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Equipment  .M-- .  --2 >leaks>=-- .  --2 N provisionNH-- .  --2 ^does not^F-- .  --2 napplyn=-- %III--- $EINE--- !B--  .  -- 2 MYesM-- !=--%-- .  --92 !Equipment leaks provision applies  --%7u7777--- $<72<--- !---  .  -- 2 .Yes@-- %!!-!---- $(-y2(--- !--  .  -- 2 $No$-- .  --~2 O* See Chapter 4 of the updated PR Guidance Document for Group 1 and Group 2 emi        2  ssion points.J- METAFILEPICT>,>R  ~  R>  #` - !a- "-%yyy-&Arial-- .  &Arial -&ArialNe-"Systemn--?2 >%Is it a vent from a wastewater system    >--- .  ---@2 N&drain, tank mixer or sample valve on a  N--- .  ---2 ^ storage tank?^e--- !--%uuu-- .  &Arial-&Arial---F2 *Is it an emission of organic hazardous air --- .  ---<2 #pollutants from a pump, compressor,   --- .  ---H2 +pressure relief device, sampling connection --- .  ---C2 (system, open-ended valve or line, valve, --- .  ---?2 .%or instrumentation system "in organic  .--- .  ---H2 >+hazardous air pollutant service" (equipment >--- .  ---62 Ncontaining or contacting fluid Ns--- .  --- 2 Nt>N|--- .  ---2 N| 5% by N--- .  ---.2 ^weight total organic HAP)?  ^---y77- "-- $<72<--- !/-&Arial- -  .  -- 2 0No>-- !aZ--%yZZyy-- .  --2 . 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WP 7 [2] `.@pPresentations 3.0 Drawing Embed SourceWPDraw30.Drawing9qY*WPCeO&/5,/519 Ȑ+'13 0,,|/|/,+'13 !_.*?%2A`Arial?        @ Doestheventcontainagasstreamwith 20ppmbyvolumeorganicHAPandisit &-?%2A`Arial?        @ continuouslyorperiodicallydischargedduringnormaloperations? +'13 'l%%(+l(+l%+'13 ( E*?%2A`Arial?        @Isthevent/gasstream: )(?%2A`Arial?        @ *(?%2A`Arial?        @- +(?%2A`Arial?        @directlydischargedtotheatmosphere ,(?%2A`Arial?        @or -)(?%2A`Arial?        @ .)(?%2A`Arial?        @- /)(?%2A`Arial?        @routedtoacontroldevicepriortodischargetotheatmosphere 0)(?%2A`Arial?        @or 1v'?%2A`Arial?        @ 2v'?%2A`Arial?        @- 3v',?%2A`Arial?        @divertedtoaproductrecoverypriortocontrolordischargetotheatmosphere? 4 &5?%2A`Arial?        @Note:Theabovelistgivesexamplesofventorgasstreamsandmaynotbeallinclusive.+'13 5?#3#3#?#?#+'13 6 "?%2A`Arial?        @Doestheventorgasstreamcomefrom: 7bE!?%2A`Arial?        @-Gasstreamsroutedtoafuelgassystem 8b ?%2A`Arial?        @-Reliefvalvedischarges 9b?%2A`Arial?        @-Leaksfromequipmentregulatedunder40CFR63.648 :b)?%2A`Arial?        @-Episodicornonroutinereleasessuchasmaintenanceorupsets ;bu?%2A`Arial?        @- <u?%2A`Arial?        @Insitu ={u?%2A`Arial?        @samplingsystems(onstreamanalyzers) >b?%2A`Arial?        @-Catalyticcrackingunitcatalystregenerationvents ?b ?%2A`Arial?        @-Catalyticreformerregenerationvents @bZ?%2A`Arial?        @-Sulfurplantvents Ab?%2A`Arial?        @-Ventsfromcontroldevices Bb>?%2A`Arial?        @-Ventsfromanystrippingoperationsappliedtocomplywiththewastewaterprovisionsof40CFR Cb>?%2A`Arial?        @򀀀63SubpartCC,G,orFF Db@?%2A`Arial?        @-Cokingunitventsassociatedwithcokedrumdepressuringatorbelowacokedrumoutletpressure Eb>?%2A`Arial?        @򀀀of15poundspersquareinchgauge,deheading,draining,ordecoking(cokecutting)orpressure Fb"?%2A`Arial?        @򀀀testingafterdecoking Gbm?%2A`Arial?        @-Ventsfromstoragevessels Hb?%2A`Arial?        @-Emissionsfromwastewatercollectionandconveyancesystems?+'13 I__+'13 J2=?%2A`Arial?        @Doestheventorgasstreamcomefrom:causticwashaccumulators,distillationlowercondensers/ KI}??%2A`Arial?        @accumulators,flash/knockoutdrums,reactorvessels,scrubberoverheads,stripperoverheads,vacuum L$?%2A`Arial?        @accumulators,blowdowncondensers/accumulators,anddelayedcokervents? 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       @Group1miscellaneous w ?%2A`Arial?        @processvent*+'13 x+'13 y'?%2A`Arial?        @Group1miscellaneous zb ?%2A`Arial?        @processvent*+'13 {r yyr r +'13 | ?%2A`Arial?        @Group2miscellaneous }. ?%2A`Arial?        @processvent*+'13 ~  +'13 [?%2A`Arial?        @Group2miscellaneous  ?%2A`Arial?        @processvent*+'13   1 `1 `mm.n.n+'13 za?%2A`Arial?        @Yes+'13      1 `4   4 1 `  .i .i +'13 a?%2A`Arial?        @No+'13 QQ=))1 `h)h1 `..+'13 a?%2A`Arial?        @Yes+'13 QQW]]1 `]1 `..+'13 a?%2A`Arial?        @No+'13  $&$&  $+'13 !?%2A`Arial?        @Miscellaneous !?%2A`Arial?        @processvent G"[?%2A`Arial?        @provision !?%2A`Arial?        @doesnotapply+'13 3.@3.e#3.e# 1 `# u#7# #  3i  `Y " Y Y "1 `>  >+'13 ?%2A`Arial?        @Yes+'13 U(U(u#U(u# 1 `# u#7# #  _u#u# `7#u#$#7#+'3 *?%2A`Arial?        @*SeeChapter4forapplicablerequirementsforGroup1andGroup2emissionpoints.+'13 `"( $( $("("(+'13 '#E(?%2A`Arial?        @No+'13 `"$$c"c"+'13 3#?%2A`Arial?        @No+'13 _ _   _ +'13 & ?%2A`Arial?        @Isventassociatedwithanexistingornewsource?+'13 #1 `2 x321 `"- $- $x."x."-+'13 '#-?%2A`Arial?        @No+'13 `$XX[$[$+'13 I?%2A`Arial?        @Yes% '$   +"""!"*"""!!,""   % """""" $$.*" BOlePartOlePres0009T"QdNT '*   d"Q3f3333f333ff3fffff3f3f̙3f3333f3333333333f3333333f3f33ff3f3f3f3333f3333333f3̙333333f333ff3ffffff3f33f3ff3f3f3ffff3fffffffffff3fffffff3fff̙ffff3fffff???__ߟ߿3f3333f333ff3fffff3f3f̙3f3f3333f333ff3fffff̙̙3̙f̙̙̙3f̙3f3f3333f333ff3fffff3f3f̙3f45    "--$5T5TPP55 "---%5T5TPP55-&Arial-- .  &Arial-&Arial-"Systemn--B2 x'Does the vent contain a gas stream with   [---B2 [' 20 ppm by volume organic HAP and is it  1-- .  ---i2 &Acontinuously or periodically discharged during normal operations? & --- !uY[--%[[YSYS[-- .  &Arial-&Arial- -- *2 kIs the vent/gas stream: k--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- B2 e' directly discharged to the atmosphere  2--- .  - -- 2 5or@--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- i2 eA routed to a control device prior to discharge to the atmosphere  --- .  - -- 2 or--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- ~2 eO diverted to a product recovery prior to control or discharge to the atmosphere  2 ?--- .  - -- ~2 ]ONote: The above list gives examples of vent or gas streams and may not be all    2  inclusive.1--- !)C--%CCkkC-- .  - -- @2 &Does the vent or gas stream come from:    --- .  - -- F2 $F* - Gas streams routed to a fuel gas system   $&--- .  - -- .2 2F - Relief valve discharges2--- .  - -- W2 @F5 - Leaks from equipment regulated under 40 CFR 63.648   @q--- .  - -- g2 OF@ - Episodic or nonroutine releases such as maintenance or upsets O--- .  - -- 2 ]F - ]Q--- .  - -- 2 ]PIn situ]p--- .  - -- @2 ]q& sampling systems (onstream analyzers)   ]F--- .  - -- X2 kF6 - Catalytic cracking unit catalyst regeneration ventskV--- .  - -- C2 zF( - Catalytic reformer regeneration vents z--- .  - -- '2 F - Sulfur plant vents--- .  - -- 32 F - Vents from control devices --- .  - -- ~2 FO - Vents from any stripping operations applied to comply with the wastewater pr  $2 ovisions of 40 CFR L--- .  - -- .2 F 63 Subpart CC, G, or FF  --- .  - -- ~2 FO - Coking unit vents associated with coke drum depressuring at or below a coke    '2 drum outlet pressure [--- .  - -- ~2 FO of 15 pounds per square inch gauge, deheading, draining, or decoking (coke c$2 utting) or pressureL--- .  - -- -2 F testing after decoking--- .  - -- 32 F - Vents from storage vessels --- .  - -- f2 F? - Emissions from wastewater collection and conveyance systems?     --- !XY2+--%++22+-- .  - -- ~2 DOODoes the vent or gas stream come from: caustic wash accumulators, distillation      "2 D lower condensers/ DV--- .  - -- ~2 RDOaccumulators, flash/knockout drums, reactor vessels, scrubber overheads, stripp  %2 Rer overheads, vacuum Rb--- .  - -- s2 `Haccumulators, blowdown condensers/accumulators, and delayed coker vents?    `"--- .  - -- ~2 }1ONote: The above list gives examples of where vent or gas streams may originate    '2 } and may not be all i }E-- 2 }E nclusive.}s--- !L 7--%7G7??G7G-- .  - -- 2 Existing Source:--- .  - -- 32 ,@Is organic HAP concentration  ,--- .  - -- 2 ,>,--- .  - -- 2 , 20 ppmv,  ,--- .  - -- 2 ,and,3--- .  - -- %2 :`total VOC emissions   :--- .  - -- 2 :>:--- .  - -- 2 : 33 kg/day?:--- !L!w--%wGwGwG-- .  - -- 2  New Source:  &--- .  - -- 32 ,Is organic HAP concentration  ,--- .  - -- 2 ,>,&--- .  - -- 2 ,& 20 ppmv,  ,]--- .  - -- 2 ,^and,r--- .  - -- 2 ,t total,--- .  - -- 2 :VOC emissions   : --- .  - -- 2 : >:--- .  - -- 2 : 6.8 kg/day?:U---5VQW--- $[OWYQP[O--- !>L-&Arial- -  .  -- 2 IMYesI_--WW--- $\WR\--- !M--  .  -- 2 MYes_--W)W--- $\(W2R(\(--- !O--  .  -- 2 PNo ^--%VV--- $--- !(--  .  -- 2 Existing--%VV--- $  --- !--  .  -- 2 New-- !(p--%pp-- .  --'2 $Group 1 miscellaneous  -- .  --2 = process vent*-- !(pj--%jjppj-- .  --'2 tGroup 1 miscellaneous  -- .  --2  process vent*-- !(p--%pRpR-- .  --'2 Group 2 miscellaneous  F-- .  --2  process vent*--- !(p--%pp-- .  --'2 Group 2 miscellaneous  -- .  --2 5 process vent*}--%G\\b\bh--- $gfbp]fgf--- !T--  .  -- 2 _Yes_--%G\\ \ h--- $f pff--- !T--  .  -- 2 _No_--%G\\\h--- $fpff--- !T--  .  -- 2 _Yes_--%G\0\Y\Yh--- $_fYpUf_f--- !T(--  .  -- 2 _)No_7-- !rmE--%E E -- .  --2 k Miscellaneous k-- .  --2 z process ventz-- .  --2  provision-- .  --2 does not apply-- %eW=--- $<E<<---~k~--- $y~y--- !v{--  .  -- 2 |Yes-- %S`=--- $<E<<--- %]]]--- $--- .  --~2 QO* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission po     2 ints.-- !--  .  -- 2 No-- !U--  .  -- 2 `No`-- !H--%-- .  --R2 2Is vent associated with an existing or new source? --WV--- $[VQ[--- !--  .  -- 2 !No!-- !K--  .  -- 2 NYes`- METAFILEPICT"QpVT"Qd '*   d"Q3f3333f333ff3fffff3f3f̙3f3333f3333333333f3333333f3f33ff3f3f3f3333f3333333f3̙333333f333ff3ffffff3f33f3ff3f3f3ffff3fffffffffff3fffffff3fff̙ffff3fffff???__ߟ߿3f3333f333ff3fffff3f3f̙3f3f3333f333ff3fffff̙̙3̙f̙̙̙3f̙3f3f3333f333ff3fffff3f3f̙3f45    "--$5T5TPP55 "---%5T5TPP55-&Arial-- .  &Arial-&Arial-"Systemn--B2 x'Does the vent contain a gas stream with   [---B2 [' 20 ppm by volume organic HAP and is it  1-- .  ---i2 &Acontinuously or periodically discharged during normal operations? & --- !uY[--%[[YSYS[-- .  &Arial-&Arial- -- *2 kIs the vent/gas stream: k--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- B2 e' directly discharged to the atmosphere  2--- .  - -- 2 5or@--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- i2 eA routed to a control device prior to discharge to the atmosphere  --- .  - -- 2 or--- .  - -- 2 ] `--- .  - -- 2 a-e--- .  - -- ~2 eO diverted to a product recovery prior to control or discharge to the atmosphere  2 ?--- .  - -- ~2 ]ONote: The above list gives examples of vent or gas streams and may not be all    2  inclusive.1--- !)C--%CCkkC-- .  - -- @2 &Does the vent or gas stream come from:    --- .  - -- F2 $F* - Gas streams routed to a fuel gas system   $&--- .  - -- .2 2F - Relief valve discharges2--- .  - -- W2 @F5 - Leaks from equipment regulated under 40 CFR 63.648   @q--- .  - -- g2 OF@ - Episodic or nonroutine releases such as maintenance or upsets O--- .  - -- 2 ]F - ]Q--- .  - -- 2 ]PIn situ]p--- .  - -- @2 ]q& sampling systems (onstream analyzers)   ]F--- .  - -- X2 kF6 - Catalytic cracking unit catalyst regeneration ventskV--- .  - -- C2 zF( - Catalytic reformer regeneration vents z--- .  - -- '2 F - Sulfur plant vents--- .  - -- 32 F - Vents from control devices --- .  - -- ~2 FO - Vents from any stripping operations applied to comply with the wastewater pr  $2 ovisions of 40 CFR L--- .  - -- .2 F 63 Subpart CC, G, or FF  --- .  - -- ~2 FO - Coking unit vents associated with coke drum depressuring at or below a coke    '2 drum outlet pressure [--- .  - -- ~2 FO of 15 pounds per square inch gauge, deheading, draining, or decoking (coke c$2 utting) or pressureL--- .  - -- -2 F testing after decoking--- .  - -- 32 F - Vents from storage vessels --- .  - -- f2 F? - Emissions from wastewater collection and conveyance systems?     --- !XY2+--%++22+-- .  - -- ~2 DOODoes the vent or gas stream come from: caustic wash accumulators, distillation      "2 D lower condensers/ DV--- .  - -- ~2 RDOaccumulators, flash/knockout drums, reactor vessels, scrubber overheads, stripp  %2 Rer overheads, vacuum Rb--- .  - -- s2 `Haccumulators, blowdown condensers/accumulators, and delayed coker vents?    `"--- .  - -- ~2 }1ONote: The above list gives examples of where vent or gas streams may originate    '2 } and may not be all i }E-- 2 }E nclusive.}s--- !L 7--%7G7??G7G-- .  - -- 2 Existing Source:--- .  - -- 32 ,@Is organic HAP concentration  ,--- .  - -- 2 ,>,--- .  - -- 2 , 20 ppmv,  ,--- .  - -- 2 ,and,3--- .  - -- %2 :`total VOC emissions   :--- .  - -- 2 :>:--- .  - -- 2 : 33 kg/day?:--- !L!w--%wGwGwG-- .  - -- 2  New Source:  &--- .  - -- 32 ,Is organic HAP concentration  ,--- .  - -- 2 ,>,&--- .  - -- 2 ,& 20 ppmv,  ,]--- .  - -- 2 ,^and,r--- .  - -- 2 ,t total,--- .  - -- 2 :VOC emissions   : --- .  - -- 2 : >:--- .  - -- 2 : 6.8 kg/day?:U---5VQW--- $[OWYQP[O--- !>L-&Arial- -  .  -- 2 IMYesI_--WW--- $\WR\--- !M--  .  -- 2 MYes_--W)W--- $\(W2R(\(--- !O--  .  -- 2 PNo ^--%VV--- $--- !(--  .  -- 2 Existing--%VV--- $  --- !--  .  -- 2 New-- !(p--%pp-- .  --'2 $Group 1 miscellaneous  -- .  --2 = process vent*-- !(pj--%jjppj-- .  --'2 tGroup 1 miscellaneous  -- .  --2  process vent*-- !(p--%pRpR-- .  --'2 Group 2 miscellaneous  F-- .  --2  process vent*--- !(p--%pp-- .  --'2 Group 2 miscellaneous  -- .  --2 5 process vent*}--%G\\b\bh--- $gfbp]fgf--- !T--  .  -- 2 _Yes_--%G\\ \ h--- $f pff--- !T--  .  -- 2 _No_--%G\\\h--- $fpff--- !T--  .  -- 2 _Yes_--%G\0\Y\Yh--- $_fYpUf_f--- !T(--  .  -- 2 _)No_7-- !rmE--%E E -- .  --2 k Miscellaneous k-- .  --2 z process ventz-- .  --2  provision-- .  --2 does not apply-- %eW=--- $<E<<---~k~--- $y~y--- !v{--  .  -- 2 |Yes-- %S`=--- $<E<<--- %]]]--- $--- .  --~2 QO* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission po     2 ints.-- !--  .  -- 2 No-- !U--  .  -- 2 `No`-- !H--%-- .  --R2 2Is vent associated with an existing or new source? --WV--- $[VQ[--- !--  .  -- 2 !No!-- !K--  .  -- 2 NYes`- *#  _   FIGURE22.DeterminationofApplicabilityforMiscellaneousProcessVents   WPWin 6.0/OLE 1.0 Prefix Information MarkerWPDraw30.Drawingtࡱ>   "#$%&'()*+,-./012345678Root Entry`.@p@G/Ole 9WPG208CompObjp)F! WPWin61[1] `.@pPresentations 3.0 Drawing Embed SourceWPDraw30.Drawing9qX3WPC6#,&,k519+'13*C*Cw,w,*+'13 ! +?%2A`Arial?        @ Isitwaterorwastewaterthat,duringproductionorprocessing: +'13 " c c& & +'13 ## $?%2A`Arial?        @Comesintodirectcontactwithorresults $ $?%2A`Arial?        @fromtheproductionoruseofanyraw %D O#?%2A`Arial?        @material,intermediateproduct,finished &{ "?%2A`Arial?        @product,byproduct,orwasteproduct?+'13 ' ccg g +'13 (x 0?%2A`Arial?        @Isdischargedintoanyindividualdrain )g?%2A`Arial?        @system?+'13.**  }B (c(c  (+'13 + $?%2A`Arial?        @Doesrefineryhaveatotalannualbenzene , [?%2A`Arial?        @loading -L [?%2A`Arial?        @> . [?%2A`Arial?        @10megagramsperyear, //[?%2A`Arial?        @ and  0\[?%2A`Arial?        @a 1{ ?%2A`Arial?        @flowrate 2( ?%2A`Arial?        @> 3 ?%2A`Arial?        @0.02litersperminute, 4??%2A`Arial?        @ and  5 ?%2A`Arial?        @benzeneconcentration 6?%2A`Arial?        @> 7?%2A`Arial?        @10ppmby 8 ?%2A`Arial?        @weight, 9 ?%2A`Arial?        @ and  :G ?%2A`Arial?        @subjecttocontrolrequirements ; ;?%2A`Arial?        @under40CFR61SubpartFF?+'13 <*@'1 `=/O'&O'/O' >  `?/g/1 `@wwkk+'13 A?%2A`Arial?        @Yes+'13 BS [ [ S S +'13 C_ ?%2A`Arial?        @Group1wastewater D ?%2A`Arial?        @stream*+'13 E     +'13 F(_ ?%2A`Arial?        @Group2wastewater G ?%2A`Arial?        @stream*+'13 H(c c c 1 `I   1 `Jl l ``+'13 Kw ;?%2A`Arial?        @Yes+'13 L(cc c 1 `ML    L 1 `N__+'13 O;?%2A`Arial?        @No+'13 Pc##8#81 `Qx8kx1 `RoC$o#,#,C$+'13 S{#?%2A`Arial?        @No+'13 Tg!!kgkg+'13 U4?%2A`Arial?        @Wastewaterprovision Vk?%2A`Arial?        @doesnotapply+'13 W1 `X//1 `Ywswkks+'13 Z?%2A`Arial?        @Yes+'13 [c1 `\?g?1 `]\CC\+'13 ^?%2A`Arial?        @No+'13 _O{"{"+O+O{+'13 `p<?%2A`Arial?        @[Examplesofwastewaterare:feedtankdrawdown;waterformedduringachemicalreactionorusedasa ap>?%2A`Arial?        @reactant;waterusedtowashimpuritiesfromorganicproductsorreactants;waterusedtocoolorquench bp<??%2A`Arial?        @organicvaporstreamsthroughdirectcontact;andcondensedsteamfromjetejectorsystemspullingvacuum cps?%2A`Arial?        @onvesselscontainingorganics.] d*?%2A`Arial?        @*SeeChapter4forapplicablerequirementsforGroup1andGroup2emissionpoints.+'13" e__+'13 f?%2A`Arial?        @Applicability g@?%2A`Arial?        @criteriaarethe h/?%2A`Arial?        @samefor ig?%2A`Arial?        @existingand j?%2A`Arial?        @newsourcesBOlePartOlePres000!.PJ^r. 9   ^PJ3f3333f333ff3fffff3f3f̙3f3333f3333333333f3333333f3f33ff3f3f3f3333f3333333f3̙333333f333ff3ffffff3f33f3ff3f3f3ffff3fffffffffff3fffffff3fff̙ffff3fffff???__ߟ߿3f3333f333ff3fffff3f3f̙3f3f3333f333ff3fffff̙̙3̙f̙̙̙3f̙3f3f3333f333ff3fffff3f3f̙3f45   - !1t- "-%t5t5t5-&Arial-- .  &ArialNe-&Arial-"Systemn--g2 !|@Is it water or wastewater that, during production or processing:    ! --- !y x--%xx-- .  --E2 )Comes into direct contact with or results   -- .  --?2 %from the production or use of any raw  -- .  --C2 (material, intermediate product, finished  -- .  --?2 %product, byproduct, or waste product? -- !; 9--%s99ss-- .  --B2 R'Is discharged into any individual drainR-- .  --2 c.system? c_-- !--%;;;-- .  --E2 )Does refinery have a total annual benzene -- .  --2 loading -- .  &Arial-&Arial--- 2 >--- .  --+2  10 megagrams per year,   -- .  --- 2 and --- .  -- 2  a-- .  --2  flow rate   -- .  --- 2 >--- .  ---2  0.02 liters per minute,  -- .  --- 2 and --- .  --(2 benzene concentration f-- .  -- 2 g>o-- .  --2 o 10 ppm by -- .  --2 weight, -- .  --- 2 and  --- .  --62 subject to control requirements -- .  --02 under 40 CFR 61 Subpart FF?   --5GpG- "- - $LnGxBnLn---G0G-- - $L/G9B/L/--- ! =-&Arial- -  .  -- 2 >YesP-- !=|--%|;|;-- .  --"2 Group 1 wastewater   /-- .  --2 stream*  -- !=|S--%SS||S-- .  --"2 _Group 2 wastewater   -- .  --2 stream* --%G4GXXXs-- - $r|rr--- !Q--  .  -- 2 [Yes[&--%G4GXqXXs-- - $r|rr--- !Qi--  .  -- 2 [jNo[w-- %VV0-- - $\/V9R/\/--- ! --  .  -- 2 No-- !:9--%r99rr-- .  --%2 RWastewater provision  R-- .  --2 b+does not applyb--sGG-- - $LGBL--- !=--  .  -- 2 >YesP--VV-- - $QV[Q--- !O--  .  -- 2 YNoY-- !a0--%0L0L0L-- .  --~2 2O[Examples of wastewater are: feed tank drawdown; water formed during a chemica        '2 l reaction or used as-- 2  a-- .  --~2 2Oreactant; water used to wash impurities from organic products or reactants; wat     '2 er used to cool or qu|-- 2 |ench-- .  --~2 (2Oorganic vapor streams through direct contact; and condensed steam from jet ejec   '2 (tor systems pulling v (--2 (acuum (-- .  --72 82 on vessels containing organics.]8-- .  --~2  O* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission po      2 ints.-- -$&u&u&---%&u&u&-- .  --2 ! Applicability g-- .  --2 criteria are theo-- .  --2 *same for ^-- .  --2 ! existing andh-- .  --2   new sources k- METAFILEPICTPJoz.PJ^ 9   ^PJ3f3333f333ff3fffff3f3f̙3f3333f3333333333f3333333f3f33ff3f3f3f3333f3333333f3̙333333f333ff3ffffff3f33f3ff3f3f3ffff3fffffffffff3fffffff3fff̙ffff3fffff???__ߟ߿3f3333f333ff3fffff3f3f̙3f3f3333f333ff3fffff̙̙3̙f̙̙̙3f̙3f3f3333f333ff3fffff3f3f̙3f45   - !1t- "-%t5t5t5-&Arial-- .  &ArialNe-&Arial-"Systemn--g2 !|@Is it water or wastewater that, during production or processing:    ! --- !y x--%xx-- .  --E2 )Comes into direct contact with or results   -- .  --?2 %from the production or use of any raw  -- .  --C2 (material, intermediate product, finished  -- .  --?2 %product, byproduct, or waste product? -- !; 9--%s99ss-- .  --B2 R'Is discharged into any individual drainR-- .  --2 c.system? c_-- !--%;;;-- .  --E2 )Does refinery have a total annual benzene -- .  --2 loading -- .  &Arial-&Arial--- 2 >--- .  --+2  10 megagrams per year,   -- .  --- 2 and --- .  -- 2  a-- .  --2  flow rate   -- .  --- 2 >--- .  ---2  0.02 liters per minute,  -- .  --- 2 and --- .  --(2 benzene concentration f-- .  -- 2 g>o-- .  --2 o 10 ppm by -- .  --2 weight, -- .  --- 2 and  --- .  --62 subject to control requirements -- .  --02 under 40 CFR 61 Subpart FF?   --5GpG- "- - $LnGxBnLn---G0G-- - $L/G9B/L/--- ! =-&Arial- -  .  -- 2 >YesP-- !=|--%|;|;-- .  --"2 Group 1 wastewater   /-- .  --2 stream*  -- !=|S--%SS||S-- .  --"2 _Group 2 wastewater   -- .  --2 stream* --%G4GXXXs-- - $r|rr--- !Q--  .  -- 2 [Yes[&--%G4GXqXXs-- - $r|rr--- !Qi--  .  -- 2 [jNo[w-- %VV0-- - $\/V9R/\/--- ! --  .  -- 2 No-- !:9--%r99rr-- .  --%2 RWastewater provision  R-- .  --2 b+does not applyb--sGG-- - $LGBL--- !=--  .  -- 2 >YesP--VV-- - $QV[Q--- !O--  .  -- 2 YNoY-- !a0--%0L0L0L-- .  --~2 2O[Examples of wastewater are: feed tank drawdown; water formed during a chemica        '2 l reaction or used as-- 2  a-- .  --~2 2Oreactant; water used to wash impurities from organic products or reactants; wat     '2 er used to cool or qu|-- 2 |ench-- .  --~2 (2Oorganic vapor streams through direct contact; and condensed steam from jet ejec   '2 (tor systems pulling v (--2 (acuum (-- .  --72 82 on vessels containing organics.]8-- .  --~2  O* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission po      2 ints.-- -$&u&u&---%&u&u&-- .  --2 ! Applicability g-- .  --2 criteria are theo-- .  --2 *same for ^-- .  --2 ! existing andh-- .  --2   new sources k- *#  _   FIGURE23.DeterminationofApplicabilityforStorageVessels   ~D:\EricF\MACT\graphics\Pvents.wmfWPCeO&/5,/519 Ȑ+'13 0,,|/|/,+'13 !_.*?%2A`Arial?        @ Doestheventcontainagasstreamwith 20ppmbyvolumeorganicHAPandisit &-?%2A`Arial?        @ continuouslyorperiodicallydischargedduringnormaloperations? +'13 'l%%(+l(+l%+'13 ( E*?%2A`Arial?        @Isthevent/gasstream: )(?%2A`Arial?        @ *(?%2A`Arial?        @- +(?%2A`Arial?        @directlydischargedtotheatmosphere ,(?%2A`Arial?        @or -)(?%2A`Arial?        @ .)(?%2A`Arial?        @- /)(?%2A`Arial?        @routedtoacontroldevicepriortodischargetotheatmosphere 0)(?%2A`Arial?        @or 1v'?%2A`Arial?        @ 2v'?%2A`Arial?        @- 3v',?%2A`Arial?        @divertedtoaproductrecoverypriortocontrolordischargetotheatmosphere? 4 &5?%2A`Arial?        @Note:Theabovelistgivesexamplesofventorgasstreamsandmaynotbeallinclusive.+'13 5?#3#3#?#?#+'13 6 "?%2A`Arial?        @Doestheventorgasstreamcomefrom: 7bE!?%2A`Arial?        @-Gasstreamsroutedtoafuelgassystem 8b ?%2A`Arial?        @-Reliefvalvedischarges 9b?%2A`Arial?        @-Leaksfromequipmentregulatedunder40CFR63.648 :b)?%2A`Arial?        @-Episodicornonroutinereleasessuchasmaintenanceorupsets ;bu?%2A`Arial?        @- <u?%2A`Arial?        @Insitu ={u?%2A`Arial?        @samplingsystems(onstreamanalyzers) >b?%2A`Arial?        @-Catalyticcrackingunitcatalystregenerationvents ?b ?%2A`Arial?        @-Catalyticreformerregenerationvents @bZ?%2A`Arial?        @-Sulfurplantvents Ab?%2A`Arial?        @-Ventsfromcontroldevices Bb>?%2A`Arial?        @-Ventsfromanystrippingoperationsappliedtocomplywiththewastewaterprovisionsof40CFR Cb>?%2A`Arial?        @򀀀63SubpartCC,G,orFF Db@?%2A`Arial?        @-Cokingunitventsassociatedwithcokedrumdepressuringatorbelowacokedrumoutletpressure Eb>?%2A`Arial?        @򀀀of15poundspersquareinchgauge,deheading,draining,ordecoking(cokecutting)orpressure Fb"?%2A`Arial?        @򀀀testingafterdecoking Gbm?%2A`Arial?        @-Ventsfromstoragevessels Hb?%2A`Arial?        @-Emissionsfromwastewatercollectionandconveyancesystems?+'13 I__+'13 J2=?%2A`Arial?        @Doestheventorgasstreamcomefrom:causticwashaccumulators,distillationlowercondensers/ KI}??%2A`Arial?        @accumulators,flash/knockoutdrums,reactorvessels,scrubberoverheads,stripperoverheads,vacuum L$?%2A`Arial?        @accumulators,blowdowncondensers/accumulators,anddelayedcokervents? M`aI?%2A`Arial?        @Note:Theabovelistgivesexamplesofwhereventorgasstreamsmayoriginateandmaynotbeallinclusive.+'13 N8 8 +'13 OD ?%2A`Arial?        @ExistingSource: P"?%2A`Arial?        @IsorganicHAPconcentration Q ?%2A`Arial?        @> RG ?%2A`Arial?        @20ppmv, S?%2A`Arial?        @and T(?%2A`Arial?        @totalVOCemissions U( (?%2A`Arial?        @> V (?%2A`Arial?        @33kg/day?+'13 WJY Y 8 J8 J+'13 XD ?%2A`Arial?        @NewSource: Y?%2A`Arial?        @IsorganicHAPconcentration Z?%2A`Arial?        @> [?%2A`Arial?        @20ppmv, \?%2A`Arial?        @and ]?%2A`Arial?        @total ^n(?%2A`Arial?        @VOCemissions _(?%2A`Arial?        @> `(?%2A`Arial?        @6.8kg/day?+'13 a,+1 `b+(+x++1 `c3~,3+3+3~,+'13 d@+?%2A`Arial?        @Yes+'13 e% $1 `f$#|$$1 `g:$:6$96$9$+'13 hFi$?%2A`Arial?        @Yes+'13 i#1 `j|1 `kWwWw+'13 lc?%2A`Arial?        @No+'13 m_ 3 3  3  1 `nY  8  Y 1 `o +'13 p ?%2A`Arial?        @Existing+'13 q_ 3 3 Q3 Q 1 `r Q8   1 `sq q   +'13 t} ?%2A`Arial?        @New+'13 u>EE>>+'13 v?%2A`Arial?        @Group1miscellaneous w ?%2A`Arial?        @processvent*+'13 x+'13 y'?%2A`Arial?        @Group1miscellaneous zb ?%2A`Arial?        @processvent*+'13 {r yyr r +'13 | ?%2A`Arial?        @Group2miscellaneous }. ?%2A`Arial?        @processvent*+'13 ~  +'13 [?%2A`Arial?        @Group2miscellaneous  ?%2A`Arial?        @processvent*+'13   1 `1 `mm.n.n+'13 za?%2A`Arial?        @Yes+'13      1 `4   4 1 `  .i .i +'13 a?%2A`Arial?        @No+'13 QQ=))1 `h)h1 `..+'13 a?%2A`Arial?        @Yes+'13 QQW]]1 `]1 `..+'13 a?%2A`Arial?        @No+'13  $&$&  $+'13 !?%2A`Arial?        @Miscellaneous !?%2A`Arial?        @processvent G"[?%2A`Arial?        @provision !?%2A`Arial?        @doesnotapply+'13 3.@3.e#3.e# 1 `# u#7# #  3i  `Y " Y Y "1 `>  >+'13 ?%2A`Arial?        @Yes+'13 U(U(u#U(u# 1 `# u#7# #  _u#u# `7#u#$#7#+'3 *?%2A`Arial?        @*SeeChapter4forapplicablerequirementsforGroup1andGroup2emissionpoints.+'13 `"( $( $("("(+'13 '#E(?%2A`Arial?        @No+'13 `"$$c"c"+'13 3#?%2A`Arial?        @No+'13 _ _   _ +'13 & ?%2A`Arial?        @Isventassociatedwithanexistingornewsource?+'13 #1 `2 x321 `"- $- $x."x."-+'13 '#-?%2A`Arial?        @No+'13 `$XX[$[$+'13 I?%2A`Arial?        @Yes% '$   +"""!"*"""!!,""   % """""" $$.*" D:\EricF\MACT\graphics\Svessels.wmfWPCXX!0ƚX>P [ 0   -  "-$x} } xx} "--% Arial-"Systemn- . -!,Is it a tank or other vessel that is used to!/store organic liquids? (i.e., is this a storage!#vessel "as described in the rule"?)JA- -  "-$W W ---- . -!Is it permanently attached to a!motor vehicle such as a truck,d!railcar, barge or ship?$- -  "-${  {{---- . -!+Is it a pressure vessel designed to operate!*in excess of 204.9 kilopascals and without !emission to the atmosphere?o- -  "-$W W ---- . -!!Does it have a capacity less thanVV!40 cubic meters?y- -  "-$`    ` ` ---- . -! Is it used as a bottoms receiverg y !tank? R - -  "-% } c-- "- $ [  [ [-- Arial---- $s s 9 9 -- . -!Yesy - -  "-%  --- $    ------ $ ]   ]-- . -!No - -  "-%  --- $    ------ $ (   (-- . -!Noj - -  "-%  --- $ ------ $ J J -- . -!No - -  "-$# . .## ---- . - !Storage !vessels ! provisionZ!does!not"  !apply - -  "-%W K K  ss--- $T#sT---- . - -  "-%W os--- $T#sT---- . - -  "-$Y[ [ >Y>Y[---- . -!Is tank associated with an!existing or new source?- -  "-$`5  5   ` `5 ---- . -!Is it used as a wastewater  ! storage tank? - -  "-%  --- $  ------ $ e e -- . -!No - -  "-% 5 --- $  > ------ $ -- . -!No - -  "-$52525--0 Arial--% Arialig- - Arial- -( ArialK- -- -- -- -- . -!Existing Source:0y- ! Is capacity - !>9- ! 177 mi- !3f-! - !and -!vapor pressure G- !>- ! 10.4!kPa (maximum) and a- !>a-! 8.3 kPa (annual average)a!,am- !and 6-!!liquid HAP content > 4% by weight!(annual average)?)- -  "- $ VV2 2 V-- --- -- -- -- -- -- -- -- -- -- -- . - ! New Source: - ! Is capacity y' - !>y - ! 151 my - !3^ -! y - !and y* -!vapor pressure y - !>y- ! 3.4 kPayG ! (maximum),  - !and  -!!liquid HAP content > 2% by weight !(annual average)?A~ - !OR -!Is capacity between 76 Tv - !andT - ! 151 mTm- !39j- ! , and vaporT ! pressure  - !>p -! 77 kPa (maximum),  - !and-! liquid HAP >2%1!by weight (annual average)? - -  "- $5ff55f-- -- . -!Group 1 storage !vessel*r- -  "- $ f f   f-- -- . -!Group 1 storage !vessel*< - -  "- $OffOOf-- -- . -!Group 2 storage !vessel*- -  "- $fff-- -- . -!Group 2 storage !vessel*V- -  "- %ttt- -- $------ $F>>F-- . -!Yes- -  "- %t tt- -- $00------ $F;;F-- . -!No- -  "- % V    - -- $    ------ $ ~   ~-- . -!Yes - -  "- % V - -- $------ $~~-- . -!No- -  "- % [ [- -- $#2#------ $-- . - !Existing- -  "- % [    - -- $  2  ------ $w w   -- . -!New} - -  "- %   3 ss- -- $T#sT---- . - -  "- % z ss- -- $T#sT---- . - -  "- % ss- -- $T#sT---- . - --$H 22H H ---- . -!Yese - --$g # #m g m g ---- . -!Yes - -  "- $tt**t-- -- . -!Storage vessels !provision does4 ! not applyL- -  "- %x- -- $------ $ZZ-- . -!No- -- . -0!T* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.B- --$d   7d 7d ---- . -!Yes - --$N &9&9N N &---- . -!Yes - --$N 9 9L N L N ---- . -!Yes -(Vm$0   (,!$0  0` (#(#  D:\EricF\MACT\graphics\Gasoline.wmfWPCXX]]!]lƚ]XI  0  ] -  "-$Vq Vq V "--% Arials -"Systemn- . -!Is it any of the following:n!,loading arms, pumps, meters, shutoff valves,!relief valves, or!)other piping and valves necessary to filliT!gasoline cargo tanks?- -  "-$}c }c }---- . -!Is it a gasoline loading rack7!classified under SIC 2911?;- -  "-$ c c    ---- . -!$Does it have a gasoline throughput > !'75,700 liters (20,000 gallons) per day?R g- -  "-%(V*-- "- $I* I-- Arial---- $tiit-- . -!Yes- -  "-$[GG [ [G---- . -!Group 1 gasoliner ! loading rack*.- -  "-$uG G u uG---- . -!Group 2 gasoliner ! loading rack*H- -  "-%* * #   --- $<   < ------ $  c c -- . -!Yes - -  "-%* * 0 7 7 --- $V 7  V ------ $  a a -- . -!No - -  "- %q    --- $    ------ $  X X -- . -!No - -  "-$ gg  g---- . -!Gasoline loading racks: !provision does not apply - -  "-%*}* --- $I *  I ------ $jj-- . -!Yes- -  "-%c  --- $    ------ $  ] ] -- . -!No - -- . -0!T* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.^- - "-$j I I \  j  j I ---- . - ! ApplicabilityW !criteria are the !same for ! existing and ! new sources - *#  _   FIGURE25.DeterminationofApplicabilityforGasolineLoadingRacks   TABLE AC *#  _   FIGURE26.DeterminationofApplicabilityforMarineTankVesselLoading D:\EricF\MACT\graphics\Marine.wmfWPCXX77!7Xƚ7XR  0  7 -  "-$0  5050 "--% Arialig-"Systemn- . -!&Is it a land- or sea-based terminal or!*structure that loads liquid commodities inz!bulk onto marine tank vessels?@- -  "-$C  CC---- . -!(Is marine tank vessel loading associated!with an existing or new source?:- -  "-%z | d-- "- $ \| ] ] \-- Arials ---- $; f;   f-- . -!YesA - -  "-$55---- . -!Marine tank vessel!loading provisionz !does not apply- -  "- % a a`a--- $XBaXXB------ $| 3|   3-- . -!Nou - -  "-$5* *  5 5* --0 ArialE--% Arial- -( Arialt5- -- . -!Existing Source:B y-!#Is vapor pressure of liquid loaded  z- !> V- ! 10.3 kPa  - !and -!-emissions > 9.1 megagrams of any one HAP or >s |!%22.7 megagrams of total HAP per year? +- -  "- $ * *  * -- --- -- . - ! New Source: -!#Is vapor pressure of liquid loaded s w - !>s S- ! 10.3 kPa?s - -  "- %| | T @T T x - -- $#p  p #p ------ $&   & -- . - !Existingh - -  "- %| | T T T x - -- $ p p p ------ $] & ] & -- . -!Newh c - -  "- $5^5^5-- -- . -!Group 1 marine tank~!vessel loading*e- -  "- $   ^ ^ -- -- . -!Group 1 marine tankH !vessel loading*e - -  "- $O^O^O-- -- . -!Group 2 marine tank!vessel loading*e- -  "- $^^-- -- . -!Group 2 marine tankb!vessel loading*e- -  "- %* DDD(- -- $ ^  ------ $r>r>-- . -!YesX- -  "- %* D DD(- -- $0 ^ 0 ------ $r;r;-- . -!NoX- -  "- % * D D D (- -- $  ^  ------ $  r r -- . -!YesX - -  "- % * DDD(- -- $ ^  ------ $rr-- . -!NoX- -- . -0!T* See Chapter 4 for applicable requirements for Group 1 and Group 2 emission points.- *#  _   FIGURE27.DeterminationofApplicabilityforEquipmentLeaks   D:\EricF\MACT\graphics\Equipm~1.wmfWPCP/'#%H519+'13jA!A!%j%jA!+'13 ! /$?%2A`Arial? Isitaventfromawastewatersystem  " g#?%2A`Arial? drain,tankmixerorsamplevalveona  #5 "k?%2A`Arial? storagetank? +'13 $j'j'j+'13 %G ?%2A`Arial?Isitanemissionoforganichazardousair & ?%2A`Arial?pollutantsfromapump,compressor, ' ?%2A`Arial?pressurereliefdevice,samplingconnection (c A?%2A`Arial?system,open-endedvalveorline,valve, ) z?%2A`Arial?orinstrumentationsystem"inorganic *?%2A`Arial?hazardousairpollutantservice"(equipment + }?%2A`Arial?containingorcontactingfluid ,-_?%2A`Arial?> -d?%2A`Arial?5%by .X !x?%2A`Arial?weighttotalorganicHAP)?+'13 /+A!*1 `0g*'g1 `1+'13 2 Z?%2A`Arial?No+'13 3A!fA!f%%A!+'13 4$a?%2A`Arial?Equipment 5u/$]?%2A`Arial?leaks 6g#a?%2A`Arial?provision 7"`?%2A`Arial?doesnot 8r!]?%2A`Arial?apply+'13 9#z##1 `:##[##1 `;#=#=##+'13 <r#[?%2A`Arial?Yes+'13 =^z z g^g^z +'13 >O y?%2A`Arial?Equipmentleaksprovisionapplies+'13 ?**-331 `@r3gr1 `A UU +'13 B[?%2A`Arial?Yes+'13 Cs77 1 `D 7A!v  1 `E/l/l+'13 F<Z?%2A`Arial?No G?%2A`Arial?*SeeChapter4oftheupdatedPRGuidanceDocumentforGroup1andGroup2emissionpoints.@@ !  _eX3XXXXX3Vm    Vmw0 @ @   _#X3XX# G!XX3Petroleum_ԀRefineryMACT#X3X! G#XX3Vmw݌ p Ќ  Vm    Vm0 @ @   #X3Xq#=XX3DeterminingApplicabilityVm݌ d Ќ  Vm  Vm0 @ @   _#X3X=Z#XX3(Revisedtoincluderuleamendments,November2000)Vm݌   Ќ  Vm  Vm0 @ @   _Vm݌̌    8']Xdd8  #9#@#Xԟ X@P#R`Y Q XԟNotice#RQ R`Y#RYQR#X3XRY+#& %X3   r#X3X%& #XX3Thestatementsinthisdocumentareintendedsolelyasguidance.Thisdocumentisnotintended,norcan  4  itbereliedon,tocreateanyrightsenforceablebyanypartyinlitigationwiththeUnitedStates.EPAandStateofficialsmaydecidetofollowtheguidanceprovidedinthisdocument,ortoactatvariancewiththeguidance,basedonananalysisofspecificsitecircumstances.ThisguidancemayberevisedwithoutpublicnoticetoreflectchangesinEPAspolicy#s#@ 4  #@Q##X']X #XX']   @  @`  @  @  @h  @  @ #X3X# G!XX3Contents#X3X! G #XX3 d   Vm  Vm 0     I.0s#s#GENERALAPPLICABILITY###Js#.  $s#s##2Vm 8 ݌ h Ќ  Vm  Vm 0     II.0s#s#APPLICABILITYFORSPECIFICEMISSIONPOINTS###Js#.9s#s##2Vm  ݌  Ќ  !  ! 0  0` s#s#    A.0` ` s#` s#MiscellaneousProcessVents###Js#./` s#` s##4!  ݌ X Ќ  !  ! 0  0` s#s#    B.0` ` s#` s#StorageVessels###Js#.#` s#` s##4! ݌ h Ќ  !  ! 0  0` s#s#    C.0` ` s#` s#WastewaterStreams###Js#.tt&` s#` s##5! ݌ ( Ќ  !  !0  0` s#s#    D.0` ` s#` s#GasolineLoadingRacks###Js#.pp*` s#` s##6!݌  Ќ  !  !0  0` s#s#    E.0` ` s#` s#MarineTankVesselLoading###Js#..` s#` s##6!݌ X Ќ  !  !0  0` s#s#    F.0` ` s#` s#EquipmentLeaks###Js#.ll#` s#` s#####X']X #7!݌ h Ќ  X3XXX']2.1  ApplicabilityoftheRule##Js#.DD(8 @   2.20 ` HowDoesaFacilityDeterminetheEmissionPointstoWhich,` s#` s# 0  0` s#s#theControlRequirementsApply?###Js#.3` s#` s##9    2.30 ` WhatAretheControlRequirements?#""Is#.LL6` s#` s##11     2.40 ` WhenMustAFacilityComply?#""Is#.0` s#` s##11  ! 0   s#s# #X']XXX3#X3XXX']Figure210 ` EmissionPointswithinanAffectedSource###Js#.=` s#` s##8 x"# Figure220 ` DeterminationofApplicabilityforMiscellaneousProcessVents#""Is#.00R` s#` s##14 d#$ Figure230 ` DeterminationofApplicabilityforStorageVessels#""Is#.F` s#` s##13 P$% Figure240 ` DeterminationofApplicabilityforWastewaterStreams#""Is#.44I` s#` s##15 <% & Figure250 ` DeterminationofApplicabilityforGasolineLoadingRacks#""Is#.xxM` s#` s##16 (&x!' Figure260 ` DeterminationofApplicabilityforMarineTankVesselLoading#""Is#.Q` s#` s##17 'd"( Figure270 ` DeterminationofApplicabilityforEquipmentLeaks#""Is#.F` s#` s##18 (P#) #X']XXX3W# X']XXX'] X X']*ThisapplicabilityinformationwastakenfromtheUpdatedPetroleumRefineryMACTStandardGuidance )(%+ document,(EPA/305B97010),November,2000.# F#Ԁ#[# # X']X e#ԀForcommentsorquestionsconcerningthetechnical *%, contentofthisdocument,pleasecontactJimDurhamat9195415672orat(durham.jim@epa.gov).#X']XX X']#X3XXX'] x,'.  d-(/| Ї#X']XXX3ج#!  !!0  0` s#s#    !!<݌ ` s#` s# Ќ  *"ddd Xdd Xdd Xs#s#,dd ,dd +   L  XX']  I.0 l GENERALAPPLICABILITY   1'" ll  1 '"  '## ,X1.0 @ IstherefineryamajorHAPsource?=@@  \ 0 @ []0l@@Potentialtoemit10tonsperyear(tpy)ofanyofthe188HAPslistedin    112(b)oftheCleanAirAct;or ll 0 @ []0l@@Potentialtoemit25tpyoftotalHAPs.##  1"$" ll" 1# |#Yes[]No[  \ ]##  $ " $# [ #2.0 @ DotherefiningprocessunitsatrefineriesthataremajorHAPsourcesemitor  p  containanyofthefollowing28organicHAPs?Pleasecheckthesubstancesbelowthatapply. @@ *,4!X,*0 @ []0l@@Benzene 0 ll0H   0tH H 0tt[]0Ethyleneglycol p 0 @ []0l@@_Biphenyl_ 0 ll0H   0tH H 0tt[]0Hexane0 0 @ []0l@@Butadiene(1,3)0 ll H 0t  0tt[]0Methanol 0 @ []0l@@Carbondisulfide H 0tll0tt[]0Methylethylketone(2_butanone_)` 0 @ []0l@@Carbonylsulfide H 0tll0tt[]0Methyl_isobutyl_Ԁketone(_hexone_) p 0 @ []0l@@Cresol(mixedisomers)0tll  []0ttMethyl_tert_Ԁbutylether0 0 @ []0l@@Cresol(m) 0 ll0H   0tH H 0tt[]0Naphthalene 0 @ []0l@@Cresol(o) 0 ll0H   0tH H 0tt[]0Phenol` 0 @ []0l@@Cresol(p) 0 ll0H   0tH H 0tt[]0Toluene p 0 @ []0l@@_Cumene_ 0 ll0H   0tH H 0tt[]0_Trimethylpentane_Ԁ(2,2,4)0 0 @ []0l@@_Dibromoethane_Ԁ(1,2)0tll0tt[]0Xylene(mixedisomers)# # 0 @ 0l@@0ll(ethylene_dibromide_)  #Y+#0[]0Xylene(m)` 0 @ []0l@@_Dichloroethane_Ԁ(1,2)0tll0tt[]0Xylene(o) p  0 @ []0l@@_Diethanolamine_ H 0tll0tt0[]0Xylene(p)0! 0 @ []0l@@_Ethylbenzene_#.,#  "ll # .#Yes[]No[]#/#   ` & # u/#3.0 @ Areanyofthefollowingemissionpointslocatedwithinpetroleumrefining D' processunits?Pleasechecktheemissionpointsbelowthatapply. @@ 0 @ []0l@@Miscellaneousprocessventsthatcontain20_ppmv_ԀtotalorganicHAP4!*ll 0 @ []0l@@Storagevessels(pressurevesselsandvessels<_m3_areexempt)!D+ll 0 @ []0l@@Wastewaterstreamsandtreatmentoperations",ll 0 @ []0l@@Equipmentcontainingorcontactingafluidthatis5%byweighttotal t#- organicHAPs#/#  4$.ll # '3#Yes[]No[]#3#   t 1 # 3#4.0 @ Areanyofthefollowingemissionpointslocatedatarefinerythatisamajor % 2 source?Pleasechecktheemissionpointsbelowthatapply.0@@H&!3 0 @ []0l@@Marinevesselloadingoperations'#5ll 0 @ []0l@@GasolineloadingracksinSIC2911(#6ll 0 @ []0l@@Storagevesselsandequipmentleaksassociatedwithbulkgasoline H)$7 terminalsinSIC2911#84#  *X%8ll # 6#Yes[]No[]#7# @  'X";   # @n7#II.0 @ APPLICABILITYFORSPECIFICEMISSIONPOINTS #7# 7 4"'%\+&<@"@" 4#Z8#* ,,4!X*  A.0 @ MiscellaneousProcessVents 79 #8#d@@  1.0 @ Doestheventcontainagasstreamwith20_ppmv_ԀorganicHAP and isit  continuouslyorperiodicallydischargedduringnormaloperations?#9# 1"$"d@@" 1#:#Yes[]No[]#c;# $d " $#;#2.0 @ Istheventorgasstreamanyofthefollowing?Pleasecheckthedescriptions h   belowthatapply. @@ 0 @ []0l@@Directlydischargedtotheatmosphere  ll 0 @ []0l@@Routedtoacontroldevicepriortodischargetotheatmosphereh ll 0 @ []0l@@Divertedtoaproductrecoverypriortocontrolordischargetothe ( x atmosphere ll #$<#Note:Theabovelistgivesexamplesofventorgasstreamsandmaynotbeall h  inclusive#>#.#Q?#  ,|  #?#Yes[]No[]#?#   8 #D@#3.0 @ Doestheventorgasstreamcomefromanyofthefollowing?Pleasecheck   theitemsbelowthatapply. @@ 0 @ []0l@@Gasstreamsroutedtoafuelgassystemll 0 @ []0l@@Reliefvalvedischargesll 0 @ []0l@@Leaksfromequipmentregulatedunder40CFR63.648@ll 0 @ []0l@@Episodicor_nonroutine_ԀreleasessuchasmaintenanceorupsetsPll 0 @ []0l@@Insitusamplingsystems(onstreamanalyzers)ll 0 @ []0l@@Catalyticcrackingunitcatalystregenerationventsll 0 @ []0l@@CatalyticreformerregenerationventsD ll 0 @ []0l@@SulfurplantventsT!ll 0 @ []0l@@Ventsfromcontroldevices"ll 0 @ []0l@@Ventsfromanystrippingoperationsappliedtocomplywiththewastewater # provisionsof40CFR63SubpartCC,G,orFF ll 0 @ []0l@@Cokingunitventsassociatedwithcokedrum,_depressuring_Ԁatorbelowa T% cokedrumoutletpressureof15poundspersquareinchgauge,_deheading_,draining,ordecoking(cokecutting)orpressuretestingafterdecoking ll 0 @ []0l@@VentsfromstoragevesselsT)ll 0 @ []0l@@Emissionsfromwastewatercollectionandconveyancesystems*ll Note:Iftheanswertoquestion3is Yes,themiscellaneousprocessvents D!, provisiondoesnotapply.#@#  "X- #H#Yes[]No[]#NI#  P0 #I#4.0 @ Doestheventorgasstreamcomefromanyofthefollowing?Pleasecheck d theitemsbelowthatapply. @@ 0 @ []0l@@Causticwashaccumulators  0ll[]0StripperoverheadsT 0 @ []0l@@Distillationlowercondensers/0ll[]0Vacuum#J#Ԁaccumulators#L#d 0 @ 0l@@0ll#VL#accumulators#L#Ԁ#9M#$ #|M#0 @ []0l@@_Blowdown_Ԁcondenser/0tll0tt0[]0Delayed_coker_Ԁ#M#vents#N#0#BO#  0 @ 0l@@0llaccumulators#O#0H 0tH H 0tt#9P#000$#P#T $$ 0 @ []0l@@Flash/knockoutdrums0tll0tt0[]0Reactorvessels  #5Q# d  0 @ []0l@@Scrubberoverheads $ ll Note:Theabovelistgivesexamplesofwhereventorgasstreamsoriginateand T    maynotbeallinclusive.#?R#  h  #S#Yes[]No[]#S#   #4T#5.0 @ Istheventassociatedwithanexistingornewsource?l @@ 0 @ []0l@@Existingsource< ll 0 @ []0l@@Newsource ll #T# Existingsources 󀄀sourcesthatcommencedconstructiononorbeforeJuly14, ,| 1994.  @ Newsources 󀄀sourcesthatcommencedconstructionafterJuly14,1994.#U#Ԁ#V#A t processunitconstructedatanexistingsourceissubjecttonewsourcerequirementsifthenewunithasthepotentialtoemit10tonsperyear(tpy)ormoreofanyoneHAPor25tpyormoreoftotalHAPs.Otherwiseitissubjecttoexistingsourcestandards.Achangetoanexistingsourceoranadditionofanemissionpointissubjecttoexistingsourcestandards,unlessitisareconstructedsource,whichissubjecttonewsourcestandards#?W#.  H #VY#  l  #Y# Foranexistingsource:  L! 6.0 @ IstheorganicHAPconcentration20_ppmv_, and total_VOC_Ԁemissions33 $# kg/day?=@@ $ Note:Iftheanswertoquestion6is Yes,itisaGroup1miscellaneousprocess l& vent.Iftheansweris No,itisaGroup2miscellaneousprocessvent.#Z#  0' #+\#Yes[]No[]#\#  L, #\# Foranewsource:  4!- 7.0 @ IstheorganicHAPconcentration20_ppmv_, and total_VOC_Ԁemissions6.8 " / kg/day?=@@ #0 #4]#Note:Iftheanswertoquestion7is Yes,itisaGroup1miscellaneousprocess %T 2 vent.Iftheansweris No,itisaGroup2miscellaneousprocessvent.#^#  %!3 #_#Yes[]No[]#_# @  4$8 # @I`#  B.0 @ StorageVessels ` #`#'l"9@@ 1.0 @ Isitatankorothervesselusedtostoreorganicliquids?=@@##a#Ԉ  (#; #a#Yes[]No[]#Fb#  \)$? #b#2.0 @ Isitpermanentlyattachedtoamotorvehiclesuchasatruck,railcar,barge,or *&@ ship?=@@#b#Ԉ  p+&A #c#Yes[]No[]#$d#  0,'D #}d#3.0 @ Isitapressurevesseldesignedtooperateinexcessof204.9_kPa_Ԁandwithout d emissiontotheatmosphere?=@@#d#Ԉ  $ #e#Yes[]No[]#4f#   #f#4.0 @ Doesithaveacapacitylessthan40_m3_?#f# 8@@ #g#Yes[]No[ 8 ]#g#   #Oh#5.0 @ Isitusedasabottomsreceivertank?#h#  L @@ #i#Yes[]No[  L  ]#}i#     #i#6.0 @ Isitusedasawastewaterstoragetank?=@@#@j#Ԉ   `  #j#Yes[]No[  `  ]#*k#    #k#Note:Ifanyoftheanswerstoquestions2through6is Yes,thestoragevesselsprovisiondoesnot $t  apply.#k#  8  #l#7.0 @ Istankassociatedwithanexistingornewsource?< @@ 0 @ []0l@@Existingsource ll 0 @ []0l@@Newsource| ll #m##]n# Existingsources 󀄀sourcesthatcommencedconstructiononorbeforeJuly14, L 1994;   Newsources 󀄀sourcesthatcommencedconstructionafterJuly14,1994.#n#Ԁ#o#A D processunitconstructedatanexistingsourceissubjecttonewsourcerequirementsifthenewunithasthepotentialtoemit10tonsperyear(tpy)ormoreofanyoneHAPor25tpyormoreoftotalHAPs.Otherwiseitissubjecttoexistingsourcestandards.Achangetoanexistingsourceoranadditionofanemissionpointissubjecttoexistingsourcestandards,unlessitisareconstructedsource,whichissubjecttonewsourcestandards.# p#   #$r##X3X#XX3  <  #{r#Foran existingsource : l! 8.0 @ Isthecapacity177_m3_ and vaporpressure10.4_kPa_Ԁ(maximum)and # 8.3_kPa_Ԁ(annualaverage) and liquidHAPcontent>4%byweight(annual l$ average)? @@ =Note:Iftheanswertoquestion8is Yes,itisaGroup1storagevessel.Ifthe  ' answeris No,itisaGroup2storagevessel.#s#  x!( #u#Yes[]No[]#u#  ,. #Yv#Fora newsource : "/ 9.0 @ 0l@@Isthecapacity151_m3_ and vaporpressure3.4_kPa_Ԁ(maximum) and  T$1 liquidHAPcontent>2%byweight(annualaverage)?=ll %l 2 0 @ 0l@@OR &!4ll 10.0 @ Isthecapacitybetween76and151m3 and vaporpressure77_kPa_ $(t#6 (maximum) and liquidHAP>2%byweight(annualaverage)?=@@ (<$7 Note:Iftheanswertoquestion9or10is Yes,itisaGroup1storagevessel.If t*%9 bothanswersare No,itisaGroup2storagevessel.#v# @  8+&: Yes[]No[]# @Sz#  %\ > #z#Yes[]No[ ($C ]#{# @ " )$D # @{#  C.0 @ WastewaterStreams | #{#d@@  1.0 @ Isitwaterorwastewaterthat,duringproductionorprocessing:@@ 0 @ Comesintodirectcontactwithorresultsfromtheproductionoruseofanyraw l material,intermediateproduct,finishedproduct,byproduct,orwasteproduct? @@ =0 @ Isdischargedintoanyindividualdrainsystem?#t|# 1"$"\ @@" 1#~~#Yes[]No[]#~#   #N#Yes[]No[  d ]## $ $" $##2.0 @ Doesrefineryhaveatotalannualbenzeneloading10_megagrams_Ԁperyear, ( x  and aflowrate0.02litersperminute, and benzeneconcentration10_ppm_  8  byweight, and subjecttocontrolrequirementsunder40CFR61SubpartFF? @@ =Note:Wastewaterstreamsapplicabilitycriteriaarethesameforexistingandnew 8  sources.Iftheanswertoquestion2is Yes,itisaGroup1wastewaterstream.Iftheansweris No,itisaGroup2wastewaterstream.#x#    #f#Yes[]No[]## " h  ##  D.0 @ GasolineLoadingRacks #q# `@@ 1.0 @ Isitanyofthefollowingequipment,whichisnecessarytofillgasolinecargo   tanks?Pleasechecktheequipmentbelowthatapplies. @@ 0 @ []0l@@Loadingarms0 ll H []0t  Shutoffvalves(#tt 0 @ []0l@@Pumps0 ll0    []0H  Reliefvalves$H H  0 @ []0l@@Meters0 ll0    []0H  Otherpipingandvalves## 1"$"X%H H " 1##Yes[]No[]#Y# `*  $ +" $##2.0 @ IsitagasolineloadingrackclassifiedunderSIC2911?#/# ,@@ ##Yes[]No[ - ]##  l. ##3.0 @ Doesithaveagasolinethroughput>75,700liters(20,000gallons)perday?#ۊ#/@@ #w#Note:Gasolineloadingracksapplicabilitycriteriaarethesameforexistingand @1 newsources.Iftheanswertoquestion3is Yes,itisaGroup1gasolineloadingrack.Iftheansweris No,itisaGroup2gasolineloadingrack.#܋#  3 #-#Yes[]No[ 4 ]## @  5 # @#  E.0 @ MarineTankVesselLoading #G# h6@@  i1.0 @ Isitalandorseabasedterminalorstructurethatloadsliquidcommoditiesin !8 bulkontomarinetankvesselloading?=@@#Ď#Ԉ  `"9 ##Yes[]No[]#B#  #h> ##2.0 @ Isvesselloadingassociatedwithanexistingornewsource?d@@ 0 @ []0l@@Existingsourcell 0 @ []0l@@NewsourceTll  Existingsources 󀄀sourcesthatcommencedconstructiononorbeforeJuly14, $ 1994;##    Newsources 󀄀sourcesthatcommencedconstructionafterJuly14,1994.#Ē#A  h  processunitconstructedatanexistingsourceissubjecttonewsourcerequirementsifthenewunithasthepotentialtoemit10tonsperyear(tpy)or moreofanyoneHAPor25tpyormoreoftotalHAPs.Otherwiseitissubjecttoexistingsourcestandards.Achangetoanexistingsourceoranadditionofanemissionpointissubjecttoexistingsourcestandards,unlessitisareconstructedsource,whichissubjecttonewsourcestandards.#v#      d ##Foran existingsource : @  3.0 @ Isvaporpressureofliquidloaded10.3_kPa_Ԁ and emissions>9.1 x  _megagrams_ԀofanyoneHAPor>22.7_megagrams_ԀoftotalHAPsperyear?=@@ @ Note:Iftheanswertoquestion3is Yes,itisaGroup1marinetankvessel  loading.Iftheansweris No,itisaGroup2marinetankvesselloading.##   #}#Yes[]No[]#Ԙ#  @ #/#Fora newsource : ( 4.0 @ Isvaporpressureofliquidloaded10.3_kPa_?`@@ Note:Iftheanswertoquestion4is Yes,itisaGroup1marinetankvessel 0! loading.Iftheansweris No,itisaGroup2marinetankvesselloading.##  " #6#Yes[]No[]## " h& ##  F.0 @ EquipmentLeaks #F#H'@@  h1.0 @ Isitaventfromawastewatersystemdrain,tankmixer,orsamplevalveona ) storagetank? @@ =Note:Iftheanswertoquestion1is Yes,theequipmentleaksprovisiondoesnot , apply.## '" -" '#M#Yes[]No[]## 0""H2  " 0##2.0 @ IsitanemissionoforganicHAPsfromanyofthefollowingwhichis/are in d organichazardousairpollutantservice(equipmentcontainingorcontacting $ fluid5%byweighttotalorganicHAP)##:@@ 0 @ 0l@@pump?0 ll0  #ՠ#d   0 @ 0l@@compressor?0 ll0H   ##$H H  0 @ 0l@@pressurereliefdevice?0ll0#?#  0 @ 0l@@samplingconnectionsystem?0ll0##T  0 @ 0l@@openendedvalveorline?0ll0#ȣ# d  0 @ 0l@@valve? 0 ll0   ## $    0 @ 0l@@instrumentationsystem?0ll0#C#   0 @  @@ ##Note:Equipmentleaksapplicabilitycriteriaarethesameforexistingandnew d   sources.## (  #F#Notetoinspector:Theapplicabilitysectionsofthischecklist(i.e.,General X  ApplicabilityandApplicabilityforSpecificEmissionPoints)determineswhetherthePetroleumRefineryMACTStandardappliestoaparticularrefinery,andwhetheritappliestoaparticularemissionpoint.Unlessotherwisenoted,refineriesarerequiredtocontrolemissionsfromallGroup1emissionpointstowhichtheMACTstandardapplies.Group2emissionpointsaresubjectonlytorecordkeepingrequirementsunlessotherwisenotedintheinspectionguide.## +"","" +##Yes[]No[]## $ ##Yes[]No[   ]Yes[]No[]#:#  $  Yes[]No[]## T " Yes[]No[]#*# $ $ Yes[]No[]## T & Yes[]No[]## @ $ ( # @q#(T* ! "" ( #ɭ#@#Xԟ X@r#R`Y Q Xԟ2.10  04s#s#ApplicabilityoftheRule#Xԟ X R`Y##X']X Xԟ?#X3XX'] L04s#4s# rEdJ:6r|Y p'"@E ] Y  @ Theaffectedsourceisthecombinationofalltheemissionpointslocatedatarefinery,andeachpointisconsideredpartofthesingleaffectedsource.TheMACTstandardalsoappliesonlytomajorsourcesasdefinedbySection112(a)oftheCleanAirActwith s#s#                             8,'C  thepotentialtoemithazardousairpollutants.Forclarificationonwhetherasourceisamajorsource,seeAppendixE.Figure21givesanexampleofeachoftheemissionpointswithinanaffectedsource.#X']XXX3"#Xԟ XXX']ԀTABLE21presentstheemissionpointstowhichthePetroleumRefineryMACT  standardapplies.IfanyofthepointsinTABLE2-1isnotlocatedattherefinery,theMACTstandarddoesnotapply.  TABLE21.ApplicabilityofthePetroleumRefineryMACTStandard  8 5*x",d"ddd dd "s#s#x,<dd ,<dd +  *$ ` *@ XXԟTheRuleAppliesTo A$,!t"$ ATheRulesDoesNotApplyTo#Xԟ X@#R`Y Q XXԟ -#!t"$ -#Xԟ X QR`YR#@ XXԟ3 ,r,4!X,3 C  C10  "0r  RefineriesthataremajorHAPsourcesundereitherofthefollowing d definitions:C1L݌ rr Ќ  0  0rPotentialtoemit10tonsperyear(tpy)ofanyofthe188HAPsin D AppendixAofthismanual; orrr  0  0rPotentialtoemit25tpyoftotalHAPs*rr C  CZ0  "0r  Refiningprocessunitsatrefineriesthataremajorsourcesandemitor  J  containanyofthe28HAPsinAppendixBofthismanualCZu݌ rr Ќ  C  C0  "0r  Thefollowingemissionpointswithinpetroleumrefiningprocessunits  *  atmajorsources:C݌ rr Ќ  0  0rMiscellaneousprocessventsthatcontain20_ppmv_Ԁtotalorganic   HAP rr 0  0rStoragevessels(pressurevesselsandvessels<40_m3_areexempt) rr 0  0rWastewaterstreamsandtreatmentoperations*z rr 0  0rEquipmentcontainingorcontactingafluidis5%byweighttotal J  organicHAPs. rr C  C0  "0r  Thefollowingemissionpointsiflocatedatrefineriesthataremajor *z sources:C ݌ rr Ќ   0  0rMarinevesselloadingoperations Zrr 0  0rGasolineloadingracksinSIC2911*zrr 0  0rStoragevesselsandequipmentleaksassociatedwithbulkgasoline J terminalsinSIC2911.#Xԟ X@˷#R`Y Q XXԟ  Z rr 7 , ,r,4!X7-PX,p0X,- #Xԟ X QR`Yk#@ XXԟ C  C}0  "0""  RefineriesthatarenotmajorHAPsourcesC}݌d!"" Ќ  C  CG0  "0""  EquipmentthatdoesnotemitorcontainanyoftheHAPsin 4# AppendixBofthismanualCGb݌ "" Ќ  C  CH0  "0""  CatalyticcrackingandreformingcatalystregenerationventsCHc݌d&"" Ќ  C  C%0  "0""  SulfurrecoveryplantventsC%@݌4 ("" Ќ  C  C0  "0""  ResearchanddevelopmentfacilitiesC݌T *"" Ќ  C  C0  "0""  UnitsprocessingnaturalgasC݌t ,"" Ќ  C  Cb0  "0""  UnitsforrecyclingdiscardedoilCb}݌ ."" Ќ  C  C$0  "0""  ShaleoilextractionunitsC$?݌  0"" Ќ  C  C0  "0""  EthyleneprocessesC݌$ 2"" Ќ  C  C0  "0""  UnitssubjecttothehazardousorganicNESHAP(HON)[40CFR D 4 63SubpartsF,G,H,andI]C݌ "" Ќ  C  C0  "0""  StormwaterfromsegregatedstormwatersewersC݌$ 7"" Ќ  C  Ce0  "0""  SpillsCe݌D9"" Ќ  C  C 0  "0""  EquipmentinorganicHAPservice<300hoursduringthe d; calendaryear.#Xԟ X@J#R`Y Q XXԟC '݌#$<""  #Ќ  i1 ,PX,p0X1 #RQ R`Y:#R`Y QR#Xԟ X R`Y#R`Y Q Xԟ2.20  HowDoesAFacilityDeterminetheEmissionPointstoWhichthe B= ControlRequirementsApply?#Xԟ X R`Y#R`Y Q Xԟ >s#s# #RQ QR`Y#RYQQR#X3XQRY#Theintroductiontothischapterpresentedhowafacilitydeterminesifitisclassifiedas 2@ anexistingornewsource.Oncethisdeterminationhasbeenmade,afacilitymust nA assesswhetheritmeetsthecriteriaforrequiringcontrolsonitsemissionpoints.TABLE22presentsthecontrolapplicabilitycriteriaforeachtypeofemissionpoint.EmissionpointsthatmeetthesecriteriaarecalledGroup1emissionpoints,whileallotheremissionpointsarecalledGroup2emissionpoints.Group1emissionpointsaresubjecttoallapplicablerequirementsoftheMACTstandard. Group2emissionpoints # F arenotsubjecttothecontrolormonitoringrequirementsoftheMACTstandard . $G However,Group2emissionpointsaresubjecttocertainrecordkeepingrequirements.  TABLE22.ControlApplicabilityCriteriaforEmissionPointsRYQXX3  R)$L *x@"Xdd<dd <<dd <",s#s#x,dd , dd , dd +  /"">'  / #X3XQRY #XX3#)#Emission d points A">',!,""">' AForExistingSources,ControlsMustBeUsedIf: A">"',!,"">' AForNewSources,ControlsMustBe d UsedIf: 7"(&,"  ">"' 7MiscellaneousProcessVents $H" $(1)0 ; OrganicHAPconcentration20 8  _ppmv_, and H ; ;  (2)0 ; Total_VOC_Ԁemissions33kg/day. ("  ; ;  ((1)0  OrganicHAPconcentration20 8  _ppmv_, and H"" (2)0  Total_VOC_Ԁemissions6.8kg/day. 3"$" """ 3StorageVessels $ " $(1)0 ; Capacity177_m3_, and  $; ;  (2)0 ; Vaporpressure10.4_kPa_ \  (maximum)and8.3_kPa_Ԁ(annual  l average), and , ; ;   (3)0 ; OrganicliquidHAPconcentration> l  4%byweight(annualaverage). (",| ; ;  ((1)0  Capacity151_m3_, and $""  (2)0  Vaporpressure3.4_kPa_ d  (maximum), and$ t""  (3)0  OrganicliquidHAPconcentration>   2%byweight(annualaverage). t !""   OR  L # Y(1)0  Capacity76and<151_m3_, and  %"" (2)0  Vaporpressure77_kPa_Ԁ(maximum),  \'  and(""  (3)0  OrganicliquidHAPconcentration> \* 2%byweight(annualaverage). 3"$"l+""" 3WastewaterStreams $0-" $(1)0 ; Totalannualbenzeneloading10 p. _megagrams_Ԁperyear, and 0/; ;  (2)Flowrate.02litersperminute, 1  and  x2 (3)0 ; Benzeneconcentration10_ppm_Ԁby P4 weight, and 5; ;  (4)0 ; Notexemptfromcontrolsunder40 H7 CFR61SubpartFF. (" X8; ;  ((1)0  Totalannualbenzeneloading10 p9 _megagrams_Ԁperyear, and 0:"" (2)0  Flowrate.02litersperminute, and <"" (3)0  Benzeneconcentration10_ppm_Ԁby @> weight, and P?"" (4)0  Notexemptfromcontrolsunder40 A CFR61SubpartFF. 3"$"HB""" 3GasolineLoadingRacks $",E" $PartofbulkgasolineterminallocatedatfacilitiesdesignatedunderSIC2911withgasolinethroughput>75,700litersperday. " #I Partofbulkgasolineterminal##Ԁlocatedat \!J facilitiesdesignatedunderSIC2911##Ԁwith "lK gasolinethroughput>75,700litersperday.#L# +""#M" +MarineTankVesselLoading +"p&!P"" +(1)0 ; Vaporpressureofliquidloaded $@ Q 10.3_kPa_, and %!R; ;  (2)0 ; Emission>9.1_megagrams_Ԁofany 8'"T HAPor>22.7_megagrams_ԀoftotalHAPperyearafterAugust18,1999. 7""$"($V; ; " 7(1)0  Vaporpressureofliquidloaded $@ W 10.3_kPa_ "" (2)0  Noparallelemissionratecutoffsfor 0'"Z newsources. 5""$"'@#["""" 5EquipmentLeaks +"*&]"" +Equipmentcontainingorcontactingfluidthatis5%byweighttotalorganicHAPs. -""*&_" -Equipmentcontainingorcontactingfluidthatis5%byweighttotalorganicHAPs.#X3X#RYQXX3(*&a  "" ( + 'a Ї#X3XQRY<#IncludedattheendofthischapterinFigure22through26aredecisionflowcharts  whichshowhowafacilitycandeterminefirstifitissubjecttotheMACTstandard,andsecondifGroup1orGroup2requirementsapply.DecisionflowchartshavebeenincludedforeachemissionpointthatispotentiallysubjecttotheMACTstandard(i.e.,#X']XXX3#X3XXX'] t miscellaneousprocessvents,storagevessels,wastewaterstreams,gasolineloadingracks,marinetankvesselloading,andequipmentleaks#X']XXX3J#X3XXX']). L  RYQXX3 #RQRY*#R`Y QR#Xԟ X R`Y`#R`Y Q Xԟ2.30  WhatAretheControlRequirements?#Xԟ X R`Y#R`Y Q Xԟ #RQ QR`Y#RYQQR s#s# #X3XQRY^#TABLE23summarizesthecontrolrequirementsforemissionpointsmeetingthecriteria l  inTABLE22. PleasenotethatwhileTABLE23providesaninclusive(asof X  November)summaryofthecontrolrequirementsfortheseemissionspoints, L  specificrequirementscanbefoundinthereferencedsectionoftheCodeofFederalRegulations.  4  RYQXX3#RQQRY# R`Y QR#Xԟ X R`Y#R`Y Q Xԟ2.40  WhenMustAFacilityComply?#RQ R`Y#R`Y QR #Xԟ X QR`Y?#R`Y Q XXԟ ps#s# #RQ QR`Y#RYQQR#X3XQRY#TheMACTstandardspecifiesthedatesbywhicheachemissionpointatnewand   existingsourcesmustbeincompliancewiththecontrolrequirements.AllemissionpointsatnewsourcesmustbeincomplianceatstartuporbyAugust18,1995,whicheverislater.    Thereisaspecificcompliancedateforeachemissionpointatexistingsources.MiscellaneousprocessventsandgasolineloadingrackshaveacompliancedateofAugust18,1998.WastewaterstreamsalsohaveacompliancedateofAugust18,1998,andsourcesshouldbeincompliancewiththebenzenewasteoperationsNESHAPfoundin40CFR61SubpartFF.FixedroofstoragevesselsmustbeincompliancebyAugust18,1998aswell;however,thepreamblesuggestscompliancebyAugust18,1999ifthetankmustbereplaced.  ! #X']XXX3V#X3XXX']   TABLE23.ControlRequirementsforProcessUnits/EmissionPoints#X']XXX3#X3XXX']  RYQXX3 3*?"Adddd  dd dd @"Xs#s#,dd ,dd +  /"">' < /#X3XQRY#XX3Emissionpoints A">"',!P""">' AControlRequirements 7"(&P"  ">"' 7 MiscellaneousProcessVents -"l " -0  ReduceorganicHAPsby98%orto20_ppmv_Ԁusingincinerators,  boilers,processheaters,orotherdevices; or l "" ###7#0  Useaflare. 3"$"  """ 3StorageVessels -" I " -#}#C  CF0  "0""  ComplywithstoragevesselNESHAP[40CFR63SubpartG],  I  whichrequires:CF݌ "" Ќ  0  0""#a#Internalfloatingroofwithspecifiedseals; or  ; "" ##0  0""Externalfloatingroofwithspecifiedseals; or $t "" #5#0  0""Externalfloatingroofconvertedtointernalfloatingroofwith ]  specifiedseals; orm ""  ##0  0""Closedventsystemwith95%efficientcontroldevice. 5""$"] """ 5WastewaterStreams -"""" -####0  ComplywithbenzenewasteoperationsNESHAP[40CFR61  SubpartFF],whichrequires: "" 0  0""Reducingbenzenemassemissionsby99%usingsuppression  followedbyanothertreatmentprocess(e.g.,steamstrippingor_biotreatment_); and #s"" 0  0""Reducingemissionsfromventsfromstreamstrippers,other \ wastemanagement,ortreatmentunitsby95%withacontroldeviceorto20_ppmv_Ԁattheoutletofthecontroldevice. 6"'",!"""" 6GasolineLoadingRacks 0"0"" 0#/###0  ComplywithgasolinedistributionNESHAP[40CFR63SubpartR], 0# whichrequires: "" 0  0""Reducingemissionsoftotalorganiccompoundsto10milligrams "r& perliterofgasolineloaded; and 2'"" 0  0""Loadingonlyinvaportightcargotanksthathavebeentestedto k) assurevaportightness. 5"""$"+*""" 5MarineTankVesselLoading -"""!?,""" -###U#0  ComplywithmarinetankvesselloadingNESHAP[40CFR63 /!- SubpartY],whichrequires: "" 0  0""ReducingHAPby97%forexistingsources!#q0"" 0  0""ReducingHAPby98%fornewsources. 5""$"S$2""""" 5EquipmentLeaks -""% 3"" -####0  Complywithequipmentleakrules[40CFR63SubpartHor40CFR % 4 60Subpart_VV_]forexistingsourcesand[40CFR63SubpartH]fornewsources,whichrequire: "" 0  0""Leakdetectionandrepairwithspecifiedleakdefinitionsand Y(#8 monitoringfrequencies "" ##@0  0""Equipmentspecificationsforsometypesofequipment.#Xԟ X@(#R`Y Q XXԟ2(&K*%;""  "" 2   ;+&; z1D40p|0 *p%H/ "E|(g%< efY)z s#s#                                                              +p&  z1D 40p|0GP&pP&/ "EG,)%e)z s#s#                                                              +p&  z1_BD 40p|0 *p#,"E|(%efY)z s#s#                                                              +p&  z1D 40p|0  *p& "E\(%evY(z s#s#                                                              +p&  z1D 40p|0  *p%n* "E#"eYE$z   z1D 40p|0  *p0' "E|(%&efY)z s#s#                                                              +p&  #RQ QR`Y #RYQQR#X3XQRY? #FloatingroofstoragevesselshaveacompliancedateofAugust18,2005,orthenext  scheduledmaintenanceanddegassingafterAugust18,1998,whicheverisfirst.MarinetankvesselloadingmustbeincompliancebyAugust18,1999,unlessusedinemissionsaveraging.Ifusedtogeneratecreditinanemissionsaverage,itmustcomplybyAugust18,1998,unlessacasebycase1yearextensionisgranted.AcompliancedateofAugust18,1998issetforequipmentleaks.Sourceshavetheoptionofcomplyingwith40CFR60Subpart_VV_Ԁor40CFR63SubpartH,whichallowsfor3phasesofemissionsreductions.(SeeChapter4formoredetailedinformationoncompliancedatesforequipmentleaks.)#X']XXX3p%#X3XXX']XX3#(# *ThisaboveapplicabilityinformationwastakenfromtheUpdatedPetroleumRefineryMACTStandardGuidance @  document,(EPA/305B97010),November,2000.# +)#Ԁ#'*# # X']X (#ԀForcommentsorquestionsconcerningthetechnical X  contentofthisdocument,pleasecontactJimDurhamat9195415672orat(durham.jim@epa.gov).#X']XX X']j*#XX']