P. 1 

# OAR Box 1867 Prepped by Ollie Stewart



### Document

Number: 

# 67 ) ll-B-12 1 Docket Number: 

# A-90-1 9

Printed 12/2/20086:27:23 AM

Sheet 67 of 95P. 2



## MEMORANDU M TO : Proces s Vents Docke t A-90-1 9 FROM : WandaFloy

d DATE : Novembe

r 199 1 

# A-90-1 9 ll-B-12 1

\ != 1 

# SJLLli l

„ 

## , . _ __-_

j SUBJECT : HON NESHAP : Industr y Characteristics /

Acetophenone ^ ^» R

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y (PPS ) wa

s no t forme do n thi s particula

r chenjiea l becaus e i

t wa s foun dt o b e aby-product

o f phenol(108952A) . Therefore , referenc e shouldb e mad e to al l section s o

f pheno l excep

t section 2D .

i~RtfFn<7: Sdili i laiiili i 

# f M 

# ico n iranc

e A-90-1 9 x

### ll-B-25 2P. 3 

# f\ Preparer : Date : * /? . i/to Reviewer : ADMINISTRATIV

E NOTE S 

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$ Cod e tftitd

A Hour s spen t o n thi s PP

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' P- P Nam e Incomplet

e Item s (part s o f for m yo u canno tcomplete ) Min e » an

d description ) Dat e Cleare d Initial s 

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Chemical s missin

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v bu t n o Count v (plan t name , city , state )P. 4 

### Preparer : fc/

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## Chej&ita rH« i HtthpU**^

PRODUCT-PROCES S SUMMAR

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# CA M M° i7 

# ~ Kare n Flf W-ClfeiRtca

T Nunfre > MA** CHEMICA L SPECIFI C INFORMATIO N 1. 0 U.S . Productio n Re f # , P

g I , Re

f Yea r 

### (indicat e th e sam e referenc e informatio

n fo r an y answer s belo w fro m a differentreference

) L I Urr^T^rprwfucifef

t(circl e on*) million s o

f k o o r million s o

f gallons 1.2 U , S » Cieacitj i 

## 1. 3 V* s: ' c$*c l t y tm i Natio n I,A $;:$; 1. 7 Produc

tPric e 1.7* 1 Wft$PrM& I.jr* 2 IM%'ji£¥M$HHHH | $/K q q r S/qaHQ n

1.8 Comment

sP. 5

2. 0 Chemica l End-Us e Re f # , P g # ' R e f y e a r 1& 2 Percen t 

## /(]* d^3. 0 U.S . Producer s Re f # . , P g # . , Re f Yea r iPli , 9B£ l million s o f k o o r million s o f gallon s 3. 2 Name , Location , an d Capacit y

Location , Proces s Use d (us e P- P # ) 

# ts ?

Tota l Capacit yP. 7

PRODUCT-PROCES S SPECIFI C INFORMATIO N 4. 0 Potentia l Product-Processe s (P-P ) Re f I , P g I Commerciall y% Nat' l 

## Items. Viabl e (y/n ) capacit y p- p 1 P- P 2 P- P 3 P- P 4 P- P 5 P- P 6 4. 1 Documentatio n o f P-P s Exclude d

P- P no t Commerciall yViabl e Reason s

in t&t$ *P. 8


## gra« nRef # , p g

## # Ai r Oxidatio nReactio n Oxidatio nReactio n Alkylatio nReactio n Carbonylatio nReactio n Halogenatio nReactio n Condensatio nReactio n Dehydrogenatio nReactio n Dehydrohalogenatio nReactio n Esterificatio nReactio n Hydrogenatio nReactio n Hydrohalogenatlo nReactio n Hydroformylatlo nReactio n Hydrolysi s Reactio n Nitratio nReactio n Oxyacetylatio nReactio n Oxyhalogenatlo nReactio n Sulfonatio nReactio n Catalyti c Reformatio n Hydrodimerizatlo nReactio n Generi c Reactio n 4. 4 Explai nhow

yo u selecte d th e reactio ntyp e inlin e 4.3 .P. 9

4. 5 Writte nDescriptio n I nth e lef t margin , indicat e reference s an d pag e number s throughou t writte n description .P.1 0

5. 0 Proces s Flow

Diagram (attac ha t end o f package ) 5. 1 Flow

Diagram Reference : Re f # , P g # 5. 2 Comment s on Flow

Diagram


## M * Prom s Componen t Type s Distillatio nColumn s Absorber s Stripper s Reactor s Condenser s Vaporizer s Other s Re f I . , P g #

: : : x : x^;<404:^:<&«&c<M<tf<35& $P.1 1

6. 0 Chemica l Dat a 6. 1 Balance d Chemica l Reaction s Re f # . , P g #

6. 2 Chemica l Tre e Re f # . , P g #P.1 2

6. 4 Stoichlometr y

Re f # f p g # Show calculation s an

d assumption s an

d the nsummariz e intabl e onnex t page .P.1 3

St<ftfolet ^ 

# um mm ~ 

# "" • * " yxvftWx W :x->x:x*x-x « 6.4. 1 Produc t 6.4. 2 Ra

wMaterial(s ) # 1 # 2 # 3 # 4 # 5 6.4- 3 Co-PrQduct $ # 1 # 2 # 3 # 4 # 5 6.4. 4 Bv-Product s # 1 # 2 ._ # 3 # 5 

### §•4,5 . Intermediate ? # 1 • # 2P.1 4

6. 4 Stoichlometr y

Conversio nFactor s 

# a ) m^m^wrwrmmim c ) Cfeti***!* ! Facto r fo r co-Pt&Juc t t% d ) Conversio n fttUt

fo r Cft-frwfite * 1 3 e ) Conversio n factor"ffl rCe-Fttttfkft Ki f f ) Conversio n Facto rComment sP.1 5



### 7. 0 Proces s Ven t Emissio nSource s *• * JM*SMHP$»& & 

### ***t mtesnnst

(Y/N

) 7*2 WflggffiW

>M»i;«ifssl08S| (Y/N ) Re f I , P

g #

7. 3 Comment

s Re f # , P

g #

7. 4 Reacto r ven t efe1ssfoj*s ? (Y/N ) Re f # , P g # 7. 5 Comment

s Re f I , P g # _P.1 6 

### «r$&fssf<m$ $ •VCSWA-> ^

. • «. A * Ji&sdsZjf. £.?/<<*** 7.8 •""""

" (Y/N ) Re f # . , Pg #
7. 9 Comment

s Re f # . » P g #P.1 7

8. 0 Transfe rEmissio n Source s & - r^JllllP^^« c t $ Transferre d 8. 2 Mha

t fa- H arslransFerred ? Re f # . , P

g # (Y/N )

8.2. 1 Produc

t 8.2. 2 Co-Products

8. 3 Comment

s Re f # . , P

g #P.1 8

9. 0 Storag

e Emissio

n Source s Re f # , P g # 9. * * ArCJH^n * stored ? (Y/N ) 

### 9. 2 What;Mterlal s ar

e stored ? Storage Servic e CA S I Typ

e 9.2. 1 Produc t 9.2. 2 Co-Product s

9.2. 3 Ra w Material s

9.2. 4 Intermediate s
9. 4 Comment s10.0 . Wastewate r Emissio nSource s

10. 2 Describ e wastewate r P.1 9

Re f # . , P g * (Y/N )

Strea m Equipmen t Componen t Numbe r Producin g Wastewate r Comment s o nflow # 1 # 2 # 3 10. 3 Strea

m Compositio n (provid e onl y

i f readil y

available ) Strea m # 1 Re f # Stea m # 2 . , Pg # Organic s Organic s
HAP s HAP s
Wate r Othe r Wate r Othe rStrea

m # 3 Organic s .
HAP s
Wate r Othe r P.2 0

10. 4 Comment s Re f # __ , Pg §