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Home My WebLink About20151603.tiff A COPHE COLORADO Co .13.- Department of Public _• Health fr Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board RECEIVED 1150O St PO Box 758 MAY 2 9 2015 Greeley, CO 80632 WELD COUNTY May 26, 2015 COMMISSIONERS Dear Sir or Madam: On May 27, 2015, the Air Pollution Control Division will begin a 30-day public notice period for ARB Midstream, LLC - Niobrara Connector. 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 £t Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, /I 7; Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure RUt ) 2015-1603 4300 Cherry Creek Drive S., Denver,CO 80246-1530 P 303-692-2000 www.colorado-govi cdphe I i_4• :! •'! .c�.. ii John W. Hickenlooper. Governor ; Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer i,. ., vl\.s f8f. +... CDPHE Air Pollution Control Division co int v, Notice of a Proposed Project or Activity Warranting Public Comment Website Title: ARB Midstream, LLC - Niobrara Connector - Weld County Notice Period Begins: May 27, 2015 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: ARB Midstream, LLC Facility: Niobrara Connector Crude terminal facility 7300 47th Avenue, Evans, Colorado 80645 Weld County The proposed project or activity is as follows: Crude terminal facility consisting of truck loadouts, condensate tanks, crude oil tanks and associated fugitive emissions. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 15WE0018 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Stephanie Chaousy Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us V rOLOA ADO 1 I Lel b; . f ° STATE OF COLORADO 0t.c0 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT �� AIR POLLUTION CONTROL DIVISION � o TELEPHONE: (303) 692-3150 s/an t CONSTRUCTION PERMIT PERMIT NO: 15WE0018 E001 8 Issuance 1 DATE ISSUED: ISSUED TO: ARB Midstream, LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas facility, known as the Niobrara Connector, located at 7300 4th Avenue, Evans, Colorado 80645, in Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Manifest I Truck loadout of condensate. Emissions from the loadout Crude 001 are controlled by a vapor balance system with a minimum Operation destruction efficiency of 98%. Loading Truck loadout of condensate. Emissions from the loadout Rack Crude 002 are controlled by an enclosed combustor (John Zink, model Operation and SN: TBD). Fugitive Component 003 Fugitive VOC leak emissions Leaks Tank 1 and Two (2) above ground 95,000 bbl atmospheric condensate 2 — 004 storage tanks. The tanks will be external floating roof tanks Condensate with mechanical shoes. The roof will be a self-supported geodesic dome. Two (2) above ground 95,000 bbl atmospheric crude Tank 3 and storage tanks. The tanks will be external floating roof tanks 4- Crude 005 with mechanical shoes. The roof will be a self-supported geodesic dome. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION AIRS ID: 123/9D6E Page 1 of 19 Condensate Loadout TM Version 2012-1 Co do p e o Public Health and Environment Air Pollution Control Division 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days of the latter of commencement of operation or issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at https://www.colorado.ciov/pacific/cdphe/other-air- permitting-notices. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, II I.F.4.) 4. The operator shall retain the permit final authorization letter issued by the Division after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 5. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility Tons per Year Equipment ID AIRS Point Emission Type VOC Manifest Crude 001 8.1 Point Operation Loading Rack 002 66.9 Point Crude Operation Fugitive Component 003 18.6 Fugitive Leaks Tank 1 and 2— 004 1.7 Point Condensate Tank 3 and 4- 005 1.7 Point Crude AIRS ID: 123/9D6E Page 2 of 19 Col- do pa Me o Public Health and Environment ! Air Pollution Control Division i6LEs' , - _ See "Notes to Permit Holder'for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 6. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit (Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Control Device Equipment ID Point Controlled Manifest Crude 001 Vapor balance system VOC and HAPS Operation Loading Rack 002 Enclosed combustor VOC and HAPS Crude Operation Tank 1 and 2— 004 External floating roof VOC and HAPS Condensate Tank 3 and 4- 005 External floating roof VOC and HAPS Crude PROCESS LIMITATIONS AND RECORDS 7. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rate shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits AIRS Process Parameter Annual Limit Point 001 Condensate Loading 2,409,000 BBL 002 Condensate Loading 13,300,000 BBL 004 Condensate Throughput 13,300,000 BBL 005 Crude Throughput AIRS ID: 12319D6E Page 3 of 19 :;' Co do • p e o Public Health and Environment Air Pollution Control Division The owner or operator shall calculate monthly process rates based on the calendar month. Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 8. The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 9. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 10. Points 001 and 002: This source is located in an ozone non-attainment or attainment- maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 11. Points 001 and 002: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations onsite at the time of inspections to monitor compliance with Condition 11 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 12. Points 001 and 002: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 13. Point 003: This source is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. The operator shall comply with all applicable requirements of Section XII. 14. Point 003: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part AIRS ID: 123/9D6E Page 4 of 19 iij, cor do p, e o Public Health and Environment Air Pollution Control Division B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a quarterly basis. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. 15. Points 004 and 005: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 16. Points 004 and 005: The tanks covered under AIRS points 004 and 005 are subject to the New Source Performance Standards requirements of Regulation No. 6, Part A, Subpart Kb, Standards of Performance for Volatile Organic Liquid Storage Vessels (Including Petroleum Liquid Storage Vessels) for which Construction, Reconstruction, or Modification Commenced after July 23, 1984 including, but not limited to, the following: AIRS ID: 123/9D6E Page 5 of 19 Co do op e o Public Health and Environment Air Pollution Control Division • 40 CFR, Part 60, Subpart A General Provisions • §60.112b—Standard for volatile organic compounds (VOC) • §60.112b(a) The owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 containing a VOL that, as stored, has a maximum true vapor pressure equal to or greater than 5.2 kPa but less than 76.6 kPa...shall equip each storage vessel with one of the following: • §60.112b(a)(2) An external floating roof. An external floating roof means a pontoon-type or double-deck type cover that rests on the liquid surface in a vessel with no fixed roof. Each external floating roof must meet the following specifications: • §60.112b(a)(2)(i) Each external floating roof shall be equipped with a closure device between the wall of the storage vessel and the roof edge. The closure device is to consist of two seals, one above the other. The lower seal is referred to as the primary seal, and the upper seal is referred to as the secondary seal. • (A) The primary seal shall be either a mechanical shoe seal or a liquid-mounted seal. Except as provided in §60.113b(b)(4), the seal shall completely cover the annular space between the edge of the floating roof and tank wall. • (B) The secondary seal shall completely cover the annular space between the external floating roof and the wall of the storage vessel in a continuous fashion except as allowed in §60.113b(b)( • §60.112b(a)(2)(ii) Except for automatic bleeder vents and rim space vents, each opening in a noncontact external floating roof shall provide a projection below the liquid surface. Except for automatic bleeder vents, rim space vents, roof drains, and leg sleeves, each opening in the roof is to be equipped with a gasketed cover, seal, or lid that is to be maintained in a closed position at all times (i.e., no visible gap) except when the device is in actual use. Automatic bleeder vents are to be closed at all times when the roof is floating except when the roof is being floated off or is being landed on the roof leg supports. Rim vents are to be set to open when the roof is being floated off the roof legs supports or at the manufacturer's recommended selling. Automatic bleeder vents and rim space vents are to be gasketed. Each emergency roof drain is to be provided with a slotted membrane fabric cover that covers at least 90 percent of the area of the opening. • §60.112b(a)(2)(iii) The roof shall be floating on the liquid at all times (i.e., off the roof leg supports) except during initial fill until the roof is lifted off leg supports and when the tank is completely emptied and subsequently refilled. The process of filling, emptying, or refilling when the roof is resting on the leg supports shall be continuous and shall be accomplished as rapidly as possible. AIRS ID: 123/9D6E Page 6 of 19 Col do ..p rt e o Public Health and Environment th 4 Air Pollution Control Division sad • §60.113b—Testing and procedures • The owner or operator of each storage vessel as specified in §60.112b(a) shall keep records and furnish reports as required by paragraphs (a), (b), or (c) of this section depending upon the control equipment installed to meet the requirements of §60.112b. The owner or operator shall keep copies of all reports and records required by this section, except for the record required by (c)(1), for at least 2 years. The record required by (c)(1) will be kept for the life of the control equipment. • §60.113b(b)After installing the control equipment required to meet §60.112b(a)(2) (external floating roof), the owner or operator shall: • §60.113b(b)(1) Determine the gap areas and maximum gap widths, between the primary seal and the wall of the storage vessel and between the secondary seal and the wall of the storage vessel according to the following frequency. ▪ (i) Measurements of gaps between the tank wall and the primary seal (seal gaps) shall be performed during the hydrostatic testing of the vessel or within 60 days of the initial fill with VOL and at least once every 5 years thereafter. • (ii) Measurements of gaps between the tank wall and the secondary seal shall be performed within 60 days of the initial fill with VOL and at least once per year thereafter. • (iii) If any source ceases to store VOL for a period of 1 year or more, subsequent introduction of VOL into the vessel shall be considered an initial fill for the purposes of paragraphs (b)(1)(i) and (b)(1)(ii) of this section. • §60.113b(b)(2) Determine gap widths and areas in the primary and secondary seals individually by the following procedures: • (i) Measure seal gaps, if any, at one or more floating roof levels when the roof is floating off the roof leg supports. • (ii) Measure seal gaps around the entire circumference of the tank in each place where a 0.32-cm diameter uniform probe passes freely (without forcing or binding against seal) between the seal and the wall of the storage vessel and measure the circumferential distance of each such location. • (iii) The total surface area of each gap described in paragraph (b)(2)(ii) of this section shall be determined by using probes of various widths to measure accurately the actual distance from the tank wall to the seal and multiplying each such width by its respective circumferential distance. • §60.113b(b)(3)Add the gap surface area of each gap location for the primary seal and the secondary seal individually and divide the sum for each seal by the nominal diameter of the tank and compare each ratio to the respective standards in paragraph (b)(4) of this section. AIRS ID: 123/9D6E Page 7 of 19 lip ' Co ak do P p e o Public Health and Environment II Air Pollution Control Division • §60.113b(b)(4) Make necessary repairs or empty the storage vessel within 45 days of identification in any inspection for seals not meeting the requirements listed in (b)(4) (i) and (ii) of this section: • (i) The accumulated area of gaps between the tank wall and the mechanical shoe or liquid-mounted primary seal shall not exceed 212 cm2 per meter of tank diameter, and the width of any portion of any gap shall not exceed 3.81 cm. • (A) One end of the mechanical shoe is to extend into the stored liquid, and the other end is to extend a minimum vertical distance of 61 cm above the stored liquid surface. • (B) There are to be no holes, tears, or other openings in the shoe, seal fabric, or seal envelope. • (H) The secondary seal is to meet the following requirements: • (A) The secondary seal is to be installed above the primary seal so that it completely covers the space between the roof edge and the tank wall except as provided in paragraph (b)(2)(iii) of this section. • (B) The accumulated area of gaps between the tank wall and the secondary seal shall not exceed 21.2 cm2 per meter of tank diameter, and the width of any portion of any gap shall not exceed 1.27 cm. • (C) There are to be no holes, tears, or other openings in the seal or seal fabric. • (iii) If a failure that is detected during inspections required in paragraph (b)(1) of§60.113b(b) cannot be repaired within 45 days and if the vessel cannot be emptied within 45 days, a 30-day extension may be requested from the Administrator in the inspection report required in §60.115b(b)(4). Such extension request must include a demonstration of unavailability of alternate storage capacity and a specification of a schedule that will assure that the control equipment will be repaired or the vessel will be emptied as soon as possible. • §60.113b(b)(5) Notify the Administrator 30 days in advance of any gap measurements required by paragraph (b)(1) of this section to afford the Administrator the opportunity to have an observer present. • §60.113b(b)(6) Visually inspect the external floating roof, the primary seal, secondary seal, and fittings each time the vessel is emptied and degassed. • (i) If the external floating roof has defects, the primary seal has holes, tears, or other openings in the seal or the seal fabric, or the secondary seal has holes, tears, or other openings in the seal or the seal fabric, the owner or operator shall repair the items as necessary so that none AIRS ID: 123/9D6E Page 8 of 19 oM. s m. Co do e o` Public Health and Environment n? 3 Air Pollution Control Division of the conditions specified in this paragraph exist before filling or refilling the storage vessel with VOL. • (ii) For all the inspections required by paragraph (b)(6) of this section, the owner or operator shall notify the Administrator in writing at least 30 days prior to the filling or refilling of each storage vessel to afford the Administrator the opportunity to inspect the storage vessel prior to refilling. If the inspection required by paragraph (b)(6) of this section is not planned and the owner or operator could not have known about the inspection 30 days in advance of refilling the tank, the owner or operator shall notify the Administrator at least 7 days prior to the refilling of the storage vessel. Notification shall be made by telephone immediately followed by written documentation demonstrating why the inspection was unplanned. Alternatively, this notification including the written documentation may be made in writing and sent by express mail so that it is received by the Administrator at least 7 days prior to the refilling. • §60.115b— Reporting and recordkeeping requirements • §60.115b(b) After installing control equipment in accordance with §61.112b(a)(2) (external floating roof), the owner or operator shall meet the following requirements. • §60.115b(b) (1) Furnish the Administrator with a report that describes the control equipment and certifies that the control equipment meets the specifications of§60.112b(a)(2) and §60.113b(b)(2), (b)(3), and (b)(4). This report shall be an attachment to the notification required by §60.7(a)(3). • §60.115b(b) (2) Within 60 days of performing the seal gap measurements required by §60.113b(b)(1), furnish the Administrator with a report that contains: • (i) The date of measurement. • (ii) The raw data obtained in the measurement. • (iii) The calculations described in §60.113b (b)(2) and (b)(3). • §60.115b(b) (3) Keep a record of each gap measurement performed as required by §60.113b(b). Each record shall identify the storage vessel in which the measurement was performed and shall contain: • (i) The date of measurement. • (ii) The raw data obtained in the measurement. • (Hi) The calculations described in §60.113b (b)(2) and (b)(3). • §60.115b(b) (4)After each seal gap measurement that detects gaps exceeding the limitations specified by §60.113b(b)(4), submit a report to the Administrator within 30 days of the inspection. The report will identify the vessel and contain the information specified in paragraph (b)(2) of this AIRS ID: 123/9D6E Page 9 of 19 .:. Co A do DI) e o Public Health and Environment Air Pollution Control Division section and the date the vessel was emptied or the repairs made and date of repair. • §60.116b— Monitoring of operations • §60.116b(a) The owner or operator shall keep copies of all records required by this section, except for the record required by paragraph (b) of this section, for at least 2 years. The record required by paragraph (b) of this section will be kept for the life of the source. • §60.116b(b) The owner or operator of each storage vessel as specified in §60.110b(a) shall keep readily accessible records showing the dimension of the storage vessel and an analysis showing the capacity of the storage vessel. • §60.116b (c) Except as provided in paragraphs (f) and (g) of this section, the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 3.5 kPa or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 15.0 kPa shall maintain a record of the VOL stored, the period of storage, and the maximum true vapor pressure of that VOL during the respective storage period. • §60.116b (d) Except as provided in paragraph (g) of this section, the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 5.2 kPa or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 27.6 kPa shall notify the Administrator within 30 days when the maximum true vapor pressure of the liquid exceeds the respective maximum true vapor vapor pressure values for each volume range. • §60.116b(e) Available data on the storage temperature may be used to determine the maximum true vapor pressure as determined below. • §60.116b(e) (2) For crude oil or refined petroleum products the vapor pressure may be obtained by the following: • §60.116b(e) (2) (i) Available data on the Reid vapor pressure and the maximum expected storage temperature based on the highest expected calendar-month average temperature of the stored product may be used to determine the maximum true vapor pressure from nomographs contained in API Bulletin 2517 (incorporated by reference—see §60.17), unless the Administrator specifically requests that the liquid be sampled, the actual storage temperature determined, and the Reid vapor pressure determined from the sample(s). • §60.116b(e) (2) (ii) The true vapor pressure of each type of crude oil with a Reid vapor pressure less than 13.8 kPa or with physical properties that preclude determination by the recommended method AIRS ID: 123/9D6E Page 10 of 19 Col do p e o Public Health and Environment a Air Pollution Control Division is to be determined from available data and recorded if the estimated maximum true vapor pressure is greater than 3.5 kPa. In addition, the following requirements of Regulation No. 6, Part A, Subpart A, General Provisions, apply. a. At all times, including periods of start-up, shutdown, and malfunction, the facility and control equipment shall, to the extent practicable, be maintained and operated in a manner consistent with good air pollution control practices for minimizing emissions. Determination of whether or not acceptable operating and maintenance procedures are being used will be based on information available to the Division, which may include, but is not limited to, monitoring results, opacity observations, review of operating and maintenance procedures, and inspection of the source. (Reference: Regulation No. 6, Part A. General Provisions from 40 CFR 60.11 b. No article, machine, equipment or process shall be used to conceal an emission which would otherwise constitute a violation of an applicable standard. Such concealment includes, but is not limited to, the use of gaseous diluents to achieve compliance with an opacity standard or with a standard which is based on the concentration of a pollutant in the gases discharged to the atmosphere. (§ 60.12) c. Written notification of construction and initial startup dates shall be submitted to the Division as required under§ 60.7. d. Records of startups, shutdowns, and malfunctions shall be maintained, as required under§ 60.7. e. Written notification of opacity observation or monitor demonstrations shall be submitted to the Division as required under§ 60.7. f. Excess Emission and Monitoring System Performance Reports shall be submitted as required under§ 60.7. g. Performance tests shall be conducted as required under§ 60.8. h. Compliance with opacity standards shall be demonstrated according to § 60.11. OPERATING & MAINTENANCE REQUIREMENTS 17. Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) 18. Points 001 and 002: The owner or operator of a loadout at which vapor balancing is used to control emissions shall: a. Install and operate the vapor collection and return equipment to collect vapors during loading of tank compartments of outbound transport trucks and return these vapors to the stationary source storage tanks. AIRS ID: 123/9D6E Page 11 of 19 Co A do I• p e o Public Health and EnvironmentI III Air Pollution Control Division b. Point 001 only: Include devices to prevent the release of vapor from vapor recovery hoses not in use. c. Install dry-break loading couplings to prevent hydrocarbon liquid loss during uncoupling from vehicles. d. Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. e. Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. f. Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. g. Inspect pressure relief devices (PRD) annually for proper operation and replace as necessary. PRDs shall be set to release at a pressure that will ensure flashing, working and breathing losses are routed to the control device under normal operating conditions. h. Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. 19. Point 002: Flare shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare, or by other convenient means approved by the Division, determine whether the flare is operating properly. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 20. Point 003: Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, the operator shall complete a hard count of -components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. Periodic Testing Requirements 21. Point 003: On an annual basis, the owner or operator shall complete an extended gas analysis and liquids analysis of liquids that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas and liquids analyses shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ADDITIONAL REQUIREMENTS 22. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) AIRS ID: 123/9D6E Page 12 of 19 e;ra h Cola do Lipari e or Public Health and Environment Air Pollution Control Division a. Annually by April 30' whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO,) in ozone nonattainment areas emitting less than 100 tons of VOC or NO. per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 23. Federal regulatory program requirements (i.e. PSD, NANSR) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 24. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 25. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for AIRS ID: 123/9D6E Page 13 of 19 llCo do a p. e o Public Health and Environment a Air Pollution Control Division obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. 26. 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. 27. 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. 28. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 29. 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. 30. 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: Stephanie Chaousy, PE Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to ARB Midstream, LLC. Newly permitted truck loadouts, condensate tanks, crude oil tanks and associated fugitive emissions. Synthetic minor facility. AIRS ID: 123/9D6E Page 14 of 19 Co do Cap rt e of Public Health and Environment Air Pollution Control Division , n a 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 shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1. of the Common Provisions Regulation. See: https://www.colorado.gov/pacific/cdphe/aqcc-reqs 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. Uncontrolled ' Emission Are the Controlled AIRS Rate emissions Emission Point Pollutant CAS# BIN (Ib/yr) reportable? Rate (lb/yr) Benzene 71432 A 3395 Yes 68 Toluene 108883 C 9458 Yes 189 001 Ethylbenzene 100414 C 1374 Yes 28 Xylenes 1130207 C 4526 Yes 91 Benzene 71432 A 11247 Yes 562 Toluene 108883 C 31330 Yes 1567 002 Ethylbenzene 100414 C 4552 I Yes 228 Xylenes 1130207 C 14995 I Yes 750 Benzene 71432 A 157 I No 157 Toluene 108883 C 436 Yes 436 003 Ethylbenzene 100414 C 63 No 63 Xylenes 1130207 C 209 No 209 Benzene 71432 A 14 No 14 Toluene 108883 C 40 No 40 004 Ethylbenzene 100414 C 6 No 6 Xylenes 1130207 C 19 No 19 005 Benzene 71432 A 14 No 14 AIRS ID: 123/9D6E Page 15 of 19 up Co n; do e p e o Public Health and Environment 1 Mk Air Pollution Control Division Toluene 108883 C 40 No 40 Ethylbenzene 100414 C 6 No 6 Xylenes 1130207 C 19 No 19 5) The emission levels contained in this permit are based on the following emission factors: Point 001: Emission Factors - Emission Factors-Controlled Uncontrolled CAS Pollutant lb/1000 gal Source Lb/100 gal Source loaded loaded VOC 7.99 AP-42 0.1598 AP-42 71432 Benzene 0.0336 Mass Balance 0.0007 Mass Balance 108883 Toluene 0.0937 Mass Balance 0.0019 Mass Balance 100414 Ethylbenzene 0.0139 Mass Balance 0.0003 Mass Balance 1130207 Xylenes 0.0447 Mass Balance 0.0009 Mass Balance The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46*S*P*M/T S = 1.0 (Loading: dedicated vapor balance service) P (true vapor pressure) = 6.54 psia M (vapor molecular weight) = 50 lb/lb-mol T(temperature of liquid loaded) = 510 °R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors by the VOC emission factor. Controlled emission factors are based on the vapor balance system efficiency of 98%. Point 002: Emission Factors - Emission Factors—Controlled Uncontrolled CAS Pollutant lb/1000 gal Source Lb/100 gal Source loaded loaded VOC 4.79 AP-42 0.0958 AP-42 71432 Benzene 0.0202 Mass Balance 0.0004 Mass Balance 108883 Toluene 0.0562 Mass Balance 0.0011 Mass Balance 100414 Ethylbenzene 0.0083 Mass Balance 0.0002 Mass Balance 1130207 Xylenes 0.0268 Mass Balance 0.0005 Mass Balance The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L = 12.46*S*P"M/T S = 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) = 6.54 psia M (vapor molecular weight) = 50 Ib/lb-mol AIRS ID: 12319D6E Page 16 of 19 Co • f do rttme' f Public Health and Environment i a w Air Pollution Control Division s' a SS T (temperature of liquid loaded) = 510 °R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors by the VOC emission factor. Controlled emission factors are based on the flare efficiency of 95%. Point 003: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 15 --- 80 --- Flanges 114 --- 1300 --- Open-ended Lines --- --- --- Pump Seals --- --- 7 -- Valves 68 --- 415 --- Other* 20 --- 15 --- VOC Content(wt. 1.0 0 1.0 0 fraction) Benzene Content (wt. 0.0042 0.0042 fraction) Toluene Content(wt. 0.0117 0.0117 fraction) Ethylbenzene (wt. 0.0017 --- 0.0017 --- fraction) Xylenes Content(wt. 0.0056 0.0056 fraction) n-hexane Content(wt. 0 0 fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors(kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R95-017 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas and liquids analyses. Point 004: CAS# Pollutant Emission Factors Source Uncontrolled AIRS ID: 123/9D6E Page 17 of 19 Co do p e o Public Health and Environment Air Pollution Control Division lb/1000 gal Condensate Throughput VOC 0.0123 EPA Tanks 4.0.9d 71432 Benzene 0.000052 EPA Tanks 4.0.9d 108883 Toluene 0.00014 EPA Tanks 4.0.9d 100414 Ethylbenzene 0.000021 EPA Tanks 4.0.9d 1330207 Xylene 0.000069 EPA Tanks 4.0.9d Point 005: Emission Factors CAS# Pollutant Uncontrolled Source lb/1000 gal Crude Throughput VOC 0.0123 EPA Tanks 4.0.9d 71432 Benzene 0.000052 EPA Tanks 4.0.9d 108883 Toluene 0.00014 EPA Tanks 4.0.9d 100414 Ethylbenzene 0.000021 EPA Tanks 4.0.9d 1330207 Xylene 0.000069 EPA Tanks 4.0.9d 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC, toluene, total HAPS NANSR Synthetic Minor Source of: VOC 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY AIRS ID: 123/9D6E Page 18 of 19 . aia CoIr do r p `r e o Public Health and Environment Air Pollution Control Division MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN —Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/9D6E Page 19 of 19 Construction Permit Application Preliminary Analysis Summary Section 1 —Applicant Information Company Name: ARB Midstream, LLC Permit Number: 15WE0018 Source Name: Niobrara Connector Source Location: 7300 47th Ave., Evans, CO 80645, Weld County (non-attainment) Point 001: Condensate truck loadout Point 002: Condensate truck loadout Equipment Description: Point 003: Fugitive emissions Point 004: Condensate storage tanks Point 005: Crude oil tanks AIRS ID: 123-9O6E Review Date: Stephanie Chaousy, PE Review Engineer: Chris Laplante Section 2 —Action Completed X CP1 Modification APEN Required/Permit Exempt Final Approval Transfer of Ownership APEN Exempt/Permit Exempt Section 3 —Applicant Completeness Review Was the correct APEN submitted for this source type? X Yes No Is the APEN signed with an original signature? X Yes No Was the APEN filled out completely? X Yes No Did the applicant submit all required paperwork? X Yes No Did the applicant provide ample information to determine emission rates? X Yes No If you answered "no" to any of the above, when did you mail an See Section 14 Information Request letter to the source? On what date was this application complete? December 4, 2014 Section 4—Source Description AIRS Point Equipment Description Truck loadout of condensate. Emissions from the loadout are controlled by a vapor 001 balance system with a minimum destruction efficiency of 98%. 002 Truck loadout of condensate. Emissions from the loadout are controlled by an enclosed combustor(John Zink, model and SN: TBD). 003 Fugitive VOC leak emissions Two (2) above ground 95,000 bbl atmospheric condensate storage tanks. The tanks will 004 be external floating roof tanks with mechanical shoes. The roof will be a self-supported geodesic dome. Two (2) above ground 95,000 bbl atmospheric crude storage tanks. The tanks will be 005 external floating roof tanks with mechanical shoes. The roof will be a self-supported geodesic dome. Page 1 Is this a portable source? Yes X No Is this location in a non-attainment area for any criteria X Yes No pollutant? If"yes", for what pollutant? PM10 CO X Ozone Is this location in an attainment maintenance area for Yes X No any criteria pollutant? If"yes", for what pollutant? (Note: These pollutants are subject to minor source PM10 CO Ozone RACT per Regulation 3, Part B, Section III.D.2) Is this source located in the 8-hour ozone non- attainment region?(Note: If"yes" the provisions of X Yes No Regulation 7, Sections XII and XVII.C may apply) Points 001 and 002: Is this source located at an oil Yes X No _and gas exploration site? Points 001 and 002: Is this source located at a facility that is considered a major source of hazardous air Yes X No pollutant(HAP) emissions? Points 001 and 002: Will this equipment be operated X Yes No in any NAAQS nonattainment area? Points 001 and 002: Does this source load gasoline Yes X No into transport vehicles? Section 5—Emission Estimate Information AIRS Point Emission Factor Source AP-42: Chapter 5.2, Equation 1 L= 12.46*S*P*MI 001 L = loading losses in lb per 1000 gallons loaded S = Saturation Factor P =true vapor pressure of liquid loaded [psia] M = molecular weight of vapors [lb/lb-mole] T= temperature of bulk liquid loaded [deg. R] AP-42: Chapter 5.2, Equation 1 L = 12.46*S*P*M/T 002 L= loading losses in lb per 1000 gallons loaded S = Saturation Factor P =true vapor pressure of liquid loaded [psia] M = molecular weight of vapors [lb/lb-mole] T= temperature of bulk liquid loaded [deg. R] 003 EPA-453/R-95-017, Table 2-4 004 Source provided site-specific VOC emission factor using EPA Tanks. Mass balance was used to calculate HAP emissions. 005 Source provided site-specific VOC emission factor using EPA Tanks. Mass balance was used to calculate HAP emissions. Did the applicant provide actual process data for the emission inventory? Yes X No Basis for Potential to Emit(PTE) AIRS Point Process Consumption/Throughput/Production 001 2,409,000 BBL per year condensate loaded 002 13,300,000 BBL per year condensate loaded Page 2 Equipment Type Gas Heavy Oil (or Light Oil (or Water/Oil Heavy Liquid) Light Liquid) Connectors 15 --- 80 --- 003 Flanges 114 --- 1300 --- Open-Ended Lines --- --- --- --- Pump Seals --- --- 7 --- Valves 68 --- 415 --- Other 20 --- 15 --- 004 6,650,000 BBL per year condensate 005 6,650,000 BBL per year condensate Basis for Permitted Emissions(Permit Limits) AIRS Point Process Consumption/Throughput/Production 001 2,409,000 BBL per year condensate loaded 002 13,300,000 BBL per year condensate loaded Equipment Type Gas Heavy Oil (or Light Oil (or Water/Oil Heavy Liquid) Light Liquid) Connectors 15 I --- 80 --- 003 Flanges 114 I --- 1300 --- Open-Ended Lines --- --- --- I --- Pump Seals --- --- 7 I --- Valves 68 --- 415 --- Other 20 --- 15 I --- 004 6,650,000 BBL per year condensate 005 6,650,000 BBL per year condensate Does this facility use control devices? X Yes No % Reduction AIRS Point Process Control Device Description Granted 001 01 Vapor balance system 98 002 01 Enclosed combustor 95 004, 005 01 External floating roof Part of equipment Section 6—Emission Summary (tons per year) Point NO, VOC CO Single HAP HAP 001 --- 404.2 --- 4.7 (toluene) 9.4 002 --- 1338.9 --- 15.7 (toluene) 31.2 003 --- 18.6 --- I 0.2 (toluene) 0.4 PTE: I 004 --- 1.7 i 0.02 (toluene) 0.04 005 --- 1.7 --- 0.02 (toluene) 0.04 Total --- 1765.1 --- 20.6 (toluene) 41.1 001 --- 404.2 --- 4.7 (toluene) 9.4 002 ' --- 1338.9 --- 15.7 (toluene) 31.2 Uncontrolled point 003 --- 18.6 --- 0.2 (toluene) 0.4 source emission rate: 004 --- 1.7 --- 0.02 (toluene) 0.04 005 --- 1.7 --- 0.02 (toluene) 0.04 Page 3 001 --- 8.1 --- 0.1 (toluene) 0.2 002 --- 66.9 --- 0.8 (toluene) 1.6 Permitted point source 003 --- 18.6 --- 0.2 (toluene) 0.4 emission rate: 004 --- 1.7 --- 0.02 (toluene) 0.04 005 --- 1.7 --- 0.02 (toluene) 0.04 Total --- 97.0 --- 1.2 (toluene) 2.3 Section 7—Non-Criteria/ Hazardous Air Pollutants Uncontrolled Are the Controlled Emission Pollutant CAS# BIN Emission Rate emissions (lb/yr) reportable? Rate(lb/yr) Point 001 Benzene 71432 A 3395 Yes 68 Toluene 108883 C 9458 Yes 189 Ethylbenzene 100414 C 1374 Yes 28 Xylenes 1130207 C 4526 Yes 91 Point 002 Benzene 71432 A 11247 Yes 562 Toluene 108883 C 31330 Yes 1567 Ethylbenzene 100414 C 4552 Yes 228 Xylenes 1130207 C 14995 Yes 750 Point 003 Benzene 71432 A 157 No 157 Toluene 108883 C 436 Yes 436 Ethylbenzene 100414 C 63 No 63 Xylenes 1130207 C 209 No 209 Points 004 and 005 each Benzene 71432 A 14 No 14 Toluene 108883 C 40 No 40 Ethylbenzene 100414 C 6 No 6 Xylenes 1130207 C 19 No 19 Note: Regulation 3, Part A, Section lI.B.3.b APEN emission reporting requirements for non-criteria air pollutants are based on potential emissions without credit for reductions achieved by control devices used by the operator. Section 8—Testing Requirements Will testing be required to show compliance with any emission rate or regulatory X Yes No standard? If"yes", complete the information listed below AIRS Point Process Pollutant Regulatory Basis Test Method 003 01 VOC, State only Hard component HAPS count Page 4 Section 9—Source Classification Is this a new previously un-permitted source? X Yes No What is this facility classification? True X Synthetic Major Minor Minor Classification relates to what programs? X Title V PSD X NA NSR MACT Is this a modification to an existing permit? Yes X No If"yes"what kind of modification? Minor Synthetic Major Minor Section 10—Public Comment Does this permit require public comment per CAQCC Regulation 3? X Yes No If"yes", for which pollutants?Why? For Reg. 3, Part B, III.C.1.a (emissions increase > 25/50 tpy)? X Yes No For Reg. 3, Part B, III.C.t.c.iii (subject to MACT)? Yes X No For Reg. 3, Part B, III.C.1.d (synthetic minor emission limits)? X Yes No Section 11 —Modeling Is modeling required to demonstrate compliance with National Ambient Yes X No Air Quality Standards(NAAQS)? AIRS Point Section 12— Regulatory Review Regulation 1 - Particulate, Smoke, Carbon Monoxide and Sulfur Dioxide Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of 001-005 the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.1. &4.) Requlation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are 001-005 measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. Page 5 Regulation 3-APENs, Construction Permits. Operating Permits, PSD Criteria Pollutants: For criteria pollutants, Air Pollutant Emission Notices are required for: each individual emission point in a non-attainment area with uncontrolled actual emissions of one ton per year or more of any individual criteria pollutant(pollutants are not summed) for which the area is non-attainment. 001-005 (Applicant is required to file an APEN since emissions exceed 1 ton per year VOC) Part B—Construction Permit Exemptions Applicant is required to obtain a permit since uncontrolled VOC emissions from this facility are greater than the 2.0 TPY threshold(Reg.3, Part B, Section ILD.2.a) Part B, III.D.2- RACT requirements for new or modified minor sources This section of Regulation 3 requires RACT for new or modified minor sources located in nonattainment or attainment/maintenance areas. This source is/is not located in the 8-hour ozone nonattainment area, but not the 1-hour ozone area. 001 The date of interest for determining whether the source is new or modified is therefore November 20, 2007 (the date of the 8-hour ozone NA area designation). Since the tank battery from which loadout is occurring will be in service after the date above, this source is considered "new or modified." Operator is dedicated vapor balance sysetm (1.0 saturation factor), therefore, RACT requirements are satisfied. Part B, III.D.2- RACT requirements for new or modified minor sources This section of Regulation 3 requires RACT for new or modified minor sources located in nonattainment or attainment/maintenance areas. This source is/is not located in the 8-hour ozone nonattainment area, but not the 1-hour ozone area. 002 The date of interest for determining whether the source is new or modified is therefore November 20, 2007 (the date of the 8-hour ozone NA area designation). Since the tank battery from which loadout is occurring will be in service after the date above, this source is considered "new or modified." A vapor combustion unit will also control emissions by a minimum destruction efficiency of 95% Part B, III.D.2- RACT requirements for new or modified minor sources This section of Regulation 3 requires RACT for new or modified minor sources located in nonattainment or attainment/maintenance areas. This source is/is not located in the 8-hour ozone nonattainment area. 003 The date of interest for determining whether the source is new or modified is therefore November 20, 2007 (the date of the 8-hour ozone NA area designation). Since the fugitives will be in service after the date above, this source is considered "new or modified." Operator has agreed on the Division's standard conditions. Regulation 6- New Source Performance Standards 001, 002 No applicable subpart. This facility is not a bulk gasoline terminal. NSPS OOOO: Standards of Performance for Crude Oil and Natural Gas Production, Transmission and Distribution. For fugitive emissions at natural gas processing plants subject to NSPS OOOO. This subpart establishes emission standards and compliance schedules for the control of volatile organic compounds(VOC)and 003 sulfur dioxide (SO2) emissions from affected facilities that commence construction, modification or reconstruction after August 23, 2011. Is this source at a"natural gas processing plant?" No Is this source subject to NSPS OOOO? No WHY? Facility is not defined as a"natural gas processing plant." NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. Is this source greater than 19,800 gallons(471 bbl)? Yes 004, 005 Is this source subject to NSPS Kb?Yes WHY? Tanks are greater than 19,800 gallons and are therefore subject. Tanks will have external floating roofs. NSPS OOOO: Tanks with the potential to emission equal to or greater than 6 TPY. 004, 005 Are uncontrolled VOC emissions greater than 6 TPY? No Source is not subject to NSPS OOOO requirements. Page 6 Regulation 7—Volatile Organic Compounds No sections apply. Per Regulation 7, Section VI.C, a terminal is defined as a petroleum liquid storage and distribution facility that has a daily average throughput of more than 001, 002 76,000 liters of gasoline (20,000 gallons), which is loaded directly into transport vehicles. This facility is neither a terminal, nor a bulk plant per definitions in Reg 7, Section VI.C. Section XII.G: If facility is a natural gas processing plant located in non-attainment 003 area, then subject to Section XII.G. Facility is not a natural gas processing plant, therefore, not subject to this subpart. XII. VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is subject to the emission control requirements for condensate tanks since it is located in a non-attainment area.) 004, 005 XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is not currently subject to this since actual uncontrolled emissions are less than 6 tpy of VOC.) Regulation 8—Hazardous Air Pollutants 001, 002 None MACT HH: If facility is MAJOR source for HAP at a natural gas processing plant ONLY(summation of HAPS of dehydrators and fugitives), then fugitive emissions are subject to MACT HH. 003 Is this facility considered MAJOR for HAPS? No Is this source subject to MACT HH? No WHY?Facility is considered area source for MACT HH. Only TEG dehydrators would be subject to MACT HH at this facility at this time (no dehydrators at this issuance). MACT EEEE: Organic Liquids Distribution 004, 005 This source is not subject to MACT EEEE because it is not located at a major source of HAP. 004, 005 MACT HH This source is not subject to MACT HH because it is not located at a major source of HAP. Section 13—Aerometric Information Retrieval System Coding Information Process/ Emission Process Emission Pollutant/ Fugitive Control Point Process Description throughput Factor CAS# (Y/N) Factor (%) Limit Source 7.99 VOC No AP-42 98 lb/1,000 gal 0.0336 Benzene/ Mass lb/1,000 gal 71432 No Balance 98 Truck Condensate 2,409,000 0.0937 Toluene/ Mass 01 Loadout BBLJyr lb/1,000 gal 108883 N° Balance 98 001 0.0139 Ethylbenzen Mass lb/1,000 gal e/ 100414 No Balance 98 0.0447 Xylenes/ Mass lb/1000 gal 1130207 No Balance 98 SCC 40600142: Crude Oil: Submerged Loading (balanced Service) 4.79 VOC No AP-42 95 lb/1,000 gal 0.0202 Benzene/ Mass lb/1,000 gal 71432 No Balance 95 Truck Condensate 13,300,000 0.0562 Toluene/ Mass 01 Loadout BBL/yr lb/1,000 gal 108883 No Balance 95 002 0.0083 Ethylbenzen Mass lb/1,000 gal e/ 100414 No Balance 95 0.0268 Xylenes/ No Mass 95 lb/1.000 gal 1130207 Balance SCC 40600132: Crude Oil: Submerged Loading (Normal Service) Page EPA-453/R- 01 Fugitive VOC Leak Emissions VOC Yes 95-017, NA 003 Table 2-4 SCC 31000220: All Equip. Leak Fugitives (Valves,flanges, connections, seals, drains) 0.0123 VOC No EPA Tanks NA lb/1000 gal 0.000052 Benzene/ Mass lb/1000 gal 71432 No Balance NA 01 Condensate 6,650,000 0.00014 Toluene/ No Mass NA 004 Storage Tanks BBLJyr lb/1000 gal 108883 Balance 0.000021 Ethylbenzen No Mass NA lb/1000 gal e/ 100414 Balance 0.000069 Xylenes/ Mass lb/1000 gal 1130207 No Balance NA SCC 40400321 —External Floating Roof Tank, Condensate,working+breathing+flashing losses 0.0123 VOC No EPA Tanks NA lb/1000 gal 0.000052 Benzene/ No Mass• NA lb/1000 gal 71432 Balance Crude Oil 6,650,000 0.00014 Toluene/ Mass 01 No Storage Tanks BBLJyr lb/1000 gal 108883 Balance 005 NA 0.000021 Ethylbenzen No Mass NA lb/1000 gal e/ 100414 Balance 0.000069 Xylenes/ Mass lb/1000 gal 1130207 No Balance NA SCC 40400321 —External Floating Roof Tank, Condensate, working+breathing+flashing losses Page 8 Section 14—Miscellaneous Application Notes AIRS Point 001 Truck Condensate Loadout Units Basis S 1.0 Loading: dedicated vapor balance service P 6.54 Psia Estimated M 50 Lb/lb-mole Estimated T 510 Deg R Based on source's knowledge of bulk liquid temperature L 7.99 Lb/10^3 gal This value is used to calculate annual emissions 0.336 Lb/bbl AP-42: Chapter 5.2 Equation 1 L = 12.46*S*P*M/T L= loading losses in lb per 1000 gallons loaded S= Saturation Factor P=true vapor pressure of liquid loaded [psia] M =molecular weight of vapors [lb/lb-mole] T=temperature of bulk liquid loaded [deg. R] L 7.991b/10^3 gal 3.36E-011b/bbl Annual requested Throughput 101,178,000gal/yr Annual requested VOC emissions 808,3171b/yr Uncontrolled 404.2tpy Assuming 98% vapor balance 8.1tpy HAP emissions were calculated using weight% provided by representative E&P sites. The highest HAP content was selected to provide conservative emissions assessment for HAP emission. Operator provided 6 gas analyses all sampled 8/24/2014: Component I Antelope T44- Crow Valley French Lake Hoff 6- Park 0-K- Tsubaki Hills P41-18HC 7-62-22-2H 4-36-36-1H 62-15-1H 4HC (vol%) 8-62-34-4H I (vol%) (vol%) (vol%) (vol%) (vol%) Benzene I 0.38 0.24 0.26 0.26 0.27 0.25 Toluene 11.07 0.63 0.71 0.71 0.86 0.67 Ethylbenzene 0.14 0.10 0.12 0.12 0.16 0.11 Xylenes 0.50 0.34 0.38 0.38 0.52 0.38 n-hexane 10 0 0 0 0 0 Vol%was converted to wt% using this equation: mass percent= (volume%of solute) *(Density of solute(g/mi))/density of solution(g/ml). The density of the solution varied between the different samples. I have listed them in the table below: Component Density Antelope Crow French Hoff 6- Park 0- Tsubaki (g/ml) T44-P41- Valley Lake 4- 62-15- K-4HC Hills 8- 18HC 7-62- 36-36- 1H (wt%) 62-34- (wt%) 22-2H 1H (wt%) 4H (wt%) (wt%) (wtc/0) Density of 0.7976 0.828 0.8358 0.8373 0.8035 0.8463 solution g/ml Benzene 0.8831 0.421 0.256 0.275 0.274 0.297 0.261 Toluene 0.8743 1.173 0.665 0.743 0.741 0.936 0.692 Ethylbenzene 0.8745 0.153 0.106 0.126 0.125 0.174 0.114 Xylenes 0.8640 0.542 0.355 0.393 0.392 0.559 0.388 Component Uncontrolled Operator- Controlled Operator- Emission factor Emission factor emissions Uncontrolled emissions Controlled (lb/bbl) lb/1000 gal (Ib/yr) emissions (Ib/yr) emissions (Ib/yr) (Ib/yr) Benzene 3403 3395 68 68 0.0014 0.0336 Toluene 9483 9458 190 189 0.0039 0.0937 Ethylbenzene 1407 1374 28 28 0.0006 0.0139 Xylenes 4519 4526 90 91 0.0019 0.0447 Page 9 AIRS Point 002 Truck Condensate Loadout Units Basis S 0.6 Submerged loading:dedicated normal service P 6.54 Psia Estimated M 50 Lb/lb-mole Estimated T 510 Deg R Based on source's knowledge of bulk liquid temperature L 4.79 Lb/10^3 gal This value is used to calculate annual emissions 0.201 Lb/bbl AP-42: Chapter 5.2 Equation 1 L= 12.46*S*P*M/T L=loading losses in lb per 1000 gallons loaded S=Saturation Factor P=true vapor pressure of liquid loaded[psia] M =molecular weight of vapors[lb/lb-mole] T=temperature of bulk liquid loaded[deg. R] L 4.791b/10^3 gal 2.01 E-011 b/bbl Annual requested Throughput 558,600,000gal/yr Annual requested VOC emissions 2,677,6131b/yr Uncontrolled 1338.8tpy Assuming 95%combustor 66.9tpy HAP emissions were calculated using weight% provided by representative E&P sites. The highest HAP content was selected to provide conservative emissions assessment for HAP emission. Operator provided 6 gas analyses all sampled 8/24/2014: Component Antelope T44- Crow Valley French Lake Hoff 6- Park O-K- Tsubaki Hills P41-18HC 7-62-22-2H 4-36-36-1H 62-15-1H 4HC (vol%) 8-62-34-4H (vol%) (vol%) (vol%) (vol%) (vol°/0) Benzene 0.38 0.24 0.26 0.26 0.27 0.25 Toluene 1.07 0.63 0.71 0.71 0.86 0.67 Ethylbenzene 0.14 0.10 0.12 0.12 0.16 0.11 Xylenes 0.50 0.34 0.38 0.38 0.52 0.38 n-hexane 0 0 0 0 0 0 Vol%was converted to wt%using this equation: mass percent=(volume%of solute) *(Density of solute(g/ml))/density of solution (g/ml). The density of the solution varied between the different samples. I have listed them in the table below: Component Density Antelope Crow French Hoff 6- Park O- Tsubaki (g/ml) T44-P41- Valley Lake 4- 62-15- K-4HC Hills 8- 18HC 7-62- 36-36- 1H (wt%) 62-34- (wt%) 22-2H 1H (wt%) 4H (wt%) (wt%) (wt%) Density of 0.7976 0.828 0.8358 0.8373 0.8035 0.8463 solution g/ml Benzene 0.8831 0.421 0.256 0.275 0.274 0.297 0.261 Toluene 0.8743 1.173 0.665 0.743 0.741 0.936 0.692 Ethylbenzene 0.8745 0.153 0.106 0.126 0.125 0.174 0.114 Xylenes 0.8640 0.542 0.355 0.393 0.392 0.559 0.388 Component Uncontrolled Operator- Controlled Operator- Emission factor Emission factor emissions Uncontrolled emissions Controlled (lb/bbl) lb/1000 gal (Ib/yr) emissions (Ib/yr) emissions (lb/yr) (Ib/yr) Benzene 11273 11247 564 562 0.0008 0.0202 Toluene 31408 31330 1570 1567 0.0024 0.0562 Ethylbenzene 4659 4552 234 228 0.0004 0.0083 Xylenes 14968 14995 748 750 0.0011 0.0268 Page 10 AIRS Point 003 Fugitive VOC Leak Emissions A permit will be issued because the uncontrolled VOC emissions are greater than 2 TPY(permit threshold). Six extended gas analyses were provided in the application dated 8/24/2014. The highest HAP content was selected to provide conservative emissions assessment for HAP emission. The gas analyses were perfomed less than a year of submittal. An updated extended gas analysis will not be required because an extended gas analysis was performed within a year of this submittal and included with this package. AIRS Point 004 Condensate Storage Tanks A permit will be issued because the source triggered an APEN with uncontrolled VOC emissions 1 TPY (APEN threshold) and the total facility is has uncontrolled VOC emissions greater than 2 TPY (permit threshold). Operator used EPA Tanks to calculate emissions from these tanks (2-95,000 bbl). EPA tanks model was for 1 tank so emissions were multiplied by 2. HAP emissions were calculated using weight% provided by representative E&P sites. The highest HAP content was selected to provide conservative emissions assessment for HAP emission. Operator provided 6 gas analyses all sampled 8/24/2014. These are the same values used for Points 001, 002, 003 and 004. Component Wt% Emissions Emissions Emission Emission factor (TPY) (Ib/yr) factor (lb/bbl) (lb/1000 gal) VOC --- 1.72 3440 0.00052 0.0123 Benzene 0.42 --- 14 0.0000022 0.000052 Toluene 1.17 --- 40 0.0000059 0.00014 Ethylbenzene 0.17 --- 6 0.00000088 0.000021 Xylenes 0.56 --- 19 0.0000029 0.000069 AIRS Point 005 Crude Oil Storage Tanks A permit will be issued because the source triggered an APEN with uncontrolled VOC emissions 1 TPY (APEN threshold) and the total facility is has uncontrolled VOC emissions greater than 2 TPY (permit threshold). Operator used EPA Tanks to calculate emissions from these tanks(2-95,000 bbl). EPA tanks model was for 1 tank so emissions were multiplied by 2. HAP emissions were calculated using weight% provided by representative E&P sites. The highest HAP content was selected to provide conservative emissions assessment for HAP emission. Operator provided 6 gas analyses all sampled 8/24/2014. These are the same values used for Points 001, 002, 003 and 004. Component Wt% Emissions Emissions Emission Emission factor (TPY) (Ib/yr) factor (lb/bbl) (lb/1000 gal) VOC --- 1.72 3440 0.00052 0.0123 Benzene 0.42 --- 14 0.0000022 0.000052 Toluene 1.17 --- 40 0.0000059 0.00014 Ethylbenzene 0.17 --- 6 0.00000088 0.000021 Xylenes 0.56 --- 19 0.0000029 0.000069 Page 11 c9 "4 x `o m .... c o Z o o o o c c E fzs' o °° '^ ° W c c c c Y c' = 0. a - .- C., n L a Y r r x a� E W v[] d M M M V C C Y ll C C O C O L a T 0 Y �,C T a� 0\ N G y _ ❑ 0 ❑ ❑ 0 'j d r a - .� Nr. �c�c �o Q F c ❑ E cA " o a RR'-,4--, d t C F ❑ ❑ ❑ ❑ ❑ r D a > E N r. 0 'n gym-, 8 ..� 0. o d o vNi �°i-Id C .E y^y c > / _ Z �C o"e `7 d —°° m C" F E E Y 2 z z z. z c E 7, 3°°^"° `c Z " J ✓1 a U ereN > yyY 4 O O L u® E. N C y V ° Y y Y s O ❑ CI El E t C U. 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