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# OAR Box 1672 Prepped by Charmelle Mathews



### Document

Number: 

# ll-C-7 Docket Number: 

# A-98-1 3

Printed 9/30/2008 11:01:00 AM Sheet 36 of 132P. 2 

### A-W-/ 3

' * * %UNITE D STATE S ENVIRONMENTA LPROTECTIO N AGENC Y I KMK ^ u j Offic e ofAi rQualit yPlannin g an d Standard s \ -V^l ^ " Researc h Triangl e Park , Nort h Carolin a 2771 1 

## DE C 1-0199 7 %

—S

Mr . T . Te d Cromwel l Sr . Director , Ai r Program s Regulator yAffair s Chemica l Manufacturer s Associatio n 130 0 Wilso n Boulevar d Arlington , Virgini a 2220 9 Dea r Mr . Cromwell : Enclose d wit hthi s lette r i s th e U.S . Environmenta l Protectio n Agency' s draf t industrysurve yfo r th e organi c liquid s distributio n (non-gasoline ) sourc e category . Th e EP Ai s providin g thi s draf t fo r you r revie wan d comments . Th e surve yi s base d o n th e surve ydevelope d fo r th e Refiner yNESHA P whic hwa s extracte d fromOM B for m No . 2060-023 9 an

d formatte d t o mak e i t mor e relevan t t o tha t industry . I n you r review , w e ar e looking fo r technica l correction s an d addition s t o th e survey , an d als o fo r alternat e format s an d way s o f requesting informatio n tha t wil l simplif yth e survey , mak e i t mor e understandabl e and beneficial , an

d minimiz e th e burde n o n facilitie s tha t ar e responding . W e als o woul d appreciat e you r assistanc e i n identifyin g appropriat e surve yrecipients . Currentl yw e hav e tw o source s o f informatio n fo r facilit yowners . The yar e th e 199 7 Director yo f th e Independen t Liqui d Terminal s Associatio n (ILTA ) and th e 199 7 Petroleu

mTermina l Encyclopedi a (Oi l Pric e Informatio n Service) . W e als o hav e no t determine d ho wt o locat e an d surve ysmalle r facilitie s tha t blend and/o r packag e organi c liquid s i n container s suc ha s drums , gallo n an d quar t containers , etc . T o some degre e (se e Tabl e 3 i n th e survey) , w e hav e addresse d thes e operation s whe n the yar e collocate d a t terminals . However , w e nee d ai d i n requestin g th e prope r informatio n fromthes e packagin g operation s o n th e enclose d surve yand you r thought s o n a second surve ytargete d a t th e facilitie s no t collocate d wit h terminals . W e pla n t o send thi s surve you t i n Januar y1998 , an d wil l b e continuin g t o develo p the compan ymailin g lis t unti l tha t time . Du e t o ou r projec t schedule , w e nee d t o receiv e an ycomment s from



### AP. 3



### yo u byJanuar y7 , 1998 . I f yo u hav e an yquestion s o r woul d lik e a meetin g t o discus s thi s material , pleas e cal l m e a t (919 ) 541

- 5397 , o r Gre g LaFlamo f Pacifi c Environmenta l Service s a t (919 ) 941-0333 . You r hel p i n makin g thi s surve yaccurat e an d efficien t i n gatherin g neede d informatio n i s appreciated . Sincerely , Stephe n A . Shedd Wast e and Chemica l Processe s Group Emission s Standard s Divisio n 1 Enclosur e cc : Stev e Shedd (EPA/OAQPS/ESD/WCPG ) (w/ o enclosure ) Gre g LaFlam

(PES )P. 4



### Enclosur e 1 (Draf t cove r lette r an d EP Ainformatio n reques t fo r Organi c Liquid s Distributio n NESHAP - 12/8/9 7 revision ) [Field s belo wt o b e fille d i n frommailin g list ]

Dea r Mr./Ms . &&&&%-. Th e U.S . Environmenta l Protectio n Agenc y(EPA ) i s compilin g detaile d informatio n o n source s an d quantitie s o f hazardou s ai r pollutan t (HAP ) emission s an d contro l techniques . Thi s informatio n wil l b e use d i n setting nationa l emissio n standard s fo r hazardou s ai r pollutant s (NESHAP ) unde r Sectio n 11 2 o f th e Clea n Ai r Ac t (CAA) , a s amende d i n 1990 . Th e standard s wil l appl yt o non-gasolin e handling operation s a t bot hexistin g an d ne worgani c liquid s distributio n facilities . Thes e standard s ar e schedule d t o b e promulgate d b yNovembe r 2000 . Th e EPA' s initia l ste p fo r thi s endeavo r i s t o collec t informatio n o n HA P emission s and emissio n reductio n technique s i n th e organi c liquid s distributio n industry . You r assistanc e i n providin g informatio n i s critica l i n developin g a regulatio n tha t i s realisti c and workable , a s wel l a s protectiv e o f th e environment . Enclosur e 1 itemize s the informatio n tha t yo u ar e requeste d t o submit . Th e EP Awil l us e the informatio n t o quantif yHA P emissions ; defin e th e curren t statu s o f emissio n control ; and asses s th e environmental , energy , an d economi c impact s o f installing and operatin g feasibl e emissio n contro l techniques . Th e informatio n neede d fo r regulatorydevelopmen t i s containe d i n th e informatio n collectio n for mapprove d b yth e Offic e o f Managemen t and Budge t (OM B No . 2060-0239 ) . W e ar e sensitiv e t o th e amoun t o f labo r require d t o respond t o thi s request ; therefore , t o minimiz e demand s o n you r time , informatio n specifi c t o th e organi c liquid s distributio n industr yha s bee n extracte d fro mOMB for

mNo.,2060-023 9 an d formatte d t o mak e i t mor e relevan t t o thi s industry . Enclosur e 1 i s th e reformatte d versio n o f th e OM B approve d form . Th e OM B approve d for m i s availabl e upo n request .P. 5



### Th e authorit yfo r th e EPA' s informatio n gatherin g i s include d i n Sectio n 11 4 o f th e CA A(4 2 U.S.C . 7414 ) . Enclosur e 2 contain s a summaryo f thi s authority . Yo u shoul d als o b e awar e tha t anyfailur e t o compl ywit hou r reques t i s a violatio n o f Sectio n 11 4 an

d a s suc hi s subjec t t o enforcemen t unde r Sectio n 11 3 (specifically , 11 3 (d ) (1 ) (B ) o f th e CAA , whic hprovide s civi l penaltie s o f u

p t o $25,00 0 pe r dayo f violation) . I f yo u believ e tha t disclosur e o f anyspecifi c informatio n tha t yo u submi t woul d revea l a trad e secret , clearl yidentif ysuc hinformatio n a s discusse d i n th e enclosure . Anyinformatio n subsequentl y determine d t o constitut e a trad e secre t wil l b e protecte d unde r 1 8 U.S.C . 1905 . I f n o clai mo f confidentialit yaccompanie s th e informatio n whe n i t i s receive d b yth e EPA , i t ma yb e mad e availabl e t o th e publi c byth e EPAwithou t furthe r notic e (4 0 CF R Par t 2.203 , Septembe r 1 , 1976) . Sectio n 11 4 o f th e CA A exempt s emissio n dat a fromclaim s o f confidentialit yand emissio n dat a collecte d ma yb e mad e availabl e t o th e public . A clarificatio n o f wha t th e EP Aconsider s t o b e emissio n dat a i s containe d i n Enclosur e 3 . A s note d i n Enclosur e 4 , w e hav e designate d Pacifi c Environmenta l Services , Inc . (PES ) a s a n authorize d representativ e o f th e EPA . Therefore , PE S ha s th e right s discusse d abov e and i n Enclosur e 2 . A s a n authorize d representativ e o f th e EPA , PE S i s subjec t t o th e provision s o f 4 2 U.S.C . 741 4 respectin g confidentialit yo f method s o r processe s entitle d t o protectio n a s trad e secrets . Th e PE S contrac t wit h th e EP Ai s No . 68D60013 . Enclosur e 5 summarize s th e EPA' s policie s an d procedure s fo r handlin g privilege d informatio n an d describe s EP Acontracto r commitment s an

d procedure s fo r using confidentia l materials . I t i s th e EPA' s polic ytha t complianc e b ya n authorize d representativ e wit hth e requirement s detaile d i n Enclosur e 5 provide s sufficien t protectio n fo r the right s o f submitter s o f privilege d information .P. 6



### W e reques t tha t yo u retur n th e complete d informatio n reques t b y[date to b e inserted ] . I f yo u hav e an yquestion s regardin g thi s request , pleas e contac t Mr . Stephe n Shedd o f m ystaf f a t (919 ) 541-5397 . Sincerel yyours ,

Bruc e C . Jorda n Directo r Emissio n Standard s Divisio n

5 Enclosure s
cc : EP ARegiona l Offic e (w/ o enclosure s 2-5 ) Stat e Ai r Contac t (w/ o enclosure s 2-5 )P. 7



### MAXIMU M ACHIEVABL E CONTROL TECHNOLOG Y(MACT ) STANDARD S DEVELOPMENT INFORMATIO N REQUES T I . Instruction s Thi s informatio n reques t i s t o b e complete d fo r operation s tha t compris e th e organi c liquid s distribution(non gasoline ) sourc e categor ya t you r plant . Th e sourc e categor yi s thos e activitie s associate d wit hth e storag e and distributio n o f organi c liquid s othe r tha n gasoline , a t site s whic hserv e a s distributio n point s from whic horgani c liquid s ma yb e obtaine d fo r furthe r us e and processing . Thi s reques t cover s th e storag e and transfe r o f organi c liquid s (including equipmen t leaks) , and als o consider s wast e and wastewate r treatmen t and disposa l practices . W e ar e requestin g informatio n regardin g eac hcompound identifie d a s a hazardou s ai r pollutan t (HAP ) tha t i s use d i n o r emitte d b yan yoperations , includin g fugitiv e emissio n sources , tha t ar e par t o f th e organi c liquid s distributio n (non-gasoline ) sourc e categor ya t you r facility . Not e that , fo r thi s survey , w e woul d als o lik e informatio n o n anygasolin e storag e and distributio n activitie s a t eac hfacilit yi n orde r t o completel y characteriz e th e operation s an d t o understand th e tota l emission s pictur e a t th e facility . Fil l ou t thi s informatio n reques t a s completel ya s possibl e fromexistin g information . A t a minimum , provid e (1 ) informatio n o n th e presenc e o f HA P emission s an d (2 ) HAP emissio n estimate s base d o n previousl yobtaine d tes t dat a o r o n engineerin g calculations , provide d ther e i s a basi s fo r suc h calculations . Attachmen t Ainclude s th e EPA' s lis t o f hazardou s ai r pollutant s tha t yo u shoul d refe r t o whe n completin g th e survey . Al l dat a and response s shoul d b e base d o n calenda r yea r 199 7 emissions , material s handled , and emissio n contro l equipmen t (unles s yo u ca n justif yselectio n o f a n alternat e bas e year) . Pleas e b e sur e t o kee p a copyo f th e complete d surve yfo r you r records . Yo u shoul d als o kee p copie s o f anynote s o r calculation s yo u performi n completin g th e survey . I f yo u nee d mor e spac e t o complet e you r response , 

# 6P. 8



### pleas e includ e th e additiona l informatio n i n a clearl y labele d attachment . I f yo u believ e ther e i s additiona l informatio n tha t i s no t requeste d i n th e surve ytha t ma yb e helpfu l t o th e EP Ai n developin g HAP emissio n standard s fo r thi s industry , pleas e includ e thi s informatio n i n a separat e attachment . I f yo u hav e an

yquestion s regarding thi s request , pleas e contac t Mr . Stephe n Shedd , U.S . EPA , Emissio n Standard s Division , a t (919 ) 541-5397 . Retur n thi s informatio n reques t an d an yadditiona l informatio n to : Bruc e C . Jordan , Directo r

Emissio n Standard s Divisio n (MD-13 ) U . S . Environmenta l Protectio n Agenc y Offic e o f Ai r Qualit yPlanning an d Standard s Researc hTriangl e Park , N C 2771 1 Attention : Stephe n Shedd II . Genera l Informatio n A . Nam e o f lega l owne r o f plant : ;

B . Nam e o f lega l operato r o f plant , i f differen t fro m lega l owner : C . Addres s o f lega l owner/operato r (pleas e specif y which) : D . Siz e o f company :

Approximat e numbe r o f employee s o f th e busines s enterpris e tha t own s thi s plant , includin g wher e applicable , th e paren t compan yan d al l subsidiaries , branches , an d unrelate d establishment s owne d byth e paren t company(answe r mayb e give n usin g th e following ranges : 0-100 ;P. 9



### 101-250 ; 251-500 ; 501-750 ; 751-1,000 ; 1,001-1,500 ; an d >1,500) :

2 . Numbe r o f plan t employee s associate d wit hth e organi c liquid s distributio n (non-gasoline ) operation :

E . Nam e o f plant : F . Stree t addres s o f plant : Latitud e and longitud e coordinate s o f plant :

H . Nam e o f contact(s ) abl e t o answe r technica l question s abou t th e complete d survey : Nam e Nam e Titl e Titl e Telephon e Telephon e III . Plan t Operation s A . Provid e a n plo t pla n o f th e entir e facilit ywithi n th e fenceline . Thi s figur e shoul d clearl yindicat e al l storag e tank s and thei r identifie r codes , produc t loadin g o r transfe r areas , produc t flo wlines , an d wastewate r drain s and treatmen t areas . Us e th e sam e terminology/code s i n identifying facilit yequipmen t a s yo u wil l us e i n completin g Table s 1 through9 i n Sectio n IV . B . Provid e a brie f writte n descriptio n o f the facility' s operations . Lis t th e categorie s (gasoline , refine d petroleum , solvents , glycols , etc. ) o f organi c liqui d material s handle d during th e bas e year , an d th e approximat e volum e throughpu t o f eac htyp e o f material , Als o describ e al l activitie s tha t generat e HA P emissions , includin g th e storage , transfer , handling , 

# 8P.1 0



### and processin g (suc ha s blendin g o r packaging ) o f th e materials , a s wel l a s wastewate r and othe r wast e handling . Again , us e consisten t terminologyand code s betwee n th e plo t plan , th e writte n description , an d Table s 1 through9 i n Sectio n IV . IV . HAPs--Emission s and Control s A . Complet e Table s 1 through9 fo r th e HA P emissio n point s and contro l technique s tha t exis t a t th e facility . Sampl e entrie s ar e shown (in bol d print ) i n severa l o f th e tables . Wher e necessary , mak e sufficien t copie s o f blank table s t o provid e spac e fo r complet e responses . Guidanc e t o hel p yo u fil l ou t thes e table s i s provide d below : 1 . Tabl e 1--Ente r a cod e fo r eac horgani c liqui d stored , handled , o r loade d a t th e facility . Thi s include s bot hpur e liquid s (e.g. , benzene , methanol ) and an

yliqui d mixture s wit ha n organi c liqui d content , suc ha s wastewater . Code s ar e give n fo r severa l potentia l liquids . Wher e known , includ e th e requeste d liqui d propertie s and th e identit yan

d concentratio n o f HAP s presen t i n th e liquid . 2 . Tabl e 2 --Ente r a cod e fo r eac hstorag e tank wit h greate r tha n 10,000-gallo n («250-barrel ) capacity . Sho weac horgani c liqui d store d i n eac htank durin g the bas e year , usin g th e same liqui d code s a s use d fo r Tabl e 1 . Fo r eac hadd-o n contro l devic e use d t o contro l vapo r emission s fromstorag e tanks , fil l ou t Tabl e 8 fo r tha t typ e o f device . 3 . Tabl e 3--Ente r eac hloading rack/loadin g armtha t transfer s organi c liquid s t o tank trucks , railcars , barges , o r tanke r ships . W e ar e als o intereste d i n operation s tha t packag e thes e liquid s int o smalle r containers , suc ha s 55-gallo n drums , 1-gallo n o r 1

- quar t cans , etc . A s i n Tabl e 2 , fil l ou t Tabl e 8 fo r eac hcontro l devic e use d t o contro l vapo r emission s fromliqui d transfers .P.1 1



### 4 . Tabl e 4- -Lis t th e principa l source s o f wastewate r generation , usin g th e supplie d code s o r you r own description . Estimat e th e annua l flowrat e from eac hsource . Drain s ar e th e individua l entryway s

. t o conduit s tha t mov e wate r t o storag e o r treatment . 5 . Tabl e 5- -I n thi s tabl e w e wis ht o lear n ho w wastewate r i s collecte d and treate d a t you r facility(ies) . Fo r eac hwastewate r sourc e a s liste d i n Tabl e 4 , lis t th e numbe r o f collectio n unit s o r treatmen t approache s applicabl e t o eac h source . Th e las t fou r column s reques t informatio n o n whethe r and ho wai r emission s fromeac hare a ar e controlled . A s i n Table s 2 and 3 , fil l ou t Tabl e 8 fo r eac hcontro l devic e use d t o contro l vapo r emission s fromwastewater . 6 . Tabl e 6- -Non-aqueou s wast e (semi-soli d material , o r sludge ) ma ycontai n and emi t HA P during storage , handling , o r treatment . Identif yeac hindividua l typ e o f waste , and provid e informatio n o n ho wth e wast e i s collecte d and treated . A s i n Table s 2 , 3 , an d 5 , fil l ou t Tabl e 8 fo r eac hcontro l devic e use d t o contro l ai r emission s fro mnon-aqueou s waste . 7 . Tabl e 7--Identif yth e numbe r o f eac htyp e o f equipmen t componen t bytyp e o f servic e (selecting th e mos t prevalen t servic e fo r eac hcomponent) . LDA R program s involv e a forma l lea k surve yo f component s o n a fixe d schedul e (an d ma yinclud e a non-instrument , visua l program) . A s i n Table s 2 , 3 , 5 , and 6 , fil l ou t Tabl e 8 fo r eac hcontro l devic e use d t o contro l vapo r emission s fro m equipmen t components . 8 . Tabl e 8--Complet e th e applicabl e sectio n o f Tabl e 8 fo r eac hai r pollutio n contro l devic e i n us e a t th e facility . Fil l i n th e requeste d parameter s i f known , bu t eve n i f yo u d o no t kno wthe values , a t leas t identif yth e presenc e o f th e devic e by returnin g a tabl e showin g th e typ e o f devic e and th e emissio n source s tha t i t controls . B e specifi c



# 1 0P.1 2



### whe n listin g th e emissio n sources ; e.g. , Tank s 1 , 2 , 3 , an d 7 ; Loading Rack s 1- 5 and 11-15 ; al l Oil

Wate r Separators ; and s o forth .



# l lP.1 3



### TABL E 1 . ORGANI C LIQUID S HANDLE D AND HA P CONTENT(a )

Organic LiquidCode (b) : JT O Liqui dMolecula

r Weigh t (lb/lb-mole) : , 9 2 Vapo r Molecula r Weigh t ,9 2 (lb/lb-mole) : Averag e True Vapor

Pressur e of Liquid(psia) : , 0. 3 OR! Rei dVapor

Pressur e of Liquid(RVP) : . Averag e Liqui dDensit

y (Lb/Gal) : , 7. 3 Avg
. Temperatur

e of LiquidTransferred(°F) : , 6 0 Nameo f HAP s PresentinLiquid
. Avg . HA PConcentrationinLiquid (ppmwo rpercent ) 1,3-Butadien

e , Acrylonitrile . Benzene . Cumene , Ethylbenzen e . Ethylene dichloride . Ethylene glyco l , Ethylene oxide . Formaldehyd

e . Methanol , m-Xylene , o-Xylene . Phenol , p-Xylene , Styrene . 

# iP.1 4

8 TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HA P CONTENT(a ) (Continued ) Toluen ej 100 % Viny l chlorid e, 

### (tij

1 '

a ) Fo r an

yliqui d propert yo r HA P conten t tha t i s unknown , ente r tt UK" o n th e correspondin g blank . b ) Selec t th e organi c liqui d nam e tha t describe s th e materia l stored : A S = asphal t A V = aviatio n gasolin e B Z = benzen e C R = crud e oi l D I = diesel/distillat e fue l J F = je t fue l (JP-4 , etc. ) J K = je t kerosene/kerosen e L O = lub e oi l M G = moto r vehicl e gasolin e 

# 1 3P.1 5

9 TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HA P CONTENT(a ) (Concluded )

N A= naphth a O G = oxygenate s (MTBE , other ) R F = residua l fue l oi l 

### B U A C CU E B E D E G E O FO M E M X O X PH PX S T T O V A V C X X 

### 0 = = = = = = = = = = = = = = = = = = = 1, 3 -butadien e acrylonitril e cumen e ethy l benzen e ethylen e dichlorid e ethylen e glyco l ethylen e oxid e formaldehyd e methano l m-Xylen e o-Xylen e pheno l p-Xylen e styren e toluen e viny l acetat e viny l chlorid e slo p oil/transmix/wast e produc t other , pleas e specif y c ) Provid e th e name s o f an yadditiona l HAP s no t listed .



# 1 4

### 1 0 TABL E 2 . STORAG E TANK CONTRO L DAT A

Tan k I D Code (a) 1- A 1- A 1- B 1- B 1- C Tan

k Capacit y (Bbl) (b ) 20,00 0

u 24,00 0

w 12,500 Name o f

Store d Liqui d (c ) A G J F T X L Annua

l Throughput (Bbl/Yr ) 60,000 120,000 40,00 0 50,00 0 50,000 Roo f

Configuratio n (d ) CE F

M IF R
« FX R Floating

Roof Tanks Only : Sea l Typ e (e ) MS3

u LM 3

u

— Tan

k Roof Fitting s (f ) AHBG , GFWBG , VB G

u

M

U

— Add-o n

Contro l Devic e (g ) C

u

u

u

—P.1 7

1 1 TABL E 2 . STORAG E TAN K CONTRO L DAT A(Continued )

a ) Provid e a uniqu e identifie r cod e fo r eac htank (e.g. , A-l , B-1) . b ) Provid e th e maximu m capacit yfo r eac htank . c ) Us e th e sam e organi c liqui d code s a s i n footnot e b o f Tabl e 1 . d ) Selec t th e storag e tank roo f configuration : FXR = fixe d roo f IF R = interna l floating roo f EF R = externa l floatin g roo f CE F = externa l floating roo f converte d t o a n interna l floatin g

roof . e ) Fo r floatin g roo f tanks , ente r th e floating dec k sea l type : VM l = vapor-mounte d primarysea l onl y VM 2 = vapor-mounte d primarysea l wit hweathe r shiel d VM 3 = vapor-mounte d primarysea l wit hrim-mounte d secondaryseal . LM l = liquid-mounte d primar ysea l onl y LM 2 = liquid-mounte d primar ysea l wit hweathe r shiel d LM 3 = liquid-mounte d primar ysea l wit hrim-mounte d secondarysea l MS I = mechanica l sho e primarysea l onl y MS 2 = mechanica l sho e primarysea l wit hweathe r shiel d MS 3 = mechanica l sho e primar ysea l wit hrim-mounte d • secondar ysea l 0 = othe r (pleas e specif ytype) . f ) Fo r floatin g roo f tanks , selec t th e code s tha t bes t describ e th e type s o f roo f fitting s i n place : GPWUU= guid e pol e well , unslotted , ungaskete d sliding coverGPWUG =

guid e pol e well , unslotted , gaskete d sliding cove r GPSWSU N= guid e pole/sampl e well , slotted , ungaskete d sliding cover , withou t floa t GPSWSU F = guid e pole/sampl e well , slotted , ungaskete d slidin g

cover , wit hfloa t GPSWSG N= guid e pole/sampl e well , slotted , gaskete d slidin g cover , withou t floa t GPSWSG F = guid e pole/sampl e well , slotted , gaskete d sliding cover ,

wit hfloa t AHB G = acces s hatch , bolted , gaskete d AHUU= acces s hatch , unbolted , ungaskete d AHU G = acces s hatch , unbolted , gaskete d GFWUU= gauge-floa t well , unbolted , ungaskete d 

# 1 6P.1 8

1 2 TABL E 2 . STORAG E TAN K CONTRO L DAT A(Concluded )

GFWUG = gauge-floa t well , unbolted , gaskete d GFWB G = gauge-floa t well , bolted , gaskete d GHSWG = gauge-hatch/sampl e well , gaskete d GHSWU= gauge-hatch/sampl e well , ungaskete d VB G = vacuu mbreaker , gaskete d VB U= vacuu m breaker , ungaskete d g ) Selec t th e code(s ) tha t bes t describ e contro l systems , i f any , use d t o contro l vapor s emitte d fro man ypar t o f th e tank , includin g ri m seals , fittings , etc. : VCS 1 = vapo r collectio n systemventin g t o a vapor/liqui d absorptio n

uni t (scrubber ) VCS 2 = vapo r collectio n systemventin g t o a n incinerator/boile r VCS 3 = vapo r collectio n systemventin g t o a flar e VCS 4 = vapo r collectio n systemventin g t o a vapor/soli d adsorptio n

uni t VCS 5 = vapo r collectio n systemventin g t o a condense r B = groun d leve l burne r o r therma l oxidize r C = catalyti c oxidize r 0 = other , pleas e provid e a ful l descriptio n (us e extr a sheet ) N= none .



# 1 71 3 TABL E 3 . LIQUI D TRANSFE ROPERATION S

Rac kAr

m I D Cod e(a) I D Cod e(b ) Organi

cLiqui d Transferre d Throug h Ar m(c ) Typ

eo f Transpor t Vehicleo r Containe r Fille d (d) Annua

l Volumeo f Transferre d Liqui d (Gal/Yr ) Metho

d o f Loadin g(e ) Average

Loadin g Rat e (Gal/Min) Vapo r Contro l Device(f

) Contro

l Devic e Efficienc y (g ) 1 1 1 2

O C 1- 1

1- 2 1- 2 2- 1 B Z

T O M X MG T

T R 500,00 0

400,00 0 600,00 0 1,000,00 0 SU

B 50 0

50 0 50 0 20 0 VCS 1

VCS 2 95(EJ )

95(EJ ) 95(EJ ) 90(ST )

C OP.2 0

1 4 TABL E 3 . LIQUI D TRANSFE R OPERATION S (Concluded )

a ) Provid e a uniqu e identifie r cod e fo r eac hloadin g rac k o r othe r fillin g equipment . b ) Provid e a uniqu e identifie r cod e fo r eac hloadin g armi n a rac k o r equipmen t unit . c ) Us e th e same organi c liqui d code s a s i n footnot e b o f Tabl e 1 . d ) Selec t th e typ e o f transpor t vehicl e loade d o r containe r filled : T = tank truc k R = tank ca r (railroad ) B = barg e T = tanke r shi p S C = smal l containe r ( 1 gallo n o r less ; specif ysize ) M C = mediumcontaine r (> 1 gal. , <5 5 gal. ; specif ysize ) L C = larg e containe r (5 5 gal . dru mo r larger ; specif ysize) . e ) Selec t th e metho d o f loading material : SP L = splas h(top ) SUB = to p submerge d BTM = botto m

loading . f ) Us e th e same contro l devic e code s a s i n footnot e g o f Tabl e 2 . g ) Basi s fo r contro l devic e efficienc yestimate : S A= samplin g an d analysi s E J = engineerin g judgmen t S T = sourc e test .



## 1 9P.2 1



### 1 5 TABL E 4 . WASTEWATE R FLO W RATE S AN D DRAI NCONTROL S

Sourc eo f Wastewate r (a ) OrganicLiquid Content (b ) Total Flo w Rat e (Gal/Yr) Numbe ro f

Drains with Emissio n Suppressio n (c ) Numbe ro f

Drains without Emissio n Suppression (c )



### a )

b ) Selec t th e code s tha t bes t describ e th e point s o f wastewate r generation : T D S R L R L B 0 tank drain s (identif yth e specifi c tank s usin g th e same

tank code s a s i n footnot e a o f Tabl e 2 ) stormwate r runof f loading rack s (identif ythe specifi c rack s usin g th e same rac k code s a s i n footnot e a o f Tabl e 3 liqui d blending/packagin g operation s other , pleas e provid e ful l descriptio n (us e extr a sheet , i f necessary) . Lis t th e principa l organi c liquid s typicall ypresen t i n eac h wastewate r stream . c ) Emissio n suppressio n control s reduc e emission s fromdrai n pipe s and include , bu t ar e no t limite d to , wate r sea l pot s and p-traps . 

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### 1 6 TABL E 5 . WASTEWATE R COLLECTIO NAN D TREATMEN T CONTROL(a )



## r o Wastewate rTreatmentUni t Collectio nUnits : Manhole s JunctionBoxe s Sumps/Catc

h Basin s Lif tStation s Storag eTanks (f)

TreatmentApproaches : Oil/Wate rSeparators Ai rFlotationSystems Coagulation/

Precipitatio n Unit s Sand FiltrationUni t No . o f No . o f

No . o f

Unit s Uncovere d Covere d thatVen t Unit s tha tUnit s thatEmission s t o Tota l Numbe rVen tt o th eVen tto th eaContro l Control Devic e Sourc eo f

Wastewate ro f Unit s Atmospher eAtmospher eDevic e(e ) (b ) (c ) (d ) (d )

r o r o

### 1 7 TABL E 5 . WASTEWATE R COLLECTIO NAN D TREATMEN T CONTROL(a ) (Continued )



## r o Wastewate

rTreatmen

tUni t Equalizatio

nUnit s Treatmen tApproaches : Oxidatio nPond s Activated SludgeUnit

s Tricklin gFilter s Clarifier s Filte rPresse s Stripper s Stormwate

rRetentio n Effluent / Recycl ePon

d Rotatin gBiologica

l Contactor s Shi p Of f Sit e 

### ( 0 Tota l Numbe r Sourc eo f Wastewate

rof

Unit s (b ) (c ) No . o f Uncovered Unit s tha t Ven tt o the Atmospher

e (d ) No . o f

Covere d Unit s ma t Ven tt o th e Atmospher

e (d ) No . o f

Unit s tha tVent Emissions t o aContro l Devic e

. } Contro

l Devic e (e )

r o c oP.2 4

1 8 TABL E 5 . WASTEWATE R COLLECTIO NAN D TREATMEN T CONTRO L (a ) (Concluded )

a ) Includ e al l wastewate r collectio n an d treatmen t unit s and anycontro l device s controlling vapo r emission s fromsuc hunits . D o no t repor t informatio n o n drain s i n thi s table ; repor t drai n informatio n i n Tabl e 4 . b ) Ente r th e source s o f wastewate r i n th e same ro wa s th e collectio n unit s and treatmen t system s i n us e a t th e facility . Us e th e sam e code s a s i n footnot e a o f Tabl e 4 , o r you r own description . c ) Ente r th e tota l numbe r o f eac htyp e o f collectio n uni t and treatmen t syste mfo r eac hwastewate r source . d ) Auni t shoul d b e considere d covered i f i t ha s emissio n suppressio n device s i n place . e ) Fo r eac hcollectio n uni t o r treatmen t systemvente d t o a contro l device , lis t th e devic e an

d fil l ou t th e applicabl e sectio n o f Tabl e 8 . Us e th e sam e contro l devic e code s a s i n footnot e g o f Tabl e 2 . f ) Provid e th e name(s ) and othe r informatio n fo r an yadditiona l wastewate r collectio n unit(s ) presen t a t th e facility . g ) Provid e th e name(s ) and othe r informatio n fo r anyadditiona l wastewate r treatmen t approach(es ) use d a t th e facility .



# 231 9 TABLE6
. NON-AQUEOUS WAST ECOLLECTIO NAN D CONTROL(a )



### t o »* * Typeo f

Wast e (b ) Wast

eGeneratio

n Rat e (Tons/Yr ) (c ) Wast

eCollecte d i na Closed System? (Yes/No ) (d) Metho d o f On Sit eStorag e (e ) Wast

eTreate d or Disposed o f

OnSite ? (Yes/No ) 

### (0 Metho

d o f OnSit eTreatemen

t orDisposa

l (g ) Contro

l Devic e onTreatmen

tor Disposa l Unit (h )P.2 6

2 0 TABL E 6 . NON-AQUEOU S WAST E COLLECTIO NAN D CONTRO L (Continued )

a ) Non-aqueou s wast e i s considere d t o contai n betwee n 1 0 an d 9 0 percen t solids . b ) Selec t th e wast e cod e tha t bes t describe s th e non-aqueou s wast e type : A P = oil-wate r separato r sludg e B l = biotreatmen t sludg e H C = contaminate d soi l O T = oil ytras han d debri s S O = slo p oi l emulsion s S S = sump/sewe r clean-ou t sludg e B = tan k bottom s Z Z = other , pleas e specif y(us e extr a sheet , i f necessary) . c ) Lis t th e annua l non-aqueou s wast e generatio n rat e i n ton s pe r year . d ) Identif y(Ye s o r No ) whethe r th e wast e i s collecte d i n a close d vapo r collectio n system . Aclose d syste mha s equipmen t t o preven t o r minimiz e wast e contac t wit hth e atmosphere , suc has : vapo r recover y systems , enclose d pipes , o r collectio n unit s wit hcovers . e ) Selec t th e storag e cod e tha t bes t describe s th e metho d b ywhic hnon aqueou s wast e i s store d on-sit e prio r t o treatmen t o r disposal : .A A= ope n tank s B B = fixe d roo f tank s C C = floatin g roo f tank s D D = seale d DO T container s (5 5 gallo n drums , 11 0 gallo n bins ,

etc. ) E E = ope n roll-of f boxe s F F = covere d roll-of f boxe s G G = ope n pond s H H = covere d pond s I I = ope n pil e J J = covere d pil e KK = other , pleas e specif y(us e extr a sheet , i f necessary) . f ) Identif ywhethe r wast e i s treate d o r dispose d o f On-Sit e (Yes ) o r transporte d Off-Sit e fo r treatmen t and/o r disposa l withi n 9 0 day s o f generatio n (No ) .



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TABL E 6 . NON-AQUEOU S WAST E COLLECTIO NAN D CONTRO L (Concluded )

g ) I f wast e i s treate d o r dispose d o f On-Site , selec t th e treatmen t and/o r disposa l code(s ) tha t bes t describe(s ) ho wth e wast e i s manage d (i f mor e tha n on e cod e i s applicable , separat e multipl e code s wit ha comma ) : L F = land buria l L T = land treatment/farmin g D W = dewaterin g S T = solidification/stabilizatio n B l = biotreatmen t I N= incineration/therma l destructio n R E = recycle d O = other , pleas e specif y(us e extr a sheet , i f necessary) . h ) Us e th e sam e contro l devic e code s a s i n footnot e g o f Tabl e 2 .

### 2 2 TABL E 7 . EQUIPMEN T LEA K CONTRO L DAT A

Lea k Definition(a )

Equipment Component HA P Equipment Servic e (b ) Total

Equipment Coun t Equipmen t

Coun ti n LDA R Program Leak

Repai r Respons e Tim e (c ) LDA R

Monitoring Frequenc y (Times/Yr ) Equipmen tCounts

wit h Mechanica l Contro l Device s (d ) Equipmen t

Counts wit h aClose d Ven t System(e ) Close d Ven t

Syste mContro l Devic e 

### ( 0 Valve s

Compressors

Flange s2 3 TABL E 7 . EQUIPMEN T LEA K CONTRO L DAT A(Continued )

\ 3 X ) Equipment Componen t Open-ende d line s

Samplin g connection s

Pressurerelie f valve s Lea k HA PEquipmen tRepai rLDA REquipmen tCount s Equipmen tClose d Ven t EquipmentTotal Coun ti nRespons eMonitorin gwit h Mechanica l Counts wit h Syste mContro l Servic eEquipmentLDA RTim eFrequency Contro l Device s aClose d Devic e (b ) Coun tProgra m(c ) (Times/Yr ) (d ) Ven t(f ) System(e )

•P.3 0

2 4
TABL E 7 . EQUIPMEN T LEA K CONTRO L DAT A(Concluded )

a ) Th e VO C concentratio n leve l (ppmv ) a t whic hequipmen t component s ar e considered ' t o b e leakin g i n th e facility' s lea k detectio n an d repai r (LDAR ) progra m(i f applicable) . Ente r "VISUAL " i f yo u hav e a visua l lea k inspectio n program . Ente r "NONE " i f yo u d o no t hav e a forma l lea k program . b ) Selec t th e equipmen t servic e definitio n tha t bes t describe s th e physica l stat e o f liquid s a t operatin g conditions : Ga s = proces s fluid s containin g HAP s i n a gaseou s stat e a t

operatin g condition s L L = proces s fluid s containin g HAP s i n a liqui d stat e a t

operatin g condition s wit ha vapo r pressur e greate r tha n kerosen e (0.0 4 psi a a t 6 8 degree s F ) H L = proces s fluid s containin g HAP s i n a liqui d stat e a t

operatin g condition s wit ha vapo r pressur e les s tha n kerosene . c ) Indicate s th e averag e repai r respons e tim e (i n days ) onc e a lea k ha s bee n discovered . d ) Provid e equipmen t count s fo r equipmen t wit hmechanica l contro l device s suc has : sealles s valves , pump s wit hdua l mechanica l seal s an d a barrie r fluid , compressor s wit hmechanica l seal s an d a barrie r fluid , open-ende d line s wit hcaps/plugs/blin d flanges , an d pressur e relie f valve s wit hruptur e disks . e ) Provid e equipmen t count s fo r equipmen t wit ha vapo r collectio n an d recover y(close d vent ) system . f ) Us e th e sam e contro l devic e code s a s i n footnot e g o f Tabl e 2 .



# 2 9P.3 1



### 2 5 TABL E 8 . AI R POLLUTIONCONTRO L EQUIPMENT PARAMETERS(a ) Contro l Device : Scrubbe r Identifie r Code : Type o f scrubber : ventur i packedbe d impingemen

t othe r (specify) Gas inlet temperature , " F Pressur e drop , inH„ 0

2 3 Liquid-to-ga s ratio , gal/1 0 acf m Inlet scrubbing liquor : P H percent solid s typ e o f alkali added , if

any rate (lbs/gal ) Wastewate

r generationrate , gal/min HA Pcompositiono f

wastewater, mg/ { Emissio nSource s (b )



# 3 0P.3 2



### 2 6 TABL E 8 . AI R POLLUTIONCONTRO L EQUIPMENT PARAMETERS(a ) (Continued ) Control Device : Incinerato r Identifie r Code : Type : therma

l catalyti c Combustionchambe

r temperature . ° F (pleas e note if

temperatur

e measuremen

t i s not i nchamber ) Exces s air , % Nomina l residenc e time , s Hea t recovery : recuperative , percen

t hea t recover y regenerative , percen

t hea t recover y 

### EmissionSources (b )

Control Device : Flar

e Identifie r Code : Type : n o assis t stea massis t air assis t pressur e assist Location : ground elevated Hea t conten t o f ventedstream , Btu/scf Flar e ga s exit velocity , ft/s Flar e ti p diameter , in
. Flar e height , ft Supplementar

y fue l for : pilot , scf m combustionpurposes , scf

m Stea mrequirement , Ib/h

r Emissio nSource s (b )



# 3 1P.3 3

2 7 TABL E 8 . AI R POLLUTIO NCONTRO L EQUIPMEN T PARAMETERS(a ) (Concluded ) Contro l Device : Carbo nAdsorbe r Identifie r Code : Typ e o f carbonbedandnumber : fixed fluidized How man y pound s o f

carbonpe r bed Configuration : parallel seria l Numbe r o f bed s on-line Numbe r o f bed s desorbing Pressur e drop
. in
. H2 0 Gas inle t temperature , ° F Typ e o f regeneration Regenerationtime Adsorptiontim

e Emissio nSource s (b )

Contro l Device : Condense r Identifie r Code : Typ e of condenser : surface contact Ti f contac t se e scrubbe d Gas inle t temperature , ° F Gas outlet temperature , ° F Emissio nSource s (b )

* , •

a ) Aseparat e tabl e shoul d b e fille d ou t (afte r makin g copie s o f th e blan k table ) fo r eac hindividua l scrubber , incinerator , flare , carbo n adsorber , o r condense r a t th e facility . Fo r othe r type s o f contro l device , provid e th e mos t importan t parameter s o f operatio n o n a separat e sheet . b ) Lis t specifi c storag e tanks , loading racks/arms , and wastewate r and non-aqueou s wast e treatmen t o r disposa l processes , usin g I D code s an d name s fromTable s 2 , 3 , 5 , an d 6 . 

# 32