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# OAR Box 1384 Prepped by Charmelle Mathews



### Document

Number: 

# 69 ) ll-E-2 9 Docket Number: 

# A-94-5 2

Printed 7/2/20088:42:05 AM

Sheet 69of 264P. 2 M W22-QS1\E 9:1 0 CRAN E CO RTE C FA

X NO . 335217 1

CO R TE C COMPAN Y P . 0 1 A-94-5 2

TCLEPHONe - (81<) 33S-S40 0 FAX-(81<)33Wa4 a 

# CO R TE C

23S 1 KENSKIL L WASHINGTO N COUR T HOUSE , O H 4316 0

FACSIHIL E COVE

R SHEE T

DATEs At**"*- J J. /9?S TIHE : # O P PAGES : 

# JL

TO * AfA!>e/£/rA//? OT/IUr+i



## 9/9- 5TW- oejX

ATTH s

FROM : 

# Joe rfc KJPJS.

OU R FA X MUHBE R IS- ! 614/335-217 1 I F YO UEXPERIEH E PROBLEH S WIT H THI S TRAHSHISSIOM , O R D O HO T RECEIV

E TH E COMPLET E TRAHSHISSIOH , PLEAS E CALL t

614/335-2984 .

FA X SEH T BY

J (INITIALS )P. 3 

### f - '0-^9 5 TU E 9:1 0 CRAN E CO RTE C FA

XNO . 335217 1 P . 0 2



## CO R TE C

CO R TE C COMPAN Y 23S 1 KENSKIL L TELEPHON E - (6U) 33&S4O 0 FA X

_(814

) aas-49 «

WASHINGTO N COUR T HOUSE , O H 4316 0

To : Madelein e Stru m U.S . Environmenta l Protectio n Agenc y Fax : 919-541-007 2 From : Jo e Prior , Jo e Smart , Mar k Smit h Corte c Co . W e hav e reviewe d th e draf tContac tRepor tfrom ou r Augus t8,199 S conferenc e telephon e cal l an

d sugges tth e revision s note d i n th e attached . Pleas e call i f

yo u need furthe

r information .



# zEA . FA X NO . 335217 1 P . 0 3 '.AUG-22-9 5 TU

E 9:1 1 CRAN

E CO RTE C

CONTAC T REPOR T From : Wank a Dunston , U S Environmenta l Protectio n Agenc y

Madelein e Stnim,U 5 Environmenta l Protectio n Agenc y A 4') pal e o f Contact : Augus t8,199 5 Contacts : Jo e Prior , Presiden t Jo e Smar t Mar k Smit h Company/Agency : Cran e Cor te c Compan

y Tdephon e Numbe n (018)44 3 609 1 (fel ^ 335-lJ f 0 0
CONTAC T SUMMARY Note s prepare

d by Wanit

a Dunston .

• Process : Resi n i s pumpe d i n a batc h proces s int o dispensin g troughs . Th e trough s hol d th e catalyze d resin . I ti s poure d int o th e laminatin g area . Movin g cart s (wit h hole s o n th e sid e fo rdispensin g resin ) ar e use d t o dispens e resi n an d t o pou ri tont o tb e pane l Tha t pourin g i s no tcontrolle d becaus e I) th e resi n i s no temittin g a significan tamoun to f styren e an d 2 ) panel s ar e o n th e orde ro f 60 ' x I T an d th o amoun to f ai rrequire d t o
• —calculat e th o ooptur o efficienc y ea a no tb e determined . AhlfrJ T U}0iJi* b B-f c ( 1MJW.UCA L "f a CONTROL . A M0V/A/ & ,M/*/0fcScv£C-£ . • Wit h gelcoat , Co rte e ca n eontro l th e process ; bu twit h lamination , ther e i s a grea tdea l o f movement , and

ther e i s n o wa y t o fix collectio n points ; i e t o attac h hoods , etc . t o captur e th e emissions . Vacuu m ba g emission s ar e minimal . O n a pound-to-poun d basis , emission s ar e low .

• I n 1990 , Emissio n tes treport , emission s from vacuu m baggin g ar e given . I S I T GENERA L ENOUG H T O US B FO RVACUU M BAGGIN G EMI S SIO N FACTORS ? W e fee l tha ti ti s a goo d representatio n o f vacuu m baggin g processes .

• WHEREDOESTHE30TPYFIGURECOMEFROM 7 Asoflastyear,rigorousemisio n testin g wa s done . Informatio n give n befor e tha tax e no ta s rigorous . So , th e 3 0 tp y figure i s actuall y obsolete . 4 2400-250 0 lb s o f

styren e totaUro m th e vacuu m baggin g proces s i s stated , an d th e Emissio n fectori s base d o n th e 199 0 stud y a t199 4 productio n levels .

• 232 5 lb s tota l emisicm^fro m th e vacuu m baggin g process . Som e leakag e occur s wit h vacuu m baggin g an d a smal l amoun tofth e leakag e carie s wit h i tstyrene . I ti s essentiall y 

## 3VAUG722-9

5 TU E 9:1 1 CRAN

E CO RTE C FA

X NO . 335217 1 ?- m

a close d process .

• Becaus e ofth e 6. 9 tp y figure, the y ar c no ta majo

r source .

• The

y installe d th e incineiato r t o contro l troug h diyingove n are

a foHih o t o Xui| , den e i n 4994 : Emissions from troug h diyin g are

a ar e nrinima T Testin g sinc e the

n show s i ti s lo w comparativel

y speaking . Incinerato

r controls approximatel

y 2 tp y for troug

h diyin g area .

• Th e troug

h siz e is^l O i n wide , 1 0 ftlong . Resin a ttha tpointi a handle d ou ta tambien t temperatures . Emissions com e fim heatin g an d curing. Resi n i n th e troug h has no tye t reache d gelation . I tdoesn' tgelat e unti l afte r th e vacuu

m bagging occurs . Th e trough s are-Mtcovered . Th e cyd e tim e from r^ p to tough is m th e order



### &cte W Te e A 6UJ» % 

### uouT. . • Emission los s from th e troug h i s include

d i n th e table emisions "An y emission leavin g th e troug h o r suffic e are

a o f par tbefor e vacuu m baggwg.. M -refere d t o a a "resi n t o ai r contacts'' .

• TH

E TRAD E ASSOCIATION WOUL D CAL L YO U CONTINOUS LAMINATION . We ar e no tcontinuous lamination. Processe s -whic h relat e t o u s ar e gelcoatinfl , han

d layu p an d etc . Probabl

y w e ar e mostlike han

d layu p wit h emissio n reduction throug h vacuu m bagging . Ou

r han d layu p i s different

, i ti s automated .

• Proces s description s wer e sentvi a fa^an d thoychould moi l omigoie n tes tiiifumiaU'oi>

i 

### A
• YOUHAVEALOWPLOWRAIETOTHEOXlDIZER;WBDlDNOTKNOWr r WA S THA T LOW

. Th e cos teffectivenes s seems t o b e (S200,000/yr)/2 5 tons-th a quantit y Incinerate

d whic h equals $8000Aon ; whic

h i s fiirry hig

h sinc e i ti s abov e 5000 . Baaed oiHPPfl

y a o penni tha s booo-rooorded . Whe n w e eateee

d 1 0 tpy , w c will nee d

* )

Informatio

n i s accurate : 

# -?V* r



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# Fa x Cove r Shee t

, - . M&
. MAoasuu e STRU M 

# tu*i£i**. $7***"

. To : *Mrs
. Wanit

aDunston ( i , -,^- 1 USEP A (*» ) SV - ^S< Phone:(919)541-230 6 Fax : (919 ) 541-007 2 » rrom : Mar

k Smit h n A -*

—. Crane Cor Te c Compan

y UpflME
. CO Rl£t / Phooe : (614)335-940 0 Fax : (614)335-484 3 WThtT (LePNC r Date : Augus t

8 , 1995 Subject : Additiona

l Datape r Phone Conference o n Augus t 8,199 5

Dea r Mrs
. Dunslon , Per you r request , th e addiliona

l proces s emission s datayo

u requeste di s a s follows : -Vacuu mbagging /

oven curing proces s emissio n factor : E(f ) = .00055 8 l

b styrene / l b resi n (basedo n 199

0 les l dat aan

d1994 TR I facilit y calculations ) -Tabl e laminatio

n an d trough application proces s emissio n factor : E(f ) = .0026 8 I

b styrene / l b resin (base don 199

4 tes t dat aan d199 4 TR I facilit y calculations ) -199 4 Tota

l Facilit y Losse s (pe

r 199 4 TR I calculations: ) Fugitiv e Poin

t Quantit

y Tota

l Losse s Losse s Incinerated Losse s (lb/yr ) (lb/yr

) (lb/yr

) (lb/yr) Vacuu mba g / ovens r 0 2.32 5 0 2,32 5 TableilamlnaliO

h an d 11,16 2 0 0 11,16 2 troug h application 

# 5P. 7 AUG-48-9 5 FR I 15:3 9 P . 0 2

Not e tha tth e variance i

n th e su m o f tota l losse s for al

l emission s source s an

d th e 6.9 0 ton s per year fo r th e facilit

y i s du e t o incidenta

l incineration o f

backgroun

d styrene b y inle t draf tinto th e catalyti c oxidizer . The dat a provided abov e i s based o n emission s testin g an d bes tengineerin g judgementregardin g ou r manufacturin

g processes . I f

yo u hav e any question s o r requir

e additiona

l information, pleas e contac tm e atyou r convenience . Sincerely ,

lar k Smit h Application s Enginee r Cran e Co r Te c Compan

y



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# 94-RA111.03 Demonstratio n o f

Captur e an d Contro l Efficiency fo r a Styren e Emissio n Sourc e

y v 

### *-* • 

# ^d^.-A'*

AI R& WAST E MANAGEMEN T ASSOCIATIO N

• SINC E 190

7 For Presentatio n a tth e 87th Annua l Meetin g & Exhibitio n Cincinnati,Ohi o June 19-24,199 4 

# A

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94-RA1I1.0 3 94-RAI I
,tai« . Contro l aw tOwrd l Efficiencie s (• ) Fitur e 1 . Gdooo

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# CWSE

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### •AUG---7-9 5 HO

N 15:4 7 CRAN

E CO RTEC FA

X NO , 335217 1 P- 0 1

To : Wanit

a Dunston ; E.P.A . —. . Fax : 919-541-0072 (^ ^ -f£ £ From ; J . Prio r Corte c Co . Washingto n Cour tHouse, Ohi

o Date : Augus

t7,199 5 I n respons e to you r reques tfo r informatio

n faxed t o u s o

n Jul y 28,1995 , w e hav

e prepare d th e attache d responses . W

e wil l pla n aconferenc

e cal l discussio n wit h yo u tomorro w (Augus t8 ) a s yo u suggeste d t o clarif y an y question

s yo u ma y have. A s I mentione d t o you , w e woul

d lik e t o reques tacop y ofth e draf

trepor ttha ti s prepare

d as . a resul tofth e dat

a tha twe ar e providing

.

/ /AUG-.7-9 5 MO

N 15:4 7 CRAN

E CO RTE C FA

X NO . 335217 1 P.1 3 P . 0 2

Augus t1 , 199 5 Co r Te c manufacture

s fiberglass/resin reinforced , plywoo d core d structura l panels , primaril

y fo r th e transportatio

n industry . Thermosetting polyeste r resin , fiberglass, plywood , an d either a polyeste r ge l coa to r Tedla r film ar e bonded togethe r utilizin g a vacuu m baggin g process . Gel coa tfinishes ar e prepare d i n a seperat

e sprayin g operation , an

d transporte

d t o th e vacuu

m table s afte r the y are cure

d fo r incorporation int

o th e laminate . The manufacturin g proces s i s a batch-typ e process . Afte r th e panel s ar e cured , they ar

e cu tt o siz e usin g computer-controlle d saws . (Se e attached proces s diagram) . Emissio n point s currentl

y vente d t o th e oxidize r includ e th e ge l coater , resi n troug h filling stations , an

d resi n troug h diyin g cabinet. Th e emissions fro m 199 4 to r thes e sources , a s calculated fo r th e facility' s 199 4 TR I for m R submissions , ar

e a s follows :

Ge l Coate r Troug h filling Trough diyin g Fugitiv e

Losse s (lb/yr ) 3,01 1 0 0 Poin

t Losse s (lb/yr ) 1,573 4 11 8 Quantit

y Incinerated (lb/yr ) 49,18 0 13 3 3,67 3 Tota

l Losse s Gb/yr ) 4,78 0 4 11 8 Averag e inletflow rat

e t o th e oxidize r i s 459 6 dscf m (dr y standar d cubi c f t/ min) , an d th e average outle tflo w rat e i s 477 8 dscfm . Averag e inletconcentratio n o f styren e t o th e oxidize r i s 276. 6 pp m an d th e averag e outle tconcentratio n o f styren e i s 14. 3 pp

m (pe r testin g conducted February , 1994) . Captur e efficiencies : ge l coate r 94.4 %

trough filling no testablished (insignificant ) troug h dryin g 100 % (total enclosure ) Destructio n efficienc

y o f catalytic oxidizer : 96.9 % (abov e dat

a from Februai y 199 4 testing ) Capita l investment : $ 700,000.0 0 Annualized operating costs : $ 89,000.0 0 I'h e laminatin

g proces s an

d vacuu m proces s ar

e no tvente d directly t o th e oxidize r du e t o th e prohibitive volume o f ai rwhic h woul d b e require

d t o effectivel y collec temission s fro m thes e sources . 

## LoP. M 

### 3-.7-9 5 K M 15*4 8 CRAN E CC RTE C FA

X NO . 335217 1 P.0 3

8 . Th e PermitEnginee r mos tfamilia r with ou r operatio n i s Chri s Bulinski , Ohi o Environmenta

l Protectio n Agency . 9 . Th e referenced paper i n th e questions doe s pertain t o ou r facility . 10 . Tota

l HA P (styrene ) emissions fo r 1994 , a s calculated fo r th e 199 4 filing o f Toxi c Releas e Inventoi y (TRI ) For m Rsubmissions fo r th e facility , wer e 6.9 0 ton s during 1994 .



## 13P.1 5 

### f• AUGT-7-9 5 

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15:4 8 CRAN E CO RTE C FA X NO
. 335217 1 

# .,-tiit : 

# CO R TE C

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T>t4<rtA+1• P.1 6 « --AUG; - 9-9 5 WE D 15:0 3 P . 0 1


# Fa x Cover Shee

t

To : Mrs . Wanit a Dunsto n USEP A Phone : (919 ) 541-230 6 Fax : (919 ) 541-007 2 From : Mar

k Smit h Cran e Co r Te c Compan

y Phone : (614)335-940 0 Fax : (614)335-484 3 Date : Augus t8 , 199 5 Subject : Additiona

l Dat a pe r Phon e Conference on August8 , 199 5

Dea r Mrs . Dunston , Per you r request, th e additiona l proces s emission s dat

a yo u requested i s as follows : -Vacuum bagging /

ove n curin

g proces s emissio n factor : E(f ) - .00055 8 l

b slyrenc /

l b resi n (base d o n 199 0 les tdal a an d 199 4 TR I facilit y calculations ) -Tabl e lamination an

d troug h application proces s emissio n factor : E(f ) = .0026 8 lb styrene /

I b resi n (based o n 199 4 tes tdat a an d 1994 TR I facilit y calculations ) -199 4 Tota

l Facilit y Losse s (per 199 4 TR

I calculations: )

Vacuu m bag / oven s Table lamination an

d troug h application Fugitiv e

Losse s Ob/yr ) 0 11,16 2 Poin

t Losse s (lb/yr) 2,32 5 0 Quantit

y Incinerate d (lb/yr) 0 0 Tota

l Losse s (lb/yr) 2,32 5 11,16 2


# JsP.1 7 •AtBr*9-9 5 ME

D 15:0 4 P . 0 2

Not e tha tth e variance i n th e su m o f total losse s for al

l emission s source s an

d th e 6.9 0 ton s per year fo r th e facilit

y i s du e t o incidenta

l incineratio

n o f backgroun

d styrene by inlet draf tint o th e catalyti c oxidizer . Th e dat a provide d abov e i s base d o n emissions testin g an d bes tengineering judgemen tregardin g our manufacturin

g processes . If

yo u have an

y question s o r requir

e additiona

l information , pleas e contactm e a tyou r convenience . Sincerely ,

Mar k Smit h ^- ^ Applications Engineer Cran e Co r Te c Compan

y



# U