P. 1


# OAR Box 1670 Prepped by Charmelle Mathews



### Document

Number: 

# S" ? ^S 5 ll-D-16 9 Docket Number: 

# A-98-1 3

Printed 9/24/2008 11:55:14

AM Sheet 38 of 56P. 2 

# PAKTAN KCORPORATIO N

Augus t 17 , 199 8 200 0 Wes t Loo p South , Suit e 220 0 Houston , Texas 77027-359 7 (713 ) 623-000 0 FAX : (713 ) 623-448 0 E-Mail : paktank@pakhoedcorp.co m 

# FIL E COP wfpsUfs
Bruc e C
. Jordan , Directo r Emissio n Standard s Divisio n (MD-13 ) Office o f Air Qualit y Plannin g an

dStandard s U.S
. Environmenta

l Protectio n Agency Researc h Triangl e Park , N C 2771 1 Attention : Stephen Shed d RE : Paktan

k Corporatio n - Dee

r Par k Termina l O.L.D
. Surve

y Dea r Mr
. Jordan : Pleas e fin denclose dacomplete dO.L.D
. survey fo r Paktan k Corporatio n - Deer

Par k Terminal
. Shouldyou hav e an

y question s regardin g th e survey , pleas e cal l Thomas Lando r m e a t 713

- 623-0000
. Ver y trul y yours , 

# -fa 6 *»» o , ,^4- , Quirin o Q
. Wong Manager , Environmenta

l Affairs On behalf o f Paktan k Corporatio n - Dee

r Par k Termina l QQW/TDL:rmm

/P. 3



## Bruc e C . Jordan , Directo r Emissio n Standard s Divisio n (MD-13 ) Offic e o f Ai r Qualit

y Plannin g an d Standard s U.S . Environmenta

l Protectio n Agency Research Triangl e Park , N C 271 1 Attention : Stephen Shedd IT . GENERA

L INFORMATION A
. Nam e o f lega l owne r o f plant : Paktan

k Corporation DeerPar

k Termina l B
. I s th e compan

y publicly o

r privately owned ? Privately C
. Nam e o f lega l operator o f th e plant , i f

differen t fro mlega l owner : Sam

e D
. Addres s o f

lega l owner/operator : 275 9 Battleground
. Dee r Par k Texas
. 7753 6 E
. Size o f company/plant : 1
. Approximat

e numbe r o f employee s o

f the busines s enterpris e tha

t own s thi s plant , includin g wher

e applicable , th e paren

t compan y an dal l subsidiaries , branche s and unrelate destablishment s owne dby th e paren

t company : \___ 2. Tota l numbe r o f employee s o

f the busines s enterpris e tha

t operate s thi s plant : 11 2 3
. a ) Numbe r of employee s a

t th e entir e plan t site
. 11 9 b ) Numbe r of employee s associatedwit

h th e organic liqui ddistributio n operation s a t thi s plant : 8 2
c ) Numbe r of organic liquid s distribution operation s employee s tha t ar e contrac t employees._

5 F
. Nam e of plant : Paktan

k Corporation - Dee

r Par k Termina l G
. Stree t addres s of

plant : 275 9 BattlegroundR d City , State , Zip code : Dee

r Par k Texas
. 7753 6 H
. Du n an dBradstreet

number : 19-875-278 4 I
. Latitud e an dLongitude coordinate s of

plant : 29 degrees
. 44 minutes
. 3 0 seconds
. Nort h 97degrees
. 5 minutes
. 3 0 seconds
. East
. 

# Z

_P. 4

J
. Name of

contac t abl e to answe

r technica l question s abou

t th e complet

e survey : Thoma s Lan

d Environmenta

l Specialis t 713-623-000 0 Davi dCarte

r Environmenta

l Superviso

r 281-479-605 1



# 2 >P. 5

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dName (b ) Benzene II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. )
a . Averag e Tru e Vapo r

Pressur e (psia) : 1.5 3 (a)
. 7 0 F b
. Densit y (lb/gal) : 7.36 5 c . Rei dVapor

Pressur e (psia) : 3.22 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 7 8 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : _____ III
. HAP S Constituent s (o f th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Benzene CA S No
. 71-43- 2 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r

Weigh t %

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a )P. 6



### (SURVEYE

D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Ethy l Benzene II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. )
a . Averag e Tru e Vapor

Pressur e (psia) : 0.1 5 @
. 7 0 F b
. Densit y (lb/gal) : 7.25 9 c . Rei dVapor

Pressur e (psia) : (____ d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 106.1 7 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : NA III
. HAP S Constituent s (o f th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Ethylbenzen e

.

'

i CAS No
. 100-41- 4 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



# t>P. 7

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e Co) Ethylene Glycol II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , an dindicat e temperature. ) a . Averag e Tru e Vapo

r Pressur e (psia) : b
. Densit y (lb/gal) : c . Rei dVapor

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : III
. HAP S Constituent s (of th e organi c liqui dliste dabove) : 0.00 8 @
. 7 0 F 9.25 7 0.00 8 6 2 N A

HA P Constituent s (c ) Ethylen e glyco l CA S No
. 107-21- 1 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %

&P. 8

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Meth y Ethyl Ketone II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a . andb. , an

dindicat e temperature. )
a . Averag e Tru e Vapor

Pressur e (psia) : 1.4 6 (g)
. 7 0 F b
. Densit y (lb/gal) : 6.71 2 c . Rei dVapo

r Pressur e (psia) : U
_ d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 2 2 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : NA . III
. HAP S Constituent s (of

th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Methyl ethy l keton e CAS No
. 78-93- 3 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

Weigh t %

^P. 9

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Methyl Alcoho l II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. )
a . Averag e True Vapo

r Pressur e (psia) : 1.9 7 (a)
. 7 0 F b
. Densit y (lb/gal) : 6.6 3 c . Rei dVapo

r Pressur e (psia) : 4. 5 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 32.04 e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : NA
. III
. HAP S Constituent s (of th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Methy l Alcoho l CA S No
. 67-56- 1 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %P.1 0

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dName (b ) MIB E II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. )
a . Averag e Tru e Vapor

Pressur e (psia) : 4.6 3 @
. 7 0 F b
. Densit y (lb/gal) : 6.21 3 c . Rei dVapo

r Pressur e (psia) : 2___ d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : MA e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (o f th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Methy l ter t buty l ethe r CA S No
.

1634-04- 4 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

Weigh t %



# 9P.1 1

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Paraxylene II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. ) a . Averag e Tru e Vapo

r Pressur e (psia) : b
. Densit y (lb/gal) : c . Rei dVapor

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : III
. HAP S Constituent s (o f

th e organi c liqui dlistedabove) : 0.1 3 @ 7 0 F 7.1 7 0.3 4 106.1 7 N A

HA P Constituent s (c ) Paraxylene CA S No
. 106-42- 3 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



## J OP.1 2

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Propylene Oxid

e II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. )
a . Averag e Tru e Vapor

Pressur e (psia) : 9.1 8 (g)
. 7 0 F b
. Densit y (lb/gal) : 6.969 6 c . Rei dVapo

r Pressur e (psia) : 16.6 6 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 58.0 8 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (o f

th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Propylene Oxid

e CA S No
.

75-56- 9 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

Weigh t %

; /P.1 3

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Styrene Monome

r II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. )
a . Averag e Tru e Vapo

r Pressur e (psia) : 0. 1 (g)
. 7 0 F b
. Densit y (lb/gal) : 7.58 7 c . Rei dVapor

Pressur e (psia) : 0.27 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 145.1 4 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (of

th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Styrene Monome

r CA

S No
. 100-42- 5 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



## )?-P.1 4

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Toluene II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a . an db. , an dindicat e temperature. )
a . Averag e True Vapo

r Pressur e (psia) : 0.4 5 (g>
. 7 0 F b
. Densit y (lb/gal) : lf___ c . Rei dVapo

r Pressur e (psia) : 1.2 9 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 92.1 4 e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : H A III
. HAP S Constituent s (of th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Toluen e CAS No
. 108-88- 3 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



# 1 3P.1 5

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Vinyl Acetat

e II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a. andb. , an

dindicat e temperature. )
a . Averag e Tru e Vapo

r Pressur e (psia) : 1.7 3 @, 7 0 F b
. Densit y (lb/gal) : 7.822 c . Rei dVapo

r Pressur e (psia) : 3.97 7 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 86.0 4 e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (of th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Viny l Acetat

e CAS No
.

108-05- 4 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



# 4P.1 6

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Xylene II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. )
a . Averag e Tru e Vapo

r Pressur e (psia) : 0.1 3 @.70 F b
. Densit y (lb/gal) : 7.25 1 c . Rei dVapo

r Pressur e (psia) : 0.2707 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 106.1 7 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (of th e organi c liqui dliste dabove) :
HAP Constituent s (c ) Xylen e CA S No
. 1330-20- 7 Averag e Liqui d

Weigh t % 100 % Averag e Vapo r Weigh t %



## lt>P.1 7

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dName (b ) Aromati c 200 Solven t II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , an dindicat e temperature. ) a . Averag e Tru e Vapo

r Pressur e (psia) : b. Densit y (lb/gal) : c . Rei dVapor

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : III
. HAP S Constituent s (of th e organi c liqui dliste dabove) : 0.134(g)
. 7 0 F 8.20 6 0.234 8 7 0 N A

HA P Constituent s (c ) Naphthalen e CAS No
. 91-20- 3 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

Weigh t %



### l(J>P.1 8

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dName (b) Aromati c 15 0 Solven t II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. ) a . Averag e Tru e Vapor

Pressur e (psia) : b
. Densit y (lb/gal) : c . Rei dVapo r

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : III
. HAP S Constituent s (of

th e organi c liqui dliste dabove) : 0.20 6 @
. 7 0 F 7.4 2 0.5 0 14 2 N A

HA P Constituent s (c ) Naphthalen e CAS No
. 91-20- 3 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

L

_Weigh

t %



## l^hP.1 9

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dName (b ) Stea mCrackedNaphth a II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. ) a . Averag e Tru e Vapo

r Pressur e (psia) : b
. Densit y (lb/gal) : c . Rei dVapor

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : 0.6 8 @
. 7 0 F 7.33 9 2.368 0 11 1 N A III
. HAP S Constituent s (o f th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Benzene Styrene Xylene Toluen e Naphthalen e Ethylbenzen e CAS No
. 71-43- 2 100-42- 5 1330-20- 7 108-88- 3 91-20- 3 100-41- 4 Averag e Liqui d

Weigh t % Averag e Vapor

Weigh t %



# ' 8P.2 0

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b) Hypalon Solven

t II
. Propertie s ( us e th e sam e referenc e temperatur

e fo r a . andb. , andindicat

e temperature. )
a . Averag e Tru e Vapo

r Pressur e (psia) : 1.7 6 (g>
. 7 0 F b
. Densit y (lb/gal) : 13.21 8 c . Rei dVapo

r Pressur e (psia) : 3.937 0 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : 15 4 e . Vapo r Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (o f

th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Carbon Tetrachloride Chlorofor m CA S No
. 56-23- 5 67-66- 3 Averag e Liqui d

Weigh t % Averag e Vapor

Weigh t %



# 1 9P.2 1

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Reformat

e II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . andb. , an

dindicat e temperature. )
a . Averag e Tru e Vapor

Pressur e (psia) : 2.8 5 @
. 7 0 F b. Densit y (lb/gal) : 7.50 6 c . Rei dVapo

r Pressur e (psia) : 4, 5 d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : H I e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : N A III
. HAP S Constituent s (o f

th e organi c liqui dliste dabove) :
HA P Constituent s (c ) Benzene Toluene Xylene CAS No
. 71-43- 2 108-88- 3 1330-20- 7 Averag e Liqui d

Weigh t % Averag e Vapor

Weigh t %



## 2 0P.2 2

TABL E 1 . ORGANI C LIQUID S HANDLE D AN D HAP S CONTENT(a ) (SURVEYE D LIQUIDS ) I
. Organi c Liqui dNam

e (b ) Naphth aReformat

e II
. Propertie s (us e th e sam e referenc e temperatur

e fo r a . an db. , andindicat

e temperature. ) a . Averag e Tru e Vapor

Pressur e (psia) : b
. Densit y (lb/gal) : ' c . Rei dVapor

Pressur e (psia) : d
. Liqui dMolecula

r Weigh t (lb/lb-mo l @ 7 0 F) : e . Vapor Molecula r Weigh t (lb/lb-mo l @ 7 0 F) : III
. HAP S Constituent s (o f th e organi c liqui dliste dabove) : 2.851(g) , 7 0 F 6.8 3 4. 0 7 8 N A

HA P Constituent s (c ) Benzene CAS No
. 71-42- 2 Averag e Liqui d

Weigh t % 100 % Averag e Vapor

Weigh t %



# ZA

# t o 1 " 1 Tan k I D

Cod e (a )
30 3 30 2 40 3 40 4 40 5 40 6 40 7 40 8 50 0 50 1 50 2 50 4 50 6 50 6 51 0 51 1 51 2 51 3 51 4 31 5 52 0 52 5 52 7 53 1 53 8 Tan k Capacit y (gal ) (b )
50400 0 50400 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 336000 0 1260000 1260000 1260000 1260000 1260000 Name(s ) o f Store d Liquid(s ) (c )
Aromati c 10 0 Aromati c 15 0 MTB E MTB E MTB E MTB E MTB E MTB E Methy l Alcoho l Methy l Alcoho l Methy l Alcoho l Benzen e Reformat e MTB E Toluen e Paraxyle n Benzen e Benzen e Benzen e Benzen e Methyl Ethy

l Keton e Toluen e Xylen e Viny l Acetat e Viny l Acetat e TABL E 2 . Annua l Throughpu t (gal/yr ) (d ) 33199 0 33589 5 49080527 4182054 1 3668900 0 4115545 1 3893778 0 3528573 3 1948562 6 504720 2 1534225 9 973765 3 205478 2 205478 2 1656886 0 281383 2 5076966 2 3614218 2 4159823 1 3312437 5 852828 4 1771177 7 1037679 6 341188 5 1076215 1 STORAGE TAN KCONTRO L DAT A Roo f Configuratio n (e )
FX R FX R IF R IF R IF R IFR IFR IFR IFR IF R IF R IF R IFR IF R IF R IF R IF R IFR IF R IF R IFR IFR FX R IFR IF R Floatin g Roo f Tan k Only : Sea l Typ e ffl

VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3

VM 3 VM 3 Tan k Roo f Fitting s (g )

GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N

GPSWSG N GPSWSG N Add-o n Contro l Devic e (h ) N N N N N N N N N N N N N N N N N N N N N N N N N Applicabl e Ai r

Regulation s (i )
k k k k k k k k b k k k k k k k k k k k k k k k k k See endo f tabl e fo r footnotes
.TABL E 2
. STORAG E TAN K CONTRO L DAT A (CONTINUED )



## 0 1 Tan k I D Cod e (a )
60 0 60 1 60 2 60 3 60 6 60 7 60 8 61 2 61 4 61 5 71 9 71 9 72 0 73 6 73 7 77 6 78 4 78 7 79 0 79 1 79 2 81 6 90 8 91 0 91 1 Tan k Capacit y (gal ) (b )
336000 0 3360000 3360000 336000 0 3360000 3360000 336000 0 336000 0 126000 0 126000 0 2310000 2310000 231000 0 126000 0 126000 0 50400 0 126000 0 126000 0 126000 0 231000 0 231000 0 126000 0 126000 0 126000 0 126000 0 Name(s ) o f Store d Liquid(s ) (c )
MTB E MTB E MTB E MTB E MTB E Stea m Cracke d Naphth a Xylen e MTB E Aromati c 15 0 Aromati c 20 0 Reformate(Swee tBenzene ) Xylen e Refonnat e (Swee tBenzene ) Ethy l Benzen e Ethylen e Glyco l Toluen e Styren e Monome r Styrene Monome r Refonnat e (Swee tBenzene ) Styren e Monome r Styren e Monome r Xylen e Methyl Alcoho l Aromati c 15 0 Ethy l Benzen e Annua l Throughpu t (gal/yr ) (d ) 3106423 4 3156506 4 2597338 7 2840828 2 822475 0 1166528 1 1186949 8 44745 2 362928 7 116806 9 334571 7 222253 2 211522 6 99625 0 74110 6 38345 9 1008242 5 506361 3 72825 9 199654 4 2834005 4 227156 1 87740 0 304043 7 269476 1 Roo f Configuratio n (e )
IF R IF R IFR IF R IFR IFR IF R IF R IF R IF R IFR IFR IF R FX R IF R IF R FX R FX R IF R FX R FX R FX R IF R FX R FX R Floatin g Roo f Tan k Only : Sea l Typ e ( 0 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3 VM 3

VM 3 VM 3

VM 3

VM 3 Tan k Roo f Fitting s (g )

GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N GPSWSG N

GPSWSG N GPSWSG N

GPSWSG N

GPSWSG N Add-o n Contro l Devic e (h ) N N N N N N N N N N N N N N N N N N N N N N N N N Applicabl e Ai r

Regulation s (0
k k k k k k k k b k b k b k a k a k a k a k a k a k a k a k a k a k a k b k b k b k b Se e en do f tabl e fo r footnotes
.

# 1 Tan

k I D Cod e (a ) 91 2 913 91 8 92 0 Tan

k Capacit y (gal ) (b ) 126000 0 126000 0 231000 0 231000 0 TABL E 2
. STORAG E TAN K CONTRO L DAT A (CONTINUED ) Name(s ) o f

Store d Liquid(s ) (c ) Ethy l Benzen e Propylen e Oxid e Methy l Ethy l Keton e Methy l Alcoho l Annual

Throughpu t (gal/yr ) (d ) 161313 7 4610635 1 125504 4 1779794 0 Roo f

Configuratio n (e )
FX R IF R IF R IF R Floatin g Roo f

Tan k Only : Sea l Typ e ffl

VM 3 VM 3 VM 3 Tan

k Roo f Fitting s (g )

GPSWSG N GPSWSG N GPSWSG N Add-o n

Contro l Devic e (h ) N N N N Applicabl e Ai r

Regulation s ( 0
k b k b k b k b

- Se e en dof tabl e fo r footnotes
.Organi c Liqui d

Transferre d Throug h Facility (a )

Aromati c 15 0 Aromati c IS O Aromati c 15 0 Aromatic 15 0 Aromati c 15 0 Aromati c 15 0 Aromati c 20 0 Benzene Benzene Benzene Carbo n Tetrachloride Ethy l Benzene Ethy l Benzene Ethy l Benzene Ethy l Benzene Ethylen e Glycol Meth y Ethy l Keton e Meth y Ethy l Keton e Meth y Ethy l Keton e Meth y Ethy l Keton e Melh y Ethy l Keton e Methy l Alcoho l Methy l Alcohol Methy l Alcohol Methy l Alcohol Methy l Alcoho l Methy l Alcoho l Methy l Alcohol MTB E MTB E MTB E MTB E Naphth a Refonnat

e Naphth a Reformat

e Naphth a Reformat

e Naphth a Refonnat

e Paraxylen e Paraxylen e Incomin g Typ e

o f Transpor t Vehic k o r Containe r (b ) RC , BG . TS , T T RC , BO , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC,T T PL , BG , T S PL , BG , T S PL , BG , T S RC,T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , T S RC , BG , T S RC , BG , T S RC , BG , T S BG.T S BG.T S BG.T S BG,T S RC , BG , TS , T T RC , BG , TS , T T Loadin g

Rac k I D Cod e <e )

SD 1 BD 1 SD 2 ST 7 ST2 2 ST1 3 ST 7 BD 1 SD 1 SD 2 ST2 0 ST2 2 BD 5 BD S SD 3 SD 2 SD 2 BD 1 SD 1 ST I ST 4 SD 3 BD 6 BD I SD 1 ST 6 SD 2 ST2 2 SD 1 BD 2 SD 2 ST 9 BD S BD 6 SD 3 BD I SD 1 BD I Loadin g

Ara n I D Cod e (d )

LN2 5 LN2 5 LN2 5 LN 5 LN2 6 LN3 LN 4 LN5 LN 4 LN62 X LN 7 ST22-1 9 LN10 6 LN10 6 LN10 6 LN62 X LN62 X LN3 4 LN3 4 LN 8 LN1 1 LN 1 LN 1 LN 1 LN 1 LN 6 LN62 X LN3 7 LN 7 LN 7 LN 7 LN 2 LN8 4 LN8 4 LN8 4 LN8 4 t_N1 7 LN1 7 Outgoin g

Typ e o f Transpor t Vehicl e o r Containe r

T S B G T S TT,R C T T TT.R C TT.R C B G T S T S T T T T B G B G T S T S T S B G T S T T T C T S B G B G T S T C T S T C T S B G T S T C B G B G T S B G T S B G Annua l Volum e

o f Transferre d Liqui d (gal/yr )

97684 9 76670 4 9024 6 176148 9 348425 5 55871 2 2834 9 7,503,830.0 0 5,437,419.0 0 419,653.0 0 86,970.0 0 9,464.0 0 404,369.0 0 3,251,299.0 0 1,164,175.0 0 738,040.0 0 429,526.0 0 473,549.0 0 6,450,315.0 0 2,720,496.0 0 431,677.0 0 7,637,562.0 0 18,206,646.0 0 6,155,097.0 0 12,104,945.0 0 135,562.0 0 831,399.0 0 9,964,226.0 0 167,494,664.0 0 70,324,249.0 0 100,254,604.0 0 38,515,020.0 0 511363 4 547690 2 222929 9 119008 5 2,725,006.0 0 105,466.0 0 Metho d o f

loadin g o r Unloadin g (« )

BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M Averag e

Loadin g o r Unloadin g Mat e pe r Arm i (gal/min ) 250 0 250 0 250 0 25 0 25 0 25 0 25 0 370 0 370 0 370 0 25 0 25 0 150 0 150 0 1050 0 125 0 1400 0 1050 0 1400 0 25 0 25 0 1400 0 1050 0 1050 0 1400 0 25 0 1400 0 25 0 1400 0 650 0 1400 0 25 0 650 0 650 0 650 0 650 0 1050 0 450 0 Vapio r

Contro l Devic e O D

N N N N N N N VCS 3 VCS 3 VCS 3 VCS 5 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 N N Contro l

Devic e Efficienc y (g )

98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 %Reformat e Refonnat e Stea m Cracke d Naphth a Stea m Cracke d Naphth a Stea m Cracke d Naphth a Styren e Monome

r Styren e Monome

r Styren e Monome

r Styren e Monome

r Toluen e Toluen e Toluen e Toluen e Toluen e Toluen e Toluen e Vinyl Acetat

e Viny l Acetat e Xylen e Xylen e Xylen e Xylen e Xylen e Xylen e Xylen e BG,T S BG,T S BG.T S BG.T S BG,T S BG.T S BG,T S BG.T S BG.T S RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T BG.T S BG.T S RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T RC , BG , TS , T T SD 2 BD I BD 5 BD I SD#3 SD 3 BD 5 BD 6 SD 2 BD I SD 2 BD 5 SD 3 BD 6 SD 1 ST 8 SD 2 SD 1 BD I SD 1 BD 6 SD 2 ST 7 ST I ST 4 LN 4

LN 4 LN3 5 LN3 5 LN3 5 LN7 0 LN7 1 LN7 2 LN6 7 LN4 3 LN1 5 LN11 0 LN11 0 LN11 0 LN4 3 LN 1 LN1 9 LN1 9 LN3 3 LN3 3 LN3 3 LN3 3 LN 4 LN 1 LN 8 T S

B G T S B G T S T S B G B G T S B G T S B G T S B G T S T T T S T S B G T S B G B G TT,R C T T TT.R C 121902 6 83935 0 1018098 3 49445 6 167857 1 61,441,734.0 0 610,049.0 0 423,373.0 0 1,681,688.0 0 6,969,692.0 0 416,514.0 0 1,232,640.0 0 1,274,859.0 0 155,462.0 0 13,947,260.0 0 12,863,203.0 0 9,079,660.0 0 4,711,756.0 0 4,036,771.0 0 10,135,166.0 0 939,350.0 0 2,688,790.0 0 4,830,052.0 0 1,339,106.0 0 790,705.0 0 BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M BT M 650 0

650 0 350 0 350 0 350 0 750 0 320 0 320 0 750 0 1100 0 1400 0 1100 0 1400 0 1100 0 1400 0 25 0 350 0 350 0 350 0 350 0 350 0 350 0 25 0 25 0 25 0 VCS 3

VCS 3 VCS 3 VCS 3 VCS 3 N N N N VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 VCS 3 N N N N N N N 98 %

98 % 98 % 98 % 98 %

98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 % 98 %TABL E 4 . WASTEWATE RFLO W RATE S AN D DRAI N CONTROL S



## C O Sourc e o f OL D Wastewate r (a ) N/ A Tota l Flo w Rat e (gal/yr ) HA P Nam e

(b ) HA P Concentratio n

in Water (ppmw ) (c ) Numbe r o f Drain s wit h Emissio n Suppressio n (d ) Numbe r o f Drain s withou tEmissio n Suppressio n (d )

a)
. OL

D = Organi c Liquid s Distribution
. Selec t th e code s tha

t bes t describ e th e point s o f

wastewater

generatio n (inser

t code s a s require dan d provid e aful

l description) : T C =tan k cleaning s L R=loadin g rack s (identif y th e specifi c rack s usin g th e sam e rack code s a s i n footnot e "a " o f Tabl e 3
. L C = lin e cleaning s L B =liqui dblending/packagin g operation s O T =other , pleas e provide ful l descriptio n (us e extrasheet , if necessary)
. b)
. Lis t

th e principa

l HAP s typicall y present

i n eac h wastewate

r stream . c)
. Estimate dannua

l averag e concentratio n durin g period s o f nomina l flo w i n ppmw . d)
. Emission suppressio n control s reduc e emission s fro mdrain pipe s an

dinclude , but

are no t limite dto , water

sea l pot s an dp-traps .

### TABL E 5 . WASTEWATE R COLLECTIO NAND TREATMENT CONTRO L (a )



# G P OL D Wastewate

r Treatmen t Uni t Tota

l Numbe r o f Unit s on Sit

e (c ) No
. o f

Uncovere d Unit s tha t Ven t to th e Atmospher

e (d ) No
. o f

Covere d Unit s tha t Ven t t o th e Atmospher

e (d ) No
. o f

Unit s tha t Ven t Emission s t o a Contro l Devic e Contro l Devic e (e ) Sourc e of Wastewate

r (b) : No

t Applicabl e Coltetfttat t tfait s Manhole s Junctio n Boxe s Sumps/Catch Basin s Lif t Station s Storag e Tanks ( 0 N/

A N/ A N/ A N/ A N/ A
Treatmen tUnit s Oil/Wate r Separator s Ai r Flotatio n System s Coagulation/Precipitatio n Unit s San dFiltratio n Uni

t Equalizatio n Unit s N/ A N/ A N/ A N/ A N/ A Se e en do f tabl e fo r footnotes
.TABL E 5 . WASTEWATE RCOLLECTIO N AN D TREATMEN T CONTRO L (a ) (Continued )



# - 0 OL D Wastewate r Treatmen t

Uni t Tota l

Numbe r o f Unit s o n Sit e (c ) No
. o f

Uncovere d Unit s tha t Ven t t o th e Atmospher e (d ) No
. o f

Covere d Unit s tha t Ven t t o th e Atmospher e No
. o f Unit s tha t Ven t Emission s t o a Contro l Devic e Contro l Devic e (e )

Sourc e o f Wastewate r

(b) : No t

Applicabl e Treatmen tUnit s Oxidatio n Pond s Activate dSludg e Unit s Tricklin g Filter s Clarifier s Filte r Presse s Stripper s Effluent/Recycl e Pon d Rotatin g Biologica l Contractor s Ship Of f Sit e (g ) N/A N/ A N/A N/ A N/ A N/A N/A N/ A 0

Se e en dof tabl e fo r footnotes
.

l o 1 °TABL E 6 . SEMI-AQUEOU S WAST E COLLECTIO N AN D CONTRO L (a )

« Typ e o f

Wast e (b )
Not Applicabl e Wast

e Generatio n Rat e (tons/year) Wast

e Collecte di

n aClosedSystem ? (Yes/No ) (d ) Methodo f

On-Sit e Storag e (e ) Wast

e Treate do r Dispose do f

On

Site ? (Yes/No ) ( 0 Metho do f

On-Site Treatment o r Disposa l (g ) Contro l Devic e on

Treatment o r Disposa l Uni t (h )

See en do f tabl e fo r footnotes
.

C OP.3 2



# TABL E 7 . EQUIPMEN

T LEA K CONTRO L DAT

A 1
. I s there aformal , periodi c lea k detectio n an

drepai r (LDAR ) program ? Ye s X N o Comments : Benzene monitoring i s done on amonthl y bases
. 2
. Pleas e indicat

e which Federal/State/loca

l rule s requir

e a n LDA Rprogra ma t thi s facility : a l 4 0 CF R6 1 Subpar

t V b)
. 3
. I f aforma l equipmen

t LDA Rprogra mha s bee n implemente

da t you r plant , provide th e followin g information : Definitio n o f Leak a Lea k Detectio n Method b Lea k Respons e Time c A A Begi n 5 days , Complet

e 1 5 day s



# ~z>\Equipment

Component
Valve s Compressors Flange s Pump s Inspectio n

Frequenc y (a ) Q Q Q Q Tota l

Equipmen t Coun t 725 9 0 1459 3 15 7 Equipmen t

Counti n LDA R Progra m 725 9 0 1459 3 15 7 Equipmen t

Counti n LDA Rwit h HA P Servic e 183 5 0 369 4 1 1 Equopmne tcount s

wit h Mechanica l Contro l Device s (b ) 0 0 0 0 Equipmen tCount s wit h a

Close d Ven tSyste m (c ) 4 4 0 9 7 0 Close d Ven t

Syste m Contro l Devic e (d ) VCS 3 VCS 3

* Carbon Tetrachlorid e (Hypalo n Solvent ) close d systemcontro l devic e = VCS 5



# w yP.3 4

1 2 TABL E 8 . COMPOUNDING/BLENDING/PACKAGIN G OPERATION S Part L N/

A
Produc tNam e (a ) No tApplicabl e Chemica l Compositio n (b ) Annua

l Quantit y Produced (gal ) (c ) Doe s a chemica l reaction tak

e place ? Applicabl e

Regulation s

a)
. b)
. c)
. d)
. e)
. Provid

e th e produc t

name s resultin g fro

mblending , compounding , an dpackaging operations
. Name s mus t

match thos e providedi

n Tabl e 1
. Fo

r familie s o f

blends , includ

e only th e family nam e liste di n Tabl e 1
. Provid e the name s o f

th e ra w material s (mus t

match Table 1 ) tha

t ar e use dt o blend/compoun d th e product
. Provid e the annua

l quantitie s o f

th e product s produced
. Specif y whethe r achemica l reactio n take s plac e durin g th e compoundin g or blendin g o f organi c liquid s (i.e. , yes-compounding , no-blending , etc.)
. Pleas e identif

y an y regulation s (pertainin g t o ai r emissions ) tha

t appl y t o th e compounding/blending operation
. Parin , Th e question s belo w ar

e facility-wide , an

dd o not needt o b e answeredo

n aproduct-by-product

basis
. Pleas e answe

r th e following question s wit h a s muc h detai l a s possible
. Inser

t sheets as necessary . 1
. Provid

e adescriptio n of

the principa

l methods/mechanism s use

dfo r blending/compounding
. 2
. Provid

e adetaile ddescriptio n of

an y mechanism s o f

vapo r balancing o

r othe r vapor emissio n contro l utilize dfo

r thes e processe s (e.g. , submergedfill)
.



# 3 5P.3 5



### TABL E 9 . AI RPOLLUTIO N CONTROL EQUIPMEN T PARAMETER S
Contro l Device : Flar

e (b ) Identifie r Cod e (d): Lan dFlar e 60 0 Type : no assist : stea massist : ai r assist : X pressur e assist : Location : groun d:_ X elevated : Hea t conten t o f vente dstream , Btu/scf

: 40 1 avg . Flar e ga s exi t velocity , ft/s: 19. 4 Flar e tip diameter , in
. 24.7 3 in 2 Flar e height , ft: 5 0 Supplementar

y fue l for : Pilot , scfm: 5 4 Combustion purposes , scf

m22 8 Stea mrequirements , lb/hr : N/

A Emission Source s (c ) 1
. Tan k Truc k Loading 2
. Railca r Loading



# 34 -P.3 6



### TABLE 9 . AI

RPOLLUTIO N CONTROL EQUIPMEN T PARAMETER S
Contro l Device : Flar

e (b ) Identifie r Cod e (d): Lan dFlar e 890 0 Type : n o assist : stea massist : ai r assist : X pressur e assist : Location : ground : _X elevated : Hea t conten t of ventedstream , Btu/scf

: 40 1 avg . Flar e ga s exi t velocity , ft/s: 39. 2 Flar e tip diameter , in. : 13.74 in 2 Flar e height , ft: 5 0 Supplementar

y fue l for : Pilot , scfm: 5 4 Combustion purposes , scfm : 400 Stea mrequirements , lb/hr : N/

A Emission Source s (c ) 1
. Tan k Truck Loading 2
. Railca r Loading



# 2 ^P.3 7



### TABLE 9 . AIRPOLLUTION CONTROL EQUIPMENT PARAMETERS

Contro l Device : Flar

e (b ) Identifie r Code (d) : Marine Flar

e Type : no assist : stea massist : ai r assist : X pressur e assist : Location : ground: X elevated : Hea t conten t o f ventedstream , Btu/scf

: 60 1 avg . Flar e ga s exi t velocity , ft/s: 13 4 Flar e ti p diameter , in
. 39.4 1 in 2 Flar e hight , ft: 6 0 Supplementar

y fue l for : Pilot , scfm : 120

0 Combustion purposes , scf

m170 3 Stea mrequirements , lb/hr : N/

A Emissio n Source s (c ) 1
. Tanke r Shi p Loading 2
. Barg e Loading



# ^U>P.3 8



### TABL E 9 . AI RPOLLUTION CONTROL EQUIPMEN T PARAMETERS

Contro l Device : Flar

e (b ) Identifie r Code (d): Vapo

r Condense r Typ e of condenser : surface : X contact : Ga s inle t temperature , F 8 0 Ga s outlet temperature , F 3 2 Emission Source s (c ) 1
. Tan k Truck Loadin g 2
. Railca r Loading



# irrvP.3 9



### TABLE 9 . AI RPOLLUTION CONTROL EQUIPMENT PARAMETERS

Contro l Device : Flar

e (b ) Identifie r Cod e (d) : CA S Typ e o f carbo n bedan

dnumber : regenerative : non-regenerative : X
_ fixed: X fluidized : Ho w man y pound s o f

carbon pe r bed : 3001bs parallel : Serial : X Numbe r o f bed s on-line : 2 Numbe r o f bed s desorbing : N/

A Pressur e drop
. in
. H 2 0 : 2 inche s Ga s inle t temperature , F 6 0 avg Typ e o f regeneration : N/

A Regeneratio n time : N/

A Adsorptio n Time : N A Emission Source s (c ) 1
. Tan k Truc k Loading 2
. Railca r LoadingP.4 0

ATTACHMEN

T "A " SECTIO N II I - PLO T PLA N



## 2> ^P.4 1



### Docke t No
. A-98-1 3 Subcategor

y II- D

Th e enclosure s for thi s document, which ar e noteasily photocopied , (plo tplans , maps , etc. ) are located i n th e WCP G files a tEPA:ESD:WCPG , RTP , NC , Mutua l Building .



# 4- 0P.4 2

ATTACHMEN

T "B " SECTION I H - PLANT OPERATIONS Paktan k Corporatio n - Dee

r Par k Termina l i s a"For-Hire " bulk

liqui dstorag e termina

l (oil/chemica

l storag e an

dhandling SIC 4226)
. The facility' s operation s consis t of 23 6 storag e tank s rangin g i n siz e from100 0 barrel s t o 80,00 0 barrel s in capacity
. The terminal operate s a tota l o f 2 2 tank-truc k

andtank-ca

r loadin g station s alon g wit h thre e shi p dock s andeight

barg e docks
. Produc t

transfer s are conducte dfromtank truck , tan

k car , o r marin e vessel s int

o and out o f th e bul k liqui dstorag e tanks
. There are n o blendin g o r packagin g operation s a

t thi s terminal
. Th e termina

l operate s twenty-fou

r hour s aday , seve

n day s aweek
. Th e following categorie s o f

organi c liquid s wer

e store ddurin g th e surveye dyear : Alcohol s Parafin s Aromatic s Lubricant s Solvent s

Glycol s Olefin s Naphtha s

Naphthalen e Cyclo-olefin s Ether s

Ester s Ketone s Refinedpetroleu m

Oxygenate s Acetate s The HAP s consis t

o f 42 % o f th e tota l product s shippedfromth e terminal
. Th e HAP emission s generate dare estimate dto b e 114. 7 ton s pe r yea r which represent s 100 % of th e HAP emissions
.



# 4- 1