16.8 sef/hr ,; Pilot Fuel Gas Heating Value: � 2301;;Btu/scf 2134,7 MMBTU/yr Section 04-Emissions Factors&Methodologies Will this storage tank emit flash emissions? Emission Factors Condensate Tank Uncontrolled Controlled Pollutant (lb/bbl) (lb/bbl) Emission Factor Source (Condensate (Condensate Throughput) Throughput) VOC 6/'M0500 0.5130 5s'tr5peccbd,€,E$iaoclstav ifvdh)//*:-..-.i . Benzene 110657 0.0033 5 S1vc5f1cE ::(aiaclodot loch) Toluene £1.0455 0.0025 5ZtmT)3eci'hpEF4iovlo APlo4Er1/•/44 f8 Ethylbenzene 0.0061 0.0003 Sit;Specifac8Er:firi8f1( 'flog(4'g13' > Xylene 0.0104 0,0005 S€ .6 eciflc E.8.088)a046ftashfS 4° n-Hexane • :0,1094 0.0205 SECS E.F.:)fnctudvu1louhy 224TMP 00019 0.0601 �.., PT-(fncfp*uflosh! Control Device Uncontrolled Uncontrolled Pollutant (Ih/MMBtu) (Ih/hhl) Emission Factor Source (waste heat (Condensate combusted) Throughput) PM10 t 75 0.00 0 `RkT11 PM2.5 069750 0.0030 tTi& 3; P1v NOx E5RRRtt - -0.0272 '4 ,. CO `..109 0.1238 WN€2 Pilot Light Emissions Uncontrolled Uncontrolled Pollutant (lb/MMBtu) (lb/MMscf) Emission Factor Source (Waste Heat (Pilot Gas Combusted) Throughput) PM10 00075 216153 i1P4ZTopSu1A-2)f 10/YM2.5} PM2.5 0,0075 21.6155 #s4T a�*2'•"- OT 2'5 NOx 0.4680 18`s 2630 �i��` CO ;4';,,,.0,3'104 593 3100 ;Sr', Section 05-Emissions Inventory Potential to Emit Actual Emissions Requested Permit Limits Requested Monthly Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled Controlled (tons/year) (tons/year) (tons/year) (tons/year) (tons/year) (lbs/month) VOC 669.4 557.8 27,9 869,4 33,5 56852 PM10 0,1 0.1 0.1 0,1 0.1 21.2 PM2.5 5.1 .0,1 0.1 0,1 0.1 21,2 NOx 1.1 1.0 1.0 1.1 1.1 193.3 CO 5,2 4,4 4.4 5.1 5,2 881.2 Potential to Emit Actual Emissions Requested Permit Limits Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled (Ibs/year) (lbs/year) (lbs/Year) (Ibs/year) fibs/Year) Benzene 5155.8 4296.5 214.8 51555.2 257.3 Toluene 3884,5 3737,1 161..0 3804,0 154.2 Ethylbenzene 487.4 406.2 20.3 487,4 24.4 Xylene 815.4 679,5 34,0 815.4 40.8 2 of 13 C:\Users\Ilakocy\Desktop\Remote Working Docs\Package 4424786\13WE1101.CP5 Condensate Storage Tank(s)Emissions Inventory n-Hexane I 32127.7 I 26773,1 1333.7 I 32127,7 I 1606.4 224 TMP 149.1 124.3 6.2 149.1 7.5 • • • • 3 of 13 C:\Users\Ilakocy\Desktop\Remote Working Dons\Package#424786\13WE1101.CP5 Condensate Storage Tank(s)Emissions inventory Section 06-Regulatory Summary Analysis Regulation 3,Parts A,B Source requires a permit Regulation 7,Section XII.C,D,E,F Storage took is subject to Regulation 7,Section 511.0-F Regulation 7,Section XI I.G,C Storage Tank is not subject to Regulation 7,Section 011.0 Regulation 7,Section XVII.B,C.1,C.3 Storage took is subject to Regulation 7,Section XVII,B,0.1&C3 Regulation 7,Section XVII.C.2 Storage tank is subject to Regulation 7,Section 0011.0.2 Regulation 6,Part A,HOPS Subpart Kb Storage Took Is not subject to NSPS Kb Regulation 6,Part A,NSPS Subpart 0000 Storage Took is not subject to SOPS€0000 NSPS Subpart OOOOa Storage tonk is not subject to NSPS OOOO0. Regulation 8,Part E,MACF Subpart HH Storage Tank is not subject to AMACT HI-I (See regulatory applicability worksheet for detailed analysis) Section 07-Initial and Periodic Sampling and Testing Requirements Does the company use the state default emissions factors to estimate emissions? iEs " If yes,are the uncontrolled actual or requested emissions estimated to be greater than or equal to80 tons VOC per year? If yes,the permit will contain an"Initial Compliance"testing requirement to develop a site specific emissions factor based on guidelines in PS Memo OS-01. Does the company use a site specific emissions factor to estimate emissions? rs If yes and if there are flash emissions,are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted?This sample should be considered representative which generally means site-specific and collected within one year of the application received date.However,if the facility has not been modified(e.g.,no new wells brought on-line),then it may be appropriate to use an older site-specific sample. If no,the permit will contain an"Initial Compliance"testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. - g.`y Does the company request a control device efficiency greater than 95%for a flare or combustion device? If yes,the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 Technical Analysis Notes 4.24 ,suri'e'd Iq. 'taken 101d4t2 • )('159 psIS,134 F3 upstream of pg,.•: age seMr;g9,0" •oam one of the aaasClW r 4 The,&ayrae then,mpr• the hi r1..ss reside /,sap futar�at\\ X63 r and t&;', lid the oil taxi *duding working/breuuhinge)rilsslons.Initiatlytbe source had modeled tl ti tar ing brbating'emissipi eFl on 9 4• I)o)s C wave? k�c u�ethei� 46qu1d 1'itpn o „qie.509,,,,,,„.61AgiaQlrii iereforellaveaer-vapar'space ar�d7ikeljmar�e 4farking/6reat}lap�.4ns 1'he 5aures'r',esilb �d there �ssiarrs eafculatkens auks whic�l� _zaceptzd �6 _ jjii :�i ,� /. `\•;a, '-?„%////% ...%/i`'. 0 r re psis being apmrtiingleii•.W, x- prage#ahkcfi•;§, kheatt "adfiaxihty diagram,the awe '770/5,-'5.trdttssaywl)not hepertratted separatety,buttbas�ercrl5j ..S;� i i j Bred w7Eh.the tams tosissignf as?�is t afitted f (i t� o vslog,dK i�ss�agesepsrator to its lull cape0J•fy u k 44,.r€ot:i#O je'tontgtir the'eparated"law pressnro 8M t,,thraagh Tile taa•Rxr The n iN sa Dded to kiss, chi le;tage epa*is.'The source will 6'•••••."' e.,bsamplef'rat�rtitti%f^�sx�g25tage�sample point 3"&madel�hetan�r��//�I�,EsnsframxMe•e�tlstlr�J�ath1 .,�1,,�,:well,ands\nt�le�,f• Ex4st;r� •e(Ps3gnlertageseP •s�r�t iftt"and,,";,VW 7/7/10'tt asoU.4nedontheattachdfaafii.Ati.0r7�i s art of 1130.4f cerdf.4140,P. ciitra049.they$urc .pulre uEatnit pewAPEN:f 440;ndQnsajgt nk \ q s�GYtc��jrii�stpltfacturs 6asedontteslfe=,s'peel7¢�afnplas/madalingand�welghUn � e 1�erenEs3re>attis' fipu�� age th,r so-urce'is so close ka iW—iotdfor required addltlanal moretonng pert?&�"ee if perini4ie,*le will be PegUtrod. •i"••""" ••• jj\ Theyalu4s₹arthe HAps'diffesligittlyartthapa��nrcfram tho gd adtive,likely due taminnijo .es.q 02#0..v thz sefuYce ;,. Pee haesaurce•and COGCC s website,Lethal-04512(APt7105`#.23 35$47,)which was onginally - .e Mugged an8 aban c.4.,,t1,-.4%6xs who.(;Is well;snot included within r tRe tesfllTg can dltrpry ..:-.. 4\""'"'/i/•,. ,,, / t % �� a �� Section 09-Inventory 5CC Coding and Emissions Factors Uncontrolled Emissions AIRS Point# Process# 5CC Code Pollutant Factor Control%Units 003 01 ,,,�,_-e,,,�,. � ��s � � , 311:11��s;�� ---_ PM10 0.08 0 lb/1,000 gallons condensate throughput PM2.5 0,170 0 1b/1,000 gallons condensate throughput NOx O.50 0 lb/1,000 gallons condensate throughput VOC 40€1.2 95 lb/1,000 gallons condensate throughput CO 0.15 0 lb/1,000 gallons condensate throughput Benzene 1.56 95 lb/1,000 gallons condensate throughput Toluene 1,10 95 lb/1,000 gallons condensate throughput Ethylbenzene 0,15 95 16/1,000 gallons condensate throughput Xylene 0,25 95 lb/1,000 gallons,condensate throughput n-Hexane 9.75 95 lb/1,000 gallons condensate throughput 224 TRAP 0.05 95 lb/1,000 gallons condensate throughput 4 of 13 - C:\Users\Ilakocy\Desktop\Remote Working Does\Package#424786\13 WE1101.CPS Received 4/7/2020 P-64 To Gas Gathering Pipeline y t7 Tank Vapors to Enclosed Flare............................. _........r._.__.._....._._.._..__............................ Flow Meter ECDs Existing 2-stage Sample',tint 2 low Pressure Gas Enioting 2-stage Sample Point 1 \\I Truck Wit to Tanks CorEdensate Tanks Well-head fluid onto Sterage-linke Existing Well 2-stage Oil Truck Loadout Latham O-K-12HNB separator43 1_ ■ _F mWater drains to vaults during truck lnadout t- - 1 oil to Storage Concrete Vaults Tanks `� (uncontrolled) Well-head fluid Single-Stage Separator Existing Well P 6 PW Tanks Latham 14-11-12HZ � _- _ Palming We:I Single tags Pr Jutrd Water Spsample Point Produced Water Water Trucked Out rt 11 Well-head fluid Single-Stage on to Storage Tanks 411. Separator New Well Produced Water Latham F11-J14-14HNB P New Well Sample Point Latham 14-12 Production Facility s. SW%SW%Sec. 12,T4N, R63W Weld County,Colorado Received 3/10/2020 T rdel • ❑- x F `-'1JAPYSIQ S'�dFf£dd'br'$PaYc9T2ffiY9h°P3tih�Rtdr�/1911eG LU2tIfiY C6SAAM:9ilECQr5'� ..y R2�»tY LH ... .. .• mcsult iaorkn�d Hrat'tl 4v � - . � 4 � r}�Regart[Fta�R�a+,j tt+rn�s .-. , Urns PrctessSdeani _...... ........ _.._ (Masked tirn:id ..... Y.... ......... ... .............. ..... ........ .. ....... ......... ......... ........ .... ..... ......................... ........ .................................... .. Tape GeOtr tr'dpel Cylinder,. Ebel Length. .. .. .. ... ... ... ... Number of Storage Tanks Employed i Y . Lode-Gan . r 'Erne Frame jYear .._R partC portents: Ali - .................. ..... Set Belk Temperatre to Stream Temperature? I r ', Use AP42Reou't's Vap a Pressure?:. .... .. - -......- te T,,,,, -. ...Me F aen F81 fTank ....... ... .... .. .. ...9g AperageFracton 5N f7a,k: I SG 5ti, Morena!Categary link C>a rod a -- - Shed Paint Conrltoo i Good t Breather\e-itP .....1 g•D p g Breather Vawem Pressure 7.83 Poe poofTyPe Ewe Slope of Coned Roof I0.0oS Roof C !Teo Roof P iC dlfiort Good Flashing Temperature i 66.18; r L5,5 ✓N Calndale Loading Lasses? 1- Qutput Flashing Losses? I r - - - Output 6 os55,g,E dung tosses E • Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 1 of 1 • ..• .... :,_,: 9 •5 4,. .. 4 R c ve Y • :- �� ;: .; P .; *lam i an°, 5 .T ..,,,,;s ue�r_ ti • ts, • ._ r:.r •'• PCankSchema is f Cllent Name: , ,. :' Bonanza Creek ::" ,. ass o t , Location: Latham'14-12 �a.*.,,4 ;` ,:.:.. '" Job'•Flowsheet: Flows heet1 : „'.: $ a • / n T,ait-planK,;;Nr PStreams"Total Tank Emissions"/"Flashed Liquid"Entire Vapor Stream EF=137.8 SCF/bbl Latham 14-12 Production Facility Bonanza Creek Energy Operating Company, PStreams"Total Tank Emissions"/"Flashed Liquid"VOCs EF=17.06 lb/bbl LLC PStreams"Total Tank Emissions"/"Flashed Liquid"Benzene EF=0.06565 lb/bbl PStreams"Total Tank Emissions"/"Flashed Liquid"Toluene EF=0.04954 lb/bbl PStreams"Total Tank Emissions"/"Flashed Liquid"Ethylbenzene EF=0.006214 lb/bbl PStreams"Total Tank Emissions"/"Flashed Liquid"Xylenes EF=0.01039 lb/bbl Properties Sales Gas Std Vapor Volumetric Flow(Total)I 0.022957 IM,M1SCFD PStreams"Total Tank Emissions"/"Flashed Liquid"n-Hexane EF=0.4094 lb/bbl Properties Total Tank Enissions Std Vapor Volumetric Flow(Totel)I 0.029619 I MMSCFD PStreams"Total Tank Emissions"P'Flashed Liquid"2,2,4-Trimethylpentane EF=0.00185 lb/bbl Sales Gars—► Tana Flash Gas Total Tank Emissions --► MIX-100 Separator 'Breathing Losses Pressurized Liquid -- To Tanky--►}," --1---- oil Tank Annual tank loss calculations for"Flashed Liquid". — Total working and breathing losses from the Vertical Cylinder are 25.25 ton/yr. — VLVE-100 "All components are reported. Tank-1 Flashed Liquki r "Total Tank Emissions"C3+Mass Flow=669.4 ton/yr Properties Flashed Liquid Narnes Units Total Tank Emissions Tank Flash Gas Std Liquid Volumetric Flow(Total)l 215 I bbl/d CO2(Mass Row) ton/yr 3.6079 3.4861 Methane(Mass Flow) ton/yr 6.503 6.4202 Benzene(Mass Flow) ton/yr 2.576 2,5288 Toluene(Mass Flow) ton/yr 1.9437 1.9088 tahylbenzene(Mass Row)• ton/yr 0.24382 0.23938 o-Xylene(Mass Row) ton/yr 0.40764 0.40156 Hexane(Mass Row) toNyr 16.063 15.615 2,2,4-Trinethylpentane(Mass Row)ton/yr 0.072571 0.070714 • *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright d 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pnix Page 1 of 10 Process Streams Report ' • 1 All Streams Tabulated by Total Phase " Client Name: -_Bonanza Creek . :fob: Location: :_Latham14-12 . Flowsheet: _Flowsheetl . SO�� '72 Vt/iii.,,.,, ... ,,-..'W, .. .; �//1i,i�...�__.. ..o•. ;-Wo.�,.... ,,, ,.7.T.,, i,,,, Connections Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas From Block -- Oil Tank -- Separator Oil Tank To Block MIX-100 -- Separator -- MIX-100 4 iii...: `, -4 . `:,�,,Z\ s Stream Composition Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas Mole Fraction %n %u % % °/n CO2 0.548105 0.00560539 0.3539 * 2.27998 0.576542 Nitrogen 0.00182532 2.6981E-05 0.0607999 * 0.495669 0.0202611 Methane • 1.02186 0.0111667 3.5109 * 26.3927 2.91289 Ethane 18.4608 0.283554 5.12119 * 25.7377 13.1441 Propane 37.7861 2.6967 10.3682 * 27.3267 35.7351 i-Butane 6.08632 1.23184 2.1785 * 2.93761 6.38034 n-Butane 21.5125 6.43061 9.17929 * 9.21239 23.1242 i-Pentane 4.3143 3.60543 3.5725 * 1.59707 4.99248 n-Pentane 5.1759 5.9289 5.50149 * 1.92674 6.20154 Cyclopentane 0.421561 0.800961 0.686499 * 0.158169 0.52924 Hexane 1.02941 4.30706 3.4166 * 0.39451 1.31884 Cyclohexane 0.266604 1.76868 1.375 * 0.115159 0.386261 Isohexane 2.18928 6.41556 5.23579 * 0.824353 2.78396 Heptane 0.577398 8.69418 6.57279 * 0.269142 0.85518 Methylcyclohexane 0.192648 2.8256 2.1359 * 0.0856562 0.277647 2,2,4-Trimethylpentane 0.00321998 0.0437373 0.0331 * 0.00139719 0.00450579 Benzene 0.119617 0.825078 0.651399 * 0.0701915 0.235633 Toluene 0.0754677 1.86421 1.4034 * 0.0473815 0.150767 Ethylbenzene 0.00829091 0.631302 0.469 * 0.00556998 0.0164115 o-Xylene 0.0113459 1.32461 0.982799 * 0.00943819 0.0275302 Octane 0.162665 8.57486 6.37789 * 0.0895783 0.263821 Nonane 0.0348517 6.43001 4.7578 * 0.0228999 0.0627406 C10+ 8.49735E-07 35.3003 26.0553 * 4.98472E-06 5.73417E-06 C11AIkanes(normal) 0 0 0 * 0 0 C12AIkanes(normal) 0 0 0 * 0 0 Cl3Alkanes(normal) 0 0 0 * 0 0 C14 0 0 0 * 0 0 C15 0 0 0 * 0 0 C16 0 0 0 * 0 0 C17 0 0 0 * 0 0 C18 0 0 0 * 0 0 C19 0 0 0 * 0 0 C20 0 0 0 * 0 0 C21 0 0 0 * 0 0 C22 0 0 0 * 0 0 C23 0 0 0 * 0 0 C24 0 0 0 * 0 0 C25 0 0 0 * 0 0 C26 0 0 0 * 0 0 C27 0 0 0 * 0 0 C28 0 0 0 " 0 0 C29 0 0 0 * 0 0 C30 0 0 0 * 0 0 C31 0 0 0 * 0 0 C32 0 0 0 * 0 0 C33 0 0 0 * 0 0 C34 0 0 0 * 0 0 C35 0 0 0 * 0 0 C36 0 0 0 * 0 0 Decane 0 0 0 * 0 0 Zkiir i/; LW Z//" t /,Air i , " c��y ��E i 4 , ire;Altar'. NM`M, *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbI tanks.pmx Page 2 of 10 Process Streams Report All Streams Tabulated by Total Phase Client Name: , Bonanza Creek ••. Job: '• Location: Latham 14-12 Flowsheet: Flowsheetl ;3.0 \\W,1. o ,m 6,,,--,:-.:17.5t,' r"111Pk' yz2 loll✓%/ \ Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas Molar Flow lbmol/h lbmol/h Ibmol/h Ibmol/h Ibmollh CO2 0.000365715 0.000893736 0.0764481 * 0.0574695 0.0180848 Nitrogen 1.21792E-06 4.30191E-06 0.0131338 * 0.0124939 0.000635546 Methane 0.00068182 0.00178044 0.758411 * 0.66526 0.0913707 Ethane 0.0123177 0.0452105 1.10626 * 0.648749 0.412302 Propane 0.0252122 0.429969 2.2397 * 0.6888 1.12093 i-Butane 0.00406101 0.196408 0.470591 * 0.074046 0.200137 n-Butane 0.0143539 1.02531 1.98288 * 0.232209 0.725355 i-Pentane 0.00287865 0.574858 0.771717 * 0.040256 0.156603 n-Pentane 0.00345355 0.945318 1.18841 * 0.0485656 0.194528 Cyclopentane 0.00028128 0.127707 0.148295 * 0.00398684 0.0166011 Hexane 0.000686858 0.686727 0.73804 * 0.0099441 0.0413691 Cyclohexane 0.000177888 0.282003 0.297022 * 0.00290271 0.0121161 Isohexane 0.00146077 1.02291 1.13102 * 0.0207788 0.0873265 Heptane 0.00038526 1.38622 1.41983 * 0.00678404 0.0268251 Methylcyclohexane 0.000128542 0.45052 0.461389 * 0.00215906 0.00870917 2,2,4-Trimethylpentane 2.14848E-06 0.00697358 0.00715013 * 3.52178E-05 0.000141336 Benzene 7.98128E-05 0.131552 0.140713 * 0.00176926 0.00739127 Toluene 5.03547E-05 0.297233 0.303157 * 0.00119431 0.00472922 Ethylbenzene 5.53199E-06 0.100656 0.101312 * 0.000140398 0.000514791 o-Xylene 7.5704E-06 0.211199 0.212301 * 0.000237901 0.00086356 Octane 0.000108536 1.3672 1.37773 * 0.00225793 0.00827546 Nonane 2.32543E-05 1.02522 1.02776 * 0.000577218 0.00196803 C10+ 5.66973E-10 5.62836 5.62836 * 1.25646E-07 1.79868E-07 C11AIkanes(normal) 0 0 0 * 0 0 C12Alkanes(normal) 0 0 0 * 0 0 C13Alkanes(normal) 0 0 0 * 0 0 C14 0 0 0 * 0 0 C15 0 0 0 * 0 0 C16 0 0 0 * 0 0 C17 0 0 0 * 0 0 C18 0 0 0 * 0 0 C19 0 0 0 * 0 0 C20 0 0 0 * 0 0 C21 0 0 0 * 0 0 C22 0 0 0 * 0 0 C23 0 0 0 * 0 0 C24 0 0 0 * 0 0 C25 0 0 0 * 0 0 C26 0 0 0 * 0 0 C27 0 0 0 * 0 0 C28 0 0 0 * 0 0 C29 0 0 0 * 0 0 C30 0 0 0 * 0 0 C31 0 0 0 * 0 0 C32 0 0 0 * 0 0 C33 0 0 0 * 0 0 C34 0 0 0 * 0 0 C35 0 0 0 * 0 0 C36 0 0 0 * 0 0 Decane 0 0 0 * 0 0 Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas Mass Fraction - - " era % % % % . CO2 0.482569 0.00160073 0.12406 * 2.73936 0.490025 Nitrogen 0.00102295 4.90443E-06 0.0135667 * 0.37908 0.0109615 Methane 0.327953 0.00116241 0.448638 * 11.5592 0.902475 Ethane 11.105 0.0553248 1.22658 * 21.1282 7.63294 Propane 33.3332 0.771603 3.64171 * 32.8969 30.432 i-Butane 7.07695 0.464582 1.00857 * 4.66133 7.16188 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500b51 tanks.pmx Page 3 of 10 t Process Streams'Report , ,; Ta . . -..ea Phase g l l 'Client Name_ Bonanza Creek , Job aa' Location:_••; - 'Latham 14^12• • � ` Flowsheet'' iFlowsheet1 �a ,,.;�c � %M �'� 1.:„.,:: 5',. ;;"' % % r� „/err/,�.: .� "ry � r.. Breathing Flashed - -Pressurized Sales Gas Tank"Flashl. Losses Liquid -:_ Liquid Gas %_ •Mass Fraction ' %7.:' % " % % ;:4 n-Butane 25.014 2.42527 4.2497 * 14.618 25.9567 i-Pentane 6.22714 1.68792 2.05309 * 3.14576 6.95643 n-Pentane 7.47076 2.77568 3.16167 * 3.79511 8.64111 Cyclopentane 0.591469 0.364501 0.383503 * 0.302842 0.716829 Hexane 1.77468 2.4084 2.34522 * 0.928142 2.19491 Cyclohexane 0.448869 0.96587 0.921748 * 0.26459 0.627805 Isohexane 3.77429 3.58742 3.59395 * 1.93941 4.63326 Heptane 1.15745 5.65289 5.24606 * 0.736258 1.65491 Methylcyclohexane 0.378412 1.80022 1.67046 * 0.229605 0.526483 2,2,4-Trimethylpentane 0.0073583 0.0324184 0.0301168 * 0.00435715 0.00993999 Benzene 0.186922 0.418193 0.405295 * 0.149684 0.355462 Toluene 0.139108 1.11455 1.02998 * 0.119185 0.268279 Ethylbenzene 0.0176089 0.434895 0.396607 * 0.0161439 0.0336488 o-Xylene 0.0240974 0.912505 0.831099 * 0.0273554 0.0564458 Octane 0.371723 6.35575 5.80308 * 0.279351 0.582001 Nonane 0.0894229 5.3512 4.86057 * 0.0801826 0.155405 C10+ 4.63233E-06 62.418 56.5547 * 3.70835E-05 3.01771E-05 C11AIkanes(normal) 0 0 0 * 0 0 C12AIkanes(normal) 0 0 0 * 0 0 C13AIkanes(normal) 0 0 0 * 0 0 C14 0 0 0 * 0 0 C15 0 0 0 * 0 0 C16 0 0 0 * 0 0 C17 0 0 0 * 0 0 C18 0 0 0 * 0 0 C19 0 0 0 * 0 0 C20 0 0 0 * 0 0 C21 0 0 0 * 0 0 C22 0 0 0 * 0 0 C23 0 0 0 * 0 0 C24 0 0 0 * 0 0 C25 0 0 0 * 0 0 C26 0 0 0 * 0 0 C27 0 0 0 * 0 0 _. C28 0 0 0 * 0 0 C29 0 0 0 * 0 0 C30 0 0 0 * 0 0 C31 0 0 0 * 0 0 C32 0 0 0 * 0 0 C33 0 0 0 * 0 0 C34 0 0 0 * 0 0 C35 0 0 0 * 0 0 C36 0 0 0 * 0 0 Decane 0 0 0 * 0 0 •;Ut .,w 4,t; , it ir..;,: .."ltr _ ,0•7 t ...;fib )ia', t. ._ =A : i- 1, -q,,w ... „ Breathing , - • Flashed '.. Pressurized ' Sales Gas Tank Flash, , Losses Liquid Liquid Gas 'Mass.Flow Ib/h: lb/h Iblh Ib/h iblh CO2 0.0160949 0.0393329 3.36444 * 2.5292 0.795905 Nitrogen 3.4118E-05 0.000120511 0.367922 * 0.349997 0.0178038 Methane 0.0109381 0.0285627 12.1668 * 10.6724 1.46581 Ethane 0.370381 1.35944 33.2642 * 19.5073 12.3975 Propane 1.11175 18.9597 98.7609 * 30.3731 49.428 i-Butane 0.236035 11.4157 27.3518 * 4.30372 11.6324 n-Butane 0.834281 59.5934 115.249 * 13.4965 42.1592 i-Pentane 0.207691 41.4753 55.6785 * 2.90442 11.2987 n-Pentane 0.249169 68.2036 85.7425 * 3.50395 14.035 Cyclopentane 0.019727 8.95647 10.4004 * 0.279609 1.16428 Hexane 0.0591903 59.179 63.6009 * 0.856936 3.565 Cyclohexane 0.0149709 23.7332 24.9972 * 0.244291 1.01969 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 4 of 10 Process Streams Report .Ali Streams Tabulated by Total Phase Client Name: I Bonanza Creek Job: Location. _ Latham 14-12 Flowsheet: Flowsheetl Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas Mass Flow _ I lb/h lb/h lb/h lb/h lb/h Isohexane 0.125882 88.1498 97.4658 * 1.79062 7.52539 Heptane 0.0386038 138.902 142.27 * 0.679774 2.68792 Methylcyclohexane 0.012621 44.2348 45.3019 * 0.21199 0.855119 2,2,4-Trimethylpentane 0.000245418 0.796581 0.816749 * 0.00402288 0.0161447 Benzene 0.00623432 10.2758 10.9913 * 0.1382 0.577346 Toluene 0.00463961 27.3866 27.9324 * 0.110042 0.435743 Ethylbenzene 0.000587304 10.6862 10.7557 * 0.0149054 0.0546528 o-Xylene 0.000803712 22.422 22.5389 * 0.0252567 0.0916798 Octane 0.0123979 156.173 157.376 * 0.25792 0.945293 Nonane 0.00298248 131.489 131.816 * 0.0740311 0.25241 C10+ 1.545E-07 1533.73 1533.73 * 3.42385E-05 4.9014E-05 C11AIkanes(normal) 0 0 0 * 0 0 C12Alkanes(normal) 0 0 0 * 0 0 C13Alkanes(normal) 0 0 0 * 0 0 C14 0 0 0 * 0 0 C15 0 0 0 * 0 0 C16 0 0 0 * 0 0 C17 0 0 0 * 0 0 C18 0 0 0 * 0 0 C19 0 0 0 * 0 0 C20 0 0 0 * 0 0 C21 0 0 0 * 0 0 C22 0 0 0 * 0 0 C23 0 0 0 * 0 0 C24 0 0 0 * 0 0 C25 0 0 0 * 0 0 C26 0 0 0 * 0 0 C27 0 0 0 * 0 0 C28 0 0 0 * 0 0 C29 0 0 0 * 0 0 C30 0 0 0 * 0 0 C31 0 0 0 * 0 0 C32 0 0 0 * 0 0 C33 0 0 0 * 0 0 C34 0 0 0 * 0 0 C35 0 0 0 * 0 0 C36 0 0 0 * 0 0 Decane 0 0 0 * 0 0 Stream Properties Property Units Breathing Flashed Pressurized Sales Gas Tank Flash Losses Liquid Liquid Gas Temperature °F 66.1767 85.9132 113 * 104.969 85.9132 Pressure psia 12.7715 12.37 183.37 * 62.37 * 12.37 * Mole Fraction Vapor % 100 0 1.40839 100 100 Mole Fraction Light Liquid % 0 100 98.5916 0 0 Mole Fraction Heavy Liquid % 0 0 0 0 0 Molecular Weight Ib/Ibmol 49.9862 154.111 125.543 36.6292 51.7796 Mass Density Ib/ft^3 0.115322 48.4187 39.7384 0.393201 0.111368 Molar Flow lbmol/h 0.0667235 15.9442 21.6016 2.52062 3.13678 Mass Flow lb/h 3.33526 2457.19 2711.94 92.3282 162.421 Vapor Volumetric Flow ft^3/h 28.9214 50.7488 68.2448 234.812 1458.41 Liquid Volumetric Flow gpm 3.60578 6.32712 8.50845 29.2752 181.828 Std Vapor Volumetric Flow MMSCFD 0.000607692 0.145214 0.196739 0.0229568 0.0285685 Std Liquid Volumetric Flow sgpm 0.0125877 6.27083 7.2713 * 0.402749 0.597715 Compressibility 0.980981 0.00672461 0.0942635 0.958858 0.982297 Specific Gravity 1.72589 0.77633 1.26471 1.78782 API Gravity 48.0743 Enthalpy Btu/h -3326.64 -2.04403E+06 -2.31317E+06 -110742 -158403 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig500bb1 tanks.pmx - Page 5 of 10 ' Process Streams Report 3«r ...,. II Streams F 4, Tabulated by Total Phase Client Name: Bonanza Creek Job: Location: Latham'14-12 Flowsheet: I Flowsheetl .,. �. . �Z.41g,f%/.✓., ! ''"..1'.; %!i'4 .,.... iii„ ,, Stream Properties Property .Units - Breathing Flashed Pressurized Sales Gas -" Tank Flash Losses :Liquid Liquid .......:Gas Mass Enthalpy Btu/lb -997A16 -831.856 -852.959 -1199.44 -975.262 Mass Cp Btu/(Ib*°F) 0.39589 0.480632 0.506525 0.436716 0.406289 Ideal Gas CpCv Ratio 1.11252 1.0355 1.04168 1.14568 1.10504 Net Ideal Gas Heating Value Btu/ft^3 2591.4 7608.75 6224.17 1879.25 2677.8 Gross Ideal Gas Heating Value Btu/ft^3 2811.78 8135.64 6665.6 2047.92 2904.04 rg,/,.,�.�%i ii/ ,vir✓, . .. vA i;,,,,,��i;k\.i.�F'� ffi ii i, /��kF ..k. h.t4k �:‘ _Y,iy ).:"'",1''' „z1:1-''-1:r#' , � i Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 6 of 10 . Process Streams Report v, AEIStrearns ", a Tabulated by Total Phase , - Cli n# 7a1t;11 Bonanza Creek Job: Locettott Latham 14-12- . � F Flowshpe(' ..K .. ..,.. :Latham eetl• W as } r', Connections To Tanks Total Tank Working 1 Emissions Losses . From Block Separator MIX-100 -- VLVE-100 y�Too!/�Block , VLVE-100 -- MIX-100 Oil Tank ,r,e H 7i r,.,,e,€ir,.'iii` u,ij,' Fh// , �. ,',/,'-',',"�.� , -3 ..... „ia 'j4f j-' ,� Stream Compositi 's on To Tanks Total Tank Working 1 Emissions Losses CO2 0.0994632 0.575534 0.548105 0.0994632 Nitrogen 0.00335332 0.0196074 0.00182532 0.00335332 Methane 0.488188 2.84584 1.02186 0.488188 Ethane 2.39774 13.3326 18.4608 2.39774 Propane 8.12796 35.8078 37.7861 8.12796 i-Butane 2.07822 6.36992 6.08632 2.07822 n-Butane 9.17492 23.0671 21.5125 9.17492 i-Pentane 3.83345 4.96843 4.3143 3.83345 n-Pentane 5.97372 6.16517 5.1759 5.97372 Cyclopentane 0.756292 0.525422 0.421561 0.756292 Hexane 3.81582 1.30858 1.02941 3.81582 Cyclohexane 1.54142 0.382018 0.266604 1.54142 Isohexane 5.81855 2.76287 2.18928 5.81855 Heptane 7.40551 0.845331 0.577398 7.40551 Methylcyclohexane 2.40674 0.274633 0.192648 2.40674 2,2,4-Trimethylpentane 0.0372879 0.0044602 0.00321998 0.0372879 Benzene 0.728177 0.231519 0.119617 0.728177 Toluene 1.58253 0.148097 0.0754677 1.58253 Ethylbenzene 0.530219 0.0161235 0.00829091 0.530219 o-Xylene 1.11138 0.0269563 0.0113459 1.11138 Octane 7.20859 0.260234 0.162665 7.20859 Nonane 5.38328 0.0617518 0.0348517 5.38328 O10+ 29.4972 5.56098E-06 8.49735E-07 29.4972 C11Alkanes(normal) 0 0 0 0 C12Alkanes(normal) 0 0 0 0 C13AIkanes(normal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 m User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 7 of 10 Process Streams Report ;All Streams . Tabulated by Total Phase . Client Name: Bonanza Creek Job: Location: Latham 14-12 Flowsheet: Flowsheetl ,. � ,.I. la, ` ,--1-4-w ///iii„ a,:y ,e,e N,.,.,,, To Tanks Total Tank Working 1 Emissions Losses Molar Flow Ibmol/h lbmol/h Ibmol/h Ibmol/h CO2 0.0189786 0.0187169 0.000266298 0.0189786 Nitrogen 0.000639848 0.00063765 8.86835E-07 0.000639848 Methane 0.0931511 0.092549 0.000496472 0.0931511 Ethane 0.457512 0.433588 0.00896919 0.457512 Propane 1.5509 1.1645 0.0183584 1.5509 i-Butane 0.396545 0.207155 0.00295705 0.396545 n-Butane 1.75067 0.750161 0.0104519 1.75067 i-Pentane 0.731461 0.161578 0.00209611 0.731461 n-Pentane 1.13985 0.200497 0.00251472 1.13985 Cyclopentane 0.144308 0.0170872 0.000204816 0.144308 Hexane 0.728096 0.0425561 0.00050014 0.728096 Cyclohexane 0.294119 0.0124236 0.00012953 0.294119 Isohexane 1.11024 0.0898509 0.00106367 1.11024 Heptane 1.41305 0.0274909 0.00028053 1.41305 Methylcyclohexane 0.45923 0.00893131 9.35985E-05 0.45923 2,2,4-Trimethylpentane 0.00711491 0.000145049 1.56443E-06 0.00711491 Benzene 0.138944 0.0075292 5.81161E-05 0.138944 Toluene 0.301963 0.00481624 3.66661E-05 0.301963 Ethylbenzene 0.101171 0.000524351 4.02815E-06 0.101171 o-Xylene 0.212063 0.000876643 5.51243E-06 0.212063 Octane 1.37547 0.00846302 7.90311 E-05 1.37547 Nonane 1.02718 0.00200822 1.69328E-05 1.02718 010+ 5.62836 1.80848E-07 4.12845E-10 5.62836 C11AIkanes(normal) 0 0 0 0 C12AIkanes(normal) 0 0 0 0 C13Alkanes(normal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 019 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 To Tanks Total Tank Working 1 Emissions Losses Mass Fraction % % % % CO2 0.0318841 0.48977 0.482569 0.0318841 Nitrogen 0.000684236 0.0106209 0.00102295 0.000684236 Methane 0.0570456 0.882786 0.327953 0.0570456 Ethane 0.525153 7.75193 11.105 0.525153 Propane 2.61061 30.5315 33.3332 2.61061 i-Butane 0.879828 7.15897 7.07695 0.879828 - *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 8 of 10 41 ��'.Process Streams Repo s 4 An Streams �v,�,3 ., ,iii„ Tabulated by Total Phase .,.3i3O Client Name: Borianza'Creeit,- Job a Ni*Er Location: ,Latham 14-.12 "-:' z, Fiowsheet Flowsheetl ' To Tanks Total Tank Working 1 Emissions Losses Mass Fraction 9/. % % n-Butane 3.88427 25.9244 25.014 3.88427 i-Pentane 2.01458 6.93144 6.22714 2.01458 n-Pentane 3.13934 8.601 7.47076 3.13934 Cyclopentane 0.386346 0.712533 0.591469 0.386346 Hexane 2.39516 2.18051 1.77468 2.39516 Cyclohexane 0.944909 0.621672 0.448869 0.944909 lsohexane 3.65227 4.60382 3.77429 3.65227 Heptane 5.405 1.63786 1.15745 5.405 •Methylcyclohexane 1.72125 0.521408 0.378412 1.72125 2,2,4-Trimethylpentane 0.0310247 0.00985152 0.0073583 0.0310247 Benzene 0.414304 0.349686 0.186922 0.414304 Toluene 1.06208 0.263853 0.139108 1.06208 Ethylbenzene 0.410017 0.0330991 0.0176089 0.410017 o-Xylene 0.859427 0.0553372 0.0240974 0.859427 Octane 5.99776 0.574795 0.371723 5.99776 Nohane 5.02905 0.153144 0.0894229 5.02905 C10+ 58.548 2.93017E-05 4.63233E-06 58.548 C11AIkanes(normal) 0 0 0 0 C12Alkanes(normal) 0 0 0 0 C13AIkanes(ruormal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 - 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 2 ' -≥ To Tanks P2aTgtal Tank Working rt Mass low_< ti b)h - ��mlb/ tons Losses h Ib/h Iblh CO2 0.835238 0.823719 0.0117196 0.835238 Nitrogen 0.0179243 0.0178628 2.48433E-05 0.0179243 Methane 1.49437 1.48471 0.00796462 1.49437 Ethane 13.7569 13.0376 0.269695 13.7569 Propane 68.3878 51.3493 0.809526 68.3878 i-Butane 23.0481 12.0403 0.17187 23.0481 n-Butane 101.753 43.601 0.607486 101.753 i-Pentane 52.774 11.6576 0.151232 52.774 n-Pentane • 82.2385 14.4656 0.181434 82.2385 Cyclopentane 10.1208 1.19837 0.0143643 10.1208 Hexane 62.744 3.66729 0.0430997 62.744 Cyclohexane 24.7529 1.04556 0.0109012 24.7529 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 9 of 10 Process Streairr>s$Report i All Streams" Tabulated by Total Phase .Client Name .BonanzaCreek':'. `.loci_' L"ovation:. Latham'40'12 , Flowsheet Flowsheetl t To Tanks Total.Tank : . Working 1 Emissions ...Losses,. Mass Flow lb/h ,:,]lb/h ib/h . :. lb/h Isohexane 95.6752 7.74293 0.0916618 95.6752 Heptane 141.59 2.75464 0.0281096 141.59 Methylcyclohexane 45.0899 0.87693 0.00919007 45.0899 2,2,4-Trimethylpentane 0.812726 0.0165688 0.000178703 0.812726 Benzene 10.8531 0.58812 0.00453956 10.8531 Toluene 27.8224 0.443761 0.00337836 27.8224 Ethylbenzene 10.7408 0.0556678 0.000427649 10.7408 o-Xylene 22.5136 0.0930688 0.000585228 22.5136 Octane 157.118 0.966719 0.00902761 157.118 Nonane 131.742 0.257564 0.00217171 131.742 C10+ 1533.73 4.9281E-05 1.125E-07 1533.73 C11Alkanes(normal) 0 0 0 0 C12Alkanes(normal) 0 0 0 0 C13AIkanes(norm al) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 iii - ..,2.--3.&.,. .,:A ,Fz;:. iaix " Si RA rye... Stream Properties • Property . : :Units To Tanks • .Total Tank Working 1 is Emissions Losses = Temperature °F 104.969 85.2416 66.1767 85.9132 Pressure psia 62.37 12.37 12.7715 12.37 Mole Fraction Vapor % 0 100 100 16.4393 Mole Fraction Light Liquid % 100 0 0 83.5607 Mole Fraction Heavy Liquid % 0 0 0 0 Molecular Weight Ib/Ibmol 137.289 51.7161 49.9862 137.289 Mass Density Ib/ft^3 46.9093 0.111371 0.115322 1.7358 Molar Flow Ibmol/h 19.081 3.25208 0.0485851 19.081 Mass Flow lb/h 2619.61 168.185 2.42859 2619.61 Vapor Volumetric Flow ft^3/h 55.8441 1510.13 21.0593 1509.16 Liquid Volumetric Flow gpm 6.96239 188.276 2.62557 188.155 Std Vapor Volumetric Flow MMSCFD 0.173782 0.0296187 0.000442495 0.173782 Std Liquid Volumetric Flow sgpm 6.86855 0.619469 0.00916579 6.86855 Compressibility 0.0301243 0.982275 0.980981 0.167101 Specific Gravity 0.752128 1.78562 1.72589 API Gravity 51.4429 Enthalpy Btu/h -2.20243E+06 -164152 -2422.31 -2.20243E+06 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 10 of 10 Process Streams Report �" Tabulated by Total Phase :,:,,,,,:j,,,,,',.ii,.,,,:',.,,i,., Client Name: Bonanza Creek •• Job Location: Bonanza l 1412 . ° , Fiowsheet Blowstreet1 � �u,,,,,.:. /r,;V.p.."�,.'i9// / i �� c.,/j O ,r @aie�.�. - \\��`��wyN i3 ��rr_/�U .; .. t',..r/ l�i/�i/i/vuiu �/p, .,....,,,i�///i//� � �2.a�pY '�i/(/s,H..:r.,, �,. ., 4; ... Stream Properties Property pmts - "To Tanks Total Tank Working [ �.:_ Emissions Lo ses � Mass Enthalpy Btu/lb -840.748 -976.021 -997.416 -840.748 Mass Cp Btu/(Ib*°F) 0.49789 0.40593 0.39589 0.476023 Ideal Gas CpCv Ratio 1.0386 1.10528 1.11252 1.03984 Net Ideal Gas Heating Value Btu/ft^3 6798.14 2674.74 2591.4 6798.14 7275.61 Gross Ideal Gas Heating Value Btu/ft^3 7275.61 2900.77 2811.78 Remarks User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 1 of 1 Biocks MIX-100 Mixer/Sputter Report. Client Name: • ' Bonanza Creek " Job Location: Latham 14-12 Modified:12:03 PM,2/25/201.9 Flowsheet: . Flowsheetl Status:Solved 1:52 PM,3/10/2020 • Connections Stream Connection Type Other Block ,Stream Connection Type " Other Block Tank Flash Gas Inlet Oil Tank Working Losses Inlet Breathing Losses Inlet Total Tank Emissions Outlet Block Parameters Pressure Drop 0 psi Fraction to Stream Total 100 % Tank Emissions Flow Multiplier 100 % Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 1 Blocks Oil Tank Separator Report Client Name: I Bonanza Creek _ I Job Location: i Latham 14-12 j Modified: 12:06 PM,2/25/2019 Flowsheet: Flowsheetl ;_ I Status:Solved 12:38 PM, 1/23/2020 Connections Stream Conn'ectionType Other Block ;Stream Connection Type Other;;Block 1 Inlet VLVE-100 Tank Flash Gas Vapor Outlet MIX-100 Flashed Li uid Light Liquid Outlet 1��✓f�z��." Y"'f�'�� y� " 7,4 .kid ... Block Parameters Pressure Drop 0 psi Main Liquid Phase Light Liquid Mole Fraction Vapor 16.4393 % Heat Duty 0 Btu/h Mole Fraction Light Liquid 83.5607 % Heat Release Curve Type Plug Flow Mole Fraction Heavy Liquid 0 % Heat Release Curve 10 Increments � Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 1 Blocks Separator Separator Report } Client Name: Bonanza Creek jobs .., Location: Latham 14-12 Modifed<243 PM.16'15/2020 Flowsheet: ! Flowsheetl Status:;Solved-.12:38 PM,1/23/202 ��, ' Connections Stream Connection Type k Other Blo . Stream !; -Connection Type Other.Block Pressurized Liquid Inlet Sales Gas Vapor Outlet To Tanks Light Liquid Outlet VLVE-100 Block Parameters Pressure Drop 121 psi Main Liquid Phase Light Liquid Mole Fraction Vapor 11.6686 % Heat Duty 0 Btu/h Mole Fraction Light Liquid 88.3314 % Heat Release Curve Type Plug Flow Mole Fraction Heavy Liquid 0 % Heat Release Curve 10 Increments Remarks User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 1„,,o1,1 of 1 Blocks VLVE=100 .. =-JT-Va1veReport” '. lfertt.Narrte:' Bonanza Greek . 1 v, ation: Latham.14-1,Z ,,,:;. ' :Modified:812AM�7/312019 = ; Fl.owsheet: Flowsheetl : Status:Solved:'12 38 PM, 112312020 ,,. \ Connections Stream Gonnec#ion Tppe Other Block - Stream Connection Type Other;Block To Tanks Inlet Separator 1 Outlet Oil Tank s \\ i �,iyle, of Block Parameters Pressure Drop 50 psi Calculate Flow False Joule-Thomson Coefficient 0.381119 °F/psi Simple Incompressible Cv 0.853924 Pressure Drop Method User Set ? Simple Compressible Cv 88.5727 Allow Pressure Increase True Remarks *User Specified Values ProMax 5,0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 1 Flovvsheet Environment 'Envirolnrnentil Client Narne�.,, . . Bonanza:�Creek Lo'�cpt'ron: i �,�atham'14-12 ' -'' ..'::::':::::',:::',:::":-.,,:-:::.):.::':,.:7::.::..: . . .i, Flowsheet. -i3 .... ,: lowsheetl Environment Settings Number of Poynting Intervals 0 Phase Tolerance 1 % Gibbs Excess Model 77 °F Emulsion Enabled False Evaluation Temperature Freeze Out Temperature 10 °F Threshold Difference Components Component Name Henry's,Law Phase.. . Component Name Henry's Law Phase ..- ,:: Initiato',.Component ,-.: Initiator ;; ' Component r CO2 False False C13AIkanes(norm al) False False Nitrogen False False C14 False False Methane False False C15 False False Ethane False False C16 False False Propane False False C17 False False i-Butane False False C18 False False n-Butane False False C19 False False i-Pentane False False C20 False False n-Pentane False False C21 False False Cyclopentane False False C22 False False Hexane False False C23 False False Cyclohexane False False C24 False False Isohexane False False C25 False False Heptane False False C26 False False Methylcyclohexane False False C27 False False 2,2,4-Trimethylpentane False False C28 False False Benzene False False C29 False False Toluene False False C30 False False Ethylbenzene False False C31 False False o-Xylene False False C32 False False Octane False False C33 False False Nonane False False C34 False False C10+ False False C35 False False C11AIkanes(normal) False False C36 False False C12AIkanes(no rmal) False False Decane False False Physical Property Method Sets Liquid Molar Volume COSTALD Overall Package Peng-Robinson Stability Calculation Peng-Robinson Vapor Package Peng-Robinson Light Liquid Package Peng-Robinson Heavy Liquid Package Peng-Robinson Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 1 of 1 • Environments Repay M ... F ....t. n_ s i Chon ,00ne Bonanza-Creek • ,�� 1:600,0 111-1211.&1 atharn [4 12 ._...: r, :. vas NFt x Pro'ect-Wide Constants - Atmos.heric Pressure 12.37 .sia Ideal Gas Reference Pressure 14.6959 •sia Ideal Gas Reference Temperature 60 °F Ideal Gas Reference Volume 379.484 ft^3/Ibmol Liquid Reference Tern•erature 60 °F :-.411,Prtniiiiiligallania'21:224ANIMONEWEEEMErNaltaioNmonsimogrom :11111111411111M RIM.EitiNtga#MAN•age•gligalAW:MM.M0Environment.[Environment'i Environment Settin•s Number of Po ntin. Intervals 0 Phase Tolerance 1 % Gibbs Excess Model 77 °F Emulsion Enabled False Evaluation Temperature Freeze Out Temperature 10 °F Threshold Difference ,x AI ..IE.; .... , .... .:.. .'a.. Components Component'Name : Henry's'Law Phase Component Name Henry's Law Phase Com•onent :°:•initiator. - Com•onertit,. ..In'ifiator „ ;:;CO2 False False C13Alkanes normal False False Nitro.en False False C14 False False Methane False False C15 False False Ethane False False C16 False False Pro.ane False False C17 False False i-Butane False False C18 False False n-Butane False False C19 False _ False i-Pentane False False C20 False False n-Pentane False False C21 False False C clo.entane False False C22 False False Hexane False False C23 False False C clohexane False False C24 False False Iohexane False False C25 False False He.tane False False C26 False False Meth lc clohexane False False C27 False False 2,2,4-Trimeth I•entane False False C28 False False Benzene False False C29 False False Toluene False False C30 False False Eth (benzene False False C31 False False o-X lene False False C32 False False Octane False False C33 False False Nonane False False C34 False False 010+ False False C35 False False C11Alkanes normal False False C36 False False C12Alkanes(normal False False Decane False False Ph sical Pro•e rt Method Sets Li.uid Molar Volume COSTALD Overall Packa.e Pen.-Robinson Stabilit Calculation Pens-Robinson Va.or Packa.e Pen.-Robinson Li.ht Liquid Packase Pen.-Robinson Hea Liquid Packa.e Pen.-Robinson if Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/20201:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 1 ✓r`24'% Sitagie Oil Report c10+ I • Client Name: Bonanza Creek Job: Location: Latham 14-12 Properties Volume Average Boiling 640.26 °F Low Temperature Viscosity 6.29289 cP Point * Molecular Weight 272.5 Ib/ibmol Temperature of High T 210 °F Viscosity * Specific Gravity 0.857 High Temperature Viscosity 1.70166 cP API Gravity 33.6109 Watson K 12.045 Critical Temperature 942.802 °F ASTM D86 10-90%Slope 0 °F/% Critical Pressure 204.624 psia ASTM D93 Flash Point 323.579 °F Critical Volume 16.3154 ft"3/Ibmol Pour Point 48.0566 °F Acentric Factor 0.828643 Paraffinic Fraction 66.8697 % Carbon to Hydrogen Ratio 6.43068 Naphthenic Fraction 24.8849 % Refractive Index 1.47439 Aromatic Fraction 8.24537 % Temperature of Low T 100 °F Ideal Gas Heat Capacity 96.5503 Btu/(Ibmol*°F) Viscosity ....:. _,.< .„��:�.�� ;� .,;:'.;, ,,,, ;•; <e'r,. „\,c.C�`�1.; '.. 1044..I ,��,/,,�ii �i:,,�'„ ." Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 1 of 1 i I j I Calculator Report Client Name: ° fBonanza Creek Job: LOcation: I Latham 14-12 - I Simple;Solver„1 Source Code Residual Error(for CV1)=SalesOil/215-1 Calculated Variable[CV1] Source Moniker ProMax:ProMax!Project!Flowsheets!Flowsheetl!PStreams!Pressurized Liquid!Phases!Total!Properties!Std Liquid Volumetric Flow Value 249.302 Unit i, Measured Variable[SalesOil] Source Moniker ProMax:ProMax!Project!Flowsheets!Flowsheetl!PStreams!Flashed Liquid!Phases!Total!Properties!Std Liquid Volumetric Flow Value 215 Unit Solver Properties Status: Solved Error -2.78666E-14 Weighting 1 Calculated Value 7.2713 sgpm Priority 0 Lower Bound sgpm Solver State Active Upper Bound sgpm Group Step Size sgpm Skip Dependency Check False Is Minimizer False Block Dependencies 3 Algorithm Default Recycle Dependencies 0 Iterations 2 Solver Dependencies 1 Max Iterations 20 `�`•.�u +. ro_. � iii `.' % � ` , .. r, � �''s� .Y` i.'_._:. ,�.: .... .. ,.,, ,.. ,_ .� mom. ,i:ic.L<g.�b� ,,,,,,, Y„ck.,., .. Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx .. Page 1 of 6 '4O,411z �j h � z Monlommlo User\la�ue'S�� F�eport �� y f Client Name: Bonanza Creek Job. Location: Latham 14-12 User Value[CnPlusSum] * Parameter - 669.356 ton/yr Upper Bound ton/yr Lower Bound ton/yr * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={4E534736-DD77-4051-8O38-5AF9922CF203} User Value [BlockReady] • Parameter 1 _Upper Bound Lower Bound * Enforce Bounds False User Value'[ShellLength] * Parameter 25 ft Upper Bound ft Lower Bound ft * Enforce Bounds False User Value IShellDiam] * Parameter 12 ft per Bound ft Lower Bound ft * Enforce Bounds False User Value BreatherVP] * Parameter _ 0.03 psig Upper Bound psig Lower Bound psig * Enforce Bounds False User Value[BreatherVacP] * Parameter -0.03 psig Upper Bound psig Lower Bound psig * Enforce Bounds False User Value [DomeRadius] Parameter ft Upper Bound ft Lower Bound ft * Enforce Bounds False 11 ;,. User Value [OpPress] * Parameter _ 0 psig 1 Upper Bound psig Lower Bound psig I* Enforce Bounds False H.. User Value[AvAc PercentLiq] * Parameter 50 % Upper Bound % Lower Bound %. * Enforce Bounds False User Value [MaxPercentLiq] * Parameter _ 90 % Upper Bound Lower Bound % * Enforce Bounds False User ValuejAnnNetTP] * Parameter 213.292 bbl/day Upper Bound bbl/day Lower Bound bbl/day * Enforce Bounds False User Value [OREff] Parameter % Upper Bound % Lower Bound % * Enforce Bounds False *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated nn 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 2 of 6 ,User Value Sets Report Client Name: Bonanza Creek . Job: Location: Latham 14-12 User Value[MaxAv•T * Parameter 64.1833 °F U..er Bound °F Lower Bound °F * Enforce Bounds False 'k • ~w•5. User Value MinAv•T * Parameter 36.2417 °F U..er Bound °F Lower Bound °F * Enforce Bounds False User Value BulkLi•T * Parameter 51.7925 °F U.eel-Bound °F Lower Bound °F * Enforce Bounds False User Value Av•P * Parameter 12.122 •sia U..er Bound •sia Lower Bound .sia * Enforce Bounds False User Value[Therml * Parameter 1568.58 Btu/ft^2/da U..er Bound Btu/ft^2/da Lower Bound Btu/ft^2/da * Enforce Bounds False User Value [Av•WindSpeed] * Parameter 8.63333 mi/h U..er Bound mi/h Lower Bound mi/h * Enforce Bounds False User Value MaxHourl Loadin•Rate Parameter bbl/hr U..er Bound bbl/hr Lower Bound bbl/hr * Enforce Bounds False User Value[Flashin•T] * Parameter 66.1767 °F U..erBound °F Lower Bound °F * Enforce Bounds False User Value[EntrainedOilFrac] * Parameter 1 % U..er Bound % Lower Bound % * Enforce Bounds False User Value[TurnoverRate_ * Parameter 19.0837 U..er Bound Lower Bound * Enforce Bounds False User Value[LLossSatFactor] Parameter U..er Bound Lower Bound * Enforce Bounds False User Value[AtmPressure] * Parameter 12.122 .sia U..er Bound •sia Lower Bound •sia * Enforce Bounds False y °�, o-%v:�N„',�`':,...i:'i.. , : •. .,r>.,.., , i.::.L�i� .. ��.. ✓;x'n as ��Eu&d�`ap��e;\;k \ 3 F User Value TVP * Parameter 7.28917 .sia U..er Bound .sia Lower Bound •sia * Enforce Bounds False User Value MaxVP * Parameter 8.5602 .sia U..er Bound •sia Lower Bound •sia * Enforce Bounds False *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright G 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 3 of 6 � � °° ' i 4 User Value Sets Report �d ft�, Client Name: Bonanza Creek Job: Location: Latham 14-12 User Value MinVP] * Parameter 6.17599 •sia U••er Bound •sia Lower Bound psia * Enforce Bounds False User Value Av•Li•SurfaceT * Parameter 56.4258 °F U••er Bound °F Lower Bound °F * Enforce Bounds False :''-' . ''' . ..-.._ .:4).i.7.:Z*`. User Value _MaxLi•SurfaceT * Parameter 66.1767 °F U••er Bound °F Lower Bound °F * Enforce Bounds False User Value TotalLosses] * Parameter 25.2456 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value orkin•Losses * Parameter 1.18191 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value Standin•Losses * Parameter 1.62316 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User.Value RimSealLosses * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value _ ithdrawalLoss . * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False ~ User Value Loadin•Losses * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value[MaxHourl Loadin•Loss ,- * Parameter 0 lb/hr U••er Bound lb/hr Lower Bound lb/hr * Enforce Bounds False t <....��G� r „„,�';'_ : `� �� , ai.1771 q it User Value PStar ., Parameter U..er Bound Lower Bound * Enforce Bounds False , User Value AIICTotalLosses - * Parameter 25.2456 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value AIICLoadin•Losses * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value AIICMaxHLoadin•Loss * Parameter 0 lb/hr U••er Bound lb/hr *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 4 of 6 User Value Sets Report Client Name: Bonanza Creek Job: Location: Latham 14-12 User Value AIICMaxHLoadin•Loss] Lower Bound lb/hr * Enforce Bounds False User Value AIICFlashin•Losses * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value' DeckFittin•Losses] * Parameter 0 ton/ r U•.er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False '4412.24111511g21, •• User Value DeckSeamLosses] * Parameter 0 ton/ r U.•er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value[Flashin•Losses] * Parameter 0 ton/ r U••er Bound ton/ r Lower Bound ton/ r * Enforce Bounds - False _' aH , User Value _TotalResidual] * Parameter 10737.2 ton/ r U..er Bound ton/ r Lower Bound ton/ r * Enforce Bounds False User Value[GasMoleWei•ht * Parameter 0.0499862 k•/mol U••er Bound k•/mol Lower Bound k•/mol * Enforce Bounds False User Value VapRe•ortableFrac] * Parameter 100 % U••er Bound Lower Bound 9'° * Enforce Bounds False User Value [LiqRe•ortableFrac]' * Parameter 100 % U••er Bound Lower Bound % * Enforce Bounds False User Value [FlashRe•ortableFrac] * Parameter 0 % U••er Bound Lower Bound % * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={71F8CF4D-A151-4973-AC9C-B4870F23D964} xa Factor24 User Value Emission Factor * Parameter 17.0591 lb/bbl U••er Bound lb/bbl • Lower Bound lb/bbl * Enforce Bounds False f o!' -. "�� , 1s��.rte."..:;.. Remarks This User Value Set was programmatically generated. GUID={826817D6-3650-40B5-9716-4413B92266A1} *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 5 of 6 a User Value Sets Report �f Client Name: Bonanza Creek Job: Location ,.- Latham.1-4 12 Emission Factor.1n:User Value [EmissionFactor] * Parameter 137.762_S_CF/bbl ___Upper Bound _ SCF/bbl Lower Bound SCF/bbl * Enforce Bounds False 1.11.115 Remarks This User Value Set was programmatically generated. GUID={281705D6-A60D-4727-976C-9AFA500669B3} Emission Factor.126 User Value [EmissionFactor] * Parameter _ 0.0656506 lb/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={F7472464-EDCC-4B8A-B6DE-91A614438380} Emission Factor.127` User Value [EmissionFactor] * Parameter 0.0495361 lb/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={2DEBAE13-F6EA-4AB5-9E39-361 D441 DB5E5} Emission Factor.128 User Value [EmissionFactor] * Parameter 0.00621407 1b/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={07B86E0D-AE84-43DE-B685-FCAA781 FB9C2} User Value [EmissionFactor] * Parameter _ 0.0103891 lb/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={4DBE84F5-AB43-480A-939A-1080C3FE9994} E ission;:F stor'13tt' User Value,[EmissionFactor] * Parameter 0.409372 lb/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 6 of 6 User Value Sets Report di nt Na bonanza Creek Job: 'Location ;_Latham 14-12 This User Value Set was programmatically generated. GUID={61 C5C810-457E-40DE-9DCB-079396320A52} v 9' FC 'i'iJ f ! � :sston Factor.131,� User Value [EmissionFactor] * Parameter 0.00184954 lb/bbl Upper Bound lb/bbl Lower Bound lb/bbl * Enforce Bounds False Remarks This User Value Set was programmatically generated. GUID={7930F5C7-FC87-4335-AD0B-5812B0A2D4D9} *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 11 Recoveries Report Client Name: Bonanza Creek Job: Location:• , Latham 14-12 "° \\\ iii �. //l�F a Stattas ,01 0 �.�\��....F= .�` . �f��%,. �� Gtarnpgn�n�=,. e� v+��l � ,��t�t��l�� /. ,f�� n,.�<.... .�. , ��: Recovery Stream Data Source-All Inlets in Project Flowsheet PStream Flowsheet PStream Flowsheet1 Breathing Losses Flowsheetl Working Losses Flowsheet1 Pressurized Liquid Parameters * Composition Basis Molar Flow * Summation Option Streams and Summation * Calculate Ratios False * Atomic Basis False 7- u rn . _ ;P r, '''i ,:-,O 53--:- - Tabulated Data Flowsheet1:Breathing Flowsheet1:Pressurized Flowsheet1:Working Summary Table Losses Liquid Losses Index Ibmol/h lbmol/h Ibmol/h Ibmol/h CO2 0.000365715 0.0764481 0.000266298 0.0770801 Nitrogen 1.21792E-06 0.0131338 8.86835E-07 0.0131359 Methane 0.00068182 0.758411 0.000496472 0.759589 Ethane 0.0123177 1.10626 0.00896919 1.12755 Propane 0.0252122 2.2397 0.0183584 2.28327 i-Butane 0.00406101 0.470591 0.00295705 0.477609 n-Butane 0.0143539 1.98288 0.0104519 2.00768 i-Pentane 0.00287865 0.771717 0.00209611 0.776692 n-Pentane 0.00345355 1.18841 0.00251472 1.19438 Cyclopentane 0.00028128 0.148295 0.000204816 0.148781 Hexane 0.000686858 0.73804 . 0.00050014 0.739227 Cyclohexane 0.000177888 0.297022 0.00012953 0.297329 Isohexane 0.00146077 1.13102 0.00106367 1.13354 Heptane 0.00038526 1.41983 0.00028053 1.4205 Methylcyclohexane 0.000128542 0.461389 9.35985E-05 0.461611 2,2,4-Trimethylpentane 2.14848E-06 0.00715013 1.56443E-06 0.00715384 Benzene 7.98128E-05 0.140713 5.81161E-05 0.140851 Toluene 5.03547E-05 0.303157 3.66661 E-05 0.303244 Ethylbenzene 5.53199E-06 0.101312 4.02815E-06 0.101321 o-Xylene 7.5704E-06 0.212301 5.51243E-06 0.212314 Octane 0.000108536 1.37773 7.90311E-05 1.37792 Nonane 2.32543E-05 1.02776 1.69328E-05 1.0278 C10+ 5.66973E-10 5.62836 4.12845E-10 5.62836 C11AIkanes(normal) 0 0 0 0 C12Alkanes(normal) 0 0 0 0 C13Alkanes(normal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 , 0 C34 0 0 0 0 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 2 of 11 Recoveries Report... Client Name: _Bonanza Creek .. ' Job: Location: '": Latham 14-12 : .,...' r ' ;�; 4ty L„.:2 iii -. Tabulated Data Flowsheetl:Breathing Flowsheet1Pressurized . Flowsheetl:Working Summary Table Losses Liquid Losses Index Ibmol/h Ibmol/h lbmol/h Ibmol/h C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 Total 0.0667235 21.6016 0.0485851 21.7169 s y ir, ii/i/ '%."' : ii \ ° tq w t. Remarks '' " `vm orient Recover'1LS�`PP ro ect Out)" %f �I h am " �i�77�. ,, r�.:.�, •�� _..� � ,,.. � - .. _�ia�... � ice„ �� vK ': Recovery Stream Data Source-All Outlets in Project Flowsheet PStream Flowsheet PStream Flowsheet1 Flashed Liquid Flowsheetl Total Tank Emissions Flowsheet1 Sales Gas Parameters * Composition Basis Molar Flow * Summation Option Streams and Summation * Calculate Ratios False * Atomic Basis False Tabulated Data Flowsheetl:Flashed Flowsheet1:Sales Gas Flowsheetl:Total Tank Summary Table Liquid Emissions" Index Ibmol/h Ibmol/h Ibmol/h Ibmol/h CO2 0.000893736 0.0574695 0.0187169 0.0770801 Nitrogen 4.30191E-06 0.0124939 0.00063765 0.0131359 Methane 0.00178044 0.66526 0.092549 0.759589 Ethane 0.0452105 0.648749 0.433588 1.12755 Propane 0.429969 0.6888 1.1645 2.28327 i-Butane 0.196408 0.074046 0.207155 0.477609 n-Butane 1.02531 0.232209 0.750161 2.00768 i-Pentane 0.574858 0.040256 0.161578 0.776692 n-Pentane 0.945318 0.0485656 0.200497 1.19438 Cyclopentane 0.127707 0.00398684 0.0170872 0.148781 Hexane 0.686727 0.0099441 0.0425561 0.739227 Cyclohexane 0.282003 0.00290271 0.0124236 0.297329 Isohexane 1.02291 0.0207788 0.0898509 1.13354 Heptane 1.38622 0.00678404 0.0274909 1.4205 Methylcyolohexane 0.45052 0.00215906 0.00893131 0.461611 2,2,4-Trimethylpentane 0.00697358 3.52178E-05 0.000145049 0.00715384 Benzene 0.131552 0.00176926 0.0075292 0.140851 Toluene 0.297233 0.00119431 0.00481624 0.303244 Ethylbenzene 0.100656 0.000140398 0.000524351 0.101321 o-Xylene 0.211199 0.000237901 0.000876643 0.212314 Octane 1.3672 0.00225793 0.00846302 1.37792 Nonane 1.02522 0.000577218 0.00200322 1.0278 C10+ 5.62836 1.25646E-07 1.80848E-07 5.62836 C11AIkanes(normal) 0 0 0 0 C12AIkanes(normal) 0 0 0 0 C13Alkanes(normal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 3 of 11 ' - , t✓ate Recoveries Report 0 Client Name: Bonanza Creek 1Job: ., ;.;;,,, tr Location: Latham 14-12 I _ �` ``itg I - Tabulated Data Flowsheetl:Flashed Flowsheetl:Sales Gas Flowsheet1:Total Tank Summary Table i, Liquid Emissions Index Ibmol/h Ibmol/h Ibmol/h Ibmol/h C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 Total 15.9442 2.52062 3.25208 21.7169 W ice Remarks _ ... ,, , ! k,,;r: Comporte t Recoveries-Project Losses Status: solved - Reference Stream Data Source -All Outlets in Project Flowsheet PStream Flowsheet PStream Flowsheetl Flashed Liquid Flowsheetl Total Tank Emissions Flowsheetl Sales Gas , �.;..,;,..,_,,,,,,,_,.W;.,_,..... :; s ab +un dd.�4Rkb�/<A'✓✓�< yriii. ,;;O:' �1�,,.. )� h Recovery Stream Data Source -All Inlets in Project .:•::F:lowsheet ... . Psteetli'l!:!!"..•1'..'.,::J::::::;,-...' • • :Flowsheet,..... PStream Flowsheetl Breathing Losses Flowsheeti Working Losses Flowsheetl Pressurized Liquid Parameters * Composition Basis Molar Flow * Summation Option Summation Only * Calculate Ratios False * Atomic Basis False ----;fir:, . .. '', • „ '_:' - ✓., r. --4,-4,"'"7"7e:*--- q Tabulated Data Summary Table Index Ibmol/h CO2 1.10143E-16 Nitrogen 1.89308E-17 Methane 9.91287E-16 Ethane 1.32172E-15 Propane 4.40572E-16 i-Butane 1.10143E-16 n-Butane 0 i-Pentane 2.20286E-16 n-Pentane 2.20286E-16 Cyclopentane 2.75358E-17 Hexane -3.30429E-16 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 4 of 11 Recoveries Report Client Name: Bonanza Creek i Job: ------------ Location: Latham 14-12 Tabulated Data Summary Table •! • index Ibmol/h' • Cyclohexane -5.50715E-17 Isohexane -4.40572E-16 Heptane -4.40572E-16 Methylcyclohexane -1.10143E-16 2,2,4-Trimethylpentane -2.58148E-18 Benzene 0 Toluene 0 Ethylbenzene -1.37679E-17 o-Xylene -2.75358E-17 Octane 0 Nonane 0 C10+ -3.52458E-15 C11Alkanes(normal) 0 C12AIkanes(normal) 0 C13AIkanes(normal) 0 G14 0 O15 0 O16 0 G17 0 O18 0 O19 0 C20 0 O21 0 C22 0 O23 0 C24 0 O25 0 C26 0 C27 0 C28 0 O29 0 C30 0 C31 0 C32 0 C33 0 C34 0 C35 0 C36 0 Decane 0 Total -3.52458E-15 Remarks � � � Component Recoveries Project Recoveries status: Solved Reference Stream Data Source -All Inlets in Project Flowsheet PStream Flowsheet PStream Flowsheet1 Breathing Losses Flowsheet1 Working Losses Flowsheet1 Pressurized Liquid Recovery Stream Data Source -All Outlets in Project Flowsheet PStream Flowsheet PStream Flowsheet1 Flashed Liquid Flowsheet1 Total Tank Emissions Flowsheetl Sales Gas user Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 5 of 11 r.. ',MOM RID•14 �5 `NN/ Recoveries Report - A • Client Name: Bonanza.Creek N M :2, / .Location: - Latham"'1:4-12 .�"l.:y :.,,.. .. > � 9r i ar,. :E?a�x !-.-----„:,-,,dffigisrttgmomotnsogkiaefoEg gin\ n\k"'0-- 1.1111117.3' 111111101111111111 Parameters " Composition Basis. Molar Flow " Summation Option Streams and Summation * Calculate Ratios True * Atomic Basis False Tabulated Data Flowsheet1:Flashed ;i Fl.owsheet1:Sales Gas Flowsheetl:Total Tank Summary„Table Liquid' Emissions' Index OO2 1.15949 74.5582 24.2823 100 Nitrogen 0.0327493 95.113 4.85426 100 Methane 0.234396 87.5815 12.1841 100 Ethane 4.00963 57.5363 38.4541 100 Propane 18.8313 30.1673 51.0014 100 i-Butane 41.1232 15.5035 43.3734 100 n-Butane 51.0694 11.566 37.3645 100 i-Pentane 74.0137 5.183 20.8033 100 n-Pentane 79.1472 4.06618 16.7867 100 Cyclopentane 85.8356 2.67967 11.4848 100 Hexane 92.898 1.3452 5.75684 100 Cyclohexane 94.8454 0.976261 4.17838 100 Isohexane 90.2403 1.83308 7.92657 100 Heptane 97.5871 0.477582 1.9353 100 Methylcyclohexane 97.5975 0.467724 1.93481 100 2,2,4-Trimethylpentane 97.4801 0.492292 2.02757 100 Benzene 93.3984 1.25612 5.34552 100 Toluene 98.0179 0.393844 1.58824 100 Ethylbenzene 99.3439 0.138567 0.517514 100 o-Xylene 99.475 0.112052 0.4129 100 Octane 99.2219 0.163865 0.61419 100 Nonane 99.7484 0.0561604 0.19539 100 C10+ 100 2.23237E-06 3.21315E-06 100 C11Alkanes(normal) C12Alkanes(normal) C13Alkanes(normal) C14 C15 C16 C17 C18 C19 C20 C21 C22 C23 C24 C25 C26 C27 C28 C29 C30 C31 C32 C33 C34 C35 C36 Decane Total 73.4184 11.6067 14.9749 100 Remarks User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 6 of 11 Recoveries Report . . Client Name bonanza Creek ,lob: Location: Latham 14-12 . a.., , ,.,,�.,.. .e 7tw.., y, :;;- gi tea i,ii., ....a.Y a Ax 1C %- w Btatu Solved v �� r/�a -�Ya�„;, �tTl tPT'�R8C01ir~T1E� _ QM�S�'1� I�t5 :;s,�sr � a�.,.... �.., �� -�C Recovery Stream Data Source-All Inlets in Flowsheet Flowsheet ".PStream Flowsheet PStream Flowsheet) Breathing Losses Flowsheetl Working Losses Flowsheet1 Pressurized Liquid Parameters * Composition Basis Molar Flow * Summation Option Streams and Summation * Calculate Ratios False * Atomic Basis False tea`\ Y lei sET- ,; �,e fz ^ti �- \�� z ,,;+f i6-f it � �,,ri�r,.;,:: �� .. . ��.. . .� „� . ..... ..��'... ,/,, -., �.�r�.., .�„may,/� .., , Tabulated Data Flowsheet1:Breathing Flowsheet1:presurized Flowsheetl:Working - Summary Table Losses • Liquid Losses Index Ibmol/h Ibmol/h Ibmol/h Ibmol/h 002 0.000365715 0.0764481 0.000266298 0.0770801 Nitrogen 1.21792E-06 0.0131338 8.86835E-07 0.0131359 Methane 0.00068182 0.758411 0.000496472 0.759589 Ethane 0.0123177 1.10626 0.00896919 1.12755 Propane 0.0252122 2.2397 0.0183584 2.28327 i-Butane 0.00406101 0.470591 0.00295705 0.477609 n-Butane 0.0143539 1.98288 0.0104519 2.00768 i-Pentane 0.00287865 0.771717 0.00209611 0.776692 n-Pentane 0.00345355 1.18841 0.00251472 1.19438 Cyclopentane 0.00028128 0.148295 0.000204816 0.148781 Hexane 0.000686858 0.73804 0.00050014 0.739227 Cyclohezane 0.000177888 0.297022 0.00012953 0.297329 Isohexane 0.00146077 1.13102 0.00106367 1.13354 Heptane 0.00038526 1.41983 0.00028053 1.4205 Methylcyclohexane 0.000128542 0.461389 9.35985E-05 0.461611 2,2,4-Trimethylpentane 2.14848E-06 0.00715013 1.56443E-06 0.00715384 Benzene 7.98128E-05 0.140713 5.81161E-05 0.140851 Toluene 5.03547E-05 0.303157 3.66661E-05 0.303244 Ethylbenzene 5.53199E-06 0.101312 4.02815E-06 0.101321 o-Xylene 7.5704E-06 0.212301 5.51243E-06 0.212314 Octane 0.000108536 1.37773 7.90311E-05 1.37792 Nonane 2.32543E-05 1.02776 1.69328E-05 1.0278 C10+ 5.66973E-10 5.62836 4.12845E-10 5.62836 C11Alkanes(normal) 0 0 0 0 C12Alkanes(normal) 0 0 0 0 C13AIkanes(normal) 0 0 0 0 C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright O 2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 7 of 11 Recoveries Report 1 r '' Client Name: •. • Bonanza Creek Job: '4 : Location: Latham 14-12 . . . Tabulated Data Flowsheetl:Breathing Flowsheet1:Pressurized Flowsheetl:Working Summary Table- Losses Liquid Losses Index Ibmollh ... . lbmol/h.. Ibmol/h Ibmol/h ` C30 I 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 Total 0.0667235 21.6016 0.0485851 21.7169 Remarks oiri/ 'r ail;% . M: / Sioos . alv6t -. . . ,.,.,,,.,. ,.... . .-:,: .;,,./r. Oo►>r�I,pt3rte�ilg,�couerj�s ��a �,s.�ee��l,D.ut�e;,_. .. " Recovery Stream Data Source-All Outlets in Flowsheet Flowsheet PStream . •Flowsheet • PStream Flowsheetl Flashed Liquid Flowsheetl Total Tank Emissions Flowsheet1 Sales Gas zs..ac rric v x,, .1. _- /a=,.:C yz ,>'�� la �',ri; 'e".. �v • Parameters * Composition Basis Molar Flow * Summation Option ' Streams and Summation ' * Calculate Ratios False * Atomic Basis False Tabulated Data Flowsheet1:Flashed .Flowsheetl:Sales;G„as ::".= Flowsheetl:Total Tank Summary Table Liquid ' ' Emissions Index lbmol/h .... ... Ibmol/h " Ibmol/h Ibmol/h , CO2 0.000893736 0.0574695 0.0187169 • 0.0770801 Nitrogen 4.30191E-06 0.0124939 0.00063765 0.0131359 Methane 0.00178044 0.66526 0.092549 0.759589 Ethane 0.0452105 0.648749 0.433588 1.12755 Propane 0.429969 0.6888 1.1645 . 2.28327 i-Butane 0.196408 0.074046 0.207155 0.477609 n-Butane 1.02531 0.232209 0.750161 2.00768 i-Pentane 0.574858 0.040256 0.161578 . 0.776692 n-Pentane 0.945318 0.0485656 0.200497 . 1.10438 Cyclopentane 0.127707 0.00398684 0.0170872 . 0,148781 Hexane 0.686727 0.0099441 0.0425561 0.739227 Cyclohexane 0.282003 0.00290271 0.0124236 • 0.297329 Isohexane 1.02291 0.0207788 0.0898509 1.13354 Heptane 1.38622 0.00678404 0.0274909 1.4205 Methylcyclohexane 0.45052 0.00215906 0.00893131 0.461611 2,2,4-Trimethylpentane 0.00697358 3.52178E-05 0.000145049 .0.00715384 Benzene 0.131552 0.00176926 0.0075292 0.140851 Toluene 0.297233 0.00119431 0.00481624 0.303244 Ethylbenzene 0.100656 0.000140398 0.000524351 0.101321 o-Xylene 0.211199 0.000237901 0.000876643 0.212314 Octane 1.3672 0.00225793 0.00846302 1.37792 Nonane 1.02522 0.000577218 0.00200822 . 1.0278 C10+ 5.62836 1.25646E-07 1.80848E-07 5.62836 C11Alkanes(normal) 0 0 0 0 C12AIkanes(normal) 0 0 0 0 C13AIkanes(normal) 0 0 0 0 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 8 of 11 Recoveries Report Client Name: Bonanza Creek :." Job: Location Latham 14-12 Tabulated Data Flowsheetl:Flashed Flowsheetl:Sales Gas Flowsheetl:Total Tank Summary Table Liquid Emissions Index Ibmol/h Ibmol/h Ibmol/h Ibmol/h C14 0 0 0 0 C15 0 0 0 0 C16 0 0 0 0 C17 0 0 0 0 C18 0 0 0 0 C19 0 0 0 0 C20 0 0 0 0 C21 0 0 0 0 C22 0 0 0 0 C23 0 0 0 0 C24 0 0 0 0 C25 0 0 0 0 C26 0 0 0 0 C27 0 0 0 0 C28 0 0 0 0 C29 0 0 0 0 C30 0 0 0 0 C31 0 0 0 0 C32 0 0 0 0 C33 0 0 0 0 C34 0 0 0 0 C35 0 0 0 0 C36 0 0 0 0 Decane 0 0 0 0 Total 15.9442 2.52062 3.25208 21.7169 Remarks ..... r;;; ✓,.. !- i -.!.!V:7: .> ,...,.,. aia.,.. .\Ctr' .... .,..., a� �'s ///ri,.. \k;...... 4g Coa ipon n Recoverle ,, Flowsheetl LOSse oo#.; %�` g tatus Salved Reference Stream Data Source-All Outlets in Flowsheet Flowsheet PStream Flowsheet PStream Flowsheet1 Flashed Liquid Flowsheet1 Total Tank Emissions Flowsheet1 Sales Gas ...�7�a ' T:.a��»„ ,'� ; „ ?'N>g )N ailli >.`Yrd; s..i -:.- .>.. .. ,..7.:-'.—,.-:., '',711,'""-"•-7.:..,:,;:.l,-.,7S'� 71z•741,....,r,..;.,.., Recovery Stream Data Source-All Inlets in Flowsheet Flowsheet PStream Flowsheet PStream Flowsheet1 Breathing Losses Flowsheetl Working Losses Flowsheet1 Pressurized Liquid ._, iiiiti „<7 T�<t ,.,s,. .,✓i ,V4 �:4:.� ter- wr ; "�� r/iyii,7.7r z.....c: Parameters Composition Basis Molar Flow * Summation Option Summation Only Calculate Ratios False " Atomic Basis False Tabulated Data Summary Table Index Ibmol/h CO2 1.10143E-16 Nitrogen 1.89308E-17 Methane 9.91287E-16 Ethane 1.32172E-15 Propane 4.40572E-16 i-Butane 1.10143E-16 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 9 of 11 Recoveries Report • Client Nanl'e: -. 'Bonanza Creek :Job: Location: 'Latham 1442 Tabulated Data Summary Table Index Ibmol/h n-Butane 0 i-Pentane 2.20286E-16 n-Pentane 2.20286E-16 Cyclopentane 2.75358E-17 Hexane -3.30429E-16 Cyclohexane -5.50715E-17 Isohexane -4.40572E-16 Heptane -4.40572E-16 Methylcyclohexane -1.10143E-16 2,2,4-Trimethylpentane -2.58148E-18 Benzene 0 Toluene 0 Ethylbenzene -1.37679E-17 o-Xylene -2.75358E-17 Octane 0 Nonane 0 C10+ -3.52458E-15 _ C11AIkanes(normal) 0 C12AIkanes(normal) 0 C13Alkanes(normal) 0 C14 0 C15 0 C16 0 C17 0 C18 0 C19 0 C20 0 C21 0 C22 0 C23 0 C24 0 C25 0 C26 0 C27 0 C28 0 C29 0 C30 0 C31 0 C32 0 C33 0 C34 0 C35 0 C36 0 Decane 0 Total -3.52458E-15 �4vYv... ��\ / _ .a;*mv�\.,,i/r.�.�-ate ,...._, „ ,,,,,,.,r.,,. ..i viyii,�..- '" -�:. � .'� �.w��v��^ �.v ,,,,,,,, „T�, r�/i<��.' .oi'%rs Remarks r, riir �r d, , iii..�» �ir,.r.' .:.,.. _ ��... ..... r/is a��`�v _ - �i,'.,,..� �'!.� ��s.�a,n�wv�3, ,..i/%i.;��. in .,�i,�i�rl r rrifi rr... ....aa��.,,,,i�� ., �, Reference Stream Data Source-All Inlets in Flowsheet Flowsheet PStreaml Flowsheet PStream Flowsheet1 Breathing Losses Flowsheetl Working Losses Flowsheetl Pressurized Liquid %rte a H y*User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bbl tanks.pmx Page 10 of 11 Recoveries Report Client Name: Bonanza Creek Job: Location: Latham 14-12 apt Recovery Stream Data Source-All Outlets in Flowsheet Flowsheet PStream Flowsheet PStream F6owsheet1 Flashed Liquid Flowsheet1 Total Tank Emissions Flowsheet1 Sales Gas Parameters * Composition Basis Molar Flow * Summation Option Streams and Summation * Calculate Ratios True * Atomic Basis False Tabulated Data Flowsheet1:Flashed Flowsheet1:Sales.Gas Flowsheet1:Total Tank Summary Table Liquid Emissions Index CO2 1.15949 74.5582 24.2823 100 Nitrogen 0.0327493 95.113 4.85426 100 Methane 0.234396 87.5815 12.1841 100 Ethane 4.00963 57.5363 38.4541 100 Propane 18.8313 30.1673 51.0014 100 i-Butane 41.1232 15.5035 43.3734 100 n-Butane 51.0694 11.566 37.3645 100 i-Pentane 74.0137 5.183 20.8033 100 n-Pentane 79.1472 4.06618 16.7867 100 Cyclopentane 85.8356 2.67967 11.4848 100 Hexane 92.898 1.3452 5.75684 100 Cyclohexane 94.8454 0.976261 4.17838 100 Isohexane 90.2403 1.83308 7.92657 100 Heptane 97.5871 0.477582 1.9353 100 Methylcyclohexane 97.5975 0.467724 1.93481 100 2,2,4-Trimethylpentane 97.4801 0.492292 2.02757 100 Benzene 93.3984 1.25612 5.34552 100 Toluene 98.0179 0.393844 1.58824 100 Ethylbenzene 99.3439 0.138567 0.517514 100 o-Xylene 99.475 0.112052 0.4129 100 Octane 99.2219 0.163865 0.61419 100 Nonane 99.7484 0.0561604 0.19539 100 C10+ 100 2.23237E-06 3.21315E-06 100 C1 lAlkanes(normal) C12Alkanes(normal) C13AIkanes(normal) C14 O15 C16 C17 C18 C19 C20 C21 C22 C23 C24 C25 C26 C27 C28 C29 C30 C31 _ C32 C33 C34 *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pna Page 11 of 11 Recoveries Report y ' Client Name. 'Bonanza Creek Job: Location: I Latham 14-12 _ Tabulated Data Flowsheetl:Flashed Flowsheetl:Sales Gas Flowsheetl:Total Tank I Summary Table Liquid Emissions Index C35 C36 Decane Total 73.4184 11.6067 14.9749 100 Remarks User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. Simulation Initiated on 3/10/2020 1:54:03 PM Latham 14-12_50 psig_500bb1 tanks.pmx Page 1 of 1 • 'Energy Budgets Report • . Client Name: Bonanza Creek Job: t r cation Latham 14-12 • . .. • PoVv r,Budget Pcdj Ct Power Budget 4.,._:.. °ved.. Parameters Net Power hp Total Power Required hp Total Power Supplied hp External Energy Onl True 9liev e iii/ Remarks �aiy✓ a g i:,. °' ;f, 'ay'',/Hest Budgeter Pbject eat,$ fidget.,: :, .:I8tatus ..Solved Parameters Net Duty Btu/h Total Duty Required Btu/h Total Duty Supplied Btu/h External Energy Only True Remarks is- a \� >: 'a \ :• v ti:a Parameters Net Power hp Total Power Required hp Total Power Supplied hip External Energy Only True Remarks y !/li.. � ,.,,,..,..�,..,,. � .sr-�,.,.,. ., �ii'� .:. .:. ,,;,',%yi; ,_. '��?',.!,�y4!!i �_�. - -.. �i ,,.,ak.. .,. ._.... ,.;,:.�.�.�.i_. .. Heat Budget=F.lo rstteet1;Heat:Budget i Status iveJ Parameters Net Duty Btu/h Total Duty Required Btu/h Total Duty Supplied Btu/h External Energy Only True Remarks *User Specified Values ProMax 5.0.19050.0 Licensed to SLR International Corporation and Affiliates ?Extrapolated or Approximate Values Copyright©2002-2019 BRE Group,Ltd. • Condensate Tank Regulatory Analyzk Worksheet The regulatory requirements below are determined hosed an requested emissions. 1.Ape uncontrolled amelemIssions from navaua source greaterthanEM lRegutaton 3,Part A,aetlon ]al,2.'stile _�• /n a1./31nno2lsa PBMema05a10efinR ns112 an and Section 2!wadtnm gudamem,andfatyerappllIXbA*7 3 A Ve hn1D m aremras greaterman 10'MY lRegu alan3 Part 0,ar Sno ULana 1,Are oiwontrcetl ssrnsfrom an coda wants from this individual saute rate man xTrr lRegvhtlon3,PanA.smwn DxaP B�� anAPOg Dokot v w g + x,tithe cmnmetfonrote lsevtednal prlorto12/30/2001and not moaned akal2nlno0xlsc PS Memo 05n10wnxmsllxandlla andsdmnx foraddttlonal gwdammorpwanmaheraPPAcabgrt02 el 0o to naquesuon 3.Arc total facilitym ne grater-thanE TM Nat greater thane Tr,or CO emissions greater than 10 TRY IReeletion 3.Pan e,sectfnl.0.x1, Source Require.permit 1. cont.area or any ozone non.attaMreent area or rea,n located n the e hr ozone 2.Is'Ns storage tank looted at an oil and gas apon and Ptodun ea/ma 44511asddp tmnl = Faco ndrotdthe 3 Is thIsnx mofa n pug at n,wtu as comp eo.sd en oral ,.eg so is sub. Sae.. —General Requirements for Mr a tank hen Control q pm rat—.mention of Leakage section IRO rd R 55Wramemss 1.Is this storage rank located the g.nrosea control area oranv ozone nomanelnment•ra omnafmmat/mahnten•raearea) 'ioa Continue W erminml 2.Is thissturage tank located at a natural gas promfrg t,s Plan -Von sublet t 3.Dark n°leg ran emissions and have uncontrolled actual emesaore greatermana equalmz too per yarVOC, Source is subject 6atIf Control Requlrementst sectloo MIL. oral Requhtemnls for.Pdlutlon Control Equipment—Prlentlon d Leakage Colorado...don 7,5.r.fon 1.Is thls tank located at a 6on/stor nt'6located at anl oil and as aleloratfon and production operation,uell production faanityar natural gas compressoratatton'or natural gas processing Plant, M1au 3.Kt.rondan•ate storage tank a feted roorstorage tan. Go to the nmt guest. 9.Are Uncontrolled acluaremIsslans.oftus storage tank equal tear gmtertnan6 tons nor Year ,4 1411 Source Iss bjento parts a mu Section — fm P Equipment and Prevention of isslma Yaq dMtrot andMonI,oHn PrmblMa Section ents 5.Deco onhy'st d'Iuldsi 1,-.W,Vid5ourte Is subject to all vravLsbm enra sad,.nii.c.2•capture and monrtoringforstorage-ranks Wed wIth Pollutbn Control Equipment Pert 60.5u he. suMords of P•dorm•nce for your§o°atonicuaerd1teraa• )6)2 700) era(0)6472 002211 2.Don ldl20i413 �'ag g Tankbnd sublet rvsPs a.Does the vessel has afdsg c•paMvl.tthan oaqualto1s30.514 47'1-10,000 e04 used for petroleum'or condensate stored,processed,ortreatea Plato asmytransfer'as aenad In 60.11115, 3.Walt.condensate storage tank .a(me defnnon•907 oxl an yi,1930 42i the deliniton orstarage. n - R 5 v1u a kH 5.Does stmagewsel st�a"volatile organcR 1 bj eg n60111b, s,9 4.Dom the 5,Does stow amac!m gads oral exempt.. N+t tan mat essd.pra.�a�f�.Idelgndtoopenteloacas orx9as war l'Es,,WI and wrzma emrsamn•tomeamosphere160.11oNd11Elp;or ,g b:nndclflnmp.avls greater than or equal tolslm 1`550 Bell and mores a llquidwltne m•vrmumtmevapor gmsure•less than 3.s kge(5u.110Nb1N;or c.The a co t m M'1,2 e62).4lasOen 151 nil,oesti and stores 21.1dwltNa murmur,true vapor pressure`less than 15.50alw.la0bM 7.Don uagenk meet empnons from control rquremems. a.TM dear gn a m1'nts Berland sturesalle,olwrths maemum true tape o 3,5 kpa hut WI than5.2 kW, to 75 BBL]but less than 151 m'I-550 Saki tn•momomtry PO q Pressure V..tnanoua muokP.wt askh•nx,6YP., 1 >' , b Mssin sfr(v...t6R. 49 em wn6o zubP•rt 0000(000D.,x.ded.afP.rterm.ae 3orerda oR•ndu•anlca.vroductton,T.•rwmwfnnad of en 1.Is this mndeaaatestnnge veal located at a 1,01,In the anshoreoll and natural gas pmdualonaegwent,natural gas pram.,segment or natural astanamisston and storage segment✓the industry, doted the 2. a this an et tell )between August 25 2011 and 3egemWi6,20157 roe Go to the qumtbanad 3. condensate stone sg>==onstructed,r 1 1 dember16,20157 N Rim\ krs not subject NSFS a.Ares potential we emissions'Pram the Indli4dual storage vessel greaterthan or equal to5 tons per year, nk Is not subject RSPB 5.Dom.'s condensate storage 4 ,rage vessel'per 505430(60.54300 oa 6.Is the s vessel subject to ad controlled nacoownce with requirements emmrage vessels In.aR Part 50 subpart kb or-40 csR Parte subpartxH, :gyi8OP homgeTor.,:s vet: sew usp5�2r Now curry datarrnIned to be sublaa 0000/0000 oem6mm o above tons gryerVOC on<h•pelkab0e7 d.rmlo•tin ro man m sal..to ry 600 5P5000D/70 par 6o.s3551•gx1/5u.536sa1•IIx1•v.n if pm...1.C cop below 5 ton per year] u• 40 CFR Part 63 suborn MARHH.nll and o•s PndwronsacIlNe9 ].Ist s an c6 1641 wog criteria: - '.cx Ito tlnue You havelndlatadkhe a.Afro Rytdat Pr...upgmaesorsstoredhydlrocarbonll W (53.6010(M the • . • b. naturalploy to the paint at whla natural s mere the natural gastnnsmbalen and storage source categorvgria dmvena _doer'(53.,52ol13)I, 2.Is theta,.wtdattd4200. Nita- p4f 24M2242,4 Tanklsnoeu4.2MAn 3,Dom t4. hetank matt' prc not ton[evaselwInssx6li on e, wehthep,Subpart 6]. 4, 5.Is the t subject tomrrtro tank meat the elrqurdmenu undvaotm Part 6a,submnXborwbpan0000,rat • ,22,32122342,2,63,64 041-212141 §s PrmM16m�iunspmnwl�wnaa� -. 463.773-Monitoring •• 463.774-Recordteepine • - - - _ - RAm MAW fa q old eaguiatwn,does not applyAND Ow tank Is In the non-artilment area.If thatank moots both cr.,s,tit.n revIew RAU requamem•. ElIsclalmer inf.,document ssels opamfora wM elerminmp applicabikv ore.afn requireme.of the Clean AC414.es impremen121662111 Control c6mmu' its.TM1damn..iof a ode regulation a Osten*. M en gee.ms may no.apps,hapadkular d upon M andchange'substitute for any lav -' ake,,or other legally binding requeemenl and is not legally enforceable.In the event of any Gone.between the language of this document end the language of4Fe 0leen:V est.Ss Imdereen log regulafbns,and A40aaliy control comnissionregulalb=s,Ne mop.,4471404616(041 repuls107...it,The ndalwy language..as'rec724574"may.""ShOeht'and'can;Is Intended lerpele andrec mendatbn use to describe controllingrMnirements under the terms of the clean An Act and AiOally control colnnissbn rsgdhtionsn Old Ws document Mandatory t es6ellsh legally requirementsu�nd 9110417 Produced Water Storage Tank(s)Emissions inventory Section 01-Administrative Information 'Facility AIRS ID: 123,„'.. County PI t Pint Section 02-Equipment Description Details Detailed Emissions Unit Description: 06,41.390•,,,,y,4,,, ��t xetl wof #t t &h sipxageafcadaeegd zajez ice„3 .`�\\O\\� Emission Control Device , ] `• BodosorU'Rr1aaH5$(on Desnces = Description: •! //// .. \ ,,;a Requested Overall VOC&.HAP Control Efficiency jj Section 03-Processing Rate Information for Emissions Estimates Primary Emissions-Storage Tank(s) Actual Produced Water Throughput= 6S;39S'{Barrels)bbl)peryear Requested Permit Limit Throughput= 78,a7i+::'Barrels(bbl)peryear Requested Monthly Throughput= 6555 Barrels(bbl)per month Potential to Emit(PTE)Produced Water Q\ Throughput 78,475.;Barrels(bbl)per year Secondary Emissions-Combustion Device(s) Heat content of waste gas 14965X;Btu/scf Volume ofwaste gas emitted per BBL of liquids ��j/ produced= /�/�/ 3021$scf/bbl Actual heat content of waste gas routed to combustion device= 3521.0 MMBTU peryear Requested heat content of waste gas routed to combustion device= 4220,4 MMBTU peryear Potential to Emit(PTE)heat content of waste gas routed to combustion device= 4226.4 MMBTU per year Control Device Pilot Fuel Use Rate• scth OA MMscf/yr Pilot Fuel Gas Heating Value: /f?�-;,Btu/scf U.0 MMBTU/yr Section 04-Emissions Factors&Methodologies ,Y7:7114-11 Will this storage tank emit flash emissions? t �� Emission Factors Produced Water Tank Uncontrolled Controlled Pollutant (lb/bbl) (lb/bbl) Emission FactorSeorce (Produced Water (Produced Water Throughput) Throughput) VOC 2 V.0131 r nshcdesfiashj_Deco- Benzene S8t}7d qC D.n094 a£e brae tca } ran Toluene 4",.$ 0,0930 Ethylben ene //%%/�_ i-i,0000 Piedv€9 Wsnor Xylene ;;m 0,0000 „97911cea, $ - a`r n-Hexa e '$$$$$$”1-91 IF 0,UV._ia ₹'coduced WwtecSta�: 224TMP :\ O,1000 ArnaueerdWot r5tato E_F_)iScka a. Control Device Uncontrolled Uncontrolled Pollutant (Ib/MMBto) (lb/bbl) _ Emission Factor Source (waste heat (Produced Water combusted) Throughput) PM10 Dt₹Q7$�� 9.0104:3 '`'r1f 1.4,ZfRirPloili6� PM2.5 StvR7$5`a�4�"` 9.01041 2#k„, $Y)PARS333'lV 2") y NOx //iD�oHBVD 0,00366 h atra�t�r�ircpxj CO ,., 0.31000 i. 0.G167J t3 ) i4 „; Section 05-Emissions Inventory Potential to Emit Actual Emissions Requested Permit Limits Requested Monthly Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled Uncontrdled Controlled Controlled (tons/year) (tans/year) (tans/year) Bons/year) to ohs/month) VOC 10.3 8.6 0:4 10.3 0.5 67.3 PM10 0.0 0.0 0.0 0,0 0.0 2.7 PM2.5 0.0 0.9 0.0 0.n 0.0 2.7 Nth 0.1 0.1 0.1 0.1 0.1 24.4 CO 0.7 U.S GS 0.7 0.7 .511.3 Potential to Emit Actual Emissions Requested Permit Limits Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled (Ibs/year) (Ibs/year) (lbs/year) (lbs/year) (Ibs/Year) Benzene 849.3 457.8 22.9 549.3 67.5 Toluene 0,0 0.0 Sit 0.0 DA Ethylbenzene 0,0 0,n 0:0 0.6 0.0 Xylene 0,0 0.0 0,0 0.0 D.0 n-Hexane 1726,5 1439.7 71.9 1726,5 86.3 224 TMP 0,0 0.0 U.S 0.0 0.0 • 6 of 13 C:\Users\Ilakocy\Desktop\Remote Working Does\package#424786\13W E1101.CP5 Produced Water Storage Tank(s)Emissions inventory Section 06-Regulatory Summary Analysis Regulation 3,Parts A,B Source requires'a permit Regulation 7,Section XVII.B,C.1,C.3 Storage tank is subject to Regulation 7,Section XV0,0,.C,2 A C.3 Regulation 7,Section XVII.C.2 Storage tank is subjek to Regutetiun 7,Section KVa.C.2 Regulation 6,Part A,NSPS Subpart Kb Storage tank is not subject to N505 Kb Regulation 6,Part A,NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 NSPS Subpart 0000a • .Storage tank is not subinct to MPS 00000. (See regulatory applicability worksheet for detailed analysis) Section 07-Initial and Period-a Sampling and Testing Requirements Does the company use a site specific emissions factor to estimate emissions? If yes and if there are flash emissions,are the emissions factors based on a pressurized liquid water sample drawn at the facility being permitted and analyzed using flash liberation analysis?This sample should be considered representative which generally means site-specific and collected within one year of the application rend ved date However,if the facility has n t been modified(e.g.,no new wells brought on line),then it may be appropriate to use an older site-specific sample. If no,the permit will contain as"Initial Compliance"testing requirement to develop a site specific emissions factor.See PS Memo 14-03,questions 5.9 and 5.12 for additional guidance on testing. s Does the company request a control device efficiency greater than 95%fora flare or combustion device If yes,the permit will contain compliance testing requirements to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 Technical Analysis Notes PIF91i lgmtsslwn6 afeper ed um3erthe concEensatelaks#AI(CSButnt 004 /R FT °, / , Section 09-Inventory SCC Coding and Emissions Factors Uncontrolled Emissions • AIRS Point Process SCC Code Pollutant Factor Control%Units 004 01 4-04-003-15 Fixed Roof Tank,Produced Water,working+breathing+flashing losses PM10 0.0090 0.0 lb/1,000 gallons liquid throughput PM2.5 0.0090 0.0 lb/1,000 gallons liquid throughput NOx 0.0872 0.0 lb/1,000 gallons liquid throughput VOC 6.2891 95.0 lb/1,000 gallons liquid throughput CO 0.3975 0.0 Ih/1,000 gallons Squid throughput Benzene 0,1657 95.0 Ih/1,000 gallons Squid throughput Toluene • 0.0900 95.0 lb/1,000 gallons liquid throughput Ethylhenzene 0.0600 95.0 lb/1,000 gallons liquid throughput Xylene 0,0000 95.0 lb/1,000 gallons liquid throughput n-Hexane 0.5208 95.0 lb/1,000 gallons liquid throughput 224 TMP 0,0300 95.0 lb/1,000 gallons liquid throughput 7 of 13 C,\Users\Ilakocy\Desktop\Remote Working Docs\Package 0424786\13WE1101.CPS Produced Water Storage Tank Regulatory Analysis Worksheet The regulatory requirements below ore determined based on requested emissions. Colorado Repulation 3 Parts A and a.ARES and Permit Requirements Source is in the reoa-Attahussant Ares ATTAINMENT 1. Are uncontrolled actual emissions from any criteria pollutants from this individual source greater than 2 TPY(Regulation 3,Part A,Section l i.D.1.a)? 2. Is the operator claiming less than 1%crude oil and is the tank located atanon-commercial facility for processing oil and gas wastewater?(Regulation 3,Part B,Section ll.D.1.M) 3. Are total facility uncontrolled VOC emissions greater than 5TPV,NOx greater than 1OTPY or CO emissions greaterthan 10TPY(Regulation 3,Part B,Section ii.D.3)? IYoo have Indicated that source Is in the Nan-Attainment Arm NON ATTAINMENT 1. Are uncontrolled emisslons from any criteria pollutants from this individual source greaterthan l TOY(Regulation 3,Part A,Section Pat a(7 i1 .in'.Source Requires an AP 2. Is the operator claiming less than 1%erode oil and is the tank located at a non-commercial facility for processing at and gas wastewater?(Regulation 3,Part 0,section l i.D.1.M) (xul�/=G to t q stion 3. Are total facility uncontrolled VOC emissions greater than 2 TPY,NOx greater than 5TPY or CO emissions greater than to TPY(Regulation 3,Part B,Section ll.D.2)? 1ety iiii Source Requires a pen I5ource requires a permit Colorado Regulation 7.Section XVII 1. Is this tank located et a transmission/storage facility? No Continue-You have lr 2. Is this produced water storage tank'located at en oil and gas exploration and production operation,Ac?production facility',natural gas compressor station'or natural gas processing plant? Yes Continue-You have it 3. Is this produced water storage tank a fixed roof storage tank? Go to the next queseic 4. Are uncontrolled actual emissions'of this storage tank equal to or greater than 6 tons per year VOC? RSource is subject to pe (Storage tank Is subieccto Regulation 7,Section XVII,5,0.1&C3 Section XVILB—General Provisions for Air Pollution Control Equipment and Prevention of Emissions Section XVII.C.1-Emissions Control and Monitoring Provisions Section XVII.C.3-Recordkeeping Requirements 5. Does the produced water storage tank contain only"stabilized"liquids?If no,the following additional previsions apply. tlM a"Source Is subject to at (storage tank Is su(i;ect to Permission 7,Section XVII.C.2 rat" Section XVII.C.2-Capture and Monitoring for Storage Tanks fitted with Air Pollution Control Equipment 40 CFR,Part 60.Subpart Kb,Standards of Performance for Volatile Oreenic Liquid Storage Vessels 1. Is the individual storage vessel capacity greater than or equal to 75 cubic meters(m)I-472 BB1s]? hx' Storage Tank is not sui 2. Does the storage vessel meet the following exemption In 60.111b(d)(4)? tgA, a.Does the vessel has a design capacity less than or equal to 1,589.874,0'("10,000 BBL]used for petroleum'or condensate stored,processed,or treated prior to custody transfer'as defined in 60.1116? 3. Was this condensate storage tank constructed,reconstructed,or modfied(see definitions 40 CFR,60.2)after luly 23,19847 t3 4. Does the tank meet the definition of"storage vessel"'in 60.1110 5. Does the storage vessel store a"volatile organic liquid(VOL)"'as defined in 60.11167 6. Does the storage vessel meet any one of the following additional exemptions: a.Is the storage vessel a pressure vessel designed to operate in excess of204.9 kPa("29.7 psi]and without emissions to the atmosphere(60.110b(d)(2))?;or b.The design capacity is greater than or equal to 151 m'("950 BB11 and stores a liquid with a maximum true vapor pressure'less than 3.5 kPa(60.110b(b))?;or c.The design capacity is greaterthan or equal to 75 M'("472 BBL]but less than 151 m'("950 BBL]and stores a liquid with a maximum true vapor pressure'less than 15.0 kPa(60.11Db(b))? 7. Does the storage tank meet either one of the following exemptionsfram control requirements: a.The design capacity is greaterthan or equal to 151 m'(^'950 BBL]and stares a liquid with a maximum true vapor pressure greaterthan or equal to 3.5 kPa but less than 5.2 kPa?;or b.The design capacity is greater than or equal to 75M'(^'472 RBI]but less than 151m'("950 BBL]and stores a liquid with a maximum true vapor pressure greater than or equal to 1&01dia but less than 27.6 kPa? .Storage'rank is not.subject to PuSP5 Xh 40 CFR.Part 60,Subpart 0000/0000a,Standards of Performance for Crude 03 and Natural Gas Production.Transmission and Distribution 1. Is this produced water storage vessel located at a facility In the onshore oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? Yes Continue-You have Jr 2. Was this produced water storage vessel constructed,reconstructed,or modified(see definitions 40 CFR,60.2)between August 23,2011 and September 16,2015? "IT ;'Go to the question 4. 3. Was this produced water storage vessel constructed,reconstructed,or modified(see definition 40 CFR,60.2)after September 18,2015? NsaPaM.Storage Tank is not sui 4. Are potential VOC emissions'from the individual storage vessel greater than or equal to?tons per year? tea&fat Storage Tank is not sul 5. Does this produced water storage vessel meet the definition of"storage vessel"'per 60,5430/60.5430a? NA 6. Is the storage vessel subject to and controlled In accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HI-I? (Sterne Tank is rsm.sgblect to NSPS 11000 (Nate:If a storage vessel is previously determined to be subject to NSPS 0000/00000 due to emissions above 6 tans per year VOC on the applicability determination date,it should remain subject to NSPS 0000/00000 RACT Review RACY review is required if Regulation 7 does not apply AND if the tank is In the non-attainment area.If the tank meets both criteria,then review PACT requirements.. Disclaimer This document assists operators with determining appfcabdity of certain requirements of the Clean Air Act,its Implementing regulations,and Air Qualdy Control Commission regulations.This document is not a rule or regulation,and the analysis d contains may not appy to a particular situation based upon the individual facts and circumstances.This document does not change or substgLle for any law,regidatbni or any other legally binding requirement and Is not legally enforceable.In the event of any conflict between the language of this document and the language of the Clean Air Act„Rs implementing regulations,and Air Qualdy Control Commission regulations,the language of the statute or regulation will control The use of non-mandatory language such as 'recommend,"may,"should"and"can,"Is intended to describe APCD interpretations and recommendations.Mandatory terminology such as'must"and"required"are intended to describe controlling requirements under the terms of the Clean Air Act and Air Qualdy Control Commission regulations,ht.(this document does not establish/egely binding requirements in and of itself. Hydrocarbon Loadout Emissions inventory Section 01-Administrative Information Facility AIRS ID: ��/i///%%/,. T ,.'.�\\\� �? .• County Plant Pint Section 02-Equipment Description Details • ✓/� " Description: Emission Control Device ^//7 i/!%/`" fffii 1� \\O\ Description: Englo3� sban:E4avtces ��, � Is this loadout controlled? Requested Overall VOC&HAP Control Efficiency%: Section 03-Processing Rate Information for Emissions Estimates Primary Emissions-Hydrocarbon Loadout Actual Volume Loaded= 475f Barrels(bbl)per year Requested Permit Limit Throughput= ///,,,' , 73 Q7 sBarrels(bbl)per year Requested Monthly Throughput= 0061 Barrels(bbl)per month Potential to Emit(PTE)Volume Loaded= 0'-',170 41,b.Barrels(bbl)per year Secondary Emissions-Combustion Device(s) Heat content of waste gas= 21S:W Btu/scf Actual Volume of waste gas emitted per year= 107980 scf/year Requested Volume of waste gas emitted per year= 107900 scF/year Actual heat content of waste gas routed to combustion device= 244 MMBTU per year Requested heat content of waste gas routed to combustion device= 244 MMBTU per year Potential to Emit(PTE)heat content of waste gas routed to combustion device= 244 MMBTU per year Control Device Pilot Fuel Use Rate: • P �'/%/scfh 0.0 MMscf/yr Pilot Fuel Gas Heating Value: �% Btu/scf 0.0 MMBTU/yr Section 04-Emissions Factors&Methodologies Does the company use the state default emissions factors to estimate emissions? Does the hydrocarbon liquid loading operation utilize submerged fill? ate+ 3,e state default emissions factors may be used to estimate emissions. Emission Factors Hydro arbon Loadout Uncontrolled Controlled Pollutant (lb/bbl) (lb/bbl) Emission Factor Source (Volume (Volume Loaded) Loaded) VOC 2.30E-01 1.13E-02 .. oadout State E? Benzene 4.100-04 2,05E-OS s n Loadout Siato E.6 i Toluene 0.001,00 0,00E+00 Cmt€€emsa .. ° `�• Ethylbenzene 0.00E+00 0.00E4,00 Xylene X0.001000 0,041E+00 n-Hexane 3.00E-03 1.80E 04 Cmas3ensa a ,;�`, 224 TMP 0.000000 0.00E+00 n }T,y'y.s,≥s r Control Device Uncontrolled Uncontrolled Pollutant (Ib/MMBtu) (lb/bbl) Emission Factor Source (Volume (waste heat combusted) Loaded) PM10 Ci0905 \ at? '" 231f05 AAP-4ZTa 3,-,140/(E114` € PM2 5 % 0,097,5///// - 1.01 00 :fti3 s' Q,�P ,"+;< SOx 1.83E-06 NOx 5.0003 A 201E04 ZiN g2 A 2% CO '5310f7 �� ii 5.020-04 ,,,_,;, „n ndustcha,Lager, .-.. 9 of 13 C:\Users\Ilakory\Desktop\Remote Working Docs\Package#424786\13WE1101.CP5 Hydrocarbon Loadout Emissions inventory Section 05-Emissions Inventory Potential to Emit Actual Emissions Requested Permit Limits Requested Monthly Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled Controlled (tons/year) (tons/year) (eons/year) (tons/year) (tons/year) (Ibs/month) PM10 0.00 0.00 0.00 0.04 0.00 0 PM2.5 0,00 0.00 0.00 0.00 0.00 0 SOx 0.00 0.00 0.00 0.00 0.00 0 NOx 0,01 0.01 0.01 0.01 0.01 1 VOC 9.26 0.36 0.4E 9.26 0.4E 70 CO 0.04 0.04 0.04 0.04 0.04 0 Potential to Emit Actual Emissions Requested Permit Limits Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled - Uncontrolled Controlled (Ibs/year) (Ibs/year) (Ibs/year) (Ibs/year) (Ihs/year) Benzene 32 32 2 32 2 Toluene 0 0 0 0 0 Ethylbenzene 0 0 0_ 0 0 Xylene 0 0 0 0 0 n-Hexane 283 283 14 283 14 224 TMP 0 0 0 0 0 Section 06-Regulatory Summary Analysis Regulation 3,Parts.A,B Source requires a permit RACT-Regulation 3,Part B,Section III.D.2.a The loadout must be operated w?ch submerged fill to satisfy RACF. (See regulatory applicability vnrksheet for detailed analysis) Section 07-Initial and Periodic Sampling and Testing Requirements Does the company request a control device efficiency greater than 95%for a flare or combustion device? y 'a, If yes,the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08-Technical Analysis Notes a .RCS g e{htsston a ecmi a oF27 11erh)seco'ndenFltetanks(AIR4P }Ak• / - / - A - ; Section 09-Inventory SCC Coding and Emissions Factors Uncontrolled Emissions AIRS Point# Process# SCC Code Pollutant Factor Control% Units 006 01 4-06-001-32 Crude Oil:Submerged Loading Normal Service(S=0.61 PM10 0.00 0 lb/1,000 gallons transferred PM2.5 0.00 0 lb/1,000 gallons transferred SOx 0.00 0 lb/1,000 gallons transferred NOx 0.01 0 lb/1,000 gallons transferred _ VOC 5.6 95 lb/1,000 gallons transferred CO 0,02 0 lb/1,000 gallons transferred Benzene 0.01 95 lb/1,000 gallons transferred Toluene 0,00 95 lb/1,000 gallons transferred Ethylbenzene 0.00 95 lb/1,000 gallons transferred Xylene 0.00 95 lb/1,000 gallons transferred n-Hexane 0,00 95 lb/1,000 gallons transferred 224TMP 0.30 9S lb/1,000 gallons transferred • 10 of 13 C:\Users\llakocy\Desktop\Remote Working Docs\Package#424786\13WE1101.CPS Hydrocarbon Loadout Regulatory Analysis Worksheet The regulatory requirements below are determined based on requested emissions. Colorado Regulation 3 Parts A and B-APEN and Permit Requirements Source is in the Non-Attainment Area ATTAINMENT 1. Are uncontrolled actual emissions from any criteria pollutants from this individual source greater than 2 TPY(Regulation 3,Part A,Section II.D.1.a)? 2. Is the loadout located at an exploration and production site(e.g.,well pad)(Regulation 3,Part B,Section II.D.1.l)? tl • 3. Is the loadout operation loading less than 10,000 gallons(238 BBLs)of crude oil per day on an annual average basis? 4. Is the loadout operation loading less than 6,750 bbls per year of condensate via splash fill? r 5. Is the loadout operation loading less than 16,308 bbls per year of condensate via submerged fill procedure? 6. Are total facility uncontrolled VOC emissions greater than 5 TPY,NOx greater than 10 TPY or CO emissions greater than 10 TPY (Regulation 3,Part B,Section II.D.3)? �,u You have indicated that source is in the Non-Attainment Area NON-ATTAINMENT 1. Are uncontrolled emissions from any criteria pollutants from this individual source greater than 1 TPY (Regulation 3,Part A,Section II.D.1.a)? I"44'Go to next 2. Is the loadout located at an exploration and production site(e.g.,well pad)(Regulation 3,Part B,Section II.D.1.I)? y ,'` Go to the i 3. Is the loadout operation loading less than 10,000 gallons(238 BBLs)of crude oil per day on an annual average basis? , •y ;".Go to next 4. Is the loadout operation loading less than 6,750 bbls per year of condensate via splash fill? N3 Go to next 5. Is the loadout operation loading less than 16,308 bbls per year of condensate via submerged fill procedure? Go Go to next 6. Are total facility uncontrolled VOC emissions from the greater than 2 TPY,NOx greater than 5 TPY or CO emissions greater than 10 TPY (Regulation 3,Part B,Section II.D.2)? YP§, The loadoi (Source requires a permit 7. RACT-Are uncontrolled VOC emissions from the loadout operation greater than 20 tpy(Regulation 3,Part B,Section III.D.2.a)? ND The loadol [The loadout must be operated with submerged fill to satisfy RACT. Disclaimer This document assists operators with determining applicability of certain requirements of the Clean Air Act,its implementing regulations, and Air Quality Control Commission regulations. This document is not a rule or regulation, and the analysis it contains may not apply to a particular situation based upon the individual facts and circumstances. This document does not change or substitute for any law,regulation, or any other legally binding requirement and is not legally enforceable. In the event of any conflict between the language of this document and the language of the Clean Air Act„its implementing regulations, and Air Quality Control Commission regulations, the language of the statute or regulation will control. The use of non-mandatory language such as"recommend,""may,""should,"and"can,"is intended to describe APCD interpretations and recommendations.Mandatory terminology such as "must"and"required"are intended to describe controlling requirements under the terms of the Clean Air Act and Air Quality Control Commission regulations, but this document does not establish legally binding requirements in and of itself. COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION FACILITY EMISSION SUMMARY Bonanza Creek Energy Operating Company Name Company LLC County AIRS ID 123 History File Edit Date 4/7/2020 Plant AIRS ID 9AC2 Ozone Status Non-Attainment Facility Name Latham 14-12 Production Pad Last Modified By: Lauraleigh Lakocy EMISSIONS-Uncontrolled(tons per year) EMISSIONS With Controls(tons per year) POINT PERMIT Description PM10 PM2.5 H2S S02 NOx VOC Fug VOC CO Total PM10 PM2.5 H2S S02 NOx VOC Fug VOC CO Total REMARKS AIRS ID HAPs HAPs Previous FACILITY TOTAL 0.3 0.3 0.0 0.0 46.4 937.6 0.3 45.9 35.4 D.2 0.2 0.0 0.0 -7.5 65.4 0.3 19.8 7.8 From March 2018 Previous Permitted Facility total 0.2 0.2 0.0 0.0 45.5 929.4 0.0 45.2 35.4 0.2 0.2 0.0 0.0 7.5 65.4 0.0 19.8 7.8 001 13WE1038.CN: SI RICE Gas-lack Gj230,;40RB,46 HP Cancel led 7124/2510-5°'rte nalonger exists at the 1SN:51157)compressor engine ' ,`'; 00 conic y 002 13WE1089.CN SI RICE GasJack GJ230,4SRB,46 HP Cancelled 7/10/2213-Sousse no longer nit at the (ON:50407)compressor engine ,-F', facility. Six(6)400 bbl and three(3)500 bbl fixed 0.1 0.1 1.1 669.4 5.2 0.1 0.1 1.1 33.5 5.2 Updating SSEF,throughput 003 13WE1101 roof condensate storage vessels,PLUS 21.3 1.1 pilot light emissions One(1)400 bbl and one(1)300 bbl fixed 0.1 10.3 0.7 1.1 0.1 0.5 0.7 0.1 Converted from SPUD to CP,state EF 004 13WE1101 roof produced water storage vessels 005 GP02 SI RICE ArrowA-62,4SRB,80 HP,(SN: 0.1 0.1 11.4 0.3 4.5 co 0.1 0.1 1.9 0.3 3.7 0.0 No Change 6B12C004125) _ 006 13WE1101 Loadout 00.09.3 0.0 0.2 0.0 0.5 0.0 0.0 Updating throughput.state EF 0.3 - ,(, 0.3 Cancelled 4/17/2015-Emissions are below APE 007 13WE11D1,CN Fugitives GO 0'O reporting threshold One(1)Sandpiper G18(SN:1981450) Cancellation Reed 03/05/2020(no longer exists) 008 13W01101.CN natural gas driven pneumatic pump used 6:0 : 0.0 for water transfer... SI RICE Caterpillar 03304NA,4SRB,95 Cancelled 6/6/2015-Source no longer exists at the 009 GP02.CN 00 0.0 HP(SN:N4F01709) facility. SI RICE Caterpillar G3306NA,4SRB,145 Cancelled 03/30/18.Source no longer exists at the facility: 010 GP02.CN HP(SN:6GX00226) 0.0 0'.0 On(1)Sandpiper G1F(SN.2076836) 0:2 Cancelht oy Rec'd 03/05/2020(no longer exists) 011 13Wt1101.CN natural gas drven pneumabo pump used 'OM 0.0 for water transfer. 012 13WE1101 Emergency Flare 00 0.0 Cancelled'7/25/2517•Source was never installed 013 13WE1101.CN LP Separator Gas u0 0.0 Cancellation Recd 04107/2520-source no longer exists One(1)Sandpiper GlF(SN:4068358) Cancellation Recd 03/01/2025(no longer exists) 014 13WE1101.CN natural gas driven pneumatic pump used 0.0 0.0 for heat trace. 015 GP02 SI RICE Caterpillar G3306TA,4SRB,203 0.1 0.1 32.5 2.0 32.5 0.6 D.1 0.1 4.0 2.0 7.9 0.6 No change HP(SN:07Y07152) XA Produced Water Vaults 0.8 0.1 0.8 0.1 Inisignificant Source per Form APCD-102 reed 4/7/20 XA Heated Separators D.1 0.1 1.0 0.1 0.8 0.0 0.1 0.1 1.0 0.1 0.8 0.0 Inisignificant Source per Form APCD-152 reed 4/7/20 XA Pneumatic Devices 3.2 0.1 3.2 0.1 InisIgnificant Source per Form APCD-102 reed 4/7/20 XA Compressor Slowdown 0.2 0.0 0.2 0.0 Inisignificant Source per Form APCD-102 reed 4/7/20 0A Fugitive Equipment Leaks 0.3 0.0 0.3 0.0 InisIgnificant Source per Form APCD-102 recd 4/7/20 VOC:Syn Minor(NANSR and OP) NOx:True Minor(NANSR and OP) FACILITY TOTAL 0.4 0.4 0.0 0.0 46.1 695.6 0.6 43.7 23.4 0.4 0.4 0.0 0.0 8.3 41.1 - 0.6 18.3 1.9 CO:True Minor(PSD and OP) HAPS:Syn Minor n-Hexane - Permitted Facility Total 0.3 0.3 0.0 0.0 45.1 691.3 0.0 42,9 23.3 0.3 0.3 0.0 0.0 7.1 36.8 0.0 17.5 1.7 Excludes units exempt from permits/APENs Pubcom required because source Is requesting synthetic (A)Change In Permitted Emissions 0.1 0.1 0.0 0.0 -0.4 -28.6 0.0 -2.3 minor limit under serious nonattalnment.Modeling not required based on division guidelines. Total VOC Facility Emissions(point and fugitive) 41.7 Facility is eligible for GP02 because<45 tpy (A)Change in Total Permitted VOC emissions(point and fugitive) -28.6 Project emissions less than 25 tpy Note 1 Note 2 Page 12 of 13 Printed 4/8/2020 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION DIVISION FACILITY EMISSION SUMMARY-HAPs Company Name Bonanza Creek Energy Operating Company LLC County AIRS ID 123 Plant AIRS ID 9AC2 Facility Name Latham 14-12 Production Pad Emissions-uncontrolled(Ibs per year) POINT PERMIT Description Formaldehyde Acetaldehyde; Acroleln Benzene Toluene Ethylbenzene Xylenes n-Hexane McAH 224 TRIP HAS TOTAL OW)) Previous FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0.0 9•0t it'' ..,....\ `%�'z SRO:O:IN'-' �J�qk GJY.3a'.dSRRi reel!' 'il 7 .'f::;/J .. ,�, g', ,4. " _. %'\� f=;\ � � �1'OomprassUrCnglne �s -/r � �.. i��'"� ... ��/ �. r% \\\\. 90; %. ! V:',14.104411 V0soq) pJuyaJ r.71N, at-!::,ttat.tt °, ,. ;, irr�. ... „ ,a\:r: sit(6)400 bbl and three(3)500 RN fixed roof 5152 3888 488 815 32128 145 212 003 13WE1101 condensate storage vessels,PLUS pilot 0ght mission - 004 13WE1101 One(1)400 ELI and one(1)300 bbl fixed roof 549 1727 1.1 produced water storage vessels 005 GP02 SI RICE Arrow A-62.4508,80 HP,(AN: 135 IS 10 9 3 1 .c 0.1 6BI2C004125) 006 13WE1101 Loadout 02 283 D.2 007 2299.9.9%299 2222,29929WE1201,20242N7 290,2es 7.2 •2`V5 7t•Mr 4'19,` 22.9 .229.222‘22222.29,\/alU'%Y .2.1-,, '0.15 ' '3 •IL;IIIRUya" ,1r,:: .. :21TT°•D_V c pnetl)3andpiaeralF(SN 15B145p-1 / / .'../�/ .\ \I\ /' .. \ Da 90� 22' J3StsIEa1('!'U.G 9,;2 1lgasdrnen pnalttne0• 92.ae99A.. . \ \ \... ® // r � � let' 4r: �` ., � •• / '\ BSI R[CE CetstpOfar G3304NAm49RB 8�5}E ,• F 111114./ i U0�\\\ 9OB fiF02YlNY SN N4F4170Di .. �/ �\ • \�\ alp • GP 114 6/SI RSCECetIrp,,,,,.3308NA r1SRB '+I5 HS \ t` / IIEk`N HP�sNsc�De�s� ?` \r • ,..74,,,,,,i„,„:4,0,10.4,1 ;H � �� /'`�� ii \� ,i\,.;; • ✓',,,Cwe 1 sand Iperp1f SN"p76&'18:� %-'''''5.,...,N:.'; /f :J\`C f _� AA AA. \ 010 f3w 10y. •9,07741220,&,n p•t�e Pana 'am to .: \ \ %''- �\\ay,U \A% / '\\\\\../�\\. A• , V R sxd \ :\\.\Dot- \ , r"...,..14,-,..\.„, =a'%;,; .....olr 9N9..,:/v\ OiiBP3l1wie' 7. - S ,\. ,:\s /, 412 / iiT"4J =13)NE4101 Eli»AeuiHV Flan . \,451 \ „.„O4,O, Or \\ 041.... 013 '\" a�'&13WEd101 i5i5T LE Beparulol'O 2..411 2, ' \ 42/ /r L@. \ . a 7i \\\\\\\\ ON ' ' /' a�?Rna(t an 4>enG1P(6NN"Afa6B38� \\\' \ Z\/ ,;,,,,!A; j% ,f'\T, rga. 4 •� / T3WI10 L`:y n(agile t .ah UhMSN,(Pump, rllb i y 1 \ --,,, ,-..k,.., ., .,heal tra .�, :G�`,,,,; :.'•-- �'t::•�xJ� ., ' :� a�.4�d ��a L� ,,.,., �\.. �L%9..., 015 GP02 SI RICE Caterpillar G3306TA,45R8,203 980.2 40.2 3'r.0 22.6 44.1 0.6 HP(cedW07152) XA 'Produced Water Vaults 45 141 0.1 XA Healed Separators I 24 0.0 XA Pneumatic Devices 11 ID 1 3 44 0.1 XA Compressor Slowdown 1 1 4 0.0 XA Fugitive Equipment Leaks 2 0.0 TOTAL(tpy) 0.6 0.0 0.0 2.9 2.0 0.2 0.4 17.2 0.0 0.1 0.0 0.0 23.4 Emissions with controls(lbs per year) POINT PERMIT Description Formaldehyde Acetaldehyde Acrolein Benzene Toluene Ethylbenzene Xylenes n-Hexane McOH 224 TMP HOS TOTAL 11111 Previous FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0.0 L.'.4' 1 114114'1 TIO1eE G0TJack4J239 4SR6 40 F(P(AN E ice„ a 0 \ �\ .., I r/�ir s1i5A cromoYeesor�SDgiOe 0, 1;�p;:; %"\\\":•` �` "' Sk 102E 44aoJ 4T 0J230 4586,40 VP AN r \// \ \ \ \ u9z�„ �///%��,. ..t a3Wgx039C31 �.. t rim� � �' ��' �� :��..:....y//;i/i��i�\\,. ��\t .....,..v,✓. ..,. :.SD(0)40DBendrhree(3 .' .,o, �:: %"e ,,�'� m.�94 ,.• % .,.... A; ''- Six(6)400 bM and three(3)500 bbl fixed roof 258 794 24 41 7606 7 - ' 003 13WE1101 condensate storage vessels,PLUS pilot light 1.1 emissions 004 13WE1101 One(1)400 bbl and one(1)300 bbl fixed roof 28 e6 0.1 produced water storage vessels 005 12P02 SI RICE Arrow A62,4208,80 HP,(SN: SI IS 15 8 3 I III 0.0 681202004125) 006 13WE1101 Loadout 14 0.0 0EIT M' 7'. .•11WEt001 t0100.rdoDivo&2, ' . ' . .•:...`:. 4 31 Q.. :3 ' ,T`3J\W\:\\\V1 _ ,R0 t�% \�,�` ,dna(i) @nd}21�lr CT1F(3N'1981459p' • \\ . 008 // \p\ 131Nii1nlen :OAIIal sfiok�p4abmaeapnrnpusadfpr //,\.,rc ,3 \\ \ .:- io. i/ . . ,wetcrlrn§Tat '\ it ;. .��,�? ''� ��: //--- ��\\�� %. DD9 Ga,,,, SI R b-Wa grp(Ilare'-+I 64NA�sl1•W g5 HP '9'2214 i l i 4-41m NIA A 0\� �% GP02-GN' •••,.11800E ITRILIA YO3306TN 45128',145�} i r T\ '\ HPISN BGX08228) \\-/\ 0! pJ TOi, \\ Gfne(i)S dppe GiF(51J 27t[6836) r.�;,,q. \ r 014 . 4 tE 0e 'nafural gas dmen pDeumatiap iapusedt¢r Ili \_ J 'j, `,'' ,. ,6, \ s v, \ 4aiitranwer. „i • 2 J: \ ,oe ,,v%. : 912 4) 40VJE1101'"k E1rergeltoyFlero: \\\ / \\� ' 2"'°\ 10 17l 9`111 913 / 9999 45WE510d08l LPSBUerator1as•:: //` i3 4„2�9, \ 292 22227,212WA "' / '//j 01'41)sa0apipef GIF SN$040000 I \ , tt4 /. 54/4v01fOfC naalmecesdrmefpnelanatepj\A4 4 \\`,iii io�/.4 % a �i /AAA�\:., .X �r r' .J„ rF, „r tic,...... .. /, ��... \.... „ . 015 GP02 SI RICE Caterpillar G3306TA,4500,203 980.2 40.2 37.9 23 411.1 0,5 HP(SN:07VD7152) XA Produced Water Vaults 45 141 - 0.1 XA Healed Separators 1 24 0.0 XA Pneumatic Devices 17 13 1 3 84 0.1 XA Compressor Blovalown 1 1 4 0.0 XA ,Fugitive Equipment Leaks 2 0.0 TOTAL(tpyl 0.5 0.D 0.0 0.2 0.1 0.0 D.0 1.0 0.0 0.0 D.0 0.0 1.9 , 13 13WE1101.CP5 4/8/2020 Received 4/7/2020 Colorado Department of Public Health and Environment Form APCD-102 Air Pollution Control Division 's v. kl" • Facility Wide Emissions Inventory Form Ver.April,2015 Company Name:Bonanza Creek Energy Operating Company.LW Source Name:Latham 14-12 Production Facility(COGCC 4429825) • 9cr Source AIRS ID:123-9AC2 Uncontrolled Potential to Emit(PTE) Controlled Potential to Emit(PTE) Criteria(IPV) HAP:0bs/yr) Criteria(TP1) HAP:9bs/yr) AIRS 110 Equipment Description TSP PMII PAD.5 002 NO: VOC CO HCHO Acetyl Acro BZ Tol. EH Xyl n-Hex Meth 224-TMB' TSP PMIO PM2.5 502 NOz VOC CO HCHO Metal Acro BZ Tol El X31 n-Hex Meth 224-TMI' 123/9AC2/003 Condensate Tank Battery t - - - - 669.9 - - - - 5,152 3,888 488 815 32,128 - 145 0.2 0.2 0.0 1.1 33.5 5.2 - - - 258 194 24 41 1,606 - 7 123/9AC2/004 Produced Water Tank - - - - 10.3 - - - - 550 0 0 D 1,728 - 0 - - - 0.1 0.5 0.7 - - - 28 0 0 0 88 - 0 123/9AC2/006 Trod:Loadine - - - - 9.3 - - - - 32 0 0 0 283 - 0 0.0 0.0 0.0 0.0 0.5 0.0 - - - 2 0 0 0 14 - 0 I23/9AC2/005 Arrow A62 0.1 0.l 0.0 11.4 0.3 4.5 139 16 15 9 3 0 I - I0 - 0.1 0.1 0.0 1.9 0.3 3.7 33 16 15 9 3 0 1 - 18 - 123/9AC2/015 CaterpillmO3306TA 0.1 0.1 0.0 32.5 2.0 323 980 40 38 23 B 0 3 - 44 - 0.1 0.1 0.0 3.9 2.0 7.9 980 40 38 23 8 0 3 - 44 - 1 Permitted Sources Subtotal= 0.0 0.2 0.2 0.0 43.9 691.2 37.0 11,119 56 03 5,766 3,899 488 819 34,138 62 145 0.0 0.4 0.4 0.0 7.1 36.7 17.5 1,013 56 53 319 206 25 45 1,709 62 7 APES Exempt/Insignificant sources Produced Water Vaults Heated Separators 0.1 0.1 00 1.0 0.1 0.8 2 - - 0 0 - 36 - - 0.0 0.1 0.0 1,0 0.1 0,8 1,5 - - DA 0.1 36.4 .. - Pncumatic Devices 1 Fugitive Equipment Leaks Compressor Blowdorm - 0.2 - - - - - 0 0 0 0 2 - 0 - - 0.2 - - - - 0 0 0 0 2 - 0 Insignificant Subtotal= 11.0 11.1 0.1 0.0 1.0 4.5 11.8 2 0 0 59 20 2 11 246 0 3 0.0 0,0 0.1 0.0 1.0 4.5 0,8 I 2 0 0 59 20 2 11 246 0 3 Total,All Sources=II 0.0 I 0.3 1 0.3 I 0.0 I 44.0 I 695.7 1 37.8 1,121 I 56 I 93 I 5,825 1 3,919 I 490 I 830 I 34,384 I 62 1 148 1 0.0 I 0.4 I 0.4 I 0.0 I e.1 I 413 1 18.3 1 1,010 1 96 I 53 1 378 I 225 I 27 I 56 I 1,955 1 62 1 ID Uncontrolled)IAPs Summitry(1P1)=I 0.6 I 0.0 I 0.0 I 2.9 I 2.0 H2 1 0.4 I 17.2 I CO I 0.1 1 Controlled HAPsSummary(TPY)=I 0.5 1 0.0 I 0.0 I 0.2 i 0.1 i 0.0 1'0.0 I 1.0 I 0.0 I 0.0 Uncontrolled Total,All HAPs(TP1)=1 23,4 i Controlled Total,All HAP:(TP1)=I 1.9 I Footnotes: 1.This form should he completed to include both existing sources and all proposed new or modifications to existing emissions sources 2.If the emissions source is new then enter"proposed"under the Permit No.and AIRS ID data columns 3.HAP abbreviations include: BZ=Benzene 224-TMP=2,2,4-Trimethylpentane Tol=Toluene Acetal=Acetaldehyde EB=Ethylbenzene Acro=Acrolein XyI=Xylene n-Hen=n-Hexane HCHO=Formaldehyde Meth=Methanol 4.APEN Exempt/Insignificant Sources should be included when warranted. 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