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# OAR Box 1672 Prepped by Charmelle Mathews



# Document

Number: 

# f)/Jffl\\-B-7
Docket Number: 

# A-98-1 3

Printed 9/30/2008 11:01:00 AM Sheet 13 of 132

# T P. 2



# ,t £P a(= 3 

# A-W 3

MEMORANDU

M

TO :



# FROM :

DATE : SUBJECT : Project

Fil e Organic Liquid s Distributio nNESHA P ES D Project

No

. 96/0 5 Bern dHanek e Pacific Environmenta

l Services , Inc

. (PES ) April 28,199 8 Sit e Visit to GAT X Terminal s Corporationfacilit y i nPhiladelphia , Pennsylvani a I . Purpos e The purpos e o

f thi s sit e visit wa s to tou

r the facilit y t o educat e EP A andcontractor personnel concerning organic liquid s distributio noperation s an dt o collect informationrelate d t o ai r emission s fromthe operations

. Thi s wor k i s i nsuppor t o f th e developmen

t of nationa l emissionstandard s fo

r hazardou s ai

r pollutant s (NESHAP

) fo r the organi c liquid s distributio n (non-gasoline ) sourc e category

. II . Location an

d Dat e GAT X Terminal s Corporation 3300 N

. Delawar

e Avenue Philadelphia , Pennsylvani a Decembe r 19,199 7 (8:3 0 a

m-12:3 0 pm

) EP AAI R DOCKE T



# III . Participant

s GAT X Terminal s Corporation Steve n Kuhrt z - Vic e President , Environmen t an dSafet y Alfre dJ

. Sha y - Operation s Manage

r Christophe r D

. Car y - Environmenta

l Manage r EPA/DOT/USC GProgram s Thomas J

. Stafinia

k - Manager , Environment , Healt handSafet

y Environmenta

l Protectio nAgency Stephe nShed d- Project Officer, OAQPS/ESD/WCP G ResearchTriangle Park, NC Pacific Environmenta

l Services

. Inc

. (PES ) Greg LaFla

m- Environmenta

l Engineer , RTP , N

C 

# TLP. 3 

# T

Sit e Visit Memo/GATX-Philadelphi a Apri l 28,199 8 Pag e 2 BerndHanek e - Environmenta

l Scientist , RTP , N C Ja y Helm s - Environmenta

l Engineer , RTP , NC

IV . Pre-Tou rDiscussio n Introductio n Afte r th e participant s introduce dthemselves , Steve Kuhrtz , GATX , opene dth e meetin g wit ha nintroductio nt o th e GAT

X Terminal s Corporation

. GAT X currently operate s 2 5 terminal s inth e U.S

. and20 oversea s terminal s inEurop e andAsia

. GAT X terminal s handl e approximately 8 0 percent

petroleumproduct s an

d20 percen

t chemicals

. Fiv e o f

th e GAT X terminal s handl e chemical s exclusively

. The Philadelphi atermina l handle s primarily chemicals , wit

hth e exceptio no f

aviatio ngasoline

. Stev e Shedd , EPA , followedMr

. Kuhrt z wit hadiscussio no f

th e backgroundan d rational e fo

r EPA' s regulatio no f

hazardou s air

pollutan t (HAP) emissions

. Prior

t o th e Clea

n Ai r Act Amendment s of

1990 (CAAA) , regulation s wer e onth e basi s o f

individua l HA Pan d fe w regulation s wer

e enacted

. Th

e CAA A includedalis t

o f HA Pandmandate dtha

t nationa l emissio nstandard s fo

r HA P(NESHAP) b e developedfo r categorie s o f

source s of

th e HAPs

. The stringency of

th e Organi c Liquid s Distributio n(non-gasoline ) NESHAP(fo r existin g sources ) wil l b e base donalevel of contro l representing th e averag e contro l achieve dby th e top 1 2 percent o f facilitie s inth e category

. Th e Organic Liquid s Distributio nstandard s are slatedto b e propose din1999 , wit

hpromulgatio nof

th e final rul e inNovembe

r 2000

. Mr

. Shed dstate dtha

t th e EP A ha s prepareda

nindustr y questionnair

e anddistribute di t t o trade organization s fo

r their review an dcomment

. The questionnaire , whenfinal, wil l b e sen t t o severa l companie s withi nth e Organi c Liqui dDistributio nsourc e category

. He als o describedth e EPA' s procedure s fo r handling informationtha

t th e compan

y consider s t o b e confidentia

l busines s information(CBI)

. Mr

. Shed dinquire dandGAT

X representative s di d no t claimanything durin g th e EP A sit e visit a s confidential

. The compan y wil l hav e a

n opportunit y to revie w th e draf

t sit e visit repor t preparedby PES , to commen t o nit s accuracy an dto identif y anything i n th e repor

t they conside

r to b e CBI

. Thi s report , wit han y CB I withheld , wil l b e made apar t o f th e publi c recor

dfo r thi s rulemaking

. Facilit y Descriptio n The Philadelphi afacilit

y i s abulk storag e termina

l locate do napproximately 3 5 acre s o f propert y onthe Delawar

e River jus t nort hof downtownPhiladelphia

. The termina l ha s approximately 10

0 tank s wit

hatota l storag e capacit

y o f 1.2 millio nbarrels

. The storag e tank s locateda t th e termina

l rang e insiz e from71 5 t o 100,000 barrels

. Product s are handle dbyP. 4



# Sit e Visit Memo/GATX-Philadelphi a April 28,199 8 Page 3 marine vessel (barg e andtanke r ship) , railcars , an

dtrucks

. Ther

e ar e tw o marine docks , one fo r bot hship s andbarge s (bert

h#2 ) an dthe othe r bert h(bert h#1 ) i s fo r barge s only

. I

n 1990 , a ne w abov e groundpipelin e syste mwas constructedfo

r th e marine loading andunloading

. In general , th e facilit

y i s graduating fromundergroundtowar dabov e grounddedicate dpipelines

. Th e facilit y ha s 1 7 tan

k truck loading/unloading station s whichhav e th e abilit y t o servic e multipl e tanks

. Liqui dchemical s ar

e brough t int o th e facilit

y andsen t out fromth e facilit

y by marine vessel , railcar , andtan

k truck

. The facilit

y receive s an

dship s out

product s ownedby other s o n afor-hir e basis

. The facilit

y blend s variou s recipe s a

t th e on sit e denaturedspirit s plant , inlcuding brucine an

dalcohol

. Som

e proprietar

y blending of

ethyl alcoho l basedmaterial s i s als o performeda

t th e denaturedspirit s plant

. Th e facilit y als o blend s othe

r acide s sucha s formic an daceti c acid

. Most

of the blending tha

t occur s her

e i s "in-lin e blending" , tha

t i s to sa y tha t liquid s ar e blende das they ar

e being transferredint

o tan k trucks

. Liquid s tha

t mov e throughth e termina

l i n larg e quantitie s ar

e phenol , benzene , cumene , acetone , organi c acids , an dfue l grade ethanol

. GATX/Philadelphi ahandle s bot hdomesti c andinternationa l shipments

. The approximat

e quantitie s handledpe

r year , by deliver

y mode , are :

- 24 milliongallons/yea

r by tank truck s

- 1 2 milliongallons/yea

r by railcar s

—6 6 milliongallons/yea

r by barge s

—1 2 milliongallons/yea

r by tanke r ship s The storag e tank s a

t th e facilit y consis t of cone roof , specialt y dom e roof , an daluminum as well a s steel interna

l floating roo f

tanks

. A fe

w o f th e storag e tank s ar

e dedicatedt o certai n products , sucha s th e benzene tank , whichha s a ninterna l floating roof

. Som e o f th e storag e tank s ar e subject to th e NSP S requirement s fo r storag e tank s (Subpar

t K, Ka , o r Kb)

. Emission s Inventor

y GATX/Philadelphi ai s currentl y trying to obtainasyntheti c minor status

. Tan

k emissions , fugitive emissions , andloading los s summarie s are include dinAttachment s 1 through3

. A plo t

pla nof th e facilit y i s containedinAttachmen t 4

. Separat

e inventorie s ar

e shownfo r tank emissions , fugitive emissions , an dloading losses

. A copy of th e 199 6 emission s inventor

y wa s obtainedduring the sit e visit , andemission s fromth e facilit y ar e showna s follows : 

# 3P. 5



# Sit e Visi t Memo/GATX-Philadelphi a Apri l 28,199 8 Pag e 4 TABLE 1 . SUMMAR

Y O F 1996 EMISSION S INVENTOR Y (Compiledb y EPA/PE S project tea musing informationsuppliedby GATX/Philadelphia)

Emission Sourc

e Fugitiv e Emission s Storag e Tanks Loading Losse s Wastewate r Tota l VOC(tpy )

1.0 0 20.0 8 10.4 3 No t Available 31.5 1 HAP(tpy ) 0.40 16.22 4.0 2 No t Available 20.6 4 

# Accordin g t o th e emission s inventor y suppliedto th e EPA/PE S project team , th e facilit

y i s no t amajo r sourc e fo r HAPs

. No informationwa s obtaine dregardin g th e emissio nfactor s tha t wer e use dt o calculate fugitive emissions

. Product s Handled Compan y representative s distribute dalistin g o f th e HA Pliqui dproduct s handle dby th e facilit y in1996

. The facilit

y handle s primarily chemicals , wit hth e exceptio no f

aviation-grade gasoline

. The chemical s handledar e primarily benzene , cumene , methanol , methy l chloroform , methy l ethy l ketone , methylene chloride , phenol , andtrichloroethylene

. Cumene i s th e primar y chemical , comprisin g approximately 3 3 percent of all chemical s handled

. Among th e acid s handle dandstoreda

t th e terminal , aceti c acid , whichha s afreezing point o f 6 2 degree s Fahrenhei t

(°F) , i s transferredandstore di ninsulate dline s andheate dtanks

. Contro l Measure s Th e compan

y ha s incorporatedcertaincontro l measure s t o reduc e air emission s o f volatil e chemica

l product s a

t the GAT X facility

. One specific contro l systemi s inuse : a n enclose dcombustio nsystem(therma l oxidizer) wit

habacku p systemo f

fou r carbo ncanisters

. Th e therma

l oxidizer , suppliedby Nationa l Air Oil (NAO) , i s usedto contro l vapor s displace ddurin g tan

k truck loading o f

benzene andaviatio ngasoline , andals o emission s from th e fixed-roof

tank storag e o f acrylate s (fo

r odor contro l purposes)

. Thi s systemi s approximately 2. 4 meter s ( 8 feet ) indiameter , an

dha s abacku

p o f fou r carboncanisters , i ncas e o f problem s resultin g inth e temporar y shutdowno f

th e unit

. The unit

utilize s No

. 2 fue

l oi l t o maintai nth e prope

r operating temperature

. Additionally , th e therma l oxidize r ha s acapacit

y o f 25 0 scfm

. Temperatur

e i s monitoredcontinuously a t th e therma

l oxidize r to ensur e tha t i t i s functioning properly

. The idea l operating temperatur

e ha s beenset

a t 1,250°F

. A s mentione d 

# 4 -P. 6



# Sit e Visit Memo/GATX-Philadelphi a April 28,199 8 Pag e 5 above , shoul dthe therma

l oxidize r malfunction , ther

e i s afou r carboncaniste

r (carbo n adsorption ) backu

p system

. Benzene , a s well as othe

r vapor s tha

t ar e routedto the therma

l oxidize r ar e first store d an daccumulatedintw o 30,000 gallontank s tha t wer e previously usedt

o stor e liquifie d petroleumga s (LPG)

. Th

e syste moperate s unde

r 5 inche s of

vacuum , an

dwhencapacit

y i s reached , th e vapor s ar

e ventedto the therma

l oxidizer

. The GAT X facilit y als o monitor s it s equipmen t fo r leaks onaregula

r basis

. There i s a monthly monitoring progra mfo r equipmen t tha t i s inbenzene servic e (pumps , flanges , valves , etc.)

. Additionally , pump s tha t ar e inbenzene servic e ar

e monitoredfo

r leak s onaweekly basis

. Equipmen

t handling VOC i s monitore donaquarterl y basis

. Beside s th e monitorin g program s mentionedhere , equipmen t i s visually monitoredona

nongoing basi s by GAT

X personnel

. All equipmen

t handling VOC' s wit

haRV Pgreate r tha n4 ar e monitore do na monthly basi s a s specifiedinth e RACT plan

. The facilit y doe s not employ an

y typ e o f wastewate

r treatmen t system , except

fo r a n oil/wate r separator tha t treat s contaminatedwast

e water

. The treate dstor

mwater i s discharge d int o apublicly ownedtreatmen t works facilit

y (POTW)

. It

i s estimatedtha

t a naverag e o f

4 0 gal/mindischarg e fromth e AP I oil/wate r separator i s atypica l value fo r stor mevents

. Wastewate

r a t GAT X i s primarily aproduc t

of tan k an dpipeline cleanings , an dspills

. A naverag e o f

1 5 tanks/yea

r ar e cleaneda

t th e facility

. Tanks ar

e cleanedwit

haho t water causti c wash

. Alternatively , tank s ar e strippe do f

all product

prior to being either

causti c washed , detergen

t washed , fresh wate

r washedor

ai r dried

. A membe

r o f th e EPA/PE S projec t tea minquire da s to the availabilit y of emissio nfactors fo

r tan k cleanings

. GAT

X representative s repliedtha

t no suc hfactors wer

e inexistenc e a

t thi s time

. Drum s ar e usedfo r the storag e o f

hazardou s wast

e andnon-hazardou s waste s ar e store d insevera l small tanks

. Wast

e wate r whichi s aproduct

o f tan k washing s i s dispose do f

off-sit e by acontractor

within9 0 day s of

generation

. Late

r conversation s betwee

nMr

. Sha y an dMr

. Hanek e indicate dtha

t approximatel

y 30,000 gallon s of

wast e wate r ar e generate donth e facilit

y ona nannua l basi s an dtreate doff-sit

e by acontractor

. V . Items Requested b y the EP A ProjectTea

m Variou s item s wer

e requestedby th e EP

A project tea mduring the site visit

. I n particular , Mr

. LaFla

mrequested : 1

. The result s of

the efficienc

y tes t o f th e therma

l oxidizer , 2

. The operating cost s of

th e therma

l oxidizer , 

# £P. 7



# Sit e Visit Memo/GATX-Philadelphi a April 28,199 8 Pag e 6 3

. The dolla

r amoun t o f th e therma

l oxidizer' s annua

l servic e contract , and 4

. The dolla

r amoun t of th e capita l cost s fo r installing th e therma

l oxidizer

. Othe r item s requestedby th e EPA/PE S project tea mincluded : 1

. The volume s o f

wastewate

r (non-stormwater

) generatedper

yea r a t th e facility , 2

. The HA

Pconcentratio no f

th e wastewate

r (i f known) , and 3

. Emissionfactors use dt o calculat e fugitive emission s fo

r th e facility

. V . PlantTour A t th e conclusiono f

th e discussio nsummarizedinSectionI V above , Mr

. Sha

y too k th e EPA/PE S tea

monawalking tour

o f th e facility

. The tour bega nwit hatri p acros s Delawar

e Avenue to th e ship loadin g dock whic h border s th e Delawar

e River

. Mr

. Sha

y explaine dt o th e grou

p th e proces s o f

loadin g and unloadin g amarine vessel

. Numerou s hose s wer e observedtha

t servedto unloadship s and barges

. Thes e hose s wer

e connectedto abov e groundpipeline s tha t convey liquid s t o th e main facility

. Mr

. Sha

y als o explaine dth e mean s by whichpipeline s ar e pigged

. Piggin g o f pipeline s serve s the purpos e o f cleanin g a s well a s th e remova l o f th e majorit

y o f th e produc t fro mth e line prior

to using th e lin e fo

r simila r products

. Next , Mr

. Sha

y ledth e grou

p t o one of

th e railca r loading racks

. He explaine dth e proces s by whicharailca

r i s loadedandunloaded

. Th e car s ar e usually to p loade dandbotto m unloade dwit

hvariou s liquids

. Som

e rai l ca r position s hav e vapo

r recover y lines

. Additionally , rai l ca r tank s ca nb e purgedor

blankete dwit

hnitrogeno

r heatedwit

hsteam

. Whenloadin g aceti c acid , it

i s necessar

y to hea t th e liqui ddue to it s highfreezing point

. At th e tim e o f

th e sit e visit , th e facilit

y wa s not loadin g an

y product s int

o railcar s tha

t require dvapor

recovery . Next , th e tour

continue do nto th e denaturedspirit s plant , whichi s where th e facility' s small blendin g operation s tak e place

. The operatio ninvolve s eigh t 5,000 gallo ntank s a s wel l a s product s in5 5 gallondrum s usedfo r th e denaturing process . Ther e ar e als o fou r mai n storag e tank s tha

t hav e atota

l capacit y o f 2,342,00 0 gallon s tha

t stor e ethanol

. Following the denaturedspirit s plant , Mr

. Sha y ledthe grou

p t o th e thermal oxidizer

. The therma

l oxidize r wa s discusse dandviewedonsite , an da nalar mwa s service ddurin g th e EPA/PE S project

tea msit e visit

. Fou

r carboncanister s whichserv e a s backup s t o th e therma l oxidizer wer e als o vieweda

t thi s location , as wa s th e No

. 2 fue l oil tank whichprovide s fue

l fo r th e therma l oxidizer

. At one poin t inth e facility , aserie s of

tw o pressur

e vessel s wer

e observe dtha

t serv e t o 

# 6P. 8



# Sit e Visit Memo/GATX-Philadelphi a April 28,199 8 Pag e 7 captur e vapor s fromstorag e tanks

. Thes e vapor s ar e collectedinth e storag e vessel s an d subsequently ar

e sen t t o th e therma

l oxidizer

. Loading racks andtheir

associatedloading arm s wer e als o observe da

t th e GAT X plant site

. A rack

tha t handle s aviatio ngrad

e gasoline was observed , along wit hit s vapor retur n lines

. Ther

e wer e als o rack s wit

hdedicatedbenzene service , along wit harack handlin g acrylates

. VI . Post-Tou rDiscussion Following th e plant

tour , abrief

discussionwas heldto review th e content o f th e tour an dadditiona

l question s wer

e asked

. Th

e EPA/PES tea

mals o reviewe dth e item s it wishedt o have sen t following th e site visit

(se e Section V , Items Requested b y th e EP A Project Team) . The EPA/PE S tea

mexpressedtheir

thanks andth e visit

wa s concluded

.

VII . Action Items The EP A an dPE S will prepar

e adraf t sit e visit trip report , whichwil l b e sen t out t o th e GAT X facilit y fo r technica l review andidentificationof an y CBI

. The EPA/PE S projec t tea m expressedadesir

e to receiv e th e requestedinformationwithinareasonabl e amoun t o f time

.



# 7-GAf XTerminal s Corporatio n Tan k Emission s Summary •199 6

Ton k It Typ e Product(s ) (H.I.V ) Tank # Typ e Producl(s ) (H.I.V ) 5 1 V 5 2 V 5 3 V 5 4 V 5 5 V 5 6 V 5 7 V 5 8 V 104 V 10 5 V 10 6 V 107 1 10 8 V 12 1 V 12 2 V 12 3 1 12 4 1 12 4 1 12 5 V 12 6 V JQ12 7 V 12 8 V 12 9 V 13 0 V 13 1 V 13 3 V 13 4 V 13 4 V 13 5 V 13 5 V 13 7 V 14 0 V 14 1 V 14 2 V 14 3 1 144 V 14 5 V 14 5 V 14 6 V 14 7 V 14 8 I 14 8 1 Methy l Isobuty l Keton e

Methy l Isobuty l Keton e Isopropy l Alcoho l Ethy l Acetat e Ethano l Ethano l Methy l Alcoho l Buty l Alcoho l (-lert ) Oiocty l Phthalat e Methy l Methacrylat e Oicyclopentadien e Jet Napth a empty Cyclohexan e Nonylpheno l Ethoxylal e Cumen e Xylen e Cyclohexan e Cumen e Cyclohexan e Empt y Dicyclopentadien e Causti c Sod a Cumen e Was h Wate r Empt y Pheno l Was h Wate r Cumen e Pheno l Pheno l Cumen e 2-Ethy l Hexano l Empt y Nonylpheno l Ethoxylal e Isobuty l Alcoho l Ethy l Acetate Not Use d
. Isopheron e • Furfura l • Empt y • 2-Ethy l Hexy l Alcoho l Cumen e Xylen e ' Tan k CapacThrupu t Breathin g Losse s 100 0 gallo n 100 0 gallo n (Ib/yr ) Tan k CapacThrupu t (T/yr )

Breathin g Losse s 100 0 gallo n 100 0 gallo n (Ib/yr )

5 5 5 5 5 5 5 5 40 9 40 9 53 3 12 3 12 2 20 7 41 1 65 0 151 1 151 1 204 7 20 8 93 3 40 9 70 8 12 1 12 1 81 7 41 0 41 0 61 2 61 2 20 7 12 2 41 1 20 4 38 7 41 0 41 0 41 0 41 1 41 0 76 2 76 2 0

5 4 6 1. 2 5 1 2 8 9 1 5 0 147 7 42 2 41 7 0 105 5 64 5 423 5 23 5 692 0 5686 3 94 5 0 7 6 0 129 8 0 46 3 79 0 0 38 4 155 9 21 2 0 0 0 47 6 0 38 1 23 0 0 126 5 2 4 1 7 9.4 4

9.4 4 14.3 1 55.1 9 24.8 7 24.8 7 27. 7 15. 3 272.2 7 1166.4 5 76.0 9 285.6 3 1573.7 8 111.4 5 33.7 3 26.0 8 1063.6 6 908.1 8 1573.7 8 112.9 1 0 7.0 8 74.1 6 99.1 3 29.5 8 67. 2 47.2 4 6.2 6 68.7 3 192.5 3 43 7 205. 9 3.2 2

13.5 8 13.2 6 8.0 8 (T/yr ) 0.004 7 0.004 7 0.007 2 0.027 6 0.012 4 0.012 4 0.013 9 0.007 7 0.136 1 0.583 2 0.03 8 0.142 8 0 0.786 9 0.055 7 0.016 9 0.01 3 0.531 9 0.454 1 0.786 9 0 0.056 5 0.003 5 0 0.037 1 0.049 6 0.014 8 0.033 6 0.023 6 0.003 1 0 0.034 4 0.096 3 0.218 5 0 0.10 3 0.001 6 0 0.006 8 0.006 6 0.00 4 Workin g Losse s (Ib/yr ) (T/yr ) Workin g Losse s (Ib/yr ) 0 2.3 5 27.8 4 2.5 8 51.4 8 28. 1 8.3 5 9. 5 0 1299. 9 13.6 1 2.9 3 228 9 37.4 6 16.4 8 0.6 2 16.1 7 7117. 8 2050. 1 0 0 24.3 3 19.7 1 111.2 8 0 16.3 5 166.8 4 2.0 9 0 0 2.6 4 63.2 3 4.2 4

12.4 5 0.1 7 0.1 3 (T/yr ) 0 0.00 1 0.01 4 0.00 1 0.02 6 0.01 4 0.00 4 0.00 5 0 0.6 5 0.00 7 0.00 1 0 1.14 5 0.01 9 0.00 8 0.00 0 0.00 8 3.55 9 1.02 5 0 0 0.01 2 0 0.0 1 0.05 6 0 0.00 8 0.08 3 0.00 1 0 0 0 0.00 1 0 0.03 2 0.00 2 0 0.00 6 0.00 0 0.00 0 Uncontrolle d Emi s ControEfficiVO C Breathin g (Ib/yr ) (T/yr ) (% ) (Y/N ) (T/yr ) Uncontrolle d Emi s ControEfficiVO C Breathin g (Ib/yr ) 9.4 4 11.7 9 42.1 5 57.7 7 76.3 5 52.9 7 36.0 5 24.8 0 272.2 7 2466.3 0 89.7 0 288.5 6 0.0 0 3862.7 9 148.9 1 50.2 1 26.7 0 1080.0 3 8025.9 3 3623.8 5 0.0 0 112.9 1 0.0 0 31.4 1 0.0 0 93.8 7 210.4 1 29.5 8 0.0 0 83.5 5 214.0 8 0.0 0 8.3 5 0.0 0 68.7 3 192.5 3 439.6 4 0.0 0 269.1 3 7.4 6 0.0 0 26.0 3 13.4 3 8.2 1

TNKSUM96.WK 4 (T/yr ) 0.004 7 Non e 0.005 9 Non e 0.021 1 Non e 0.028 9 Non e 0.038 2 Non e 0.026 5 Non e 0.018 0 Non e 0.012 4 Non e 0.136 1 Non e 1.233 2 Incln e 0.044 9 Non e 0.144 3 Non e 0.000 0 Non e 1.931 4 77 ? 0.074 5 Non e 0.025 1 Non e 0.013 4 Non e 0.540 0 Non e 4.013 0 Non e 1.8119?? ? 0.000 0 Incin e 0.056 5 Non e 0.015 7 Non e 0.000 0 Incin e 0.046 9 Non e 0.105 2 Non e 0.014 8 Non e 0.041 8 Non e 0.107 0 Non e 0.004 2 Non e 0.000 0 Incin e 0.034 4 Non e 0.096 3 Non e 0.219 8 Non e 0.000 0 Non e 0.134 6 Non e 0.003 7 Non e 0.000 0 Non e 0.013 0 Non e 0.006 7 Non e 0.004 1 Non e (%) (Y/N ) (T/yr )

O Y O Y O Y O Y O Y 0 Y O Y 0 Y 0 Y 9 9 Y O Y 0 Y O N 9 9 Y 0 Y O Y 0 Y O Y O Y 9 9 Y 9 9 N O Y N O Y 9 9 N 0 Y 0 Y 0 Y 0 Y

•• 0 Y O Y 9 9 N O Y O N 0 Y O N 0 Y O Y O N 0 Y 0 Y 0 Y 0.0047 2

0.0047 2 0.00715 5 0.02759 5 0.01243 5 0.01243 5 0.0138 5 0.0076 5 0.13613 5 0.00583 2 0.03804 5 0.14281 5 0.00786 9 0.05572 5 0.01686 5 0.0130 4 0.5319 3 0.4540 9 0.00786 9 0.05645 5 0.0035 4 0.0370 8 0.04956 5 0.0147 9 0.033 6 0.0236 2 0.0031 3 0.03436 5 0.218 5 0.1029 5 0.00161
.

0.0067 9 0.0066 3 0.0040 4 Workin g HA P Breathin g

(T/yr ) (Y/N ) (T/yr ) Workin g HA P Breathin g (T/yr ) (Y/N ) (T/yr )

O Y 0.00117 5 Y 0.0139 2 N 0.0012 9 N 0.0257 4 N 0.0140 5 N 0.00417 5 Y 0.0047 5 N O N 0.00649 9 Y 0.00680 5 N 0.00146 5 N

N 0.01144 5 N 0.0187 3 N 0.0082 4 Y 0.0003 1 Y 0.00808 5 N 3.55887 5 Y 0.0102 5 N

N 0 N N 0.01216 5 Y

N 0.00985 5 Y 0.0556 4 Y 0 Y 0.00817 5 Y 0.0834 2 Y 0.00104 5 N

N O N N 0.0013 2 N

N 0.03161 5 N 0.0021 2 N

N 0.00622 5 N 0.00008 5 Y 0.00006 5 Y 0.0047 2

0.0047 2

0.0138 5

0.00583 2

0.01686 5 0.0130 4

0.4540 9

0.0035 4 0.0370 8 0.04956 5 0.0147 9 0.033 6 0.0236 2

0.0066 3 0.0040 4 Workin g

(T/yr ) Workin g (T/yr ) 0 0.00117 5

0.00417 5

0.00649 9

0.0082 4 0.0003 1

3.55887 5

0.01216 5 0.00985 5 0.0556 4 0 0.00817 5 0.0834 2

0.00008 5 0.00006 5

Pag e 1 05/12/9 7 cd

C OGATXTerminal s Corporatio n Tan k Emission s Summar y -199 6

Tan k U Typ e Product(s ) (H.I.V ) / 14 9 I > / 15 0 1 15 1 1 15 2 1 15 3 V 154 V 15 5 V 15 6 V 15 7 V 15 8 V 15 9 1 16 0 1 16 1 I 16 2 I 16 3 1 16 4 I

. 19 8 V r\19 9 v ^20 0 V 20 1 V 20 2 V 20 3 V 20 4 1 20 5 V 20 6 V 20 7 V 20 8 V 20 9 V 21 0 V 21 1 V 21 2 V 21 2 V -/'21 3 1 21 4 V S 21 5 1 sr 21 6 1 ''21 6 1 21 7 V 21 8 V 21 9 V 22 0 V 22 1 V 22 2 V Xylen e

Trichloroethylen e , . Cumen e Benzen e Minera l Spirits ' Minera l Spirits Parrafi n Wa x Parrafi n Wa x alpha-Methy l Styren e Plasticize r 16 0 Aceton e Aceton e Aceton e Aceton e Aceton e Cumen e Pheno l Neo-Penty l Glyco l Slurr y Aceti c Aci d Formi c Aci d Propioni c Aci d Aceli vAnhydrid e Cumen e Methy l Ethy l Ketoxim e 1,2-Dichlorobenzen e Cumen e Cumen e Em.pt y Nonen e Cumen e Cumen e Cyclohexanon e Methylen e Chlorid e n-Buty l Acetat e Trichloroethylen e Trichloroethylen e Methylen e Chlorid e Isoocten e Nonen e Nonen e Nonen e Hepten e Heplen e Tan k CapacThrupu t 100 0 gallo n 38 4 38 7 77 3 76 8 41 1 41 1 81 8 81 5 41 1 41 0 79 8 79 8 79 8 79 8 79 8 79 8 30 1 30 0 30 1 30 1 20 7 20 7 123 7 49 4 49 4 49 4 49 4 49 4 49 4 49 4 49 3 49 3 25 6 27 9 27 9 28 1 28 1 49 6 49 6 49 5 49 4 49 5 49 5 100 0 gallo n

0 4 7 391 4 328 7 418 6 23 3 352 7 82 6 163 4 5 3 1057 6 1024 8 949 0 950 5 764 1 208 1 176 7 57 4 189 7 138 2 39 2 79 4 2590 3 25 6 53 6 67 6 129 7 0 123 6 53 0 46 5 30 5 46 6 63 1 30 3 6 3 13 3 19 2 253 8 308 7 248 0 152 9 117 9 Breathin g Losse s (Ib/yr)5.8 9 268.0 6 37.4 5 648.5 4 114:2 8 89.4 1 0.0 1 0.0 1 80.6 4 0 973.6 9 1012.2 7 910.4 5 1012.2 7 2119.4 4 13.7 8 55.7 4 303.1 9 469.8 3 1114.4 5 35.2 2 170.5 5 40. 2 80.4 6 72.8 1 52.24 - 205.5 9 237.1 8 52.2 4 52.2 4 70.0 8 3498.2 8 259.4 6 253.0 1 214.0 2 367.8 3 2334.8 8 237.1 8 237.1 8 237.1 8 2331.7 6 2331.7 6 (T/yr )

0.002 9 0.13 4 0.018 7 0.324 3 0.057 1 0.044 7 5E-0 6 5E-0 6 0.040 3 0 0.486 8 0.506 1 0.455 2 0.506 1 1.059 7 0.006 9 0.027 9 0.151 6 0.234 9 0.557 2 0.017 6 0.085 3 0.020 1 0.040 2 0.036 4 0.026 1 0.102 8 * 0 0.118 6 0.026 1 0.026 1 0.03 5 1.749 1 0.129 7 0.126 5 0.10 7 0.183 9 1.167 4 0.118 6 0.118 6 0.116 6 1.165 9 1.165 9 Workin g Losse s Uncontrolle d Emi s ControEfficiVO C Breathin g (Ib/yr ) 0 0.1 8 14.4 1 12.4 3 345.9 3 14. 2 0 0 95.1 3 0 36.6 7 38.8 2 29.2 9 35.9 4 28.9 8 6.4 2 75.2 1 95.3 9 478.6 2 817.9 3 11.1 3 108.4 4 83.9 3 20. 5 23.8 7 88.4 1 162. 4 178.3 7 69.3 3 60.7 6 43.6 9 4.8 5 186.2 9 3.6 6 0.7 4 1.4 2 261.6 4 366.2 2 445.3 4 357.8 4 2142. 1 1650. 8 (T/yr ) (Ib/yr )

0 5.8 9 0.00 0 268.2 4 0.00 7 51.8 6 0.00 6 660.9 7 0.17 3 460.2 1 0.00 7 103.6 1 0 0.0 1 0 0.0 1 0.04 8 175.7 7 0 0.0 0 0.01 8 1010.3 6 0.01 9 1051.0 9 0.01 5 939.7 4 0.01 8 1048.2 1 0.01 4 2148.4 2

0.0 0 0.00 3 20.2 0

0.0 0 0.03 8 130.9 5 0.04 8 398.5 8 0.23 9 948.4 5 0.40 9 1932.3 8 0.00 6 46.3 5 0.05 4 278.9 9 0.04 2 124.1 3 0.0 1 100.9 6 0.01 2 96.6 8 0.04 4 140.6 5 0.08 1 367.9 9 0 0.0 0 0.08 9 415.5 5 0.03 5 121.5 7 0.0 3 113.0 0 0.022
. 113.7 7 0.00 2 3503.1 3 0.09 3 445.7 5 0.00 2 256.6 7 0.00 0 214.7 6 0.00 1 369.2 5 0.13 1 2596.5 2 0.18 3 603.4 0 0.22 3 682.5 2 0.17 9 595.0 2 1.07 1 4473.8 8 0.82 5 3982.5 6

TNKSUM96.WK 4 (T/yr ) 0.002 9 Non e 0.134 1 Non e 0.025 9 Non e 0.330 5 Non e 0.230 1 Non e 0.051 8 Non e 0.000 0 Non e 0.000 0 Non e 0.087 9 Non e 0.000 0 Non e 0.505 2 Non e 0.525 5 Non e 0.469 9 Non e 0.524 1 Non e 1.074 2 Non e 0.010 1 Non e 0.065 5 Non e 0.199 3 Non e 0.474 2 Non e 0.966 2 Non e 0.023 2 Non e 0.139 5 Non e 0.062 1 Non e 0.050 5 Non e 0.048 3 Non e 0.070 3 Non e 0.184 0 Non e 0.000 0 Non e 0.207 8 Non e 0.060 8 Non e 0.056 5 Non e 0.056 9 Non e 1.751 6 Non e 0.222 9 Non e 0.128 3 Non e 0.107 4 Non e 0.164 6 Non e 1.298 3 Non e 0.301 7 Non e 0.341 3 Non e 0.297 5 Non e 2.236 9 Non e 1.991 3 Non e (% ) (Y/N ) (T/yr )

0 Y O N O Y O Y 0 Y 0 Y O Y O Y O Y O Y O N O N O N O N O N

•• O Y 0 Y 0 Y O Y O Y O Y 0 Y 0 Y 0 Y 0 Y 0 Y 0 Y 0 N 0 Y 0 Y 0 Y 0 Y 0 N 0 Y O N O N 0 N 0 Y 0 Y 0 Y 0 Y 0 Y 0 Y 0.00294 5

0.01872 5 0.3242 7 0.0571 4 0.04470 5 5.0E-0 6 5.0E-0 6 0.0403 2 0

0.0068 9 0.0278 7 0.15159 5 0.23491 5 0.55722 5 0.0176 1 0.08527 5 0.020 1 0.0402 3 0.03640 5 0.0261 2 0.10279 5 0.1185 9 0.0261 2 0.0261 2 0.0350 4

0.1297 3

1.16744 * 0.1185 9 0.1185 9 0.1185 9 1.1658 8 1.1658 8 Workin g HA P Breathin g

(T/yr ) (Y/N ) (T/yr )

0 Y Y 0.00720 5 Y 0.00621 5 Y 0.17296 5 N 0.007 1 N 0 N 0 N 0.04756 5 N 0 N N N N N N 0.0032 1 Y 0.03760 5 Y 0.04769 5 N 0.2393 1 N 0.40896 5 N 0.00556 5 N 0.0542 2 N 0.04196 5 Y 0.0102 5 N 0.01193 5 N 0.04420 5 Y 0.081 2 Y N 0.08918 5 N 0.03466 5 Y 0.0303 8 Y 0.02184 5 N

Y 0.09314 5 N

Y Y Y 0.1308 2 N 0.1831 1 N 0.2226 7 N 0.1789 2 N 1.0710 6 N 0.825 4 N 0.00294 5

0.1340 3 0.01872 5 0.3242 7

0.0068 9 0.0278 7

0.020 1

0.0261 2 0.10279 5

0.0261 2 0.0261 2

1.7491 4 0.12650 5 0.1070 1 0.18391 5 Workin g

(T/yr ) 0 0.0000 9 0.00720 5 0.00621 5

0*0032 1 0.03760 5

0.04196 5

0.04420 5 0.081 2

0.03466 5 0.0303 8

0.00242 5 0.0018 3 0.0003 7 0.0007 1

Pag e 2 05/12/9 7 c d

### GAT

X Terminal s Corporatio n Tan k Emission s Summar

y• 199 6



# J n k # Typ e Product(s ) (H.I.V ) 22 3 I 22 4 I 22 5 1 22 6 1 22 7 1 22 8 1 30 1 1 30 2 1 30 3 1 30 4 1 30 5 V 42 0 H 44 0 V 45 0 V 45 0 V 45 1 V 46 0 H 47 0 H 47 1 H 48 1 H 48 2 H 48 3 H 48 4 H 48 5 H 48 6 H 48 7 H 48 8 H 48 8 H Ethy l Acetat e

1,1. 1 •Trichloroethan e Ethano l Ethano l Ethano l Ethano l Ethano l Empty Empt y Empt y Aceti c Aci d No
. 2 Fue l Oi l Cyclohexanon e Methylen e Chlorid e Cyclohexan e Neo-Penty l Glyco l Slurr y Gasolin e (RV P 10 ) Distillat e fue l oi l No
. 2 Distillat e fue l oi l No
. 2 Methylen e Chlorid e 1.1. 1 -Trichloroethan e 1.1. 1 -Trichloroethan e Cyclohexan e Moto r Oi l Empty Empty Methylen e Chlorid e No
. 2Fue l Oi l Tan k CapacThrupu t Breathin g Losse s 100 0 gallo n 100 0 gallo n (ib/yr ) 45 8 45 2 45 4 45 4 s 49 4 96 4 105 0 353 2 100 2 383 5 30 1 2 0 3 2 3 0 3 0 3 0 1 2 1 0 2 2 8 2 8 2 8 2 8 2 8 2 8 2 8 2 8 2 8 73 7

5 213 9 167 1 87 6 506 7 0 0 0 0 116 8 20 7 10 5 5 6 2 3 16 0 6 0 2 5 4 0 0 3 8 59 8 0 0 4 6 1 3 662.7 2 1503.3 4 50.4 9 50.4 9 80.7 1 80.7 1 597.9 1

215.1 2 2.6 8 10.2 7 782.3 4 62.7 9 24.0 1 214.2 1 1.3 3 0.2 6 5245. 6 1606.2 8 1576.0 5 679.8 9 1637.9 8

4702.4 5 0.4 3 (T/yr ) 0.331 4 0.751 7 0.025 2 0.025 2 0.040 4 0.040 4 0.29 9 0 0 0 0.107 6 0.001 3 0.005 1 0.391 2 0.031 4 0.01 2 0.107 1 0.000 7 0.000 1 2.622 8 0.803 1 0.78 8 0.339 9 0.81 9 0 0 2.351 2 0.000 2 Workin g Losse s (Ib/yr) 4.1 6 0 10.2 5 8.0 1 4.3 5 24.6 2 0

243.8 6 3.6 2 11.6 1 728.5 8 46.1 2 23.9 5 42.2 7 0 0.0 3 560. 4 0 0 82. 3 3089. 4

501. 9 0.1 9 (T/yr ) 0.00 2 0 0.005 0.00 4 0.00 2 0.01 2 0 0 0 0 0.12 2 0.00 2 0.00 6 0.36 4 0.02 3 0.01 2 0.02 1 0 0.00 0 0.2 8 0 0 0.04 1 1.54 5 0 0 0.25 1 0.00 0 Uncontrolle d Emi s ControEfficiVO C Breathin g (Ib/yr ) 666.8 8 1503.3 4 0.0 0 60.7 4 58.5 0 85.0 6 105.3 3 597.9 1 0.0 0 0.0 0 0.0 0 458.9 8 6.3 0 21.8 8 1510.9 2 108.9 1 47.9 6 256.4 8 1.3 3 0.2 9 5806.0 0 1606.2 8 1576.0 5 762.1 9 4727.3 3 0.0 0 0.0 0 5204.3 5 0.6 2 (T/yr ) 0.333 4 Non e 0.751 7 Non e 0.030 4 Non e 0.029 3 Non e 0.042 5 Non e 0.052 7 Non e 0.299 0 Non e 0.000 0 Non e 0.000 0 Non e 0.000 0 Non e 0.229 5 Non e 0.003 2 Non e 0.010 9 Non e 0.755 5 Non e 0.054 5 Non e 0.024 0 Non e 0.128 2 Non e 0.000 7 Non e 0.000 1 Non e 2.903 0 Non e 0.803 1 Non e 0.788 0 Non e 0.381 1 Non e 2.363 7 Non e 0.000 0 Non e 0.000 0 Non e 2.602 2 Non e 0.000 3 Non e (% ) (Y/N)(T/yr )

0 Y O N 0 Y 0 Y 0 Y O Y O Y O N O N 0 N 0 Y 0 Y 0 Y O N 0 Y 0 Y 0 Y 0 Y O Y 0 N O N O N 0 Y 0 Y O N O Y O N O Y 0.3313 6

0.02524 5 0.02524 5 0.04035 5 0.04035 5 0.29895 5

0.1075 6 0.0013 4 0.00513 5 0.03139 5 0.01200 5 0.10710 5 0.00066 5 0.0001 3

0.33994 5 0.8189 9 0 0.00021 5 10.2 7 Workin g HA P Breathin g (T/yr ) (Y/N ) (T/yr ) 0.0020 8 N

Y 0.00512 5 N 0.00400 5 N 0.00217 5 N 0.0123 1 N 0 N N N N 0.1219 3 N 0.0018 1 N 0.00580 5 N

Y 0.0230 6 N 0.01197 5 N 0.02113 5 N 0 N 0.00001 5 N

Y Y Y 0.0411 5 N 1.54467 5 N

Y 0 N Y 0.00009 5 P k 9.8 1 \ 0.7516 7

0.3911 7

2.622 8 0.8031 4 0.78802 5

0 2.35122 5 11.2 8 Workin g (T/yr ) 0

0.3642 9

0.280 2 0 0

0 0.2509 5 4.9 4



### TNKSUM96.WK

4 Pag e 3 05/12/9 7 cd c

### •GAT

XTerminal s Corporatio

n Fugitiv e Emissions •1996

TAN K PRODNAM E V I N

5 1 B P RUB.SOLV

. T0 NETGALPUMP I TIM E I N S FUGITIV E CO M EMISSIO N FACTOR S ANNUA L VO C VO C Emission s HA P HA P Emission s gp m HOUR S PUMVA L FLA N PUMPSVALV E FLAN G EMISSION S (Y/N ) (Y/N ) (LB/H R (LB/H R (LB/H R (lb/year ) (T/yr ) (lb/year

) (T/yr ) (lb/year) (T/yr) 157. 0 20 0 0.0 1 1 1 8 3 5 0.10 9 0.01 6 0.002 0.00601 8 3.0E-0 6 Y0.00601 8 3.0E-0 6 Y0.00 6 3.0E-0 6



# U 5 2 BPSPARE/MIB K 5 2 BPSPARE/MIB K 5 3 BPISOPROPY L 5 3 BPISOPROPY L 5 4 B P ETHY L AC E 5 4 B P ETHY L AC E 5 5 5 5 5 5 5 6 5 6 5 6 T T T T T T BRUCINE C BRUCINE T BRUCINE T BITRE XC BITREX T BITRE XT 5 7 METHANO L T 5 7 METHANOL T 5 8 5 8 10 4 DO P 10 5 METHY L 10 5 METHY L 10 5 METHY L 10 6 DCP D 10 6 DCP D 10 6 DCP D 10 6 DCP D 10 7 A V GA S 10 7 A V GA S TB A MIX T

TB A MIX T

MET H MET H MET H

12 1 CYCLOHEXAN E 12 1 CYCLOHEXAN E 12 2 ULTR A 9 5 12 2 ULTR A 9 5 12 3 CUMEN E 12 3 CUMEN E 12 3 CUMEN E T



## s T T T c c s T T 

## s c

s T B B s 1 0 0 1 0 1 0 0 1 0 0 1 1 0 0 1 0 1 1 0 0 1 0 1 0 1 1 0 1 0 0 1 1 4025. 0

2248. 0 33903. 0 34779. 0 461. 0 918. 0 16799. 0 21874. 0 348. 0 8923. 0 10106. 0 46. 0 6490. 0 5861. 0 758. 0 7824. 0 113999. 0 1099121. 0 8480. 0 1199309. 0 2294. 0 47867. 0 464555. 0 268872. 0 234533. 0 312904. 0 622343. 0 789919. 0 483544. 0 495483. 0 1972722. 0 463983. 0 2712516. 0 20 0

•20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 175 0 20 0 20 0 20 0 20 0 20 0 175 0 20 0 20 0 175 0 20 0 175 0 20 0 140 0 140 0 175 0 0.3 4

0.1 9 2.8 3 2.9 0 0.0 4 0.0 8 1.4 0 1.8 2 0.0 3 0.7 4 0.8 4 0.0 0 0.5 4 0.4 9 0.0 6 0.6 5 9.5 0 10.4 7 1 0.7 1 1 99.9 4 1 0.1 9 1 3.9 9 1 38.7 1 1 2.5 6 1 19.5 4 1 26.0 8 1 5.9 3 1 65.8 3 2 4.6 1 1 41.2 9 1 23.4 8 1 5.5 2 1 25.8 3 1 1 1 8

1 1 8 1 1 8 1 1 8 1 1 8 1 1 8 1 3 7 1 3 7 1 3 7 1 3 7 1 3 7 1 3 7 1 7 0 7 0 1 7 1 7 2 1 4 2 2 2 3 3 1 4 4 4 1 8 1 4 1 2 4 1 8 1 8 1 8 3 5 3 5 3 5 3 5 3 5 3 5 7 4 7 4 7 4 7 4 7 4 7 4 13 9 13 9 3 5 3 5 1 7 2 4 1 7 1 7 1 7 1 6 1 6 2 4 5 5 2 2 2 6 2 0 1 5 2 4 2 4 2 4 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.01 6

0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6

FUGITV96.WK 1 0.00 2

0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.15429 2

0.08617 3 1.29961 5 1.33319 5 0.01767 2 0.0351 9 1.1678 1 1.52060 8 0.02419 2 0.62029 7 0.70253 5 0.00319 8 0.80000 1 0.72246 6 0.02804 6 0.28948 8 1.63018 6 3.93799 4 0.12126 4 17.1501 2 0.03280 4 0.74114 1 7.1928 6 0.9633 3 3.55708 4 4.74571 1 2.58776 1 32.1760 3 1.55194 6 8.2580 5 10.33 8 2.43149 2 11.371 9 0.00007 7 Y

0.00004 3 Y 0.0006 5 Y 0.00066 7 Y 8.8E-0 6 Y 0.00001 8 Y 0.00058 4 Y 0.0007 6 Y 0.00001 2 Y 0.0003 1 Y 0.00035 1 Y 1.6E-0 6 Y 0.000 4 Y 0.00036 1 Y 0.00001 4 Y 0.00014 5 Y 0.00081 5 Y 0.00196 9 Y 0.00006 1 Y 0.00857 5 Y 0.00001 6 Y 0.00037 1 Y .0.00359 6 Y 0.00048 2 Y 0.00177 9 Y 0.00237 3 Y 0.00129 4 Y 0.01608 8 Y 0.00077 6 Y 0.00412 9 Y 0.00516 9 Y 0.00121 6 Y 0.00568 6 Y 0.15429 2

0.08617 3 1.29961 5 1.33319 5 0.01767 2 0.0351 9 1.1678 1 1.52060 8 0.02419 2 0.62029 7 0.70253 5 0.00319 8 0.80000 1 0.72246 6 0.02804 6 0.28948 8 1.63018 6 3.93799 4 0.12126 4 17.1501 2 0.03280 4 0.74114 1 7.1928 6 0.9633 3 3.55708 4 4.74571 1 2.58776 1 32.1760 3 1.55194 6 8.2580 5 10.33 8 2.43149 2 11.371 9 0.00007 7 Y

0.00004 3 Y 0.0006 5 N 0.00066 7 N 8.8E-0 6 N 0.00001 8 N 0.00058 4 N 0.0007 6 N 0.00001 2 N 0.0003 1 N 0.00035 1 N 1.6E-0 6 N 0.000 4 Y 0.00036 1 Y 0.00001 4 N 0.00014 5 N 0.00081 5 N 0.00196 9 Y 0.00006 1 Y 0.00857 5 Y 0.00001 6 N 0.00037 1 N 0.00359 6 N 0.00048 2 N 0.00177 9 N 0.00237 3 N 0.00129 4 N 0.01608 6 N 0.00077 6 N 0.00412 9 N 0.00516 9 Y 0.00121 6 Y 0.00568 6 Y 0.154 3

0.086 2

0. 8 0.722 5

3.93 8 0.121 3 17.1 5

10.33 8 2.431 5 11.37 2 0.00007 7

0.00004 3

0.000 4 0.00036 1

0.00196 9 0.00006 1 0.00857 5

0.00516 9 0.00121 6 0.00568 6

Pag e 1 05/12/9 7 c d

to

### GAT

XTerminal s Corporation Fugitiv e Emissions •199

6

TAN KPRODNAM E V I N

12 4 CYCLOHEXAN E B 1 12 4 CYCLOHEXAN E s 1 12 4 CYCLOHEXAN E C 1 12 4 CYCLOHEXAN E C 0 12 4 CYCLOHEXAN E T0 12 4 XYLEN E s 0 12 4 XYLEN E T0 12 4 XYLEN E T1 12 5 CUMEN E B 1 12 5 CUMEN E B 0 12 5 CUMEN E s 1 12 6 CYCLOHEXAN E S 1 126 CYCLOHEXAN E C 0 128 OCP O S 1 128 DCP D T0 -4^13 0 WAS H WATE R s 1 13 0 WAS H WATE R T0 13 3 PHENO L B 0 133 PHENO L B 1 13 4 CUMEN E B 0 13 4 CUMEN E s 1 13 4 PHENO L B 0 13 5 CUMEN E B 0 13 5 CUMEN E s 1 135 PHENO L B 1 135 PHENO L B 0 13 5 PHENO L s 0 13 7 2-EH A T0 13 7 2-EH A S 1 14 1 ULTR

A 6 0 T0 14 2 HULS-ISOBUT

. T0 14 3 VINYUETHY; L ACE l 1 14 3 VINYL7ETHY; L ACE T0 NETGALPUMP I TIM E I N SFUGITIV E CO M EMISSIO N FACTOR S ANNUA L gpm HOUR S PUMVA L FLA N PUMPSVALV E FLAN G EMISSION S (LB/H R (LB/H R (LB/H R (lb/year ) (T/yr) VO C VO C Emission s

(Y/N ) (lb/year

) (T/yr ) HA P HA P Emission s (Y/N ) (lb/year

) (T/yr) 667222. 0 4349552. 0 170711. 0 4853505. 0 10488. 0 1485734. 0 6580. 0 25721. 0

564875. 0 709463. 0 57104. 0 184656. 0 963791. 0 967134. 0 293347. 0 347297. 0 314727. 0 789883. 0

543806. 0 1169263. 0 288043. 0 274146. 0 31263. 0 137483. 0 158981. 0

118200. 0 189494. 0 255919. 0 126 0

175 0 20 0 20 0 20 0 124 0 20 0 20 0 1093711. 0 175 0 40913353. 0 140 0 38020168. 0 175 0

175 0 20 0 175 0 20 0 175 0 20 0 70 0 175 0 140 0 175 0 23364. 0 70 0

140 0 175 0 175 0 70 0 70 0 20 0 175 0 6556. 0 20 0

20 0 20 0 20 0 8.8 3

41.4 2 14.2 3 404.4 6 0.8 7 19.9 7 0.5 5 2.1 4 10.4 2 487.0 6 362.1 0 5.3 8 59.1 2 0.5 4 15.3 9 9.1 8 80.5 9 6.9 8 3.3 1 3.7 5 7.5 2 0.5 6 6.4 7 11.1 4 2.7 4 6.5 3 0.7 4 11.4 6 1.51 0.5 5 9.8 5 15.7 9 21.3 3 1 3

1 8 1 3 1 3 1 3 1 3 1 3 1 3 1 5 1 5 1 5 1 2 0 1 2 0 1 2 0 2 0 2 0 1 0 1 0



## I f 1 1 1 1 1 1 1 1 5 1 1 2 2 2 4 2 2 2 2 2 2 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 2 2 0.10 9 2 2 0.10 9 2 2 0.10 9 2 4 0.10 9 2 4 0.10 9 2 4 0.10 9 2 7 1 4 2 7 1 4 2 7 1 4 2 5 2 5 2 6 2 6 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 3.1472 4 18.2349 8 5.07296 2 144.2 3 0.31166 8 7.12113 9 0.19553 6 0.76434 2 4.08527 1 191.026 4 142.014 4 1.88076 5 7.93416 1 0.19012 9 2.0650 7 3.20896 5 10.8157 8 3.3106 3 1.56779 8 1.18322 4 2.37566 7 0.00157 4 Y

0.00911 7 Y 0.00253 6 Y 0.07211 5 Y 0.00015 6 Y 0.00356 1 Y 0.00009 8 Y 0.00038 2 Y 0.00204 3 Y 0.09551 3 Y 0.07100 7 Y 0.0009 4 Y 0.00396 7 Y 0.00009 5 Y 0.00103 3 Y 0.00160 4 Y 0.00540 8 Y 0.00165 5 Y 0.00078 4 Y 0.00059 2 Y 0.00118 8 Y 1 0 2 6 0.10 9 0.01 6 0.00 2 0.17567 5 0.00008 8 Y 2 4 2 4 2 4 2 4 2 4 6 2 4 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 2.12472 8 3.65478 2 0.9003 4 2.14225 5 0.24429 8 2.28909 2 0.49692 9 0.00106 2 Y

0.00182 7 Y 0.0004 5 Y 0.00107 1 Y 0.00012 2 Y 0.00114 5 Y 0.00024 8 Y 1 5 0.10 9 0.01 6 0.00 2 0.09178 4 0.00004 6 Y 1 5 0.10 9 1 5 0.10 9 1 5 0.10 9 0.01 6

0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 1.9 7 3.15823 3 4.26531 7 0.00098 5 Y

0.00157 9 Y 0.00213 3 Y 3.1472 4

18.2349 8 5.07296 2 144.2 3 0.31166 8 0.00157 4 N

0.00911 7 N 0.00253 6 N 0.07211 5 N 0.00015 6 N 7.12113 9 0.00356 1 Y 0.19553 6 0.00009 8 Y 0.76434 2 0.00038 2 Y 4.08527 1 0.00204 3 Y 191.026 4 0.09551 3 Y 142.014 4 0.07100 7 Y 1.88076 5 7.93416 1 0.19012 9 2.0650 7 3.20896 5 10.8157 8 3.3106 3 1.56779 8 1.18322 4 2.37566 7 0.0009 4 N

0.00396 7 N 0.00009 5 N 0.00103 3 N 0.00160 4 N 0.00540 8 N 0.00165 5 Y 0.00078 4 Y 0.00059 2 Y 0.00118 8 Y 0.17567 5 0.00008 8 Y 2.12472 8 3.65478 2 0.9003 4 2.14225 5 0.24429 8 2.28909 2 0.49692 9 0.00106 2 Y

0.00182 7 Y 0.0004 5 Y 0.00107 1 Y 0.00012 2 Y 0.00114 5 N 0.00024 8 N 0.09178 4 0.00004 6 N 1.9 7 3.15823 3 4.26531 7 0.00098 5 N

0.00157 9 Y 0.00213 3 Y 7.121 1 0.00356 1

0.195 5 0.00009 8 0.764 3 0.00038 2 4.085 3 0.00204 3 191.0 3 0.09551 3 142.0 1 0.07100 7

3.310 6 1.567 8 1.183 2 2.375 7 0.00165 5

0.00078 4 0.00059 2 0.00118 8 0.175 7 0.00008 8 2.124 7 3.654 8 0.00106 2

0.00182 7 0.900 3 0.0004 5 2.142 3 0.00107 1 0.244 3 0.00012 2

3.158 2 4.265 3 0.00157 9

0.00213 3

FUGITV96.WK 1 Pag e 2 05/12/9 7 cd c

### GAT

XTerminal s Corporatio n Fugitiv e Emissions •199 6

TAN K PRODNAM E V I N NETGALPUMP I TIM E IN S FUGITIV E CO M EMISSIO N FACTOR S ANNUA L VO C VO C Emission s

14 5 ISOPHO/FURFU R S 1 14 5 ISOPHO/FURFU R T0 14 5 ISOPHO/FURFU R C 1 14 5 ISOPHO/FURFU R C 0 14 7 X-ALCOHO L T0 14 7 X-ALCOHO L S 1 14 8 XYLEN E S 1 14 8 XYLEN E B 0 14 8 XYLEN E T0 14 9 XYLENE/14 9 T0

• ' 15 0 ACI-TC E T0 v^ ' 150 ACI-TC E T1 15 1 CUMEN E T0 15 1 CUMEN E S 1 15 2 BENZEN E B 1 /• w15 2 BENZEN E C 1 ^ 15 2 BENZEN E S 1 15 2 BENZEN E T1 15 2 BENZEN E T0 15 3 SU N SPIRIT S C 1 15 3 SU N SPIRIT S T0 15 4 SPIRIT S 6 6 C 1 15 4 SPIRIT S 6 6 T O 15 5 SLACKWA

XC 0 15 5 SLACKWA

XS 1 15 5 SLACKWA

XT0 15 6 WA X156 C 0 15 6 WA X15 6 S 1 15 6 WA X15 6 T0 15 7 AM S C 1 15 7 AM S C 0 15 7 AM S S 0 15 7 AM S T1 15 7 AM S T0 15 8 PLASTI C 16 0 T O 158 PLASTI C 16 0 T1 418697. 0 318075. 0 40046. 0 60368. 0 889565. 0 948393. 0 gpm HOUR S PU M VA L FLAN PUMPSVALV E FLAN G EMISSION S (Y/N ) (LB/HR(LB/H R(LB/H R(lb/year ) (T/yr ) 4 1 5 0.10 9 0.01 6 0.00 2 0.79751 8 0.00039 9 Y 4 1 5 0.10 9 0.01 6 0.00 2 5.3012 5 0.00265 1 Y 4 1 5 0.10 9 0.01 6 0.00 2 0.66743 3 0.00033 4 Y 4 1 5 0.10 9 0.01 6 0.00 2 1.00613 3 0.00050 3 Y

78961. 0 35412. 0 1589224. 0 2923249. 0 418867. 0 1450341. 0 428029. 0 168385. 0 2669977. 0 3139807. 0 2953280. 0 174552. 0 268487. 0 672969. 0 2645548. 0 1487562. 0 84895. 0 619853. 0 616803. 0 75284. 0 40381. 0 1180020. 0 1150309. 0 113786. 0 38465. 0 39804. 0 175 0

20 0 20 0 20 0 20 0 175 0 1458509. 0 175 0 16422. 0 20 0 556. 0 20 0 722. 0 20 0

20 0 20 0 20 0 175 0 175 0 20 0 175 0 20 0 20 0 20 0 20 0 20 0 20 0 20 0 175 0 20 0 20 0 175 0 20 0 20 0 20 0 124 0 20 0 20 0 20 0 20 0 

### 3.9 9

26.5 1 3.3 4 5.03 74.1 3 9.0 3 13.8 9 1.37 0.0 5 

### 0.0 6 6.5 8 2.9 5 132.44 27.8 4 

### 3.9 9 120.8 6 4.0 8 14.0 3 222.5 0 261.6 5 246.1 1 

### 14.5 5 22.3 7 56.0 8 25.2 0 123.9 6 

### 7.07 5.9 0 51.4 0 6.2 7 3.3 7 15.8 6 95.8 6 9.4 8 3.2 1 3.3 2 4

4 4 1 2 1 2 3 1 2 3 3 4 4 4 4 * » 5 1 1 5 5 1 1 

### 5 5 5 1 1 5 5 1 2 

### 1 2 1 5 1 5

1 5 2 6 95 1 5 95 1 5 1 5 1 5 1 5 1 5 1 5

1 5 1 5 1 8 1 5 1 5 3 0 3 0 0.10 9 0.10 9 0.01 6 0.00 2 0.01 6 0.00 2 1 5 0.10 9 1 5 0.10 9 1 5 0.10 9 0.01 6

0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 14.8260 8 1.806463 2.77811 2 0.273 7 

### 0.009267 0.00741 3 Y

0.000903 Y 0.001389 Y 0.000137 Y 4.6E-0 6 Y 1 5 0.10 9 0.01 6 0.00 2 0.01203 3 6.0E-0 6 Y 1 5 0.10 9 0.01 6 0.00 2 1 5 0.10 9 0.01 6 0.00 2 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9
0.10 9 0.10 9 0.10 9 0.10 9 1 5 0.10 9 1 4 0.10 9 1 5 0.10 9 1 5 0.10 9 1 4 0.10 9 1 5 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 Q.00 2 0.00 2 1.31601 7

0.590 2 26.4870 7 9.68291 4 1.88290 7 22.2385 6 1.92409 2 2.58190 3 40.9396 5 52.3301 2 49.2213 3 2.909 2 4.47478 3 0.00065 8 N

0.00029 5 N 0.01324 4 Y 0.00484 1 Y 0.00094 1 Y 0.01111 9 Y 0.00096 2 Y 0.00129 1 Y 0.0204 7 Y 0,02616 5 Y 0.02461 1 Y 0.00145 5 Y 0.00223 7 Y 12.1134 4 0.00605 7 Y 7.81570 5 0.00390 8 Y 26.7761 2 0.01338 8 Y 1.5281 1 0.00076 4 Y 1.83122 3 0.00091 6 Y 11.1024 5 0.00555 1 Y 1.35511 2 0.72685 8 5.03411 8 20.7055 6 2.04814 8 1.13792 3 1.17753 5 0.00067 8 Y

0.00036 3 Y 0.00251 7 Y 0.01035 3 Y 0.00102 4 Y 0.00056 9 Y 0.00058 9 Y (lb/year

) (T/yr) 0.79751 8 0.00039 9 N 5.3012 5 0.00265 1 N 0.66743 3 0.00033 4 N 1.00613 3 0.00050 3 N

HA P HA P Emission s (Y/N ) (lb/year

) (T/yr )

14.8260 8 1.80646 3 2.77811 2 0.273 7 0.00926 7 0.00741 3 N

0.00090 3 N 0.00138 9 Y 0.00013 7 Y 4.6E-0 6 Y 0.01203 3 6.0E-0 6 Y

Y Y 26.4870 7 9.68291 4 1.88290 7 22.2385 6 1.92409 2 2.58190 3 40.9396 5 52.3301 2 49.2213 3 2.909 2 4.47478 3 12.1134 4 7.81570 5 26.7761 2 1.5281 1 1.83122 3 11.1024 5 1.35511 2 0.72685 8 5.03411 8 20.7055 6 2.04814 8 1.13792 3 1.17753 5 0.01324 4 Y

0.00484 1 Y 0.00094 1 Y 0.01111 9 Y 0.00096 2 Y 0.00129 1 Y 0.0204 7 Y 0.02616 5 N 0.02461 1 N 0.00145 5 N 0.00223 7 N 0.00605 7 N 0.00390 8 N 0.01338 8 N 0.00076 4 N 0.00091 6 N 0.00555 1 N 0.00067 8 N 0.00036 3 N 0.00251 7 N 0.01035 3 N 0.00102 4 N 0.00056 9 N 0.00058 9 N 2.778 1 0.00138 9

0.273 7 0.00013 7 0.009 3 4.6E-0 6 0.01 2 6.0E-0 6 1.31 6 0.590 2 26.48 7 9.682 9 1.882 9 22.23 9 1.924 1 2.581 9 40.9 4 0.00065 8 0.00029 5 0.01324 4 0.00484 1 0.00094 1 0.01111 9 0.00096 2 0.00129 1 0.0204 7

FUGITV96.WK 1 Pag e 3 05/12/9 7 cd c

### GAT

XTerminal s Corporatio n Fugitiv e Emission s •1996

TAN KPRODNAM E

16 4 CUMEN E 16 4 CUMEN E

20 1 FORMI C 20 1 FORMI C 20 1 FORMI C Tc T20 2 PROPIONI C O 20 2 PROPIONI C 20 2 PROPIONI C

20 4 CUMEN E 20 4 CUMEN E 205 MEKO 20 5 MEKO 20 5 MEK O 20 5 MEK O V I

N

S 0 B 0 19 8 SYN

. PHENO L C 0 19 8 SYN

. PHENO L C 1 19 8 SYN

. PHENO L S 0 19 8 SYN

. PHENO L T1 19 9 NEOL/HOECHS TS 1 19 9 NEOL/HOECHS TT0 19 9 NEOL/HOECHS TC 0 19 9 NEOL/HOECHS TT1 20 0 ACETI C ACI D C 0 20 0 ACETI C ACI D S 1 200 ACETI C ACI D T0 C 0 S 1 T0 C 1 S 1 T0 20 3 ACEANHYDRID E C 1 20 3 ACEANHYDRID E S 1 20 3 ACEANHYDRID E T0 B 0 S 1 C C T T NETGALPUMP I TIM E IN S FUGITIV E CO M EMISSIO N FACTOR S ANNUA L

gp m HOUR S PUMVA L FLAN PUMP S VALV E FLAN G EMISSION S (LB/HR(LB/H R(LB/H R(lb/year ) (T/yr ) 1560413. 0 673238. 0 203 0

140 0 4607.0 ^ 20 0 57339. 0 20 0 1212276. 0 70 0 1267705. 0 20 0 425748. 0 175 0 379072. 0 20 0 75693. 0 20 0 4931. 0 20 0 41243. 0 1422478. 0 1341702. 0

187792. 0 106149. 0 297849. 0 450343. 0 144937. 0 656171. 0 18442826. 0 19379816. 0 39177. 0 62788. 0 215208. 0 192938. 0 20 0

175 0 20 0 277176. 0 20 0 1036740. 0 175 0 789327. 0 20 0

20 0 175 0 20 0 20 0 175 0 20 0 140 0 175 0 20 0 20 0 20 0 20 0 12.8 1

8.0 1 0.3 8 4.7 8 28.8 6 105.6 4 4.0 5 31.5 9 6.3 1 0.4 1 3.4 4 13.5 5 111.8 1 23.1 0 9.8 7 65.7 8 15.6 5 1.0 1 24.8 2 37.5 3 1.3 8 54.6 8 219.5 6 184.5 7 3.2 6 5.2 3 17.9 3 16.0 8 1 4

1 4 4 4 7 1 2 1 1 4 4 4 9 1 2 9 9 1 2 9

1 2 9 1 4 1 4 1 8 1 8 1 8 1 8 4 1 4 1 0.10 9 0.10 9 1 5 0.10 9 1 5 0.10 9 1 0 0.10 9 3 3 0.10 9 2 5 0.10 9 1 5 0.10 9 1 5 0.10 9 1 5 0.10 9 1 9 0.10 9 1 9 0.10 9 1 9 0.10 9 19 . 0.10 9 1 9 0.10 9 1 9 0.10 9 9 1 9 0.10 9 1 2 1 9 0.10 9 9 1 9 0.10 9 1 9 0.10 9 1 9 0.10 9 1 9 0.10 9 2 2 2 2 0.10 9 0.10 9 2 3 0.10 9 2 3 0.10 9 2 3 0.10 9 2 3 0.10 9 0.01 6

0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 5.21162 6 3.26039 5 0.07678 3 0.9556 5 6.89842 8 38.0734 1 1.33806 5 6.31786 7 1.2615 5 0.08218 3 0.98708 2 4.54109 2 32.1?1 4 6.63374 6 3.30966 9 18.8912 3 4.49448 9 0.33886 8 7.12851 9 10.7782 1 0.46269 4 15.7043 6 81.8071 1 68.7706 6 1.43126 6 2.29385 5 7.86226 6 7.04866 8 V O C VO C Emission s HA P HA P Emission s

(Y/N ) (Y/N ) (lb/year ) (T/yr ) (lb/year ) (T/yr ) 0.00260 6 Y5.21162 6 0.00260 6 Y5.211 6 0.00260 6 0;0016 3 Y3.26039 5 0.0016 3 Y3.260 4 0.0016 3 0.00003 8 Y 0.00047 8 Y 0.00344 9 Y 0.01903 7 Y 0.00066 9 Y 0.00315 9 Y 0.00063 1 Y 0.00004 1 Y 0.00049 4 Y 0.00227 1 Y 0.01605 6 Y 0.00331 7 Y 0.00165 5 Y 0.00944 6 Y 0.00224 7 Y 0.00016 9 Y 0.00356 4 Y 0.00538 9 Y 0.00023 1 Y 0.00785 2 Y 0.04090 4 Y 0.03438 5 Y 0.00071 6 Y 0.00114 7 Y 0.00393 1 Y 0.00352 4 Y 0.07678 3 0.00003 8 Y

0.9556 5 0.00047 8 Y 6.89842 8 0.00344 9 Y 38.0734 1 0.01903 7 Y 1.33806 5 0.00066 9 N 6.31786 7 0.00315 9 N 1.2615 5 0.00063 1 N 0.08218 3 0.00004 1 N 0.98708 2 4.54109 2 32.111 4 6.63374 6 3.30966 9 18.8912 3 0.00049 4 N

0.00227 1 N 0.01605 6 N 0.00331 7 N 0.00165 5 N 0.00944 6 N 4.49448 9 0.00224 7 N 0.33886 8 0.00016 9 N 7.12851 9 0.00356 4 N 10.7782 1 0.00538 9 N 0.46269 4 0.00023 1 N 15.7043 6 0.00785 2 N 81.8071 1 68.7706 6 1.43126 6 2.29385 5 7.86226 6 7.04866 8 0.04090 4 Y

0.03438 5 Y 0.00071 6 N 0.00114 7 N 0.00393 1 N 0.00352 4 N 0.076 8 0.00003 8

0.955 7 0.00047 8 6.898 4 0.00344 9 38.07 3 0.01903 7

81.80 7 68.77 1 0.04090 4

0.03438 5

206 ODC B 20 6 ODC B 20 6 ODC B 456234. 0 401641. 0 32776. 0 124 0

20 0 20 0 6.1 3 33.4 7 2.7 3 1 1 4 2 1 8 2 1 8 2 9

2 0 2 0 0.10 9 0.10 9 0.10 9 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 2.36211 5 18.1407 9 1.480383 0.00118 1 Y

0.0090 7 Y 0.0007 4 Y 2.36211 5 0.00118 1 N

18.1407 9 0.0090 7 N 1.480383 0.00074 N 207 CUMEN E 207 CUMEN E 207 CUMEN E 207 CUMEN E 20 8 CUMEN E 20 8 CUMEN E S T B S B S 484631. 0

191485. 0 484398. 0 169041. 0 485949. 0 973042. 0 175 0

20 0 140 0 124 0 140 0 175 0 4.6 2

15.9 6 5.7 7 2.2 7 5.7 9 9.2 7 1 4

1 8 1 4 1 4 1 4 1 4 2 9 3 7 2 2 2 9 2 9 2 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.10 9 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.01 6 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 1.77790 3 7.39770 4 2.14865 1 0.87519 6 2.22842 3 3.56967 4 0.00088 9 Y

0.00369 9 Y 0.00107 4 Y 0.00043 8 Y 0.00111 4 Y 0.00178 5 Y 1.77790 3

7.39770 4 2.14865 1 0.87519 6 2.22842 3 3.56967 4 0.00088 9 Y

0.00369 9 Y 0.00107 4 Y 0.00043 8 Y 0.00111 4 Y 0.00178 5 Y 1.777 9

7.397 7 2.148 7 0.875 2 2.228 4 3.569 7 0.00088 9

0.00369 9 0.00107 4 0.00043 8 0.00111 4 0.00178 5

FUGITV96.WK 1 Pag e 4 05/12/9 7 cd c

T lGATXTerminal s Corporatio n Fugitiv e Emission s •199 6 

# ~ l

TAN K

21 C 21 0 21 1 21 1 21 1 21 1 PRODNAM E

NONEN E NONEN E CUMEN E CUMEN E CUMEN E CUMEN E 21 2 CUMEN E 21 2 CUMEN E 21 2 CYCLOHEXAN E 21 2 CYCLOHEXAN E 21 2 CYCLOHEXAN E / 21 3 / 21 3 21 4 21 4 21 4

J 21 5

•21 5 M
. CHLORID E

M
. CHLORID E N- B ACETAT E N- B ACETAT E N- B ACETAT E PETRO-TC E PETRO-TC E V

C T B S S T B T T T C S T S T T S T 21 6 METHYLEN E CHL O S

' 21 6 METHYLEN E CHL O T / 21 6 TC E T 

# V 1 7

21 8 21 8 21 9 21 9 22 0 22 0 22 1 22 1 22 2 22 2 22 3 22 3 ISO-OCTEN E TE XNONEN E TE XNONEN E TE XNONEN E TE XNONEN E TE XNONEN E TE XNONEN E TE XHEPTEN E TE XHEPTEN E TE XHEPTEN E TE XHEPTEN E ETHY L ACETA T ETHY L ACETA T T

S T S T S T S T S T S T I N

1 0 0 0 1 1 0 1 1 0 1
1 0 1 1 0 1 0 1 0 0 1 0 1 0 1 0 1 0 1 0 1 1 0 NETGALPUMP I TIM E I N S FUGITIV E CO M EMISSIO N FACTOR S ANNUA L VO C VO C Emission s HA P HA P Emission s

gp m HOUR S PU M VA L FLA N PUMPSVALV E FLAN G EMISSION S (Y/N ) (Y/N ) (LB/H R (LB/H R (LB/H R (lb/year ) (T/yr ) (lb/year ) (T/yr ) (lb/year ) (T/yr ) 927209. 0 20 0 77.2 7 1 1 8 5 0.10 9 0.01 6 0.00 2 31.3705 7 0.01568 5 Y31.3705 7 0.01568 5 N 721091. 0 20 0 60.0 9 1 1 8 5 0.10 9 0.01 6 0.00 2 24.3969 1 0.01219 8 Y24.3969 1 0.01219 8 N 67901. 0 446054. 0 67916. 0 462285. 0 447087. 0 464674. 0 286175. 0 304235. 0 19308. 0 335633. 0 160478. 0 473166. 0 452. 0 474841. 0 183524. 0 88914. 0 98920. 0 66978. 0 49851. 0 144170. 0 1884754. 0 1903713. 0 2054092. 0 2314985. 0 1573312. 0 1860134. 0 844234. 0 1147061. 0 714892. 0 683968. 0 552666. 0 492945. 0 s 140 0

124 0 175 0 20 0 140 0 20 0 20 0 20 0 20 0 175 0 20 0 175 0 20 0 20 0 175 0 20 0 175 0 20 0 20 0 20 0 124 0 20 0 124 0 20 0 124 0 20 0 124 0 20 0 124 0 20 0 175 0 20 0 0.8 1

6.0 0 0.6 5 38.5 2 5.3 2 38.7 2 23.8 5 25.3 5 1.6 1 3.2 0 15.0 4 4.5 1 0.0 4 39.5 7 1.7 5 7.4 1 0.9 4 5.5 8 4.1 5 12.0 1 25.33 r 158.6 4 27.6 1 192.9 2 21.1 5 155.0 1 11.3 5 95.5 9 9.6 1 73.6 6 5.2 6 41.0 8 1 1 4

1 1 4 1 1 4 1 1 8 1 1 4 1 1 8 1 1 8 1 1 8 1 1 8 1 1 3 1 1 2 1 1 4 1 1 8 1 1 8 1 1 4 1 1 8 1 1 4 2 1 8 2 1 8 1 1 2 1 1 3 2 1 2 1 1 3 1 1 2 1 1 3 1 1 2 1 1 4 2 1 2 1 1 4 1 1 2 1 1 3 1 1 2 2 9

2 9 2 9 3 7 2 9 3 7 3 7 3 7 5 2 3 7 2 9 5 5 2 9 5 2 9 5 5 1 2 2 4 1 2 2 3 1 2 2 4 1 2 2 6 1 2 2 4 1 2 2 3 7 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9
. 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.10 9 0.01 6 0.00 2

0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.00 2 0.31137 5

2.30940 9 0.24915 5 17.8596 1 2.05021 3 17.9519 1 11.0558 9 11.7536 1 0.65325 4 1.14562 7 4.71649 2 1.73584 3 0.01529 3 16.0654 5 0.67327 1 3.00825 7 0.36289 5 2.87447 3 2.13943 9 3.8757 7 9.12484 4 68.4702 1 9.89498 1 62.2345 1 7.61702 9 50.006 6 4.30967 8 41.2559 6 3.61481 7 23.7640 1 1.88643 3 12.882 3 0.00015 6 Y

0.00115 5 Y 0.00012 5 Y 0.0089 3 Y 0.00102 5 Y 0.00897 6 Y 0.00552 8 Y 0.00587 7 Y 0.00032 7 Y 0.00057 3 N 0.00235 8 N 0.00086 8 Y 7.6E-0 6 Y 0.00803 3 Y 0.00033 7 N 0.00150 4 N 0.00018 1 N 0.00143 7 N 0.0010 7 N 0.00193 8 Y 0.00456 2 Y 6.03423 5 Y 0.00494 7 Y 0.03111 7 Y 0.00380 9 Y 0.02500 3 Y 0.00215 5 Y 0.02062 8 Y 0.00180 7 Y 0.01188 2 Y 0.00094 3 Y 0.00644 1 Y 0.31137 5

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FUGITV96.WK 1 Pag e 5 05/12/9 7 cd c

- o C D

### GAT

XTerminal s Corporatio n Fugitiv e Emissions -199 6

TAN KPRODNAM E

v224 TRI-ETHAN E

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FUGITV96.WK 1 Pag e 6 05/12/9 7 cd c

### GAT

XTerminal s Corporation Fugitiv e Emissions •1996

TAN A PRODNAM E



### 48 5 MOTO R OI L 485 MOTO R OI L 485 MOTO R OI L 48 5 MOTO R OI L V I N NETGALPUMP I TIM E I N SFUGITIV E CO M EMISSIO N FACTOR S ANNUA L gp m HOUR S PUMVA L FLA N PUMPSVALV E FLAN G EMISSION S (LB/H R (LB/H R (LB/H R (lb/year ) (T/yr ) 363854. 0 63679. 0 84465.0 - 389696. 0 20 0

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### Y 0.398 8 0.00019 9 Y 0.375 1 0.00018 8 235205.6 1 6867.9 5 2040.29 8 1.020149 2015.89 9 1.00794 9 814.4 2 0.40721 1

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FUGITV96.WK 1 Page 7 05/12/9 7 cd c

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s Facto r Uncontrolle d Emission s Contro l DeviEfficiene y 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 O. S 0. 5 0. 5 O. S TOTALS 0.40999 1

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0.05017 3 Non e 0.30206 1 Non e 0.44275 6 Non e 0.0130 5 Non e 0.07697 8 Non e 0.00346 9 Non e 0.17277 5 Non e 0.00481 5 Non a 0.00613 3 Non a 0.10311 5 Non e 0.01708 4 Non a 0.01052 3 Non e 0.00436 2 Non e O.00S21 9 Non a 0.00085 3 Non e 0.13982 8 Non e 0.00118 7 Non e 0.00175 5 Non e 0.02636 7 Non e 0.00175 1 Non e 13.9711 5 

## (%

) 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Controlled Emission s VO C VO C Emission s HA P HA P Emission s (Ib/yr ) 100.345 8 604.122 8 885.512 7 26.1008 8 153.956 6 6.93788 2 345.549 6 8.63084 9 12.2664 4 206.229 6 34.1671 3 21.0460 5 8.72302 9 10.4382 6 1.70568 3 279.655 5 2.37369 2 3.51030 4 52.7335 4 0 - 3.50238 4 23887.9 2 (T/yr )

0.05017 3 Y 0.30206 1 Y 0.44275 6 Y 0.0130 5 Y 0.07697 8 Y 0.00346 9 Y 0.17277 5 N 0.00481 5 Y 0.00613 3 Y 0.10311 5 N 0.01708 4 N 0.01052 3 N 0.00436 2 Y 0.00521 9 Y 0.00065 3 Y 0.13982 8 N 0.00118 7 Y 0.00175 5 Y 0.02636 7 Y 0.00175 1 Y 11.9439 6 (Ib/yr)

100.345 8 604.122 8 885.512 7 26.1008 8 153.956 8 6.93788 2 9.63084 9 12.2664 4

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0.13982 8 0.00118 7 0.00175 5 0.02636 7 0.00175 1 4.02106 5 HA P T/y r 111/53. 0 thousan d gallon s throughput



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LOADNG96.WK 1 Pag e 3 05/12/9 7 cd c

T lG A U PHILADELPHIA
. P A TERMINA L ^ .Mi.ll.ll l *ll t PLA N