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Home My WebLink About20163486.tiffCOLORADO Department of Public Health Er Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 11500 St PO Box 758 Greeley, CO 80632 November 3, 2016 Dear Sir or Madam: RECEIVED NOV 072016 WELD COUNTY COMMISSIONERS On November 10, 2016, the Air Pollution Control Division will begin a 30 -day public notice period for Noble Midstream, LLC - Roan Oil Storage Facility. 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: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickenlooper, Governor Rbtic Rtvieu t/tut ( ot(t Larry Wolk, MD, MSPH, Executive Director and Chief Medical Officer cc : pL c tin Mf T P) , H L C P6), Pc,J C £ 12 ( 0-1 / 3 -en/ CAC.) .) It/4S/(Co 2016-3486 Air Pollution Control Division Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Noble Midstream, LLC - Roan Oil Storage Facility - Weld County Notice Period Begins: November 10, 2016 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Noble Midstream, LLC Facility: Roan Oil Storage Facility Oil Storage and Pipeline Injection Facility Section 25, Township 3N, Range 65W Weld County The proposed project or activity is as follows: The operator is requesting permit coverage for three (3) 250,000 barrel internal floating roof tanks, three (3) 100,000 barrel internal floating roof tanks, two (2) 5,000 barrel internal floating roof tanks, fugitives and hydrocarbon loadout at a new synthetic minor facility. 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 15WE1451 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: Harrison Slaughter Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us EKri c om vxm a a a 1 I ': axuA.,n�:ussn.unem: Colorado Air Permitting Project Version No. 1.00 Project Details Review Engineer: Package #: Received Date: Review Start Date: Section 01- Facility Information Harrison Slaughter 340974 11/20/2O15 8/16/2016 *Updated application materials received 08/11/16. Company Name: County AIRS ID: Plant AIRS ID: Facility Name: Physical Address/Location: Type of Facility: What industry segment? Noble Midstream, LLC 123 9E3A Roan Oil Storage Facility Section 25, Township 3N, Range 65W Oil Storage and Pipeline Injection .9,4-& Natural Gas Production & Processing Is this facility located in a NAAQS non -attainment area? Yes If yes, for what pollutant? ❑ Carbon Monoxide (CO) ❑ Particulate Matter (PM) Section 02 - Emissions Units In Permit Application Q Ozone (NOx & VOC) AIRS Point # Emissions Source Type Emissions Control? Permit # Issuance # Self Cert Required? Action Engineering Remarks 001 CondensateStorageTank Yes. 15WE1451 1 Yes Permit:initial' Issuance 002 Fugitive Correisanent Leaks No 15WE1451 1 Yes Permit Initial ..:° Issuance 005 Hydrocarbon Liquid Loading Yes 15WE1451 1 Yes Permit Initial Issuance: 006 Condensate Storage Tank Yes 15WE1451 1 Yes Permit'Initial Issuance .-.:. 007 Condensate Storage Tank es" 15WE1451 1 Yes-' Permit Initial Issuance Section 03 - Description of Project Noble Midstream LLC submitted an application requesting a facility wide permit for a new oil storage and pipeline injection facility located in the ozone non -attainment area. With this application, the operator is requesting permit coverage for three (3) 250,000 bbl internal floating roof tanks, three (3) 100,000 bbl internal floating roof tanks, two (2) 5,000 bbl internal floating roof tanks, fugitives and hydrocarbon loadout. The storage vessels will receive crude oil or condensate via pipeline or from tanker trucks. Crude oil or condensate from the proposed tanks will be transferred off --site via pipeline or through the use of tanker trucks. Emissions from the storage vessels were conservatively estimated assuming a reid vapor pressure of 12. This assumption is intended to provide a conservative estimate that would exceed potential emissions from tanks storing crude oil, condensate or mixed liquid and thus provide operational flexibility if a storage vessels needs to change liquid service. The operator also reported two (2) emergency diesel generator engines. These engines are APEN required because uncontrolled actual NOx emissions are > 1 tpy; however, the engines are categorically permit exempt because they are used for emergency back-up power 250 fir/yea€(Regulation 3 Part B Section l l.D.1.c.(ii). These engines were processed by the XP pilot program and are not included in this preliminary analysis. However, emissions from these sources are accounted for in the facility totals (see history file). Section 04 - Public Comment Requirments Is Public Comment Required? If yes, why?' Section 05 - Ambient Air Impact Analysis Requirements Colorado Air Permitting Project Version No. 1.00 Was a quantitative modeling analysis required?2 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? Io Is this stationary source a synthetic minor? lfes" If yes, explain what programs and which pollutants here: Title V Operating Permits (OP) : VOC, Toluene, Xylenes, n -Hexane, & Total HAPs Non -Attainment New Source Review (NANSR): VOC Is this stationary source a major source? If yes, explain what programs and which pollutants here: Facility is classified as synthetic minor as described above. Condensate Storage Tank(s) Emissions Inventory Section 01- Adminstrative Information Facility AIRs ID: 123',, County Plant Point Section 02- Equipment Description Details Detailed Emissions Unit Three (3).250,000 barrel internal floating roof condensate/crude oil storage vessels Description: Emission Control Device Emissions are controlled using an internal floating'. roof, Description: Requested Overall VOC & HAP Control Efficiency %: " 0 Section 08 - Technical Analysis Notes section for additional information. The internal floating roof is considered an integrated control device. Please see Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Condensate Throughput = Requested Permit Limit Throughput = Potential to Emit (PTE) Condensate Throughput = Secondary Emissions - Combustion Device Heat content of waste gas= Volume of waste gas emitted per BBL of liquids - produced = 164,250,000. Barrels (bbl) per year 164,250,000 Barrels (bbl) per year 164,250,000 Barrels (bbl) per year "This facility does not utilize a combustion device to control emissions. Btu/scf scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = 0 MMBTU per year 0 MMBTU per year Potential to Emit (PTE) heat content of waste gas routed to combustion device = 0 MMBTU per year Section 04- Emissions Factors & Methodologies Will this storage tank emit flash emissions? Standing & Withdrawal Losses Total Number of Vessels Total Emissions: Pollutant VOC Benzene Toluene Ethylbenzeve Xylenes n -Hexane 2,2,4-TMP Weight % 0.0106575: 0.0292065:: 0.0081945 0.033549 0.064731 0-008046 lb/year nggonf Entbslotls:During Normal -Operations EPATanks 4-0.9d emissions report for internal '.f floating roof tank w/ gasogne RVP lbs/year Source 65291.55 AP -42- 695.8446941 Mass Balance, 1906.937655 Mass. Balance'`'. 535.0316065 Mass Balance 2190.466211 Mass Balance 4226.387323 Mass Balance 525.3358113 Mass Balance :ess 02:.Roof Landing Emission Calalations for Internal Floating Roof with Full Liquid Neel - Parameters Value Units Source True Vapor Pressure (P) 5.4851 psia EPA Tanks 4.0.9d - Average Vapor pressure w/ gasoline RVP 12 Average Temperature of vapor and liquid below floating roof (T) -' 509.9 'R ;: EPA Tanks -40.Rd:-Liquid Bulk Temp Ideal Gas Constant ( R') 10.731 - -: (Psete)/(Ib- molR) Ideal Gast.aw Constant Number of days tank stands idle with floating roof landed (na) 1 days Engineer €stimate Stock Vapor Molecular weight, (M„) Ib/Ib-mol ' EPATanks 40,9d, Vappr"molatularwsdghtfor gas RVP 22,"" Saturation Factor (5) _0L6- " -_ \X `AP-42Table 73r17• Value for full liquid'heel Height of vapor space under floating roof (h.,) 4 ft Operator eed value stimat Tank Diameter (D) - 190 ft ''Operator provided value Daily maximum ambient temperature (T„) 52397 „ 'R AP•42Tab le7.1.7-Aitnual'averagevaluefarDenver, co, Daily minimum ambient temperature (T,,,) 49587 'R AP`42-Table 747- Annual average value for Denver, CO Daily Total Insolation Factor (I) ':1568 Btu/ftzyda Y AP�f'2T^able 7.1.7- Annual average value for Denver, CO Tank paint solar absorptance(a) 0.17IISIIIIN. _ _� - AP=42Tab7.1"6-White Pant in good condition Atmospheric pressure (P,) - . 12 " psia Anrbie t re for Denver Co ,,', , q #xessu ... Reid Vapor Pressure -new, Estimate ' .• "'- ' Actual Condensate Throughput While Emissions Controls Operating = 164,250,000 Barrels (bbl) per year 3 of 35 K:\PA\2015\15 W E1451.CP 1.xlsm Condensate Storage Tank(s) Emissions Inventory Volume of Vapor Space (V,) 113411.4948 fe - AP -42 Chapter 7 Equation.1-3 Vented Vapor Saturation Factor (K,) 0.462354795ill AP-42 Chapter -7 Equation 1-20 - - Vapor Pressure Constant B for Crude Oil Stocks (B) 4239.353514 'R AP -42 Figure 7.1-16: Daily Ambient Temperature Range (ATA) 28.1 'R AP -42 Chapter 7 Equation2 ,].-i Daily Vapor Temperature Range (4T„)uation 27.69568 It - - AP -42 Chapter 7 Eq 1•B Vapor Space Expansion Factor pace (Ke) 0.244418674 ��, . AP-42 - See Equation for Kr on page 7.1-89 Event Standing Losses (L.) 822.2542765 lb/roof landing event AP -42 Chapter 7 Equation 2-16 Event Filling Losses (Lri) 4365.637204 lb/roof landing event AP -42 Chapter 7 Equation 2-26 - Total Landing Loss Emissions (41 = In+Lsi) 5187.89148 lb/roof landing event -AP-42 Chapter 7 Equation 2-10 Total Number of Roof Landing events Total Emissions: Pollutant VOC Benzene Toluene Ethylbenzene Xylenes n -Hexane 2,2,4-TMP Weight 6 lbs/year Source 15563.67444 AP -42' 0.0106575 - 165.8698604 Mass Balance 0.0292065 -- 454.5604576 Mass Balance 0.0081445- 127.5365302 Mass Balance -. 0833549 - 522.1457138 Mass Balance 0.064731 1007.45221 Mass Balance 0,008046 125.2253245 Mass Balance Process Olt Internal Floating Roof Emissions During No ns Pollutant PM2.5 Condensate Storage Tanks Uncontrolled E.F. (Ibs/bbl Condensate Throughput) Controlled E.F. (lbs/bbl Condensate Throughput) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) \1.x\1. 11 MMI:MMElx.N.XXXVIOINNWINIMMINI 4.236E-06 � k Uncontrolled E.F. (Ibs/bbl Condensate Throughput) 0.0000 0.0000 0.0000 Emissions Factor Source Citation 0.0000 Process 02) Roof landing Emission Calculations foe Internal Floating Roofwith Full Liquid Heel Pollutant Condensate Storage Tanks Uncontrolled E.F. (lbs/roof landing event) Controlled E.F. (lbs/roof landing event) Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) NV Ilib:111041b t XiNg ®'.,,.,6167,1191,,,,,, MITMECIII6WiellANN.X.1% IIMME'--'-`55L2so' ®'' OO%."%X.%; %XXX% ®' 1XV`.. 43,532, ' P %'% r. ,!e. IIMMITE374;049 ®''' \ \ W IIIIIIIIMIT335.81T MMIEEMN 4 7:: 41:742\\\IIIOr.\\\\ 22 Control Device Uncontrolled E.F. (Ibs/bbl Condensate Throughput) 0.0000 0.0000 0.0000 Emissions Factor Source Citation 0.0000 Section 05 - Emissions Inventory Piocetatl32Rlternaf Foitip(jRoo Emfssions OWfkrg NO efadans Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 32.646 32.646 32.646 32.646 32.646 Total lb/year VOC 80855.22 Benzene 861.7146 Toluene 2361.498 Ethylbenz ene 662.5681 Xylenes 2712.612 n -Hexane 5233.84 2,2,4-TMP 650.5611 4 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory CO 0.0 0.0 I 0.0 0.0 I 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 3.5E-01 3.5E-01 3.5E-01 3.5E-01 3.5E-01 9.5E-01 9.5E-01 9.5E-01 9.5E-01 9.5E-01 2.7E-01 2.7E-01 2.7E-01 2.7E-01 2.7E-01 1.1E+00 1.1E+00 1.1E+00 1.1E+00 1.1E+00 2.1E+00 2.1E+00 2.1E+00 2.1E+00 2.1E+00 2.6E-01 2.6E-01 2.6E-01 2.6E-01 2.6E-01 Process 02: Roof Landing Emission Calculations for Internal Floating Roof, with Full Liquid Heel: Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 7.782 7.782 7.782 7.782 7.782 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 8.293E-02 8.293E-02 8.293E-02 8.293E-02 8.293E-02 2.273E-01 2.273E-01 2.273E-01 2.273E-01 2.273E-01 6.377E-02 6.377E-02 6.377E-02 6.377E-02 6.377E-02 2.611E-01 2.611E-01 2.611E-01 2.611E-01 2.611E-01 5.037E-01 5.037E-01 5.037E-01 5.037E-01 5.037E-01 6.261E-02 6.261E-02 6.261E-02 6.261E-02 6.261E-02 Total Emissions from Internal Floating. Roof Tank Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 40.428 40.428 40.428 40.428 40.428 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 4.309E-01 4.309E-01 4.309E-01 4.309E-01 4.309E-01 1.181E+00 1.181E+00 1.181E+00 1.181E+00 1.181E+00 3.313E-01 3.313E-01 3.313E-01 3.313E-01 3.313E-01 1.356E+00 1.356E+00 1.356E+00 1.356E+00 1.356E+00 2.617E+00 2.617E+00 2.617E+00 2.617E+00 2.617E+00 3.253E-01 3.253E-01 3.253E-01 3.253E-01 3.253E-01 Section 06 - Regulatory Summary Analysis Regulation 3, Parts A, B Source requires a permit Regulation 7, Section VI Storage tank is subject to Regulation 7, Section VI Regulation 7, Section XII.C, D, E, F Storage Tank is not subject to Regulation 7, Section XII Regulation 7, Section XII.G, C Storage Tank is not subject to Regulation 7, Section X11.6 Regulation 7, Section XVII.B, C.1, C.3 Storage Tank is not subject to Regulation 7, Section XVII Regulation 7, Section XVII.C.2 Storage Tank is not subject to Regulation 7, Section XVII.C.2 Regulation 6, Part A, NSPS Subpart Kb Storage tank is subject to NSPS Kb, including but not limited to, thi Regulation 6, Part A, NSPS Subpart OOOO Storage Tank is not subject to NSPS OOOO NSPS Subpart OOOOa Storage Tank is not subject to NSPS OOOOa Regulation 8, Part E, MAC Subpart HH Storage Tank is not subject to MACT HH (See regulatory applicability worksheet for detailed analysis) 5 of 35 K:\PA\2015\15W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 07- Initial and Periodic Sampling and Testing Requirements wow Does the company use the state default emissions factors to estimate emissions? If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01 Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use an older site -specific sample. If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. N/A - Operator developed site specific emission factors Does the company request a control device efficiency greater than 95%for a flare or combustion device? `'t h. N/A - A combustion device is not used to control emissions. If yes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 - Technical Analysis Notes 1. This facility does not utilizea combustor to control emissions from the storage vessels,. As such, there are no secondary combustion emissions associated withthis source. 2. According to PS Memo 05-01, custody transfer occurs at the: exploration and production site. Since this facility receives condensate via tanker trucks andpipelines from nearby well production facilities,it would be located at a point after custody transfer. As a result, this facility would not be considered an exploration and -production -site. Duet° this, Regulation 7Section fill and XVII do net apply to this . facility. This result is consistent with the Division's determination for other similar facilities. - - - - ---- 3. To calculate the vapor space volume, the operator used a value of 4' for the height of the vapor space.. In the applicat€on,the operator indicated that the height of the roof when ended would be 3.5' andthey estimated a full liquid leg at 025'. Using this information along w€th equation 1-15 in Chapter 7 of AP -42, the heightof the vapor space wolflike - 0.25' = 3.25'.: Thus, the estimate of 4' leads to a conservative estimate of the volume of the vapor space and thus the resulting emissions. As such, the operator estimate was determined to be acceptable for permitting purposes. - - - 4. Since these storage vessels are subject to Regulation 7 Section VI and NSPS Kb, RACT is satisfied through the requirement to ut€l€ze internal floating roofs. 5. The type and number of fittings used to estimate emissions in the EPA Tanks 4.0.9d simulation were calculated-bythe program. The program estimates the type and number of fittings that is typical for the tank type input by the user. Since this program is based on AP-42,[determined this estimate was reasonable for determining the type and number of fittings associated=withthe tank. 6. The control device for these storage vessels is an internal floating rook The internal floating roof is integrated -,into the designof each storage vessel. Since the internal floating roof is not an add-on control, there is not an accurate means for calculating uncontrolled. emission. For this -reason, only the controlled emissions are considered: in this 7. The weight %values used to determine the. HAP emissions f{amthis source are based on anaverage of five (5) representative stable hydrocarbon liquids analyses. Please see the "Hydrocarbon Composition" tab for calculations conducted to determine the values used in this analysis. 8. Since the operator provided site -specific emissionfactars-based on representative stable hydrocarbon liquid analyses and the storage vessels at this facility containstabiized oil (no flash), I an initial test would not be required for this source. - --- - ------ - 9. The operator was provided with a draft permit to review prior to public comment: The operator reviewed the permit and had the following request "The only comments had was woaldit be possible to list the equipment description for each of the size tankv(250k'bbf, 100K bbl and 5K ball as "up to" those volumes just in case a smaller tank makes it into the final design? This would be consistent withhow some of our CG€ permitnhave beenissued and our engineering team appreciates the design flexibility provided " Based on discussions with supervisors, it was determined this request was reasonable for providing the operator with fleo,btity, if needed, for the final design of this facility Additionally, d was determined a condition would be added to the permit requiring the operator tor°odifythe permit in the event the final storage vessel design deviatedfr,sin the original application that was used in this preliminary analysis a ndthe basis for permitted emissions: The condition: added to the permit is as: follows: "Paints -001, 006 and 007: Within thirty (301 days after commencemetrtof operation of the storage vessels covered by points 002,006 and 007 the owner o ropero₹orshalI submit to the Division a complete APEN and application to modify the permit to reflect the equipment installed under this permit. the owner or operator wit not be required to modify the permit per this condition in the event the owner or operator installs the Mowing equipment as provided in the original application as the basis for permitted emtsslo ns: (1)Po/et001: Three (3) 250,000 barrelinteral floating roof storage vessels CI) Point006:Three (3)100,000barrel interim( floating roof storage vessels RI) Point007:Two(2)5,000bdrrelfntema!floating roof storage vessels," By structurirg the penaitthis way, the operator will still be able to begin construction if a smaller tank than wasor€ginally permitted makes €t into the final design while ensuring the permit is modified appropriately in the event a smaller tank is installed.: The condition also ensures the operator would not be required to modrfythe permit if the final design of the facility matches with the original application. Finally, it should be noted that if smaller tanks are installed, the emissions will likely be lower duet° lower throughput capabilities. The operator was provided with a draft permit containing the updates discussed above. The operator reviewed' the palm and eipressedthat they agreed with the changes. made and that they did -not have any further comments. Section 09 - Inventory SCC Coding and Emissions Factors Uncontrolled Emissions AIRS Point # Process # SCC Code Pollutant Factor Control % Units 001 01/02 PM10 0.000E+00 0 lb/1,000 gallons condensate throughput PM2.5 0.000E+00 0 lb/1,000 gallons condensate throughput NOx 0.000E+00 0 lb/1,000 gallons condensate throughput VOC 1.172E-02 0 lb/1,000 gallons condensate throughput CO 0.000E+00 0 lb/1,000 gallons condensate throughput Benzene 1.249E-04 0 lb/1,000 gallons condensate throughput Toluene 3.423E-04 0 lb/1,000 gallons condensate throughput Ethylbenzene 9.605E-05 0 lb/1,000 gallons condensate throughput Xylene 3.932E-04 0 lb/1,000 gallons condensate throughput n- Hexane 7.587E-04 0 lb/1,000 gallons condensate throughput 224 TMP 9.430E-05 0 lb/1,000 gallons condensate throughput "Note - Emission factors for process 01 and 02 have been combined here solely for inventory purposes. When calculating actual emissions, the operator will calculate emissions for process 01 and 02 independently using separate emission factors as described in the preliminary analysis above. 6 of 35 K:\PA\2015\15WE1451.CP1.xlsm Condensate Tank Regulatory Analysts Worksheet Cebrade Refutation 3 Paw Wand S. ADEN and Permit Rssmirameks ATTAINRI6777 • This W. 4 bntad In the Omni MlNstaMmemt arta. SI. Ws moo doss POs ands GO. OP questions In Ibis section an htW as WA 1. Are wled actual emissiora from any criteria polatane bootindividual spume greater than 2171(Regulation 3, Part A, 2ction 2. Is the construction date (service date). to 12/02002 and not modified after 12131/2a021Ye PS Memo R5-01 Definitions 1.12 emit l0 and m Section z for additional guidance grandfather applicability), rgi 3. Al acuity uncmo-med 2l% emissions greater than 5 TR, Nos greater than 10 TOL or Co emissions greaten than 10 lnq (Regulation 3, Part 9, Section 11.0.3)? "Not enough imormaton 1. Are uncontrolled emissions Iran any mteria pollutants from this individual source greater than 1 TPy (Regulation 3, Pan A, Section 11.0.1.6)? z. is the date (service date) prior to 12/30/2002 and not modified after 12/31/2002)See PS Memo 05-01 Definitions 1.12 and1.12 and Section 2 br additional guidance on grandfather applkabilityl? 3. Are total facility �c trolled VVCemissions from the greater than 2TPy, Nos greater than 5333 or Co emesioa greater than 5TN/ (Regulation 3, Ian 3, section 11.0.21? 'Source squires a permit on?. Senlogy( 1. Does this storage tank s"petroleum nu m, as defined by Regulation] Yctio n 212.28? Dons this storageank meet anvol the eaemptiors list. in Regulation vial? 3. Does the tank have a storage pasty greater than 40,000 gallonsa(952 barrels), 4. Does Pie storage khave a fixed roof? 5. IS the fined roof tank used for Me storage of petroleum liquids which have a true vapor pressure between 0.6S pia and llo psis at 20T (WO), 6. Is de rued roof tank equipped with an internal ',peen, noon St page tank is Soren to Repletion T. Section VI.B.2.6144 Stotage tank Is subject to Regulation 0, Seaton 0.2.1.8./) 5maeetank neugea to Regulation 7, Ymgns21.0.2.6.RPHiip 7. Is the tank equippedn s52hi, AND stores petroleum liquid AND a orated n ozone nonaminnentarea? e. Does the to kmeet any of the exemt pti toof Section VkR22.0001111? 9. Does the tank meet any of the exemption of section vr.aoc 11101121? 10. Does the tank stare petroleumliquds with true vapor pressure (as stored) above 1.3 psis? (storage Tat& is not subad toRegulation],ion vl.n.2t 11. Dces the storage tank have capacity less Mai 00,000 gallons (952 barrels), Dees .e forage tank store aliquids with a we vapor pressure between 1.5 psis and 11.0 psis at 20'C? 13. Is the snng'on k at age fa'N ility tot receives and stores petroleum addressed by Regulation? Sectors VI.G.2 or VI.C.37 rr ubjecttoRegulation 7,3eainnVl.a3 : cub,. to Regulation 7, Seaton VI Colon. Regulation 1 Section XII 1. Is as storage tank l¢ ozone control or ark ozone non -attainment a 6 7.a/ma ncearea Is thp storage .k locat. at an es vial ratio production ration , natu gm ornsor station or nature gas drip station? a is Ns storage b roof �t 'Storage u2je. to Regulatimn75ation Mil Source Requires an APEN. Go to. next question Go to next question Source Requires a permit `wa Go to the next question Go to the rest question Yu.» Sources subjectto Regulation 'Section V.a2.b.; Go to the neat question Sources sup. to Regulator 7 Section v az a Go to the neat question Source ISsuhjen Reguaeon> Restonv 2.a Pk Go to the next qualm sks.'......:.Source s subject to Regulation 2 section v. a2.a.f11l, Goon Pe nen q eon settee MII.G.1- Nr',futon Contra Equipment- Preventionol leakage Hahn AI.U- Emission Requirements Procedures SsslIon - Emission Control Requirements 'r Stab', MILE-Recodkeess. and Repining Colorado n ?. Section MR.G I. 3 as storage Nnk located in the gihr atone contr. area ozone rcnattainmem arta or attainment/maintenance area? 2. Is this processing plant, 3. Does ongege tankexetl'rtaPlaM1ra'egstoring non -stabilized liquids) emissions and have uncontrolled actual emissions greater than or equal to tons per year VOC? 1st', subject to teflon 7, Sectionail.G canon Mat.5..2 • Emission Control Requirerrene Section - nl Requirements for Air Pollution Control Equipment -Retention m Leakage Hahn 11042 -Emission Estimation Procedures CObn. Refutation? Section MV1 a a a ion/sror facility? 2. N the conden ate storage .0 located at an oil and gas exploration and production operation, well production adllty2, natural gas compressor station' or natural gas processing plant, thismstorage tank a reed roof storage tank,? 6. Arzu ml5tila greater ton 6 ton per year ROC? semen mete- General Pronsions for Pollution Control Equip settion - Emissnns Control and Monitoring ProWsions Sec.n3- Recondkeepky Rryuirtmma Does %kn only starlit.. Gums? the condensate abj.tk contain Regulation 2, Section nkrll.C.2 Samos M2ll.c.z vntureta. Morltkng for storage ranks fit. wins fir Pollution mntia Equipment land &on& frontons at CRS, Pert 60 Suboan RP, Standards of Penbnnrarw for V,l.91h Osvaldo I...Story, 5toruea Vessels pacify greater Man or equal to 75 cube meters lm'I (-622 3020)? 2. Does the storage vessel meet the bllowing exemption'', 50.2102(2((61? Storage Tank's not subject to Regulation 1, Section 21.3.2.13. Source is not subject to Reg 7, .c VI.0.3. Go to the next question Storage Tank is not subject to Regulation?, Yctim%II Go to the next question Storage ark is not subject to Regulation?, Section Yee Ga. next question Storage rank snot subject to Regulation 2, Section n/II TOW ('Storage Tanks not subject to Reggadon? Melton 2211.132 lies toss........o fosse ass question a. Does Me vessel has a design less than s n equal tol,560.5Oam' 1'10,000 Peg used forpetmleum or condensate stored, processed. a treated pd« to custody transfer' as defined in 60.111br Was rs condensate storage tart constructed, reconstructed, modified (see definitions AO CFR, 60.2) after July 23, 1584, t t. definition of tomge s.see ea as e;d Nosy. defined in 60.1116, Dces Ds one of the following additional exemptions, a. Is the storage pressure vessel es in Pa( -z. psi]and without emissions toatmosphere(E0 Gb(d)(2)1?: design capacity is grter Ilan or equal m151,p'1"IS00RLl and stores akliquid with a maximum true van pressure' less an kPa (4O.11Gb(bll?rn . The design capacity'is greater man a equal . 75 M' 1- 4? Da] but less than 151 m' ("`150 06LI and stores a liquid with amaximum true vapor pressures less than 15.0 kPa1b0.110b(blir [ Storage mnk suhiNct to ASPS Kb, including but not limbed to, Me following provisions Subpart 3, General Provision §6631m- Emission Contra Standards for YOC g60.x13b-Testing and Procedures 460.113b -Reporting and ...seeping Requirements 5601166 - Monitoring of Operations SOCFR, eee60.Subwd OOOO.SI.nd.de of eenformanio for Condo O8 and Wtu.,fadsP,d3ctbn.TteesmWon end OMributbn 1. Was this condensa. storage vesselconstructed, m modified (see definitions 60 CFR,'60.21 after August 23, 2011 and prior d September 2015? 2. ores ms comenate storage vessel meet the definition of 'storage vesreN ,per 60vv? 3. Is this condensate vessel boated at a lasts;.the onshore oil and natural gas production segment, natural gas proces313 segment, natural gas vansmssi0n and smrege segment of Me indusw, a. Are potential v« em;ss;ons nom individual storage vessel greater roan or equal to 6 tons per year? O tithe Gungevesselsubject to and controlled in accordance with requirements fosteragevessels ;n40<FR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HIM [St Subpart/, General womb. per 460.54x5 Table §623335 - Emissions Control Standards for vac §60.5413 -Testing and Procedures 560.535511s)- Noti3cadon, Reporting and Recadkeep;ng 171uamenb 1.60.541.1-1over and Closed Vent System Monitoring Requirements 4603417. Control Devoe 552.70 ire Requirements (Wtpreviously determined ubjed to taus 4000 due to emissions above 6 tons peryear v0em the applicability determination dete, It should remain subject to NSPS 0000 per 60.536s1e32)even po ntial.%emisio. p low 6t p. year] s 00CFR. ea. . Subpart O00Os, St... of eerbmtee. for C.M 411 and 3.tu.l Gas fealties., whirl Construction, ModMutbn, or Reconstruction Commenced Alter September L 2015 condensatee vessel constructed, reconstructed,modified n ied(see definitions 40 CFR, 60.21 after September0R, 2115? Do. 4. Dovessel meet the definition of "storage vessel"s per 60.5430a? 3. Is Mscondensate facility 'inthe crude oil and natural gas production segment, nawral gas processing segment or natural gas transmission and Goagesrymmtof,..dustry? a. VOC ' from the stooge vessel greater 5. the storage vessel subKmMcontrolled f to ail in with a ? h.ouirements for n r storage vessels tiCFR Port 60 Subpart Kb er 40CFR Part 63 Subpart HH? [Storage nk sent subject to ASPS oOWa 30CFR. Pert 63. Subpart MAR He. Oil and Gas Production Fealties Is the lank located at a facility that is major for 2. Is the storage a an al and natural gas production facility that meets either of the following criteria: a. A facility that processes, upgrades or stares hydrocarbon liquids[ 163760161(211; OR array thst processes,es or stores naturalnn to the point at which natural gas enters the natural gas transumsron and storage source category o;delisered to a final end uses'(63.?m(a131(7 tank meet n onof 'storage vessel"iDoes Me tank meet the definition of 1stomge %Ansel t potential for flash enksoon"s per 761, 5. Is the tank suniect to control requirements under AO CFR Part 61 Subpart Kb n Subpart OON. Subpar A, General Orons;on per 463166 (al Table 563.766 -Emissions Contra Standards 56.771 -Monitoring 563.776-Racalkeeprg 563,771 -Reporting Rea Rev. Rea review Is required R Reauetbn 7does not ...WO 77107.1k is le. nomettabment.m. Helot.. meets bath critarie,then.dew MCI nwlem nts. Declaimer This tamed assists spd bas *Oh determining appnic.1Yilyd 07.3 raglua .533 of the Chen Air Ad, as implementing regulation, and A6 (hairy CARrd Cwsmssun rep2Ytirns. Thin dcu . is not a the c.',dd.. and dm analysis amd.4. myvM apply to a pardon., sada, based upon that i.Nd*I facts end c0cum6farce6. 5364 dammed dsae not Mena orwb.btda for any any., reputation, or any other *gad, banana 1adrar.d amid not Mgelyedacwbb. In the overt dw,y con. be7smt 756 lerguepe this document end...gape df?e clean Air Act, 63 implementing rivaled,*and Air Qualify GNnd Commission rt72216, en Mrypxgadthe statute or r36073274gl tondo! Theusedronmerrlaory language such as'rtcnmrnn1""mey."'shoukl' and tan'is inter... dascdba x707 WerpSMbns and " . Memie.yRemnology sreh as'nu07.,t'.aeren are wended. dve7be cond.. ngdmmeN6 rude ea Mau &Me Cfun Air Act and Air Quaky Gonna' 045,5.3 inn reWla003s, but this dzuref nines not seedfan legally Nixing regdramds in and67153621 33 '. NA . Me next question °to the next queStion °M. next question Storage nk is not subject NSFS OD00- This tank was constructed after the applicability date. Go to the next question Go to the next question Go to the next question Go. the neat question Storage Tank is not subject NSPS oorsoa orage Tools is not subject MAR XX- There are no MACT XXrequirerneno for tanks at area sources Section 01 - Adminstrative Information Facility AIRs ID: 123 1. 9E3A 002 County Plant Point Section 02 - Equipment Description Details Detailed Emissions Unit Description: Emission Control Device Emissions from this source are not controlled. Description: -- - - Requested Overall VOC & HAP Control Efficiency %: Equipment leaks (fugitive VOCs facility. rude oil/condensate storage and transport Section 03 - Processing Rate Information for Emissions Estimates This section Is applicable to fugitives. Section 04 - Emissions Factors & Methodologies Regulation 7 Information Operating Hours: 8760 hours/year Emission Factor Source SrreeningEFS EPA -45118-95.017 Table 2-8 Control Efficiency Source: Calculations None Service Component Type Count Emission Factor (kg/hr- source) Table 2-4 Table 2-8 Control (%) Pollutant Mass Fraction Emissions (tpy) Reg. 3 Connectors 988 2.00E-04 1.00E-05 0.0% VOC 1 '.' 0.6211955 Flanges 188 3.90E-04 5.70E-06 0 0% Benzene 0.0106575 '.'. 0.0066204 Open -Ended Lines 0 2.00E-03 1.50E-05 0.0% Toluene 0.0292 '.'. 0.0181389 Gas Pump Seals 0 2.40E-03 3.50E-04 0.0 % Ethylbenzene 0.0081945 0.0050904 Valves 532 4.50E-03 2.50E-05 0.0% Xylenes 0.033549 0.0208405 Other 334 '. 8.80E -O3 1.20E-04 0.0% n -Hexane 0.064731 0.0402106 --- --- -- --- --- 2,2,4-TMP 0.008046 0.0049981 Connectors -0 7.50E-06 7.50E-06 0.0% VOC 0'. 0 Flanges I0 3.90E-07 3.90E-07 0 0% Benzene 0 0 Open -Ended Lines '.0 1.40E-04 7.20E-06 0.0% Toluene 0 0 Heavy Oil Pump Seals 0 0.00E+00 0.00E+00 0.0% Ethylbenzene 0'. 0 Valves ;.0 8.40E-06 8.40E-06 0.0% Xylenes 0 0 Other '_0 3.20E-05 3.20E-05 0.0% n -Hexane 0 0 -- -- -- -- --- 2,2,4-TMP 0'. 0 Connectors 872 2.10E-04 9.70E-06 0.0% VOC 1i '. 0.7834883 Flanges 146 1.10E-04 2.40E-06 0.0% Benzene 0.0106575 0.00835 Open -Ended Lines ':0 1.40E-03 1.40E-05 0.0% Toluene 0.0292 0.0228779 Light Oil Pump Seals 18 1.30E-02 5.10E-04 0.0% Ethylbenzene 0.0081945 0.0064203 Valves 950 2.50E-03 1.90E-05 0.0% Xylenes 0.033549 0.0262852 Other 410 7.50E-03 1.10E-04 0.0% n -Hexane 0.064731 0.050716 -- -- -- -- --- 2,2,4-TMP 0.008046 0.0063039 Connectors 88 1.10E-04 1.00E-05 0.0% VOC 1 0.0568284 Flanges 18 2.90E-06 2.90E-06 0.0% Benzene 0.0106575 0.0006056 Open -Ended Lines 0 2.50E-04 3.50E-06 0.0% Toluene 0.0292 0.0016594 Water/Oil Pump Seals '.0 2.40E-05 2.40E-05 0.0% Ethylbenzene 0.0081945 0.0004657 Valves 170 9.80E-05 9.70E-06 0.0% Xylenes 0.033549 0.0019065 Other 56 1.40E-02 5.90E-05 0.0% n -Hexane 0.064731 0.0036786 -- --- -- -- --- 2,2,4-TMP 0.008046 0.0004572 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source VOC 1.46 tpy 1.46 tpy Screening El Benzene 31.15 lb/yr 31.15 lb/yr Screening El Toluene 86.35 lb/yr 85.35 lb/yr Screening El Ethylbenzene 23.95 lb/yr 23.95 lb/yr Screening Ef Xylenes 98.06 lb/yr 98.06 lb/yr Screening Ef n -Hexane 189.21 lb/yr 189.21 lb/yr Screening El 2,2,4-TMP 23.52 lb/yr 23.52 lb/yr Screening El Regulatory Applicability Reg. 3 Reg. 6 Reg. 7 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 s - EPA -453/R-95-017 Table 2-8 Review Regulation 3, Part B, Section 111.0.2 to determine is RACT is required? Review 40 CFR, Part 60, Subpart KKK to determine if applicable to this source? Review 40 CFR, Part 60, Subpart 0000 to determine if 60.5380 and/or 60.5385 is applicable? Review Section XVII.F to determine is LDAR is applicable? Additional Regulatory Considerations Regulation 1 Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15 -second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, AppendixA (July, 1992)) in all subsections of Section II. A and B of this regulation. Regulation 2 Section I.A - No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. Reg. 3 Part A-APEN Requirements 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. 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 II.D.2.a) Is this source located in an ozone non -attainment area or attainment maintenance area? Yes If yes, is this source subject to leak detection and repair (LDAR) requirements per Regulation 7, Section XVII.F or XII.G or 40 CFR, Part 60, Subparts KKK or OOOO? No Part B, 111.O.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 attainmentlmaintenance areas. This source is located in the 8 -hour ozone nonattainment area. 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." Although operator is not subject to LDAR requirements per Regulation 7, Section XVII.F, the operator intends to voluntarily follow the WAR requirements per Regulation 7 Section XVII.F. As such, it was determined the use of the Screening EF from table 2-8 of EPA -4531R-95-07 was appropriate for this source. Following the LDAR requirements per Regulation 7, Section XVII.F also Regulation 6 Is this source at an onshore "natural gas processing plant as defined in 40 CFR, Part 60.631? No _ Did this source commences construction, reconstruction, or modification after January 20, 1984, and on or before August 23, 2011? No -: This source is not subject to NSPS KKK because it is not located at a "natural gas processing plant" Additionally, the facility will commence construction after August 23, 2011. Did this source commences construction, reconstruction, or modification after August 23, 2011 and on or before September 18, 2015? Na Source is not subject to NSPS OOOO because this is a new that facility will commence construction after September 18, 2015. Regulation 7 Is this source located in an ozone non -attainment area or attainment maintenance area? _Yes Is this source at an onshore "natural gas processing plant as defined in 40 CFR, Part 60.631? ii:iiiiiiiiNo '.! Facility is not a natural gas processing plant. Therefore, this source is not subject to Regulation 7 Section XII.G. Is the facility classified as a well production facility or natural gas compressor station? Since this facility is not classified as a well production facility or natural gas compressor station, it is not subject to Regulation 7 Section XVII.F. Regulation 8 Is this source at a "natural gas processing plant" as defined in 40 CFR, Part 63.761? No '.. Is this facility considered a "major source" of HAP as specifically defined in 40 CFR, Part 63.761 for sites that are not prodcution field facilities? No If you repond "yes" to both questions above, further review if the provisions of 40 CFR, Part 63.769 "Equipment Leak Standards" apply? Source is not subject to MACT HH because the facility is classified as a true minor source of HAPs. NSPS OOOOa Did this source commence construction, reconstruction, or modification after September 18, 2015? Is this source at a well site, compressor station or onshore "natural gas processing plant as defined in 40 CFR, Part 60.5430a? NO This facility does not meet the definitions of well site, compressor station or onshore "natural gas processing plant" as defined by 40 CFR, Part 60.5430a. Therefore, the fugitive emissions at this facility are not subject to NSPS OOOOa. Additional Notes: 1. Although this facility is not subject to Regulation 7 Section XVII.F (see Regulatory analysis above), the operator has expressed they will voluntarily implement and follow the leak detection and repair program (LDAR) per Regulation 7 Section XVII.F. Due to this the operator used the screening emission factors from Table 2-8 in the EPA -453/R-95-017 document to calculate emissions. Since sources subject to Regulation 7 Section XVII.F may use these emission factors, I determined the operator's voluntary compliance with Regulation 7 Section XVII.F was sufficient to allow the use of these emission factors as well. The permit will contain a condition requiring the operator follow the LDAR program per Regulation 7 Section XVII.F. Following this program also satisfies the RACT requirements for this facility. '.. 2. The operator assumed 100% VOC weight content for the gas, light oil and water/oil streams. This is the most conservative weight % estimate the operator can make when calculating fugitive VOC emissions. Additionally, the HAP concentrations used in this analysis were determined to be conservative estimates. Due to this, I determined it was unnecessary for the source to conduct initial or periodic testing in order to determine VOC and HAP concentrations at this facility. 3. It was determined that this facility is not subject to Regulation 7 Sections XII and XVII. In terms of Section XII, this facility is not classified as a oil and gas exploration and production operation, natural gas compressor station, natural gas drip station, or natural gas processing plant. In terms of Section XVII, the facility is not classified as a well production facility or natural gas compressor station. Due to this, the permit will not contain conditions pertaining to Regulation 7 Secstion XII and XVII. This determination is consistent with the Division's determination for other similar facilities. 4. The operator was provided with a draft permit to review prior to public comment. The operator reviewed the permit and expressed that they did not have any comments regarding this source in the permit. AIRS (County/Plant) 123/9E3A Permit No. 15WE1451 Date 8/16/2016 Point # SCC Pollutant or CAS Uncontrolled Emission Factor Emisison Factor Source Controlled Actual Emissions (tpy)* Controlled Requested Emissions (tpy)` PTE (tpy)* Ctrl. Eff% NCRP = reportable ? 002 31000220 VOC Screening Efs - EPA -435/R-95- 017 Table 2-8 -- 1.5 1.5 0% Yes 002 31000220 Benzene Screening Efs - EPA -435/R-95- 017 Table 2-8 -- 31.2 31.2 0% No 002 31000220 Toluene Screening Efs - EPA -435/R-95- 017 Table 2-8 --- 85.4 85.4 0% No 002 3100022O Ethylbenzene Screening Efs - EPA -435/R-95- 017 Table 2-8 -- 24 24 0% No 002 31000220 Xylenes Screening Efs - EPA -435/R-95- 017 Table 2-8 -- 98.1 98.1 0% No 002 31000220 n -Hexane Screening Efs - EPA -435/R-95- 017 Table 2-8 -- 189.2 189.2 0% No 002 31000220 2,2,4-TMP Screening Efs - EPA -435/R-95- 017 Table 2-8 --- 23.5 23.5 0% No "HAP Emissions have units of lbs/year Section 01- Adminstrative Information Facility AIRs ID: 123 County 9E3A 005 Plant Point Section 02 - Equipment Description Details Detailed Emissions Unit Description: Emission Control Device Description: Condensate [oadout to tank trucks. Emissions from this source are controlled by an ECD. Requested Overall VOC & HAP Control Efficiency 95 Section 03 - Processing Rate Information for Emissions Estimates Actual Throughput = Annual requested Throughput = Section 04 - Emissions Factors & Methodologies Calculations L = 12.46*S*P*M/T (AP -42: Chapter 5.2, Equation 1) L = loading losses in lb per 1000 gallons loaded 4380©00? Barrels (bbl) per year 4380000 Barrels (bbl) per year 183960000 gal/yr Factor Meaning Value Units Source S Saturation Factor 0.6 AP -42 Table 5.2-1: Submerged Loading - dedicated normal service P True Vapor Pressure 5.4851 psia EPA Tanks 4.0.9d - True Vapor pressure for Gasoline RVP 12 M Molecular Weight of Vapors 64 lb/lb-mole EPA Tanks 4.0.9d - Vapor molecular weight for Gasoline RVP 12 T Liquid Temperature 510.23 deg. R EPA Tanks 4.0.9d - Liquid Bulk Temperature (Location: Denver, CO) L NCRPs Component 5.144 lb/10^3 gal 2.16E-01 lb/bbl Mass Fraction Benzene 0.0115 Toluene 0.0301 0.0085 0.0346 .. Ethylbenzene Xylenes n -Hexane 0.0732 0.1 2,2,4-TMP 97 Source: b 0 Analysis - See additional notes section for more Sta le information. Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2160 lb/bbl 473.11 tpy 23.66 tpy AP -42 Benzene 2.482E-03 lb/bbl 10869.20 lb/yr 543.46 lb/yr Mass Balance Toluene 6.511E-03 lb/bbl 28516.21 lb/yr 1425.81 lb/yr Mass Balance Ethylbenzene 1.838E-03 lb/bbl 8050.04 lb/yr 402.50 lb/yr Mass Balance Xylenes 7.478E-03 lb/bbl 32751.97 lb/yr 1637.60 lb/yr Mass Balance n -Hexane 1.581E-02 lb/bbl 69245.26 lb/yr 3462.26 lb/yr Mass Balance 2,2,4-TMP 2.086E-03 lb/bbl 9138.46 lb/yr 456.92 lb/yr Mass Balance NOx 7.993E-04 lb/bbl 1.75 tpy 1.75 tpy CDPHE Memo 2005-03- 22 CO 2.031E-03 lb/bbl 4.45 tpy 4.45 tpy CDPHE Memo 2005 -03 - 22 Regulatory Review Regulation 1 - Particulate, Smoke, Carbon Monoxide and Sulfur Dioxide Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15 -second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A (July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5 - Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2 — Odor Section I.A - No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. Regulation 3 - APEN and Permitting Requirements Is this site considered an exploration and production location (e.g. well pad)? If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons (238 BBLs) per day of crude oil on an annual average basis? If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section 11.O.1.1 No Part A-APEN Requirements 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. (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 II.D.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 located in the 8 -hour ozone nonattainment area, but not the 1 -hour ozone area. 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 come into service after the date above, this source is considered "new or modified." Operator is using submerged fill (0.6 saturation factor), therefore, RACT requirements are satisfied. Regulation 6 - New Source Performance Standards No applicable subpart. This facility is not a bulk gasoline terminal. 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 76,000 liters of gasoline (20,000 gallons), which is loaded directly into transport vehicles. A bulk plant is defined as a petroleum liquid storage and distribution facility that has an average daily throughput of 76,000 liters of gasoline (20,000 gallons) or less, which is loaded directly into transport trucks This facility is neither a terminal, nor a bulk plant per definitions in Reg 7, Section VI.C. Regulation 8 — Hazardous Air Pollutants MACT EEEE: Not subject because facility is classified as a synthetic minor source of HAPs Additional Notes: 1. The mass fractions used to calculate HAP emissions associated with the loadout operation are based on a set of five (5) representative stable hydrocarbon liquids analyses. In order to obatin the HAP mass fractions used in this analysis, the following calculations were conducted: (i)The maximum HAP content for each component from each stream was scaled by a factor of 1.5. (ii)The non-VOC content was removed from the analyses. (iii) The VOC components were averaged and and normalized so the composition totaled 100%. (iv) The mole fractions were then converted to a weight fraction using the molecular weight of each component. These steps led to a conservative estimate of emissions and were thus accepted for use in this analysis. The tab labeled "Hydrocarbon Composition" demonstrates these calculations. 2. Periodic testing is not generally required for hydrocarbon loadout. The operator calculated VOC emissions using AP - 42 and HAP emissions using conservative weight % values as discussed above. Since these are standard calculation methods, I determined periodic testing would not be warranted for this source. 3. An initial compliance test (EPA Method 9) was included for this source in order to verify the enclosed combustor is operating in compliance with permit limits (i.e. 30% opacity). The O&M plan addresses ongoing compliance demonstration with regards to the enclosed combustor. 4. The operator was provided with a draft permit to review prior to public comment. The operator reviewed the permit and expressed that they did not have any comments regarding this source in the permit. AIRS (County/Plant) 123/9E3A Permit No. 15WE1451 Date 8/16/2016 Point # SCC Pollutant or CAS Uncontrolled Emission Factor Emisison Factor Source Controlled Actual Emissions (tpy)* Controlled Requested Emissions (tpy)* PTE (tpy)* CSI. Eff% NCRP= reportable ? 005 40600132 VOC 5.144 lb/1000 gallons AP -42 -- 23.7 473.11 95% Yes 005 40600132 NOx 0.01903 lb/1000 gallons CDPHE Memo 2005-03-22 -- 1.8 1.8 0% Yes 005 40600132 CO 0O4835 lb/1000 gallons CDPHE Memo 2005-03-22 -- 4.5 4.5 0% Yes 005 40600132 Benzene 0.05908 lb/1000 gallons Mass Balance -- 544 10870 95% Yes 005 40600132 Toluene 0.15501 lb/1000 gallons Mass Balance -- 1426 28517 95% Yes 005 40600132 Ethylbenzene 0.04376 lb/1000 gallons Mass Balance -- 403 8050 95% Yes 005 40600132 Xylenes 0.17804 lb/1000 gallons Mass Balance -- 1638 32752 95% Yes 005 40600132 n -Hexane 0.37641 lb/1000 gallons Mass Balance -- 3463 69246 95% Yes 005 40600132 22,4-TMP 0.04968 lb/1000 gallons Mass Balance -- 457 9139 95% Yes **HAP Emissions have units of lbs/year. Condensate Storage Tank(s) Emissions Inventory Section 01- Adminstrative Information Facility Al Rs ID: 323 9E3A 006 County Plant Point Section 02 - Equipment Description Details Detailed Emissions Unit Three (3) 300,000 barrel. Internal float Description: condensate/crude oil storagevessel5 Emission Control Device Emissions are controlled using an internal floating roof. Description: Requested Overall VOC & HAP Control - - -The internal floating roof is considered an integrated control device. Please see Efficiency %: 0' - Section 08 -Technical Analysis Notes section for additional information. Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Condensate Throughput= Requested Permit Limit Throughput = Potential to Emit (PTE) Condensate Throughput = Secondary Emissions - Combustion Device Heat content of waste gas = Volume of waste gas emitted per BBL of liquids produced = scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = 109500,000 Barrels (bbl) per year 109,500,000 Barrels (bbl) per year 109,5008000 Barrels (bbl) per year Actual Condensate Throughput While Emissions Controls Operating = 109;500;000; Barrels (bbl) per year "This facility does not utilize a combustion device to control emissions. Btu/scf 0 MMBTU per year 0 MMBTU per year Potential to Emit (PTE) heat content of waste gas routed to combustion device = 0 MMBTU per year Section 04- Emissions Factors & Methodologies Will this storage tank emit flash emissions? Standing & Withdrawal tosses Total Number of Vessels 1261164 - lb/year 5ng Roof Emissions During Normal Operations EPA Tanks 4. 0.9d emissions report for Internal floating roof tank w/ gasoline RVP' 12 Total Emissions: Pollutant Weight % Ibs/year Source VOC -- 37834.92-AP-42 Benzene :0.0106575 403.2256599 _Mass Balance Toluene 0.0292065- 1105.025591 Mass Balance Ethylbenzene 0-0081945 I-. 310.0382519 Mass Balance Xylenes 0.033549 1269.323731 Mass Balance n -Hexane 0.064731 - 2449.092207 Mass Balance 2,2,4-TMP 0.008046 '- 304.4197663 Mass Balance Parameters ess 02:Rooflanding Emission Calculations for Internal Floating Roof wIth Full liquid. Heel. Value 5.4851 Units psia Source True Vapor Pressure (P) Average Temperature of vapor and liquid below floating roof (T) Ideal Gas Constant ('R') 509.9 10.731 'R lii101ta)/(Ib- mol•R) EPA Tanks 4.0-9d - Average Vapor pressure w/ gasoline RVP 12 EPATanks4.0.9d- (Bid Bulk Temp....... Con Number of days tank stands idle with floating roof landed (na) 12a: days A Tanks 4.0.9d- Va Stock Vapor Molecular weight, (M,) Saturation Factor (5) Ib/Ib-mol Height of vapor space under floating roof (h,) ft AP -42 Table 7. 17- Value ;for full Ilquid„iheel Tank Diameter (D) Daily maximum ambient temperature (T„) ft Operator: provided value Daily minimum ambient temperature (T,,,) -42 Table 7.1-7 - Annual average value for Deem Daily Total Insolation Factor (I) Tank paint solar absorptance (a) Atmospheric pressure (P,) 2 Btu/ft4day psia APE42 table 7.1.7-; AP-42Table 7 ure,forOn LCO condition Reid Vapor Pressure 19 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory 1 X 1 \Y .00 ��\'�.1t1►\'\\\\1 IIIIMEMMANNAANNAW NNIANNO :ITEINEEMETIMIBM11,104%.-‘14040 0404000.: \\\1.71.%.1 0.0000 2.780E-06 Process 02: Roof Landing Emission Calculations for Internal Floating Roof with Full Liquid Keel Pollutant Condensate Storage Tanks Uncontrolled E.F. (lbs/roof landing event) Controlled E.F. (lbs/roof landing event) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (lbs/bbl Condensate Throughput) 0.0000 0.0000 0.0600 Emissions Factor Source Citation Volume of Vapor Space (V„) 47529.15526 ft' AP42 Chapter 7 Equation 1-3 Vented Vapor Saturation Factor (K,) 0.462354795lik - AP42 Chapter 7 Equation120: Vapor Pressure Constant B for Crude Oil Stocks (B) 4239.353514 It AP-4214gure7.1-16:--- Daily Ambient Temperature Range (ATO) 28.1 'R AP -42 Chapter 7 Equation 1=12 Daily Vapor Temperature Range (AT„) 27.69568 It AP -42 Chapter 7 £quatlon1�6 Vapor Factor (KOSpace ,ansion 0.244418674 i N AP -42.- See Equation for Kr on page 7.184 Event Standing Losses(Lsi) 344.5951509 lb/roof landing event AP -42 Chapter 7 Equalh..r 2-16 Event Filling Losses (L,) 1829.576877 lb/roof landing event AP -42 Chapter 7 Equation 2-26 Total Landing Loss Emissions (LTC=Lrt+Ls5) 2174.172028 lb/roof landing event AP -42 2 Chapter 7 lorr 2.10 Total Number of Roof Landing events Total Emissions: Pollutant VOC Benzene Toluene Ethylbenzene Xylenes n -Hexane 2,2,4-TMP Weight % 0.0106575 .8,0292065 0.0081945 0.033549 0,064711.': 0.008046.': lbs/year 6522.516083 69.51371516 190.499866 53.44875805 218.8238921 422.2089886 52.48016441 Source AP -42 Mass Balance Mass Balance Masse Balance Mass Balance Mass Balance Mass Balance process 01: Internal Flouting: Roof Emissions Duri onnal Opel VOC Benzene Toluene Ethylbenzene Xylenes n -Hexane 2,2,4-TMP Pollutant PM2.5 Condensate Storage Tanks Uncontrolled E.F. (lbs/bbl Condensate Throughput) Controlled E.F. (lbs/bbl Condensate Throughput) Control Device Uncontrolled E.F. (lbs/MMBtu waste heat combusted) 1009E -45::- 2 447 I N \ NVIAN. 7 ®►\XXl\ANNX% MGMEMX1r`l l'\\l N MEM=ANNAN"i'\' ' ' IMINEEZIMIIIIIIIIMILMAXXXVOL.N.XX 1.009E-05 Uncontrolled E.F. (lbs/bbl Condensate Throughput) 0.0000 0.0000 0.0000 Emissions Factor Source Citation 140.736 0.0000 Section 05- Emissions Inventory P Ocesatii teteKna)FIOatul Roof ER et00$ pltring Fltnir+af 0 Potential to Emit Requested Permit Limits Actual Emissions Criteria Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled (tons/year) (tons/year) (tons/year) (tons/year) (tons/year) PM10 0.0 0.0 0.0 0.0 0.0 PM2.5 0.0 0.0 0.0 * 0.0 0.0 NOt 0.0 0.0 0.0 0.0 0.0 VOC 18.917 18.917 18.917 18.917 18.917 Total (Ib/yr) (lb/bbl) 44357.4361 4.0509E-04 472.739375 4.3173E-06 1295.52546 1.1831E-05 363.48701 3.3195E-06 1488.14762 1.3590E-05 2871.3012 2.6222E-05 356.899931 3.2594E-06 20 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory CO 0.0 0.0 I 0.0 0.0 I 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 2.016E-01 2.016E-01 2.016E-01 2.016E-01 2.016E-01 5.525E-01 5.525E-01 5.525E-01 5.525E-01 5.525E-01 1.550E-01 1.550E-01 1.550E-01 1.550E-01 1.550E-01 6.347E-01 6.347E-01 6.347E-01 6.347E-01 6.347E-01 1.225E+00 1.225E+00 1.225E+00 1.225E+00 1.225E+00 1.522E-01 1.522E-01 1.522E-01 1.522E-01 1.522E-01 Process 02: Roof Landing Emission Calculations for Internal Floater Roof with Pull liquid Heel: Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 3.261 3.261 3.261 3.261 3.261 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 3.476E-02 3.476E-02 3.476E-02 3.476E-02 3.476E-02 9.525E-02 9.525E-02 9.525E-02 9.525E-02 9.525E-02 2.672E-02 2.672E-02 2.672E-02 2.672E-02 2.672E-02 1.094E-01 1.094E-01 1.094E-01 1.094E-01 1.094E-01 2.111E-01 2.111E-01 2.111E-01 2.111E-01 Z.111E-01 2.624E-02 2.624E-02 2.624E-02 2.624E-02 Z.624E-02 Total Emissions from. Internal Floating, Roof Tank Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 22.179 22.179 22.179 22.179 22.179 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 2.364E-01 2.364E-01 2.364E-01 2.364E-01 2.364E-01 6.478E-01 6.478E-01 6.478E-01 6.478E-01 6.478E-01 1.817E-01 1.817E-01 1.817E-01 1.817E-01 1.817E-01 7.441E-01 7.441E-01 7.441E-01 7.441E-01 7.441E-01 1.436E+00 1.436E+00 1.436E+00 1.436E+00 1.436E+00 1.784E-01 1.784E-01 1.784E-01 1.784E-01 1.784E-01 Section 06 - Regulatory Summary Analysis Regulation 3, Parts A, 8 Source requires a permit Regulation 7, Section VI Storage tank is subject to Regulation 7, Section VI Regulation 7, Section XII.C, D, E, F Storage Tank is not subject to Regulation 7, Section XII Regulation 7, Section 0I I.3, C Storage Tank is not subject to Regulation 7, Section XII.6 Regulation 7, Section XVII.B, C.1, C.3 Storage Tank is not subject to Regulation 7, Section XVII Regulation 7, Section XVII.C.2 Storage Tank is not subject to Regulation 7, Section XVII.C.2 Regulation 6, Part A, NSPS Subpart Kb Storage tank is subject to NSPS Kb, including but not limited to, thi Regulation 6, Part A, NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 NSPS Subpart 00OOa Storage Tank is not subject to NSPS OOOOa Regulation 8, Part E, MACT Subpart HH Storage Tank is not subject to MACT HH (See regulatory applicability worksheet for detailed analysis) 21 of 35 K:\PA\2015\15WE1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 07 - Initial and Periodic Sampling and Testing Reouirements Does the company use the state default emissions factors to estimate emissions? If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? is If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in P5 Memo 05-01. Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use an older site -specific sample. If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. N/A - Operator developed site specific emission factors Does the company request a control device efficiency greater than 95%for a flare or combustion device? �, yr#' hu'2 N/A - A combustion device is not used to control emissions. Ifyes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08 - Technical Analysis Notes 1. This facility does not utilize a combustor to control emissions -from the storage vessels. As such, there are no secondary combustion emissions associated'withrhis source.. 2. According toPS Memo 05-01, custody transfer occurs at the exploration and production site. Since this faclity receives condensate via tanker trucks and pipelines from nearby well production facilities, it would be located at a point after custodytransfer. As a result, this facility would not be considered an eoploration and production site. Due to this, Regulation 7 Section XII and XVII do not apply to this facility. This result isconsistent with the Division's determination for other similar facilities- 3.. To calculate the vapor space volume, the operator useda value. of 4' for the height of the vapor space. In the application, t he operator indicated that the height of the roof when landed would be 3.5' _ - and they estimated a full liquid leg at 0.25'. Using this informationalong with equation 1-15 in Chapter 7ofAP-42,:the height of the vapor space would be 3.5' - 0.25' = 3.25'. Thus, the estimate of 4' leads to a conservative estimate of thevolume of the vapor space and thus the resulting emissions. As such,the operator estimate was determined to be acceptable for permitting purposes. ---- 4. Since these storage vessels are subject to Regulation 7 Section Vi and NSPS Kb, RACE is satisfied through the requirement to utilize internal floating zoo 5. The type and number of fittings used to estimate emissions in the. EPA Tanks 4.0-9d simulation were calculated by. the program. The program estimates the type and number of fittings that is typical for the tank type input by the user. Since this program is based on AP -42, d determined this estimate was reasonable for determining thetype and number of fittings associated with the tank. 6. The control device for these storage vessels is an internal floating roof The internal floating roof is integrated into the design of each storage vessel. Since the internal floating roof is not an add-on control, there is not an accurate means for calculating uncontrolled emission. For this reason, only the controlled emissions are considered in this analysis. 7. The weight St values used to determine the HAPemissionsfrom this source are based on an average of five (5) representative stable hydrocarbon liquids analyses. Please see the" Composition" tab for calculationsconducted to determine the values used in this analysis. - -- ---- 8. Since the operator provided site -specific emission factors based on representative stable hydrocarbon liquid analyses and the storage vessels attars facility -contain stab an initial test would not berequired for this source. 9. The operator was provided with a draft permitto review prior to public comment The operator reviewed the permit and had the following request. "The -only comments l -had was wouldit be possible to list the equipment description foreachof the size tanks (250K bbl, 100K bbl and 5Kbblj as "up to" those: volumes, just in c ase_o-smaller tank makes it into the final design? This would be consistent with how some of our CGF permits have been issued and our engineering team appreciates the design flexibility provided.:"'based on discussions with supervisors, it determined this request was reasonable for -. providing the operator with flexibility, if needed, for the final design of this facility. Additionally, it was determined a condition would be added to the permit requiring the operator to modifytise permit in the event the final storage vessel design deviated from the original application that was used in this preliminary analysis a rid the basis for permitted emissions. The -Condition added to the permitis as follows: "Polnts001, 006 and 007,. Within thirty(30)duys after commencementof operation of the storage vessels covered by points 001, 006 and 007 the owner or operator shall submit to the Division a. complete APEN and application tomodify .the permit to reflect the equipment installed under Chit permit The owner or operator will not be required to modify- the permit per this cond/tioain the event the owner or operator installs the following equipment as provided in the original application as the basis for permitted emissio nu: (i) Paint 001: Three(3) 250,000berrel internal floating roof storage vessels (if) PointtO06t Three (3) 100,000 barrel internal floating roof storage vessels. (hi)Point 007: Two (2)5,000 barrelrnteme! floating roof storage vessels. Sy structuring the perm it this: way, the operator will' still be able to beginconstruction :ifa smaller tank: than wasoriginally permitted makes it into the final design white ensuring the permit is modified appropriately in theevent a smaller tank is installed. The condition also ensuresthe operator would not be required tomodify the permit if the -final design of the faolllty matches with the original application. finally, it should be noted that if smaller tanksare installed, the emissions will likely be lower dueta:lower throughput capabilities. The operator was provided'wiith a draft permit containing the -updates :discussed 'above. The operator reviewed the permit and expressed that they agreedwith the changes made and that they did not have any further comments. - - - - ---- --- Section 09 - Inventory 5CC Coding and Emissions Factors AIRS Point 8 Process a SCC Code 006 01/02 • (no flash), I determined: - - Uncontrolled Emissions Pollutant Factor Control % Units PM10 0.000E+00 0 Ib/1,000 gallons condensate throughput PM2.5 0.000E+00 0 Ib/1,000 gallons condensate throughput NOx 0.000E+00 0 lb/1,000 gallons condensate throughput VOC 9.645E-03 0 lb/1,000 gallons condensate throughput CO 0.000E+00 0 lb/1,000 gallons condensate throughput Benzene 1.028E-04 0 lb/1,000 gallons condensate throughput Toluene 2.817E-04 0 lb/1,000 gallons condensate throughput Ethylbenzene 7.904E-05 0 lb/1,000 gallons condensate throughput Xylene 3.236E-04 0 Ib/1,000 gallons condensate throughput n -Hexane 6.243E-04 0 Ib/1,000 gallons condensate throughput 224 TMP 7.760E-05 0 lb/1,000 gallons condensate throughput **Note - Emission factors for process Ol and 02 have been combined here solely for inventory purposes. When calculating actual emissions, the operator will calculate emissions for process 01 and 02 independently using separate emission factors as described in the preliminary analysis above. 22 of 35 - K:\PA\2015\15WE1451-CP1.xlsm Condensate Tank Rapzlatt 2 Malysb McMahan Colorado Mandon 3 Pats Aend B - MEN and Nenmk Requimneata ATTAINMENT- Ms worse h kwmLd In the ozone ne.atalomeat area. Slow Mh source Sonnet Emil CO. all questions In.. section enlisted es N/A 1. Are ortontrolled xtual nor pdwone from this individual source greater than 2TPr (Regulation 3, Part a Section 1.0.1.2)7 on date (service date) prior to 11/30/2)02 and not modified after 12/31/2002 (Ye PS Memo05-01 DefiMbons 1.12 and1.10 and section 2 for additional guidance m grandfather applkabilinl? 3. Me total facility uncontrolled V emissions greater than 5 TPy, NOx greater than 10TPy or Co emissions greater Nan 10 Toy (Re guati6,3, Part P. Section 11.0.3)?information Not NON -ATTAINMENT 1. Are uncontrolled emssions from any criteria pollutant from this indiidual source greater than l TPY (Regulation 3, Pan A section 11.0.1.x1? 2. Is the constructionate (service date) prior to 12/30/2002 and not modified aMr 12/31/2002 (See PS Memo 05-01 monitions 1.12 andl.1e and Section 2 for additional guidance o, grandfather avpliobilln)? 3 Am total facility uncontrolled VOC emissions from Ow greater tfun 2 TPI, MN greaterthan 5TPf or CO emissions greater,Nn5TOY(Regulation 3, Partg,Seotkn 1.0.2)? 'Source requires a permit Coloae n J Seaton V( 1. Dces this storage tank petrokum 1iquk" u defined by Regulation J Section VI.A.2.g? 2. Does this swage tank meet any of the exemption list. in Regulation? Section VI.B.1? 3. Dees the rank have a storage capacity greater than 40,000 gallons (952 barrels)? 4. Does the tank have a fixed roof? 5. Is thefee roof used Mr. storage tar petroleum lquiaa whim lave a true vapor paessure between 0.65 psis and 11.0 nix x 20, ISMFG 6. 1s the !Wed roof tank equipped with an imemal floating roof? Storage tank Is sutler" to Regulation J, 5ettlnn m.e.2.asb Storage tank Is sniped .a.( Storage la. is subject to Rceulation J, 9eaions VI.g.2..0i/772( 7. Is the tank equipped with an external floating roof AND is larger than 952bb AND stores petroleum liquid AND is looted in ozone nonutoinment area, S. Does Me tank meet any of Me ons of Section V.e.2c3)(6(1)? 9. Does the tank meet any of the exemption of Section VI.R.2.10)(R((2)? 10. Does tie ank store petroleum liquds with true vapor pressure lax stored) above 1.3 psis? (Storage Tani( hat subka to Regulation, section *.&2.c 11. Dces the storage tank have capacity less than 40,000 galdns (952 barrels', 12.. Dos a a'quds with a true vapor pressure between l.5 pia and 0 Psi. GIPC? 1 sine �'Stornk at a tan�rconthat receives and stores petroleum addressed by Regulation J Sectons V.C.2 or VI.C.3? a subject to Regulation t. Section)0. I.aB Colorado Regulation J. Season AN 1_ Is this storage tank located 0n ozone control areao one attainment/maintenance area? do al and gas exploration and production oneu nicer natunlagas compressor Potion a natural gas drip station? 3. l,0221100..,07771,322227,4,331729.221' ISharage Tank b not subsecl to Regular. 7. Section MI Section XII.C1 -General Requirement for Air Pollution Control Equipment -Pre.ent,6, of leakage Section 2 -Emission Estimation Prmedunes Section ONO -Emissions Control Requirement Sealbn .E - Monitoring M 33 S lon XII.P - Record PM andPepoeSng Colorado Rendeloe J Section ggi.tg 1 h Ws storage tank !Meted in the 8 -Hr ozone control area or any maneronata0nment area or attirmenl/marderaree area? 2. Is this storage Lank lcuated at natural processing Oyes mane tank erh'bt'Ras, llegsstplant? storing nonstabzed)quad emissions and have urcontroYed actual emissions greater than or equal m 2 toss per year VOC? 'Store, Tank Is not ul*.ct to Regulation 7, Section X11.6 Mellon M.G3 -Emissions Control Ronuirement anon Coned Equipment- Prevention or leakage Latin M.C.2-Emissu ion Estimation Procedures Colorado Mgubtlon J. Section XNI et a ansmissl0Nstaa x101? 2.Is this condensate sin age tank' loated at an oil and ga exploration and production operation , well production lacility', natural gas compressor station' or natural gas processing plant? is this condense. storage lank Med rcof storage tank, 0. Are uncontrolled xtual emissiorts4of Nis store tank equal res ter rMan 6 tons per y VOC. ISto blest eo Reguktlon 7, Secton X*1 SeaWe XWJ-Generat Prdwsiom Ion Air Pollution Control Equips Loon XVn.C.1. Emissions Control and Monitoring ProNsions ae¢3d2.keepine 1 lOoremo G Does Me condensate storage tank...only "stabilized. liquids? n and Pre wTank is. ssissed ba Regulation 7, Section 1VII.7.1 Section XNI.C2-Capture and Mgrvtaing for Storage Tanks fitted wiM Air Pollution Control Equipment MEM. Pert M. Subvert ION Stenden3a of Perform.. for 8,2.13.panic INN. Storage W22Ie 1. Es theiNiv.al image vessel capacity greater dun or equal to 73 cubk meters (m) I-<72 66141? 2 Does Me storage vessel meet Me fo'lowira exemption in 60.1101(deret Scarce Requires an MEN. Go to the neat question Go to next question Source Requires a permit Go to the next question GP m the next question burce is subject to Regulation 7 Section VI.B.2.b.) Go to the next quesdm burce is subject to Regulation J Section 2.; Go to Me next question Source is subject to Regulation J section 01.02.2.31: Soto Me next question Sources subjectto Reguatwn7 Section V1.9.2.a1g0.0 Soto tle next question Storage Tank is not subject to Regulation ), Section V1.R.2c. tourss isna suMsst to Reg 7, .cVI.IS 3. Go to the next question Storage Tank is rot ubect to Regulation 7, Section Xll TER m N e next question ]S Orage Tana c not subject to RegulationJSecdm%II.G Go to next question Storage Tank tai not subject to Regulation J, Section XVII nge Tank is not subject to Regulation 7, Section WILD. Go m the next questlm Go m Me next question a. Dods Oxeyes. ns design capacity less than or equal to 1,589.874 m' 1'10,000 SRO used for petroleum a condensate stoned, processed a treated pna to custody transfer' as defined in 60.111!? W. this man n constructed, reconstructed, a modified (see definitions 40CFR, 5021 after hilt 23, 1984, 4. Does the tank rues definition of "storage vessel"'in 5. Does the storage vessel store a'volatile organic liquid ,MOW' as defined in 60.1116? 6 Does me stooge vessel meet anyone of to allowing additional exemptions: me storage vessel a pressure vessel designed mapemte in excess of 204.9 kna (-29.7 psi, and wittxutemissian ro the atmmPhere (60.1106(d1(211,; or 3 The design pasty is greater than «equal to 151 rut (950 84[1 and stores a liquid vdtn a maximum true noon pressures less Man 15 kpa (60.1100(bllr or c. The design panty is greater than «equal to 7s Mt ("472 BBL] but less Iran 151 m [-ISO enLI and stores a liquid wins a maximum true vapor pressure' less than 15.0 kpa(60.11.Mb11, (Sid ;object ro N5PSRb,maurng hid not limned to, the following pions non Subpart". General 750,4:ons 460.1123 - Emrol Standards for VOC 460.1133 -Testing aProcedures 360.1153 - Reporting and Recankeeping Requirements §60.116b • Monitoring olOpentia's Part 60. Subpart 0000. Sian.. of Perbrmame for crude ON end 'Rotund 6as Production. Trapani -store and Dbtributbn Was this condensate storage vessel constructed, reconstructed, or modified (see definitions 40 CFR, 60.2)after August 23, 2011 and prior to September 18, 2015, 2. Does dys condensate storage vessel meet the definition -storage vessel" per 50.5420P is condensate storage vessel located at a facility in the onshore dl and natural gas production segment, natural gas Processing segmenta?41504ga tmnsnkssion and as... Segment dtla ibustry7 as potential VOC emissionst from the individual o 5. Is the storag'ses and controlled naccordance tall requirements for store a vessels in 40 CFR Fart 605ubpart Kb or 40CFR Part 63 Subpart HH, Go to the next question Go to the next question Go to the next question Source is subject to NSPS Kb Subpart 1, General Provisions per §60.5425 Table §60.538 - Emissions Control Standards for VCC §60.5413 -Testing and Procedures §40.538(g) -notification, 430.541630 - Cover and Closed Vent Srtterr Monitoring Requirements 460.5417. Control Device Monibnng Requirement (Note: Oa storage vessel b enviously determined to !mashie.] to NSPS OOOO duo to massless above 6 tons partner VOC pa tlneaplkebilmr determination date, it should remain subject to N0P50000 per60.536s)aX11 even C pat.05l 000 etrbslom bop ...Pt. Pe 54.4 00 PR, Port 63. Sul art 00004.5ntedards of Parlermance for Crud.OII end Metals, Gas Fealties for *id 04,141«045, ModNkwbn. or 250350 uct544 Commenced Altar 5.445ober L, 2015 I Was this condensatestorage vessel constructed, reconstructed, or modified (see definitions 40 CFR, 60.2) after September 1g, 2015? 2. Does Mis condensate storage vessel meet the an 'storage vessel's per 60.5630'7 3. Is this condensate «and ate acilii tyin thecrude m: and natural accluction segment, gas processing segment natural gas transmission and storage segment of me mdusty, greater than or equal to 6 tons 5. Is the stoagevessel subject to onga tank do to accordance with requirements for store vsse`s inn 40 CFR Part 60 Subpart Kb or 40CFR Part 53 subpart HH, r ;u554 00o0a gMR, Part 63. Subpart MKT HP. Oil and 664 Production Nattier L Is the tank lasted at a facility Mat ismaja f8HAF17 2. Istes e at an oil and natural gas production facility that meet either of to following criteria: a. A ra0lily that processes, upgrades or stores hydrocarbon liquids' (63060411211; OR s. facility tat processes. 4pgra454 or stores natural gas 4n« to the point at which natural gas enters to natural gas transmisson are storage source ategory05 b delivered to a final end user' 163.0Ro(a)(31(, 3. Coes the tanke he definition of 'storage vessel.' in 63.,61, a. Co: the tank meet the definition of "storage vessel with the potential for gash emissions"s per 63.,61? 5. Is the R Part 60. Subpart Kb a Subpart 0000? (Sts Subpart A, General provisions per §61.164 (al Table 2 663.766 - Emissions Control Standards 563.753- Monit0dng §63.7)4. RttOrdkeeping 663.ns Reporting R Review MR reNew tr. requited N Pagination dpar not apply AND if Ms tank is in tM non -attainment area. If tM1. tank masts both criteria, then my. PACT requirements. Disclaimer Dix dxumentessis0 operant with determining epkebintyal cans. rqueemertY of tie Chian Air Act its lmpbnseirg rguYtipv, and Ai Quay CalmlComsinbn regulations. Ms *mime. is note rub or 64110. ion. end. anal,' N contains may notappj ro e pr3uMr sans,m based lions Me inclendust tents and circumstances. Tres document..., not change ormann, . bury law, mgulabm. or any other legallybbd)g requirement end is not legally conformal In Me event deny careen b0Meerj Ce Pmmuege ci Min document and the langu 040,0 Chan Air An„ Ion implementing a9u44o44, and Air amain, Gan. Commission regulations. Me Nnuaces,......a'mPStlal0MlcalVdl TM usedrorvmarkilaY Yrgt Q. 4485 as'mcwnnlerd."'nreY.""staakS art,"uR"Y intendadb desenbeAPCO iMrpmYMYnt end mnernme5 moves. Megnbrysermirabgy such as "we' an:"re mirm'me 000430054154144105 caemeng requirements Undo,. Moms dtfte Clean Ah Act andAir Qusiy Cannot Canons* regulations, 4419,s dxunwg does rot estebish kgalylabdry requirements in elm d itself Vex........_' Storage Tank is not subject NSPS 0000 .TMs (sink was cons4ucted after the applicability MM. Go to the next question Go to the next question Go. the next question Go to me next question Storage Tart is not subject NSPS 0000a R4 J NA......... rage Tanks not subject MAR XX There are no MAR XX requirements fa tanks at area sources Condensate Storage Tank(s) Emissions Inventory Section 01- Adminstrative Information Facility AIRs ID: 123 - - 963A 407 County Plant Point Section 02 - Eauioment Description Details Detailed Emissions Unit Two (2) 5,000 barrel internal floating roof condensate/aude oil storage vessels Description: Emission Control Device Emissions are controlled using an internal floating roof, Description: Requested Overall VOC & HAP Control Efficiency %: - 0 Section 08 - Technical Analysis Notes section for additional information. The internal floating roof is considered an integrated control device. Please see Section 03 - Processing Rate Information for Emissions Estimates Primary Emissions - Storage Tank(s) Actual Condensate Throughput = Requested Permit Limit Throughput = Potential to Emit (PTE) Condensate Throughput = Secondary Emissions - Combustion Device Heat content of waste gas = Volume of waste gas emitted per BBL of liquids produced = scf/bbl Actual heat content of waste gas routed to combustion device = Request heat content of waste gas routed to combustion device = Potential to Emit (PTE) heat content of waste gas routed to combustion device = Section 04- Emissions Factors & Methodologies Will this storage tank emit flash emissions? Standing & Withdrawal Losses Total Number of Vessels 730;000 Barrels (bbl) per year 0,000 Barrels (bbl) per year .,..730,000 Barrels (bbl) per year ••This facility does not utilize a combustion device to control emissions. Btu/scf 0 MMBTU per year 0 MMBTU per year 0 MMBTU per year Process 01: Internal Floating Roof Omiss ons During Normal Operations EPA Tanks 40.9d emissions teat foe internal floating roof tank w/: gasoline RVP .42 lb/year 12 Total Emissions: Pollutant Weight % lbs/year Source VOC - - 6286.84 AP -42. Benzene 0.0106575 - 67.0019973 Mass. Balance Toluene 0.0292065= - 183.6165925 Mass Balance Ethylbenzene - -0.0081945 51-51751038 Mass Balance Xylenes 0.033544 'i 210.9171952 Mass Balance n -Hexane 0.064731 406.95344 Mass Balance 2,2,4-TMP 0.008046:- 50.58391464 Mass Balance Parameters Process 02:Roof landing Emission Calculations for Internal Floating Roof with Full liquid Heel Value 5.4851 Units psia Source True Vapor Pressure (P) Average Temperature of vapor and liquid below floating roof (T) S09.9 EPA Tanks 4.0,9d.- Average Vapor pressure w/ gasoline RVP 12 EPA Tanks 4.0.9d - Liquid Bulk Temp Ideal Gas Constant ('R') 2.751 (Psi'fts)/(Ib• mol'R) Constant Number of days tank stands idle with floating roof landed (na) 523.97 days AT Stock Vapor Molecular weight, (M,) Ib/Ib-mol Saturation Factor (S) Height of vapor space under floating roof (h,) ft AP•42 Tables 7.147 Value for full1kpiid heel Tank Diameter (D) Daily maximum ambient temperature (Ta) ft 2Ta Operator provided.ealue -: Daily minimum ambient temperature (T,,) 495.87 2 Table 7 eel average value. Daily Total Insolation Factor (I) Tank paint solar absorptance (a) Atmospheric pressure (P,) Btu/ftz'day psia 2 Table 7.1-7 - Annual average value for Denver, CO AP-42Table 7.16 .Whi ales in good' condition Reid Vapor Pressure Actual Condensate Throughput While Emissions Controls Operating = _ - "730,000 Barrels (bbl) per year 27 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Volume of Vapor Space (y.) 2827.433388 ft' AP -42 chapter 7 Equation 1.3 Vented Vapor Saturation Factor (K,) 0.462354795 AP -42 Chapter 7 Equation 1-20 Vapor Pressure Constant B for Crude Oil Stocks (B) 4239.353514 'R AP-42Figure 7.1-i6 �. Daily Ambient Temperature Range (AT0) 28.1 'R - AP -42 Chapter 7 Equation 1-12 Daily Vapor Temperature Range (4T,) 27.69568 'R AP -42 Chapter 7 Equation 1-8 Vapor Space Expansion Factor (Kr) 0.244418674 �iz AP -42- See Egoation for Kt on page 7.1.89 Event Standing Losses L l sJ 20.4994141 lb/roof landing event AP-42Cha ptet T Equation 2-16 Event Filling Losses (LO108,8386006 lb/roof landing event AP -42 Cfpptei?Equation 2-26 Total Landing Loss Emissions (Lit = Lrt+Lst) 129.3380147 lb/roof landing event -AP-42 Chapter 7 Equation 2.10 Total Number of Roof Landing events Total Emissions: Pollutant VOC Benzene Toluene Ethylbenzene Xylenes n -Hexane 2,2,4-TMP Weight % lbs/year Source -- 258.6760295 AP -42 0.0106575 2.756839784 Mass 8atance • 0.0292065- 7.555021455 Mass Balance X50081945 - 2.119720724 Mass Balance 0.033549 8.678322113 Mass Balance 0.064731 16.74435806 - Mass Balance 0.008046 2.081307333 Mass Balance Process 02: Internal Floating; Roof Emissions During formal Operatiant Pollutant PM2.5 Condensate Storage Tanks Uncontrolled E.F. (Ibs/bbl Condensate Throughput) Controlled E.F. (Ibs/bbl Condensate Throughput) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (Ibs/bbl Condensate Throughput) 0.0000 0.0000 0.0000 IIIIIIIIMIZIMMIIMISEDEEME31111116XXXXX\\\ MTIEEIMNX7:\.`lam\\\\ Emissions Factor Source Citation 0.0000 Process 02: Roof Landing Emission Calculations for Internal Floating Roof with Full Liquid Heel Pollutant Condensate Storage Tanks Uncontrolled E.F. (Ibs/roof landing event) Controlled E.F. (Ibs/roof landing event) Control Device Uncontrolled E.F. (Ibs/MMBtu waste heat combusted) Uncontrolled E.F. (Ibs/bbl Condensate Throughput) 0.0000 0.0000 0.0000 m an,.- MEM OX\\ OMRTMEIIINIEEEIIIM =NM�\ \N u0E0 INIECEMILXXXXV \W�\\ 0.0000 Emissions Factor Source Citation Section 05 - Emissions Inventory Processaltlnteteat.Ffoating RoofFmrtahf{s Daring Nofmatt7aerdtions' _ - Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC 0.0 0.0 0.0 0.0 0:0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 3.143 3.143 3.143 3.143 3.143 Total (Ib/yr) (lb/bbl) VOC 6545.51603 8.966E-03 Benzene 69.7588371 9.556E-05 Toluene 191.171614 2.619E-04 Ethylbenzene 53.6372311 7.348E-05 Xylenes 219.595517 3.008E-04 n -Hexane 423.697798 5.804E-04 2,2,4-TMP 52.665222 7.214E-05 28 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory CO 0.0 0.0 I 0.0 0.0 I o.o Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled ltons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 3.350E-02 3.350E-02 3.350E-02 3.350E-02 3.350E-02 9.181E-02 9.181E-02 9.181E-02 9.181E-02 9.181E-02 2.576E-02 2.576E-02 2.576E-02 2.576E-02 2.576E-02 1.055E-01 1.055E-01 1.055E-01 1.055E-01 1.055E-01 2.035E-01 2.035E-01 2.035E-01 2.035E-01 2.035E-01 2.529E-02 2.529E-02 2.529E-02 2.529E-02 2.529E-02 Process 02: Roof Landing EmisstonCalculations for Internal Floating Roof with full Liquid Heel: Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.129 0.129 0.129 0.129 0.129 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled. Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 1.378E-03 1.378E-03 1.378E-03 1.378E-03 1.378E-03 3.778E-03 3.778E-03 3.778E-03 3.778E-03 3.778E-03 1.060E-03 1.060E-03 1.060E-03 1.060E-03 1.060E-03 4.339E-03 4.339E-03 4.339E-03 4.339E-03 4.339E-03 8.372E-03 8.372E-03 8.372E-03 8.372E-03 8.372E-03 1.041E-03 1.041E-03 1.041E-03 1.041E-03 1.041E-03 Tt I; Emissions from Internal Floating Roof Tank Criteria Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Umits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) PM10 PM2.5 NOx VOC CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 3.27 3.27 3.27 3.27 3,27 0.0 0.0 0.0 0.0 0.0 Hazardous Air Pollutants Potential to Emit Uncontrolled (tons/year) Requested Permit Limits Uncontrolled Controlled (tons/year) (tons/year) Actual Emissions Uncontrolled Controlled (tons/year) (tons/year) Benzene Toluene Ethylbenzene Xylene n -Hexane 224 TMP 3.488E-02 3.488E-02 3.488E-02 3.488E-02 3.488E-02 9.559E-02 9.559E-02 9.559E-02 9.559E-02 9.559E-02 2.682E-02 2.682E-02 2.682E-02 2.682E-02 2.682E-02 1.098E-01 1.098E-01 1.098E-01 1.098E-01 1.098E-01 2.118E-01 2.118E-01 2.118E-01 2.118E-01 2.118E-01 2.633E-02 2.633E-02 2.633E-02 2.633E-02 2.633E-02 Section 06- Regulatory Summary Analysis Regulation 3, Parts A, 8 Source requires a permit Regulation 7, Section VI Storage tank is subject to Regulation 7, Section VI Regulation 7, Section XII.C, D, E, F Storage Tank is not subject to Regulation 7, Section X11 Regulation 7, Section XII.G, C Storage Tank is not subject to Regulation 7, Section XII.G Regulation 7, Section XVII.B, C.1, C.3 Storage Tank is not subject to Regulation 7, Section XVII Regulation 7, Section XVII.C.2 Storage Tank is not subject to Regulation 7, Section XVII.C.2 Regulation 6, Part A, NSP5 Subpart Kb Storage tank is subject to NSPS Kb, including but not limited to, the Regulation 6, Part A, NSPS Subpart 0000 Storage Tank is not subject to NSPS 0000 NIPS Subpart 0000a Storage Tank is not subject to NIPS 00000 Regulation 8, Part E, MACT Subpart HH Storage Tank is not subject to MACT HH (See regulatory applicability worksheet for detailed analysis) 29 of 35 K:\PA\2015\ 15WE1451.CP1.xlsm Condensate Storage Tank(s) Emissions Inventory Section 07- Initial and Periodic Sampling and Testing Requirements Does the company use the state default emissions factors to estimate emissions? If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to SO tons VOC per year? If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company use a site specific emisions factor to estimate emissions? If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the facility being permitted? This sample should be considered representative which generally means site -specific and collected within one year of the application received date. However, if the facility has not been modified (e.g., no w 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. N/A - Operator developed site specific emission factors Does the company request a control device efficiency greater than 95% for a flare or combustion device? -.,, "" N/A - A combustion device is not used to control emissions. If yes, the permit will contain and intial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling Section 08- Technical Analysis Notes 1.. This facility does not utilize a combustor to control emissions from the storage vessels. As such, there are no secondary combustion emissions associated withthis source, 2- According to PS Memo 05-01, custody transfer occurs at the exploration and production site. Since this facility receives condensate via tanker trucksand pipelinesfrom nearby well production facilities, it would be located ata point after custody transfer. As a result, this facility would not be considered an explorationand production site. Dueto this, Regulation 7 Section Xli and XVII do not apply to this facility. This result inconsistent with the Division's determination for other similar facilities. 3;. To calculate the vapor space volume, the operator used a value of 4' for the height of the vapor space. In the application, the operator indicated that the height of the roof when landed would be 3.5' and they estimated -a: full liquid leg at 0.25'. Using this information along with equation 1.-15 in Chapter 7 of AP -42, the height of the vapor space would be 3.5`-0.25'.= 3.25`.. Thus, the estimate of 4' leads to. a conservative estimate of the volume of the vapor spate and thus the resulting emissions. As such, the operator estimate was determined to be acceptable for permitting purposes. - - 4:. Although these storage vessels are lesstfian 1.0,000 bbls, they do not meetthefollowingexemption in 960.11ob(d)(4): "Vessels with a design capacity lessthan or equal to 1,589.874 m' used for petroleum or condensate stored, processed, or treated prior to custody transfer.".They do not meet this exemption because the vessels =are located at a point after custody transfer. In 660.11113 custody transfer is defined as "the transfer of produced petroleum and/or condensate, after processing and/or treatment in the producing operations,. from storage vesselsor automatic transfer facllitiesto pipelines or any other forms of transportation." Based on the EPA applicability determination index documentcontralff00000g3 "The process and/or treatment could involve several forms such as physical separation (removal of water), chemical treatment, etc`This:interpretation of the ''processing and/or treatment" portion of the custadytranafer definition is echoed in the EPA applicability determination index document control #0200064_ Based an this informatiam, water is typically separated from the crude oil/condensate at the well site through the use of separators. Since thiswould "i.viratitute "processing and/or treatment,"the: storage vessels that receive crude oil/condensate atthiofacifty would be located at ap oint after custody transfer. 5. Since these storage vessels aresobjector Regulation 7 Section VI and. NSPS Kb, RACT is satisfied through the requirement to utilize internal: floating roofs. 6. The type and number of fittings used to estim ate emissions in the EPATanks 4.0.9d simulation were calculated by the program: The program estimates the type and number of fittings that is typical fo the tank type input bythe user. Since this program is based on AP -42-,I determined: this estimate was reasonable for determining the type and number of fittings associated with the tank.,. 7. The control devitefor these storage vessels is an internal floating roof.. The internal floating roof is integrated into the design of each storage vessel. Since the internal floating roof control, there is notan accurate means for -calculating uncontrolled emission. Far this reason, only the controlledemissions are considered in this:enalysts. 8. The weight % values used to determine the HAP emissions from this source are based on an average of five (5) representative stable hydrocarbon liquids analyses PI Composition" tab for calculations conducted todetermine the values used in this analysis: 9. Since the operator provided -site -specific emission factors based on representative stable hydrocarbon liquid analyses and the storage vessel an initial test would not be requiredforthis source. se see the"Hydrocarbon this facility contain stabilized oil {no flash);_ 1 determined 113. The operator was provided with a draft permit 'CO review prior to public comment. The operator reviewed the permit and had the following request: "The only comments I hod was would it be possible to list the equipment description for each of the site tanks (250Kbed, 100K bbl and 5K bbl) as up to" -those volumes, just incase a.smailer tank makes it into the final design? This would be consistentwith how some of our CGF permits have been issued and our engineering team appreciates the design flexibility provided ." Based on distussionswith supervisors, it was determined this requestwasreasonable for providing the operator with flexibility, if needed,: for the final design of this facility. Additionally, it was determined a condition would be added to the permit requiring the operator to modify the permit in the event the final storage vessel design deviated from the original application that was used in this preliminary analysis and the basis for permitted emissions. The condition added to the permit is as follows: "Points 007, 006 and 007: Within thirty (30) days after commencement of operation of the storage vessels covered by points oat, 006 and 007 the owner o r operator shall submit to the Division sr completeAAEN and applicationto modify the permit to reflect the equipment installed under this permit the owner or operator will not be required to modify the permit per this condition in the event the owner or operator installs the following equipment as provided in the original application as the basis for permittedemfssio-ns: li) Point 001: Three (3)-254000 barrel internal floating roofstorage vessels (ii) Point 006: Three (3)1a0000barrel Internal floating roof storage -vessels (ail Point 007: Two (2)5,000 -barrel internal floating roof storage vessels."_ By structuring the permit tins way, the operator will still be abletobegin construction if a smaller tank than was originally permitted makes it into the final design while ensuring the permit is modified appropriately in the event a smalertank;is Installed. The condition also ensures the operator would not be required to! modify the permit If the final design of the facility matches with the original application. finally, it should be noted that if smaller tanks are, installed, the emissions will likely be lower due to lower throughput capabilities. The operator was provided with a draft permit containing the updates d'ncussed abone. The operator reviewed the permit and, expressed that they agreed with the changes mode and that they did not have any further comments Section 09 - Inventory SCC Coding and Emissions Factors AIRS Point N Process fi SCC Code Uncontrolled Emissions Pollutant Factor Control % Units 007 01 PM10 0.000E+00 0 Ib/1,000 gallons condensate throughput PM2.5 0.000E+00 0 Ib/1,000 gallons condensate throughput NOx 0.000E+00 0 Ib/1,000 gallons condensate throughput VOC 2.135E-01 0 Ib/1,000 gallons condensate throughput CO 0.000E+00 0 lb/1,000 gallons condensate throughput Benzene 2.275E-03 0 lb/1,000 gallons condensate throughput Toluene 6.235E-03 0 lb/1,000 gallons condensate throughput Ethylbenzene 1.749E-03 0 lb/1,000 gallons condensate throughput Xylene 7.162E-03 0 lb/1,000 gallons condensate throughput n -Hexane 1.382E-02 0 lb/1,000 gallons condensate throughput 224 TMP 1.718E-03 0 lb/1,000 gallons condensate throughput **Note - Emission factors for process 01 and 02 have been combined here solely for inventory purposes. When calculating actual emissions, the operator will calculate emissions for process 01 and 02 independently using separate emission factors as described in the preliminary analysis above. 30 of 35 K:\PA\2015\15 W E1451.CP1.xlsm Condensate Tank Regulatory Analysis Worksheet Cobra. Regulation 3 Pere Aand a-33333 and Pepe Reearnerd! ATTAINMENT This sort. Is located In the amid mnrtabnerd area. Since the aura dom. emit CO, en intentions Son . notion are hied es NIA Are uncontrdled xtual emissions from any criteria pollutants from this indinclualsource greater Man 2TPy (Regulation 3, Part A, Sec3on 1921.01? x. b the oonstru ction date Dervice date) prior t012/30/2002 and not modified after 12/31/2002 IS., PS k/emo 05-01 Definitions 1.12 and1.14 and section 2 br additional guidance on grandfather applicability), 3. Are total fl'ty uncontrollednbd VOCe suns greater than 5 TCr N greater than 10 Turn emissions greater Man 10 TPy (Regulation 3, Part 3, Section Not enough 1. Are urc0ntnol ed emissions from any zriterb pollutants horn this indindual source greater Man 1 TPV (Regulation 3, Partq Section II.0.1.al? Is the construction date (service date) prior to 12/30/2002 and rot modified after 12/31/2002 (See P5 Nemo05-01 Definition 1.12 and1'.14 and Section 1 for additional guidance on grandfather applicability") 3. Are total facility 00 requires 1 emission from the greaterthan 2Ter, NCV greater Man STP7 a CO emissions greater than 5 TPr (Regulation 3, Part 3, Section ll.0.2(0 'Source 59bram Regulation 7. S3Obn VI I. Dees this stiorage tank store "petroleum liquid"defined by Regulation 7 Section Vl.A2.g7 2. fey, this stomp tank meet any of the exemptionstion 7 on Man 40,000 sailo s (952 harrel?arisv1.01. 3. Dix.s the tank have a storage capacity greater 4. Does the storage tank have a fixed roof? 5. Is fix ed tank used fa the storage of petroleum liquids eh)Or have a true vapor pressure between D65 psis and 11.0 Psis at 20,(6.5'3)7 6. tithe feed roof tank equipped TAM an imemal nwtlng's," Storage tank is subject to Regulation 7, Section VIII.2.380 Storage tank is ablM al Storage lank is stabled to Regulation 7, Sections 21.0.2.3.12Hiii) 7. A the tank equipped with an externals AND is larger Man 952nd AND stores peaaeum squid AND is located in ozone noatainment area, B. Does Me tank meet any of the of Section Vl.e.1c.(i11o11117 9. Does the tank meet any of the exemptions exemptions ptions of Section VI.a2cg11R11217 10. Doespressure las storeM mare 1.3 psi., Istorge Tank is net 035(30 to Rg21.010n 7, Sertbn 11.0.11 11. Does ....Drage tare hake a storage capacity less Man 40,000 gams (952 berrel.l7 12. Das the tank liquids with a true vapor pressure beOveen 1.5 psia and 11.0 20,2 10 I. the stoaine storage anfacJity that receiks and stores pebdeum addressed by Regal a'on 7aSections VI.C.2 o VtC.37 wg17eo 1.017,3, 1117 vl.a3 s sagest n Regulation 7, Section VI n7 Section gar 1. Is this storage tank ozone control or one nom attainment/maintenance ea? Is Mss the and gas ex aabaon and operation', natural gas pressor station a natural g drip satin? 3 Is Ns storage tank processing plant' (Storage Tank not stillest to Regulation 7. Section XII Source Requires an APEX,. Go to the neat questa, Gotta next question Source Requires a permit Go to Me next question Go to the next questlon Source s subject toRegulation 'Section VI. d2.b.; Go to the next question Source is subject to Regulation' Section VI.R2.a.; Go to the next question Source is subject to Regulation 7 Section za.(.1 Go m the next question Source is 1 m g e3 Regulation Vl.aliibliii); Goo Me next Wesson Storage Tarr is not subject to Regulation 7, Ystion VI. B. 2.c. ., ..;I5mrce is not suresto Reg 7 Sec V1.R3. 1aA 1 'hs Go tO the question Na:_..... _. Storage Tank is not zubect to Regulation 7, Yceon%II Section MCA -General Requirements for Air Pollution Contra Equipment- Prevention of Leakage Section -Emissin Estimation Praedurm SMbn OI.D- Emission Contra Requirements SMbn AI.E- Mmitonne Soles ALF- Recadkeep ng and Repatig Conroe R..ubtion 7, hoden Sae 1. Is this ,tinge tank located in Me 0hr ozone control area or any ozone nnana0ment area or attainment/maintenance area, 2. Is this storageare? 3. Dees age tank exhibit "Rash) storing rwnatabn'zed qu tls) emissions and have uncontrolled actual emissions greater [honor equal to 2tans per year VOC7 this storage Tank a not subject to Regulation 7 section un.G Sectbn ALA, Emissions Contra Requirements Seaton a MAGI Requirements eqePsaedur uir menPollution Caned EpurPmmt- Prevention of SMbn - Emission 23307.02 Reaubn. 7. Section [Vii Is s tank ie...at a mmissim/naa avury, 2. Is this condensate storage tank' located at an on and gas exploration and production operation, wen production facility', natural gas compressor station or natural gas processing plant? 1 Is this c storage ta,k a rued roof storage tank? 4. Are uncontrolled vesrf this storage and equal to cc reefer than 6 tons per year VOL? [Storage subject to Regtabtlon' Sectbn13311 SectAn =IA -General Section %VICG1 •Control nons Emissions Conaafor Ar and Moniucon Control toring PmrsionuiPmem and Preuenuon w Emissions Seaton XVII... ping Requirements 5. Does the condensate storage tank contain onry'stadllaedv Iruid$t I6b orbto Ragulatiue 7, Section 15/11‘,2 Section %Vth.C2-Upture and Montaig for Storage Tanks fitted with Air Pdludm Control Equipment 40000 Part 60. Subpart KA Standards°. Po ..7nm. for Volatile Drunk Dodd Menge Vessels m amngeressel capedt7 greater than or equal to 75 cubic Teeters (m) *2 133131? 1 Does Me storage vessel meet the blowing exemption in 10.111gdry0(7 kea5 Go to Me next question X. vr r Storage Tart n not sub'ect to Regulation 7, Section Rll.G AA Go M next question Storage Tank is not subject to Regulation 7, Section MI fk9 iSI2age Tar* a not subject to Peguabn 7, Section %VII G2 �' G2 to the nest question a. oces thewesh. a design capacity less than cr equal to 1,589.37471' ['10 Mt] used for petroleum orcordensate stored, processed. cc treated price to custody transfer` as defined in 60.11121 Was this condensate storage tank 12,,,411176184,;882131or modill.(we definitions 40 CFR, 60.2) after July 23, 1984. Does the 0. meet the definition of^storage vessel"' in Does I. stOrage vessel tore a tdatile organic liquid WOO' as defined in 60.11,7 Does one a the following additional exemptions: a. Is the semrage vessel a pressure vessel designed to in excess of 204.9lePa (-25.7 psi] and without emissions ° re (8.1130),(227; or b. T. design capacity is greater than a equal to 151711['5508131) and stores a liquid with a maximum true wapw pressure' less than 3.5243(60.1102(097; or c, The design paciry is greater (ban or equal to 75th' (-672 BBL]but less than 151m'I'950 Beyare stores a liquid wens a maximum true vapor pressure less than 15.00Pa(50.110b(b))1 'Storage tank is subj. to tl5P547,60)2ding butnotllmned to, the fallowing pmdsdns Subpart ',General Provisiors 460.11118 -Emissions Control Standards for VOC 680.1131. Testing asst Procedures 460.1152 • Reporting arch Recookeeping 72,,i,emenft §8.1162 - MOSIOIing of Operations 84CFR, Part PO, subpart 0000" standards of P.n6omamefo Cob OP and Natural Gtr Production, Transmission and DbtrlbutIon . Was this condensate storage vessel construe.. reconstruct, a modified (see definitions 40CFR, 60.2) after August 23, 2011 and prior to September 18, 2015? 2 Dees this coMemate storage vessel meet Me deli.. of"storage vessel"'par 60.5430. 3, Is this condersate storage wssel locatedat 8 fkility in the onshore al and natural gas production segment, natural gas processing segment or natural gas tansmkssion and storage segment of the industry? a. ,e potential VOC emissOns' m the individual 5. Is Itre storage vessel subject 0 and controlled in accordance with requirements for storage vessels in 40 Part 60 subpart Kb or 40 CFR Part 63 Subpart HH? 'Storage suble0 m SOPS 0000 Subpart A, General Provisions per 260.5425 Tab0 3 760.6393-Emhsions Contra Standards b 901 4605413 -Testing and Procedures 7605395)6) • Notifrcedo, Reporting an 560000eepine Re7111651ems §60.3.116(c) Cover guirements §b0.5417 -Control Device Monitaing Requirements [Noa storage vessel h maybe, e: hawipe, determined° be subjectto laps 0000 due to...Oniom Moos atone per year`a0g on the apgrab866 determination data, t should '.71.16 sable, to NIPS 0000 per 8538(.32)88.6 il potential WC emissions drop below6 to, par yeas] 40041. Pert 8. Subpam 0000. Standards of Per°mence for Cm, ON and Natural Gm F.411Xi , los which 208686u0bn Modification or Reconstruction Commenced Alter September a 2015 1. Was this Condensate storage vessel constructed, reconstructed, or modified (see de6rfitions 40CFR, 60.21 after September 18, 2015? 2. Does tivs co.ensale storage vessel meet to definiIon of"1,arage vessel' per 371? 3. Is Otise a duty in the crude oil and natural gas 0eductkn segment, natural gas processing segment or natural gas transmission and stooge segment of the industry? 4. Are dial VOC emissions'storage vessel cage vessel greater than or equal tot tons Per yeah 5. R the potential vessel subject to and controlled in accordance with requirements b store a vessels M40 CFR Part 60 Subpart Kb or 40CFR Part 63 Subpart HH? Storage Tanks not subjectto NSPS CODW 40 CM Pao 53.348245 MALT MH 011 and fie Production Facilities 1. Is she tank located at a facility that is major' for storage2. Is tha storage tank Igated at an oil and natural gas production facility that meets either of tha following criteria: a. A facility that processes, upgrades or stores hydrocarbon liquids' (63.1601.)(2)); OR facility that processes, upgrades or stores natual gas prior m the point at which natural gas enters the natural gas transmission ana swage source category or is delivered to final end user' 163.?8(a)(3)), 3 Does the definition of "storage vessel.' in 63.761? 4 Does 0e tank meet the n meet the Cefintionof 'storage vessel with the potential for flash emissions"' per 63.?61? 5 Is the tank subject to control requirements under 40 CFR Part 60, Subpart Kb a Suboart00o0? !Morn, Subp.46, General provisions per 463.164 (al Table 463.?66-Emissions Control Standards 163.71 -Monitoring 163.734-Rrordkeepirg 83.rn-Reporting Go to the rest question Go. the neat question Go to next question Source is oible, NSPS Kb PACT Review PACT mlew 6 require X Regulation? do, no apply AND if the tank Is In the non ttelnmem ana. MO.., meets ...criteria. then review PACT reonlremmts DJs la men This tumant assists °perabs with ddafrinng applicabi0ly of certain requirement, gift Clean Air Act its impS7SlingiegvAUon, and AY Quagty Cabo! Commission regulation. This Wcufaytis rota Ne campoafkvt andie analysis ecodab* nayo. apply baprt/cukv situation based upon the in1Mhal face had circumWram. Ilse widen a creamle banY eve, regulation, or any otlmr/age* Dining requirement and is not legally enforces.. In lM ever. of any co,. ..6.080 the language c 406 ...mint and Msels'Igape &Me Cbm/wACG, es implementing reg2180S, and Air Qualify Conch Convnis3 n regulation', to language of the s8Ob of aviation will coning Theuse I non.mendstory language such n'rtconxrnrc("Iney,-sbutl,'ens 'can,'is Intended to scribe APCO laemaeion and recommendations, waalabV terminology such 38 "ms,ard'nepimnfare 25.1444300p3101Mf11ep,remexs under the terra oft. Lean Air Aft and Air Cheat, Gala Commission regulation, bbd flu charred hart 'staeebgsh legally Ishcirg regiments 0, enda/04.0 Storage Tank is not subject NSP50000-This 0. was construeted after the applicability date. Go to Me nest question Gone . nest Go to nest ci,snori Storage Tank is not subject NSP50000a. Storage Tank is not subject NSF5 auoa Storage Ta.is m[ subject MAR HH There are no MALT HH requirements for tanks at area sources Representative Stable Hydrocarbon Liquid Analyses Average Floating Roof Tank Information (001, 006, 007) Loadout Information (005) Tank 0059 Wattenbong Meter Meter 236 Meier 226 Earl Pony Injection Avenge 1100%VOC' 1.5•HAP) 100% VOC;Normalized i��,,��A Pollutant Mol % Mass % Mol % Mass % Mol % Mass % Mol % Mass % Mol % Mass % Mol % Mass % Mol % Mass % Mol % Mass % MW Gas Weight Gas (Ib/Ibmol) (Ib/Ibmol) Weight% CO2 : 0.016 0.0051 0 0 0 0 0 0 0 0 0.0032 0.00102 Nitrogen 0.033 0.0067 0.021 `. 0.0044 0.022 0.0054 0.079 0.0064 :0.068 40149 0.0346 0.00756 Methane 0.023 0.0027 0 0 0 0 0 0 0 0 0.0046 0.00054 Ethane 0.165 0.0361 0.134 00301 0.106 0.0283 0.057 0.0136 0.069 00163 : 0.1066 0.02483 , Propane -.1.225 0.4086 1.274 0.4201 1.146 0,4097 0.92 0.3219 :0.999 0.3457 1.1228 0.3872 1.1228 - 0.3872 1.015194 0.357314931 44.092 0.447619231 0.401753 i-butane OS26 0.2221 0.489 0.2125 0.465 0.2353 0,539 0.2486 0.498 0.2271 0.5034 0.22908 0.5034 0.22908 0.455155 0.21139903 58.118 0.264527243 0.237422 n-butane2.627 1094 2.529 1.0992 2475 1.2514 3.073 1.4172 .2.8631 1.3056 2.71342 1.23656 2.71342 1.23656 2.453373 1.141119193 58.118 1.425851237 1.279749 i-pentane :1.4419 0,7559 1.2683 0.6843 1.2922 ➢.811 1.7816 1.0199 1.579 0.8939 1.4726 0.833 1.4726 0.833 1.33147 0.768706964 72.114 0.960176154 0.86179 'Pentane -:3319 .2157 2.109 1.1379 2.142 1.3444 2.958 16934 2.6631 1.5076 2.43822 1.3798 2.43822 1.3798 2.204547 1.27330357 72.114 1.589787249 1.426887 cyclopentane -0.8922 0.4546 0.7829 ` 0.41116 1.1474 07 1.1359 0.6321 -0.87£1 0.4799 0.9661 0,53544 0.9661 0.53544 0.873511 0.494113396 70.13 0.6125936 0.54980%3 h -Hex ''4.8123 3.0747 4.9847' 3.2124 :5.7575 4:3154 6.3074'. 4.3123 : 3.8507 2.6037 . 5.14252 3.4917 9.4611 6.4731 9.4611 6.4731 86.18 8.15357598 7.318108 Cyclohexane 1.842 11264 2.0769`. 1.3071 23541 1.7235 2.3727.. 15845 1.7592 1.1616 2.08098 1.38062 2.08098 1.38062 1.881544 1.274060281 84.16 1.583507656 1.421251 Other c6 :7.057 4.3785 7.0817 4.5196 :8.9256 6.6259 8.8553 6.002I 6.4986 4.3489 7.68364 5.175 7.68364 5.175 6.94726 4.775550502 86.18 5.987148539 5.373667 other c7 4.4395 6.8341 10.5945 1.894 12.6003 10.918 10,7522 8.5026 ..9.4684 7.3948 10.57098 8.3087 10.57098 8,3087 9,557885 7.667413665 100.21 9.577956224 8.596538 Methylcyclohexane :3.3286 2.2321 3.7221.. 2.7331 4.1674 3.5597 3.7974.. 2.9586 3.1971 2.463 3.60252 2.7893 3.60252 2.7893 3.257264 2.57401482 98.19 3.198307342 2.870588 224TMP `.0.475 0.3389 0.5423' 0.3982 0.628 0.5364 0.5315'. 0.4141 0.5383 0.4147 : 0.54302 0.42046 0.942 0.8046 0.942 0.8046 : 114.23 1.0760466 0.965788 Benzene .0.8494 0.4821 0.9031 0.5275 " 1.0456 0.7105 1.0922 0.6769 0.7018 0.4301 0.91842 0.56542 1.6383 1.06575 1.6383 1.06575 78.12 1.27983996 ,1.148699. Toluene 1.8589 1.2445 2.3535 1.6216 2.4292 1.9471 2,3703: 1.7329 : 1.7643 1.2755 2.15524 1.56432 3.6438 2.92065 3.6438 2.92065 92.15 3.3577617 3.013704. EB 0,3407 0.2628 0.3655 0.2902 - 0.5915 0.5463 0.3774 0.3179 0.5952 44958 0.45.106 0.3826 0.8928 0.81945 0.8928 0.31945 106.17 0.94788576 0.850759 Xylene 1.8863 1.4552 2.2591.. 1.7936 2.4216 - 2.2366 2.3314.'. 1.964 2.2491 18735 2.2295 1.86458 3.6324 3.3549 3.6324 3.3549 106.17 3.85651908 3.461355 Octane 8.6619 7.1839 9.464 8.0788 11.8753 11.7799 8.9556 81135 9.9072 8.8632 9.7728 8.80386 9.7728 8.80386 8.8362 8.124355972 114.73 10.09359145 9.059338 nonane 9.2376 8.5075 9.6264 9.1231 11.7641 12.9796 9.0694 9.118 11.4681 11.39556 : 10.23312 10.22476 10.23312 10.22476 9.252404 9.435587341 128.26 11.86713375 10.65115 Decanes 41.0284 58.7074 39.3615.: 54.4879 26.4168 37.243 32.616.'. 48.9297 38.0092 52.3859'. 35.08638 50.35078 35.08638 50,35078 31.72379 46.46458033 142.28 45.13661161 40.51163 Alcohols .0.0643 0.015 0.0575: 0.0138 -02254 0.0628 0.0777:. 0.0198 0.3815 0.1027 0.16128 0.04262 1 \\4\\ _\\\Y \Vek4,Xik-Xtk 1.\\\?t.\tV�\\V\4\1R\\•l1\ •NNN\IIN\\fit Total 100 100 100 100 100 100 100 100 100 100 100 100 108.4574 107.0726 100 100 111.4164404 88.24696 91.6341 79.7896 84.56155 Permit number: Date issued: Issued to: DO on trol Division Department of Public Health b Environment CONSTRUCTION PERMIT 15WE1451 Facility Name: Plant AIRS ID: Physical Location: County: General Description: Issuance: 1 Noble Midstream, LLC Roan Oil Storage Facility 123/9E3A SEC 25 T3N R65W Weld County Oil Storage and Pipeline Injection Facility Equipment or activity subject to this permit: Facility Equipment ID AIRS Point Equipment Description Emissions Control Description TANK 1, TANK 2, TANK 3 001 Three (3) up to 250,000 barrel internal floating roof storage vessels used to store crude oil and condensate. Internal Floating Roof Fugitives 002 Equipment leaks (fugitive VOCs) from a crude oil and condensate storage and transport facility. None Loading L-1 005 Truck loadout of condensate and crude oil from storage vessels. Enclosed Flare TANK 4, TANK 5, TANK 6 006 Three (3) up to 100,000 barrel internal floating roof storage vessels used to store crude oil and condensate. Internal Floating Roof TANK 7, TANK 8 007 Two (2) up to 5,000 barrel internal floating roof storage vessels used to store crude oil and condensate. Internal Floating Roof 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 ;COLORADO Air Pollution Control Division minercf Pubic Health b mivorv.K.:nt Page 1 of 19 1. lution ntrol Division (the Division) no later than fifteen days of e la o . ''" e - - of o•`"=:'ion or issuance of this permit, by submitting a Notice of Startup form to the Division for the equipment covered by this permit. The Notice of Startup form may be downloaded online at www.colorado.gov/pacific/cdphe/other-air-permitting- notices. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation Number 3, Part B, Section III.G.1. and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self -certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. A self certification form and guidance on how to self -certify compliance as required by this permit may be obtained online at www.colorado.gov/pacific/cdphe/air-permit-self-certification. (Regulation Number 3, Part B, Section III.G.2.) 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline. (Regulation Number 3, Part B, Section III.F.4.) 4. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self -certification process. (Regulation Number 3, Part B, Section III.E.) 5. Points 001, 006 and 007: Within thirty (30) days after commencement of operation of the storage vessels covered by points 001, 006 and 007 the owner or operator shall submit to the Division a complete APEN and application to modify the permit to reflect the equipment installed under this permit. The owner or operator will not be required to modify the permit per this condition in the event the owner or operator installs the following equipment as provided in the original application as the basis for permitted emissions: • Point 001: Three (3) 250,000 barrel internal floating roof storage vessels • Point 006: Three (3) 100,000 barrel internal floating roof storage vessels • Point 007: Two (2) 5,000 barrel internal floating roof storage vessels 6. 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 7. Emissions of air pollutants shall not exceed the following limitations. (Regulation Number 3, Part B, Section II.A.4.) .A.4. ) Monthly Limits: Facility Equipment ID AIRS Point Process Pounds per Month Emission Type PM2.5 NO. VOC CO TANK 1, TANK 2, TANK 3 001 01 --- --- 5,555 --- Point 02 --- --- --- --- COLORADO Mr Pollution Control Division 'k Hr6Etn 5 ^ rzvvuTIMVIL Page 2 of 19 u 0 ..,: 01 --- --- 248 --- Fugitive Loading L-1 005 01 --- 298 4,019 756 Point TANK 4, TANK 5, TANK 6 006 01 --- --- 3,228 --- Point 02 --- --- --- --- TANK 7, TANK 8 007 01 --- --- 544 --- Point Notes: 1) 2) Monthly limits are based on a 31 -day month. Process 01 and 02 for points 001, 006, and 007 are as follow: a. Process 01: Emissions during normal storage vessel operation. b. Process 02: Emissions during internal floating roof landing events. The owner or operator shall calculate monthly emissions based on the calendar month. Facility -wide emissions of each individual hazardous air pollutant shall not exceed 1,359 pounds per month. Facility -wide emissions of total hazardous air pollutants shall not exceed 3,398 pounds per month. The facility -wide emissions limitation for hazardous air pollutants shall apply to all permitted emission units at this facility. Annual Limits: Facility Equipment ID AIRS Point Process Tons per Year Emission Type PM2.5 NO, V0C CO TANK 1, TANK 2, TANK 3 001 01 --- --- 32.7 --- Point 02 --- --- 7.8 --- Fugitives 002 01 --- --- 1.5 --- Fugitive Loading L-1 005 01 --- 1.8 23.7 4.5 Point TANK 4, TANK 5, TANK 6 006 01 --- --- 19.0 --- Point 02 --- --- 3.3 --- TANK 7, TANK 8 007 01 --- --- 3.2 --- Point 02 --- --- 0.2 Notes: 1) See "Notes to Permit Holder" for information on emission factors and methods used to calculate limits. 2) Process 01 and 02 for points 001, 006, and 007 are as follow: a. Process 01: Emissions during normal storage vessel operation. COLORADO Air Pollution Control Division raurtine.^:[:�f Public Mwich ' Environment Page 3 of 19 ring internal floating roof landing events. ■ Facility -wide emissions of each individual hazardous air pollutant shall not exceed 8.0 tons per year. Facility -wide emissions of total hazardous air pollutants shall not exceed 20.0 tons per year. The facility -wide emissions limitation for hazardous air pollutants shall apply to all permitted emission units at this facility. During the first twelve (12) months of operation, compliance with both the monthly and annual emission limitations is required. After the first twelve (12) months of operation, compliance with only the annual limitation is required. Compliance with the annual limits, for both criteria and hazardous air pollutants, shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve month total is calculated based on the previous twelve months' data. The permit holder shall calculate actual emissions each month and keep a compliance record on site or at a local field office with site responsibility for Division review. 8. The owner or operator shall track emissions from all insignificant activities at the facility on an annual basis to demonstrate compliance with the facility potential emission limitations as indicated below. An inventory of each insignificant activity and associated emission calculations shall be made available to the Division for inspection upon request. For the purposes of this condition, insignificant activities shall be defined as any activity or equipment, which emits any amount but does not require an Air Pollution Emission Notice (APEN) or is permit exempt. (Reference: Regulation 3, Part C. II.E.) Total potential emissions from the facility, including all permitted emissions and potential to emit from all insignificant activities, shall be less than: • 100 tons per year of VOC 9. The emission points in the table below shall be operated and maintained with the emissions control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit. (Regulation Number 3, Part B, Section III.E.) Facility Equipment ID AIRS Point Control Device Pollutants Controlled TANK 1, TANK 2, TANK 3 001 Internal Floating Roof VOC and HAP Loading L-1 005 Enclosed Flare VOC and HAP TANK 4, TANK 5, TANK 6 006 Internal Floating Roof VOC and HAP TANK 7, TANK 8 007 Internal Floating Roof VOC and HAP 10. Point 002: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that ;COLORADO Air Pollution Control Division lent of Pvb i Ykat is & iron zenc Page 4 of 19 ted. These records shall be provided to the Division upon PROCESS LIMITATIONS AND RECORDS 11. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Regulation Number 3, Part B, II.A.4.) Process Limits Facility Equipment ID AIRS Point Process Parameter Annual Limit Monthly Limit (31 days) TANK 1, TANK 2, TANK 3 001 Condensate/Crude Oil Throughput 164,250,000 barrels 13,950,000 barrels Internal Floating Roof Landings 3 roof landings --- Loading L-1 005 Condensate/Crude Oil Loading 4,380,000 barrels 372,000 barrels TANK 4, TANK 5, TANK 6 006 Condensate/Crude Oil Throughput 109,500,000 barrels 9,300,000 Barrels Internal Floating Roof Landings 3 roof landings --- TANK 7, TANK 8 007 Condensate/Crude Oil Throughput 730,000 barrels 62,000 barrels Internal Floating Roof Landings 2 roof landings --- The owner or operator shall monitor monthly process rates based on the calendar month. During the first twelve (12) months of operation, compliance with both the monthly and annual throughput limitations is required. After the first twelve (12) months of operation, compliance with only the annual limitation is required. Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of 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 Number 1, Section II.A.1. Ft 4.) 13. These sources are subject to the odor requirements of Regulation Number 2. (State only enforceable) 14. Points 001, 005, 006 and 007: The permit number and ten digit AIRS ID number assigned by the Division (e.g. 123/4567/001) shall be marked on the subject equipment for ease of identification. (Regulation Number 3, Part B, Section III.E.) (State only enforceable) 15. Points 001, 006 and 007: These sources are subject to the applicable requirements of Regulation Number 7, Section VI.B.2. 16. Points 001, 006 and 007:These sources are subject to the New Source Performance Standards requirements of Regulation No. 6, Part A, Subpart Kb, Standards of Performance for Volatile COLORADO Air Pollution Control Division Page 5 of 19 essels 'r which construction, reconstruction or modification omm d Ju 4, in i ing, but not limited to, the following: • 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 or with a design capacity greater than or equal to 75 m3 but less than 151 m3 containing a VOL that, as stored, has a maximum true vapor pressure equal to or greater than 27.6 kPa but less than 76.6 kPa, shall equip each storage vessel with one of the following: ■ §60.112b(a)(1) A fixed roof in combination with an internal floating roof meeting the following specifications: ■ §60.112b(a)(1)(i) The internal floating roof shall rest or float on the liquid surface (but not necessarily in complete contact with it) inside a storage vessel that has a fixed roof. The internal floating roof shall be floating on the liquid surface at all times, except during initial fill and during those intervals when the storage vessel is completely emptied or subsequently emptied and refilled. When the roof is resting on the leg supports, the process of filling, emptying, or refilling shall be continuous and shall be accomplished as rapidly as possible. • §60.112b(a)(1)(ii) Each internal floating roof shall be equipped with one of the following closure devices between the wall of the storage vessel and the edge of the internal floating roof: • (A) A foam- or liquid -filled seal mounted in contact with the liquid (liquid -mounted seal). A liquid -mounted seal means a foam- or liquid -filled seal mounted in contact with the liquid between the wall of the storage vessel and the floating roof continuously around the circumference of the tank. • (B) Two seals mounted one above the other so that each forms a continuous closure that completely covers the space between the wall of the storage vessel and the edge of the internal floating roof. The lower seal may be vapor -mounted, but both must be continuous. • (C) A mechanical shoe seal. A mechanical shoe seal is a metal sheet held vertically against the wall of the storage vessel by springs or weighted levers and is connected by braces to the floating roof. A flexible coated fabric (envelope) spans the annular space between the metal sheet and the floating roof. • §60.112b(a)(1)(iii) Each opening in a noncontact internal floating roof except for automatic bleeder vents (vacuum breaker vents) and the rim space vents is to provide a projection below the liquid surface. ■ $60.112b(a)(1)(iv) Each opening in the internal floating roof except for leg sleeves, automatic bleeder vents, rim space vents, column wells, ladder wells, sample wells, and stub drains is to be equipped with a cover or lid which is to be maintained in a closed position at all times (i.e., no visible gap) except when the device is in actual use. The cover or lid shall be equipped with a gasket. Covers on each access hatch and automatic gauge float well shall be bolted except when they are in use. COLORADO Air Pollution Control Division uf P, btc Health 6. Emir=rem Page 6 of 19 b(a)(1) gin) Automatic bleeder vents shall be equipped with a gasket o be '' =d 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. • §60.112b(a)(1)(vi) Rim space vents shall be equipped with a gasket and are to be set to open only when the internal floating roof is not floating or at the manufacturer's recommended setting. • $60.112b(a)(1)(vii) Each penetration of the internal floating roof for the purpose of sampling shall be a sample well. The sample well shall have a slit fabric cover that covers at least 90 percent of the opening. • §60.112b(a)(1)(viii) Each penetration of the internal floating roof that allows for passage of a column supporting the fixed roof shall have a flexible fabric sleeve seal or a gasketed sliding cover. • §60.112b(a)(1)(ix) Each penetration of the internal floating roof that allows for passage of a ladder shall have a gasketed sliding cover. • §60.113b - Testing and procedures The owner or operator of each storage vessel as specified in §60.112b(a) shall meet the requirements of paragraph (a), (b), or (c) of this section. The applicable paragraph for a particular storage vessel depends on the control equipment installed to meet the requirements of §60.112b. §60.113b(a)(1) Visually inspect the internal floating roof, the primary seal, and the secondary seal (if one is in service), prior to filling the storage vessel with VOL. If there are holes, tears, or other openings in the primary seal, the secondary seal, or the seal fabric or defects in the internal floating roof, or both, the owner or operator shall repair the items before filling the storage vessel. §60.113b(a)(2) and (3) If the roof is equipped with a liquid mounted or mechanical shoe primary seal or a double seal system then the testing will follow the procedures outlined in §60.113b(a)(2) or (3), respectively. §60.113b(a)(4) Visually inspect the internal floating roof, the primary seat, the secondary seal (if one is in service), gaskets, slotted membranes and sleeve seals (if any) each time the storage vessel is emptied and degassed. If the internal 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, or the gaskets no longer close off the liquid surfaces from the atmosphere, or the slotted membrane has more than 10 percent open area, the owner or operator shall repair the items as necessary so that none of the conditions specified in this paragraph exist before refilling the storage vessel with VOL. In no event shall inspections conducted in accordance with this provision occur at intervals greater than 10 years in the case of vessels conducting the annual visual inspection as specified in paragraphs (a)(2) and (a)(3)(ii) of this section and at intervals no greater than 5 years in the case of vessels specified in paragraph (a)(3)(i) of this section. §60.113b(a)(5) Notify the Administrator in writing at least 30 days prior to the filling or refilling of each storage vessel for which an inspection is required by paragraphs (a)(1) and (a)(4) of this section to afford the Administrator the opportunity to have an observer present. If the inspection required by paragraph (a)(4) of this section is not planned and the owner or operator could not have known about the inspection 30 days in advance or refilling the tank, the owner or 'COLORADO Air Pollution Control Division I:an cent Public !'leahki l.C Page 7 of 19 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 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. §60.115b(a) After installing control equipment in accordance with §60.112b(a)(1) (fixed roof and internal floating roof), the owner or operator shall meet the following requirements. §60.115b(a) (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)(1) and §60.113b(a)(1). This report shall be an attachment to the notification required by §60.7(a)(3). §60.115b(a) (2) Keep a record of each inspection performed as required by §60.113b (a)(1), (a)(2), (a)(3), and (a)(4). Each record shall identify the storage vessel on which the inspection was performed and shall contain the date the vessel was inspected and the observed condition of each component of the control equipment (seals, internal floating roof, and fittings). §60.115b(a) (3) If any of the conditions described in §60.113b(a)(2) are detected during the annual visual inspection required by §60.113b(a)(2), a report shall be furnished to the Administrator within 30 days of the inspection. Each report shall identify the storage vessel, the nature of the defects, and the date the storage vessel was emptied or the nature of and date the repair was made. §60.115b(a) (4) After each inspection required by §60.113b(a)(3) that finds holes or tears in the seal or seal fabric, or defects in the internal floating roof, or other control equipment defects listed in §60.113b(a)(3)(ii), a report shall be furnished to the Administrator within 30 days of the inspection. The report shall identify the storage vessel and the reason it did not meet the specifications of §61.112b(a)(1) or §60.113b(a)(3) and list each repair made. • §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 COLORADO Air Pollution Control Division $ ihaurmerit et Public Meath 8 E•wvoru?tent Page 8 of 19 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 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. (5 60.12) c. Written notification of construction and initial startup dates shall be submitted to the Division as required under § 60.7. COLORADO Air Pollution Control Division Uc.:rrtmem of PubPubLo Wealth Ft Environment Page 9 of 19 ns, and malfunctions shall be maintained, as required 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 5 60.7. g. Performance tests shall be conducted as required under 5 60.8. h. Compliance with opacity standards shall be demonstrated according to § 60.11. 17. Point 002: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). The operator shall satisfy the requirement to apply RACT by implementing and following the leak detection and repair program (LDAR) per Colorado Regulation 7 Section XVII.F. 18. Point 005: No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Regulation Number 1, Section II.A.5.) 19. Point 005: This source is located in an ozone non -attainment or attainment -maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 20. Point 005: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.D.2): 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 at the facility (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect onsite loading equipment during loading operations to monitor compliance with above conditions. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. Point 005: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable OPERATING £t MAINTENANCE REQUIREMENTS 22. Points 001, 005, 006 and 007: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to the O&M plan are subject to Division approval prior to implementation. (Regulation Number 3, Part B, Section III.G.7.) 23. Point 005: The owner or operator of a loadout at which an enclosed flare is used to control emissions shall: 'COLORADO Air Pollution Control Division Llti,pkfi'merit Lit Public Health EmirUnl"?!IC Page 10 of 19 b. c. d. e. collection and return equipment to collect vapors during of outbound transport trucks and route these vapors to the enclosed flare. Include devices to prevent the release of vapor from vapor recovery hoses not in use. Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. f. 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. g. Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 24. Point 002: 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 25. Point 005: The owner or operator shall demonstrate compliance with opacity standards, using EPA Reference Method 9, 40 C.F.R. Part 60, Appendix A, to measure opacity from the flare. This measurement shall consist of a minimum twenty-four consecutive readings taken at fifteen second intervals over a six minute period. (Regulation Number 1, Section II.A.1 and II.A.5) Periodic Testing Requirements 26. This source is not required to conduct periodic testing, unless otherwise directed by the Division or other state or federal requirement. ADDITIONAL REQUIREMENTS 27. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Regulation Number 3, Part A, II.C.) • Annually by April 30th whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOr) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per year, a change in COLORADO Air Pollution Control Division eaE;n Page 11 of 19 e (1) ton per year or more or five percent, whichever is ed 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. 28. The requirements of Colorado Regulation No. 3, Part D shall apply at such time that any stationary source or modification becomes a major stationary source or major modification solely by virtue of a relaxation in any enforceable limitation that was established after August 7, 1980, on the capacity of the source or modification to otherwise emit a pollutant such as a restriction on hours of operation (Reference: Regulation Number 3, Part D, V.A.7.B). GENERAL TERMS AND CONDITIONS 29. 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. 30. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7- 114.5(12)(a) C.R.S. and AQCC Regulation Number 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self -certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self -Certify for Final Authorization section of this permit. 31. 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. 32. 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. 33. 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 (COLORADO Air Pollution Control Division :r?arun " ii:L( Public Health & :ZWUUnUY'unt Page 12 of 19 to self ertification and final authorization by the Air Pollution grou . " et 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. 34. 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. 35. 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: Harrison Slaughter Permit Engineer Permit Histo Issuance Date Description Issuance 1 This Issuance Issued to Noble Midstream, LLC Permit for internal floating roof storage vessels, hydrocarbon loadout and fugitive emissions at a new synthetic minor crude oil/condensate storage facility located in the ozone non -attainment area. COLORADO 7utian Control Division .anent .+cf °u :Ric kkai.h b. _^iuortrsent Page 13 of 19 No th 4W this r it issuance: 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit. (Regulation Number 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: https://www.colorado.gov/pacific/cdphe/aqcc-regs ' 4) The following emissions of non -criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. AIRS Point Pollutant CAS # Uncontrolled Emissions (lb/yr) Controlled - Emissions (lb/yr) 001 Benzene 71432 --- 862 Toluene 108883 --- 2,362 Ethylbenzene 100414 --- 663 Xylenes 1330207 --- 2,713 n -Hexane 110543 --- 5,234 2,2,4- Trimethylpentane 540841 --- 651 002 Benzene 71432 32 --- Toluene 108883 86 --- Ethylbenzene 100414 24 --- Xylenes 1330207 98 --- n-Hexane 110543 190 --- 2'2'4 Trimethylpentane 540841 24 --- 005 Benzene 71432 10,870 544 Toluene 108883 28,517 1,426 Ethylbenzene 100414 8,050 403 Xylenes 1330207 32,752 1,638 COLORADO Air Pollution Control Division it" i £r _rn IECOIT r_nc Page 14 of 19 n - ° N s 543 69,246 3,463 2,2,4- Trimethylpentane 540841 9,139 457 006 Benzene 71432 --- 473 Toluene 108883 --- 1,296 Ethylbenzene 100414 --- 364 Xylenes 1330207 --- 1,489 n -Hexane 110543 --- 2,872 2,2,4- Trimethylpentane 540841 --- 357 007 Benzene 71432 --- 70 Toluene 108883 --- 192 Ethylbenzene 100414 --- 54 Xylenes 1330207 --- 220 n -Hexane 110543 --- 424 2,2,4- Trimethylpentane 540841 --- 53 Notes: 1) 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. 2) The control devices (internal floating roofs) for points 001, 006 and 007 are integrated into the storage vessels. As such, separate "uncontrolled" emissions are irrelevant for these points. 5) The emission levels contained in this permit are based on the following emission factors: Point 001: Process 01: CAS # Pollutant Controlled Emission Factors lb/bbl Source VOC 3.98x10-4 EPA Tanks 4.0.9d 71432 Benzene 4.23x10"6 Mass Balance 108883 Toluene 1.16x10-5 Mass Balance 100414 Ethylbenzene 3.25x10-6 Mass Balance 1330207 Xylene 1.33x105 Mass Balance 110543 n -Hexane 2.57x10"5 Mass Balance 540841 2,2,4- Trimethylpentane 3.19x10"6 Mass Balance Note: The control device (internal floating roof) for point 001 is integrated into the storage vessel. !COLORADO Air Pollution Control Division Van me^a::;f Akit Health & Environment Page 15 of 19 CAS # Pollutant Controlled Emission Factors lb/roof landing event Source VOC 5,188 AP -42 Chapter 7 71432 Benzene 55.3 Mass Balance 108883 Toluene 151.5 Mass Balance 100414 Ethylbenzene 42.5 Mass Balance 1330207 Xylene 174 Mass Balance 110543 n -Hexane 335.8 Mass Balance 540841 2,2,4 Trimethylpentane 41.7 Mass Balance Note: The emission factors represented above were calculated using the equations in AP -42 Chapter 7 for storage vessels with an internal floating roof and full liquid heel (See page 7.1-87 for equations). Point 002: Component Gas Service Heavy Oil Light Oil SWater/Oil ervi Service Connectors 988 --- 872 88 Flanges 188 --- 146 18 Open -Ended Lines --- --- --- --- Pump Seals --- --- 18 --- Valves 532 --- 950 170 Other 334 --- 410 56 VOC Content (wt%) 100% --- 100% 100% Benzene Content (wt%) 1.07% --- 1.07% 1.07% Toluene Content (wt%) 2.92% --- 2.92% 2.92% Ethylbenzene (wt %) 0.82% --- 0.82% 0.82% Xylenes Content (wt%) 3.35% --- 3.35% 3.35% n -Hexane Content (wt%) 6.47% --- 6.47% 6.47% 2,2,4-Trimethylpentane (wt%) 0.80% --- 0.80% 0.80% *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 1.0E-05 7.5E-06 9.7E-06 1.0E-05 Flanges 5.7E-06 3.9E-07 2.4E-06 2.9E-06 Open-ended Lines 1.5E-05 7.2E-06 1.4E-05 3.5E-06 Pump Seats 3.5E-04 NA 5.1E-04 2.4E-05 Valves 2.5E-05 8.4E-06 1.9E-05 9.7E-06 Other 1.2E-04 3.2E-05 1.1E-04 5.9E-05 Source: Table 2-8 EPA -453/R95-017 COLORADO I Air Pollution Control Division 1 EX:p"4I'ment of Pullin: Heath 8 ,thitrortheni Page 16 of 19 p nc tt ;'emi `n`.ns its in t permit will be demonstrated by using the TOC emission factors n th e sl ++ wt ntati mponent counts, multiplied by the VOC content represented in the table above. Point 005: CAS # Pollutant Uncontrolled Emission Factors lb/bbl Controlled Emission Factors lb/bbl Source NOx 7.99x10 4 7.99x10"4 CDPHE CO 2.03x1O3 2.03x1O3 CDPHE VOC 2.16x101 1.08x10 ` AP -42 71432 Benzene 2.48x103 1.24x10-4 Mass Balance 108883 Toluene 6.51x10-3 3.25x10-4 Mass Balance 100414 Ethylbenzene 1.83x10-3 9.18x10-5 Mass Balance 1330207 Xylene 7.47x103 3.73x1O4 Mass Balance 110543 n -Hexane 1.58x10 ` 7.90x10-4 Mass Balance 540841 2,2,4- Trimethylpentane 2.08x10 3 1.04x10-4 Mass Balance Note: 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) = 5.4851 psia M (vapor molecular weight) = 64 lb/lb-mot T (temperature of liquid loaded) = 510.23 °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 an enclosed flare efficiency of 95%. Point 006: Process 01: CAS # Pollutant Controlled Emission Factors lb/bbl Source VOC 3.46x10-4 EPA Tanks 4.0.9d 71432 Benzene 3.68x10-6 Mass Balance 108883 Toluene 1.0x10"' Mass Balance 100414 Ethylbenzene 2.83x10"6 Mass Balance 1330207 Xylene 1.15x10"' Mass Balance 110543 n -Hexane 2.23x10-' Mass Balance 540841 2,2,4- Trimethylpentane 2.78x1O6 Mass Balance Note: The control device (internal floating roof) for point 006 is integrated into the storage vessel. Process 02: CAS # Pollutant Controlled Emission Factors lb/roof landing event Source VOC 2,174.2 AP -42 Chapter 7 COLORADO Mr Pollution Control Division _anrtirier.;t zt 7?vbtu. hietza e & i mr.¢orur m Page 17 of 19 CAS # Pollutant ontrolled l ion Factors lb/roof landing event Source 71432 Benzene 23.2 Mass Balance 108883 Toluene 63.5 Mass Balance 100414 Ethylbenzene 17.8 Mass Balance 1330207 Xylene 72.9 Mass Balance 110543 n -Hexane 140.7 Mass Balance 540841 2,2,4- Trimethylpentane 17.5 Mass Balance Note: The emission factors represented above were calculated using the equations in AP -42 Chapter 7 for storage vessels with an internal floating roof and full liquid heel (See page 7.1-87 for equations). Point 007: Process 01: CAS # Pollutant Controlled Emission Factors lb/bbl Source VOC 8.61x10.3 EPA Tanks 4.0.9d 71432 Benzene 9.17x10-5 Mass Balance 108883 Toluene 2.51x10-4 Mass Balance 100414 Ethylbenzene 7.05x10-' Mass Balance 1330207 Xylene 2.88x10-4 Mass Balance 110543 n -Hexane 5.57x10-4 Mass Balance 540841 2,2,4- Trimethylpentane 6.92x10"5 Mass Balance Note: The control device (internal floating roof) for point 007 is integrated into the storage vessel. Process 02: CAS # Pollutant Controlled Emission Factors lb/roof landing event Source VOC 129.3 AP -42 Chapter 7 71432 Benzene 1.4 Mass Balance 108883 Toluene 3.8 Mass Balance 100414 Ethylbenzene 1.1 Mass Balance 1330207 Xylene 4.3 Mass Balance 110543 n -Hexane 8.4 Mass Balance 540841 2,2,4 Trimethylpentane 1.0 Mass Balance Note: The emission factors represented above were calculated using the equations in AP -42 Chapter 7 for storage vessels with an internal floating roof and full liquid heel (See page 7.1-87 for equations). !COLORADO Air Pollution Control Division Health b Env'vunmenc Page 18 of 19 6) I e.a ° e hR S 5 `' 14.1, e ; h Air Pollutant Emission Notice (APEN) associated with ermi ° ` a a a y from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This permit fulfills the requirement to hold a valid permit reflecting the storage tank and associated control device per the Colorado Oil and Gas Conservation Commission rule 805b(2)(A) when applicable. 8) This facility is classified as follows: Applicable Requirement Status Operating Permit Synthetic Minor Source of: VOC, Toluene, Xylenes, n -Hexane, and Total HAPs NANSR Synthetic Minor Source of: VOC MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 9) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1 -End Subpart A - Subpart KKKK NSPS Part 60, Appendixes Appendix A - Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A - Subpart Z MACT 63.600-63.1199 Subpart AA - Subpart DDD MACT 63.1200-63.1439 Subpart EEE - Subpart PPP MACT 63.1440-63.6175 Subpart QQQ - Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ - Subpart MMMMM MACT 63.8980 -End Subpart NNNNN - Subpart XXXXXX !COLORADO Air Pollution Control Division merst%f Public 14each 6 Env6{nvr:ent Page 19 of 19 de Oil Stora AIR POLLUTANT EMISSION NOTICE (APEN) Sc Application for Construction Permit — Cr 2 C' r C3 a .C. 5 [Leave blank unless APCD has already assigned a permit Al 8. AIRS ID] 'ermit Number: [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.] acility Equipment ID: ection 01 — Administrative Information Change permit limit APEN Submittal for Permit Exempt/Grandfathered source APEN Submittal for update only (Please note blank APEN's will not be accepted) ®❑❑ ❑ ❑ ¢�3 u 00 74. O co "ai- O O. U -7c-5' CCU y Q U CJ N z� Noble Midstream, LLC Company Nam Roan Oil Storage Facility Source Name: 1625 Broadway, Suite 2200 Mailing Addre C) > shaun.higgins(Nnblenergy.com ection 03 — General Information C. t 9/1 9u NC) C C) Q) E C U C C O O 3 C C n C) C) 3 h r" O zzz Normal Flours of Source Operation: Are Flash Emissions anticipated at these tanks U C F O LE - n 0 n y L V C) o v Lel co El LE 7 fl, SID ^ - y _., c 1",' E r r u G... v p G. L i _. o z = O - E 7 • Vv) W a o c, n m L �.. n y r y 69a 0. L L L CJ G j N 0 w G V'7 C N T, d o C7 r. o COo V c, C 'V y G>= U .C '�' O C U 67 E" R '- 7 ±_ L C: C) O O C. '; CCCC ^ h L �. a O 0 y .7-- C C C O ....= + '� v' ^ �• C L O en n L V1 3.' Cs y d y = T S-, I) C G o E i, p >,'4 5d7W c 1= �� CY N L''.CD ct UUO-= C C.�. u � M, ,,_,= A 4) °> o r O `'j u° n d p i C C C 'c. m .C .y O O 'C C C!2 Cd c o p .p a 'y v° i ea o' 4 p 4 .a >G C C= L� L C = C L c'''' > o e °u C a 6. c o c 0.a a UWd > ° 52¢ gW LUt=1¢ A C O C) C. L L" y p F C) 04 — Stora O 0 i Requested Permit CC T p CC C C •C) C) C O 0 CC O U c C .C1 CV i RVP of Sales Oil ) C C) tfl r External Floating Roof: Internal Floating Roof -14 O C) ❑ IF; Cfl C7 Cr C) CO P W > O1:1 O t C) y CO O 3cd Fixed Roof: C v v ll CC"— v C IZ C1Co aa o > a. C7 z CO C7 � L m y � y O EC: C F"o --. O 1/1 N O C N b O G IA C EA ra L,03 y E' 7> a7 tog - aJ es on L CC i a. O 3t m O V ZE Ci7 C) m C 0 H a Co L CS O 7 C, L C) CC 0 d C) z El El Name of Well -. C Emission Source AIRS ID: Permit Number: at/Long or UTM tion) Location (Datum & either c Ca a Ca C Ca C © Ca a r Ca r- C Ca U 7 — C C t N c{ Ca C Ca Ca Ca a • Ca Ca - 3U¢ Lt C. Ca v. Ca 3 V > ier Diameter (inches) _ >❑ Ca Ca • :J Ca a N.15 c. C C r C ;, ti := � Lc: section 07 — Control Device Informatio Make/Model C U v: a D C Ca a U o. E- L G U a C Ca Li VOC & HAP Control Efficiency: heat content: CO n C a Ca C C C a C� secl for control Vapor Recovery Unit (VRU) Make/Mode a O 0 ssions vented) Ca C) on C) O C C a Ca O c.. Ca. O C. 0 i Information n Technolo C L C a ction 08 — Gas/Li DI) a. DC CG a Do Ca OC m a CC U • Col 9) n a CC 7-r: C a L DC h C) a vle m C CC C) C) C_) C) L J CC. a a a • U Ca a G Ca C. E CC Ca Ca CC O Ca Ca CC E W 4.44 C CC C. Ca Cl 0 Ca O CD Ca u C c CD Ca Ca 3 Ca Ca a C CC C v CC CC a i Ca L , L U pi TANKS 4.O.9d Liquid Analysis II Liquid Analysis Liquid Analysis Liquid Analysis n -Hexane _;.t,,,.l„y.i ;-5 lb/bbl 2al 7.'Z. Liquid Analysis 2,2,4-Trimeth I entane :" lb/bbl 0:2b Liquid Analysis Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions L a 1 Uncontrolled (Tons/Year) I lin •O N 611 10 fn o uA © O It- N Cr) CC nw Actual Calendar Year Emission' - a Ca o, U Uncontrolled (Tons/YearLI Emission Factor Units o o o Uncontrolled Basis � X _� X x d^S 7- 1 C C CC ] xON VOC Co 'C N N a a a a C C a Cu- m a O - +• 7.77 u G O z CD y a L G. or CJ L O CC ? o E E O C. L a o _ a C. C C. O G = C U a Ca d .C CJ c_ o c E E o L O C 4C. ,9 C C G aa. c. c CC = C O A CJ E O C h C y C y L C1 a O L n a a y, L- Ca Ca C o CCU a c 0.7 c C m 7,4 v .y Ca 4 CU C c C Ca a C CC zg C. Ca C C ,C on Ca v C o T Ca J C ;,,s c v v C •y C cS Z .C C C1. H Q ° Z CC C C +] d G L + CJ C N Ca' C a •rr C Ca G C) v 'D N Ca C- CC Ca ❑ • U1 O Issuance. U C U C C • O AP Form-APCD-210-CrudeTankAPEN 150K.do PL10P. - of onent Leak Emissions' u [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.] Facility Equipment ID: Section 02 — Requested Action (Check applicable request boxes) Section 01 — Administrative Information for NEW permit or newly reported emission source Change company name .T O ❑ Transfer of ownership ❑ ❑ to limit HAPs with a Federally enforceable limit on PTE ri1 ▪ U O 4• OO4 APEN Submittal for update only (Please note blank APENs will not be accepted) D❑ DO w N 0 0 CO V b O U N '45 ei o dz Section 03 — General Information For new or reconstructed sources, the projected startup date is: For existing sources, operation began on: ses N 3 > O Normal Hours of Source Operation: C Cp C L O E • 5 zU - C ❑ O _ • Z= o 0 �w Q) O ❑ o E 0 a � - .. U O 0 0 O O U C V i N O � • w W O -°oa 04 z P ,� W ca 0 E..9 .O Fs. V] C U L d N c0 '0 R 3 .O x s aV s- E a) = cu .�i p O O. N s 0. E L • c 3- ` en o v O A w o ti) Q I. v o o f o O •— +• asa .4 ' > U R 6. C O O G ,..� a0 • w b o 2 �o q �? L O v = o a) •—. o 70 CA .0 U 0 O • 0 0 " i A U >9ea ,.Q.0 7 OU2 O�.6 H axi'.O-� Ud4:'AQ O O oo V")ers... M M M O, Cr, O\ 'O 'O en c%1 o00z en en cn Air Pollution Control Division: Small Business Assistance Program (SBAP): 0 O O 0 Information O 0 Section 04 — Re Don't know Don't know Don't know Don't know ❑❑❑ ❑ O O O O Z z z z DODO DODO Is this equipment subject to Regulation 7, Section XVII.F? Is this equipment subject to NSPS 40 CFR Part 60, subpart Is this equipment subject to NSPS 40 CFR Part 60, subpart OOOO? Is this equipment subject to NESHAP 40 CFR Part 63, Subpart HH? Section 05 — Stream Constituents tzs A N Ct ti O. Ct U cc O C O 011 3 U O N wT C 0 a n -Hexane (wt. %) V' s .. Xylene (wt. %) e: c Ethylbenzene' I (wt. %) o x ci c c Toluene (wt. %) 6 ,-1 t-i N Benzene (wt. %) 0 O VOC (wt. %) 8 Stream Heavy Oil (or Heavy Liquid) Light Oil (or Light Liquid) O' 1. Ct 3'. Check box to request copy of draft permit prior to public notice or issuance. O Ct Ct b O a O SC c -o U > Ct C O b C O C 'C C R CO N Ct C U C O. S C C FormAPCD-203-FugitiveComponentLeaksAPEN-Ver.11-13-2014 FORM APCD-203 onent Leak Emissions' Emission Source AIRS ID: Permit Number: & Control Information Section 07 —Leak Detection & Re Section 06 — Location Information (Provide Datum and either Lat/Long or UTM) - X a 0 4) O c V a C CD P4 <CC 0 00 CO o`n Q >° O Q ❑ � C Q 0 0 v 0 O A a) 0. O a a ti 0 U U LDAR per NSPS O ❑ E 0 O a 0 z ❑ ❑ E E a C" .5 e o 00 ai so N > > Td 00 m o o Q o Q C o o 5 •- p •0 CO CO a) cr.) 0 0 -104.614370 N- O C a Water/Oil Units lb/hr/source lb/hr/source Ilb/hr/source I lb/hr/source Lo LU N N C O) t7 ca t9ili N Lo M ` '- Count2 I ��o Orr Units v n 7 S . �. y f i` W+� — SI a' J S`. s .7- 9 S i cn Light Oil (or Light 1 14f, r i w tf • un z- .� i c4 I Count2 Heavy Oil (or Heavy Liquid) I (4.1 S. W NC 0 U 44, c Units Ib/hr/source lb/hr/source lb/hr/source lb/hr/source lb/hr/source H •W Lo uJ N -, _ ' 3.31E-5 15.51E-5 Y W to (0 N — N �C O u co co co co 1532 •et c.) O) ,— O O _ 0) u - Equipment Type Connectors IFlanges Open -Ended Lines IPump Seals Valves Other3 0 0 a 0 U Y 0 E 9- 45 • Estimation Method or Emission Factor Source a r W Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. Requested Permitted Emissions5 IControlled (Tons/Year) S Uncontrolled (Tons/Year) S Actual Calendar Year Emissions4 Controlled (Tons/Year) Uncontrolled (Tons/Year) Emission Factor Units Identify in Section 08 Uncontrolled Basis Control Efficiency (% Reduction) Identify in Section 07 Control Device Description Primary Secondary Pollutant ' Benzene Toluene Ethylbenzene Xylene n -Hexane o C a) .0) a.' C 0 iv 0 u 4., 0 C.) a Signature of Person Legally Authorized to Supply Data Fonf APCD-203-FugitiveComponentLeaksAPEN-Ver.11-13-2014 C c C ti C +31 C ea rip '71'moo y U I w rO^ -713 E ' G —a 0 `v . n C C o C CJ r O i Ow -0 Z =� Q C W . =o W G CI Oy zr n FBI Cci] G G=7 z 4 it Permit Number: 0 C _D T .0 0 L U c L e G v 0 Q C G T. Lc 0 O 0. Facility Equipment ID: Section 02 —Requested Action (Check applicable request boxes) Section 01 — Administrative Information General Permit GP07 Individual Permit Action Applies 0) J (n JLL a) (B O � c O O Z 1 C C C 0 U Source Name: L C C L G G' Section 25, T3N, R65W 0 Change company name ❑ ❑ Change process or equipment 1625 Broadway, Suite 2200 Change permit limit al O O co C CI E C. F c O. C y 6.1 ea a, n CC A 0) 'O u w L C w O 61 L V '0 CD G-ur C es •� C < "C 2 get a Y <-66 y C C C 0 C. c_ N C ' N O N co C) G b •0 C.) 6) P. N 0 U a) C a) a shaun.higgins@nblenergy.com E-mail Address: Fax Number: 303-228-4286 Addl. Info. & Notes: Section 03 — General Information days/week 52 C Normal Hours of Source Opera 4 O ' E R m U OV) C O .� G Q 0 C O bA C c c - o 0 4 Ca C7 Don't know Don't know Don't know Don't know Q z z zzz El El CI 0 < < < vs te1 c.0 71 43 0) 6) Q) 0 6) >- ❑ ❑ 0 V 0- 0 0 0 CC 72 an 0 E_ a :l E I) el m Q 8) Z C C is C O o G G • - 4 Q 0 00 al N L. N iz C•-• °3 0,. 0 y -C . C C) C a H >+ C 4 U L C o y. ID V7 0 0 R 'II z ,: 0 C O C G :: -0 0 V c' C. Op •C. 0 G 0 <-V. O O a) C 0 1.1 X m p Z o o y O� cc Ca ... C.I c o -0 of 4 O c •— 6) ,0) N C 0) V 2 C - O OL -- .) O Y C. L� C n w. A O ^ .:-. pi '.E - b .0 -,-U c y'- ; a) 2 C a n C O O 03 O. C. C-- 0cc v 0 0 0) o L- c .0 0. a) m > I c = O O - 7zo x O 0 to n Q ?- u ♦ ♦ A A .' C 0 0 'C 0 G W ,.., \ Z-.�. A - M C1 f' i V o P. c °J L d n. .�)u , c CC 13 ≥ CE �":., .Y t ri_Cn -W, L.) �, 'C sf.'r�cn a C -,:c O0 L C" Z e __ 0 . ';,- U a. d > 0 . L 0. '�'� - 0. 0 . . < al O) , .4 'n Cl) _ i J if'n. 3 N ' a L mw L E cc 0 0 0. E .c C 61 0 a U - y at o o— o c _ cn a) C > V > �� V O 6) E 3 ' CC o _ o u> 0 G - " L GO L +" C�) 0. 4 `" O 4 C C. C C (� C. ^" �' T. C a �..C. O LO :n. V _L •C C V d• a Q >> C V R L N C ,O Q 0¢ rn �. •fl L R d„',U co O U a R O O_ 4o' Q7 �' O 0 p C. L 0 r.. a v, - WC" O G7 V U n O - 0 V . C •n L O. C. Uc a o s`°. A U m o_ L]. U tom^C C L MO) V - O H & EAc..) < 'C' A Cl < vs www.colorado APEN forms ermilstatus Permit status: www.colorad v/cdahe/ozone (www.colorado Condensate (e.g, "rail tank cars," or "tank trucks") LL ou 0 4) C0. G C N P• C7 L W R z C E u ) CC <a cn wC.. L 2. C E N E C V J C. _ c y _ 4. :a 76 . 44 0) ca 1 b o- 0 CD H CD 4) O C 7- 3 C. • C. ,r. True Vapor Pressure: 0 C) • Q a N C C C 5 -77 s - FORM APCD-208 ingAPGN-Vera}-14-2014 (I ).docx FormAPCD-2011-I IydrocarbonLiquidL 1f. cln CJD C WGG' 2 F — to 11 C J V C C C C 0 V O C G L C C fn C C rip E -.ao E C zc E E j L 4- C :C C C C U CA 2 2 t LL! N 15 0 O -104.614370 40.201577 (Y) ,b z > 2 L' v E E f=. Z C C/2 CJ C R3 w 0 Z C C E .c o c 1 C) V C.) CJ 7 C C U C n C l` C Q o C U v C v U3 CA 5 VT Section 08 — Emissions Inventory Information O en G C) IJ dl p C 0 O C) N n ..s L C en 0 Condensate C O C II ti CC x C c0 cc O C) C C) N C C O C U C O C) PI to O C) EID C L. C C C C) C C C CJ C V C. aCi V CJ L CJ A Emission Factor Documentation attached (If using site specific emission factor) ai2 3 - CD'Nr AP -42 CDC Ne AP -42 AP -42 .) c r 23.66 L{ .tin 0.27 M I` n.7, E c �'E ..., ._ 5.43 34.62 7 J 10/ yy 1-- 1- vi :7 a m Actual Calendar Year Emissions5 9 � _ c C O a C O liinission Factor o1-i o o = C E a a .� T C Cl _ C ' (-I X 0 Q 4 - 6 x 75 Cr L o "n to O' f -3 f: C) m E J 7 'c C) U Control Efficiency (% Reduction) Identify in Section 07 E z 0 U a. ,V. C Control Device Description Primary Secondary 2.7 Pollutant DOA XON CO Benzene C) C v x CC i C C) V C V C T O CG` o QJ c C. C L., V y c C CC C, o C C C 7 C. 'C i C C CJ C O E o C st c w .F. G n es +" c1 /^CC u G L. O. v L C/7 4=. 2 — "C N O o o = C. C — ' Q E yy '0 L UHI '..1 _, / C. " '< 4r ` o C C =V ... >N = a) ', D C ql 40t. V) Air Permitting Supe C C) O) C C (C J .J r, T c 0 O L C '4 C-) C C 'O N O C h 4-, O C ff O � z ° (V C? C- T .C L C V C C) AIRS ID Number: 123-9E3A-TBD 15WE1451 Permit Number: Noble Midstream Services, LLC Company Name: W 0 U 0_ N T.) >, 0 0 U SEC 25 T3N R65W Plant Location: Phone Number: 720-587-2459 shaun.higgins@nblenergy.com E-mail Address: Controlled Kc-r_JsA Emissions Ibs/ ear V Uncontrolled ;k«r> <<1 Emissions Ibs/ ear Emission Factor Source AP-42/Liquid Analysis AP-42/Liquid Analysis AP-42/Liquid Analysis AP-42/Liquid Analysis Emission Factor (Include Units) , d iI x p r 5 qJ - y c_ 3 re r, .1 S 7� i.�J x -r U) 6 '{ 6 ,s..../ , T Control Equipment / Reduction (%) 95 U) O3 U) 0 Chemical Name Toluene Ethylbenzene Xylenes w C Cu C a) 0Q >, a E I— N N Chemical Abstract Service (CAS) Number cow. COT- OO CCS0 0 1. O 1330-20-7 T 0 .I' 5 9 Calendar Year for which Actual Data Applies: 0 csisi cV co m to 0 0 CL 0_ a) 0 N L 0 C J 0 a) 0 a) c 1�, Air Permitting Supervisor Shaun Higgins Title of Person Legally Authorized to Supply Data Name of Person Legally Authorized to Supply Data (Please print) Form Revision Date: April 14 2014 4r AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Crude Oil Stora Emission Source AIRS ID: [Leave blank unless APCD has already assigned a permit# & AIRS ID] LA 'ermit Number: C C C J C) C F. C. C- V c C C C C) F E. u 4) -C 07. 444 c E- 1-; 'acility Equipment ID: G 0 4) G O G a 4a 4) U O 0 4 c 0 CE U G C/) ection 01— Administrative Information U ® ❑ ❑ Change company name Change process or equipment •0 Transfer of ownership Change permit limit ti CO CO 6 �' C c U V U QU — zc Noble Midstream, LLC 4) m z 0 C C.) APEN Submittal for Permit Exempt/Grandfathered source N 0 co C) -C. U N APEN Submittal for update only (Please note blank APEN's will not be accepted) tA O �z Shaun Higgins 303-228-4286 4) E z ection 03 — General Information sources, the projected startup date is: For new or reconstructed e z z z T Normal Hours of Source Operation: ®❑® n v n 4) 4) ❑®❑ Are Flash Emissions anticipated at these tanks Lri C.) 0. E C 0 V) y Storage of Oil or Condensate 0 C. C C C 4) C. .C c 4) C G 0. ')0 ll n II '� ^ N CJ E ¢. ', C O. c L .+ c z 4 • a• C: e- E o Q•bmA y +t. C r. y L aII o J e( ?) 0 7A = J a CL 0 .0 0• = u a`- m n o F O r L a acil 0.. •] i _ N. O L a. o C L ^ -� .- II. •� a 0 C v cS a o Q •y E . O C G 'n a O L >, a) N. CA.� N y ..rl _� y. 0 O T 4=, ': i C W s i N L L N c..0 o 8 0 y ° �....aUm 6o O) c> 0 0 cE •c • L. '7' Ca 61 o C; L O o ES' L c_ 0 0 0.p c u2 .- U m C) Oo c ,o .� .4) 4) y u 4 y C) o A C? a) c o •- y o o 4) _ o o o c GU. 4Oi U W d> 2 v a Q v W L U W d A r� v 4) O C C Er G C ction 04 — St O O O O 4) C Actual While Controls Operational: C. C C a. bA O RVP of Sales Oil n ef' ❑ External Floating Roof: C on C a LL 4 E a C C C 4) x En C y 5J e Of First Production S. cd .0 O Z G " C � 0) 3 7 u O G O A A nrkl I AM/ a__ C. O L Emission Source AIRS ID: 44.1 Permit Number: Section 06 —Stack (Source, if no combustion) Location (Datum & either Lat/Long or UTM) ci C d L 0 ci O Cip tin ci v C) z -104.614370 N n S C 7 6. U.. ci V C > L U .0 • > ❑ of stack outlet (check one): Opening Shape & Size (check one): N ection 07 — Control Device Information 7 CO C CC L CL C Cil al L c C r.. 7 7.1 D O y c E o Ua Make/Model 0 C) y) C F c 0 c O N N N C ..G H ci bD C aJ c •• o 7 U L n T L U O y L. C. v Requested VOC & HAP Control Efficiency: ' C 7 :Q C. a] C) CA n 2 G O 7C.- .) C C n J C > O � C > n T E I c c C 4447 f c c a) ¢U O i Cq C. C, N CA C C Wi ci C 4.3 N E G P O P-9 m c. v a) 4 = C m. TJ C 6 0 0 .- C } C U U > 3 C p .J r CV EG I., LC. Q a C C G U) . O b a = �. C C .. v r C: ^ _ , CC a 9• • 0 O E O .L".� O h 1'. ci i cS 5 O L. c C 67 4.4 0.4 c 0 0 u N t9 ci a ci 0 = 0.1 e F.; L R a R a L s J G TANKS 4.0.9d II Liquid Analysis Liquid Analysis Liquid Analysis II Liquid Analysis Liquid Analysis Liquid Analysis Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above. �I c r f C 0. 7 'l. so c — Uncontrolled Ton -/ co N Q ii)o • g m 4 en sr •o 0 ev N ..e, Actual Calendar Year Emission2 Controlled (Tons/Year) r OI C 1 Emission Factor C C A C C C C L L. L C C L C C L .C Uncontrolled Basis T J l - Lo - Pollutant x, O z VOC CO " m c a, H ci C e, >, x O a t s 2,2,4-Trimethylpentane O L t. O L U ci L ci T 444. O e x ci in ai •� L c- 41 Ca) 4,2 L CU CC.O c .- -c C n - aJ E •r C C u zg C C a aE a c m E u •0 C +C- 9 .5 C .d y C d c t O r' akC a .0 _``•.. 7 G L ^J 'l. C y J 7 20. c E Z8 C C C- CD y I ;i N :9 7i .C aJ F.4- L n ci 11-4 Z C a CC,- J C 3 o Z S LU ci C C Q 'D O C 2 Q 7 _T CD 0 G U 9 L C. T v = c C O C- C •n uids analysis, RVP & API anal C 0 0 j C: ti N x 43 0 A P Form- APCtI_11(1-Co IdeTankAPFN I(1(11< doe Pnoe ? of C ( CJ de Oil Stora i.+ E i.1 !+I .4 ir. 4.4 Q "• z O z z 0 c z O C C C C U Q C C C ^CJ C.) C C C C O C F c. C cr C C a U b C C V L ti G Ci7 U U U C U 1.4 7-1 C 1) 73 L C G C 173 CSl C o C U U 0 A P F,.,,,,_ A PC _r tri.TrAvIL. A P KI I (VW A,,,. Emission Source AIRS ID: s APCD has already assigned a permit # & AIRS ID] [Leave blank u 'ermit Number: your organization.] [Provide Facility Equipment ID to identify how this equipment is referenced witl 7acility Equipment ID: U P0 G 0' N 0 U iection 01 — Administrative Information e u 4) O .0 aa c c, , J V z C7 0 z E z t1.0 v v o Q z u C L L Y 4)) v 3 7 6! 67 C) El CIO Noble Midstream, LLC Change company name 0) 0 Transfer of ownership ❑ ❑ Change permit limit ❑ ❑ C) 0 C U 4) U w APEN Submittal for Permit Exempt/Grandfathered source APEN Submittal for update only (Please note blank APEN's will not be accepted) ❑ ❑ CO E a U 4) 0 LTA N 1625 Broadway, Suite 2200 Mailing Address 720-587-2459 Phone Number: erson To Contact: 303-228-4286 U z CO iection 03 — General Information C C r 00 p 0 C 1) C C ll 0 C Of J 3 > ZZZ z 1Z®® 4) y ) ) >- >- i- T y •c E T o .0 0 Normal Hours of Source Operation: DEC Are Flash Emissions anticipated at these tanks U C C LL c W C) 4) 40 z N L � c C ❑ o q c 7 cam' 80 H z U R Al Lo G•a 2 m C n O • Z. >- •- 0 E c ti C , m •C O LO. C r ^ O C 0 �c E o V U 2 O .l 1� C? C C U ❑ v r v � c i Al 0- c.74 00 C �n CO 0 4) CO 0 Storage of Oil or Condensate 0 C 4) 40 0 c C C C C 3) 0 r 4) C 1) m J C C 5 v E 2 U C cc L •r.+ Z W E .� c 1 v, • C C. on vNi z c. �. R Q 'vi r W s G y m s s_ Z GL -2y O U > s � C 72 6J = Q P. x R'_ L V m a E.>s u OC O u �. r+- Q rr C L O = 'y7 L C :d .„ d OCA — • n )6. V, L C c '� O CO C U ' a Lo O .Len n E c- "..:0 A', •Rwcoy, 6.e �� 0— a _� '- CO o. 8�c O c, A d > 0 F_ +- C U C 0 d m L L (n o f ^^ C= c o o. a Ern ^U R O p .O .¢ 0 63 .=.. Z a) y L. L' CZ' Q U 6i O C --76 X CC-� L� 0._UO > 0 0 U m r R C O CYO Cn C- C 'Sr C' E U W Q ° 5 3 d,ic;i L U a.i Q G Information iection 04 — Storaee Tank r- Requested Permit Li o o ea a' cia 0 O � 7.11 C C U a External Floating Root: 0 C 00 C .O CO 8) 37 ❑ C 0 4) x rank Design: d 00 L A r. N o E. C O 0. L 4) CO Y 55 0.0 O L > L C) 0- i •0 Ca i C. C z EI Name of Well AP Form-APCD-2IO-CrudeTankAPFN 1000 doe Pane 1 of c i CA e. de Oil Stora N Emission Source AIRS ID: I Permit Number: at/Long or UTM) C) C) u C C C U 0 C) L C u CS b • C C U C) 7 ots V r. CC C) C C .n U 23 e C M 00 z S F 5 — Stack Jul C U .52 3 U L' Q F G., H C ti Ca ytip U O V O • ❑ T > C.~.) ❑ C m S S CA C y C CC) 2 a=. 0 U crs C u n C ❑' CJ J CO. 7 U 3 c VOC & HAP Control Efficiency: O •on 3 C Pilot burner Constant pilot ligl v Describe Any Ot G U y V C C) v V L ti CJ v 4 J J 72. O g C _ I oc. j _ L C C E Cn 0 C C Ca L CJ C C) 0 CS Make/Model: 7 O Ca O C Li U 0 > t. C) c CC) m C CC. C L O C Ca d loop systen U j Ca CD .71 7 uo C C C CC C) C +io L CJ tr. C C` n > m y C)CID Ca oration Technolo ection 08 - Gas/Li C) is the pressu tn Y C C) CO_ o. C) Ca C' c 3 C) C C) 0, n C) CI p m 1- C) C) C) L Ur C) r s C) C- C C C C 4.. C C C C C C W C C C6 Ci GCr C a aC.. C C) G Ci C 4,1 C-. 0 C U C, N 0 rst C, C') Ca C 0 C C C) c. CC 3 u u a • • Emission Factor Data Source TANKS 4.0,9d Liquid Analysis Liquid Analysis Liquid Analysis Liquid Analysis Liquid Analysis Liquid Analysis Please use the APCD Non -Criteria Reportable Air Pollutant Addendutn form to report pollutants not listed above. } v J cx C) CI Controlled (Tons/Year) „.5`I O • C. Q CO / C Ci C t P H 76 tr m m QQ4QQ4 d: O; b Actual Calendar Year Emission2 Controlled (Tons/Year) uUncontrolled (Tons/Year) Emission Factor Units 1. L .C L L .e- A L .C A- L L Uncontrolled Basis C7 _� _X - Pollutant NOx VOC O o .- y C) Ethylbenzene Xylenes — X C C o i .c V C) ctj L C C G R. C i 4 5 d c01 • 6) • C m .ao u c C. C v) S C — C s = 3 a ✓ s L • C) ci r=j) C Sd • E E • CC. ,C C c fl C CC y L eta C. L C MNJ C _L 7. .• a u CC C C C r- = ▪ at CS. — C s L C) a) C) CJ ^ C) 9.1 s .. 06. C O trz CC U L C) U C U C O C C Ca as Shaun Hieeins U 4 zed Person U c C) U o G y C. c � CI C. C) C Z a. C N' L C� O C C i = c ti T C G C > y T C O' c C) .Ca C) Ca U C v L .D • N C) C' 9 -S7t- -75 Ca 0 G C) C C) G C q a C C) F C) O •n F G LI) C C z C r U N C. Li G u.. rt r+~ C Cam! C) Ca Hello