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Address Info: 1150 O Street, P.O. Box 758, Greeley, CO 80632 | Phone:
(970) 400-4225
| Fax: (970) 336-7233 | Email:
egesick@weld.gov
| Official: Esther Gesick -
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20183403.tiff
414, CDPHE COLORADO co ;0 Department of Public. Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150 0 PO Box 758 RECEIVED Greeley, CO 80632 OCT 1 9 2018 October 16, 2018 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On October 18, 2018, the Air Pollution Control Division will begin a 30-day public notice period for Tallgrass Terminals, LLC - Buckingham Terminal. 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 I (� c John W. Hickenlooper, Governor Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer r'Ub��c Ra.view cc' PLCTP), HLC3T) Po(ERIC( ll3R-,/c,'S,) 2018-3403 10/ 1/14?" I cDPHE Air Pollution Control Division Notice of a Proposed Project or Activity Warranting Public CO Comment Website Title: Tallgrass Terminals, LLC - Buckingham Terminal - Weld County Notice Period Begins: October 18, 2018 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: Tallgrass Terminals, LLC Facility: Buckingham Terminal Oil storage and pipeline injection facility SW Section 34, T8N, R59W Weld County The proposed project or activity is as follows: Applicant proposes to increase permitted throughput for existing tanks and add two (2) tanks up to 250,000 bbl in capacity. 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 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 14WE1593 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: Bradley Eades Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us • 1I Colorado Air Permitting Project PRELIMINARY ANALYSIS-PROJECT SUMMARY Project Details • Review Engineer: fad[ey3a fesr Package#: <3 g ) 31 ;3;; Received Date: x4/16/2018 E. Review Start Date: v//ioie. i Section 01-Facility Information Company Name: TallgrassTern2nals,Lt.C„,a;;,:,i,;.; quadrant Section Township Range County AIRS ID: 123 i4 N` yq3 , ,`�j�1� 34 8N"" 59W Plant AIRS ID: �,�§D„ "' d33 1 d,� fi13: € Facility Name: �gt?,aaitilr5ine fEkietE.f_.: , _.. ,: _ .. .,.s ,m .„';',E".., �,�--_ Physical Address/Location: SW quadrant of Section 34,Township 8N,Range 59WW County: 'Weld County I Type of Facility: , Il5td`¢a a Pipetlneiejection to'' ' v 7' What industry segment?Qai&fdetureasip #14 O Is this facility located in a NAAQS non-attainment area? _ -- Yes>'' If yes,for what pollutant? ❑ Carbon Monoxide(CO) fl Particulate Matter(PM) El Ozone(N0x @ V0C) Section 02-Emissions Units In Permit Application Emissions Self Cert • Engineering AIRS Point if Emissions Source Type Equipment Name Permit# Issuance# Action Control? Required? Remarks 10 ii,i1 33331 /, . . e , rt:rmTtiti 001 Crudeott Ea l T T-4021 4022,4023 Yes 14W51593 4 Yes, Mocftficatton IFR Tanks / is �/y" >r — No Acton n iA% Osa ,.Wr..'gatla: np€raaent ea _ .,_ Fugitives it- iELo 14VVE1593 4 .No.., 3,,,;ift&ii stsd&::: ,r3.3nr s X13 004 ....... Crud,CrgrIkpitigilatft11 T 4151 4152,4143;4154 Yes 14WE1593 3 -; ,,.4 Yes Moifl cattoru EFRTanks , 101,11V-- -- jj� l etlrli,::: rRTCks inn 005 i3ki T-4251,T-4252 t & 14W150 .4 - Yes. ISSG t1Ce an Section 03-Description of Project i TaOgrass:Terminals,LLC{tallgrass)submitted'thi 3}�pl d'f''.modifya factlltY-widepermit'at an:existtngtrUf liana d etorage antipiperineinjeclxon fak')tt jgya .'t th,fr s :g ozo"Henan-attainment area;of weld County Witlftha5`moth cation.theappliCantisregU,eStingElOakidttlon,iiftw0{2)25;000barrei,internalfl otio&£Qoft` i 5,,4 .. '001 addition of two(2)150 00 ., ek 13 3)3 v ; `' .-, A31�barrel externalfloaYngrartftanksto.Pomt004 andtwd(���3ree�Lexternal:flbatingroofFankvassetsnpto�`�Oj000obl�capadrty�T3etan scuitteontinue . 3� 1v 3 .: � � ��� 33 3Y1b>1 to store crude oil and[atlt3"ON10fj33te W3tfttlse addition of these tdit Talig�assitaeg₹r esting increased throughput llmits.to 45MN13 ha Jrt}gtf+5p3Polrit 001 a€d 124-1MM barrels for,,I Pornt004 previousFy15lylf &62iiiMLrespectively)Tallgr�ass.ls5,`e (Estuig,a�hmltef62050,000bblfortherrewtanksassigned:Point'00x_Inadditcnn_Taligra;5.€srequestmgtin,D,. cli2tt e facilrty r Ae from"fluckuagliarsa Stdtl0 ll,44111 uCkinghm,:ftrntir3at and toAsjote the equ ipmail lOs t0 iitatcla their internal inventory Iqs..3 t;"''�3r;11" `1 it - ,3 1 titi.y,: 131 1J 33 .„ 3 - t3 __ b 311 II'3.k � - p '3A4'4"'"'" ........................................ . 1.33.'r1 �, 1�3 t.'.�` - L` '3,' g Thisfactttty reces ieSsta a d cortdesisatelcrude Oi•l vie truckunlooding and prp41gr irsd*om production faciltids°Uquidsafetranspo�rtpi fr--mthekacrhryvr s H eit segLjE dgw stream fatilitass / - 1I31 __333 3 � EgidtesEisiss--E-- T . m1 6.f .f333ke °� a3 a,g, kg. fa - stw �g _ 3 ,",-_.."..,-....,- G,fM..��fE ..._„„,, .'sk ' .w.a.:,..,,.. -...... ,ve..:.u'`'�k..n`.-.,x�` ..6>,„�u3.G ..:_..__„ _ ..- ....._.,3-'_.a€ 1₹ba'�dx ;/.ems% a Section 04-Public Comment Requirements Is Public Comment Required? Se - ' Yes ui� y If yes,why? t a'E"eEl₹ e Y rio Nvn-AttaininehkEA)'ea °Rs,, Section 05-Ambient Air Impact Analysis Requirement: Was a quantitative modeling analysis required? 'lYo ENN If yes,for what pollutants? w 3lil i:::11 00P1195 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? v Yes Is this stationary source a synthetic minor? - ido��,e✓''" If yes,indicate programs and which pollutants: SO2 NOx CO VOC PM2.5 PM10 TSP HAPs Prevention of Significant Deterioration(PSD) — — — - iii ❑ Title V Operating Permits(OP) Non-Attainment New Source Review(NANSR) Is this stationary source a major source? l4i�`�,, If yes,explain what programs and which pollutants her 5O2 NOx CO VOC PM2.5 PM10 TSP HAPs Prevention of Significant Deterioration(PSD) — - - �[ - ❑ ❑ Title V Operating Permits(OP) IL�JT Non-Attainment New Source Review(NANSR) Condensate Storage Tank(s)Emissions Inventory Section 01-Adminstrative Information (Facility AIRs ID: 123 yp38County Plant Point Section 02-Equipment Description Details - - Detailed Emiss n Unit 4� - ,? r r S ree 325 0fi 6atte€a ternetfloatmg rod"Pmnd nsatH toragevesseis-` l DescriPtioo: �� sc��'- e,. _ .e. .„„ ! ,.., ;' _ - Emission Cont of Device EmtsswnsaredontrojleduPi gpteatrtprnat4loaGrrgroo€. = a`+ Description; Requested Overall VOC&HAP Control 't The internal floating roof is considered an integrated control device.Please see Efficiency 56: - p)//55 (5)5t,,'..Section 08-Technical Analysis Notes section for additional information. Section 03-Processing Rate Information for Emissions Estimates Primary Emissions-Storage Tank(s) - 5 Actual Condensate Throughput= O;.B rrels(bbl)per year Actual Condensate Throughput While Emissions Controls Operating= �ll3�(�:r,��n fl Barcels.(hhl)per year U RequestedPermitmitThroughput= 41.0.,..8"411„EBarrels(bbl)per year - Potential to Emit(PTE)Condensate Throughput #S,}100 0Q0'',Barrels(bbl)per year 3821917.808 Secondary Emissions-Combustion Device "'This facilitydoes not utilize a combustion device to control emissions. _Heat content of waste gas= Btu/scf Volume of waste gas emitted per BBL.of liquids produced— Actuaiheat content ofwaste gas routed to combustion device= 0 MMBTU per year Request heat content of waste gas routed to combustion device= 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? q\^ pmcnecR1 Soberna[Ftoa}rap,R mf'EY(Mssronst3uimg,Flgrmal i2perattans r "',-_ Total tank losses from an external floating roof during normal operation included rim seal losses(L5),withdrawal losses(L,0),and deck fitting losses)Lr)and deck seam losses(L0).The operator calculated these emissions using EPA TANKs simulation software.This software utilizes equations from AP-42 to calculate the internal floating roof emissions during normal operations.The emissions resulting from the simulation are as follow(they do not differ from the emissions/vessel permitted with issuance 2): Parameters Value Units Source Annual Throughput(Q) ,SSf#(0(kld�,.,aF bbl/year Operator Provided=Veve lrcughput for one tank) Rim Seal Losses(16) 295.549329 lbs/year i _ EPA Tanks Withdrawal Losses(Iwo) 9266.96 Ihs/year g' EPA Tanks • Deck fitting losses(Le) -,11.,W IN lbs/year 'EPATanks Deck Seam Losses(Lp) ps' p) �j` lb/year IC,Is.D fara.elned cinch Total Losses 10378.01 lb/year EPA Tanks Total Number of Vessels 3 Standing Losses: 1111.05 lb/y: Total Emissions: Pollutant Weight% lbs/year Source VOC a," j-4".4.1,5-,-/f, 31134.03 Benzene -i}. 25%. y^: 72.2309490 Mas58alence` i •Toluene 5006351 197.0784099 Mass,L Balance Ethylbenzene J, 000157= 51.9938301 Mass Ealancw Xylenes 00051,, - 158.783553 j'IaRBalancm n-Hexane DD16,e�, ;?� 498.14448 ,MasSltlanceT) 2,2,4-TM P 0.00918 192.4083054 Mass Bolancz,_ • 2 of 25 K:\PA\2014\14W E1593.CP4.xlsm Condensate Storage Tank(s)Emissions Inventory Process 0258000 Landing Emission Ca(culationsfor Internal Floating Roof with Full Liquid Heel Parameters Value Units Source AP-42 Chapter Equation 1-24(based an daily average ambient temperature-see True Vapor Pressure(P) 5.120542911 psia note 3 for Equator 23 in AP-2 Chapter 7) Average Temperature of vaporandliquidbelow 509.92 °R AP-42Chapter?Equating 1-27 floating roof(T=TM) Ideal Gas Constant('R') ifi731 1 (psl'fta)/(Ib Ideal Gas LawConstant mon) Number of days tank -- stands idle with floating 1 days - Engineer Estimate roof landed Ind) - Stock Vapor Molecular 53.61 Ih/Ih-mol AP-42Cbapter 7 Equation 1-22(Estimated by TankESP_d) weight,(M,) Saturation Factor(S) 0.6 - `,y ` - AP-42 Table 7.1-17-Value for full liquid.heel Effective Height of stock 0.17 ft - Operator estimated.value Liquid Roof Leg Height(low leg 3 553•- ft - Operator estimated value setting) Height of vapor space 3.163 ft AP-42 Chapter 7 Equation 1-15(no roof outage so fituoD) under floating roof(h,) TankDiameter(D) i 60 ft Operatorprovidedvalue Eailymaximumambient 523.91.. 'R AP-42 Table7,1-7-Average value for Denver,CO temperature(T„) Daily minimum ambient - -' 495.87: °R AP-42 Table 7,1-7-Average valuefor Denver,CO temperature(T„) Daily Total Insulation 1568 Btu/ft°'day AP-42Table 7,1-7 Average value for Denver,CO Factor(I) Tank paint solar AP-42 Table 7-16-While 0.17 -Past s good'condition absorptance(a) Atmospheric pressure(P,) 12,12 psia Ambient pressure for Denver,CO Reid Vapor Pressure 8.57 psia Engineer Estimate Vaporpressurefunction , 0.736400611 ' AP•4Z Ehapter7 Equation b3 (P„) N Volume of Vapor Space 8943.171807 ft3 AP-42 Chapter7 Equation 1-3 (V,) Vented Vapor Saturation 053809650 AP-42 Chapter 7 Equation 1-26 Factor(I(,) - Vapor Pressure Constant B -- - - 4629.181 From linear Regression of TVP at 10degTinterValsvia ASTM D6377 for Crude Oil Stocks(B) Vapor Pressure Constant A 1071151 -. "� From linear Regression of TVP at lO deg T intervals viaA5TM fl63?7 for Crude Oil Stocks(A) 1- - Daily Ambient 281 °R AP-42 Chapter?Equation 1-12 Temperature Range(AT0) Daily Vapor Temperature 2769568 °R AP-42Chapter7 Equation 1-8 Range(AT,) Liquid Bulk Temp(TO 509.94 'R AP-42 Chapter?Equation 1-20 Duly Average Liquid 512037024 'R - AP-42 Chapter 7 Equation 1-26 Surface Temp(Tu,) Vapor Pressure at Daily Max Liquid Surface 6.531844077 psia AP-42 Chapter 7 Equation 1,24 Temperature(P„,) Vapor Pressure at Daily Min Liquid Surface 3.959180237 psia AP-42 Chapter 7 Equation 1-24 Temperature(P„,) - - - Daily Vapor Pressure 2.57266384 psia AP-42 Chapter?Equation 1.9 Range(AN) VaporSpaceExpansiee ��� 0.23467109 A AP-42 Chapter?Equation 1,20 Factor(Ks) Event Standing Losses 56.6540438 lbs AP'42Chapter7-Egpation 2.16 w/out Wind - EventhilingLossesw/out 269.1921559 lbs AP-42 Chapter 7 Equation 226 Wind Event Standing Losses lb/roof landing - (1-q) 56.6540438 AF-42 Chapter?Equation 2-19 • event Event Filling Losses(1-n) 269.1921559 Ih/root landing AP-42 C 7 event Chapter Equation 227 Total Landing Lass lb/roof landing - -_ - 1-n+1-q) 325.8461997 AP-42 Chapter?Equation 2-10 Emissions(Lv= event Total Number of Roof Landing events 6 Total Emissions: Pollutant Weight% lbs/year Source VOC 1955.077198 AP-42 Benzene 0,00232 4.535779099 Mass Balance Toluene 0,00633.... 12.37563866 ':Mass Balance, Ethylbenzene 0,00167 - 3.264978921 Mass Balance Xylenes ❑0051 . 9.97089371 Mass Balance n-Hexane 0,016' 31.28123517 Mass Balance 2,2,4-TMP 0.0061.0 12.08237708 Mass Balance 3 of 25 K:\PA\2014\14WE1593.CP4.xlsm Condensate Storage Tank(s)Emissions Inventory 7ankESP d calculates the total losses from the floating roof tank during cleaning operations.The equations governing the emissions during this process are established in API Technical Reference 2568.The operator grouped this process into five stages which will be described and calculated below: Parameters Value Units Source Stage 1:Standing Idle Tank TSP d using AF 47 Chapter?Equation 2-19(Assumed 2 days standing idle Losses-Full liquid heel of 1E0.22 Ibs until cleantng curnn end, crude oil d Stage 2:Initial Vapor Purge-Full liquid heel of 435.3 Ibs dank ESP d us ng=4.042 Ccapter.,Edo,t u:^2-27 crude oil Stage 3:Daily Vapor Purge -Full Liquid Heel of crude 1488.50- - Ibs rank,ESP_d using API TR 2568 Equation 19(Max limit) oil x 3 since 3 days of vapor purge(3 days of stage 3) Stage 3 Part 1:Crude Oil Sludge Removal-Full 4793,.,. Ibs Tank ESP_ii using API IR 2569 Equatiicc 19 liquid heel with met. forced ventilation x 3 since 3 days of forced ventilation with sludge removal Stage 4:Daily Vapor Purge 7 08 Ibs Tank tSP d us ng.AP-42 Charter 7 al ust,O11 2-26 (Diesel)-Full Liquid Heel x2 since 2 days of vapor purge after diluent wash Stage 4:Sludge Removal of Diesel with cont.forced 95 Ibs l nk cSF cg AP.TO 2511 LG,:at o`�19 ventilation - 03 since 3 days of forced ventilation with diluent wash Stage5:Refilling Losses 12,56 lbs Tank ESP_d-ilsi ac AP'7 Chapter/Eq at oa 2-26(Assume Drain-d0 tank.,_,tank (Crude Oil) _ ts earl Total Losses 2.-02.04 lb/cleaning Total Number ofTank Cleaning Events 1 Total Emissions: Pollutant Weight% lbs/year Source VOC — 2840.44 AP 42 Benzene 0.00232 6.5898208 Mass Balance Toluene 000533 17.9799852 Mass Balance Ethylbenzene 0.00167 4.7435348 Mass Balance Xylenes 0.0051 14.486244 Mass Balance n-Hexane: 0'01$ 45.44704 Mass Balance 2,2,4-TMP {f 17.5539192 Mans Balance 4 of 25 _ K:\PA\2014\14WE1593.CP4.xlsm Condensate Storage Tank(s)Emissions Inventory ,; Process0i.External Ffaating RoofEtnf6eian;ENtnifgdNarenatO ai'i E3s �/�;, 5• .. �" ', '' Condensate Storage Tanks Control Device Uncontrolled E.F. Controlled E.F. Uncontrolled E.F. Uncontrolled Pollutant (Ibs/bbl (Ibs/bbl (Ibs/MMBtu E.F.(Ibs/bhl Emissions Factor Source Citation Condensate Condensate waste heat Condensate Throughput) Throughput) combusted) Throughput) Throughput) h� PM10 ��O�'c7.s�:.�.'N �� 00000 ✓ � L'.v.�i PM25 .. tit o� 'Hf31'3Y --,1133 , 0.0000 �/ _ s/ NOx \�"`.`�a..""� d ` ;;','3--,'-',33-a'.11-,::';'.5„,:,.. . `•0.0000 'A5 S _ „_ VOC ;g 050E 04 6.919E 04 :T, '�Yk �'3, �\�"\ $jtG6fi�,,e Tajijt$P°t£ Zr}¢(t 8 CO . \\\\\\\���; c `\.Z�y, 0 0000 3 f Beeaen t'';' 3,605E-06- 1605E 06 : ,, � - '�' ' Tolue •' .4380E 06 4.300E O6 � T Ethylbenz ne 34155E-06 1.155EO6 � �`tt,,I,�rO4, $lie 0 o atrkt-t+dE tlhs, ,,,,atl' „,,,,thr XYlen 1U3 529E 06 3.529E 06 y c�"l�n stWisa Site 6perefiE,'ankk�'.,s v n-Hex 3a-"'- 11529E-05'? 1.107E 05 r, .€ a. `4„ ;,. s 224 TMP 4.276E-06 4.276E-06 a \ v'C elf c . '''''.7.'r ^�-, 13r=` Process 02:Roofiandi0Emission Cal 6Cionsfnr0cternal Planting lYoofwith..., Condensate Storage Tanks Control Device Uncontrolled E.F. Uncontrolled Pollutant Uncontro0ed E.F. Controlled E.F. (Ibs/MMBtu E.F.(Ihs/bbl Emissions Factor Source Citation (Ibs/roof landing (Ibs/roof landing waste heat Condensate event) vent) ombusted) Throughput) PM10 �\v7t O�� :,y 0 0000 PM25 ��� �����,��- 00000 `-- '�'� 900 a`'`te"\ \o &v 0 0060��� VOC 325846 325 846 \� M:'�,v�rk.= 1EXt _ ng Roo jatd - 'fi co �l����.�� �� , 0 0000 �� Benzene 311I3)11f12 750.- 0756-'`.y`':S`"� 3- � Iawe 2063 _ _ 2.063 'mz' � s st Et Benzene 12144 0.544 ` z,1 -.4•L�CEta' i- "�� .... .__._._...._......��\��.`��..$ Pt" ,�f4a#e�Roof'Ha©f iandrngs �` Xvlene 1662'- 1.662 * _.® ` n;'Q-+FLC[mgt 7'ExternaTFtaahng Roaf itarsf Laru7t n-Hexane 0'216642' 214' - 5.214 .,\‘‘'‘'''41,1%.. .,-' \',tg.42fh60tsc?Extu[r54)Ff4oU6g Raaf 224 TMP ;2.014 2.014 ,. , SAP.4Zih$p[�t`}"h' aroattFRfatYktg loot<'�i41T, a� Pr9cess03:Tank Cleaning. ,, Condensate Storage Tanks Control Device Uncontrolled E.F. Uncontrolled Pollutant Uncontrolled E.F. Controlled E.F. [Ibs/MMBtu E.F.(Ibs/bbl Emissions Factor Source Citation (Ibs/cleaning (Ibs/cleaning waste heat Condensate event) event) ombusted) Throughput) PM10 \\\ \\\` S 00000 / // � / PM2 5 <:'''''''''''''''0::'*:'''\� 0 0000 Nox �� : 0 0000 5 e - j VOC 2840.44o.:s- 2140.440 � \& �`�"�`"" PI TR 2,566(21108(W/47.4212h6006i7 ,. . co Benzene 5'55°' 6.550 ink 't\nom` - .•"oTit` Os, Toluene 17.008 _ 17.980 ��, �,i ' e �ry•O Ethylbe 4.544 - - 4.744 ::\ q1 tk*ll + 'f't,:,ch, ; Xyle z 14468 4- 14.486 \‘'N `\ A 'C(t25B§(Z2/0)Yt/AE54ZCha5taT7 n-Hexne °31 145447 3 3'i 45.447 \ \�`\.., a �Apl'atzi68{5.IJfs7)w/�,Y.dxchaPtee7 224 IMP 17.554...':'.,,` 17.554 1 A ,Et,25"u8{iYf�;;WP�'G",,,,, /r,,, 5 of 25 K:\PA\2014\14W E3593.CP4.xlsm Condensate Storage Tank(s)Emissions Inventory Section 05 Emissions Inventory vex ,i,,,,, , Prosc�O.$ k;.....'.Efoatiiig,Raaf£mrssions OurnglVarsaal'S3petatkds;,`yy /e,,,,, ,. 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 PM2.5 0.0 0.0 0.0 ...- __ NOx 0.0 0.0 0.0 .'..3 VOC 15.567 15.567 15.567 1,000 CO 0.0 0.0 0.0 •^, Potential Potential to Emit Requested Permit Limits Requested Emissions Hazardous Air Pollutants- Uncontrolled Uncontrolled . Controlled ... Uncontrolled Controlled (tons/year) (tons/year) (tons/year) (lbs/year) (lbs/year) Benzene 3.6E-02 3.6E-02 3.6E-02 _ 72.23 72.23 Toluene 9.9E-02 9.9E-02- 9.9E-02 3-0.0,1, _ -- 197.08 197.08 Ethylbenzene 2.6E-02 2.6E-02 2.6E-02 ,... 51.99 51.99 Xylene 7.9E-02 7.9E-02 7.9E-02 :.7E,00 .+ 158.78 158.78 ` n-Hexane 2.5E-01 2.5E-01 2.5E-01 [:060- __ 498.14 498.14 . 224 TMP 9.6E-02 9.6E-02 9.6E-02 0.(Pk,LT, .. 192.41 192.41 -';Process 02:Roof0andmoEmiss©n•Catcufatiods4an£sternaEFlaettng Roof with Full-3quid Heel Potential to Emit Requested Permit Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled (tons/year) (tons/year) (tons/year) PM10 0.0 0.0 0.0 PM2.5 0.0 0.0 0.0 ... NOx 0.0 0.0 0.0 _ VOC 0.978 0.978 0.978 ,_ .. ` CO 0.0 0.0 0.0 u.0 . Potential to Emit Requested Permit Limits _ Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled (tons/year) (tons/year) (tons/year) (lbs/year) (lbs/year) Benzene 2.3E-03- 2.3E-03 2.3E-03 4.5E+00 • 4.5E+00 Toluene 6.2E-03 6.2E-03 6.2E-03 .. 1.2E+01 1.2E+01 Ethylbenzene 1.6E-03 1.6E-03 1.6E-03 .. 3.3E+00 -3.3E+00 Xylene 5.0E-03 5.0E-03 5.0E-03 1.0E+01 1.0E+01 n-Hexane 1.6E-02 1.6E-02 1.6E-02 ,-3 3.1E+01 3.1E+01 224 TMP 6.0E-03 6.0E-03 6.0E-03 1.2E+01 1.2E+01 fy;',;,Pm esscO3'.`�_Tank.C 4a-,An "`: Potential to Emit Requested Permit Limits _ - ..._ - Criteria Pollutants Uncontrolled Uncontrolled Controlled ,'r (tons/year) (tons/year) (tans/year) - PM10 0.0 - 0.0 0.0 ...r PM2.5 U.S 0.0 0.0 0.0 - NOx 0.0 0.0 0.0 0.0 VOC 1.420 1.420 1.420 :',(?n0 CO 0.0 0.0 0.0 Potential to Emit Requested Permit Limits ,,a u-'t'*-noun Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled .-- tso.tsu _,r.rro.lnd Uncontrolled Controlled (tons/year) (tons/year) - (tons/year) (lbs/year) (lbs/year) - Benzene 3.3E-03 3.3E-03 3.3E-03 --x;+d'.i 0,-_.5- 6.6E+00 6.6E+00 Toluene 9.0E-03 9.0E-03 9.0E-03 ..__-_., 1.8E+01 1.8E+01 Ethylbenzene 2.4E-03 2.4E-03 2.4E-03- 00 5U 4.7E+00 4.7E+00 Xylene 7.2E-03 7.2E-03 7.2E-03 Tt-,X+ 1.4E+01 1.4E+01 n-Hexane 2.3E-02 2.3E-02 2.3E-02 _. .- -..L-. 4.5E+01 4.5E+01 224 TMP 8.8E-03 8.8E-03 8.8E-03 _.. 1.8E+01 1.8E+01 ..., .lat-t#al Emissionsfrom'leReniat'Rlaat7ng Roof Tank - Potential to Emit Requested Permit Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled (tons/year) (tons/year) (tons/year) PM10 0.0 0.0 0.0 PM2.5 0.0 0.0 0.5 v NOx 0.0 0.0 0.0 ._- VOC 17.965 17.965 17.965 CO 0.0 0.0 0.0 Potential to.Emit Requested Permit Limits , ..- Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled ._ Uncontrolled Controlled (tons/year) (tons/year) (tons/year) .. (lbs/year) (lbs/year) Benzene 4.2E-02 4.2E-02 4.2E-02 -.0,...._ -. 8.3E+01 8.3E+01 Toluene 1.1E-01 1.1E-01 1.1E-01 0..tlil 0 ....- -. 2.3E+02 2.3E+02 Ethylbenzene 3.0E-02 3.0E-02 3.0E-02 1...,,.-.t 6.0E+01 6.0E+01 Xylene 9.2E-02 9.2E-02 9.2E-02 1 7:::'* 1.8E+02 1.8E+02 n-Hexane 2.9E-01 2.9E-01 2.9E-01 ..I.0k:+p0 ....-_.. 5.7E+02 5.7E+02 224 TMP 101E-01 1.1E-01 1.1E-01 0 0i0+00 2.2E+02 2.2E+02 6 of 25 K:\PA\2014\14W E1593.CP4.xlsm Condensate Storage Tank(s)Emissions Inventory • 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 011.9 - Regulation 7,Section XVILB,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,the following provisions Regulation 6,Part A,NSPS Subpart 0000 . Storage Tank is not subjectto NSPS 0000 NSPS Subpart 0000a Storage Tank is not subject to NSPS 0000a Regulation 8,Part E,MALT Subpart HH Storage Tank is not subject to MAGI'HH (See regulatory applicability worksheet for detailed analysis) • Section 07-Initial and Periodic Sampling and Testing Requirements Does the company use the state default emissions factors to estimate emissions? s., If yes,are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? .z N/A-Operator developed site specific emission factors 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 an 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 s ` wells brought on-line,then it may be appropriate psample. _g ) to use an oldersite-s site-specific ..�ir-,,. - If no,the permit will contain an"Initial Compliance"testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01. Does the company request a control device efficiency greater than 95%for a flare or combustion device? 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 efficiencyafthe combustion device based on inlet and outlet concentration sampling Section 08-Technical Analysis Notes This fadli does notutillze a combustor to controteW N missonsf[om thestorage vessels,Assuch,.there arerio-secentlary calibration emirstonsassocfated:with thrssou[ee: .> "This facilitydoes rsetmeettbe definition_ofa"natural gas comprossor-statioeor atatural gas processing plane per Regulation 7,,SectionXttand-XVII.In addition,accordmgto PS Memo.05-01,custody transferoccursattheexplorationandproductionviCe,Since this facility reeeiuescendensete via tenkertrucks and-pipelires from'nearbyweil production facilities,it would befocated.al'd point aftercustmdp f transfer.Asa result,thisfaciSty would not be considered en exploration and production site,Due totbis,Regulation 7 Action XII and XVII donut apply to this facility-5mcetbefacilitydoes nutfall within an iodustrysegment regulated by 5ectionnXiior XVII,thisfacility is subject to the requirementsin Section V€for"Storage and Transfer of PetroleumLiquid'.This result is consistent with the Division's determination for othersimilar fa"li₹ies.: - - ctto Regulation 7 Section VI and 5515 Kb,RACT:' ois satisfied through the requirement utilize internal floating roofs, i� SiSfrace these storage vessel are sUkye `The control device for these storage Veselsia-as internalncating xoof,77ve internal floatingroef is integrated into the design of each storage vessel.Since thelnterouiftoating roof is not anadd-On contrei, therein notan,accurate means for calculating-uncontrolled emissions For this reason,only the controlled-emissions are considered blunts analysis. - 'The weight%values used to determ nethe€KAP-emissionsfrom this-snurcearebased on an extended liquid analysis of unpressu rized Mobrara mode(obtained05/18/2016).The sample used is representativeof the hydrocarbon liquid that will be stored atthis facility.It should benoted thatusingtheweight%vaues from the liquid sample is a conservative estimate of emissions. Since the operator provided site specific emissionfactors based on a representatve stable hydrocarbon liquid analysisand thestoragevesse€sat this facilitycontainstabilized-oil(no flash),I determined an initial test would be required for this source 'The molecular weight used in the calculations is calculated by TenkESP using equation 1,i22 in AP-42Cirapter7.Tire m#lebilarWeightoeeesslightly based on tempereturesincethe.individual co stituentsi _... pressure vapor sure_dtan eswithtem p g perature. "The operatorindkatedinthe application that tank cleanings will occur approxboatelyevery tenyea[s-Asa result,.thepnacess limit of one tank cleaning per year isa reasonable limit within the permit andas at least conservative with respect to annual emissions, - • 'The permit contains three processes which include normal operation,roof landings and tank cleanings.These processesweresepanted cattle permit hecausethe emission's prate duringeach operation it different Byseparatingthe processes,the perms clearly identifies the emissions that will occur during each different opeeting scenario.This structure simplifies the compliance demonstration for the .{e operator since it provides a separate set of emissions factors that may be used during each operating scenario. --' Section 09-Inventory 5CC Coding and Emissions Factors Uncontrolled • Emissions AIRS Point# Process ti SCC Code Pollutant Factor Control% Units 001 01 CLEW,'_ ?{mom 'rµaul€5r,[ac'chr- t`'r�:%�%/! PM10 0.000E+00 0 lb 1,000 gallons .. ',�� _„ �fm„ �„„u.,,,.. -' t '/ ' / ga cans condensate throughpu PM2.5 0.000E+0D 0 lb/1,000 gallons condensate throughpu NOx 0.000E-000 0 lb/1,00 gallons condensate throughpu VOC L901E-02 0 lb/1,000 gallons condensate throughpu CO 0.000E+00 0 lb/1,000 gallons condensate throughpu Benzene 4.410E-05 0 lb/1,000 gallons condensate throughpu Toluene 1,2031-04 0 lb/1,000 gallons condensate throughpu Ethylbenzene 3.175E-05 0 lb/1,000 gallons condensate throughpu Xylene 9.695E-05 0 lb/1,000 gallons condensate throughpu n-Hexane 3.042E-04 0 lb/1,000 gallons condensate throughpu 224 TMP L175E-04 0 lb/1,000 gallons condensate throughpu "Note-Emission factors for process 01,02 and 03 have been combined here solely for inventory purposes.When calculating actual emissions,the operator will calculate emissions for process 01,02,and 03 independently using separate emission factors as described in the preliminary analysis above. • 7 of 25 K:\PA\2014\14W E1593.CP4.xlsm • Condensate Tank Regulatory Analysis Worksheet Colorado Peculation 3 Parts A and B.APEN and Permit Requirements ATTAINMENT-TMs source Is located In the ozone non-attainment area.Since this source does notemit COaall cuestie s6sl this seonlon are listed as N/A 1. Are uncontrolled actual emissions from any criteria pollutants from this Individual source greater than 2 TPY(Regulation 3,Part A,Section ll.D.1.a)7 NA , 2. is the construction date(service date)prior to 12/30/2002 and not modified after 12/31/2002(See PS Memo 05.01 Definitions 1.12 and1.14 and Section 2 for additional guidance on grandfather applicability)? NA 3. Are total faclity uncontrolled VOC emissions greater than 5TPY,NOx greater than 10 TPY or CO emissions greater than to TPY(Regulation 3,Part B,Section 11.0.3)7 NA...., 'Not enough Information NON-ATTAINMENT .1. Are uncontrolled emissions from any criteria pollutants from MP Individual source greater than 1 TPY(Regulation 3,Part A,Section Il.D.1.a(0 Yee'.. 'oli Source Requires an OPEN.Go to the next question 2. IS the construction date(service date)prior to 12/30/2002 and not modified after 12/31/2002(See PS Memo 05.01 Definitions 1.12 and114 and Section 2 for additional guidance on grandfather applicability)? (Jp G to nex[question 3. Are total facility uncontrolled VOC emissions from the greater than 2TPY,NOx greater than 5 Ten or CO emissions greater than STPY(Regulation 3,Part B,Section 0.0.2)2 Yaa ,' ,Source Requlresapermin 'Source requires a permit Colorado Regulation 7.Section Vi 1. Does this storage tank store"petroleum liquid"as defined by Regulation?Section VI.A2.g? - 'Goto the nest question 2. Does this storage tank meet any of the exemptions listed in Regulation?Section Vito? Go to the next question 3. Does the tank have a storage capacity greater than 40,000 gallons(952 barrels)? Source is subject to Regulation?Section Vl.B.2.b.;Go to the next question 4. Does the storage tank have a fixed roof? • . '1 Source Is subject to Regulation 7 Section Vl.B.2.a.;Go to the next question 5. Is the fixed roof tank used for the storage of petroleum liquids which have a true vapor pressure between 0.65 psla and 11.0 psis at sot(Rat)? Source Is subject to Regulation 7 Section Vl.B.2.a.(i);GO to the next question S. Is the fixed roof tank equipped with an Internal floating roof? 4,, Source Is subject to Regulation 7 Section Vl.B.2.e.(Ih-(III);Go to the next question SW1,44 tank Is suhfor4 to Regulation 1.Section l4.O.2.aAb Storage tank a.subject to Repletion 7,Section Vi.R.2.a.(i( • Storage tank is aubject to Regulation 7,Sections V1.0.2.d.(li)-jolt 7. Is the tank equipped with an external floating roof AND is larger than 952bbi AND stores petroleum Squid AND is located in ozone nonattainment area? 10/S-'-Storage Tanks not subject to Regulation 7,Section VI.B.2.c 8. Does the tank meet any of the exemptions of Section Vi.B.t.c(R(B)(1)? 9. Does the tank meet any of the exemptions of Section Vl.B.2.c.(i)(B)(2)? 10.Does the tank store petroleum Squats with true vapor pressure(as stored)above 1.3 psla7 ."... 'Storage Tank is not subjectro Regu'ation 7,Section 01.3.2.0. ' 55.Does the storage tank have a storage capacity less than 40,000 gallons(952 barrels)? N ':Source is not subject to Reg 7,Sec 01.0.3. 12.Does the storage tank store liquids with a true vapor pressure between 15 psla and 11.0 psis at 20'C7 A 13.Is the storage tank at a facility that receives and stores petroleum addressed by Regulation 7 Sections Vl.C.2 or VI.C.37 Storage Tank Is non subject to Regulation 7.Section VI.3.1 Storage tank is sobinct to Regulation 7,Section N • Colorado Regulation 7.Section Xif ' 1. Is the storage tank located in the 8-hr ozone control area or any ozone non-attainment area or attainment/maintenance area? og Go to the next question 2. Is this storage tank located at an all and gas exploration and production operations,natural gas compressor station or natural gas drip station? • Nq:;C_::x.:«Storage Tank is not subject to Regulation 7,Section XlI 3. Is this storage tank located upstream of a natural gas processing plant? IStal'age Tank is nor subject to Regulation 7,Seam,PR • Section X11.0.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section XII.C.2-Emisslon Estimation Procedures Section XII.0—Emissions Control Requirements Section PILE—Monitoring Section PILE—Recordkeeping and Reporting Colorado Regulation 7,Section XII.G 1. Is the storage tank located In the fi-hr ozone control area or any ozone nonettainment area or attainment/maintenance area? Yea iUhitI Go to the next question 2. Is this storage tank located at a natural gas processing plant? /al/l0 Storage Tank is not subject to Regulation 7,Section X11.0 3. Does this storage tank exhibit^Flash.'(e.g.storing non.stabilized liquids)emissions and have uncontrolled actual emissions greater than or equal to 2 tons per year VOL? NA2%r'n^•.:.� 'Storage Tank it rot suhiect to Regulation 7,Section X:i.Cs Section XII.G.2-Emissions Control Requirements Section XII.C.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section XII.C.2—Emission Estimation Procedures Colorado Regulation 7,Section XVII 1. Is this tank located at a transmission/storage facility? NO Go to next question 2. is this condensate storage tank'located at an oil and gas exploration and production operation,well production facility',natural gas compressor stations or natural gas processing plant? Nee:'':r,;i.';.Storage Tank is not subject to Regulation 7,Section XVII 3. Is this condensate storage tank a fixed roof storage tank? 4. Are uncontrolled actual emissions of this storage tank equal to or greater than 6 tons per year VOC? fit0. 'SinraRn Tank Is not subject to ltaguiation 7.San'.an XXII Settles WILES—General Provisions for Air Pollution Control Equipment and Prevention of Emissions Section XVII.C.1-Emissions Control and Monitoring Provisions Section XVII.C.3-Recordkeeping Requirements 5. Does the condensate storage tank contain only"stsblliaed"liquids? Storage Tank is not subject to Regulation?,Section XVII.C.2 ' I Sorage Tank 10 nut suhjeet to Rego edges 7,Section XV!I.C.2 Section XVIl.C.2-Capture and Monitoring for Storage Tanks fitted with Air Pollution Control Equipment • • 40 CFR.Part 60,Subpart Kb.Standards of Performance for Volatile Organic Mould Storage Vessels 1. Is the individual storage vessel capacity greater than or equal to 75 cubic meters(m)1-472 BBLsl? Go to the next question 2. Does the storage vessel meet the following exemption in 60.111b(d)(4)7 It.Go to the next question a.Does the vessel has a design capacity less than or equal to 1,589.874 ma 1"'10,000 BBL]used for petroleum'or condensate stored,processed,or treated prior to custody transfer'as defined in 60.010b? 3. Was this condensate storage tank constructed,reconstructed,or modified(see definitions 40 CFR,60.2)after July 23,1984? YeYY •Go to the next question 4. Does the tank meet the definition of"storage vessel'in 60.111b7 Go to the next question 5. Does the storage vessel store a"volatile organic squid(0011"x55 defined In 60.1116? yon Go to the next question 6. Does the storage vessel meet any one of the following additional exemptions: Np .I Source is subject to NSPSKb a.Is the storage vessel a pressure vessel designed to operate in excess of 204.9 bra("29.7 psi]and without emissions to the atmosphere(60.110b(d)(2))?;or N0 'i b The design capacity is greater than or equal to 151 m'(^950 BBL]and stores a liquid with a maximum true vapor pressure'less than 3.5 kPa(60.110b(b))7;or Nti C.The design capacity i5 greater than or equal to 75 Ma(^472 BBL)but less than 151 ms("950 BBL)and stores a liquid with a maximum true vapor pressure'less than 15.0 kPe(60.110b)b))? No•'! ISsorage tank Is uublect to NSPS Kb,including but not limited to,th,e following provisions I Subpart A,General Provisions §60.112b-Emissions Control Standards for VOC §60.113b-Testing and Procedures §60.115b-Reporting and Recordkeeping Requirements • 460.1166-Monitoring of Operations • 40 CFR.Part 00.Subpart 0000,Standards of Performance for Crude Ott and Natural Gas Production,Transmission and Distribution 1. Was this condensate storage vessel constructed,reconstructed,or modified(see definitions 40CFR,60.2)after August 23,2013 and prior to September 15,2015? Storage Tank Is not subject NSPS 0000-This tank was constructed after the applicability date. 2. Does thls condensate storage vessel meet the definition of"storage vessel"per 60.5430? NA rd 3. Is this condensate storage vessel located at facility in the onshore ell and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the Industry? 4M 11.,a 4. Are potential VOC emissions'from the individual storage vessel greater than or equal to 6 tans per year? 5. Isthe storage vessel subject to and controlled In accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HH? Yob.; a'.5 Storage Tank is not subject NSPS 0000 I Stara Tank is non nvbiect io NSPS 0000 subpart A,General Provisions per 460.5425 Table 3 460.5395-Emissions Control Standards for VOC 460.5413-Testing and Procedures 460,5395(g)-Notification,Reporting and Recordkeeping Requirements 960.5416(e)-Cover and Closed Vent System Monitoring Requirements 460.5419-Control Device Monitoring Requirements (Note:If a storage vessel Is previously determined to be subject to NSPS 0000 due to emissions above 6 tons per year VOL on the applicability determination date,it should remain subject to NSPS 0000 per 60,5365(e))2)even If potential VOC emissions drop below 6 tons per year] 40 CFR.Part 60.Subpart 00001.Standards of Performance far Crude Ill and Natural Gas Facilities for which Construction.Medificatlea.or Reconstruction Commenced After September it.2075 1. Was this condensate storage vessel constructed,reconstructed,or modified(see definitions 40 CFR,50.2)after September 18,20157 ¢ Go to the next question 2. Does this condensate storage vessel meet the definition of"storage vessel"'per 605430a? Ya• . Go to the next question 3. Is this condensate storage vessel located ate facility in the crude oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? Go to the next question • 4. Are potential VOC emissions'from the individual storage vessel greater than or equal to 6 tons per year? Yes,,,,, ;'d.:Ge to the next question 5. Is the storage vessel subject to and controlled in accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HO? Yob •':Storage Tank Is not subject NSPS 0000a IS:orage Tank Is nM subject so 0ip0 0000e 40 CFR,Part 63.Subpart MAR HH,Oil and Gas Production Facilities 1. is the tank located et a facility that is major for HAPs? Op,•„ '!Storage Tanks not subject MACI HO-There are no MACT HH requirements for tanks at area sources 2. Is the storage tank located at an oil and natural gas production facility that meets either of the following criteria: 1 II e.A facility that processes,upgrades or stores hydrocarbon liquids'(63.760(102));OR • b.A faclllty that processes,upgrades or stores natural gas prior to the point at which natural gas enters the natural gas transmission and storage source category or is delivered to a final end users(53,760(1))3)1? 3. Does the tank meet the definition of"storage vessel"°in 63.761? 16A_j."oi 4. Does the tank meet the definition of.storage vessel with the potential for flash emissions'per 63.7617 RrY 5. Is the tank subject to control requirements under 40 CFR Part 60 Subpart Kb or Subpart 0000? • 5:oruge Tank it aubjeeltoMACTtM Subpart A,General provisions per 653.764(a)Table 2 • 463.766-Emissions Control Standards 463.773-Monitoring 463.774 Recordkeeping • 463.775-Reporting SACS Review RACT review is required It Regulation 7 does not apply AND if the tank is In the non-attainment area.lithe tank meets both criteria,then review RACr requirements. Disclaimer This annument assists operators with determining applicability of certain requirements of the Clean Air Act,its implementing regulations,end Air Quality Control Commission regulations.This document is not a rule or regulation,end the analysis it contains may not apply toe particular situation based upon the individual facts and circumstances.This document does not change or substitute for any law, regulation,or any other legally binding requirement and is not legally enforceable.in the event of any conflict between the language of this document and the language of the Clean Air Act„its implementing regulations,end Air Quality Control Commission regulations,the language of the statute or regulation will control.The use of non-mandatory language such as"reconnnend,""may,""should,"end"can,"is intended to describe APCD interpretations and recommendations.Mandatory terminology such as"must"and"required"are intended to describe controlling requirements underthe terms of the Clean Air Act end Air Quality Control Commission regulations,but this document does not establish legally binding requirements in and of itself. Condensate Storage Tank(s)Emissions Inventory - Section Ol-AdminstTa0ve Infommtion 'Facility VIPs ID: -1Z3' ,jf;;„9Q3 _....ss,•.ii-� �4`.g�^,Ni°a C ty plant Point • - S000en 02-Equipment DesWWan Details 0e[a led Emcss on U .,...'0.,233 P,�fF33>P 13 3�3 3 _ pfd 33ifi' Faw lh73DsDUCD ,,,,, mrnaaltaeugroorcrxmema dc�' ri�. = l Daa pion. 3„s ,.",. _,"„zt_iu'.3»3�: ,,ft-99&p0.'..=.. mIl. ntnn'ptmn:nhoi 5 £mrsszc r so ntrallealnh�gah3e�'�i:lPoaa&,+93t33g.:e,h r NF" �j eFj::1'. RequestedovereitVOC&HAP Con[ Theextemaltloating roof is wmltlered an lntegmted control dewre.Pleazesee Effnenry%: I Yi1 0h s(' ,Section 08 Technical Analysis Notes loosen foraddleonel inlennetion. Section 03-Pmteseine Pam Inlonnatlon for Emissians Estliria�s Primary Emissions Storage Tanks) Atwal Condensate Throughput i to Bartels(6611 peryear Actual Condensate Throughput Whde Emissions Controls Operating= 4.0anels(Ill)pen year Requested Permit Thr.7:oughpm 4 088_Bartels(bbl)peryear Potentalto Emit(PIP)Cendeesate Throughptrt:�,d1. ',,',xy,i• '(,••iv, Bartels(bbq per year Iu,540,"'' agEgi 000entlary Omissiom-combusdon Device "This tastily does not WllzeammbusLion devicet0 tontralemiulons. Flea,. ,e •'55> Volume ofwaste gas emitted per BBL fliquids 3%333 Flea,ed „1i:33143ei313;u!,33p f/bbl ACWaI heat content 0(wazte gas routed to combustion device= o MMBTU per year 0M Request beat torten(of waste gas routed to tombustier devim= MDIV per year potential to rmh(PIE)heat wntent of waste.gas routed to combustion device= 0 9401001 per year Seatlon 04-Emissions FacWrs a Methodologies Ikti-W ilthis rtoragetank emit flesh..''''''n'' miss 2 At -'- j / 6a , :,1541Mn G.., R00FEmnt9m„Wi hg;•, //0 6'. Tonal tank losses fmm an aetemal leaflet roof during nentiel eperadan included em seal losses(La,withtlrewel losses(Laval,and deck 01001 losses(rl.The operamrmlculatedthese emissions using TankE5P_t an included s emseal This software Wllzes equatl0ns fmm AP-a2 to calculate the external floating met emissions during nmrnal eperatiens.The emissions resulting horn The simulati0n are en fallow: Parameters Value U/ye Source Annual1•The ;:o '""""10°°:::4''''' 31U25LW0 .r bbl/year 0.pere ➢,mYideadar0htm(g011/an3enkj Shell Clinga5 Fa00 (0,) I 6008; bbl/Ye'rt ,,, 3„i333•„A., AIK47T41.(ff329 An''''eO""u qud 16.4 lb/0.... 3o(3prNddvaiu/utnu nongtelta moon K 4}333)y1113h17713 -EiiiiiiiMAEZZNumberoftlaed Roof 1 wl Fixedmof e1F4[Ral310 47 gloofN !£ 1 pP rtedfi h 1o(,f3m i ilsupport Caiumns(Nt) 0al 3pYtrtla f a[io -rseaTab@?1-11= '' ' Efferitve column Diartder tile 9 ]gliu lB P I 07teois d ref ppemb 3 d"oru in` (Fr) _ _-canrtmawn drgatk re unknmvn. ZeroWlndspeed I - t - 0.6 Ibnmle/(['year AP 2iabte T.lB iM i h eon % 1� fm-bl tedsecondary}_ loss faRor(K� r :: ,-,'E 3ty3y, Wind speeddepe tl m 33' 3 bi k3'Itrmole/ft'year AP-4(2 blpltl(Ni hart 001 hoe pn ry lhhis moumeo secondary} seal loss faRo(Kaa) SealRelatedwi.peed " � �'� � Apy2T bfg7.vi�M hoi calshoeor maD wSh Rlntmo to,rronoary}'':, exponeirt ln) Averegeambie[ and ?i�,643i493BB A-Vu 20600.1.0 Tank 0lamet[0 ,,..'15N t�-' il,: Oparatorprovided value+.. Molecular Weight(M) 2361,", ib/Ih-male ,,,,,,,, , AP cchap[er2 rouuhon l-22''"' Daily Max Ambient Temp -09S4... .5 "" uP 42-!-:-:::::";::• :::;:„ :iii::::::::: - tallyMinAmbie[T Tern. 0P-42-fable 01] (,.en 0.3 499.8 Daily Daily Averege Ambient So9.9284932 'R ip42 tioultn ESua G0012J - TemP(Tu) 33 Abs.Tan9Paantml I m 339720.9 ., -" za-42 Table'.1.o Dally Totalsolarl 1 t 3g "- Fasz,,) 5h4.{;�i2fi Btu/f[tleY F422dLt].1> : UquldBulkTemp(Te) 509.0104932 'R ,,,,, VP42!'2,',-,':,;:0r.:7::quators l-28 Da IY Average liquid s12.0eueuoo P •eChaoter?Ey upon Y-26-- "' SurtaceTemp(T(T y l//i m.h.�--> Atmospheric Press (P,� psi s/� 401003PInncpressu for penverCO- - - Reid Vapor Pressure psla l/t)3ii. hdlptuttded- VaporPressureC at [ �' - £ [lOd 3 33 A 021£53 to 3f arhii�hip��e'Nf4 t I .STM il63T/ ,3 Vapor PrazsoreC .q�g 181'a— t !tE 1' tf B s nor NPs.„,',...:-,4.&.,.0!..7,7-'N A9 p VaParpressureatdaiio /8' $43 vemgelquidsurface 5.322219111 psi 02_hap`-r.Fq % 124, a temperature(P0( '-i.`9 .�n =_ oeporpraP,mfunrtier 030.3566445 C\ • 2F 42Cl�tar]£gvati ttU ',' OnedVRGatter(yy) Q_6 , :,':,- io:4:a audetds;tfarsI th rotganc hot ids:. Plm seal Looses(La 1871276262 Ib/Y "" 700 ESP d using Atx42.Chapter11 Ea,u iY :2 2 WRhdrewal Losses(Lee) ]sa1.12 Ihz/Year TOILPsP dosing AY-d2=tl4 pt#TEgU6Lonz4 - Deck Rttlng loses Qt) Si4541.173 : Ibs/year III '1k ES dunng,tG-02 Cto)Vor7 F.{u6tit 25 Tonal Losses 10600.38 Ih/year - d AP-42£hepterTEgllatltt 2-i Total NumberolV�els ,,,,,,,,,-90',U,49- Standing Lossg: 3063.21 lb/yr 3 r Tafal Emissions: Pollutant Weigh% Ibs/year Souse VOC 4241]52 AP32 21.20B2fi Benzene • _4.10232 98.4086460. A4d55R i R Toluene ' 0.00633 268.5029016 tVus0H)e m 9 J Ethylbenzene .-:-'''''':':'66-i4'''-':':.;, )08322584 .h?[asm )n 48' MaN oylena .0.0051 216329352 T Yts•3:� [an e — n-Vaoane i iijj'..:7000 67861032 RT Sg400nte' 2,2,0-TMP _,�og61s,,,g; zfizl Ds 1 S.�'Tanye- } • 10 of 25 K:\PA\2014\14WF1593.CP4xhm Condensate Storage Tank(s)Emissions Inventory Pro¢xt/i.Roof iandtnggrilt'loq Gloulationz for External Floating Roof with full Liquid Heel • Parameters Value unit Source pole AP-02 Chapter Ercatlon Y24(based an deity average ambient tempe0Lure-see Tine Vapor Pressure(P) 5.120542911 note 3 fpryquatian 231n AP-42 Chapter hapter 7) Average Temperature of vapor and liquid below 509.92 0. AP-42 Chapter 7 Equation1:27 floating roof(T=T„) Ideal Gas Constant('R') 10.733 (Psi`ft')/pa Idea:easlawCl8Y5te, morn) Number of days tank stands idle with floating ;1 days --Engineer€stimate roof landed Ina) Stack Vapor Moleolbr 530 11/I0-noel AP-42 Chapter 7 Equation l-22{Fst1Omted byTankE0P4 weight,(M.) Saturation Factor(S) x:0.6 ,\ AP42Tabbe-t1.17-Valuelor full liquid heel EffectiveHeightofstock operator estimated value'' Liquid Roof Leg Height(low leg 3333 ft -- Operatoreotlmatadval0C setting) Height of vapor space 3.163 ft A9-42 Chapter 7 Equation l-15{norobfuutage so Haq0y under floating roof(h,) • Tank Diameter(0) -150 ft Operatorprandedvalue Gaily maximum ambient 5]391 •R AP-42.61(174-7-AveragevaWofar Denver,CO temperature(T.,) Gaily minimum ambient 555.87 'R AP-44T2bie]:O-7-Average vet.for Denver.CO temperature(T.,) Daily Total lnsala[bn 3500 0tu/ft'•day AP-42.Table 7.1-J-Averagevaryofaryenver,CO Factor(I) Tank paint solar absorp[ance(a) 7 AP-42 Table 7.1.-6-wbne paint in 1004 oondRon Atmospheric pressure(P.)^. 0..1 1212....... pole Arnblontpressurefar Denver;CO geld Vapor Pressure 857 psis Englner ES000010 Vaporpressurefunction 0.]36400611 AP-42 Chapter]&Nation 2-3 (P.) Volume of Vapor Space 55694.82379 it' AP-02 Chapter?Egtwtion i-3 Vented Vaporsatuation 0.538096504 AP-42 Chanter 7 Factor(K1f EWatmn I-20. Vapor Pressure Constant 4623.081 From linear gegressivn ofTVP atl0degTlntorvalsvleA9TM 08377 ,. for Crude O l5toclts(BI V000r Pressure Constant 14.71151 0loin.linear 0egnesslonayvor at 10 deg T Intervals via ASFM 06377 far Crude Oil Storks(A) Daily Ambient 28.1 'R AP-43 Chapter]EgUaW01-12 Temperature Range(AT,) Daily VaporTemperature 2759568 'R AP42Chapter7 Equation 1-g. Range(AT,) Liquid Bulk Temp IT,) 50934 'R AP-42 Chapter?Equation 1.28 Daily Average Liquid 512.037024 'R AP-42 Chapter?Equattod 146 Surface Temp(Tid Vapor Pressure at Daily Max Liquid Surface 6531844077 polo AP-4.2 Chapter 7 Equation1--24 Temperature(P,) Vapor Pressure at Daily MinLiquidSurface 3.959180217 polo AP-42 Chapter?Equat1mi 1-24 Temperature Daily Vapor Pressure 290266384 pole AW-02 fhapter 7£gvollon l-9. flange(APy) Vapor rtbn 02346)109 "` \ AP-422 Chapter 7 Equation l-20 Factor O Eve,Standing Losses 350.00TI739 Its AY42 Chapter?lquatwn2-l0, w/out Wind Event Filling LOssesw/out 1682.450974 I00 AP-42 Chapter 7E4Uarpn 2-26 Wind • Correction Factor(Cal 0.666069420 0 AP42 Chapter7hquation 2.30 Event Standing Losses(L,,) 6252133409 Ib/rootlaoding AP-42 Chapter?ErUatf0n2-15 Event Filling Losses(Co.) 1458.465313 Ib/roof landln6 Ap42Chapter7Equatroe2.27 e M Total Landing Loss 0003.670016 lb/roof landing Ap-02 Chap oroe uatian2.10 Emissions(Ln-4L'ILu) event Total Number of Roof Landing events Total Emissions: Pollutant Weight% Ibs/year Source VOC -- 8339.214623 APA$ Bethune 000232 1933653793 Mass Balance. Tohlene 0.00633 52.75874357. Mass Balance Ethylbemene 0.00167' 1331897342 MassBalance Xylenes 0.0051 4250704458 53350 Balance n-Hexane 6.016 13 3355434 Mass Balance 2,2,4-7MP ¢,00618 5150853637 Mast Balance 11 of 25 K:\PA\2014\14WE1593.CP44lsm Condensate Storage Tank(s)Emissions Inventory P,amaf6r Tadreleanmg; Tenkt5P_d calculates the total losses from the floating roofteok during deaning aper00005.The equadone governing the emissions dudogthls process are established In API Technical Reference 2568.The operator grouped this process into five stages which will be described and calculated below: Parameters Value Units Stage l:Standl gldl ;", TanV SP tlusn Pd2 2 ed2 losses-Full liquid h l of ;129148 lbs gA I aK=t,noing ltlle crude oil .1n rG cmmtnceo) _. Stage 2:Initial Vapor Purge-Full liquid heel of -29661 I. rank ESP <<F ion227 modest Stage 3:Dally Vapor Purge-Full Liquid Heel of ""930339;x- Ibs Ta klSP1 3(g l3 TB.5634 tar]'1,Maal�^rj crude oil r.,since 3 days of vapor purge l3 days of etage3) Stage 3 Pert 11 erode Oil Sludge Removal-Full 19188 Ibs -an;.E P..us;ngnpI TP 2563 Equation:9 liquid heel with cont. forced uennledon - u 3 since 3 days of forced vent bt on with sludge removal Stage 4:Daily V po Purge(Diesel)-Full squid :0106 lbs lank ESP_d AP 42 Ch P r7590am,1.26 Heel m x2 n nce 2 days of vapor purge after dliuent mash Stage 4:SludgeR oval 5" of Diesel with cont. , ,, 3837 lbs ¢ring TR 65,5 Egpat:6 I9 forted venmleOon "1:' � x351 nce3 days oftormdvmalation with diluent wash Stage5.Retllingiossee 13,1154,: C p 171312 2�I41,,=D r e l (Crude Oil) 79789 Ibs tank is deans Total losses 166321_ Ib/cleanng Total Number drank ceasing Events „i�:.2 itl Total Emissions: Pollutant Weight% lbs/year Stufce VOC 10632.12 AP A2 Benzene 0:0232 38.5865186 Mass.Balance Toluene 0_00633 1052813106 Masse Balance Ethylbenzene 0.00167 27.7756404 Mass Balance %ylenes .0.0051 84 823812 Mass.Balance n-Hexane 0.016 26611392 Mass Balance 2,2,4-TMP d)<"_0:00618 102.7865016 A...Balance MOSe Pfmris0£:£44inai Floating Roof Emissions Dadn.Nonral Operaiions Condensate Storage Tanks Control Device Uncontrolled EF. Controlled E.F. Uncontrolled EF. Uncontrolled Pollute. (lbs/bbl (lbs/bbl (Ibs/MMBtu E.F.(lbs/bbl Emissions Fador5ourte CltaHan Condensate Condensate waste heat Condensate Throughput) Throughput) combusted) Throughput) • r PM30 R\\�\�\\\�`. .�.\\�n����N\� \�� 0.0000 ., 7 -. `�v✓'�/ � PM2.5U\\\\'\\\ l\\`u'''h��\\�\�a\� 0 i„ y 00000 WC 1,16C-04 :r1 Benzene 7:930E0) ob 2:1 Fos R'v �l\Q� 'y�r¢Etakr % EthTyl at enae n-Nexane Sd69F06 - ltl`\ � -Site SpedBeT 1rF$P d - 224TMP 3112E-06 2111E 06 \ T;'-.�\�1C' �\\��6it7Spr UC4o0bE2P„2E7 yemmnliiiii Lfl(ng. ty 1 "r Process 02:Hoof landing Emission Cakolasonafm'E%temffif0os0.3 Roof with Full 09112 Heel Control Device Uncontrolled E.F. Uncontrolled Pollutant Uncontrolled EF. Controlled E.F. (Ibs/MMBtu Er.(Ibs/bbl Emissions Fedor Source Citation llbe/rooflandln6 (Ibs/reef landing waste heat Condensate event) event) combusted) Throughput) \ i.... o 0000 083679 ® \`.,. 0 :'.\.`\`..��•`.`c5.��$ 0.0000 INIMMIE2E4834 1•22. -,`\\\\ \ \\ MM'TMIEM ® 1 : r � L.� a • =*z877 �v." ,t A. «, ., Pr0:essn3,Tank CieaMpg ,., .. , Co densnte Smrege Tanis Control Device Uncontrolled E.F. Uncontrolled Pollutant Unconttolled E.F. Controlled Fl. (Ibs/MM9tu Er.(lbs/bblEmlealom Fector5ourte Citation (lbs/cleaning O./cleaning waste heat Condensate ant) even t) combusted) Throughpr) 11111121 .0000 ® ' tea 2i6s{11107jwP( Mitt. f:X:1 11 ,212! s4.a . � �a sfis t37o v1 42 666 4 -.® mss" � 5�6�mlAp apta-24- " IOz7B7 ;� � tS�, o ;'cost os z, Section Os Emissions Inventory N\2"s ..a,ProciestraLiExlentai ltOWERE dbanne Dueragtdomret 0-0500001:,Wi Potential to Emit Requested Perms Limas ActuaiFmvsions Criteria Pollutants Uncomrplled Unm,rtmllad Controlled Uncontrolled Controlled Itons/year) (tons/yar) )tons/pear) (tans/year) (tons/year) PM10 0,0 0.0 0.0 0.0 0.0 PM25 0.0 0.0 0.0 0.0 NOx 0.0 0.0 0.0 0.0 0.0 VOC 21203 21209 2 0.000 0.000 CO 0.0 0.09 0.0 0.0 Potential to Emtt Requested Parma Umi6 Actual Emissions Requested Emvsbns Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled Uncamrolled Controlled Uncontrolled Controlled (tons/year) Itom/Pearl (tons/year) Imns/rarl (mns/rrarl Ohs/year) (lbs/year( Benxene 0.05 0.05 0.05 0.00 0.00 9841 98.61 Toluene 0.130.23 0.00 0.00 268.50 26850 EUrylbenzene 0.04 0,04 0.04 0.00 0.00 7084 70.84 Xylene 0.11 0.11 0.11 0.00 0.00 21633 21633 n-Hexane 034 034 0.34 OM 0.00 678.68 678.68 224 min 0.13 0.13 0.13 0.00 0.00 262.14 26214 12.25 K\PA\2014\14W E1593.CP4xlsm Condensate Storage Tank(s)Emissions Inventory • PYtke5,Y02:110unnaildrngEmf9slan C910010Lkn§iorFHehrefjkotrnif TWEtil F00102W1fle00r Potential to Emit Requested Permit Emits Criteria Pollutants Uncontrolled Uncontrolled Controlled , • (tans/year) (tons/year) (tons/year) , PM10 0,0 0.0 0.0 =' PM25 0-0 09 0.0 NOx 0.0 0.0 VOC 4.1. 4.162 4.167 ___ >_- . CO 0.0 0.0 0.0 _ Potential to Emit Requested Permit Emits Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled __ Uncontrolled Controlled (tons/year) (tons/year) (tans/year) ,.. - (Ibs/year) (Ils/year) Benzene 0.01 0.01 0,01 1934 • 1934_ Toluene 0,03 093 axe . 52.76 52.76 Ethylbenrene 091 001 0.01 1392 1392 • Xylene 002 0.02 0.02 4251 42.51 n-Hexane 0:07 0.07 0.07 -. 13336 13336 ' 2247MP 0.03 0.03 0.03 .-„ 3 5151 5151 T ./r $roa76_iTankdeaning: 0 Potential to Emit Requested Permit Limits - Criteria Pollutants Uncontrolled Uncontrolled Controlled _. _.. (tons/year) (tons/year) (tons/year) PMlo 0.0 0.0 0.0 .., 0. PM2.5 09 0.0 0.0 NOx 09 0.0 0.0 VOC 8316 8316 8316 - - - CO 0.0 09 0.0 ___ PotentialtoEmR Requested Permit Limits -----.= Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled .=.0 -- Uncontrolled Controlled (tons/year) (tons/year) (ion/year) ,...,so (Ibs/year) (Ibs/year) Benzene 0.02 0.02 0.02 _ 3859 3859 Toluene 0,05 0.05 0.05 - 10528' 10528 Ethylbenzene 0.01 091 0,01 t 7, 2728 27.78 Xylene 0.04 0.04 0.04 %, co 8482 Rasa n-Hexane 0,13 0.13 013 26611 266.11 224 IMP 0.05 0.0S 0.05 n..._ 0 102.79 102.79 _ .-%ri y;. %rat ,ra�;Yia,PE>tremac:4 eogm a(.Tenk.,;.C,,,,,,--,7,,,.:m r:-...- Potential to Emit Requested Permit Limns Criteria Pollutants Uncontrolled Uncontrolled Controlled - ., (tons/year) (tons/year) (tons/year) P8410 0.0 0.0 0.0 PM2.5 90 0.0 ..., NOx 0.0 09 0.0 .. VOC 33.692 33,692 33.692 CO 0.0 0.0 a:0 ,.. Potential to Emit Requested Permit Limits _. Rested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled --. Uncontrolled Controlled (tons/year) (tons/year) (tans/year) (lbs/year) fibs/Veer) Benzene 0.08 0,08 0.08 ., 15633 156.33 Toluene 0.21 0.21 0,21 426.54 42654 Ethylbenzene 0.06 0.06 0.06 - 11253 11233 Xylene 0.17 0.17 0.17 _.:. -, 34346 343.66 n.Hexane 0.54 054 0.54 1078.15 1078.15 224 TMP 0,21 021 0,21 .._L 416.44 41644 Section O6-Regulatory Summery Analysis Regulation 3,Parts A,B Source requires a permit. Regulation 7,Section VI Storage tank is subjectto Regulation 7,Section VI Regulation 7,5005115 X]I.C,O,E,F Storage Tank is notsubjectto Regulation 7,Section Xtl Regulation 7,Section 100.G,C Storage Tank is not subject.Regulation 7,Section 01.1 Regulation 7,Section XV11.B,C.l,CS Storage Tank Is not subject to Regulation 7,Section XVII Regulation 7,Section XVII.C2 Storage Tank is not subject.Regulation 7,Seaton XVII.G2 Regulation 6,Part A,NSPS Subpart Kb Storage tank is subject to N5P5 K6,including but not lime.to,the Regulation 6,Part A.NIPS Subpart 0000 Storage Tank Is not subjectto N5P50000 NSPS Subpart 0000e Storage Tank Is not subject.9575 0000a Regulation B,Part E,MACfSubpart HH Storage Tank is not subject to MACT HH (See regulatory applicability worksheet for detailed analysis) • • 13 of 23 IC\PA\2014\14WE1593.CP04lsm Condensate Storage Tank(s)Emissions Inventory Section 0J-Initial and Periodic Sampling and Tesdng Pequirements Ooesthecompany usethestatedefauhemssonsfactorstoestimateem 7 #yes,aretheu controlled artual or requested emissions estimated to begreaterihan or equal to aotans VOC peryeari at,-.rc:=, n N/A-Opemtordeveloped site spec fic eminn onfactors If yes,the permit will contain an"Initial Compliance"testing requirement to tlevelop a s#especific amissioco fawon hosed an guidelines in PS Memo 05-01. Ones the company use a site specific emis ans fanotto eat mate emissions? If yes and dihere areflssh emnslons,arethe em sslonsfactors based onapressurized llqu dsample dawn aih faalRy being permrttedl Thssample should be cons dered represeirtatrvewhrah generally means sae-specifics d �, collected with noneyear of the appbation received date.Nowever,'dthefaulRy haz no[been moddetl(e g.,n -- yn ₹ � ' wells broughtonline),Ihenhmay beappropr a[eto use an aldersi[eapecificsample. Bdfi�i4 ,,...,,... #no,the permit will contain an"Initial Compliance"testing requirement to develop a site specfic emssions factor haled on guidelines in P5 Mem005-01. Ooa the company ipnz request a control device eFfcienry greaerihan 95%far a flare or cow000tlon devices N/A-Acombusban deWreis not used to cpptrol emfss If yes,the permit will contain and indai compllancetest condition to demonstm[ethe destmRiOn efficienry0f[he combustion devi'co basetl an inlet and outlet concentration sampling SeM OS T h i I A'''''''s al i N y-Yh #od d otvti F I7T o howah-sm gP k Uwnudr.th euwnd 1y133 l l prls azl'wttkthi - - 1 4 1�l.1 1: X11333 Ilgl'df26Jrot£rlae[daedeJf((i Ufa a{ux gdS;smppresw(s1, grv.,a".":„,Aga5,,ii w gpian{P rtaF,„i a F;ect(h4aandxtnnload o a fri,: l4Me OS-�$w5fady fiawattsn 641tSU}M hfacut[p-udpmducti9h6R&ed-ar altae oeooiNentuata ats yai 000to C 44$, it treaty Ilpmu Ip hlffkSxfoYau(am Socd£eil R p ni. Cwt dy' Ries P Aa 00 eo h fsthiit cueogtt4 Id ed xpiotat atsdp duct 0,441#4 ha k4akih yet Ids/ dpeto I tayodr tfi onalft3'-31 £fi fa Ttyd rgim M dusty gme tooth ateni tot ulgrgAt(( x.lit§af IbXs bj t#aih req E 3actwn Vii St get p alsf bEPatt l ii fliu eslil¢y7--77 Ist thth Dmz det flnlh i r hdi II rf ontr 31 1 1 1 - - 1��11 t>iiriii I 1 1 ? - 1 1 '3116 3:,...?,.F!,:,„..:.",th sE t. g I bl ctNg 701 TS 17 dd%P4Y3 .GT'3sati :11,:r girtA eqp tt uUT eaT ifi abng oil. ..ay.1 >§1 I'£1 A 7H' i 1 gi ti d' f h sY & r ate[ IHmY st otct ottS lib Ij i ntegra[idirdnnl l sgw t hsY raga el 51 ₹t Met,fflo Mg aF not R di#rl natrgi�{�Ye rm £ forung ptrolied sat�,�n.£tnhraa mr Nvtb pufroiCedamitslan d ad ith_n lY - - 1 d 11 l 11 I 'Tb gM.b i d --rs.. 6 ih basedtr e# dedl'ga44.6§ M11P0d edNMi 'dl. >�0$18IZ>31§i-1h anlpl d presentat afth Lys rho Iq doh Ccdib d h tholty tt h Idb tedthot p he6eght1du tone h Iigdld p12js 3d 5 ti t to f IR17 � Mic 77 }} v5 Ce£hLOpe 3COY pfWldtd iteipen➢ m 5IBR133d�$bdsedA afep esaA[LivedtabfetydsopebOniRlu#1 rfdly5tsarydthE'staragev'en`BLS.dIub it btiTb upsHilTkd 1{no5tesb}3SIe[eY/nlnEtlaR m ttesb id t5 warm d#o th fi - 1 I' i"i 11 1 I 1 P - 1111 i1. li MTh lei(e g Lsed Rh f letw I I t d5/S Ops g qp tl b22j AP-ri2 thapt 3 Th ocukr mpht I ghNybaed t mpmatu 1 a 4h rtd Ild AI 1 P by # 02s 50 enar .x Rhtomps of r 1 1 } 11 to Ii 31 1 i RA 'fi Data d.?;m xfie�eircat nth t€ kd gs it -pp i §` _ y�As klhgid Hi lmar(b t kN.g �peOye is I Ewa/xlrcpet Rand ooi t mr#vanthe`+'Ph exp m I w 1 itt 11 11 Il 'i�'��-'.y1y, (O1 1 11 a a "Th yt ti b 0000/Am pr b o d tl maiFnperati too d g93rdt 0 k ngsadt = e$a53" teeariO.15 pam#ha ih It P0m P ii14a Pgl'p pens$rtt.$ysepatati 0/es praceec S th p01 IdGedy d mtfi a mosbr5Pha oh p uonm t t 0Hei dyglia7}7at)ng fro Tt N e Implfhp5t4emmplidRrsdemohst�dtl§lyf9�5iit pe t rtP Id separate et f m6.i Yd t thatm4 sedgy nng „,Peratm& o' 1111 i]113ije1 1 1 - 1 "'���n ufo up CEroS�eaitp it m r!ss ru�isgsppgb 111( - 1 ,�` 5000 09-i oaeOopastC Coding and Emissions Factors 00000 coned Emissions Alps Paint# Process# SCC Cod pollutant Factor Contra% Uni15 ii ,,S ,a�`� 004 01 ptACatE Hm; „ • ..SK,.' £a`r g-i__ PM10 0.0005000 0 b/1,000 gallons candensatethroughput PM25 O.o00Ei00 0 b/1,000 gallons condensatethmughput 000 0.000EM0 0 b/1,000 gallonscondnosatethroughput VOC 1293E-02 0 bin gallons coedensatethroughput CO 0.0005000 0 6/1,000 gallons00edensatethroughput - Benzene 2.999E-05 0 6/3,000 gallons condensatethnoughput - Toluene 6.184E-05 0 b/1,000 gallons condensatethroughput Ethylbenzene 2.159E-05 0 6/1,000 gallons coedensatethroughput Xylene 3593E-05 0 6/1,000 gailoco condomateth0aughput n-Hexane 3A69E-04 0 6/0,000 gallons condensatethroughput 224 TMP 2.900105 0 h/1,000 ashore condansatethr0ughWt ^Note-Emission Factors for pmraaa 01,02 and 03 have been combined hero solely 00nlnventory purposes.When calculating actual emissions,the aperatorwiil calculate emissions for process 01,oe,and 03 indepentlentty using separate enusslon factors as desnibed In the prelledoary analysis above. 14d. K:\PA\2014\34WE1593.CP4xlsm Condensate Tank Regulatory Analysis Worksheet Colorado Regulation 3 Parts A and B-OPEN and Permit Requirements ATTAINMENT-This source is located in the ozone non-attainment area,Since this source does not emit CO,all questions in this section are listed as N/A 1. Are uncontrolled actual emissions from any criteria pollutants from this individual source greater than 2 TPY(Regulation 3,Part A,Section 11.5.1.0)? 2. Is the construction date(service date)prior to 12/30/2002 and not modified after 12/31/2002(See P5 Memo 05-01 Definitions tins 112 and1.14 and Section 2 for additional guidance on grandfather applicability)? 3. Are total facility uncontrolled VOC emissions greater than 5 TPV,N0x greater than 10TPY or CO emissions greater than to TPY(Regulation 3,Part 8,Section 11.0.31? NAt 'Nat enough Information NON-ATTAINMENT 1. Are uncontrolled emissions from any criteria pollutants from this Individual source greater than 1 TPV(Rego lotion 3,Part A,Section II.D.1.a)? YenyoMO,Source Requires an APES.Go to the next question 2. Is the construction date Iservlce date)prior to 12/30/2002 and not modified after 12/31/2002(See PS Memo 05-01 Defnit ons 1.12 and1.14 and Section 2 for additional guidance on grandfather applicability)? N4 Iia Go to next question 3. Are total facility uncontrolled VOC emissions from the greater than 2 TPY,NOx greater than 5 TPY or CO emissions greater than 5 TPY(Regulation 3,Part B,Section il.D 2)? yes...r., Source Requires a permit Souron requires z permit Colorado Regulation 7,Section VI 1. Does this storage tank store"petroleum liquid"as defined by Regulation 7 Section VI.A.2.g? i'ec'Ytt Yd Go to the t question 2. Does this storage tank meet any of the exemptions listed in Regulation 7Section VI.B.17 SEV;•'.Go to the xt question 3. Does the tank have a storage capacity greater than 40,000 gallons(952 barrels)? '2so.%.Source is subject to Regulation 7 Section V1.8.2.6.;Go to the next question 4. Does the storage tank have a fixed roof? Storage Tank is not subject to Regulation 7,Section Viola. 5. Is the fixed roof tank used for the storage of petroleum liquids which have a true vapor pressure between 0.65 psis and 11.0 psla at 20"C(BLIT)7 S. Is the fixed roof tank equipped with an internal floating roof? NA Storage tank is subject to Regulation 7,Section`✓LB.2.alidr • Storage Tank is not subject to Regulation 7,Section Vl.a.2.a.(i) Storage Tank Is not subject to Regulation 7,Section Vi.B.2.a.fiij-iiilj 7. Is the tank equipped with an external fixating roof AND is larger than 952bblAND stores petroleum liquid AND is located In ozone nonattainment area? Yes _"GIs Source is subjecyto Regulation 7 Section Vl.B.2.c;Go to the next question 8, Does the tank meet any of the exemptions of Section Vl.B.2.c.(g(a)(1)? NO''',""%""4 Storage Tank Is subject to Regulation 7,Section 01.8.2.c. 9. Does the tank meet any of the exemptions of Sectlon VI.B.2[.(1)181(2)7 Na Y Storage Tank is subject to Regulation 7,Section 01.8.2.[.;Go to the next question fig,",;.So,Does the tank store petroleum Ilquds with true vapor pressure(as stored)above 1.3 psis? ( 'i:•n rSource is subject to Reg 7,Sec VI.B.2.c.(Ii)IA);Gq to next question 'Storage tank Is subject to Reguiatlun 7,Section.91.0.2.c 11.Does the storage tank have a storage capacity less than 40,000 gallons(952 barrels)? Na Source is not subject to Reg 7,Sec)/1.B.3. 12.Does the storage tank store liquids with a true vapor pressure between 1.5 psla and 11.0 psia at 21°C7 NA""":"4.01S6 13.Is the storage tank at a Mat,that receives and stores petrbiellln addressed by Regulation 7 Sections VI.C.2 or VI•C.3? NA Storage Tank is nut subject to Regulation 7,Section 01.8.3 Storage tank is sublest to Reguiation 7,Section VI Colorado Regulation 7,Section XII 1. Is this storage tank located in the 8-hr ozone control area or any ozone non attainment area or attainment/maintenance area? sY�re ;.Go to the next question 2. Is this storage tank located at an oil and gas exploration and production operation', r14,II*/.AY natural gas compressor station or natural gas drip station? +':.Storage Tank is not subject to Regulation 7,Section XII 3. Is this storage tank located upstream de natural gas processing plant? ROW"' W • 'Storage Tank Is not subject to Regulation 7,Section XII - Section XII.C.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section XII.C.2—Emission Estimation Procedures Section 011,0—Emissions Control Requirements Section 011.0—Monitoring Section XILP—Recordkeeping and Reporting Colorado Regulation 7,Section XII.G 1. Is this storage tank located In the 8hr ozone control area or any ozone non-attainment area or attainment/maintenance area? yes`. Go to the next question 2. Is this storage tank located at a natural gas processing plant? NOVStorage Tank is not subject to Regulation 7,Section 011.0 3. Does this storage tank exhibit Flash(e.g.storing non-stabilized liquids)emissions and have uncontrolled actual emissions greater than or equal to 2 tons per year VOC? NA`\ 'Storage Tank is not subject to Regoiatioa 7,Section 011.4 Section 011.6.2-Emissions Control Requirements Section XII.C.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section Oli.C.2—Emission Estimation Procedures Colorado Regulation 7,Section XVII 1. Is this tank located at a transmission/storage facility? Nd '-00`,3 Go to next question 2. Is this condensate storage tank'located at an oil and gas exploration and production operation,well production facility',natural gas compressor stations or natural gas processing plant? iii,i(„/s Storage Tank is not subject to Regulation 7,Section XVII 3. Is this condensate storage tank a fixed roof storage tank? NA'O1'n s „ 4. Are uncontrolled actual emissions'of this storage tank equal to or greater than 6 tons per year VOC? 'Storage Tank Is trot subject to Regulation 7,Section XVII Section XVILB—General Provisions for Air Pollution Control Equipment and Prevention of Emissions Section XVII.C.1-Emissions Control and Monitoring Provisions Section XVIl.C.3-Recordkeeping Requirements 5. Does the condensate storage tank contain only"stabilized"liquids? ;.?Storage Tank is not subject to Regulation 7,Section XVII.C.2 ' 'Storage Tank Is not subject to Regulation 7,Section XVR.C.2 Section XVII.C.2-Capture and Monitoring for Storage Tanks fitted with Alr Pollution Control Equipment • 40 CFR,Part 60,Subpart Kb,Standards of Performance for Volatile Organic Liquid Storage Vessels 1. Is the individual storage vessel capacity greater than or equal to 75 cubic meters(me)["472 BBLs]? 'Mill�Go to the next question 2. Does the storage vessel meet the following exemption in 60.1116(4)(4)7 Nu ,,', Go to the next question a.Does the vessel has a design capacity less than or equal to 1,589.874 m5['"10,000 BBL]used for petroleum`o condensate stored,processed,on treated prior to custody transfer'as defined in 60.111b? 3. Was this condensate storage tank constructed,reconstructed,or modified(see definitions 40 CFR,60.2)after July 23,1984? y6%, Go to the next question 4. Does the tank meet the definition of"storage vessel"'In 60.111b7 MetGo to the next question 5. Does the storage vessel store a"volatile organic liquid(VOW"'as defined in 60.11167 Me Go to the next question 6. Does the storage vessel meet any one of the following additional exemptions: No Source is subject to NSPS Kb e.Is the storage vessel a pressure vessel designed to operate in excess of 204.9 kPa["291 psi]and without emissions to the atmosphere(60.110b(d)(2))7,or N"46 n r b.The design capacity is greater than or equal to 151 m'[^950 BBL]and stores a liquid with a maximum true vapor pressure'less than 3.5 kPa(60.1106(6))7;or c.The design capacity is greater than or equal to 75 M5[-472 BBL]but less than 151 m'['950 8BL)and stores a liquid with a maximum true vapor pressures less than 15.0 kPa)60.110blbl)7 IStenage took is subject to IMPS Kb,including but nut limited to,the foi€owing provisions Subpart A,General Provisions 460.112b-Emissions Control Standards for VOC 460.113b-Testing and Procedures • 460.1158-Reporting and Recordkeeping Requirements 580.116b-Monitoring of Operations 40 CFR,Part 60,Subpart 0000,Standards of Performance for Crude Oil and Natural Gas Production,Transmission and Distribution 1. Was this condensate storage vessel constructed,reconstructed,or modified(see definitions 4D CFR,60.2)after August23,2011 and prior to September 18,2015? • t4'.Storage Tank is not subject NSPS 0000-This sank was constructed after the applicability date. • 2. Does this condensate storage vessel meet the definition of"storage vessel"'per 60.54307 NAa 3. Is this condensate storage vessel located ate facility in the onshore oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? t A�"�•.;;�,''„'': 4. Are potential VOC emissions'from the individual storage v sel greater than or equal to 6 tons per year? 5. Is the storage vessel subject to and controlled In accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HH? :7a5,-„:'.':Storage Tank is not subject NSPS 0000 I9torege Tank is not subject to NSPS 0000 Subpart A,General Provisions per 860.5425 Table 3 860.5395-Emissions Control Standards for VOC 460.5413-Testing and Procedures §60.5390(g)-Notification,Reporting and Recordkeeping Requirements 560.5416(c)-Cover and Closed Vent System Monitoring Requirements §60.5417-Control Device Monitoring Requirements [Note:If a storage vessel is previously determined to be subject to NSPS 0000 due to emissions above 6 tons per year VOC on the applicability determination date,it should remain subject to NSPS 0000 per 60.5365(e)]2[even if potential VOL emissions drop below 6 tons per year] 40 CFR,Part 60,Subpart 00000,Standards of Performance for Crude Oil and Natural Gas Facilities for which Censtructlan,Modification,or Reconstruction Commenced After September 18,2015 1. Was this condensate storage vessel constructed,reconstructed,or modified(see definitions 40 CFR,60.2)after September 18,2015? tae Go$o the next question 2. Does this condensate storage vessel meet the definition of"storage vessel"per 60.5430a? 5t0Y° i:'i Go to the next question 3. is this condensate storage vessel located at a facility in the crude oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? "t�fea" :':!'::a Go to the next question 4. Are potential VOC emissions'from the Individual storage vessel greater than or equal to 6 tans per year? }Q5 �..,�.I Go to the next question 5. Is the storage vessel subject to and controlled in accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HH? Vie It:•:Storage Tank is not subject NSPS 0000a I Storago'rant(is not subject to NSPS 00000 40 CFR,Part 63,Subpart MACT NH,011 and Gas Production Facilities 1. Is the tank located et a facility that is major'for HAPs? N? 1St age Tank is not subject MACT HH-There are no MACE HH requirements for tanks at area sources 2. Is the storage tank betted at an oil and natural gas production facility that meets either of the following criteria. NA........,, a.Afacility that processes,upgrades or stores hydrocarbon liquids'(63.760(a)l21);OR b.A facility that processes,upgrades or stores natural gas prior to the point at which natural gas enters the natural gas transmission and storage source category or is delivered toe final end user'(63.760(a)l3))? 3. Does the tank meet the definition of"storage vessel"'in 63.7617 4th 4. Does the tank meet the definition of"storage vessel with the potential for flash emissions''per 63.7617 NAAM 5. Is the tank subject to control requirements under 40 CFR Part 60,Subpart Kb or Subpart 00007 S:arage Tank is not subject Bra MACY OH Subpart A,General provisions per 463.764(a)Table 2 §63.766-Emissions Control Standards §63.773-Monitoring 463.774-Recordkeeping 463.775-Reporting RACY Review RACT review is required If Regulation 7 does not apply AND if the tank Is in the non-attainment area.If the tank meets both criteria,then review RATs requirements. Disclaimer • This document assists operators with determining applicability of certain requirements of the Clean Air Act,its implementing regulations,and Alr Quality Control Commission regulations.This document is • not a rule or regulation,and the analysis it contains may not apply toe particular situation based upon the individual facts end circumstances,This document does not change or substitute for any law, regulation,or any other legally binding requirement end is not legally enforceable.In the event of any conflict between the language of this document end the language of the Clean Air Acl,its implementing regulations,and and Air Quality Control Commission regulations,the language of the statute or regulation will control. The use of non-mandatory language such as"recommend,"'may,""should,"and"can,"is intended to describe APCD interpretations and recommendations.Mandatory terminology such as"must"and"required"are intended to describe controlling requirements under the terms of the Clean Air Act and Air Quality Control Commission regulations,but this document does not establish legally binding requirements in and of itself. Condensate Storage Tank(s)Emissions Inventory Section 01-Adminstative Information Facility AIRS ID: County Plant Point Section 02-Equipment Description Details Detailed Emissions Unit = If 3 11i ��,rr ttt;"_ „1Nf33 Two(27256.iXlRdotxat<>tlegralflsattrrootumd4is≥kCstb sse - 1 Em ss on Control D F Wsr�xB I mmlicipai 6 naemaLRoam DcooP ..- (f; £ I fl3;3--)) Description:ion. .x ulfBi Requested Overall VOC&HAP Control &arg.>₹The oedema'floating roof Is considered an integrated control device.Please sea Effloency R: ;q L p N Section 08-Technical Analysts Notes section for additional information. Section 03-Processing Rate Information for Emissions Estimates Primary Emissions-Storage Tank(s) Actual Condensate Throug hput-- II=Barrels(bbl)per year Acura'Condensate Throughput While Emrssions Controls Operating= ""1""""""5,0;:8 rtels(bbl).per year Requested Permit Limit Throughput= 6YpEQB6ffBarrels(bbl)per year Potential to Emit(PTE)Condensate Throughput — „„,Stj,�B,_g„6,fB Barrels(bbl)per year 5,270,000.00 Secondary Emissions-Combustion Device a'Thls facility does not utilize a combustion device to control-emissions. ' Heat content of waste gas= 4,4041434 - ---£ Btu/sd R404:-;' `'; � Volume of waste gas emhted per BBL of liquids l4 rN , produced= ��-� jxf/bbl il. Actual heat cadent q(waste gas routed to c0mhus[ipn device= 0 MMBTU per year Request'malcontent of waste gas routed to combustion device= 0 MMBTU per year Potential to Emh{PTEM heat content of waste gas routed to combustion device= 0 MMBTU per yew Section 04-Emissions Factors&Methodologies Will this storage tank emit flash emtsslons7 x,,,,„.1=;g,_! • EEYaM1ng H"[FIrd55[d( f}QrMB,NneilwEOPeF T;sns Total tank losses from an external floating roof during normal operation Included rim seal losses(L js withdrawal losses(Lao),and deck fitting losses(b,).The operator calculated these emissions using Tank05P_d simulation software.This software utilizes equations from AP-42 to calculate the external floating roof emissions during normal operations.The emissions resulting from the simulation areas fallow: Parameters Value Units Source Annual Throughput(O) rsioa96ap,iil:11 bb'/year ."'' ::r_9p_aoafurProWiedVat e{ttisau%hputfoean„eta k} Shell Clingege FaG ' `" i4 ! ISI s.� bbl/10o0fta -S,;". �R,iu",,, Ar'szl#aija.36 i"- Average Organic Liquid 93 j13431 Denzr ry(w) l sx :���: ro/ganpn aperamrPw dedvawe;Air.sea nodaz ,ia . Number of FnedR ofD .;� f draofF,oredorn LRw;[i g!nwRfYt1 4([hhf4 PPM�ad3.ggfizoof tank Support Columns(Noe) i9 '�'i4 pij dEErfdjl d0e 0W27100 Effective Column Dlamter iifpd9 IKi3di f1gfo14 OJi&.6urd m[et prpemW ,3 rfcWuma (Fr.) t 3 ft �a i:')'ll)''Oumt awnd aih mrnknown Zero Wind speed rim seal ��Ij 3 y Ions factor KW offit3M lb-coal/fly kt�41"'Y6�fe'11.3(A1 hamalsho=primary with Rimmnunt d duty; _ Wind speed dependent dm Y;j .E 8 " seal loss tsar (Kss) ff 'D Z' Ib-m01e/ftyear AP-4274000714(bteGfYBgial shoe Wing's,with Rim-mou d rigW,,F3=; r- 5ea'Rel.0wi^dspeetl 1 �:Ap-b2 TabPE?i83.4 h 1 I ho pr arywth Riin•mou d d igT"- exPDnentfnl Average ambient d t, Z1-9 Ie "" "07 spead(v) .... ................;: ph '',. „£„,,'AP-'42-3aWe Tank Diameter(DI ;Dour '” ft Opewt0rprorid d ejj " Molecular weight)%) 9361 lb/lb-mole i 7' AP'42Chapte 7Rqu;tiNn3; . Daly so AmbientT p 34 y/� .. '...... (Trod �ragagr 4. R AY 42?ableT1J = _- Darcy Mm Ambient Temp ; „495k7 I 'R ., APA2T INgY}`L L i :. iii it k (T.) Daily Average Ambient 509.9784932 R 3/..i .AP42L Temp(T..J hapEYr?lEg0aW(RRdT, Tank Pa nt5ol " .� - "'.- Absorptna(gl QR7' APdEbIa716 Daly Total Solar Ins - AP42I"b7e7 x7 f '�" "' 5$7Q.6602T,,, Btu/ftsday Factor ft) Liquid Bulk Temp(Te) S09.99B4032 R "II IAP-42fh al'er3:7 Fq{tdtfOc126,`7'�� Da1YAvemgnUquid ;.,' 9 :;" ,'. 512.0990899 R C .:AP-42hapt ],EquaGa 2S'_" Surface Temp(T,,J Atmospheric Press Ira) 12.12 ogle g Atm05ghedtpre:SrlttfMUehVErtO'..: Reid Vapor Pressure psis tlotppnrided,"„ l,j, r,"..":.,is Vapor Pressure Ca ht '. 1 .... .....;. A20"J:j353> ).1�'tryTlUedCR e&s3Mq dCIYPSt'd0afe¢rl≤jilTa isY5[M8637F Vapor Pressure Cons'ht 6 uY62938Y II, R '.'Fm 1 aid gt'aslon aETVPatlQdegTilRervd(SviaA5TMLM3Tt -<,. Vapor pressure at daily average liquid wrface 5-322219111 psia F „i3;.AF422hapE aFrtin 1,24 temperature(P,J /l( .�3�3rka Vapor Pressure funo'ion 0.143566445 \\\ 1 ZV. 11 3i.ihi*i ail Efl3Yiflf233 Pr "``_s ..oso00e4utl o'y5't lfisra otk Product Factor(Kg) G3F • Rinse Losses(L,) 2420.62787 lbe/y �q hyrp/'nang AF32_Chapt 7Equtwn22 Withdrawal Losses(Lyn) 5830,801546 hs/Year7 k:hsPd stag AF-02:Ckapt.t.EquaiwnZ4 y r,:, Deck fitting loss (L) 285'v34R5g4' lbs/yaar " '7ankii300,dasmg0➢-02£hapten7Equaiion 25 pt- _ Isi;yp.Total Losses lb/year - "' 'AP-42 EGa et₹.Egdation;2-i Total NumberaFV els "2 Standing Losses: 42..018454 lb/yr Tom'Emissions: Pollutant weight% Ihs/year s�ource vat `. u �. 20209.64 NOIRES, Benzene w 469863648 55=3",AjICE; Toluene O£{a083i' 122.2202. 5,55/i$ilro''-l. Ethylbenzene 4 $Yj'nBd7 33,2500988 901460E Xylenes tgQ05� I� 1030 16 tita558hignce, n-Hexane ='1Y,(f}Q ' 32335424 A4�5�3780@P - i 2,2,4TMP UQ06i8 S 955 52 Mss§E I ;N'-,;; 17 of 25 . K:\PA\2014\14WE1593.CP4xlsm Condensate Storage Tank(s)Emissions Inventory :. .....;i Prdress02,Rao€3amNrigEmfxRmi:akufallonsiorEsterml;flneGrzg KaoEviRlfFuli{S96�d 41eeL..s:..�n "�f Paremeters Value Units source True Vapor Pressure(0) 5.]10542913 Pie "AR42Ch pt Equattoie LT4(basedan"da4Srvage 4bienEtemperatuie See ba[e3{r£quatrron43in*P-42Chaptorl( 7 Average Tempem[ure of vaR.0 7 )4 sit ii: vapor and liquid below 50992 R cj�alaer7 +�pna�7`� r"4--,-.6 floating roof(T=T„,) 33 '" Ideal Gas Cons[ qq 5A4Y21 Constant 3 (1, (PIYt)/ m I RI(ib �?,; Number of days tank stands idle with floating .I0; days Engineer Ettbnat9 roof 2r1ded( ) ia..;46'.y.)11; is:: 777 Stock Vapor Molecular8,olecular ''" [�Pikk(P a4Aalptoo/Lgcdtieli'1-121FSUnw4042/2anxt5P_0 _S36�" Ib/ltrmol Saturation Factor(5) - Effective Height f k -,:aii k One eta es.:20104 0 212 2 Roof Leg Height(low leg r5.- 3u,,F!, k r;Peratorastimatndvalue. setting) "":C; M-447 Height of vapor space 3163 ft AP-42 Chapter Euationi is rental-tape underfloating roof(hi q (notaa geso Hy4xi) Tank Olameter(D) ::194:"" k = - -Operator pmvitledvalue _ - Dally maximum ambient i 3 S2454:AI R AP-42 Table FtZ Aterag I £ D ,CD temperaturen.� ti 11 >3(II Oa4min mum bi0O (2 .. '49s as ', R .; APyEeT5til 7,3 J3z,A ia>yepaWa33fgNbeNUeb c9 ,�',", Daily Totallnsolaton Btu/k'•day A➢42Tabi 137 Aveage21ayref D el€Q Tank Pamtsol 5 '. sv�= .,4pi4YFa002416=Wh3ep t od - ALmosPhercpress re(P,I ;.i 9(2g A fi A p (r s �:..3L4 .lea Reid Vapor Pressure ::.557:_' Pala Vapor pressure function i (Pal 0.136400611 \ - -A➢d26hapiet`7):gllaYtl02-3" Volume of Vapor Space (V.l 93414.02563 k �+ � �lii�lP-S2CH$t.7Equd�01113 �• VemedF apo`sat tw o s3s 96soa 31. A➢-a2cliatn Jl ql z6 sgd q x ? Factor(K) Vapor PressureC rut [B \\ £imn3inaa Regresron plxuRa[SOd gT intervals via ASfMD63Jl for cmdeOil smns(e) - - Vapor Pressure C nst t V /,: a\�a \ :Fm linear Rerrsson of TVP at 10 deg EntenralsvraASTAI 04327 for Crude 0l Stocks(A) %` \ Daly Ambient l-12 Temperature Range(4TJ 28'1 'R APa2 LM1ecYer>E4uatton Daily VaporTemperature 2769568 .R AP-42Chay.2424404204-0 Range(8;1 H4uid Bulk Temp(T.) 509.92 '5 AP 42 Chapter 7 Equation l-22 Oaily Average Liquid 50.037074 •R ,3 3IIIR3iI yLTY4 lip-42Chap[ 7£A dfI011A 26 „) r Surface Temp(T,) C a333ii77 iU}3i;v.'�.v,.ul.»hau Ib» I3 i39 y; :r d Vapor Pressure at Dairy Max Liquid Surface 6.531844071_ psla - ➢-§ECf(2yf4Yglld[1btl 12§„- Tempereture(PJ ..• Vapor Pressure at Dairy Min Liquid Surface 3.959180237 pal ii j1 4 p APA2C Y`T :x, 3 Temperature(1,,,,) 33 ��„'Y r � d3W ,3h ...A Daily Vapor Pressure :...._..._r...................._.. 3.57266384 Psia AP-02: Chapt r'Etryatton Range(AP,) Vapor Space Expansion 02346/109 AP-42Cfrapter7Eg4at 120 Factor(K ... - ... • Event 5tandngLosses 1 >a ri AP-42 M1avter]₹44/44))421 ,: 591.7682502 Ih 6 w/put Wind 04000Filling Loses w/000 2500*01J36 Ihz 4942 Chapter Equation 2-25 Wind Correction Fo4or(020( 0.936393934 AP-42 Chapter ,44atm52-SV u— Event Standing Losses(Lou) 8082553769 Ib/roof lent anding AP-42 Chapter 7 E4uatron 2,14 Event Filling Lose(l( 2632.944651 lb/roof lnndin6 AP-42 Challcnl 2/42tro02.27 Total Landing Los lb/roof landing A ;44.4171:,41•031 " iii C 1 3441.200020 Paz chapter 7-EquaNva ��a A d']] Emissions II,r 4+47 event r•ye Total Number of Roof rim teedineevents ��}HDa .. Total Emissions: Pollutant W 1phr YG Ifa/Y 00 Voc .2 ,. 6882400056 AP-4₹ Benzene f tti- 05.30716813 "AtfasH i av' Toluene I4 6 0.0 4356559236 !..!..,,,,014-00:M. trsylbenzene '�j 6.t16 M1 31 a9 xylenes �44 t 253002A025 :t4ai p„ n-Hexane .13r1136✓ yp, 110.1184003 TAazsq l 2,2,4-TMP sealika, 18 of25 K:\PA\2014\14WE1593.CP4xlsm Condensate Storage Tank(s)Emissions Inventory TenkE5P dcalculntes ihemmllosses ham the FlaeNng roof fankdudng cleening aperetlans.The equetiom goveming the emissions during this pmraas are established in API Technical Reference 2568.The operstorgrouped this process into Rue stages Which Will be described aM mlculetsdbelaw: - Peremeters value Un14 Spume St;e l:Standing Idle Tant CPA P-a₹ a'gvaedh2`s l Wormed m l�: ' ugad losses-Full liquid heel of 1616 lbs i «use on tr'fd,hewn ,aed1 ay, Stage 2:Initial Vapor Purge Fulllquid heel of 516]n lbs is nF f5P dos g.iP 32 Ci,pter]Equa[on007 Stage 3:Daily Vapor Purge-Pull squid Heal of 155019 Ibs nr 5P d 4srg AP TP 2568 cquatU 10(Max Lmt) cmde an - . x3zince3 days of vapor pange(3 days of arson 3) - Stage 3 Part 1:Crude Oil Sludge Removal-Full 29:3.2 lbs t. Ttl TN 269 rot a[o r?9 liquid heel with cont forced vendl000n x 3 since 3 days of forcedventilation with sludge removal Stage a:Daily Vapor Purge(Dlesell-Full liquid 21 Ibs ank.tSP 15,5?P a2.Cb Ite,cqr tun_�b Heel .e2 since 3 dar/s a(vapor purge aRertliluen[wash Stage 4:Sludge Removal of Diesel withcont 575.7 lbs xnt SP sin300 TN t,on c9. forced vendledan , xE since 3 days of fomadvenalauon with diNent wash Stage 5:Refilling 13346 Ibs is nN .:00042'l In 4snnre: Total Eosxs 21155.70 Ib/cleaning _ - Total Number ofTank Cleaning Event ,%!,;..1 robs Emissions: Pollutant Weight% Ibs/y®r Source VOC /0'A 313 R Benzene 2t6y5.3i? 63.001226 Mss O.yal TONene ¢00633 , 171895581 Masse I pct 1.8 EthyWereene 'tOe1wt 45950019 Arlasotralaniehng zylenes 6.0054 am Ma9g§lanes- n-H 0550 1 o.OI/./ .,�: aaauslz Mass I Rq M £k'i f O05 2,2,9-TP ahT 167822226 MtSEllalanc@'ti,... ...m% �/�/..e'�,.'/„+ Y'/',%i Pracessax:azmnattlmirig�racf.�tifssb'e""KFl ri`Rg"' :'"'grrEB..I (pn ss,°?'X' �. CondensateSmregeTanks Control Device Uncontrolled EF. Controlled Ef. Uncontrolled EF. Uncontrolled pollutant (lbs/bbl (lbs/bbl (Ibs/MMBtu Er.Ohs/bbl Emlsslom Factw5aume CRatlan Condensate Condensate waste heat Condensate Throng Po Throughput) combusted) Throughput) \ 0.0000 ., � o 3257E a4 - . . .• IIIIIIIIIIIIE • \ Illllllllllll�r� � , Process Hoof Lemke Emission Caic0lalonS'reeEetemelb WtthloatogDaof P,ll)7 c0dryeeF...0 - Control Device Uncontrolled E.F. Uncontrolled Pollutant Uncontrolled E.F. Controlled EF. (Ibs/MMatu E.F.(Ibs/hbl Emisslans Factor5oume Cltatlan (lbs/roof landing (Ibs/roof landing waste heat Condensate vent) even t) combusted) Throughput) I 1 ia\. 41'i 0 000 ®-� a\, 00000VANINENZY: 3 a.00aa .s mmetre21783 ® ti� ,{y�y��• - �l 5:7 T 6®�.\�\\\ ��```\`�iiii.. xaw.m�_ 4 • IIIIIIIIIIIIIIIIIIRI® ]550 ®' \� a\�.\\a�\ ., •-vita 5r..- ' Process03:Tcnk Cleerang Control Dance •••• Uncontrolled E.F. Uncontrolled Pollen. Uncontrolled EF. Controlled EF. (Ibs/MMBtu EF.(Ibs/bd Emlsslam FaRor5ourte Citation (Ibs/cleening 06s/cleaning waste heat Condensate ant)M�� ent) combusted) Thmughputl ore. .u!mizmu� \� �o.\\\ � 0.0000 9 h onirmismummorEommelma‘m:m::::‘,:zals•e IIIIIIIIIII_ mamm`�,,�.��.Z�\�\�\\\�''...\\„ P£��\�\���'.�� WI....Bk{ �� �ca'a��a\\\\'\\\�."\\\�.\\\\ :AFfTit25R8{ "0t?Sbe{53 19 of 25 iC\PA\EOM\14WE2593.CP4xbm Condensate Storage Tank(s)Emissions Inventory Section OS Em's I ventory _ Prottss art.Me7A08HNg1t9ePerdwonsilW Ne, iiitri,k6.,&",,,, ; '"R Potential to Emit Requested Permit Units Actual Emissions Criteria Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled Mons/year) (tons/year) (tons/year) (tons/year) (tons/year) PM10 0.0 0.0 0.0 - 0M2.5 0.0 0.0 OD Noe 0.0 0.0 0.0 _.. VOC 10105 10.105 10.105 CO 0.0 09 OD PotentialtoEmi[ Requested Permit Limits - - Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled __ Uncontrolled Controlled (tons/year) (tons/Year) (tons/yeer) -_-- - (Ibs/Year) (lbs/Year) Benzene 0.0 0.0 OD 469 469 Toluene 0.1 0.1 01 1279 127.9 Ethylbenzene 0.0 0.0 09 359 33.0 Xylene 0.1 0.3 0.1 1031 103.1 n-Hexane '0.2 02 02 323.4 323.4 224 TMP 0.1 0.1 0.1 124.9 124.9 'Prbre5s02:Roof Landing Emlsslon CatwlaUonsrcr"isternad floating Roof with FuloligmdHeel: Potential to Emit Requested Perini[Umns - --= Critera Pollutarrts Uncontrolled Uncomroged Controlled (tons/Year) (tons/year) Rons/yeer) '- PM10 0.0 0.0 0.0 PML5 0.0 Om 0.0 ....NM 0.0 0.0 0.0 0.0 VOC 3.441 3.441 3.441 CO 0.0 0.0 0.0 .-. Potential to Emlf Requested Permit Limits -::. _ Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled _-. Uncontrolled Controlled (tons/year) (tons/year) (tons/year) (lbs/year) (lbs/year) Benzene 0.0 0.0 0.0 16.0 16.0 Toluene 0.0 0.0 0.0 43.6 M. Ethylbenlene 0.0 0.0 0.0 _ _ 115 11.5 Xylene 0.0 0.0 0.0 35.1 351 n-Hexane 0.10.1 0.1 1101 110.1 224 TMP 0.0 0.0 0.0 - 425 42.5 , Pro«ss(mtTsrdts3emikrgi Potential to Emit Requested Permit Limits Criteria Pollutants Uncontrolled Uncontrolled Controlled )Iona/year) (tons/year) (tons/year) PM10 0.0 0.0 0.0 PM2S 0.0 0.0 0.0 NOx O.o 0.0 0.0 _ VOC 13578 13528 13.578 - CO 0.0 0.0 0.0 Potential to Emit Requested Permit Amos - Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled ._.. -- Uncontrolled Controlled (eons/year) (tons/ear) (tons/year) .. (Ibs/year) (lbs/year) 1 Benzene 0.0 0.0 0.0 .. 63.0 639' Toluene 0.1 17.9 1719 Etisyibenzene 0.0 0.0 0.0 ... 45.4 45.4 Xylene 0.1 0.1 0.1 _._ _.., 1385 138.5 n-Hexane 0.2 02 - .4.5 434.5 224 TMP 0.1 0.1 0.1 1673 167.8 Total EmsstonsUmnhrlemai Reaucro Root Took Potential to Emit Requested Permit Umcs Criteria Pollutants Uncontrolled Uncontrolled Controlled -.-_: (tons/year) (tons/year) )eons/yearl PM10 0.0 0.0 0.0 PM2S 0.0 0.0 0.0 NOX 0.0 0.0 0.0 VOC 27.124 27324 27.114 .... .... CO 0.0 0.0 D.0 Potential to Emk Requested Permit Limns Requested Emissions Hazardous Air Pollutants Uncontrolled Uncontrolled Controlled Uncontrolled Controlled (tons/year) (tom/ymr) (tons/year) - , (lbs/Year) (lbs/year) Benzene 0.1 0.1 0.1 ..: 125.9 125.9 Toluene 0.2 0.2 .._ 343.4 343.4 Ethylbenz0ne 0.0 0.0 0.0 '- 50.8 90.6 Xylene 0.1 0.1 0.1 :-- 276.7 276.2 n-Hexane 0.4 0.4 0.4 -- --- 8689 808.0 224 TMP 02 0.2 0.2 3353 3353 Section 06-Regulatory Summary Analysts Regulation 3,Parts 0.B Source requires a penult Regulation 7,Section VI Storage tank Is subject to Regulation 7,Section IA Regulation 7,Section XII.C,0,E,A Storage Tank Is not subject to Regulation 7,Section XII Regulation 7,Section X01.0,C ' Storage Tank is not subject to Regulation 7,Section Xll.G Regulation 7,Section XVII.0,C1,0.3 Storage Tank is not subject to Regulation',Section XVII Regulation 7,Section XVII.C.2 Storage Tank is not subject to Regulation 7.Section XVII.C2 Regulation 6,Part A,MPS Subpart Kb Storage tank Is subject to NSPS Kb.including but not limited to,the Regulation 6,Part A.N5P5 Subpart 0000 Storage Tank is not subject 50 N5P50000 IMPS Subpart 0000a Storage Tank Is not suble0tm N5P50000a Regulation B,Part E,MACTSubpart HN Storage Tank is not subject to MACE HH (See regulatory applicability worksheet for detailed analysts) 20 of25 K\PA\2014\14WE1593.CP4alsm Condensate Storage Tank(s)Emissions Inventory Section 07-Initial and Periodic Sampling and Testing Requirements Ooes the company use the state default emissions factors to estimate emissions? If yes,are the uncontrolled acual or requested emissions estimated to be greater than or equal to e0 tons VOC per year? LI N/A-Operator developed site specific emission factors If yes,the permit will contain an"Initial Compliance'testing requirement to develop a site specific emissions factor based on guldelines in PS Memo 0S-01. Does the company use a site specific emus cans fa Corte estimate emmions? If yes and if there are flash emssfons,are the emissions factors based ono pressurized liquid sample down at the fealty being permitted?Tho sample should be considered representative whic h generally means sae-specific and collected within one year of the application received date.However,rfthe facility has not been modified leg.,no new wells brought on-Ilnel,then it maybe appropriate to use an oldershespeciflc sample. If no,the permit will contain an'Initial Compliance"testing requirement to develop a site specifk evasions factor based on guidelines in PS Memo 05-01. • Does the company request a control device eRlcienry greaterthan 95%for a flare or combustion device? N/A-Acombustion device Is not used to control emissions. If yes,the permit will contain and Mal compliance test condition to demonstrate the dmtroction efficiency of the combustion device based on inlet and outlet concentration sampling Section ea-Technical Analysis Notes `This fa dray doe4 notrtilee-ammbustorta control emissions from thestoragevesseh.Ass sock there are no secouderycombusbarssnaswnsessociatecewrththissoume. Rhin facilicy does.not meetthedefi rtan of natural gascompressorstation"or'natural processing.ptant"per Rego Ilion l,5 ecdan%eandXVIT.t addition,accordingtoP5 Memo 05-0l custody. transfer occur et-the exploration and production site Since thirfacilityrece vas condensate viatdnkeF trucks andpipeln84 from.nearby wen Production fecihje{,itwooldbR located at a punt a(ter custody transfer,Asia result,thisfacllitywouldrwt b ns rder-ad an expioratioaand poducton site,Doe to this,9egulat On 7 S eotlooX.and RVgde notapplytodl's facility.Since the facility does not all within an industry segment regulated bySeetfonsXll orXVlitiirsfacilouissubjed-to the mum,hements In Sodium VI for-"StorsgeandTransf Pellnleunrocmcrd itlseesul is consistent with the Ocrecoi - • determination for other similar fealties_ - - ',since these store gevesselsaesubl tt tonegclarion:l Sedron VI alld NSPS Kb,PACT 0 satlsfiedthtough the reoolrementlotrtVize.externel floe Ling 'The control device for these rtorag salt a an extsna lfleatmgr001.Th eo external floatingrfis integn @ tedinto the desi.aofeach storage vessel.5nce the extern.floatmgroofis not an add-on control,there lsnot an accurate means for calculating uncontrolled:esnoslo r this reason,enlythecaotrnlledomission s-arc considemdwth's-analyss `The weight%values used.determwetheyAP emissionsfmotthissourceare based on an extended Nod enafrsft ofvnpreecu¢edNlobramcrude(obtained 05/18/20161.The sample used is - representative of the hydrocarbon liquid chatwd:bosteredetthisfaohby.It should be notedthatusingtheweight%valoes.fromthe lioeidsamplos a conservative estimate of emissions,. •Smcethe operator prourdeesttespedf eroa5ianfadors based orta.repraenn1vestabtohydrorzrbon liguidvulysls and.thesterageveste&atthistatifitycontain rtablliaed on(no flesh) deteeninalan 14101ltet.would not be required for this source: • `The mole cuter weight used in the calculations-safwhtedbyrankc5P usmgeglatibn 1-22 lit AP42 Chapter].The molemdar weight vans slightly basedmrtempereturesmce the individual constituent's vapor pressure changes web temperature. `Theoperatorindlcated in the applicatianthattankdeaniegswillaaarapproximately emyten years.Asaresuk the promsslfmlaf onetank cleaning per year be reasonable limit within the pennitand's at least conservative with respedtg annuakemissions. • •Theperm0 COMairsthese processeswhkh indudenumatoperaaion,rooflandingsand tank cleamngs.These processes were e the permitbecausethe emissions profile doling each operation is differenteyseparating theprocesses,thepermm dearfyident0tmtheenussians thatwilb occur during each different opentingsce rro_Tbissteumaesimplifiesthemmpliancedemonstrationforihe operatorsnceItprovdesaseparatesetofem'xslc tuytorsfhat may beusadduring each opotaningsrenarb. '0000 operator waspravidedwith a draft permit'preview priortoissuance,The Tape rater reeewed the draft and providedcommmas.The comment provided by tlreapplicant a re summoned as follows: Comment at The plantdesfgn bas not yet bean'fIna lired.whiieialigras will not Install tanks largerthan 250,0D0ikbl,lt may felt Ostmheiyessetv.Tanga.is regOesting the permit include condrrons necessary to a lltwforflexibiityto intallsrnaliertanks, nom ment2;The source does not egfeethat complianceshell bedemonstratedonarolling l2.month basis.Tallgrassandertands That Synthetic min urc shall usemihngl2-month compliance periods but would like to see gulpancewpp0rene the decision touncudethemfor this true minor far iloop gesoonseSt Thls 10 aaemente since kprovideslheoperatnrwlththeftedbility,xf needed,.onyhe final design of thefaciltty a provWltglicocvaas iona"warsmkase'oorrdsloroosrcooemission atl nscenario for the - largest possibletankn Asa rnult,T.w termin as con&tiohw0ud be added tcobe permit requiring the Operator to modify.theperrrRrin the event theflrzaistorage vets.design deooted from the original appl tahon that was oSedinthis prelunmery'analysis aadthe basis tor permitted a mlosions,Condition.2 was added as a result.6ystnuCturfngthe perrplvthisway,the operator will sill be able to begin construction If a smallertank than was on or llypermeted makes it into the.TnaI design while ensuring the permit w modified appropriately in the event a smallertank is Installed.The condition also enw rm the opereterwoold ent be required tomod0yfhepermillthe final design of the fa ditty matchawith the original'apPlkaeion-Fhialiy,d should be noted that rfsmaller tanks are InslaII d,.ih0 emssposmlllkdy be lower duet0imvertlrooghputraab ies,The opemto rwasprmnded with a draft permRcontelningthe updatesdt4ssedabove. flesoonse22:lui00000 iyagreed to remove madly gt0110 and roiling l2-moth emission calculations based onthefactt0at the facility is tfineminmf,Pleao 0110 melilD/10118. had some concern that if smallertank dimensionsorlower numberofvessak were Installed that emissions would maeasebmedon0¢reeseduvnover,.per vessel However,lre-ran theTANK5 simulation for multiple sce to iindthet attherequl shrnugflputrete,emission decrease with storage vessel edcomeiassumingdlameterana0 of fittings decrease aswell)andemisslanstlecrease as umberof?stalled vessels decease rberef re,ttse emission estimate presented here should provdearverst-case emrssioastenarlotesed onthe infomdtion',melded by the applicant Section 09-Inventory SCC Coding and Emissions Factors Uncontrolled Emissions AIRS Paint. Prot . SCCCod Pollutant Factor Control% 0010: 005 01 PM30 0.000E+00 0 b/1,000 gallons contlensatethroughprt ., xuTnatFlP?fl(t9taf .El.,.,,YT. y! PM2.5 0.000E+00 0 b/1,000 gallons condensate throughput 0100 0.000E+00 0 6/1,000 gallons condensate throughput VOC 2.082E-02 0 6/1,000 gallons condensate throughput CO 0.000E+00 0 6/1,000 gallons condensetethroughput 'Benzene 4.829E-05 0 b/3,000 gallons condensatethroughput Toluene 1318E-04 0 b/1,000 gallons condensate throughput Ethylbenzege 3.476E-00 0 b/1,000 gallons condensate throughput Xylene 1.062E-04 0 6/1,000 gallons condensate throughput n-Heave 3331E-04 0 6/1,000 gallons condensatethroughput 224 TMP 1.286E-04 0 6/1,000 gallons condensate throughput emise-Emission factors for process 01,02 and OS have been combined here solely for Inventory purposes-When calculating actual emissions,the operator will calculate emissions for process 01,02,and 03 Independently using separate siion factors as described In the preliminary analysis above. - 210025 00\PA\2014\14WEi593.cP4xlsm • Condensate Tank Regulatory Analysis Worksheet • Colorado Regulation 3 Parts A and B-APES and Permit Requirements ATTAINMENT-This source Is located in the ozone non-attainment area.Since this source does not emit CO,all questions in this section are listed as N/A 1. Are uncontrolled actual emissions from any criteria pollutants from this individual source greater than 2 TPY(Regulation 3,Part A,Section II.D.1.a)? tRAM 2. Is the constrdction date(servicedate)prior to 12/30/2002 and not modified after 12/31/2002(See P5 Memo 05-01 Definitions 1.12 and1.14 and Section 2 for additional guidance on grandfather applicability)? 3. Are total facility uncontrolled VOC emissions greater than 5 TPY,NOx greater than 10 TPY or CO emissions greater than 1O TPY(Regulation 3,Part B,Section 11.0.3)? Nut enough information NON ATTAINMENT 1. Are uncontrolled emissions from any criteria pollutants frpm this individual source greater than 1 TPY(Regulation 3,Part A,Section MIA)? WCFi'g Source Requires an APEN.Go to the next question 2, is the construction date(service date)prior to 12/30/2002 and not modified after 12/31/2002(See PS Memo 05-01 Definitions 1.12 and1.14 and Section 2 for additional guidance on grandfather applicability)? Np 1P Go to next question 3. Are total facility uncontrolled VOC emissions from the greater than 2 TPY,NOx greater than 5 TPV or CO emissions greater than 5 TPY(Regulation 3,Part 0,Section 11.0.2)? - Yasis% Source Requires a permit 'Source requires a permit Colorado Regulation 7,Section Vi • 1. Does this storage tank store petroleum liquid as defined by Regulation 7 Section 01.A.2.g? ':%'I?0 to the t question 2. Does this storage tank meet any of the exemptions listed in Regulation 7 Section 01.8.17 Md .Go to the t question 3. Does the tank have a storage capacity greater than 40,000 gallons(952 barrels)? /05.emp Source Is subject to Regulation 7 Section VI.B.2 b,Go to the next question 4. Does the storage tank have a fixed roof? N0 Storage Tank is not subject to Regulation 7,Section VI.B 2.a. S. Is the fixed roof tank used for the storage of petroleum liquids which have a true vapor pressure between 0.65 psia and 110 psia at 20'C(6g'F)? NA,ems`"- 6. Is the fixed roof tank equipped with an internal floating roof? NA' •, Storage tank is subject to Regn'.oliov 7,Section VI.B.2.a&b Storage Tank Is nor.subject to Regulation 7,Section Vi.a.2.a.fi) Storage Tank Is nut subject to Regulation 7,Suction 7. Is the tank equipped with an external floating roof AND is larger than 952bbi AND stores petroleum liquid AND is located in ozone nonattainment area? /o/ 'Source is subject to Regulation 7 Section 01.0.2.c;Go to the next question B. Does the tank meet any of the exemptions of Section Vl.B.2.clll(B)(1)7 Nq :Storage Tank is subject to Regulation 7,Section Vl.B.2c. 9. Does the tank meet any of the exemptions of Section Vl.B.2.0.(1)101(2)? No Storage Tank is subject to Regulation 7,Section Vl82c;Go to the next question 10,Does the tank store petroleum liquds with true vapor pressure(as stored)above 1.3 psia? Yes Source is subject to Reg 7,Sec VI.B.2.c.f1g(4),Go to next question (Storage tank Is subject to 000010tion 7,Section 01,1.2.0 • 11.Does the storage tank have a storage capacity less than 40,000 gallons(952 barrels)? N0. Source is not subject to Reg 7,Sec VI.B.3. 12.Does the storage tank store liquids with a true vapor pressure between 1.5 psia and 11.0 psia et 20'C? NAj:�:✓'d 13.Is the storage tank at a facility that receives and stores petroleum addressed by Regulation 7 Sections Vl.C.2 or VLC.3? Niel IStorage Tank is not subject to Regulation 7,Section 01.0.3 Storage tank is subject to Regulation 7,Section VI Colorado Regulation 7,Section XI) 1. Is this storage tank located in theehr ozone control area or any ozone non-attainment area or attainment/maintenance area? Y4is/Iv'":1 Go to the next question 2. Is this storage tank located at an oil and gas exploration and production operagon',natural gas compressor station or natural gas drip station? Storage Tank Is not subject to Regulation 7,Section XII 3. Is this storage tank located upstream of a natural gas processing plant? 'NA d,a°)P 'Storage Tank Is not subject to Regulation 7,Section XII Section%II.C.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section Xll.C.2—Emission Estimation Procedures • Section XII.D—Emisslons Control Requirements Section%II.E—Monitoring Section%ILF—Recordkeeping and Reporting Colorado Regulation 7,Section 011.0 • 1. Is this storage tank located in the 8.hr ozone control area or any ozone non attainment area or attainment/maintenance area? ilarteM Go to the next question 2. Is this storage tank located at a natural gas processing plant? NOW. Storage Tank is not subject to Regulation 7,Section X11.6 3. Does this storage tank exhibit"Flash"(e.g.storing non-stabilized liquids)emissions and have uncontrolled actual emissions greater than or equal to 2 tons per year VOC? - Nm Storage Tank is not subject to Regulation 1,Settinn 011.E • Section%11.0.2-Emissions Control Requirements Section XII.C.1—General Requirements for Air Pollution Control Equipment—Prevention of Leakage Section XII.C.2—Emission Estimation Procedures Colorado Regulation 7,Section XVII 1, is this tank located at a transmission/storage facility? NEB a Go to next question 2. Is this condensate storage tank'located at an oil and gas exploration and production operation,well production facility',natural gas compressor station'or natural gas processing plant? NMI Storage Tank is not subject to Regulation 7,Section XVII 3. Is this condensate storage tank a fixed roof storage tank? 4. Are uncontrolled actual emissions of this storage tank equal to or greater than 6 tons per year VOC? 'Storage Tank Is not subject to Regulation 7,Section X00 Section 0011.0—General Provisions for Air Pollution Control Equipment and Prevention of Emissions Section%VII.C.1-Emissions Control and Monitoring Provisions Section XVII.C.3-Recordkeeping Requirements 5, Does the condensate storage tank contain only"stabilized"liquids? NIA.. =:Storage Tank is not subject to Regulation 7,Section XVII.C.2 'Storage'tank is not subject to Regulation 7,Section XVII.C.2 Seaton XVII.C.2-Capture and Monitoring for Storage Tanks fitted with Air Pollution Control Equipment • • 40 CFR,Part 60,Subpart Kb,Standards of Performance for Volatile Organic Liquid Storage Vessels 1. Is the individual storage vessel capacity greater than or equal to 75 cubic meters lm)(^472 BBLs]? YCs .(•.'1 Go to the next question 2. Does the storage vessel meet the following exemption in 60.111b(d)(4)? :hl-O'h.43 Go to the next question e.Does the vessel has a design capacity less than or equal to 1,589.874 m'(-10,000 BBL]used for petroleum'or condensate stored,processed,or treated prior to custody transfer'as defined in 60.1116? 3. Was this condensate storage tank constructed,reconstructed,or modified(see definitions 40 CFR,60.2)after July 23,1984? Y95 Y Go to the next question 4. Does the tank meet the definition of"storage vessel"'in 60.1116? a'es Go to the next question 5. Does the storage vessel store a"volatile organic liquid(VOL)"s as defined in 60.11167 Go to the next question 6. Does the storage vessel meet any one of the following additional exemptions: 14-0:11.106i Source is subject to NSPS Kb a Is the storage vessel a pressure vessel designed to operate in excess of 204.9 kPa(-29.7rpsq and without emissions to the atmosphere(60.110b(d)(2))?;or Na b.The design capacity is greater than or equal to 151 ms]'950 BBL]and stores a liquid with a maximum true vapor pressure°less than 3.5 kPa(60.110b(b))?;or c.The design capacity is greater than or equal to 75 Ms('472 BBL]but less than 151 m°("'900 BBL]and stores a liquid with a maximum true vapor pressure'less than 15.0 kPa]60.110b(b))? Nq„..,,,,...... Storage tank is subject to NSPS Kb,Including but not limited to.the following nrovisinns Subpart A,General Provisions 660.1126-Emissions Control Standards for VIC §60.113b-Testing and Procedures 660.1156-Reporting and Recordkeeping Requirements §60.1166-Monitoring of Operations 40 CFR,Part 60.Subpart 0000.Standards of Performance for Crude Oil and Natural Gas Production,Transmission and Distribution 1. 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? UMW'I Storage Tank Is not subject NSPS 0000-This tank was constructed after the applicability date. 2. Does this condensate storage vessel meet the definition of"storage vector'per 60.5430? .,jell; 3. Is this condensate stooge vessel located atafacility in the onshore oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? 4. Are potential VOC emissions'from the Individual storage vessel greater than or equal to 6 tons per year? 5. Is the storage vessel subject to and controlled in accordance with requirements for storage vessels in 40 CFR Part 50 Subpart Kb or 40 CFR Part 63 Subpart Ho? Yes Storage Tank is not subject NSPS 0000 'Storage Tank is nat subject to NSPS 0000 Subpart A,General Provisions per§60.5425 Table 3 460.5395-Emissions Control Standards for VOC 650.3413-Testing and Procedures §60.5395(g)-Notification,Reporting and Recordkeeping Requirements 660.5416(c)-Cover and Closed Vent System Monitoring Requirements §60.5417-Control Device Monitoring Requirements [Note:If a storage vessel Is previously determined to be subject to SOPS 0000 due to emissions above 6 tons pen year TIC on the applicability determination date,It should remain subject to NSPS 0000 per 60.5365(e)(2)even If potential V Ot emissions drop below d tans per year] 40 CFR,Part SO,Subpart 0000a,Standards of Performance for Crude Oil and Natural Gas Facilities for which Construction,Modification,or Reconstruction Commenced After September 18,2015 1. Was this condensate storage vessel constructed,reconstructed,or modified(see definitions 40 CFR,60.2)after September 18,2015? 4ds r!:,Go to the next question 2. Does this condensate storage vessel meet the definition of"storage vessel"'per 60.5430a? Go Go to the next question 3. Is this condensate storage vessel located at a facility in the crude oil and natural gas production segment,natural gas processing segment or natural gas transmission and storage segment of the industry? Yasn°1^`'':'i Go to the next question 4. Are potential VOC emissions'from the individual storage vessel greater than or equal to 6 tons per year? fry,,- Go to the next question 5. Is the storage vessel subject to and controlled in accordance with requirements for storage vessels in 40 CFR Part 60 Subpart Kb or 40 CFR Part 63 Subpart HH? Yes.,,l_..?Storage Tank Is not subject NSPS OOOOa 'Storage Tank is nut subject to NSPS 0000a 40 CFR,Part 63,Subpart MAR 00.Oil and Gas Production Facilities 1. is the tank located at a facility that is major'for HAP'? No 1-Storage Tank is not subject MAR HH-There are no MACE HH requirements for tanks at area sources - 2. Is the storage tank located at an all and natural gas production facility that meets either of the following criteria: . a.A facility chat processes,upgrades or stores hydrocarbon liquids'(63.760(x)(2));OR b.A facility that processes,upgrades or stores natural gas prior la the point at which natural gas enters the natural gas transmission and storage source category or is delivered to a final end user'(63.760(a)(3)]? 3. Does the tank meet the definition of"storage vessel"'in 63.761? NA' : 4. Does the tank meet the definition of"storage vessel with the potential for flash emissions"'per 63.761? NA O 5. Is the tank subject to control requirements under 40 CFR Part 60,Subpart Kb or Subpart 0000? NA,..c. 'Storage Tank is not subject to MACT HH Subpart A,General provisions per 063.764(a)Table 2 §63.766-Emissions Control Standards §63.773-Monitoring §63.774-Recordkeeping 463.775-Reporting RACT Review • RAO'review is required If Regulation 7 does not apply AND if the tank Is In the non-attainment area.If the tank meets both criteria,then review RACT requirements. Disclaimer This document assists operators with determining applicability of certain requirements of the Clean Air Act.its implementing regulations,and Air Quality Control Commission regulations.This document is not a rule or regulation,and the analysis A contains may not apply to a particular situation based upon the individual facts and circumstances.This document does not change or substitute for any law, regulation,or any other legally binding requirement and is not legally enforceable.In the event of any conflict between the language of this document and the language of the Clean Air Act„its implementing regulations,and Alr Quality Control Commission regulations,the language of the statute or regulation will control. The use of non-mandatory language such as'recommend,""may,'"should,'and"can,"is intended to describe APCD interpretations and recommendations.Mandatory terminology such as'must"and'required"ere intended to describe controlling requirements under the terms of the Clean Air Ad and Air Quality Control Commission regulations,but this document does not establish legally binding requirements in and of Itself. COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION FACILITY EMISSION SUMMARY Company Name Tallgrass Terminals,LLC County AIRS ID 123 History File Edit Date 4/11/2017 Plant AIRS ID 9D38 Ozone Status Non-Attainment Facility Name Buckingham Station EMISSIONS-Uncontrolled(tons per year) EMISSIONS With Controls(tons per year) POINT PERMIT Description PM10 PM2.5 H2S SO2 NOx VOC Fug CO Total PM10 PM2.5 H2S SO2 NOx VOC Fug CO Total REMARKS AIRS VOC HAPs VOC HAPs ID Previous FACILITY TOTAL 0.0 0.0 0.0 0.0 0.7 25.6 1.4 0.6 1.5 From October 2016 tab Previous Permitted Facility total _ 0.0 , 0.0 0.0 0.0 0.0 25.4 1.4 0.0 1.5 001 14WE1593 One(1)25,000 bbl internal floating 18.0 0.7 - 18.0 0.7 Modification-Addition of two(2)25,000 bbl roof condensate storage vessel. internal floating roof vessel.Update throughput and emissions. O:?. "I AJi! os' -� :�� :..��=_a .i. .:�:.; - 0.0 0.0 i 003 14WE1593 Fugitives 1.4 0.1 1.4 0.1 No change 004 14WE1593 Two(2)150,000 external floating 33.7 1.3 33.7 1.3 Modification-Addition of two(2)150,000 bbl - roof condensate/crude oil storage EFR tanks.Update throughput and emissions. vessels 005 14WE1593 Two(2)250K bbl EFR tanks 27.2 1.0 27.1 1.0 New Point 0.0 0.0 XA Emergency Generator 0.7 0.2 0.6 0.0 0.7 0.2 0.6 0.0 Insignificant Source _ 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 FACILITY TOTAL 0.0 0.0 0.0 0.0 0.7 79.1 1.4 0.6 3.0 0.0 0.0 0.0 0.0 0.7 79.0 1.4 0.6 3.0 VOC: True Minor(NANSR and OP) NOx:True Minor(NANSR and OP) CO: True Minor(PSD and OP) HAPS: True Minor HH: Not applicable(area source) ZZZZ: Area Source Permitted Facility Total 0.0 0.0 0.0 0.0 0.0 51.7 1.4 0.0 2.0 0.0 0.0 0.0 0.0 0.0 78.8 1.4 0.0 2.0 Excludes units exempt from permits/APEN5 (4)Change in Permitted Emissions 0.0 0.0 0.0 0.0 0.0 53.4 0.0 0.0 Pubcom&modeling not required based on A change in emissions. 1 Total VOC Facility Emissions(point and fugitive) 80.4 Facility is eligible for GP02 because<90 tpy (A)Change in Total Permitted VOC emissions(point and fugitive) 53.4 Project emissions less than 25 tpy Note 1 Note 2 • Page 24 of 25 Printed 10/15/2018 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION DIVISION FACILITY EMISSION SUMMARY-HAPs Company Name Tallgrass Terminals,LLC County AIRS ID 123 Plant AIRS ID 9D38 Facility Name. Buckingham Station Emissions-uncontrolled(lbs per year) POINTIPERMIT 'Description Formaldehyde Acetaldehyde Acrolein Benzene Toluene Ethylbenzene Xylenes n-Hexane McOH 224 TMP H2S TOTAL(tpy) Previous FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0 0.0 001 14WE1593 One(1)25,000 bbl internal floating 83 227 60 183 575 222 0.7 roof condensate storage vessel. Oil I.4:.rl:i.i,:.:y 'TV*/ "1....0 "x: .to,:(,-i,i.) i:, 0.0 003 14WE1593 Fugitives 7 18 5 14 44 17 0.1 004 14WE1593 Two(2)150,000 external floating roof 156 427 113 344 1078 416 1.3 condensate/crude oil storage vessels 005 14WE1593 Two(2)250K bbl EFR tanks 126 343 91 277 868 335 1.0 0.0 XA Emergency Generator 0.0 0.0 0.0 0.0 0.0 0.0 TOTAL(tpy) 0.0 0.0 0.0 0.2 0.5 0.1 0.4 1.3 0.0 0.5 0.0 0.0 3.0 I `Total Reportable=all HAPs where uncontrolled emissions>de minimus values Red Text: uncontrolled emissions<de minimus Emissions with controls(lbs per year) POINTIPERMIT 'Description Formaldehyde Acetaldehyde Acrolein Benzene Toluene Ethylbenzene Xylenes n-Hexane McOH 224 TMP H2S TOTAL(tpy) Previous FACILITY TOTAL 0 0 0 0 0 0 0 0 0 0 0 0 0.0 001 14W81593 One(1)25,000 bbl internal floating 83 227 60 183 575 222 0.7 roof condensate storage vessel. f,u2' 4VVE i V v,o(2...1..,:;,0. 0.0 003 14WE1593 Fugitiv es v 7 18 5 14 44 17 0.1 004 14WE1593 Two(2)150,000 external floating roof 156 427 113 344 1078 416 1.3 condensate/crude oil storage vessels 005 14W81593 Two(2)250K bbl EFR tanks 126 343 91 277 868 335 1.0 0.0 XA Emergency Generator 0.0 0.0 0.0 0.0 D.0 0.0 TOTAL(tpy) 0.0 0.0 0.0 0.2 0.5 0.1 0.4 1.3 0.0 0.5 0.0 0.0 3.0 25 14WE1593.CP4.xlsm 10/15/2018 C H OL RA : f!ir P©, Co 1 Divi on °arm' rt of b.ic 1- 'th b.Ervlr _T lent CONSTRUCTION PERMIT Permit number: 14WE 1593 Issuance: 4 Date issued: Issued to: Tallgrass Terminals, LLC Facility Name: Buckingham Terminal Plant AIRS ID: 123/9D38 Physical Location: SW Sec. 34, T8N, R59W County: Weld County General Description: Oil storage and pipeline injection facility Equipment or activity subject to this permit: Facility AIRS Emissions Control Equipment Point Equipment Description Description ID T-4021 Three (3) 25,000 barrel internal floating T-4022 001 roof storage vessels used to store crude oil Internal floating roof T-4023 and condensate. Equipment leaks (fugitive VOCs) from a Fugitives 003 crude oil and condensate storage and No control transport facility. T-4151 Four (4) 150,000 barrel external floating T-4152 004 roof storage vessels used to store crude oil External floating roof T-4153 and condensate. T-4154 T-4251 Two (2) 250,000 barrel external floating T-4252 005 roof storage vessels used to store crude oil External floating roof and condensate. 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. cOPgE COLORADO co Air Pollution Control D3vislon Page 1 of 21 REQUI MEN.T SE a-CERT OR FtLVA AUT " RIZATION 1. Point 001 40° 005:.l UST of y the 'r Pollution Control Division (the Division) no later han 1)fitee da of e latter o commenc ment of operation or issuance of this permit, t y 1561ittingiatNoticebtStart to th _... ision for the equipment covered by this permit. The Notice of Startup form may be downloaded online at www.colorado.Rov/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 thirty(30)days after commencement of operation of the storage vessels covered by Point 005, the owner or operator shall submit to the Division complete APENs 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 005: Two (2) 250,000 barrel external floating roof storage vessels 3. 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.) 4. 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.) 5. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Regulation Number 3, Part B, Section III.E.) 6. The 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.) ) Annual Limits: Facility AIRS Tons per Year Emission Equipment ID Point Process NO, VOC CO Type 01 --- 15.6 --- T-4021 T-4022 001 02 --- 1.0 --- Point T-4023 03 --- 1.4 --- OP NE COLORADO co Air Pollution Control Division _;� Page 2 of 21 �' Tonsper Year b Emission raac 4 Pro -ss r" ac- E•4 p n ;O. �1 �� X VOC CO Type Fug ,:-s - "03 -a =team 1.4 --- Fugitive T 4151 01 --- 21.2 T 4152 004 02 --- 4.2 --- Point T-4153 T-4154 03 - 8.3 --- 01 --- 10.2 --- T-4251 005 02 -- 3.5 --- Point T-4252 03 --- 13.6 --- Notes: 1) See"Notes to Permit Holder"for information on emission factors and methods used to calculate limits. 2) Process 01, 02 and 03 are as follows: a. Process 01: Emissions during normal operation b. Process 02: Emissions during floating roof landing events. c. Process 03: Emissions during storage vessel cleaning events. Annual records of the actual emission rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. 8. 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 AIRS Control Device Pollutants Equipment ID Point Controlled T-4021 T-4022 001 Internal floating roof VOC and HAP T-4023 T-4151 T-4152 004 External floating roof VOC and HAP T-4153 T-4154 T-4251 005 External floating roof VOC and HAP T-4252 9. Point 003: 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 to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. PROCESS LIMITATIONS AND RECORDS 10. This source shall be limited to the following maximum processing rates as listed below. Annual 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.) ` COP HE COLORADO CO G" Air Pollution Control Division Page 3 of 21 Proce ., Li / 1:" i ci y W4 AIRS Process Parameter Annual Limit Equipmait I Print i _�- 45,000,000 T-4021 ondensate Crude Oil Throughput barrels T-4022 001 Floating Roof Landing Events 6 events T-4023 Storage Vessel Cleaning Events 1 event T-4151 Condensate/Crude Oil Throughput 124,100,000 T-4152 barrels T-4153 004 Floating Roof Landing Events 4 events T-4154 Storage Vessel Cleaning Events 1 event Condensate/Crude Oil Throughput 62,050,000 T-4251 barrels T-4252 005 Floating Roof Landing Events 2 events Storage Vessel Cleaning Events 1 event STATE AND FEDERAL REGULATORY REQUIREMENTS 11. 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. Et 4.) 12. Point 001, 004, 005: 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) 13. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 14. Point 001, 004, 005: This source is subject to the applicable requirements of Regulation Number 7, Section VI.B.2. 15. Points 001, 004, 005: The sources covered under AIRS point 001, 004 and 005 are subject to the New Source Performance Standards requirements of Regulation Number 6, Part A, Subpart Kb, Standards of Performance for Volatile Organic Liquid Storage Vessels (Including Petroleum Liquid Storage Vessels)for which Construction, Reconstruction, or Modification Commenced after July 23, 1984 including, but not limited to, the following: • 40 CFR, Part 60, Subpart A- General Provisions • $60.112b- Standard for volatile organic compounds (VOC) • §60.112b(a) The owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 containing a VOL that, as stored, has a maximum true vapor pressure equal to or greater than 5.2 kPa but less than 76.6 kPa...shall equip each storage vessel with one of the following: ■ Point 001: • §60.112b(a)(1) A fixed roof in combination with an internal floating roof meeting the following specifications: • §60.112b(a)(1)(i)The internal floating roof shall rest or float on the liquid surface(but not necessarily in complete contact with it)inside a storage vessel that has a fixed roof. The internal floating roof shall be floating on the liquid surface at all times, except during initial fill and during those intervals when the storage vessel is completely DP COLORADO COLORADO CO or Air Pollution Control Division Page 4 of 21 ( empt d r subegquently emptied and refilled. When the roof is esti ° thefg supports, the process of filling, emptying, or ` efilli$ shall be continuous and shall be accomplished as rapidly as 3 •ssi " e. • §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: o (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. o (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. o (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)(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. • $60.112b(a)(1)(v) Automatic bleeder vents shall be equipped with a gasket and are to be closed at all times when the roof is floating except when the roof is being floated off or is being landed on the roof leg supports. • §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. • Point 004 Et 005: • §60.112b(a)(2) An external floating roof. An external floating roof means a pontoon-type or double-deck type cover that rests on the liquid surface in a vessel with no fixed roof. Each external floating roof must meet the following specifications: ,0,, £ COLORADO +0 Air Pollution Control Division Page 5 of 21 ₹ 6, •.b §60112 a)(2)( Each external floating roof shall be equipped with a closure device between the wall of the storage vessel and the roof edge. The closure device is to consist of two seals, one kc above the other. The lower seal is referred to as the primary seal, and the upper seal is referred to as the secondary seal. o (A)The primary seal shall be either a mechanical shoe seal or a liquid-mounted seal. Except as provided in §60.113b(b)(4), the seal shall completely cover the annular space between the edge of the floating roof and tank wall. o (B)The secondary seal shall completely cover the annular space between the external floating roof and the wall of the storage vessel in a continuous fashion except as allowed in §60.113b(b)(4). • §60.112b(a)(2)(ii) Except for automatic bleeder vents and rim space vents, each opening in a noncontact external floating roof shall provide a projection below the liquid surface. Except for automatic bleeder vents, rim space vents, roof drains, and leg sleeves, each opening in the roof is to be equipped with a gasketed cover, seal, or lid that is to be maintained in a closed position at all times (i.e., no visible gap) except when the device is in actual use. Automatic bleeder vents are to be closed at all times when the roof is floating except when the roof is being floated off or is being landed on the roof leg supports. Rim vents are to be set to open when the roof is being floated off the roof legs supports or at the manufacturer's recommended setting. Automatic bleeder vents and rim space vents are to be gasketed. Each emergency roof drain is to be provided with a slotted membrane fabric cover that covers at least 90 percent of the area of the opening. • §60.112b(a)(2)(iii) The roof shall be floating on the liquid at all times (i.e., off the roof leg supports) except during initial fill until the roof is lifted off leg supports and when the tank is completely emptied and subsequently refilled. The process of filling, emptying, or refilling when the roof is resting on the leg supports shall be continuous and shall be accomplished as rapidly as possible. • §60.113b-Testing and procedures • The owner or operator of each storage vessel as specified in §60.112b(a) shall keep records and furnish reports as required by paragraphs (a), (b), or (c) of this section depending upon the control equipment installed to meet the requirements of §60.112b.The owner or operator shall keep copies of all reports and records required by this section, except for the record required by (c)(1), for at least 2 years. The record required by (c)(1) will be kept for the life of the control equipment. • Point 001: • §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 seat, 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. tk" COLORADO 44` 4i2t Polluton Control Dmislon 4, �� •� Page 6 of 21 k $6 ,1 b(a)( - sually spect the internal floating roof, the primary seal, th nda e l (if o - is in service), gaskets, slotted membranes and 46, sl eves als ( any) eac . ime the storage vessel is emptied and degassed. t tk I the i rna loating r f has defects, the primary seal has holes, tears, or other openings in the deal 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 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. • Point 004 ft 005: • $60.113b(b) After installing the control equipment required to meet $60.112b(a)(2) (external floating roof), the owner or operator shall: • $60.113b(b)(1) Determine the gap areas and maximum gap widths, between the primary seal and the wall of the storage vessel and between the secondary seal and the wall of the storage vessel according to the following frequency. • (i) Measurements of gaps between the tank wall and the primary seal (seal gaps) shall be performed during the hydrostatic testing of the vessel or within 60 days of the initial fill with VOL and at least once every 5 years thereafter. • (ii) Measurements of gaps between the tank wall and the secondary seal shall be performed within 60 days of the initial fill with VOL and at least once per year thereafter. • (iii) If any source ceases to store VOL for a period of 1 year or more, subsequent introduction of VOL into the vessel shall be considered an initial fill for the purposes of paragraphs (b)(1)(i) and (b)(1)(ii) of this section. • $60.113b(b)(2) Determine gap widths and areas in the primary and secondary seals individually by the following procedures: • (i) Measure seal gaps, if any, at one or more floating roof levels when the roof is floating off the roof leg supports. • (ii) Measure seal gaps around the entire circumference of the tank in each place where a 0.32-cm diameter uniform probe passes freely (without forcing or binding against seal) between the seal and the wall of the storage vessel and measure the circumferential distance of each such location. y "PHE COLORADO CO It Air Pollution Control Division Page 7 of 21 A a >• (iii) The total surface area of each gap described in paragraph ''.(b)(2)(ii) of this section shall be determined by using probes of y _' various widths to measure accurately the actual distance from the jw. tank wall to the seal and multiplying each such width by its `respective circumferential distance. ■ §60.113b(b)(3) Add the gap surface area of each gap location for the primary seal and the secondary seal individually and divide the sum for each seal by the nominal diameter of the tank and compare each ratio to the respective standards in paragraph (b)(4) of this section. ■ §60.113b(b)(4) Make necessary repairs or empty the storage vessel within 45 days of identification in any inspection for seats not meeting the requirements listed in (b)(4) (i) and (ii) of this section: • (i) The accumulated area of gaps between the tank wall and the mechanical shoe or liquid-mounted primary seal shall not exceed 212 cm2 per meter of tank diameter, and the width of any portion of any gap shall not exceed 3.81 cm. o (A) One end of the mechanical shoe is to extend into the stored liquid, and the other end is to extend a minimum vertical distance of 61 cm above the stored liquid surface. o (B) There are to be no holes, tears, or other openings in the shoe, seal fabric, or seal envelope. • (ii)The secondary seat is to meet the following requirements: o (A)The secondary seal is to be installed above the primary seal so that it completely covers the space between the roof edge and the tank wall except as provided in paragraph (b)(2)(iii) of this section. o (B) The accumulated area of gaps between the tank wall and the secondary seal shall not exceed 21.2 cm2 per meter of tank diameter, and the width of any portion of any gap shall not exceed 1.27 cm. o (C) There are to be no holes, tears, or other openings in the seal or seal fabric. • (iii) If a failure that is detected during inspections required in paragraph (b)(1) of§60.113b(b) cannot be repaired within 45 days and if the vessel cannot be emptied within 45 days, a 30-day extension may be requested from the Administrator in the inspection report required in §60.115b(b)(4). Such extension request must include a demonstration of unavailability of alternate storage capacity and a specification of a schedule that will assure that the control equipment will be repaired or the vessel will be emptied as soon as possible. • §60.113b(b)(5) Notify the Administrator 30 days in advance of any gap measurements required by paragraph (b)(1) of this section to afford the Administrator the opportunity to have an observer present. • §60.113b(b)(6) Visually inspect the external floating roof, the primary seal, secondary seal, and fittings each time the vessel is emptied and degassed. • (i) If the external floating roof has defects, the primary seal has holes, tears, or other openings in the seal or the seal fabric, or the secondary seal has holes, tears, or other openings in the seat or the seal fabric, the owner or operator shall repair the items as necessary so that none of the conditions specified in this paragraph exist before filling or refilling the storage vessel with VOL. • (ii) For all the inspections required by paragraph (b)(6) of this section, the owner or operator shall notify the Administrator in rDP E COLORADO co v.- Air Pollution Control Division Page 8 of 21 ., writing at least 30 days prior to the filling or refilling of each vstorage vessel to afford the Administrator the opportunity to inspect the storage vessel prior to refilling. If the inspection required by paragraph (b)(6) of this section is not planned and the owner or operator could not have known about the inspection 30 days in advance of refilling the tank, the owner or operator shall notify the Administrator at least 7 days prior to the refilling of the storage vessel. Notification shall be made by telephone immediately followed by written documentation demonstrating why the inspection was unplanned. Alternatively, this notification including the written documentation may be made in writing and sent by express mail so that it is received by the Administrator at least 7 days prior to the refilling. • §60.115b - Reporting and recordkeeping requirements • Point 001: • §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. • Point 004 8 005: • §60.115b(b) After installing control equipment in accordance with §61.112b(a)(2) (external floating roof), the owner or operator shall meet the following requirements. • §60.115b(b)(1) Furnish the Administrator with a report that describes the control equipment and certifies that the control equipment meets the specifications of§60.112b(a)(2) and §60.113b(b)(2), (b)(3), and (b)(4). This report shall be an attachment to the notification required by§60.7(a)(3). • §60.115b(b)(2) Within 60 days of performing the seal gap measurements required by §60.113b(b)(1), furnish the Administrator with a report that contains: COLORADO co Air Pollution Control Division Page 9 of 21 • - (i) The date of measurement. f ii) The raw data obtained in the measurement. • g,iii) The calculations described in §60.113b (b)(2) and (b)(3). &yam 11 bal Keep a record of each gap measurement performed as required by §60.113b(b). Each record shall identify the storage vessel in which the measurement was performed and shall contain: • ,(i) The date of measurement. • (ii)The raw data obtained in the measurement. • (iii)The calculations described in §60.113b (b)(2) and (b)(3). ■ §60.115b(b)(4) After each seal gap measurement that detects gaps exceeding the limitations specified by §60.113b(b)(4), submit a report to the Administrator within 30 days of the inspection. The report will identify the vessel and contain the information specified in paragraph (b)(2) of this section and the date the vessel was emptied or the repairs made and date of repair. • §60.116b-Monitoring of operations • §60.116b(a) The owner or operator shall keep copies of all records required by this section, except for the record required by paragraph (b) of this section, for at least 2 years. The record required by paragraph (b) of this section will be kept for the life of the source. • §60.116b(b)The owner or operator of each storage vessel as specified in§60.110b(a) shall keep readily accessible records showing the dimension of the storage vessel and an analysis showing the capacity of the storage vessel. • §60.116b (c) Except as provided in paragraphs (f) and (g) of this section, the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 3.5 kPa or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 15.0 kPa shall maintain a record of the VOL stored, the period of storage, and the maximum true vapor pressure of that VOL during the respective storage period. • §60.116b (d) Except as provided in paragraph (g) of this section, the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 5.2 kPa or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 27.6 kPa shall notify the Administrator within 30 days when the maximum true vapor pressure of the liquid exceeds the respective maximum true vapor vapor pressure values for each volume range. • §60.116b(e) Available data on the storage temperature may be used to determine the maximum true vapor pressure as determined below. • §60.116b(e) (2) For crude oil or refined petroleum products the vapor pressure may be obtained by the following: ■ §60.116b(e) (2) (i) Available data on the Reid vapor pressure and the maximum expected storage temperature based on the highest expected calendar-month average temperature of the stored product may be used to determine the maximum true vapor pressure from nomographs contained in API Bulletin 2517 (incorporated by reference—see§60.17), unless the Administrator specifically requests that the liquid be sampled, the actual storage temperature determined, and the Reid vapor pressure determined from the sample(s). • §60.116b(e) (2) (ii) The true vapor pressure of each type of crude oil with a Reid vapor pressure less than 13.8 kPa or with physical properties that 41, COP s COLORADO irk LI Co •,. Air Pollution Control Division Page 10 of 21 ,€ pr lue det • pation the recommended method is to be determined as and " corded if the estimated maximum true vapor p,.-ssu p is grater than 4^^ 5 kPa. In addition, the following requirements of Regulation Number 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 Number 6, Part A. General Provisions from 40 CFR 60.11 b. No article, machine, equipment or process shall be used to conceal an emission which would otherwise constitute a violation of an applicable standard. Such concealment includes, but is not limited to, the use of gaseous diluents to achieve compliance with an opacity standard or with a standard which is based on the concentration of a pollutant in the gases discharged to the atmosphere. (§ 60.12) c. Written notification of construction and initial startup dates shall be submitted to the Division as required under § 60.7. d. Records of startups, shutdowns, and malfunctions shall be maintained, as required under § 60.7. e. Written notification of opacity observation or monitor demonstrations shall be submitted to the Division as required under§ 60.7. f. Excess Emission and Monitoring System Performance Reports shall be submitted as required under§ 60.7. g. Performance tests shall be conducted as required under§ 60.8. h. Compliance with opacity standards shall be demonstrated according to § 60.11. 16. Point 003: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation Number 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation Number 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection Et Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a quarterly basis. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. COP E COLORADO CO s, Air Pollution Control Duns Ion „ ., Page 11 of 21 A „r, r c,jt11. Fo e , ir, va - adjacent to the equipment to be repaired will be closed if ID TA pr�Ucable, rmmn izing t o volume released. . R. /pair- com nents shall be re-screened using AVO to determine if the leak w` rezfra v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post-repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING Et MAINTENANCE REQUIREMENTS 17. This source is not required to follow a Division-approved operating and maintenance plan. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 18. Point 003: Within one hundred and eighty days (180) after commencement of operation, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self- certification process to ensure compliance with emissions limits. Periodic Testing Requirements 19. This source is not required to conduct periodic testing, unless otherwise directed by the Division or other state or federal requirement. ADDITIONAL REQUIREMENTS 20. All previous versions of this permit are cancelled upon issuance of this permit. 21. 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 NOX per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or cores COLORADO co Air Pollution Control Division Page 12 of 21 Fyn IFo, a non- rep&ale po, tant: VA If e issiops in ase y 50% or „- e (5) tons per year, whichever is less, above the ff,v,, l e n t1 ast APEN sulailitted 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 GENERAL TERMS AND CONDITIONS 22. 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. 23. 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. 24. 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. 25. 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. 26. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 27. 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. 28. 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 cortte COLORADO CO Air Pollution Control Division Page 13 of 21 Th efl ons uhd Sect n 25-7-t15 (enforcement), -121 (injunctions), -122 (civil v enal ) 1"x.1 (crlrri penaLtreA, C.R.S1 r By: Bradley Eades Permit Engineer Permit History Issuance Date Description Issuance 1 April 30, 2015 Issued to Tallgrass Terminals, LLC. Newly permitted condensate tanks and associated fugitive emissions at a true minor facility. Issuance 2 March 14, 2016 Issued to Tallgrass Terminals, LLC. Replace four (4) 5,000 bbl internal floating roof condensate tanks with one (1) 25,000 bbl internal floating roof condensate tank. Lower estimated fugitive component count due to reduction in number of tanks. Point 002 has been cancelled and removed from the permit. Issuance 3 May 16, 2017 Issued to Tallgrass Terminals, LLC. Addition of two (2) 150,000 barrel external floating roof condensate/crude oil storage vessels. Increase estimated fugitive count to account for additional sources. Update emissions factors used to calculate fugitive emissions. Issuance 4 This Issuance Issued to Tallgrass Terminals, LLC. Addition of two (2) 250,000 barrel external floating roof vessels. Addition of two (2) 25,000 barrel internal floating roof vessels. Addition of two (2) 150,000 barrel external floating roof vessels. Update number of landings based on new vessels. orw� COLORADO CO `d Air Pollution Control Division �.._ Page 14 of 21 Notes ;< Perm H the of this mit iss nce: 1) Th =permi of r requi -• _•ay fa s Oor the rocessing time for this permit. An invoice for these fe-, willA;W iss d er r e pe it i sued. Th- permit holder shall pay the invoice within 30 days • <--z oat o i --pay t oice 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 Uncontrolled Controlled Point Pollutant CAS# Emissions Emissions (Ib/yr) (lb/yr) Benzene 71432 83 83 Toluene 108883 227 227 Ethylbenzene 100414 60 60 001 Xylenes 1330207 183 183 n-Hexane 110543 575 575 2,2,4- 540841 222 222 Trimethylpentane Benzene 71432 7 7 Toluene 108883 18 18 Ethylbenzene 100414 5 5 003 Xylenes 1330207 14 14 n-Hexane 110543 44 44 2,2,4- 540841 17 17 Trimethylpentane Benzene 71432 156 156 Toluene 108883 427 427 004 Ethylbenzene 100414 113 113 Xylenes 1330207 344 344 n-Hexane 110543 1078 1078 ccrxe COLORADO O . Air Pollution Control Division Page 15 of 21 1 4 4- ,140841 J 416 416 Trap ylpen: B zen1` 71432 _3 126 126 —To IP- ea 1088 343 343 Ethylbenzene 100414 91 91 005 Xylenes 1330207 277 277 n-Hexane 110543 868 868 2,2,4- 540841 335 335 Trimethylpentane Note: All non-criteria reportable pollutants in the table above with uncontrolled emission rates above 250 pounds per year (lb/yr) are reportable and may result in annual emission fees based on the most recent Air Pollution Emission Notice. 5) The emission levels contained in this permit are based on the following emission factors: Point 001: Process 01: Emission Factors Uncontrolled CAS# Pollutant lb/bbl Source Condensate/Crude Oil Throughput VOC 6.92x1O4 AP-42 Chapter 7 71432 Benzene 1.61x10-6 108883 Toluene 4.38x10-6 100414 Ethylbenzene 1.16x1O6 1330207 Xylenes 3.53x1O6 Engineering Estimate 110543 n-Hexane 1.11x10-5 540841 2'2'4 4.28x10-6 Trimethylpentane Note: The control device (internal floating roof) for point 001 is integrated into the storage vessel. Process 02: Emission Factors CAS # Pollutant Uncontrolled Source lb/roof landing event VOC 325.85 AP-42 Chapter 7 71432 Benzene 0.76 108883 Toluene 2.06 100414 Ethylbenzene 0.54 1330207 Xylenes 1.66 Engineering Estimate 110543 n-Hexane 5.21 540841 2'2'4 2.01 Trimethylpentane Note: The emissions 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 7.1-88 for equations) * i& ; : COLORADO co Air Pollution Control Division Page 16 of 21 S'z r Proce 0 Emission actors g` ACAS# gPoftutant Unco led Source lb/storage vessel cleaning event VOC 2,840.44 API TR 2568 (11/07) 71432 Benzene 6.59 Mass Balance 108883 Toluene 17.98 Mass Balance 100414 Ethylbenzene 4.74 Mass Balance 1330207 Xylenes 14.49 Mass Balance 110543 n-Hexane 45.45 Mass Balance 540841 2'2'4 17.55 Mass Balance Trimethylpentane Note: The emissions factors represented above were calculated using equations in API TR 2568 (11/07) for storage vessels with an internal floating roof. Point 003: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 100 --- 2400 --- Flanges 0 --- 800 --- Open-ended Lines 0 --- 0 --- Pump Seals 0 --- 70 --- Valves 60 --- 1500 --- Other* 0 --- 75 --- VOC Content (wt. 1 --- 1 fraction) Benzene Content (wt. 0.00232 0.00232 fraction) Toluene Content (wt. 0.00633 0.00633 fraction) Ethylbenzene (wt. 0.00167 --- 0.00167 --- fraction) Xylenes Content (wt. 0.0051 0.0051 fraction) n-Hexane Content (wt. 0.016 0.016 fraction) 2,2,4-Trimethylpentane 0.00618 0.00618 (wt. fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors (kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 4.2E-05 --- 8.0E-06 --- Flanges 4.2E-05 --- 8.0E-06 --- Open-ended Lines 1.2E-04 --- 1.3E-04 --- Pump Seals 6.5E-05 --- 5.4E-04 --- 44, cnpHE COLORADO ►O G Air Pollution Control Division Page 17 of 21 I 'Ives 1 3E 4.3E-05 Other 'n , V 42E-04 1.3E-04 S9 • PA- R 91.1 Tab[, aurtal Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content represented in the table above. Point 004: Process 01: Emission Factors Uncontrolled CAS # Pollutant lb/bbl Source Condensate/Crude Oil Throughput VOC 3.42x10-4 AP-42 Chapter 7 71432 Benzene 7.93x10-7 108883 Toluene 2.16x10-6 100414 Ethylbenzene 5.71x10-7 1330207 Xylenes 1.74x10-6 Engineering Estimate 110543 n-Hexane 5.47x1O6 540841 2'2'4 2.11x10-6 Trimethylpentane Note: The control device(external floating roof)for point 004 is integrated into the storage vessel. Process 02: Emission Factors CAS# Pollutant Uncontrolled Source lb/roof landing event VOC 2,083.68 AP-42 Chapter 7 71432 Benzene 4.83 108883 Toluene 13.19 100414 Ethylbenzene 3.48 1330207 Xylenes 10.63 Engineering Estimate 110543 n-Hexane 33.34 540841 2, 12.88 12.88 Trimethylpentane Note: The emissions factors represented above were calculated using the equations in AP-42 Chapter 7 for storage vessels with an external floating roof and full liquid heel (See 7.1-88 for equations) Process 03: Emission Factors CAS# Pollutant Uncontrolled Source lb/storage vessel cleaning event VOC 16,632.12 API TR 2568 (11/07) 71432 Benzene 38.59 Mass Balance cerxe COLORADO CO ` Air Pollution Control Division 4 - _�. ,.. �•�, ...,_, Page 18 of 21 Sion qpctors iicont Iled CA # Pollan ; Source I; ei ,ervcleanin a vent 108883 Toluene 105.28 Mass Balance 100414 , Ethylbenzene 27.78 Mass Balance 1330207 Xylenes 84.82 Mass Balance 110543 n-Hexane 266.11 Mass Balance 540841 2,2,4- 102.79 Mass Balance Trimethylpentane Note: The emissions factors represented above were calculated using equations in API TR 2568 (11/07)for storage vessels with an external floating roof. Point 005: Process 01: Emission Factors Uncontrolled CAS # Pollutant lb/bbl Source Condensate/Crude Oil Throughput VOC 3.26x10-4 AP-42 Chapter 7 71432 Benzene 7.56x10-7 108883 Toluene 2.06x10-6 100414 Ethylbenzene 5.44x10-7 1330207 Xylenes 1.66x10-6 Engineering Estimate 110543 n-Hexane 5.21x10-6 540841 2'2'4 2.01x10-6 Trimethylpentane Note: The control device(external floating roof)for point 005 is integrated into the storage vessel. Process 02: Emission Factors CAS # Pollutant Uncontrolled Source lb/roof landing event VOC 3,441.20 AP-42 Chapter 7 71432 Benzene 7.98 108883 Toluene 21.78 100414 Ethylbenzene 5.75 1330207 Xylenes 17.55 Engineering Estimate 110543 n-Hexane 55.06 540841 2, 21.27 21.27 Trimethylpentane Note: The emissions factors represented above were calculated using the equations in AP-42 Chapter 7 for storage vessels with an external floating roof and full liquid heel (See 7.1-88 for equations) M+ COLORADO CO Air Pollution Control Division .__ - Page 19 of 21 A ri, It a c " itProce 03t a "'s ;mission Factors - z,_ ' tat au tre teed CAS# -Pollutant Source lb/storage vessel cleaning event VOC 27,155.70 API TR 2568 (11/07) 71432 Benzene 63.00 Mass Balance 108883 Toluene 171.90 Mass Balance 100414 Ethylbenzene 45.35 Mass Balance 1330207 Xylenes 138.49 Mass Balance 110543 n-Hexane 434.49 Mass Balance 540841 2, 167.82 167.82 Mass Balance Trimethylpentane Note: The emissions factors represented above were calculated using equations in API TR 2568 (11/07)for storage vessels with an external floating roof. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This 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 Status Requirement Operating Permit Minor Source NANSR Minor Source MACT HH Area Source Requirements: Not Applicable NSPS Kb Applicable NSPS OOOO Not Applicable NSPS KKK Not Applicable NSPS 0000a 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 COPH£ COLORADO CO of An-Pollution Control Division Page 20 of 21 M 0 SPS .4416d i 1 ,� art A Subpart KKKK SPS P��i rt bfl, Apndi`` s 4,pl3endix Appendix I u 6s `�� 3: Na'ClhnaFEm f"hhion dads for I-takaadous 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 • itE COLORADO CO 5 Air Pollution Control Division Page 21 of 21 O/3/1 c p Condensate Storage Tank(s) APEN AN. V410 Form APCD-205 CO i Air Pollutant Emission Notice (APEN) and Application for Construction Permit All sections of this APEN and application must be completed for both new and existing facilities, including APEN updates. An application with missing information may be determined incomplete and may be returned or result in longer application processing times. You may be charged an additional APEN fee if the APEN is filled out incorrectly or is missing information and requires re-submittal. This APEN is to be used for tanks that store condensate associated with oil and gas industry operations. If your emission source does not fall into this category, there may be a more specific APEN available for your source (e.g. crude oil storage tanks, produced water storage tanks, hydrocarbon liquid loading, etc.). In addition, the General APEN (Form APCD-200) is available if the specialty APEN options will not satisfy your reporting needs. A list of all available APEN forms and associated addendum forms can be found on the Air Pollution Control Division (APCD) website at:www.colorado.Rov/pacific/cdphe/air-permits. This emission notice is valid for five(5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: 14WE1593 AIRS ID Number: 123 / 9O38 /001 w, !_ari-_ur1 ,_.�PCD 13 ,,._u 7 ,Yx _r _ . 3rd AIRS IDl Section 1 - Administrative information Company Name': Taligrass Terminals, LLC Site Name: Buckingham Terminal Site Location Site Location: 57251 WCR 86 (SW, 534, T8N, R59W) County: Weld New Raymer, CO 80742 NAICS or SIC Code: 486110 Mailing Address: (include Zip Code) 370 Van Gordon St. Lakewood, CO 80228 Contact Person: Beau Wagner Phone Number: 303-763-3477 E-Mail Address2: beau.wagner@tallgrassenergylp.com 1 Use the full, legal company name registered with the Colorado Secretary of State.This is the company name that wilt appear on all documents issued by the APCD.Any changes will require additional.paperwork. 2 Permits,exemption letters,and any processing invoices will be issued by the APCD via e-mail to the address provided. COLORADO r:Jri.rr a-:I' _ Thrrir;s t i -."20'1,3 1 Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/001 [Leave blank unless APCD has already assigned a permit 8 and AIRS ID] Section 2 - Requested Action ❑ NEW permit OR newly-reported emission source ❑ Request coverage under traditional construction permit ❑ Request coverage under a General Permit El GP01 0 GP08 If General Permit coverage is requested,the General Permit registration fee of$312.50 must be submitted along with the APEN filing fee. -OR- ❑✓ MODIFICATION to existing permit (check each box below that applies) ❑✓ Change in equipment ❑ Change company name3 ❑✓ Change permit limit El Transfer of ownership4 El Other(describe below) -OR- ❑ APEN submittal for update only (Note blank APENs will not be accepted) -ADDITIONAL PERMIT ACTIONS- ❑ APEN submittal for permit exempt/grandfathered source ❑ Limit Hazardous Air Pollutants (HAPs)with a federally-enforceable limit on Potential To Emit (PTE) Additional Info Et Notes: Request a change to the Facility Equipment IDs. Tank T-1 should be changed to T-4021, New tanks are T-4022, T-4023. 3 For company name change,a completed Company Name Change Certification Form (Form APCD-1O6)must be submitted. 4 For transfer of ownership,a completed Transfer of Ownership Certification Form (Form APCD-104)must be submitted. Section 3 - General Information General description of equipment and purpose: Three (3) 25,000 bbl. internal floating roof storage tanks Company equipment Identification No. (optional): T-4021, T-4022, T-4023 For existing sources, operation began on: 07/26/2016 For new or reconstructed sources, the projected start-up date is: 01/01/2020 Normal Hours of Source Operation: 24 hours/day 7 days/week 52 weeks/year Storage tank(s) located at: ❑ Exploration Et Production(E&P)site CI Midstream or Downstream (non E&P)site Will this equipment be operated in any NAAQS nonattainment area? Q Yes ❑ No Are Flash Emissions anticipated from these storage tanks? ❑ Yes 0 No Is the actual annual average hydrocarbon liquid throughput a 500 bbl/day? Q Yes ❑ No If"yes", identify the stock tank gas-to-oil ratio: __ m3/liter Are these storage tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) ❑ Yes 0 No 805 series rules?If so, submit Form APCD-105. Are you requesting a 6 ton/yr VOC emissions (per storage tank), or are uncontrolled actual ❑ Yes ❑ No emissions a 6 ton/yr(per storage tank)? COLORADO Form APCD-2O5 Condensate Storage Tank(sl APEN • Revision 7/2018 2 I Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/001 IL=±3,e 1vO Section 4 - Storage Tank(s) Information Actual Annual Amount Requested Annual Permit Limit5 (bbtlyearr) (bbllyear) I Condensate Throughput: 1,238,943 45,000,000 From what year is the actual annual amount? 2017 Average API gravity of sales oil: 40.6 degrees RVP of sales oil: 8-9 Tank design: ❑ Fixed roof E Internal floating roof ❑ External floating roof Storage #of Liquid Manifold Storage Total Volume of Installation Date of Most Date of First Tank ID Vessels in Storage Tank Storage Tank Recent Storage Vessel in Production (bbl) Storage Tank(month/year) (month/year) T-4021 1 25,000 07/2016 07/2016 T-4022 1 25,000 TBD TBD T-4023 1 25,000 TBD TBD Wells Serviced by this Storage Tank or Tank Battery (EfsP Sites Only) API Number Name of Well Newly Reported Well O O O 5 Requested values will become permit limitations. Requested limit(s)should consider future growth. 6 The EaP Storage Tank APEN Addendum(Form APCD-212)should be completed and attached when additional space is needed to report all wells that are serviced by the equipment reported on this APEN form. Section 5 - Stack Information Geographical Coordinates (Latitude/Longitude or UTM) 40.613283, -103.971119 Operator Stack Discharge Height Above Temp. Flow Rate Velocity ID No. Ground Level(feet) (°F) (ACFM) (ft/sec) Indicate the direction of the stack outlet: (check one) ❑ Upward ❑ Downward ❑Upward with obstructing raincap ❑ Horizontal 0 Other(describe): N/A Indicate the stack opening and size: (check one) ❑ Circular Interior stack diameter(inches): ❑Square/rectangle Interior stack width(inches): Interior stack depth (inches): 0 Other(describe): N/A CLURADa FOrrT .:?;e f.i-:3(.l'1 ;12') .� : _ t,•:�.�, - .... Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/001 [Leave blank unless APCD has already assigned a permit 1 and AIRS ID] Section 6 - Control Device Information ❑ Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. Pollutants Controlled: Vapor Size: Make/Model: ❑ Recovery Unit(VRU): Requested Control Efficiency: VRU Downtime or Bypassed (emissions vented): % Pollutants Controlled: Rating: MMBtu/hr Type: Make/Model: Combustion ❑ Requested Control Efficiency: Device: Manufacturer Guaranteed Control Efficiency: % Minimum Temperature: Waste Gas Heat Content: Btu/scf Constant Pilot Light: ❑ Yes ❑ No Pilot Burner Rating: MMBtu/hr Description of the closed loop system: ❑ Closed Loop System Pollutants Controlled: VOC/HAPs 0 Other: Description: Internal Floating Roof Control Efficiency Requested: Inherent % Section 7- Gas/Liquids Separation Technology Information (EEtP Sites Only) What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? N/A psig Describe the separation process between the well and the storage tanks: COLORADO Form APCD-205 Condensate Storage Tank(sl APE11 - Revision 7/2018 4 I Permit Number: 14WE1 593 AIRS ID Number: 123 /9038/001 Ai=,r 1 Section 8 - Emissions Inventory Information Attach all emissions calculations and emission factor documentation to this APEN form7. If multiple emission control methods were identified in Section 6, the following table can be used to state the overall (or combined)control efficiency(%reduction): Overall Requested Control Pollutant Description of Control Methods) Efficiency (%reduction in emissions) V0C Internal Floating Roof Inherent Design NOx CO HAPs Internal Floating Roof Inherent Design Other: From what year is the following reported actual annual emissions data? 201 7 Criteria Pollutant Emissions Inventory Emission Factor? Actual Annual Emissi Requested Annual Permit Emissions Emission Limit(s) Pollutant 5 Source E Uncontrolled Controlled Uncontrolled Controlled Uncontrolled Units" (AP-42, Emissions Emissions8 Emissions " Emissions' Basis Mfg.etc) (Tons/year) (Tons/year) (Tons/year) (Tons/year) VOC 6.92E-04 lb/bbl AP-42(Ch 7,1) 0.427** 0.427** 18.0* 18.0* NOx CO Non-Criteria Reportable Pollutant Emissions inventory Chemical Emission Factor? Actual Annual Emissions Chemical Name CAS Service Abstract Source Uncontrolled Controlled trolled U e (CAS) ncon Units (AP-42, Emissions - Emissions Number Basis Mfg. etc) (Pounds/year) z (Pounds/year) Benzene 71432 Toluene 108883 Ethylbenzene 100414 Xylene 1330207 n-Hexane 110543 1.11E-05 Ib/bbl* Eng. Est. De minimis** De minimis** 2,2,4- 540841 Trimethylpentane 5 Requested values will become permit limitations. Requested limit(s)should consider future growth. 7 Attach condensate liquid laboratory analysis,stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. a Annual emissions fees will be based on actual controlled emissions reported. If source has not yet started operating, leave blank. Please see attached Emission Summary sheet for detailed breakdown of different emission processes that make up the total emission rate. **Actual emissions for 2017 CY are calculated by emission factors from Notes to Permit Holder, 14WE1593, Issuance 3. COLORADO rv.1E...r tw �,_ _cno12S-. v ,..s. .alt ;-l-i '"'.-YiSi(:t Cl i'_ 5 i • Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/001 [Leave b[ank APCD permIt;;',,,;rd AIRS O1 Section 9 -Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP01 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable General Permit. (Oh i7_,_clk'3/ v Signature of Legally Authorized Person (not a vendor or consultant) Date Beau Wagner Air Compliance Specialist Name (print) Title Check the appropriate box to request a copy of the: Draft permit prior to issuance ❑✓ Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Send this form along with $191.13 and the General Permit For more information or assistance call: registration fee of$312.50, if applicable, to: Small Business Assistance Program Colorado Department of Public Health and Environment (303) 692-3175 or (303) 692-3148 Air Pollution Control Division APCD-SS-B1 APCD Main Phone Number 43O0 Cherry Creek Drive South (303)692-3150 Denver, CO 8O246-153O Make check payable to: Or visit the APCD website at: Colorado Department of Public Health and Environment https://www.colorado.gov/cdohe/apcd I COLORADO �: tOri:�, APCD-205 Code .,I__-., _ Tank(s) r ,S„ `i 20-8 6 - Oi "10 ( v�7,ate Condensate Storage Tank(s) APEN ‘ltr Form. APCD-205 Air Pollutant Emission Notice (APEN) and Application for Construction Permit AR sections of this APEN and application must be completed for both new and existing facilities, including APEN updates. An application with missing information may be determined incomplete and may be returned or result in longer application processing times. You maybe charged an additional APEN fee if the APEN is filled out incorrectly or is missing information and requires re-submittal. This APEN is to be used for tanks that store condensate associated with oil and gas industry operations. If your emission source does not fall into this category, there may be a more specific APEN available for your source (e.g. crude oil storage tanks, produced water storage tanks, hydrocarbon liquid loading, etc.). In addition, the General APEN (Form APCD-200)is available if the specialty APEN options will not satisfy your reporting needs. A list of all available APEN forms and associated addendum forms can be found on the Air Pollution Control Division (APCD) website at:www.colorado.gov/pacific/cdphe/air-permits. This emission notice is valid for five(5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: 14WE1593 AIRS ID Number: 123 / 9D38 /004 t' .arc-friov u a ..PCL has r.i.is._rid -.IRS .0] Section 1 - Administrative Information Company Name': Tallgrass Terminals, LLC Site Name: Buckingham Terminal Site Location Site Location: 57251 WCR 86 (SW, S34, T8N, R59W) County: Weld New Raymer, CO 80742 NAICS or SIC Code: 486110 Mailing Address: (Include Zip Code) 370 Van Gordon St, Lakewood, CO 80228 Contact Person: Beau Wagner Phone Number: 303-763-3477 E-Mail Address2: beau.wagner@tallgrassenergylp.com I Use the full,legal company name registered with the Colorado Secretary of State.This is the company name that will appear on all documents issued by the APCD.Any changes will require additional paperwork. 2 Permits,exemption letters, and any processing invoices will be issued by the APCD via e-mail to the address provided. AVcola ar a �.1 APCD-2O5 CU:id;_r1x ...... -F. Tr":' _N 7:20 .._,_e. ._. Permit Number: 14WE1593 AIRS ID Number: 123 /9O38/004 [Leave blank unless APCD has already assigned a permit:!and AIRS ID) Section 2 - Requested Action O NEW permit OR newly-reported emission source ❑ Request coverage under traditional construction permit ❑ Request coverage under a General Permit ❑ GP01 ❑ GP08 If General Permit coverage is requested, the General Permit registration fee of$312.50 must be submitted along with the APEN filing fee. -OR- D MODIFICATION to existing permit(check each box below that applies) El Change in equipment O Change company name3 Change permit limit ❑ Transfer of ownership4 ❑ Other(describe below) -OR- ❑ APEN submittal for update only(Note blank APENs will not be accepted) -ADDITIONAL PERMIT ACTIONS- "• APEN submittal for permit exempt/grandfathered source ❑ Limit Hazardous Air Pollutants (HAPs)with a federally-enforceable limit on Potential To Emit (PTE) Additional Info Et Notes: Requesting a change to the Facility Equipment IDs. T-2 to T-4151; T-3 to T-4152. New IDs for T-4153, T-4154. 3 For company name change, a completed Company Name Change Certification Form (Form APCD-106)must be submitted. 4 For transfer of ownership, a completed Transfer of Ownership Certification Form (Form APCD-104)must be submitted. Section 3 - General Information General description of equipment and purpose: Four(4) - 150,000 bbl. External Floating Roof Tanks Company equipment Identification No. (optional): T-4151, T-4152, T-4153, T-4154 For existing sources, operation began on: 04/07/2018 For new or reconstructed sources, the projected start-up date is: 01/01/2020 Normal Hours of Source Operation: 24 hours/day 7 days/week 52 weeks/year Storage tank(s) located at: O Exploration&Production(E&P)site 0 Midstream or Downstream (non EaP)site Will this equipment be operated in any NAAQS nonattainment area? 0 Yes ❑ No Are Flash Emissions anticipated from these storage tanks? ❑ Yes ❑✓ No Is the actual annual average hydrocarbon liquid throughput a 500 bbl/day? Q Yes O No If"yes", identify the stock tank gas-to-oil ratio: -- m3/liter Are these storage tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) O Yes 0 No 805 series rules? If so, submit Form APCD-105. Are you requesting≥ 6 ton/yr VOC emissions(per storage tank), or are uncontrolled actual ❑ Yes ✓❑ No emissions≥6 ton/yr(per storage tank)? COLORADO Form APCD-205 Condensate Storage Tankisl APEN - Revision 7/2018 2 I 'm Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/004 Section 4 - Storage Tank(s) Information Actual Annual Amount Requested Annual Permit Limits (bbl/year) (bbt/year) Condensate Throughput: 0 124,100,000 From what year is the actual annual amount? 2017 Average API gravity of sales oil: 40.6 degrees RVP of sales oil: 8-9 Tank design: ❑ Fixed roof ❑ Internal floating roof 0 External floating roof Storage # of Liquid Manifold Storage Total Volume of Installation Date of Most Date of First Tank ID Vessels in Storage Tank Storage Tank Recent Storage Vessel in Production fbbl) Storage Tank(month/year) (month/year) T-41.51-T-1154 1 600,000 04/2018 04/2018 Wells Serviced by this Storage Tank or Tank Battery6(EEP Sites Only) API Number Name of Well Newly Reported Well ( ❑ 5 Requested values wilt become permit limitations. Requested limit(s)should consider future growth. 6 The EEtP Storage Tank APEN Addendum (Form APCD-212)should be completed and attached when additional space is needed to report all wells that are serviced by the equipment reported on this APEN form. Section 5 - Stack Information Geographical Coordinates (Latitude/Longitude or UTM) 40.613283, -103.971119 Operator Stack Discharge Height Above Temp. Flow Rate Velocity ID No. Ground Level (feet) (°f) (ACFM) (ft/sec) Indicate the direction of the stack outlet: (check one) ❑ Upward ❑Downward ❑Upward with obstructing raincap ❑Horizontal Other(describe): N/A Indicate the stack opening and size: (check one) ❑Circular Interior stack diameter(inches): ❑Square/rectangle Interior stack width(inches): Interior stack depth (inches): ❑Other(describe): N/A LCLG AG+G E' _ .t APEN 'i. i".... s F 1,I i r„ ..�. _t 5 _-F v._-,_ __ :,ice-� v3 ��.?r ,, _i 7 _,.�. 7�_.,.,_, '� Permit Number: 14WE1593 AIRS ID Number: 123 /9O38/004 [Leave blank unless APCD has already assigned a permit r and AIRS ID] Section 6 - Control Device Information ❑ Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. Pollutants Contro€led: Vapor Size: Make/Model: ❑ Recovery Unit (VRU): Requested Control Efficiency: VRU Downtime or Bypassed (emissions vented): Pollutants Controlled: Rating: MMBtu/hr Type: Make/Model: ❑ Combustion Requested Control Efficiency: Device: Manufacturer Guaranteed Control Efficiency: % Minimum Temperature: Waste Gas Heat Content: Btu/scf Constant Pilot Light: ❑ Yes ❑ No Pilot Burner Rating: MMBtu/hr Description of the closed loop system: ❑ Closed Loop System Pollutants Controlled: VOC/HAPs jl Other: Description: External Floating Roof Control Efficiency Requested: Inherent % Section 7- Gas/Liquids Separation Technology Information (E&P Sites Only) What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? N/A psig Describe the separation process between the well and the storage tanks: COLORADO Form APCD-2O5 Condensate Slot age Tanic(s)ADEN - Revision 7/2018 Permit Number: 14WE1593 AIRS ID Number: 123 19D38/004 Section 8 - Emissions Inventory Information Attach all emissions calculations and emission factor documentation to this APEN form. If multiple emission control methods were identified in Section 6, the following table can be used to state the overall (or combined) control efficiency(%reduction): Overall Requested Control Pollutant Description of Control Method(s) Efficiency;, (%reduction in emissions) VOC External Floating Roof Inherent Design NOx CO HAPs External Floating Roof Inherent Design Other: From what year is the following reported actual annual emissions data? 201 7 Criteria,Pollutant Emissions Inventory Re Emission Factor7 Actual Annual Emissions' quested Annual Permit Emission Limit(s)5 Pollutant Source Uncontrolled Controlled Uncontrolled Controlled Uncontrolled Units (AP-42, Emissions Emissions8 Emissions! Emissions Basis Mfg.etc) (Tons) ear o Y ) (Tons year) (T ns/year)' (Tons/year) VOC 3.42E-04 1b/bbl AP-42(Ch 7.1) 0** 0** 33.7* 33.7* NOx CO Non-Criteria Reportable Pollutant Emissions Inventory Chemical Emission Factor7 Actual Annual Emissions Chemical Name Abstract Source Uncontrolled Controlled Service(CAS) Uncontrolled s Units (AP-42, Emissions Emissions Number Basis Mfg. etc) Pounds) ear 8 (Pounds/year)) ' (Pounds!year) Benzene 71432 0 Toluene 108883 2.16E-06 lb/bbl* Eng. Est. ( 0 Ethylbenzene 100414 0 Xylene 1330207 1.74E-06 Ib/bbl* Eng. Est. 0 n-Hexane 110543 5.47E-06 Ib/bbl` Eng. Est. 0 2,2,4-ntane 540841 2.11E-06 Ib/bbl* Eng. Est. 0 Trime 5 Requested values will become permit limitations. Requested limit(s)should consider future growth. 7 Attach condensate liquid laboratory analysis,stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. s Annual emissions fees will be based on actual controlled emissions reported. If source has not yet started operating, leave blank. "Please see attached Emission Summary sheet for detailed breakdown of different emission processes that make up the total emission rate. *"Actual emissions for 2017 CY are zero since tanks did not go into service until 2018. e Aoo _. c I „.. Permit Number: 14WE1593 AIRS ID Number: 123 /9D381004 ape , [ .:,i:J I Section 9 - Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP01 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable General Permit. -1O,6}1a (0/3 /2-01 Signature of Leg tly Authorized Person (not a vendor or consultant) Date Beau Wagner Air Compliance Specialist Name (print) Title Check the appropriate box to request a copy of the: Draft permit prior to issuance ❑✓ Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type,etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Send this form along with $191.13 and the General Permit For more information or assistance call: registration fee of$312.50, if applicable, to: Small Business Assistance Program Colorado Department of Public Health and Environment (303) 692.3175 or(303)692-3148 Air Pollution Control Division APCD-SS-B1 APCD Main Phone Number 4300 Cherry Creek Drive South (303) 692-3150 Denver, CO 80246-1530 Make check payable to: Or visit the APCD website at: Colorado Department of Public Health and Environment https://www.coiorado.gov/cdphe/apcd CG ORADO Fun'.. tC, ,PEN • RECE SEP , a Condensate Storage Tank(s) APEN is 2O8 �DPHE StP• cD A Form APCD-205 Q nary CO VAir Pollutant Emission Notice (APEN) and Application for Construction Permit All sections of this APEN and application must be completed for both new and existing facilities, including APEN updates. An application with missing information may be determined incomplete and may be returned or result in longer application processing times. You may be charged an additional APEN fee if the APEN is filled out incorrectly or is missing information and requires re-submittal. This APEN is to be used for tanks that store condensate associated with oil and gas industry operations. If your emission source does not fall into this category, there may be a more specific APEN available for your source (e.g. crude oil storage tanks, produced water storage tanks, hydrocarbon liquid loading, etc.). In addition, the General APEN (Form APCD-200) is available if the specialty APEN options will not satisfy your reporting needs. A list of all available APEN forms and associated addendum forms can be found on the Air Pollution Control Division (APCD) website at: www.colorado.gov/pacific/cdphe/air-permits. This emission notice is valid for five (5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Permit Number: 14WE1593 AIRS ID Number: 123 / 9O38 / 0O Section 1 - Administrative Information Company Name': Tallgrass Terminals, LLC Site Name: Buckingham Terminal Site Location Site Location:• 57251 WCR 86 (SW, S34, T8N, R59W) County: Weld New Raymer, CO 80742 NAICS or SIC Code: 486110 Mailing Address: (Include Zip Code) 370 Van Gordon St. Lakewood, CO 80228 Contact Person: Beau Wagner Phone Number: 303-763-3477 E-Mail Address2: beau.wagner@tallgrassenergylp.com t Use the full, legal company name registered with the Colorado Secretary of State. This is the company name that will appear on all documents issued by the APCD. Any changes will require additional paperwork. 2 Permits, exemption letters,and any processing invoices will be issued by the APCD via e-mail to the address provided. 387325 ®� COLORADO Form APCD-2O5 Conciensace S_irz.�e Tank(s) APEN Revision 7,2018 1 I ,-„_ ,_ ,.- Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/ [Leave Clank unless,„P CD a_silo d s per a ,and ',IRS ID] Section 2 - Requested Action NEW permit OR newly-reported emission source ❑✓ Request coverage under traditional construction permit ❑ Request coverage under a General Permit ❑ GP01 ❑ GP08 If General Permit coverage is requested, the General Permit registration fee of$312.50 must be submitted along with the APEN filing fee. -OR- ❑ MODIFICATION to existing permit (check each box below that applies) ❑ Change in equipment ❑ Change company name3 ❑ Change permit limit ❑ Transfer of ownership4 ❑ Other (describe below) -OR ▪ APEN submittal for update only (Note blank APENs will not be accepted) -ADDITIONAL PERMIT ACTIONS - APEN submittal for permit exempt/grandfathered source ❑ Limit Hazardous Air Pollutants (HAPs)with a federally-enforceable limit on Potential To Emit (PTF) Additional Info a Notes: Request additional sources to be included in facility-wide construction permit 14WE1593. 3 For company name change, a completed Company Name Change Certification Form (Form APCD-106)must be submitted. 4 For transfer of ownership, a completed Transfer of Ownership Certification Form (Form APCD-104) must be submitted. Section 3 - General Information General description of equipment and purpose: Two(2)External Floating Roof crude oil storage tanks w/capacity up to 250,000 bbl. Company equipment Identification No. (optional): T-4251 , T-4252 For existing sources, operation began on: For new or reconstructed sources, the projected start-up date is: 01/01/2020 Normal Hours of Source Operation: 24 hours/day 7 days/week 52 weeks/year Storage tank(s) located at: O Exploration a Production (EEtP)site 0 Midstream or Downstream (non EELP)site Will this equipment be operated in any NAAQS nonattainment area? Yes ❑ No Are Flash Emissions anticipated from these storage tanks? ❑ Yes 0 No Is the actual annual average hydrocarbon liquid throughput≥ 500 bbl/day? 0 Yes O No If"yes", identify the stock tank gas-to-oil ratio: _- m3/liter Are these storage tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) O Yes Q No 805 series rules? If so, submit Form APCD-105. Are you requesting≥6 ton/yr VOC emissions (per storage tank), or are uncontrolled actual ❑ Yes Q No emissions≥ 6 ton/yr(per storage tank)? ®� COLORADO Form AFCJ-205 Condensate Storage g Tark(3:� APEN - Revision 7/2018 2 I =eE„,=,,,,, Permit Number: 14WE1593 AIRS ID Number: 123 /9D38/ [Leayetlenk_nll i APCD 11,s-gin& permIt r7 and AIRS DI Section 4 - Storage Tank(s) Information Actual Annual Amount Requested Annual Permit Limits (bbl/year) (bbl/year) Condensate Throughput: 62,050,000 From what year is the actual annual amount? Average API gravity of sales oil: 28-52 degrees RVP of sales oil: 6-9 Tank design: ❑ Fixed roof ❑ Internal floating roof ✓❑ External floating roof Storage #of Liquid Manifold Storage Total Volume of Installation Date of Most Date of First Tank ID Vessels in Storage Tank Storage Tank Recent Storage Vessel in Production (bbl) Storage Tank (month/year) (month/year) T-4251 1 up to 250,000 TBD TBD T-4252 1 up to 250,000 TBD TBD Wells Serviced by this Storage i anic or I arm uattery=teary Sires Gni API Number Name of Well Newly Reported Well O _ I u O 5 Requested values will become permit limitations. Requested limit(s)should consider future growth. 6 The E&P Storage Tank APEN Addendum (Form APCD-212)should be completed and attached when additional space is needed to report all wells that are serviced by the equipment reported on this APEN form. Section 5 - Stack Information Geographical Coordinates (Latitude/Longitude or UTM) 40.613283, -103.971119 Operator Stack Discharge Height Above Temp. Flow Rate Velocity ID No. Ground Level (feet) (°F) (ACFM) (ft/sec) Indicate the direction of the stack outlet: (check one) ❑ Upward O Downward ❑ Upward with obstructing raincap ❑ Horizontal ❑ Other(describe): Indicate the stack opening and size: (check one) ❑Circular Interior stack diameter(inches): ❑ Square/rectangle Interior stack width (inches): Interior stack depth(inches): ❑ Other(describe): Form APCD-2O5 Condensate SLOE :ge Tank(s) ,OPEN F v sion 7/2018 3 ®® C O L O R A D O Permit Number: 14WE1593 AIRS ID Number: 123 19D381 [Lea-,e b[ nk. r s -=CD h , � n_ od a ,per is r =nd AIRS ID] a Section 6 - Control Device Information ❑ Check this box if no emission control equipment or practices are used to reduce emissions, and skip to the next section. Pollutants Controlled: Vapor Size: Make/Model: I—I RarnvPry Unit (VRU): Requested Control Efficiency: VRU Downtime or Bypassed (emissions vented): Pollutants Controlled: Rating: MMBtu/hr Type: Make/Model: ❑ Combustion Requested Control Efficiency: Device: Manufacturer Guaranteed Control Efficiency: Minimum Temperature: Waste Gas Heat Content: Btu/scf Constant Pilot Light: ❑ Yes ❑ No Pilot Burner Rating: MMBtu/hr Description of the closed loop system: ❑ Closed Loop System Pollutants Controlled: VOC/HAPs E Other: Description: External Floating Roof Control Efficiency Requested: Inherent % Section 7 - Gas/Liquids Separation Technology Information (EO P Sites Only) What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? psig Describe the separation process between the well and the storage tanks: ®® C O L O R A D O Form AP-CD-205 Condensate _.� _g Tank(s) !,Fct�! Rerr., i �18 s �0 4 I Permit Number: 14WE1593 AIRS ID Number: 123 19D381 • [Leave dank unfe -APCD has airea ian d a perm is ' and<.IF.S IG1 Section 8 - Emissions Inventory Information Attach all emissions calculations and emission factor documentation to this APEN form. If multiple emission control methods were identified in Section 6, the following table can be used to state the overall (or combined) control efficiency (%reduction): Overall Requested Control Pollutant Descrintinn of(-Antral Mathnrl(c1 rffi-innry (%reduction in emissions) V0C External Floating Roof Inherent Design NOx CO HAPs External Floating Roof Inherent Design Other: From what year is the following reported actual annual emissions data? Criteria Pollutant Emissions Inventory Emission Factor -� — E,-;;; Requested Annual Permit Emission Limit(s)' Pollutant Source Uncontrolled Controlled Uncontrolled Controlled Uncontrolled Basis Units (AP-42, Emissions Emissions Emissions Emissions Mfg.etc) (Tons/year) (Tons/year) (Tons/year) (Tons/year) VOC I 54,248* lb/yr AP-42 27.1 I NOx I I I I CO Non-Criteria Reportable Pollutant Emissions Inventory Chemical Emission Factor Actual Annual Emissions Chemical Name Abstract Source Uncontrolled Controlled (CAS ) Uncontrolled ( ) Units (AP-42, Emissions Emissions8 Number Basis Mfg. etc) (Pounds/year) (Pounds/year) Benzene 71432 Toluene 108883 343* lb/yr 343 Ethylbenzene 100414 Xylene 1330207 277* lb/yr 277 n-Hexane 110543 868* lb/yr 868 2,2,4- 540841 335* lb/yr 335 Trimethylpentane 5 Requested values will become permit limitations. Requested limit(s)should consider future growth. 7 Attach condensate liquid laboratory analysis, stack test results, and associated emissions calculations if you are requesting site specific emissions factors according to the guidance in PS Memo 14-03. 8 Annual emissions fees wilt be based on actual controlled emissions reported. If source has not yet started operating, leave blank. *Please see attached Emission Summary sheet for detailed breakdown of different emission processes that make up the total emission rate. COLORADO Form /' -205 Condensate Sro far Innks! Revision !/2018 5 Permit Number: 14WE1593 AIRS ID Number: 123 /9038/ [LeDve APCD perm IC'-1 Section 9 - Applicant Certification I hereby certify that all information contained herein and information submitted with this application is complete, true, and correct. If this is a registration for coverage under General Permit GP01 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable General Permit. /.C;ir Signature of Legally Authorized Person (not a vendor or consultant) Date Beau Wagner Air Compliance Specialist Name (print) Title Check the appropriate box to request a copy of the: E Draft permit prior to issuance ✓Q Draft permit prior to public notice (Checking any of these boxes may result in an increased fee and/or processing time) This emission notice is valid for five (5)years. Submission of a revised APEN is required 30 days prior to expiration of the five-year term, or when a reportable change is made (significant emissions increase, increase production, new equipment, change in fuel type, etc.). See Regulation No. 3, Part A, II.C. for revised APEN requirements. Send this form along with $191.13 and the General Permit For more information or assistance call: registration fee of$312.50, if applicable, to: Small Business Assistance Program Colorado Department of Public Health and Environment (303) 692-3175 or (303) 692-3148 Air Pollution Control Division APCD-SS-B1 APCD Main Phone Number 4300 Cherry Creek Drive South (303) 692-3150 Denver, CO 80246-1530 Make check payable to: Or visit the APCD website at: Colorado Department of Public Health and Environment https://www.colorado.gov/cdphe/apcd ®® COLORADO Form APCD-205 Condensate �� ;;2 Tan!<rs APEN Reision 7;2018 6 I . . - - ,-,
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