P. 1



# OAR Box 1878 Prepped byCharmelle Matltews



## Document

Number: 

# 130) ll-E-1 4 Docket Number: 

# A-90-1 9

Printed 11/28/20081:21:26

PM Sheet 130of 145. ' * 

# RADIA N

CORPORATIO N P. 2 

# A-90-1 9 ll-E-1 4

Augus t 9 , 199 0

Mr . Le s Evan s Chemica l an d PetroleumBranc h(MD-13 ) U . S . Environmenta l Protectio n Agenc y Researc hTriangl e Park , Nort hCarolin a 2771 1 Dea r Les : \ f*=- : 

# i fU .* ' 

# L DEC 

## I 8 199

2

. . -»J.»J^ ' 

# EPAAI R r*c-. w

Enclose d ar e two (2 ) copie s o f th e meetin g note s documentin g th e Jul y12 , 1990 , EPA/CMAmeeting
. Yo u Augus t 7 , comment s an d suggeste d revision s hav e bee n incorporated
. Pleas e cal l i f w e ca n b e o f furthe r assistance
. Sincerely , Glen n D . Rive s Projec t Directo r GDR:ca o Enclosure s
cc : I P fil e Sectio n 1. 7

Progres s Center/320 0 E . Chape l Hil l Rd./Nelso n Hwy./P.O . Bo x13000/Researc h Triangl e Park , N.C . 27709/(919)541-910 0P. 3

MEETIN G BETWEE NREPRESENTATIVE S O F CM AAN D EPA/OAQP S JUL Y 12 , 199 0 MUTUA L BUILDIN G DURHAM , NORT H CAROLIN A DRAF T MEETIN G NOTE S

Representative s fro mth e Chemica l Manufacturin g Associatio n (CMA ) an d th e Environmenta l Protectio n Agency' s (EPA's ) Offic e o f Ai r Qualit yPlannin g an d Standard s (OAQPS ) met fo r th e purpos e o f discussin g th e Hazardou s Organi c NESHA P (HON ) regulator ydevelopmen t program . Afte r brie f introductions , a n agend a wa s distribute d a s a guid e fo r discussion
. Th e majo r discussio n topic s centere d aroun d th e scop e o f th e HO Neffort , th e technica l approac h bein g use d fo r determinin g MaximumAchievabl e Contro l Technolog y(MACT ) fo r th e HON , dat a needs , an d finall yth e Agency' s sourc e categor yselectio n an d prioritizatio n approac hfo r futur e regulator yefforts . Fou r attachment s ar e include d wit hthes e meetin g notes .
Attachmen t 1 Attachmen t 2 Attachmen t 3 Attachmen t 4 Meetin g Agend a

Attendee s Backgroun d Informatio n fo r th e HO N Informatio n Reques t fo r HO Nsource s
SCOP E O F HON :

Bo b Rosensteel , Chie f o f th e Chemica l Manufacturin g Section , provide d a n overvie wo f th e sourc e coverag e o f th e HO Nregulator y program , emissio n type s t o b e regulate d an d th e contro l technique s tha t ar e candidate s fo r MACT . Mr . Rosenstee l describe d th e affecte d source s a s proces s unit s withi n th e syntheti c organi c chemica l manufacturin g industr y(SOCMI ) tha t eithe r produc e o r us e a s a ra wmateria l o r intermediat e on e o r mor e o f th e HA P compound s liste d i n th e Clea n Ai r Ac t Amendment s (CAA) . Seve n non-SOCM I source s wer e als o describe d a s bein g affecte d byth e HO Nequipmen t lea k an d storag e regulations
. Page s 1- 5 o f Attachmen t 3 contai n th e discussio n points
.

cao.04 6 7-l2mt gP. 4

APPROAC H FORMACT :

Mr . Rosenstee l identifie d th e contro l technique s tha t wer e bein g considere d a s candidate s fo r MAC T (Attachmen t 3 , page s 6-8) , notin g tha t fo r mos t sources , candidat e technique s ar e thos e require d bysimila r Ne wSourc e Performanc e Standard s (NSPS) , o r NESHA P regulations
. Representative s fro mCM Asuggeste d tha t th e Agenc yshoul d conside r produc t recover y(recyclin g t o process ) a s a MAC T candidate
. Commentor s expresse d concer n tha t automati c adoptio n o f combustio n device s a s MAC T woul d no t allo wfo r initiativ e i n produc t recovery , and combustio n ma yno t necessaril yb e th e bes t solutio n fo r al l stream s whe n othe r environmenta l issue s ar e considere d (i.e. , increase d N0 x , S0 X , and C0 2 , etc.) . EP Arepresentative s responde d tha t anyforma t fo r a regulatio n (fo r exampl e a maximu m exhaus t concentratio n o r maximu memissio n rate ) woul d allo w companie s t o us e produc t recover ydevice s t o reduc e emission s belo wth e concentratio n o r emissio n rat e an d therefor e combustio n woul d not b e required
. .
CM Aparticipant s aske d i f EP Aplanne d t o rigorousl yinvestigat e th e technica l feasibilit yo f contro l option s fo r eac ho f th e approximatel y60 0 chemica l proces s types . Commenter s note d tha t som e chemical s and/o r processe s hav e uniqu e characteristic s tha t woul d no t adequatel yb e accounte d fo r i n a generi c MAC T determination
. EP Arepresentative s responde d tha t availabl e technica l dat a ar e bein g use d t o asses s th e feasibilit yo f contro l option s bu t th e analysi s doe s no t involv e a detaile d searc hfo r exceptions
. EP Arepresentative s aske d CM At o provid e informatio n o n specifi c processe s wher e suc hspecia l condition s exists
. Question s wer e raise d regardin g th e possibl e us e o f a tota l resourc e effectivenes s (TRE ) approac hfo r definin g MACT . EP A representative s responde d tha t i t i s no t expecte d tha t suc ha n approac hwil l b e used . Th e typ e o f cut-of f criteri a tha t ar e bein g discusse d an d considere d a t th e EP Astaf f leve l fo r possibl e us e i n determinin g MAC T wer e briefl youtline d (emissio n levels , exhaus t concentration , plan t production , storag e tan k siz e an d vapo r pressure , etc.) . cao.04 6 7-l2mtgP. 5

Mr . Bennet t Kin g fro mRadia n Corporatio n presente d a n overvie wo f th e technica l approac ht o develo p baselin e emissio n estimates , contro l costs , an d emissio n reductio n estimate s fo r th e HO N emissio n sources . Page s 9-1 3 o f Attachmen t 3 contai n th e principa l points
. Representative s fro mCM Aquestione d ho wEP Aplanne d t o accoun t fo r th e site-specifi c cost s associate d wit hcontro l devic e retrofitting
. Discussio n centere d aroun d safet yconcern s (i.e. , locatio n o f a flar e o r combustio n devic e i n relatio n t o proces s unit s o r othe r proces s equipment) , and physica l constraint s tha t ca n ad d significan t retrofi t cost . EP Apointe d ou t tha t flare s an d incinerator s hav e safet yconsideration s incorporate d int o thei r desig n criteri a base d o n NFP Arecommendations , bu t th e Agenc yi s unsur e o f ho wt o incorporat e retrofi t cost s int o cos t algorithm s t o b e use d fo r a broa d categor ylik e SOCM I becaus e o f th e wid e variet yo f retrofi t situations
. EP Arepresentative s welcome d suggestion s an d inpu t fro mCM Ao n approac hfo r determinin g a n appropriat e factor .
Mr . Bo b Ajax , Chie f o f th e Standard s Developmen t Branc hcommente d tha t th e emphasi s o f th e revise d CA Ai s o n applicatio n o f th e best technologie s whic har e no wi n us e t o al l simila r toxi c sources . Whil e cos t effectivenes s i s a consideratio n whe n contro l decision s ar e mad e fo r categorie s o f sources , i t i s no t clea r tha t variatio n i n cos t effectivenes s fro mfacilit yt o facilit y(o r hig hcos t effectivenes s a t individua l facilities ) wil l b e a concern .
Mr . To m

Walto n fro mEPA' s Chemica l Economic s Impact s Sectio n presente d th e Agency' s approac hfo r performin g th e econbmi c impac t analyse s o f th e HO Nregulation
. Page s 14-1 6 o f Attachmen t 3 contai n th e discussio n points
.
DAT ANEEDS :

Mr . Glen n Rive s fro mRadia n Corporatio n discusse d HO Ndat a need s

tha t wer e outline d i n a Jun e 29 , 199 0 lette r t o Ms . Kare n Fiddle r fro mMr . Le s Evan s (Attachmen t 4) . Alistin g o f th e informatio n need s i n orde r o f priorit yi s a s follows : 1 ) productio n capacity , cao.04 6 7-l2mt gP. 6

2 ) marke t price , 3 ) stoichiometry/proces s informatio n 4 ) locatio n o f producer s (stat e an d county) , an d 5 ) identit yo f batc h processes .

• Th e liste d informatio n i s requeste d bymid-August
.

• EP Arepresentative s agree d t o sen d CM Atw o items : 1 ) Th e Spait e chemica l tree s use d i n th e preliminar yidentificatio n o f affecte d chemica l processes , an d 2 ) a n electroni c dat a fil e containin g the 45 0 SOCM I chemica l product s and thei r CA S numbers .
SOURC E CATEGORYSELECTION AN DPRIORITIZATION :

• Mr . Rosenstee l describe d th e approac huse d i n developin g th e sourc e categor yrankin g syste man d reporte d tha t ther e ha s bee n n o ne wlist s o r informatio n release d sinc e las t year' s NAPCTA C meeting
.

• Ther e wa s a genera l discussio n concernin g th e implementatio n o f th e HO Nregulations
. CM Arepresentative s expresse d concer n ove r th e Agency' s plan s t o cove r al l 60 0 SOCM I source s i n singl e regulatio n al l wit hth e sam e complianc e date . Commentor s expresse d concer n abou t vendo r an d engineerin g capacit yt o suppor t suc h broa d needs , a s wel l a s th e possibilit yo f permittin g logjams
. EP Aagree d t o giv e furthe r consideratio n t o thi s point
.

cao.04 6 7-i2mtgP. 7


## ATTACHMEN T1

SUGGESTE DAGEND

A FO R7/12/9 0 MEETIN

GBETWEEN

CM A an dEP A

I . INTRODUCTION S - CM Aand EPA

It . SUMMAR Y O F CMA' S AND EPA' S OBJECTIVE S FO R MEETING - CM

A*n d EPA

III . SOURC E CATEGOR Y SELECTIO NAND PRIORITIZATIO N A . Statu s o f EPA' s activitie s - EPA B . Ke yissue s o f concer n t o CM A- CM A C . Discus s area s wher e CM Aca n contribut e - CM A*nd EPA

IV . MAC T Developmen t fo r Proces s Vents , Transfe r Operations , an d Storag e Tank s A . Statu s o f EPA' s activitie s - EPA B . Ke yissue s o f concer n t o CM A- CM A Proces s vent s

- Transfe r operation s

- Storag e tank s C . Discus s ^rea s wher e CM Aci n cout r irmt< » - CM Aan d EP A V . Wra p Up - CM

Aan d EP A A . Ident j f

ynext , step s B . Summariz e flr.tion item s C . Mak e arrangement s fo r follo wu pATTACHMEN T 2 P. 8

Nam e Bo bRosenstee l Da nAnderso n Ke nEttinge r Nei l Prang e Bria nTarant o Bo bA j a x Susa nWyat t K.C . Hustved t Penn y Lassite r Kare nFidle r A l Weh e Jo e Hoviou s Debbi e Stackhous e Lind a Chapu t Glen nRive s Bennet t Kin g Jo e Woolber t Davi dOcam b Ja nMeye r Chuc kGrigsb y Ti m Mohi n Rand y McDonal d Davi dHeis e Bruc e Wallingto n Richar dSigma n To m Walto n Kath y Baile y Lesli e Evan s Davi dGustafso n Ki m Boudreau x Joh nM . Pierrar d ComDan v 

### EP A Firs t Chem/CM A Chevro nChemica l Monsanto/CM A Exxo nChemica l 

### EP A EP A EP A EP A CM A EP A Unio nCarbid e 

### EP A EP A Radia n Radia n Texa s Eastma nC o Radia n 

### EP A BAS F 

### EP A EP A El i Lill y Merc k 

### CM A EP A CM A EP A DO W Ethy l DuPon t Telephon e Numbe r 919-541

- 601-938

- 415-842

- 314-694

- 713-870

- 919-541

- 919-541

- 919-541

- 919-541

- 202-887

- 919-541

- 203-794

- 919-541

- 919-541

- 919-541

- 919-541

- 214-237

- 919-541

- 919-541

- 201-397

- 919-541

- 919-541

- 317-276

- 201-750

- 202-887

- 919-541

- 202-887

- 919-541

- 517-636

- 504-388 - 302-366 - 560 8

222 7 588 0 574 2 611 7 557 9 567 4 5 3 9 5 5396 ' 117 6 562 3 51 8 3 525 8 535 8 910 0 910 0 547 5 910 0 525 4 280 3 534 9 540 2 395 0 764 8 131 3 531 1 118 6 541 0 295 3 777 6 287 0P. 9 

## ATTACHMEN T3

BACKGROUN DINFORMATION

FO RTH E HAZARDOU S ORGANI C NESHA P (HON )

CM A - EP A MEETING Jul y 12 , 199 0



# f\P.1 0



## PURPOSE : T OPROVID E INFORMATION CONCERNINGTH E SCOP E OF TH E HON , DESCRIB E TH E CONTRO L TECHNIQUE S THA T WIL L BE ANALYZE DFO R REDUCINGEMISSIONS , ANDDESCRIB E TH E ANALYTICAL APPROAC HT O ESTIMAT E NATIONAL IMPACT S OF CANDIDAT E REGULATOR YALTERNATIVE S



# P ^P.1 1



## SCOP E OF HON

• TH E SYNTHETI C ORGANI C CHEMICAL MANUFACTURINGINDUSTRY(SOCMI ) INCLUDE S TH E PRODUCTION O f SOME 600 + HIGHVOLUM E CHEMICAL S

• TH E HO N SCOP E INCLUDE S (1 ) SOCM I PROCESSE S THAT (A ) PRODUC E A HAP O N TH E CAA A LIS T OF 191 , O

R(B ) US E (A S REACTANT ) ON E O RMOR E HAP T O PRODUC E A CHEMICAL , an

d(2 ) STORAG E ANDEQUIPMEN T LEAK S FOR PRODUCTION

OF NEOPRENE , STYRENE-BUTADIEN E RESINS , POLYBUTADIENE , PHARMACEUTICALS , PESTICIDES , CHLORIN E ANDMISCELLANEOU S BUTADIEN E USER S

• ABOU T 45 0 CHEMICAL S HAVE BEEN IDENTIFIE DTHA T FALL WITHI N TH E HO N SCOP E

• T ODAT E WE HAVE IDENTIFIE DA N AVERAG E OF 1. 5 ROUTE S T OPRODUC E EAC H CHEMICAL , EAC HROUT E T OPRODUC E A CHEMICAL I S DEFINE DA S A PRODUC T PROCES S

• THEREFOR E ABOU T 65 0 PRODUC T PROCESSE S MA YULTIMATEL YB E SUBJEC T T OTH E RUL E

• CURREN T SCHEDUL E CALL S FO RPROPOSAL I

N AUGUST , 199 1 ANDPROMULGATION IN AUGUS T 199 2



# ?lP.1 2



## REGULATION S HAVE BEEN

DEVELOPE DFO

R SOCM I ANDOTHE REMISSION SOURCE S

• PROCES S VENT S

AI ROXIDATION

PROCESSE S (NSP S PROMULGATION ) DISTILLATIO N

OPERATION S (NSP S PROMULGATION ) REACTO RPROCESSE S (NSP S PROPOSAL )

• EQUIPMEN T LEAK S (NSP S ANDBENZEN E NESHA P PROMULGATION )

• VOLATIL E ORGANI C LIQUI DSTORAG E (NSP S PROMULGATION )

• BENZEN E NESHA P HA S BEEN DEVELOPE DFO

REMISSION S FRO

M WASTEWATE RANDTRANSFE ROPERATION S

• THES E RULE S ANDDATA FRO M THEI RANALYSE S WIL L B E USE D A S INPUT S FO

REXAMININGIMPACT S O

F REGULATORYALTERNATIVE S FO RTH E HON



# P *P.1 3



## I T I S ANTICIPATE DTHA T TH E HON WIL L REGULAT E THES E EMISSION SOURCE S

PROCES S VENT S EQUIPMEN T LEAK S STORAG E VESSEL S TRANSFE R WASTEWATE R



# P iP.1 4



## CONTRO L TECHNIQUE S THAT AR E CANDIDATE S FO RMACT :

PROCES S VENT S NO N - CHLORINATE DORGANI C VAPORCONTAINING STREAM S - 98 % COMBUSTION
HALOGENATE DORGANI C VAPORCONTAINING STREAM S - 98 % COMBUSTIO N B YINCINERATION

PLU S SCRUBBING
EQUIPMEN T LEAK S RESULT S OF TH E REGULATOR YNEGOTIATION WIL L BE USE D

^P.1 5



## CONTRO L TECHNIQUE S THAT AR E CANDIDATES FO RMACT : (CONTINUED )

STORAG E VESSEL S UNDERGROUNDO

RHORIZONTAL VESSEL S - REFRIGERATE D CONDENSER S NO N CHLORINATE D- FIXE DROO F TANK S WIT HINTERNA L FLOATINGCOVE RHAVINGACCEPTABL E SEAL(S ) CHLORINATE D- REFRIGERATE DCONDENSE R



# fP.1 6



## CONTRO L TECHNIQUE S THAT AR E CANDIDATE S FO RMACT : (CONTINUED )

TRANSFER NONCHLORINATE D- (1 ) REFRIGERATE DCONDENSER , (2 ) 98 % COMBUSTION

DEVIC E CHLORINATE D- (1 ) REFRIGERATE DCONDENSER , (2 ) 98 % INCINERATOR+ SCRUBBING
WASTEWATE R STEA M STRIPPIN

GOF AQUEOU S WAST E STREA M + WATER COOLE DCONDENSE R+ REFRIGERATE DCONDENSE R



# f*P.1 7

INDUSTRIA L PROFIL E SPECIFIC S

PURPOSE S
CHARACTERIZ E INDUSTR Y. . . CHEMICAL S PRODUCED , PROCESSE S USED , MANUFACTURIN G LOCATIONS , EMISSIO N SOURCE S

DEVELO P ASTRUCTUR E TO US E INDUSTR YCHARACTERISTIC S AN D CALCULAT E BASELIN E EMISSIONS , EMISSIO N REDUCTIONS , CONTRO L COSTS AN D OTHE R IMPACT S (FRAMEWOR KDATABAS E SYSTEM )

PROVID E SELECTE D DAT AFO R EVALUATIN G REGULATORYALTERNATIVE S



# r CtP.1 8



## INDUSTRIAL PROFIL E SPECIFIC S (CONTINUED )

FEATURE S
IDENTIFYINGUNIQU E WAY S T OPRODUC E EACHCHEMICAL (PRODUCT-PROCESSES) , HO W MUC HI S PRODUCED , ANDWH O PRODUCE S I T
FO REAC HEMISSION

SOURC E TYPE , ASSIGN

EMISSION

AND CONTROL/COS T MODEL S TOEACHPRODUCT-PROCES S

• MODEL S WIL L CALCULAT E VALUE S FO REAC HPROCES S UNI T USINGPARTICULA

RPRODUCT-PROCES S
OUTPU T FILE S CONTAININGBASELIN E EMISSION S ANDEMISSION REDUCTIONS , CONTRO L COSTS , ANDOTHE RIMPACT S FO REAC H CONTRO L OPTION

(CONTRO L TECHNOLOGY ) AT TH E PROCES S UNI T LEVE L
RESULTS : MAXIMU

M FLEXIBILIT YI

N SELECTINGANDEVALUATIN G REGULATORYALTERNATIVE S



# .p/>P.1 9



## INDUSTRIA L PROFIL E SPECIFIC S (CONTINUED )

METHO D FOR CHARACTERIZIN GINDUSTR Y

• REVIE WO F READIL YAVAILABL E LITERATUR E

• ANALYSI S O F LITERATUR E T O DETERMIN E . . NATIONA L CAPACIT YAN D PRODUCTIO N MARKE T PRIC E INDIVIDUA L PRODUCER S AN D CAPACITIE S UNIQU E COMMERCIA L PRODUCTIO NPROCESSE S (PRODUCT-PROCESSES ) FOR EAC H PRODUCT-PROCES S RELATIO NO F REACTANT S AN D PRODUCT S T O KNOW N PRODUC T CAPACIT Y(KG/K GPRODUCT )



## i°!P.2 0



## INDUSTRIAL PROFIL E SPECIFIC S (CONTINUED )

FRAMEWORKDATABAS E SYSTEM

• INPUT S .. . INDUSTRYCHARACTERISTIC S BASELIN E CONTRO L LEVEL-STAT E REGULATIONS , NESHA P EMISSION MODELS-ALGORITH M

T OCALCULAT E BASELIN E EMISSION S CONTRO L MODELS-ALGORITHM TOCALCULAT E EMISSION S REDUCTION S ANDCOST S FO

RA SPECIFI C CONTRO L OPTION (CONTRO L TECHNOLOGY ) (MODEL S DEVELOPE DB

YFIVE HON

REGULATORYPROJECTS )

• OUTPUT S . . . BASELIN E EMISSION S EMISSION REDUCTION S (FO

REAC HCONTRO L OPTION ) CONTRO L COST S (FO

REAC HCONTRO L OPTION )

/ '
-P.2 1



## INDUSTRIAL PROFIL E SPECIFIC S (CONTINUED )

METHODOLOG Y
INDUSTRYCHARACTERISTIC S I N DATABAS E O

N PRODUCT-PROCES S BASI S
LARGEL YAUTOMATE DPROCES S FO RASSIGNINGEMISSION

AND CONTRO L MODEL S T OPRODUCT-PROCESSE S
COMPLETEL YAUTOMATE DPROCES S FO RCALCULATINGBASELIN E EMISSIONS , EMISSION

REDUCTIONS , ANDCONTRO L COST S ONC E MODEL S AR E ASSIGNE DT OPRODUCT-PROCESSE S
W E WIL L PROJEC T NATIONAL IMPACT S BASE DO N TH E PRODUCT PROCESSE S COMPLETEL YDEFINE DP.2 2



## Th e Rol e o f Economi c Analyse s

0 Economi c analyse s investigat e th e behaviora l respons e t o regulation s

» • Change s i n price , production , employment , marke t structur e
» • Distributio n o f th e cos t o f contro l

O Th e result s o f th e analyse s ar e considere di ndeterminin g th e for man d stringenc yo f th e standar d
> Bot hprivat e an d socia l cost s ar e considere d

• Ar e th e sourcse s t o b e regulate d simila r t o thos e fo r who mth e contro l ha s bee ndemonstrated ?

O Th e result s ar e use dt o determin e i f othe r analyse s ar e neede d

• Regulator yFlexibilit yAnalysi s (smal l busines s concerns )

• Regulator yImpac t Analyse s (majo r regulations )



# rP.2 3



## Challenge s Fo r HO

NEconomi c Analyse s

Breadt h

• Th e HO

Nwil l cove r man

yproduct-processe s

• Our norma l analysi s tha t cover s a t leas t eac hdirectl y regulate d produc t ca n no t b e don e

O Interdependenc e

» • Th e concep t o f chemica l tree s implie s comple x interaction s among regulate d product s
» • Cumulativ e regulator ycost s ar e bot himportan t an d difficul t t o estimat e

O Time

• Preliminar

ycost s wil l no t b e availabl e unti l lat e Octobe r *• Th e preliminar

yeconomi c analysi s i s neede d b ythe middl e o f Januar

y



# Pz.P.2 4 ? 1



## Approac hFo r HO

NEconomi c Analyse s

0 Cumulativ e cos t

• Us e o f chemica l tree s
* Bot haverag e an

d highe r cos t estimate s

O Subse t selectio

nfo r detaile

danalysi s

• Cumulativ e cost s wil l b e use d t o selec t some product s o f bot haverag e an

d highe r contro l cost s
» • Wil l als o includ e the product s fo r whic hpreliminary analysi s wa s initiate d unde r th e ol d effor t

0 Subse t analysi s

*• Marke t analysi s performe d fo r eac hproduc t chose n abov e > Th e result s fo r the whol e se t wil l be use d t o addres s potentia l impac t fo r product s no t selecte d fo r detaile d analysi sP.2 5


## ATTACHMEN T4

Ms.Kare nFicile

r Manage r Ai r Program s 250 1 M Street , N.W . Washington , D.C . 2000 7 Dea r Karen : Th e Environmenta l Protectio nAgenc y i s presentl y

assemblin g informatio n onSOCM I t o suppor t th e new HON NESHA P rulemakin g effort . Fo r some chemica l product s w e hav e no t bee nabl e t o findal l th e informatio nw e woul dlik e t o have . Th e attache denclosur e i s a lis t o f th e chemica l product s fo r whic h informatio ni s required . Th e thre e column s onth e enclosur e indicat e whic h piece s o f informatio nar e neede dfo r eac hchemical . Inorde r t o us e thi s informatio nan

dmaintai nou r planne dschedul e w e woul dlik e thi s informatio n befor e Augus t 10 , 1990 . I f th e informatio ni s receive dafte r thi s dat e it wil l stil l hav e value , bu t it wil l b e mor e difficul t t o incorporate - i nth e work . Th e first , an

dhighes t priority , informatio ntyp e require di s Capacit y information . Specifically :

• Name s o f U.S . producer s • Locatio no f U.S . producer s • Specifi c capacitie s o f eac hU.S . produce r i n198 9 (o r othe r yea r i f available ) • Tota l U.S . productio ncapacit y i n198 9 (o r othe r yea r i f available ) • Tota l U.S . productio na s a percen t o f capacit y Th e secondinformatio ntyp e require di s Productio nProcess . Specifically :
• Proces s descriptio nemphasizin g basi c proces s steps : (i.e. , reaction , separation , produc t recovery , etc. ) fo r eac hcommonl y use d productio nrout e

• Chemica l reactio nequation s identifyin g al l chemical s involve d an dth e weigh t ratio s o f each . Th e thir dinformatio ntyp e require di s th e Marke t Pric e o f eac h chemical , qualifie dwit hcomment s describin g it s conditio na t th e time o f sal e (i.e. , percen t purity , percen t solution , bulk , etc. )P.2 6



### Th e fourt hinformatio ntyp e require di s a nEquipmen t Componen t Coun t fo r a typica l proces s manufacturin g thes e chemicals T 

### xher e component s ar e define d a s valves , pumps , an

dflange s only . Fo r mos t processe s complet e count s wil l no t b e available . I f th e numbe r o f pump s ca nb e approximate dw e ca nestimat e th e othe r components . We woul dappreciat e an y assistanc e th e Chemica l Manufacturin g Associatio nca ngiv e i nhelpin g u s gathe r thi s information . We ca ntal kabou t thi s durin g ou r meetin g her e i nDurham , tentativel y se t fo r th e mornin g o f Jul y 12 . W e wil l confirm

time an ddat e whe nyo uretur nt o you r offic e o n Jul y 2 . Sincerely ,

Lesli e B . Evan s Chemica l Manufacturin g Sectio n Chemical s an

dPetroleum

Branc h Enclosur e
OAQPS:ESD:CPB:CMS:EVANS:thweatt:NCM:MD-13:X5410:6/29/9 0 FIL E NAME : FIDLER.KARE NP.2 7

Chemical s Requirin g Informatio n

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.CA S NUMBE R
12173 3 1.0557 7 7507 0 10789 1 603S S 10384 4 6419 7 10824 7 10201 2 S764 1 7586 5

' 7 505 8 9886 2 7S36 5 10702 8 7906 1 7910 7 10713 1 12404 9 11169 3

- 10718 6 10705 1 10975 1 132111 5 11141 1 12330 8 176295 4 6253 3 14204 1 9004 0 10066 3 11892 3 8465 1 10333 3 10052 7 5521 0 7143 2 9848 6 9811 3 9287 5 13481 6 7693 7 6585 0 11953 9 10047 0 CHEMICA L NAK E

l-Chloro-3-nltrobenzan e Aceta l Acataldehyd a Acataldo 1 Acatantd a Acetanilid e Aceti c aci d Aceti c anhydrid e Acetoacetantlid e Acaton a Acaton a cyanohydH n (CN compound ) Acetonitril e Acetophenon e Acaty l chlorid e Acrolei n Aer y1 wid e Acryli c aci d Acrylonitril e Adlpi c aci d Adipon i tr i la ' Alky l naphthalene s (n o CAS #assigned ) (POM

) Al1y l alcoho l A l 1 y l chlorid e A l 1 y l Cyanid e Aminobenzoi c aci d Am i noethylethanolam i n a Aminopheno l (p-isomer ) Amaontua Thiocyanat e Anilin e Anilin e hydrochlorid e Anisidin a (o-iscaar ) Anlsol e Anthranili c ad d Anthraquinon e (POM

) Azobenzen e Benzaldenyd a Benzaarid e Benzen e (Includin g benzen e frca i gasolina ) Benzanedlsulfoni c aci d Benzeneiulfonl c aci d Benzidin e Benzl l (POM

) Senzlli c ad d (POM

) Benzoi c ad d Benzoi n (POM

) Benzonitril e Capacit y Informatio n Require d
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CA S NUMBE R
11961 9 9807 7 9688 4 14011 4 10051 6 12051 4 10044 7 9687 3 10046 9 9252 4 8005 7 54288 1 1086 1 7525 2 2749751 4 10699 0 11063 4 12386 4 14132 2 7136 3 7892 2 7565 0 9673 7 10973 9 '.395234 6 7564 9 3568 7 10738 0 12372 8 10792 6 10631 0 9648 0 10974 0 10560 2 6325 2 7515 0 55813 4 5623 5 7573 0 900435 7 7587 6 7911 8 53227 4 10642 9 9551 2 10647 8

i Chemical s Requirin g Information Enclosur e 1

CHEMICA L NAM E Benzophenone (POM

) Benzotr i chlorid e Benzoy l chlorid e Benzy l Acetat e Benzy l alcoho l Benzy l benzoat e (POM ) Benzy l chlorid e Benzy l d i chlorid e Benzy l amin e Bipheny l Blspheno l A (POM

) Bls(Chloromethyl)Ethe r BroMobonzono Bromofon a BroMonaphthalen e (POM ) Butadien e (1.3-tsomar ) Butanedlo l (1.4-tsomer ) Butyl , acetat e (n-isomer ) Buty l aerylat e (n-isomer ) Buty l alcoho l (n-isomer ) Buty l alcoho l (s-isomer ) Buty l alcoho l (t-lsomer. ) Buty l benzoi c aci d (p-tert-isomer ) Butylamin e (n-isomer ) Butylaann e (s-isomer ) Butylamin e (t-tsomer ) Buty l benzy l Phthalat e Butylen e glyco l (1.3-isomer ) Butyraldehyd o (n-isomer ) Butyri c ad d Butyri c anhydrid e Butyrolaceton e Butyronitril e Caprolacta * Carbary l Carbo n disulfid e Carbo n tetrabromtd e Carbo n tetrachlorid e Carbo n Tatrafluoria a Calluloa a acetat e Chlora l Chloroaceti c ad d Chloroacetophon a (2-tsower ) Chloroantlln e (•-isomer ) ChloroaniUn e (o-Isomer ) Chloroanlltn o (p-isomer ) Capacit y Informatio n Require d X X X X X X

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CA S NUMBER Chemical s Requiring Information

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CHEMICAL NAME Capacit y Informatio n Require d Productio n

Proces s Informatio n Require d Marke t

Pric e Information Require d Equipmen t

Coun t Information Require d
3591309 8 Chlorobtnzaldahyd e 10890 7 Chl orobanzan e 11891 2 Chlorobanzot c ad d(al l isomers ) 213681 4 Chlorobenzotrichlorid e (al l isomers ) 132103 5 Chlorobenzoy l chlorid e 7545 6 Ch l orodl f luoroethan e 2549729 4 Chlorodlfluoromethan e 6766 3 Chloroform 2558643 0 CMoronaphthalen e (POM ) 8873 3 Chloronitrobenzen e (o-isomer ) 10000 5 Chloronltrobenzan a (p-isomer ) 10843 0 Chloropheno l (m-Isomer ) 9557 8 Chloropheno l (o-isomer ) 10646 9 Chloropheno l (p-Isomer ) 2516780 0 Chlorophenol * 12699 6 Chloropren a (2-Chloro-l.3-8utad1ene ) 779094 5 Chlorosulfont c ad d 10841 8 Chlorotoluen e (m-isomer ) 9549 6 Chlorotoluen e (o-isomer ) 10643 4 Chlorotoluen e (p-isomer ) 7572 9 Chlorotrifluoromethan e 10839 4 Creso l (m-isomer ) 131977 3 Cresol s Cresyli c aci d(mixed ) 9548 7 Cresol s (o-isomer ) 10644 5 Cresol s (p-isomer ) 417030 0 Crotonaldohyo a 372465 0 Crotoni c ad d 8015 9 Cumen e hydroperoxid e 9882 8 Cumen e (isopropy l benzene ) 42004 2 Cyanamid e 37209 8 Cyanoacatl c ad d(C M compound ) 50677 4 Cyanoge nchlorid e (C M compound ) 10880 5 Cyanuri c ad d 10877 0 Cyanuri c chlorid e 11082 7 Cydohexan e 10893 0 Cyclohexano t 10694 1 Cyclohexanon e 11063 6 Cyclohexen e 10691 8 Cyclonexylamin e 11178 4 Cyclooctadian e 155212 1 Cyclooctadian e (1.5-isomer ) 9117 8 Oacahydronaphthalat e 12342 2 0 1 aceton e alcoho l 106721 4 Olally l Isophthalat a 13117 9 Olally l Phthalat e 2757604 1 Olaalnobanzol c ad dP.3 0

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CHEMICA L NAME Capac1t y Informatio n Require d Productio n

Proces s Informatio n Require d Market

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Coun t Informatio n Require d 13709 7 Oiaminopheno l Hydrochlorid e X 74953 Oibromoethan e X 9576 1 Oichloroanllin e (al l Isomers ) X 10646 7 Olchlorobenzen e (1.4-isomer ) (P08 ) 54173 1 Olchlorobenzan e (m-isomer ) X 9550 1 Olchlorobenzen e (o-isomer ) 133147 1 D1chlorobenz1d1n e (3.3-isamer ) X 7571 8 01chlorodlfluoromethan e 107062 0 1 ch l onset nan a (1,2- 1 saner ) (EDC ) 11144 4 Olchloroethy l ethe r(b1s(2-chloroethyl)ether ) X 54059 0 Olchloroethylen e (1.4 - Isomer ) X 9623 1 Oichlorohydrl n X 120832 01chloropheno l (2.4-iscmer ) X 54275 6 Olchloropropen e (1,3-lscmer ) 76023 6 01chloro-I-butan e (3.4-(sonar ) X 461585 Olcyanadlmld e X 101337 01cyclohexylamin e (Ctelohexylamine ) X 111422 01ethanolamin e 91667 Dlethyan1l1n e (Nt»-isomer) X 84662 01 ethy l Phthalat e X 64675 0 1 ethy l sulfat e X 10989 7 01 ethy l amin e X 579668 0 1 ethy l anilin e (2,6-isomer ) X 111466 Oiethylen e glyco l 112732 Oiethylen e Glyco l 0 1 buty l Ethe rX 11236 7 Oiethylen e glyco l diethy l c.rmr (glyco l ether ) 111966 Oiethylen e glyco l dimethy l ethe r(glyco l ether ) 12417 4 Oiethylen e Slyco l Monobuty l Ethe rAcetat e X 12417 7 Oiethylen e glyco l monobuty l ethe racetat e (glyco l ether ) 11234 5 Oiethylen e glyco l monobuty l ethe r(glyco l ether ) 11215 2 Oiethylen e glyco l monoethy l ethe racetat e (glyco l ether ) 111900 Oiethylen e glyco l monoethy l ethe r(glyco l ether ) 11177 3 Oiethylen e glyco l esnemethy l ethe r(glyco l ether ) 75376 Olfluoroethan e 2516770 8 OHsobutylen t 2676140 0 OUsodocy l phthalat e 2755426 3 Dilsoocty l phthalat e 67482 8 01katan a 119937 Dimethy l Benzidin e (3.3-1* . 115106 Olmothy l ethe r•M 6812 2 Dimethy l formamld e (NN-ls a 5714 7 0 1 methy l hydrazin e (1.1-U < 13111 3 01 methy l Phthalat e 7778 1 Olmothy l sulfat e 75183 Olmothy l sulfid e 6768 5 01methy l sulfoxid e •ar ) ir ) (Off )

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CHEMICA L NAM E Capacit y Informatio n Require d Productio n

Proces s Informatio n Require d Marke t

Pric e Informatio n Require d Equipmen t

Coun t Informatio n Require d 12061 6 Dimethy l tarephthalat e 124403 01 methy l amin e 10801 0 0 1 methy l aminoethano l (2-1somer ) 12169 7 Olmothylanilin e - N. N (N, N DiethylanllIne ) 25154545 01nltrobenzene a 99343 Olnitrobenzol c ad d (3,5-tscmer ) 51285 DIMtropheno l (2.*-isomer ) 12114 2 Oinltrotoluen e (2.4-lsomor ) (OUT ) 12391 1 Oioxan e (1.4-0lethyleneoxide ) 64606 0 01oxllan e 10181 5 01 pheny l Methan e 101848 0ipheny l oxid e (POM ) 102089 0 1 pheny l thioure a (POM ) 122394 Olphenylamln e (POM ) 2526571 8 Oi propy l en e glyco l 97392 01-o-to1yguan1d1n e 26675174 Oodecylani11n e 12101 3 Oodecylbenzen e (n-isomer ) 27193866 Oodecylpheno l 106898 Epichlorohydr1n(l-Chloro-2.3-epoxypropane ) 14U3 5 Ethanolamlne a (al l isomers ) 14173 6 Ethy l acetat e 14197 9 Ethy l acetoecetat e 14088 5 Ethy l acrylat e 10041 4 Ethy l benzen e 7500 3 Ethy l chlorid e (Chloroethana ) 10S39 5 Ethy l chloroacetat e 12251 0 Ethy l orthoformet e 9592 1 Ethy l oxalat e 4189271 1 Ethy l sodium oxalacetat e 7504 7 Ethy l amin e 10369 5 Ethy l anilin e (N-Isomer ) 57854 1 Ethy l anilin e (o-Isomer ) 900457 3 Ethy l cellulos e 10556 6 Ethylcyanoacatat e 9649 1 Ethylen e carbonat e 10693 4 Ethylen e dibromid e (Oibromoethane ) (E06 ) 10721 1 Ethylen e glyco l 11155 7 Ethylen e glyco l dlacetat a 629914 1 Ethylen e 61yco 1 0 1 ethy l Ethe r 11071 4 Ethylen e glyco l dimethy l ethe r (glyco l ether ) 11207 2 Ethylen e glyco l monobuty l ethe r acetat e (glyco l ethe r 11176 2 Ethylen e glyco l monobuty l ethe r (glyco l ether ) 1115 9 Ethylen e glyco l monoethy l ethe r acetat e (glyco l ethe r 11060 5 Ethylen e glyco l monoethy l ethe r (glyco l ether ) 11049 6 Ethylen e glyco l moncmethy l ethe r acetat e (glyco l eth e x X X X X 

### x X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X XCA S

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CHEMICA L NAM E Capacit y Informatio n Require d Productio n

Proces s Informatio n Require d Market

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10986 4 Ethylen e glyco l moncmethy l ethe r (glyco l ether ) 12299 6 Ethylen e glyco l monopheny l ethe r (glyco l ether ) 280730 9 Ethylen e glyco l monopropy l ethe r (glyco l ether ) 15156 4 Ethylen e Imin e (Aziridine ) 7521 8 Ethylen e oxid e 10715 3 Ethylenediamin e 10476 7 Ethylhexano l (2-1somer ) 10311 7 Ethylhexy l Acrylat e (2-1somer ) 5000 0 Formaldehyd e 7512 7 Formamld a 6418 6 Formi c ad d 11017 3 Fumari c aci d 11130 8 51utaraldehyd e 5681 5 Glycero l 2654573 7 Glycero l dlchlorohydrl n 2579196 2 Glycero l tr 1 ethe r 5640 6 Glycin e 10722 2 Glyoxa l 11874 1 Hexachlorobenzen e 8768 3 Hexachlorobutadien e 7747 4 Hexachlorocyclopentadien e 6772 1 Hexachloroethan e 59245 0 Hexadien e (1.4-isomer ) 62911 8 Hexemethylen e glyco l 12409 4 Hexamathylenediamin e 10097 0 Hexamathylenetetramin e 10669 4 Haxanetrio l (1.2.6 - Isomer ) 7490 8 Hydroge ncyanid e (C N compound ) 12331 9 Hydroquinon e 9996 7 Hydroxybenzoi c aci d(p-isomer ) 10663 8 Isobuty l Acrylat e 11511 7 Isobutylen e 7859 1 Isophoron e 12191 5 Isophthali c ad d 10821 4 Isopropy l acatat a 7531 0 Isopropylamin e 2516806 3 Isopropylpheno l 46351 4 Keton e

Linea r alky l sulfonat e (n o CAS* - assigned ) 12301 3 Linea r alkylbenzen e (linea r oodecylbenzene ) 11016 7 Ma i al e ad d 10831 6 Malel c anhydrid e 12333 1 Malel c Hydrazld e 691515 7 Mali c ad d 14179 7 Maalty l oxid e 12147 1 Matanlli c ad d 

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Chemical s Requirin g Informatio n

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CA S rtUMBER CHEMICA L NAME 

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7941 4 Mothacryll c ad d 563473 Methally l chlorid e 6756 1 Methano l 63683 Methionin e 79209 Methy l acetat e 105453 Methy l acetoacotat e 9633 3 Methy l Acrylat b 74839 Methy l bromid e (Bromomethane ) 7487 3 Methy l chlorId a (Chloromethane ) 78933 Methy l ethy l keton e (2-8utanone ) 10731 3 Methy l format e 60344 Methy l Hydrazin e 10811 2 Methy l Isobuty l car d n o 1 10610 1 Methy l Isobuty l keton e (Hexone) 62483 9 Methy l tsocyanat e 7493 1 Methy l Mercaptja n 8062 6 Methy l methecrylat a 9885 1 Methy l Phenol.Cardno 1 1634044 Methy l Ter t Buty l Ethe r 74895 Methy l amin e 10061 8 MethylanilIn e (n-isomer ) 10887 2 Methylcyclohexen e 1331222 Methylcyclohexanon e 7509 2 Methylen e chlorid e (Olchloromethane ) 10177 9 Methylen e dlanllin e (4,4-isomer ) (M0A ) 101688 Methylen e d i pheny l dr,sv.:yr-at e (HOI ) 7775 8 Methylpentyno l 9883 9 Methylstyren e (a-isomer ) 11091 8 Morpholln e > 108430 m-Chlorophenb l 99092 m-Nltroanllln e 108383 M-Xylen e j 9120 3 Naphthalen e 85472 Naphthalen e sulfoni c aci d (a-1saner ) (POM ) 120183 Naphthalen e jsulfoni e Mi d (b-lsomer ) (POM ) 9015 3 Naphtho l (a-isomer ) (POM ) 135193 Naphtho l (b-isomer ) (POM ) 75969 Neopmntanol c ad d 9909 2 Nltroanllln o (»-Isomer ) 88744 Nltroanllln o (o-1somer ) 10001 6 Nltroanllln o (p-Isomer ) 9123 6 NUroanlsol a (o-Isomer ) 10017 4 NUroanlsol a (p-isomer ) 9895 3 Nitrobenzen e 2717883 2 NUrobenzol e Mi d (o-.m-.ip - isomers ) 86577 Nitronaphthelen e (1-lsomer ) XX X X X

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CHEMICA L NAME Capacit y Informatio n Require d Productio n

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108027 NUropheno l (4-isomer ) 3875 5 NUropheno l (o-isomer ) (2-Nitrophenol ) 79469 Nltropropen e 1321126 Nltrotoluen e 3872 2 Nltrotoluen e (2-isomer ) 9908 1 Nltrotoluen e (3-1somer ) 9999 0 Nltrotoluen e (4-isomer ) 2515452 3 liony l pheno l 121013 ' n-Oodecylbenzen e 8812 0 N-V1nyl-2-Pyrrol1d1n e 111660 Octane- 1 2719328 8 Octylpheno l 900281 7 Paraformaldehyd e 123637 Paraldehyd e 8786 5 Pentachloropheno l 115775 Pentaerythrlto l 7921 0 Peracetl c Ad d 12718 4 Perchloroethylene(Tetrachloroethylene ) 594423 Perchloromethy l mercapta n 9470 2 Phenetldln e (o-isomer ) 156434 Phenetldln e (p-isomer ) 108952 Pheno l 7709 8 Phenolphthalai n 98679 Pheno l sulfoni c acid s (al l isomers ) 91407 Pheny l anthranili c aci d 95545 Phenylenediamin e (o-isomer ) 106503 Phenylenediamin e (p-isomer ) 10873 6 Phloroglucino l 7544 S Phosgene 38993 Phthall c Aci d 85449 Phthall c anhydrid e 8541 6 Phthalimld e 9115 6 Phthalonltril e 108996 P i co l in e (b-isomer ) 110894 Piperadln e 11085 0 Piperazin e 25322663 Polyethylen e glyco l 25322694 Polypropylen e glyco l 57578 Propiolaeton o ( b Isomer ) 123386 Propionaldehyd e 79094 Propioni c Mi d 7123 6 Propy l alcoho l (n-Isomer ) 54054 5 Propy l chlorid e 107106 Propylamine 78675 Propylen e dichlorid e (1.2-01chloropropane ) 5755 6 Propylen e glyco lP.3 5

Heal s Requirin g Informatio n Enclosur e 1

CA S NUMBE R
10798 2 7556 9 11086 1 9851 1 10651 4 10846 3 2713867 4 6972 7 11120 6 12709 3 53232 1 900432 4 392682 3 14333 9 14153 7 12441 4 13902 6 11044 1 58859 0 10042 5 11015 6 11061 2 12157 3 12633 0 52683 0 10021 0 9806 6 63279 1 63490 2 9594 3 7934 5 11708 8 7800 2 11260 7 10999 9 11964 2 8543 8 7574 1 11060 1 11018 9 10868 3 9560 7 56464 9 2647162 5 133307 9 10415 4 CHEMICA L NAM E

Propylen e Glyco l Moncmethy l Ethe r Propylen e oxid e Pyridin e p-tart-Buty l Toluen e Qu i none Rasorcino l Resorcyli c ad d Salicyli c ad d Sebad c Ad d Sodiu m acetat e Sodiu m banzoat e Sodiu m carboxymethy l cellulos e Sodiu m chloroacatat e Sodiu m Cyanid e Sodiu m format e Sodiu m Methooxlde . Sodiu m phenat e Sorbl c ad d Stllben e Styren e (Viny l Benzene) Succini c aci d Succinonitril e Sulfanlli c aci d Sulfolane ' Tartari c Ad d Terephthall c aci d tart-Buty l benzen e Tatrabromophthall c anhydrid e Tetrachlorobenzen e (1,2.3.5-lscmer ) Tetrachlorobenzen e (1,2.4,5-Isomer ) Tetrachloroathan e (1.1,2.2-isomer ) Tetrachlorophthall c anhydrid e Tetraethy l lea d Tatraethylen e Slyco l Tetrahydrofura n Tetrahydronapthalen e (Tetralln ) (POM ) Tetrahydrophthall c anhydrid e Tetramathy l lea d Tetramethylened i amin e Tetramathylethylenediamin e Toluen e Toluen e 2. 4 diamin e Toluen e 2, 4 dilsocyanat e Toluen e di1socyanate a (mixture ) Tolueneeulfonamid e Tolueneaulfonl c wid a (al l isomers ) Capacit y Informatio n Require d

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CA S NUMBER CHEMICA L NAMC 1 Capacit y Informatio n Require d Productio n

Proces s Informatio n Require d Marke t

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Coun t Informatio n Require d 9859 9 Toluenesulfony l chlorid e 9553 4 Toluidin a (o-isomer ) 634935 Trichloroanllin e (2.4.6-1scmer ) 10282 1 Trichlorobenzen e (1.2.4-isomer ) 71556 Trichloroethan e (1.1.1-tsomer ) . 79005 Trichloroethan e (1.1.2-1somer ) (Viny l Trichloride ) 7901 6 Trichloroethylene 75694 Trichlorofluoromethan e 9595 4 Trichloropheno l (2.4,5- 1 saner ) 7613 1 Tr1chlorotrifluoroethan e (1,2. 2 -1.1. 2 isomer ) 10271 6 Tr i ethano l amine' 121448 Trlethylamln e j 112276 Triethylen e glyco l 112492 Trtethylen e glyco l dimethy l ethe r(glyco l ether ) 11235 6 Triethylen e Glyco l Moncmethy l Ethe r 7756947 Triisobutylen e 75503 Trimethy l amin e 93348 2 Trlmothylcyclohoxano l 2408379 Trimethylcyclohoxanon e 77996 Trimethylopropon e 54084 1 Trimethylpentan b (2.2.4-isomer ) S713 6 Urea 108054 Viny l acetat e 7501 4 Viny l chlorid e (Chlor o Ethylene ) 25013154 Viny l toluen e ' 100403 Vlnylcyclohexen o (4-isomer ) 75354 Vinyliden e chlorid e (1.1-Olchloroethylene ) 2532141 9 Xylen e Sulfoni c Ad d 1330207 Xylene s (mixtures ) 9547 6 Xylene s (o-Isomer ) 106423 Xylene s (p-Isomer ) 130071 6 Xyleno l j 52675 0 Xyleno l (2,3-1somer ) 10567 9 Xyleno l (2.4-isomer ) 95874 Xyleno l (2.5- 1 somer ) 57626 1 Xyleno l (2.6-1somer ) 9565 6 Xyleno l (3.4-Isomer ) 108689 Xyleno l (3,5-Isomer ) 130073 6 Xy1 1 din e !

Note : XIndicate s th a Informatio n I s required .