### P. 1



# OAR Box 1500
Prepped by Ollie Stewart



# Document

Number: 

# 2 ) ll-C-2 8

Docket Number: 

# A-94-5 2

Printed 8/5/20081:45:55PM Sheet 2 oj343P. 2 

# A-94-5 2

^°ST<

9 O 

# S E UNITE D STATE S ENVIRONMENTA L PROTECTIO N AGENC Y RESEARC H TRIANGL E PARK

. N C 2771 1

•• t PRO! *



# m.. 

# m&sm

**&*

. EPA AI R DOCKE T OFFIC E O F AI R QUALIT

YPLANNIN G AN O STANDARD S



# Februar y29 , 199 6

Dea r Presumptiv e MAC T Team and/o r EP AWor k Group Member :
Thi s i s t o confirmth e teleconferenc e fo r th e reinforce d plasti c composite s projec t t o b e hel d Wednesday , Marc h 20 , 1996 , fro m1pmt o 3:30p

mEaster n Standar d Time , and t o provid e material s fo r th e meeting

. Th e meetin g wil l b e hel d a t EP Ai n Roo m63 8 o f th e Nort h Carolin a Mutua l Buildin g i n Durham , Nort h Carolina

. Th e call-i n numbe r i s (919 ) 541-1590

.
A t thi s meetin g w e wil l b e discussin g th e futur e o f th e P-MAC T process , potentia l emissio n limits , wor k practic e standard s an

d issues

. Enclose d ar e a briefin g packag e an d spreadsheets

. Th e spreadsheet s provid e th e detail s o f ou r preliminar yemissio n limi t calculations

. The ywil l no t b e discusse d i n detai l a t th e meeting , bu t ma yb e o f interes t t o thos e o f yo u wh o wis h t o kno wth e detaile d dat a from whic h th e emissio n limit s wer e derived

. Pleas e not e tha t som e value s o n thes e spreadsheet s wil l chang e a s w e continu e t o chec k ou r dat a quality

. W e woul d als o welcom e an yeffort s yo u mak e toward s thi s qualit yassurance . Pleas e hav e th e briefin g packag e availabl e a t th e Marc h 20t h conferenc e call

.
I f yo u hav e an

yquestion s o n th e enclose d materia l pleas e cal l m e a t (919 ) 541-2383

.

-/L £ Madelein e Stru

m
Enclosure s

### P. 3



# Addressee s

} • vsri 

# Moha n Balagopalan , Sout h Coas t Ai r (pual^t y Managemen t Distric t Bo b Burmark , Washingto n Departmen t ©#~Beoi < Jan e Caldwell , OAQP S (MD-15 ) '„„! Leonard o Ceron , EP ARegio n I V Lind a Chappell , OAQP S (MD-15 ) Bo b Fegley , ORD Lesly e Fraser , OG C Chuc k French , OAQP S (MD-15 ) Lind a Herring , OAQP S (MD-13 ) NormKaplan , OR D (MD-04 ) Kare n Levy , OPA

R Mari a Malave , OEC A Hail e Mariam , OSWE R Crai g Matthiessen , OSWE R Stev e McNally , Composit e Fabricator s Associatio n Christin e McPhee , Ohi o EPA Arnol d Medbery , OSDB U Richar d Nielson , Clar k Count yHealt h Distric t Carlo s Nunez , OR D (MD-61 ) Nanc yPate , OAQP S (MD-12 ) Gedde s Ramsey , OR D (MD-61 ) Solomo n Ricks , OAQP S (MD-19 ) Ro n Ryan , OAQP S (MD-14 ) Ale x Santos , Californi a Ai r Resource s Boar d Joh n Schweitzer , Societ yo f Plastic s Industry/Compositie s Institut e Jorda n Spooner , OPP T

^

# PROJEC T BRIEFIN G

REINFORCED PLASTI C COMPOSITE S PRODUCTIO N
MAC T STANDAR

D DEVELOPMENT

BRIEFIN GFOR :
WEPAP-MAC T TEAM AND EPAWORK GROUP

Projec t Lead : Madelein e Strum(ESD/CCPG ) Marc h20 , 199 6

## > 

# PURPOS E

Discus s experienc e wit

hP-MAC T teamapproac h
Present MAC T floor s andalternative s abov e th e floor
Discus s applicability o f

standard
Present suggeste dregulator

y approac han dne w projec t schedul e

T l O l

# P-MAC T TEA M APPROAC H

Forme dtea

mo f EPA , State/local , industry , an denvironmental representative s
Los t environmental representativ e
Hel dfou r teleconference s t o presen t dat aan ddiscus s issue s

\i\ Larg e an ddivers e industr y pose s proble mfo

r P-MAC T Request s fo

r input hav e bee nlargel y unsuccessfu l
Lack time/fundin g t o keep P-MAC T goin g an dge t standardout

in reasonabl e timeframe Suggestion : phas e out

P-MAC T proces s an dadop t th e conventional standard s development

approac h

p

# G \ MAC T ANALYSI S

Industr y Subcategorizatio n Approache s fo

r Numerical Emissio nLimit s Subcategory-Specifi c Analyse s - Numerica l Emissio nLimit s
Wor k Practice s

4

T l

# INDUSTR Y SUBCATEGORIZATIO N

Separate MAC T floo

r calculation s for :

~ o 

# OpenMoldin g (han dor spra y layup ) Gel Coatin g Continuou s Lamination/Continuou s Castin g Filament Windin g Compressio nMoldin g InjectionMoldin g Resi nTransfe

r Moldin g Pultrusio n Compounding - BM C Compoundin g - SM C Polyme r Castin g Centrifuga l Castin g
Notes : Dat

abas e includes polyeste rand viny l este r(styrene-containing ) resin s only
. Us e of "prepreg " i s no tparto f

sourc e category .

T l 0 0

# APPROACHE S CONSIDERE D FO RDETERMININ G BES T PERFORMIN G FACILITIE S

1

. Averagin g withResi nCure Facto r

ameasure o f

weight los s durin g cure eas y t o measure i nstati c la b tes t compatibl e wit

hSout hCoas t rul e dat afo r resin s i nus e lackin g lac k o f correlatio nwit

hstyren e conten t

o r emission s

2

. Resi nHAP(Styrene ) Content
dat aare readil y availabl e

• als o compatibl e wit

hSout hCoas t rul e

• lower

styren e content

no t th e onl y mean s o f

emissio nreductio n

T l

# - p 

# APPROACHE S CONSIDERED (continued )

3

. Percent

Reductio n(Add-ons )

4

. Facility "Contro l Status " (CS )
unit s o f l b HAP(monomer) per

gallo no f resi nmatri x (RM )

• lower

C S mean s th e facilit

y i s better controlle d

• account s fo

r quantifiabl e reductio nmeasure s inus e (lo w resi nstyren e content , fille r use , suppressants , non-spray application , add-o ncontrols )

• selecte da s th e primar y rankin g variabl e

7

# o CALCULATIO N O F FACILIT Y CONTRO L STATU S (CS )
Formula :
C S = [ Resi n(lb/yr) ] [HA PWt

. % ] x Applicatio nx VS Rx Contro l (Resi n+ Filler) Volume Facto r Facto r

Facto r

Example : Resi n= 5. 0 M M lb/yr Filler = 7. 0 MM lb/yr Styren e Wt

. % = 38. 0 (n o other HAP) Applicatio nfactor = 0.5 5 (non-spray appl. ) VS Rfactor

= 0.6 0 (vapo r

suppressant ) Contro l factor

= 1.0

0 (n o contro l device )

Calculation :
C S = (5xl0 6 

# ) x (0.38 ) x 0.5 5 x0.6 0 x1.0 0 = 0.6 9 l b HAP/gal (543,50 0 + 364,600 ) gal resi nmatri x

8

# APPROACHE S CONSIDERED (concluded )

issues: - facilitie s usin g highl y fille dresi nmixture s hav e a

built-i nadvantag e over

unfille dapplication s

- other measure s are i nus e bu t

no t include d(shorter

ge l times , resi nthickness , ai r

conditione dfacility , etc. )

- OR D developin g acomprehensiv e mode l t o predic t ope n moldin g emissions ; won' t

b e availabl e fo

r developin g proposal

- approac hcredit s same % reductio nfo r al l vapor-suppresse d resin s under

al l applications ; industr

y may reques t tailore dcredit

fo r eac hscenari o (different

suppressants , concentration s used , etc. )

### P.1 3 1



# SUBCATEGORY-SPECIFI C ANALYSE S

Note : Th e followin ganalyses d o notinclud e th e impact of workpractice standards ; se e pag e 37
.



# 10 /2
-

### P.1 4



# OPE N MOLDIN G (21/172) *
MAC T Floors : Existing : media

nC S valu e ( = 1.

4 lb HAP/ga

l RM ) New : bes t

% reductio n( = 95% )
o r bes t C S valu e ( = 0. 2 lb HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio no r other devic e t o achiev e a

t leas t 95 % reductio nor

C S valu e o f

les s thano r equa l to 0. 2 l b HAP/ga l RM

.

New : None

.

indicate s that

"floor " facilitie s compris e 2 1 out ofth e total o f 17 2 majo r sourc e openmolders

.

1 1

# EXAMPLE FO RCALCULATIN G MAC T FLOO R- OPEN MOLDIN G FACILITIE S

£ * Ran k

i 2 3 4 5 

## • 7 

## • 9 1 0 1 1 1 2 1 1 1 4 I S 1 6 1 7 1 1 I t 2 0 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 8 2 9 3 0 3 1 3 2 3 3 3 4 3 5 3 6 3 7 3 8 3 9 4 0 8pnyu p an d Han d layu p combine d I M



### BaUter a A.R.E,toc(Ma»aaion ) 1)3

. Ftborglas s Product s In c ReeoUt e Tompkin s •Lasc o Bathwar a (Elltabamtown ) Contemporar yProduct*

. Inc

. TompMn a - Lasc o Balhwar a (Lancaatar ) AiCE R Plastic s Company , kxMPtymoum , Pldc o Or ) 8.W. C Industrias

. In c (SwirfrWa y Div. ) AKE R Plastic s Company

. mctPtymoutti

. N Oa k Rd ) TompMn a - Laac o Bathwar a (Sout h Boston ) Cada rManufacturing , lnc(Bi«4na n Guts ) l^iciten' e Plastics , Ir4 c Bran m Glaa , li4 C TompMn a •Laac o Bathwar a (Moapa ) TompUn a •Laac o Bathwar a (Cordate ) Totnpkln a •Lasc o Bathwar a (Anahaim ) Tompfcin a •Lasc o Bathwar a (HU M Rivals ) Balhasftln c Unhntsal-Rundt e Corp

. (Ottumwa ) Caraml c Coolin g Towa rCompan y Tompkin s •Lasc o Bathwar a (Yetm ) (ak a Hyts c Inc. ) Warminste rFiberglas s Compan y(Jackfonvflto ) Wsrmirutet FberoJas s Compan y (Southampton ) CBIP4ant« 7 CO R Systam a Corporatio n (Corcoran ) CO R Systam s CorporaUa n (PaWka ) Centur yfcUnufacturing Compan y Custo m Ffcregtas s (Manufacturin g Co

. Nationa l Ft wGlas s Products

. In c America n Reinforce d Plastic s Prestigiou s Acoassories , Inc

. Grsa t Dan a Tralar a Indiana

. In c (FR P Plant ) Aem a Ffeerglasa

. Ire

. Diamon d Cuac h Cofporauo n Sunse t Plastic s Inc

. Bristo l Fibortt e Industria s Hes s County MutMe s o fVW

. Inc

. Fowle rlytanufacturina , In c Styl o Cras t Products GW.FDarBtass.ln c Proces s Dos e Cfid a

13*1 7

8*1 3 1 6 1 6 •

1 3 1 2 Resi n



### l__ 6866 J 375. 0 •0. 0 2124 3 190. 0 2279. 3 164. 7 300. 0 2310. 1 2770. 2 367. 0 277. 0 11690 ) 6266. 6 1976. 6 3136 3 2816. 4 944. 6 2600. 0 110. 0 2763 3 121. 0 139. 3 1017. 0 152. 0 125. 0 74. 5 553. 0 640. 0 288. 0 432. 0 375. 0 185. 0 138. 0 254. 0 247. 0 494. 0 439. 0 84. 0 1850. 0 % Styren e

AsSuooSa d 4 2 0 46. 0 24. 1 47. 7 38. 0 47. 7 36. 0 36. 0 36. 0 48. 1 36. 0 43. 0 44. 0 47. 0 47. 6 47. 7 47. 7 41. 2 46. 6 32. 0 47 3 40. 0 40. 0 43 5 34. 0 34. 0 48. 0 44. 9 48 0 40. 7 35. 0 39. 0 43. 0 40. 0 43. 0 38 2 35. 0 50. 5 24. 0 45. 0 Fila r

dey j M 

### a o 11. 4 3304 3 

### a o 3564. 7 160. 6 300 3 2378. 7 4078. 1 359 3 

### a o 1658. 0 6644. 6 1002. 2 464M. 6 4366 4 986. 9 3276. 0 

### a o 4216 3 

### a o a o 603. 0 0. 0 0. 0 60. 0 266. 0 670. 0 121. 0 

### a o 0. 0 75. 0 

### a o 215. 0 0. 0 494. 0 161. 0 0. 0 395. 0 bstvrene /

OtUBU 3.6 6 4J2 2.0 3 2.6 1 33 9 2 3 1 2.1 7 2.1 7 2J 1 23 9 2.3 8 4.1 3 2.4 6 2.4 6 2.6 1 2.5 1 2.8 1 2.5 2 16 2 2.6 4 23 4 3.6 7 3.6 7 3.1 1 3.1 2 3.1 2 3.1 8 3.3 5 3.0 9 3.1 1 3.2 1 3.5 6 3.3 1 3.6 7 2.6 1 3.5 1 2 1 7 3.9 8 2 J 0 3.7 5 Applicatio n

Easaa c 13 0 1.0 0 03 6 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.6 0 1.0 0 1.0 0 13 0 1.0 0 1.0 0 13 0 1.0 0 03 6 1.0 0 0.7 8 0.7 8 0.5 5 0.5 5 0.5 5 0.5 5 0 9 1 1.0 0 1.0 3 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 VS R

Eflflor , 1.0 0 0.6 0 1.0 0 O.I O 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 0.7 2 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 0.6 0 1.0 0 0.6 4 0.6 0 0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 0.6 0 0.6 0 0.6 0 0.6 0 1.0 0 0.6 0 1.0 0 0.7 2 0.6 0 1.0 0 1.0 0 1.0 0 0.6 0 Contro l EK&r

. 

### aos ai o 1.0 0 a7 6 1.0 0 

### a n 1.0 0 1.0 0 1.0 0 0.7 8 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 Contro l

Statu s (bHAEtaalfiiM ) 0.1 9 0.4 6 1.1 2 1.1 4 1.1 5 1.1 7 1.3 0 1.3 0 1.3 3 1.3 9 ^•'£:iMj; ••••••• • 1.4 7 1.4 8 1.4 6 1.6 0 1.6 1 1.5 1 1.5 1 1.6 7 1.6 2 1.6 2 1.7 1 1.7 1 1.7 1 1.7 2 1.7 2 1.7 5 1.6 3 1.6 5 1.8 7 1.9 3 1.9 7 1.9 8 2.0 2 2.0 2 2.1 0 2.1 7 2.1 9 Z2 0 2.2 5 Curran t Emis

.

Ora l 31. 2 6. 0 Z O 116. 1 

### a o 128. 0 9. 0 15. 9 126. 2 180. 9 21. 2 11. 3 77 3 446. 8 143. 3 227. 1 203. 9 69. 1 176. 5 4. 6 213. 3 5. 7 6. 6 61. 6 7. 2 5. 9 5. 0 34. 3 46. 6 17. 8 23. 0 20. 4 12. 1 7. 7 19. 9 14. 3 43. 7 30. 6 5. 1 126. 4 MAC TEmis

.

OfiV J 31. 2 6. 0 2. 0 116. 1 6. 0 128. 0 9. 0 15. 9 126. 2 160. 9 21. 2 10. 9 74 3 430. 8 13S. 7 216. 1 193 3 85. 7 1S9. 8 4. 3 187 3 4. 6 5. 5 51. 3 6. 0 4. 9 4. 1 26. 7 3S. 9 13. 6 17. 0 14. 7 8. 7 5. 4 14. 0 9. 7 28. 7 20. 1 3. 3 80. 1 Reductio n Technique s Inrliietalu r Cmtara.VS R Han d (100% ) Incinerator , VS R VSR , Han d (100% ) Incinerator , VS R VS R VS R VS R Incinerator , VS R (72% )

VS R VSR , Han d (90% ) A Spra y (10% )

VS R VS R VS R VS R VS R VS R VS R Han d (100% ) VS R (90% ) VSR

. Han d 6 Spra y VSR , Han d A Spra y Han d (100% ) Han d (100% ) Han d (100% ) Han d (100% ) VSR , Han d (20% ) VS R VS R VS R Vacuu m baggin g VS R Applie s wftoOer

s VS R (70% ) VS R

Han d (100% )

VS R



# 12 

# Y T l 

### o i

### P.1 6



# Issues : OPE N MOLDIN G (concluded )

Highly filledapplication s hav e abuilt-i nadvantag e ove r unfille dapplication s (lowe r net styrene content

andhenc e a lowe r contro l statu s factor)

. Top performing facilitie s consis t mainly of tub/shower

makers

. Tub/shower

facilitie s compris e 67 % ofth e 2 1 to p performin g facilitie s and27 % o

f all 172 know nopenmoldin g facilities

. A s man y as 86 % of

ope nmolder s spra

y applyin g unfille d resin s coul dneedacontrol devic e t o comply (assumin g non e coul dswitchfro

mspra y applicatio nor

beginusin g filler)

. Industr y (CFA) claim s add-o ncontrol s fo r Ne w Sourc e MAC T will kil l th e industry

. Industr y want s exemptionfo

r corrosion-resistant

application s becaus e they believ e add-oncontrol s are th e only availabl e complianc e method

. How to define acorrosion-resistant application ; shouldthe

y hav e adifferen

t numerica l limit ?
Industr y ma y wan t reductioncredit

fo r additiona l measure s (spra y technology , etc.)

.



# Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor : Emission s (tpy) : Percent Reduction : 

# 1 3 

# /< r 17 2 9,29 2 Media nC S 5,83 2 37 %

### P.1 7



# PULTRUSIO N (5/17 )
MAC T Floors : Existing : media

n% reductio n( = 47% )
or media nC S valu e ( = 1.2 l

b HAP/gal RM )

New : bes t

% reductio n( = 95% )
or bes t C S valu e ( = 0. 2 l

b HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor othe r devic e t o achiev e a

t leas t 95 % reductio nor

reduc e C S valu e t o les s thanor equa l to 0. 2 l b HAP/ga l RM

.

New : None

.

1 4

### P.1 8



# PULTRUSION (concluded )

Issues : Industr

y maintain s tha

t facilitie s usin g incinerator s cannot b e considere da s par

t ofth e MACT floor

fo r thi s subcategor

y becaus e th e incinerator s ar e there du e to other

emissio npoints

. Othe r contro l measure s ar

e inus e but

no t included

. Media n(floor ) facilit y ha s a nassumed50 % capture efficiency

. Pultrusio nIndustr

y Council want s rul e t o include equipment standard s tha

t they believ e produc e reductions

. "Fum e collector " i s inus e but

no dataar e availabl e to assig n reductio ncredit

.



# Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 1 7

167 Media n% Reductio n 9 9 4 8 % Media nC S

Valu e 6 5 6 1 %



# 1 5

i l

### P.1 9



# GE L COATIN G (18/150 )
MAC T Floors : Existing : n o numerical value *

New : bes t

% reductio n( = 95% )

Option s Abov e th e MAC T Floor : Existing : 1

. Us e low-VO C gel coats

.

2

. Us e combustio nor

other devic e t o achiev e at leas t 95 % reduction

.

New : None

.

*See wor k practice s (pag e 37)

.

1 6

### P.2 0



# Issues : GE L COATIN G (concluded )

Inclusio no f

facilitie s usin g acrylic sheet s inplac e o f gel coating woul drequire add-oncontrol s fo r existin g facilities

. Lacking facility-specifi c ge l coa t densit y datat o set

a l b HAP/ga l gel coa t standard

. Industr y say s canno t

bas e Ne w Sourc e MAC T o n A.R.E

. facilit

y (incinerator

o nbot hresi nandpaintin g operations)

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 15 0

4,340 N o Numerica

l Value 4,340 0 %



# 1 7 

# n

### P.2 1



# CONTINUOU S LAMINATION/CASTIN G

(5/13 )

MAC T Floors : Existing : media

n% reductio n( = 49% )
or media nC S valu e ( = 0. 5 l

b HAP/gal RM )

New : bes t

% reductio n( = 95% )
o r bes t C S valu e ( = 0. 2 l

b HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 95 % reductio nor

reduc e C S valu e t o les s tha nor equal t o 0. 2 l

b HAP/ga l RM

.

New : None

.

1 8 Z< 3

### P.2 2



# CONTINUOU S LAMINATION/CASTIN G

(concluded )

Issue :

• Medi.a

n(floor ) facilit y ha s a nassume d50 % captur e efficiency

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 3

1,12 3 Media n% Reductio n 61 4 45 % MedianC S

Valu e 39 1 65 %



# 1 9

### P.2 3



# FILAMEN T WINDIN G (5/31 )

MAC T Floors : Existing : media

n% HAPContent

a s Supplie d ( = 42.5% ) (equivalent

t o media nC S valu e o f

3. 9 l b HAP/ga l RM )
New : lowes t

% HAPContent

a s Supplie d( = 33% ) (equivalent

t o C S valu e o f

3. 0 lb HAP/gal RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

2 0

### P.2 4



# Issue : 

# FILAMEN T WINDIN

G (concluded

)

Many filamen

t winder s are usin g corrosion-resistant (CR) resin s an

dindustr y claim s nee dfo

r a nexemption

. (Sout hCoas t rule allow s 48 % monomer content b y weight vs
. 35 % fo

r genera l purpos e resins. ) Som

e low

styrene CRresin s ar

e enterin g th e market

.

Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 3 1

50 8 Media n% HAP Content 47 1 7 %



# 2 1 

# £2 >

### P.2 5



# INJECTIO N MOLDIN G

(5/5 )

MAC T Floors : Existing : no numerica

l value *

New : n o numerica

l value *

Option s Abov e the MAC T Floor : Existing : Requir

e combustio nor

othe r devic e t o achiev e a

t leas t 9 5 % reduction

.

New : Requir

e combustio nor

othe r devic e t o achiev e a

t leas t 9 5 % reduction

.

*See wor k practice s (pag e 37)

.

2 2

-2H

### P.2 6



# INJECTION MOLDIN G (concluded )

Issue :

• Ver

y narro w rang e o f C S values ; difficul

t t o selec t a floor value

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 5

6 3 N o Numerica

l Valu e 6 3 0 %



# 2 3 25 "

### P.2 7



# COMPRESSIO N MOLDIN G

(5/42 )

MAC T Floors : Existing : n o numerica

l value *

New : n o numerica

l value *

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e at leas t 95 % reduction

.

New : Require combustio nor other devic e t o achiev e at leas t 95 % reduction

.

*See wor k practice s (pag e 37)

.

2 4



# 2.L

### P.2 8



# COMPRESSION MOLDIN G (concluded )

issi onImpacts : No
. of

Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 4 2

35 4 N o Numerica

l Value 35 4 0 %



# 2 5 

# 2 1

### P.2 9



# RESIN TRANSFERMOLDIN G

(5/9 )

MAC T Floors : Existing : n o numerical value *

New : n o numerical value *

Option s Above th e MAC T Floor : Existing : None

.

New : None

.

*See wor k practice s (pag e 37)

.

2 6

### P.3 0



# RESI N TRANSFE

RMOLDIN

G (concluded)

Emissio n Impacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 9

5. 7 N o Numerica

l Value 5. 7 0 %



# 2 7

### P.3 1



# COMPOUNDIN G - BM C

(5/11 )

MAC T Floors : Existing : n o numerical value *

New : bes t

% reductio n( = 4 9 % )

Option s Above th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

*See wor k practice s (pag e 37)

.

28

SO

### P.3 2



# COMPOUNDIN G - BM C (concluded )

Issue :
There ma y b e othe r non-styrene resi ncompound s wit h HAPthat w e haven' t

considere d(n o data)

.

Emissio nImpacts :

No
. of Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 1

4 5 N o Numerica

l Value 4 5 0 %



# 2 9 3 1

### P.3 3



# COMPOUNDIN G

(5/14 )

MAC T Floors : Existing :

New : no numerica

l value *

best% reductio

n( = 72 - SM C

% )



# Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

'Se e wor k practice s (pag e 37)

.

3

0 32^

### P.3 4



# COMPOUNDIN G - SM C (concluded )

Emissio n Impacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 4

26 8 N o Numerica

l Valu e 26 8 0 %



# 3 1 3> 3

### P.3 5



# POLYME RCASTIN G (5/19 )

MAC T Floors : Existing : media

nC S valu e ( = 1. 1 l

b HAP/ga l RM )
New : bes t

C S valu e ( = 0. 5 lb HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Reduc e C S valu e t o les s tha nor equal t o 0. 5 l b HAP/ga l RM

.

New : None

.

32

### P.3 6



# POLYMERCASTIN G (concluded )

Issue :

• Fille

r equit y issu e - som e facilities ma

y no t be abl e t o increas e fille r usag e t o achiev e th e floo r level

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 9

4 6 Media nC S Value 3 4 26 %



# 3 3 35 -

### P.3 7



# CENTRIFUGA L CASTIN G

(5/5 )

MAC T Floors : Existing : media

nC S valu e ( = 0. 4 lb HAP/gal RM )
New : bes t

% reductio n( = 50% )
or bes t C S valu e ( = 0. 2 l

b HAP/gal RM )

Options Abov e th e MAC T Floor : Existing : Reduc e C S valu e t o les s thano r equal t o 0. 2 l b HAP/ga l RM , or require combustio nor

other devic e to achiev e a

t leas t 95 % reduction

.

New : Require combustio no r other devic e to achiev e a

t leas t 95 % reduction

.

3 4 

# 3t >

### P.3 8



# CENTRIFUGAL CASTIN G (concluded )

Issue :

• Assume

d50 % captur e efficienc y fo r Fibercas t (likel y t o b e alo w estimate ) - impact s Ne w Sourc e MACT

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 5

9 6 Media nC S Valu e 9 1 5 %



# 3 5 

# 3 ?

# EMISSION S CALCULATION S - EXISTIN G FACILITIE S

CA ) 

# Subcategor y Ope nMoldin g Ge l Coatin g Continuou s Lamination/Castin g Filamen t Windin g Compressio nMoldin g Compoundin g - SM C Pultrusio n Centrifuga l Castin g Injectio nMoldin g Compoundin g - BM C Polyme r Castin g RT M TOTAL S No
. o f Majo rSourc e Facilitie s 17 2

15 0
1 3

3 1
4 2
1 4 1 8 5 5 9 1 9 9 Baselin e Emission s (tpy )

9,29 2 4,34 0 1,12 3

50 8 35 4 26 8 16 7 9 6 6 3
4 5 4 6
6 16,30 7 MAC T Floo r

Emission s (tpy) *

5,83 2 4,34 0 39 1

47 1 35 4 26 8
6 5 9 1
6 3
4 5 3 4
6 11,95 9 Emissio n

Reductio n(tpy) * 3,46 0 (37% ) 0 (0% ) 73 2 (65% )

3 7 (7% ) 0 (0% ) 0 (0% ) 10 2 (61% ) 5 (5% ) 0 (0% ) 0 (0% )
1 2 (26% )
0 (0% ) 4,34 8 (27% )


# 'Value s d o no tinclud e emissio nreduction s du e t o P2 wor kpractices
. 

# 3 6

# ~ Q 

# POSSIBL E WOR KPRACTIC E STANDARD S

Al l Subcategorie s

- cover s onHAP-containin g vessels , includin g mixer s

- mixer s completely covere ddurin g mixin g

- clea nup spill s immediately
Gel Coatin g andSpra

y Layup

- operator trainin g progra

m

^ • SMC Compoundin g

- us e nylo nfil

m(better vapor barrier) -fol dedge s o f

SMC Compressio nMoldin g

- reduc e number

o f BMC or SMC "charges " lef

t opent o evaporat e prio r t o moldin g
Cleanin g

- some us e o f

methylen e chloride (Mel ) andother HAPsolvent s reporte d

- use da t about 20 % o f majo r source s

- mos t facilitie s us e only aceton e or substitute s

- issue: ba

nonMC I us e coul dlea

dto alawsuit

(Woo dFurniture rule ) 3 7

# APPLICABILIT Y

Dat abas e include s predominantl y polyeste r an dviny l ester

resin s containin g styren e monomer (an dsome MMA )

• Other

HAP-containin g resin s are inus e (phenolics , epoxies , etc. )

- lo w HAPcontent s

- primaril y phenol , epichlorohydrin , etc

. f

- - mostl y advanced , high-strengthapplication s (e.g. , aerospace ) "5 " - n o dat ao nthes e

• Issue: Shoul dstandardattemp t t o cover al l thermose t

resi nuse ?

3 8

T J

### P.4 2


## '



# WIDES T APPLICABILIT Y OF TH E STANDARD S

Subcategor

y OpenMoldin g

Gel Coatin g

Cont

. L«amination/Castin

g

Filament Winding

Compressio nMolding

Compoundin g - SM

C

Pultrusio n

Centrifuga l Casting

Injectio nMoldin g

Compounding - BM

C

Polymer Castin g

RT M Existin go r

Ne wPlant Existin g Ne w Existin g New Existin g Ne w Existin g New Existin g Ne w Existin g New Existin g New Existing New Existin g New Existin g New Existing New Existing New Polyesteran d Viny l Este rPlant

s Onl y X

X X

X X

X

X X All Thermoset

Resi nUse

X

X X

X X X X X X

' X X X X X

X X 

# 3 9

# NEX T STEP S



# X Meetin g wit hP-MAC T Team(Industry , S/L , Wor k Group )
Assessment

o f Impact s (additional dat agathering ) Beyond-the-Floo r

Analysi s
Possibl e Negotiation s withIndustry Review/Approval b y Wor k Group/ES D Preparatio no f

Regulator

y Proposal Framewor

k

4 0

# NEAR-TER M PROJEC T SCHEDUL E

Mileston e Sen dMAC T floors/option s packag e t o P-MAC T team P-MAC T tea

mmeetin g o nMAC T floors/option s Firs t draf t o f framework

fo r preambl e andpropose drul e Dat e early Marc h199 6 late Marc h199 6 Jun e 199 6

LONG-TER M PROJEC T SCHEDUL E

Mileston e Rul e proposal Rul e promulgatio n Date Apri l 199 7 Apri l 199 8

Al l dates ar e dependen

to n availabilit

y o f funding
.

4 1

# PROJEC T BRIEFIN G

REINFORCED PLASTI C COMPOSITE S PRODUCTIO N
MAC T STANDAR

D DEVELOPMENT

BRIEFIN GFOR :
EPAP-MAC T TEAM AND EPAWOR K GROUP

Projec t Lead : Madelein e Strum(ESD/CCPG ) Marc h20 , 199 6



# «H

# PURPOS E

Discus s experienc e withP-MAC T teamapproac h
Present MAC T floors an dalternative s abov e th e floor
Discus s applicability o f

standard
Present suggeste dregulatory approac han dne w projec t schedul e

/ 

# 4r

# P-MAC T TEA M APPROAC H

Forme dteamo f

EPA , State/local , industry , andenvironmental representative s
Los t environmental representativ e
Hel dfou r teleconference s t o present dataan ddiscus s issue s Larg e an ddivers e industr

y pose s proble mfo

r P-MAC T Request s fo

r input hav e bee nlargel y unsuccessful
Lac k time/fundin g to keep P-MAC T goin g andget standardout

in reasonabl e timeframe Suggestion : phas e out

P-MAC T proces s andadop t th e conventional standard s development

approac h

3

# MAC T ANALYSI S

Industr y Subcategorizatio n Approache s fo

r Numerical Emissio nLimit s Subcategory-Specifi c Analyse s - Numerical Emissio nLimit s
Wor k Practice s

4



# ^ 7

# INDUSTRY SUBCATEGORIZATIO N

Separat e MAC T floor

calculation s for : OpenMoldin g (han dor

spra y layup ) Gel Coatin g Continuou s Lamination/Continuou s Castin g Filament Windin g Compressio nMoldin g Injectio nMoldin g Resi nTransfer

Moldin g Pultrusio n Compoundin g - BM C Compoundin g - SMC Polymer Castin g Centrifuga l Castin g

Notes : Dat abas e include s polyeste r an dviny l este r

(styrene-containing ) resin s only

. Us e o f "prepreg " i s no t

par t o f sourc e category

.



# 5

# APPROACHE S CONSIDERE D FO RDETERMININ G BES T PERFORMIN G FACILITIE S

1

. Averagin g withResi nCur e Facto r

ameasur e o f

weigh t los s durin g cur e eas y t o measur e i nstati c la b tes t compatibl e wit hSouthCoas t rul e dat afor resin s i nus e lackin g lac k o f correlatio nwit hstyren e conten t o r emission s

2

. Resi nHA P(Styrene ) Conten t

dat aar e readil y availabl e

• als o compatibl e wit hSouthCoas t rul e

• lowe r

styren e conten t

no t th e onl y mean s o f

emissio nreductio n

6

# APPROACHE S CONSIDERED (continued )

3

. Percent

Reductio n(Add-ons )

4

. Facility "Contro l Status " (CS )

• unit s o f

lb HAP(monomer) per

gallo no f resi nmatri x (RM )

• lower

C S mean s th e facilit

y i s better controlle d

• account s fo

r quantifiabl e reductio nmeasure s inus e (lo w resi nstyren e content , filler use , suppressants , non-spray application , add-o ncontrols )

• selecte da s th e primary rankin g variabl e

7

T J

# CALCULATIO N O F FACILIT Y CONTRO L STATU S (CS )
Formula :
C S = [ Resi n(lb/yr) ] [HA PWt

. % ] x Applicatio nx VS Rx Contro l (Resi n+ Filler) Volume Facto r Facto r

Facto r

Example : Resi n= 5. 0 M M lb/yr Filler = 7. 0 MM lb/yr Styren e Wt

. % = 38. 0 (n o othe r HAP) Applicatio nfactor = 0.5 5 (non-spray appl. ) VS Rfactor

= 0.6 0 (vapo r

suppressant ) Contro l factor

= 1.0

0 (n o contro l device )

Calculation : C S = (5xl0 6 

# ) x (0.38 ) x 0.5 5 x 0.6 0 x 1.0 0 = 0.6 9 l b HAP/gal (543,50 0 + 364,600 ) gal resi nmatri x

8

U l

# APPROACHE S CONSIDERED (concluded )

issues: - facilitie s usin g highly fille dresi nmixture s hav e a

built-i nadvantag e over

unfille dapplication s

- other measure s are inus e bu t

no t include d(shorter

ge l times , resi nthickness , air

conditione dfacility , etc. )

- OR D developin g acomprehensiv e mode l t o predic t ope n moldin g emissions ; won' t

b e availabl e fo

r developin g proposal

- approac hcredit s same % reductio nfo r all vapor-suppresse d resin s under

all applications ; industr

y ma y reques t tailore dcredi t

fo r eac hscenari o (different

suppressants , concentration s used , etc. )

U l c o

### P.5 4



# SUBCATEGORY-SPECIFI C ANALYSE S

Note : Th e followin ganalyse s d o no tinclude the impac

t o f wor kpractic e standards ; se

e pag e 37
.

1 0 

# 5 ^

### P.5 5



# OPEN MOLDIN G (21/172) *
MAC T Floors : Existing : media

nC S valu e ( = 1.

4 l b HAP/gal RM )
New : bes t

% reductio n( = 95% )
or bes t C S valu e ( = 0. 2 lb HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor othe r devic e to achiev e a

t leas t 95 % reductio nor

C S valu e o f

les s thanor equal t o 0. 2 l

b HAP/ga l RM

.

New : None

.

indicate s tha

t "floor " facilitie s compris e 2 1 out ofth e tota l o f 17 2 majo r sourc e openmolders

.

1 1 

# 5-4

# EXAMPL E FO RCALCULATIN G MAC T FLOO R- OPEN MOLDIN G FACILITIE S

Ran k 1 2 3 4 S 6 7 8 9 1 0 1 1 1 2 1 3 1 4 1 5 1 6 1 7 1 8 1 9 2 0 2 1 2 2 2 3 24 2 5 2 6 27 2 8 2 9 3 0 3 1 32 3 3 34 "35 ' 3 6 ~37~ ' "3 8 3 9 4 0 Spray s ar t Han d layu p cartme d lis t

Plan t Mam a A R

. E , lnc(Massfflc<i ) US

. Rbenjas s Products Inc

. Resolit e Tompkin s - Lasco Bathwar e (Bizabethtown )
TorrpMn s - Lasco Bathwar e (Lancaster

) AKB * Plastics Company , lnc(Flymouth , Pldco Dr ) a W C Industries , Inc

. (Swirl-Wa y Ov. ) AKB * Plastics Company , lnt(Plymou1h , N Oa k Rd ) Tompkin s - Lasc o Bathwar e (Sout h Boston ) Ceda r(Manufacturing , lnc.(Brema n Sas ) Pickerfe Plasties , Inc

. Breme n Qas , In c Tompkin s - Lasco Bathwar e (Moapa ) Tompkin s - Lasco Bathwar e (Ccrdele) Tompkin s - Lasco Bathwar e (Anaheim ) Tompkin s - Lasco Bathwar e (Three Rivers) Bathcraft , In c Untvereal-ftund e Corp

. (Ottumwa ) Cerami c Coolin g Towe rCompany Tompkin s - Lasco Bathwar e (Ydm ) (ak

a Hytec Inc ) WarminsterFiberglas

s Compan

y (Jacksonville

) WfermrsterFiberglas

s Compan

y (Southampton

) CBIPlart# 7 CO R System

s Corporation (Corcoran) CO R System

s Corporation (Palatka

) Certif y Martiactuin g Compan y Custo m Fireglas s ManUactuin g Co

. National fiber Qas s Products, In c American Reiifum d Plastic s Prestigious Accessories, Ir e Grea t Dane Trailer

s InrJana, In c (FR P Plant ) Acm e Fiberglass , In c Diamond Coac h Corporation Sunse t Plastic s Ir e Bristol fiberlite Industrie

s Hes s Count y Industrie

s o fVW , Ir e Fowle rManufactuing , Inc

. Style Cres

t Product s GW

. fiberglass. In c ProcessDesc Cod e 1 1 13*1 7 1 3 1 1 1 1 1 1 4 1 1 1 1 1 1 1 1 1 1 4 8 + 1 3 1 6 1 6 3 1 1 1 1 1 4 1 1 1 1 3 1 2 1 1 Resi n

Itnrt 5860 2 375. 0 60. 8 2124 8 190. 0 2279. 3 164. 7 300. 0 2310 1 2770 2 367. 0 277. 0 1159. 0 6258. 6 1976 6 3135 5 2815. 4 944. 8 2500. 0 

### na o 2753. 9 121. 0 139. 3 1017. 0 152 0 125. 0 74. 5 553. 0 640. 0 288. 0 432 0 375. 0 185. 0 133. 0 254. 0 247. 0 494. 0 439. 0 B4 0 1850. 0 % Styren

e A s Supplie d 42. 0 46. 0 24 1 47. 7 

### 3a o 47. 7 36. 0 35. 0 36. 0 41 1 38. 0 45. 0 44. 0 47. 0 47. 8 47. 7 47. 7 4 U 46. 5 32 0 47. 8 40. 0 40. 0 43 5 34. 0 34. 0 48 0 44. 9 48 0 40. 7 35 0 39. 0 43. 0 40. 0 43. 0 38 2 35. 0 50. 5 24. 0 45. 0 Fille r

(tart 

### a o ao 11 4 3304. 6 

### ao 3564. 7 180. 5 300. 0 2378. 7 4078. 6 359 4 

### ao 1558. 0 9844. 6 3092 2 4890. 8 4386. 6 986. 9 3276 0 

### a o 4215. 6 

### ao 0. 0 608. 0 0. 0 

### a o 60. 0 266. 0 570. 0 121. 0 0. 0 0. 0 75 0 0. 0 215. 0 0. 0 494. 0 151. 0 

### a o 395. 0 l b styrene

/ oalR M 18 6 42 2 20 3 25 1 34 9 25 1 21 7 21 7 22 1 25 9 23 8 41 3 24 6 24 6 25 1 25 1 25 1 25 2 26 2 29 4 25 4 36 7 36 7 

### a n 31 2 31 2 

### ai s 3.3 5 3.09 31 1 3.2 1 3.58 33 1 3.67 28 1 3.5 1 21 7 39 3 22 0 3.7 5 Application

Factor 1.0 0 1.00 

### as s 1.00 

### as s 1.0 0 1.00 1.0 0 1.0 0 1.0 0 1.0 0 

### a« J 1.00 1.0 0 1.00 1.00 1.0 0 1.00 1.00 

### as s 1.0 0 07 8 tt78 0.55 0.5 5 0.5 5 0.55 0.9 1 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 0.5 5 1.00 1.0 0 VS R Factor 1.00 

### a n 1.0 0 

### ae o ae o O6 0 

### ae o ae o a6 0 0.72 a6 0 06 0 

### ae o 0.6 O 0.6 0 

### ae o 06 0 

### ae o 06 0 1.0 0 a6 4 06 0 0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 0.6 0 06 0 0.6 0 0.6 0 1.0 0 0.6 0 1.0 0 0.72 0.6 0 1.0 0 1.0 0 1.0 0 0.6 0 Control Fi**o c 

### ao s ai 9 1.0 0 07 6 1.0 0 07 8 1.00 1.00 1.00 a7 5 1.00 1.0 0 1.0 0 1.00 1.0 0 1.0 0 1.0 0 1.00 1.0 0 1.0 0 1.0 0 1.0 0 1.00 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.55 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.00 1.0 0 Contro l

Statu s (IbHAP/aalRM l 

### ai 9 04 8 1.1 2 1.1 4 1.1 5 1.1 7 1.30 1.30 1.33 1.39

1.4 7 14 8 14 8 1.50 18 1 15 1 15 1 1.5 7 1.62 1.62 1.7 1 1.7 1 1.7 1 1.7 2 1.7 2 1.7 5 1.8 3 1.8 5 1.8 7 1.9 3 1.9 7 1.9 6 20 2 20 2 21 0 21 7 21 9 22 0 22 5 Curren

t Ents

. (tcv ) 31. 2 5. 0 2 0 116. 1 6 0 128. 0 

### ao 15. 9 126 2 180. 9 21. 2 11. 3 77 4 446 5 143. 3 227. 1 203. 9 59. 1 176 5 4 9 213 5 5 7 6. 6 61. 6 72 5 9 5. 0 34. 3 46 6 17. 8 

### 2a o 20 4 12 1 7. 7 19. 9 14. 3 43 7 30. 8 5. 1 126. 4 MACTEmis

.

(toy ) 31. 2 5. 0 2 0 118. 1 6. 0 128. 0 

### ao 15 5 126 2 180. 9 21. 2 10 9 74 8 43a 8 135. 7 215. 1 193. 0 55. 7 159 5 4 3 187 4 4 8 5 5 51. 3 

### a o 4. 9 4. 1 26, 7 35. 9 

### ia 6 17. 0 14 7 8 7 5. 4 14. 0 9. 7 28. 7 20 1 

### a 3 33. 1 Reduction Technique

s Indnerato r C filters, VS R Han d (100%) Incinerator , VS R VSR , Han d (100%) Incinerator , VS R VS R VS R VS R Incinerator , VS R (72%) VS R VSR , Han d (90%) & Spra y (10%) VS R VS R VS R VS R VS R VS R VS R Han d (100%) VS R (90%) VSR

. Hand & Spra

y VS R Han d & Spra

y Han d (100%) Han d (100%) Har d (100%) Han d (100%) VSR , Han d (20%) VS R VS R VS R Vacuu m baggin g VS R Applie s WroOer s VS R (70%) VS R

Han d (100%)

VS R 

# 12

T l c n

### P.5 7



# Issues : OPEN MOLDIN G (concluded )

Highl y fille dapplication s hav e abuilt-i nadvantag e over unfille dapplication s (lower , ne t styren e conten t

an dhenc e a lowe r contro l statu s factor)

. To p performin g facilitie s consis t mainl y o f

tub/showe r

makers

. Tub/showe r

facilitie s compris e 67 % ofth e 2 1 to p performin g facilitie s an d27 % o f

al l 17 2 know nope nmoldin g facilities

. A s man y a s 86 % o f

ope nmolder s spray applyin g unfille d resin s coul dnee dacontro l devic e t o compl y (assumin g non e coul dswitc hfrom spray applicatio no r begi nusin g filler)

. Industr y (CFA ) claim s add-o ncontrol s for Ne w Sourc e MAC T wil l kil l th e industry

. Industr y want s exemptio nfor corrosion-resistan t

application s becaus e the y believ e add-o ncontrol s ar e th e onl y availabl e complianc e method

. Ho w t o defin e acorrosion-resistan t application ; shoul dthe y hav e adifferent numerica l limit ?
Industr y may wan t

reductio ncredi t

for additiona l measure s (spra y technology , etc.)

.



# Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor : Emission s (tpy) : Percent Reduction : 

# 13 

# S^ 172 9,29 2 Media nC S 5,83 2 37 %

# wr P.5 8



# PULTRUSIO N (5/17 )
MAC T Floors : Existing : media

n% reductio n( = 47% )
o r media nC S valu e ( = 1.2 l

b HAP/gal RM )
New : bes t

% reductio n( = 95% )
or bes t C S valu e ( = 0. 2 l

b HAP/gal RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio no r othe r devic e to achiev e a

t leas t 95 % reductio nor

reduc e C S valu e to les s thanor equa l to 0. 2 lb HAP/gal RM

.

New : None

.

1 4

### P.5 9



# PULTRUSIO N (concluded )

Issues : Industr

y maintain s tha

t facilitie s usin g incinerator s cannot b e considere da s par

t ofth e MACT floo

r fo r thi s subcategor

y becaus e th e incinerator s ar e there due to other

emissio npoints

. Othe r contro l measure s ar

e inus e but

no t included

. Media n(floor ) facilit y ha s a nassume d50 % capture efficiency

. Pultrusio nIndustr

y Council want s rul e to include equipment standard s tha

t they believ e produc e reductions

. "Fum e collector " i s inus e but

n o dataar e availabl e to assig n reductio ncredit

.



# Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 1 7

16 7 Media n% Reductio n 9 9 4 8 % Media nC S

Valu e 6 5 6 1 % •



# 1 5 

# 5^

### P.6 0



# GEL COATIN G (18/150 )
MAC T Floors : Existing : n o numerica

l value *
New : bes t

% reductio n( = 95% )

Option s Abov e th e MAC T Floor : Existing : 1

. Us e low-VO C ge l coats

.

2

. Us e combustio nor

othe r devic e t o achiev e at leas t 95 % reduction

.

New : None

.

*See wor k practice s (pag e 37)

.

1 6

### P.6 1



# Issues : GE L COATIN G (concluded )

Inclusio nof

facilitie s usin g acryli c sheet s inplac e o f gel coatin g woul drequire add-o ncontrol s fo r existin g facilities

. Lackin g facility-specifi c ge l coa t densit y datato set

a l b HAP/ga l gel coa t standard

. Industr y say s canno t

bas e New Sourc e MAC T on A.R.E

. facilit

y (incinerator

onbot hresinandpaintin g operations)

.

Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 15 0

4,34 0 N o Numerica l Valu e 4,34 0 0 %



# 1 7 

# 4 °

### P.6 2



# CONTINUOU S LAMINATION/CASTIN G (5/13 )

MAC T Floors : Existing : median% reductio n( = 49% )

or medianC S valu e ( = 0. 5 l

b HAP/ga l RM )
New : bes t

% reductio n( = 95% )
or bes t C S valu e ( = 0. 2 l

b HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e to achiev e a

t leas t 95 % reductio nor

reduc e C S valu e t o les s thanor equa l to 0. 2 l b HAP/gal RM

.

New : None

.

1 8

### P.6 3



# CONTINUOU S LAMINATION/CASTIN G

(concluded )

Issue :

• Media

n(floor ) facilit y ha s a nassume d50 % captur e efficiency

.

issi onImpacts : No
. of

Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 3

1,12 3 Media n% Reductio n 61 4 45 % Media

nC S Value 39 1 65 %



# 1 9 

# 6*
.

### P.6 4



# FILAMEN T WINDIN G (5/31 )

MAC T Floors : Existing : media

n% HAPContent

a s Supplie d (=42.5% ) (equivalent

t o media nC S valu e o f

3. 9 lb HAP/ga l RM )
New : lowes t

% HAPContent

a s Supplie d( = 33% ) (equivalent

t o C S valu e o f

3. 0 l b HAP/gal RM )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio no r other devic e t o achiev e a

t leas t 95 % reduction

.

2 0

### P.6 5



# Issue : FILAMEN T WINDIN G (concluded )

Man y filament

winder s ar

e usin g corrosion-resistant (CR) resin s andindustr

y claim s nee dfo

r a nexemption

. (Sout hCoas t rul e allow s 48 % monome

r content by weight vs
. 35% ) fo

r general purpos e resins. ) Som e low

styrene CRresin s .ar

e enterin g the m.arket

.

Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 3 1

50 8 Media n% HA P Conten t 47 1 7 %



# 2 1

### P.6 6



# INJECTIO N MOLDIN G

(5/5 )

MAC T Floors : Existing : n o numerica

l value *
New : n o numerica

l value *

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e to achiev e a

t leas t 9 5 % reduction

.

New : Require combustio nor other devic e to achiev e a

t leas t 9 5 % reduction

.

*See wor k practice s (pag e 37)

.

2 2

### P.6 7



# INJECTIO N MOLDIN G (concluded )

Issue :

• Ver

y n«arro w rang e of

C S values ; difficul

t to selec t a floo r value

.

Emissio nImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 5

6 3 N o Numerica l Valu e 6 3 0 %



# 2 3

### P.6 8



# COMPRESSIO N MOLDIN G

(5/42 )

MAC T Floors : Existing : n o numerical value *
New : n o numerical value *

Option s Abov e th e MAC T Floor : Existing : Require combustio no r othe r devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio no r othe r devic e to achiev e a

t leas t 95 % reduction

.

*See wor k practice s (pag e 37)

.

2 4

### P.6 9



# COMPRESSIO N MOLDIN G (concluded )

EmissionImpacts : No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 4 2

35 4 N o Numerica l Valu e 35 4 0 %



# 2 5

### P.7 0



# RESIN TRANSFERMOLDIN G

(5/9 )

MAC T Floors : Existing : n o numerica

l value *

New : n o numerica

l value *

Option s Abov e th e MAC T Floor : Existing : None

.

New : None

.

*See wor k practice s (pag e 37)

.

2 6

### P.7 1



# RESIN TRANSFE RMOLDIN G

(concluded )

issi onImpacts : No
. of

Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 9

5. 7 N o Numerica

l Valu e 5. 7 0 %



# 27

### P.7 2



# COMPOUNDIN G - BM C

(5/11 )

MAC T Floors : Existing : n o numerica

l value *

New : bes t

% reductio n( = 4 9 % )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e t o achiev e a

t leas t 9$i % reduction

.

New : Require combustio nor other devic e to achiev e a

t leas t 95 % reduction

.

'Se e wor k practice s (pag e 37)

.

2 8

11

### P.7 3



# COMPOUNDIN G -BM C (concluded )

Issue :
There ma y b e othe r non-styren e resi ncompound s wit h HAPtha t w e haven' t

considere d(no data)

.

Emissio nImpacts :

No
. o f Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 1 1

4 5 N o Numerica l Valu e 4 5 0 %



# 2 9 2

### P.7 4



# COMPOUNDIN G - SM C

(5/14 )

MAC T Floors : Existing : n o numerical value *

New : bes t

% reductio n( = 7 2 % )

Option s Abov e th e MAC T Floor : Existing : Require combustio nor other devic e to achiev e a

t leas t 95 % reduction

.

New : Require combustio nor other devic e to achiev e a

t leas t 95 % reduction

.

: 

# Se e wor k practice s (pag e 37)

.

30



# 7 3

### P.7 5



# COMPOUNDIN G - SM C (concluded )

iss i o nImpacts : No
. of

Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 1 4

26 8 N o Numerica

l Valu e 26 8 0 %



# 3 1 

# Ti

### P.7 6



# POLYME RCASTIN G (5/19 )

MAC T Floors : Existing : media

nC S valu e ( = 1. 1 l

b HAP/ga l RM )
New : bes t

C S valu e ( = 0. 5 lb HAP/ga l RM )

Option s Abov e th e MAC T Floor : Existing : Reduc e C S valu e t o les s thanor equal t o 0. 5 lb HAP/ga l RM

.

New : None

.

32

r*

### P.7 7



# POLYME RCASTIN G (concluded )

Issue :

• Filler

equit y issu e - som

e facilitie s ma

y no t b e abl e to increas e fille

r usag e to achiev e the floor level

.

Emissio nImpacts : No
. of Facilities : Baselin e Emissions (tpy) : MAC T Floor :

Emission s (tpy) : Percen t Reduction : 1 9

4 6 Media nC S Valu e 3 4 26 %



# 3 3 

# 7 ^

### P.7 8



# CENTRIFUGA L CASTIN G

(5/5 )

MAC T Floors : Existing : media

nC S valu e ( = 0. 4 l

b HAP/ga l RM )
New : bes t

% reductio n( = 50% )
or bes t C S valu e ( = 0. 2 l

b HAP/gal RM )

Option s Abov e th e MAC T Floor : Existing : Reduc e C S valu e to les s thanor equa l to 0. 2 l b HAP/ga l RM , or require combustio nor

other devic e t o achiev e a

t leas t 95 % reduction

.

New : Require combustio nor other devic e to achiev e a

t leas t 95 % reduction

.

34

### P.7 9



# CENTRIFUGA L CASTIN G (concluded)

Issue :

• Assume d50 % captur e efficiency fo

r Fibercas t (likely to b e alo w estimate ) - impact s New Sourc e MACT

.

Emissio nImpacts : No
. of Facilities : Baselin e Emission s (tpy) : MAC T Floor :

Emission s (tpy) : Percent Reduction : 5

9 6 Media nC S Valu e 9 1 5 %



# 35



# " 7 5

# EMISSION S CALCULATION S - EXISTIN G FACILITIE S

- r Subcategor y Ope nMoldin g Ge l Coatin g Continuou s Lamination/Castin g Filamen t Windin g Compressio nMoldin g Compoundin g - SM C Pultrusio n Centrifugal Castin g Injectio nMoldin g Compoundin g - BM C Polyme r Castin g RT M TOTAL S No
. o f Majo rSourc e Facilitie s 17 2

15 0 1 3

3 1
4 2 1 4 1 8 5 5 9 1 9 9 Baselin e Emission s (tpy )

9,29 2 4,34 0 1,12 3

50 8 35 4 26 8 16 7 9 6
6 3
4 5
4 6
6 16,30 7 MAC T Floo r

Emission s (tpy) *

5,83 2 4,34 0 39 1

47 1 35 4 26 8
6 5 9 1
6 3
4 5 3 4
6 11,95 9 Emissio n

Reductio n(tpy) * 3,46 0 (37% ) 0 (0% ) 73 2 (65% )

3 7 (7% ) 0 (0% ) 0 (0% ) 102(61% ) 5 (5% ) 0 (0% ) 0 (0% )
1 2 (26% ) 0 (0% ) 4,34 8 (27% )



# * Value s d o no t

includ e emissio nreduction s du e t o P 2 wor k practices

. 

# 3 6

# POSSIBL E WOR KPRACTIC E STANDARD S

Al l Subcategorie s

- cover s onELAP-containin g vessels , includin g mixer s

- mixer s completely covere ddurin g mixin g

- clea nup spill s immediately
Gel Coatin g andSpra

y Layup

- operator trainin g program
SMC Compoundin g

- us e nylo nfilm(better

vapo r barrier) -fol dedge s o f

SMC
O • Compressio nMoldin g

- reduc e number

o f BM C or SMC "charges " lef

t opento evaporate prior to moldin g Cleanin g

- som e us e o f methylen e chlorid e (Mel ) andother HA Psolvent s reporte d

- useda t about 20 % o f major source s

- mos t facilitie s us e only aceton e or substitute s

- issue: ba

nonMCI us e coul dlea

dto alawsuit

(Woo dFurniture rule ) 3 7

0 0

# APPLICABILIT Y

• Dat abas e include s predominantl y polyeste r an dviny l este r

resin s containin g styren e monome r (an dsom e MMA )

• Othe r

HAP-containin g resin s ar e i nus e (phenolics , epoxies , etc. )

- lo w HA Pcontent s

- primaril y phenol , epichlorohydrin , etc

. s< \- mostl y advanced , high-strengt happlication s (e.g. , aerospace )

~ ~ - n o dat ao nthes e

Issue: Shoul dstandar dattemp t t o cove r al l thermose t

resi nuse ?

3 8

### P.8 3



# WIDES T APPLICABILITY OF TH E STANDARD S

Subcategor

y Ope nMoldin g

Ge l Coating

Cont

. Lamination/Castin g

V 

# Filamen t Winding

CompressionMolding

Compounding - SM

C

Pultrusio n

Centrifuga l Casting ! 

# InjectionMoldin g

Compounding - BMC

Polyme r Casting

RT M Existingor Ne wPlant Existing Ne w Existing New Existing New Existing New Existing Ne w Existing New Existing New Existing New Existing New Existing New Existing Ne w Existing New Polyeste ran d Vinyl EsterPlant

s Onl y X

X X

X X

X

X X All Thermoset

ResinUs e

X

X X

X X X X X X

X X X X X

X X 

# 3 9 

# 1^

# NEX T STEPS

Meetin g withP-MAC T Tea m(Industry , S/L , Wor

k Group )
Assessment

o f Impact s (additional dat agathering ) Beyond-the-Floo r

Analysi s
Possibl e Negotiation s wit

hIndustr y Review/Approval b y Wor k Group/ES D Preparatio no f

Regulator

y Proposa l Framewor

k

40

o o

# NEAR-TER M PROJEC T SCHEDUL E

Mileston e SendMACT floors/options packag e to P-MAC T tea m P-MAC T tea

mmeetin g .o

nMAC T floors/option s Firs t draf t of framework

fo r preambl e andpropose drul e Dat e early Marc h199 6 late Marc h199 6 Jun e 199 6



# LONG-TER

M PROJEC T SCHEDUL E

-A Mileston e

Rul e proposa

l Rul e promulgatio n Date Apri l 199 7 Apri l 199 8

A H date s ar e dependen to navailabilit y o f funding
.



# 4 1

# Ope n Moldin g

?JQl S 1 2 3 4 S 6 7 S 9 1 0 1 1 1 2 1 3 1 4 1 5 1 6 1 7 I t 1 » 2 0 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 B 2 9 3 0 3 1 3 2 3 3 3 4 3 5 3 6 3 7 3 8 3 9 4 0 4 1 4 2 4 3 4 4 4 5 4 8 4 7 4 8 Sprayu p an d Han d layu p combine d lis t



### Pkm t N»m « A.fi.E,lnc(Maselllon ) U.S

. Flbarglaa a Product a Inc

. ReaoIK e TompMn a •Laac o Bathwar e (Bliabethtown ) Coftla44aM4

4 aP y Product ^ In c Tompkin s •Laac o Batftwar a (Lancaatar ) AKE R Plaatlc a Company , lnc.(Plymouth , PIdc o Dr ) S.W.C

. Induatilaa , Inc

. (Swirl-Wa yWv. ) AKE R Plaatlc a Company , lnc.(Plymouth

. N Oa k Rd ) TompMn a •Laac o Bathwar a (Sotit h Boston ) Cada rManufacturing , lnc(Br»me n Glas ) Plckan' a Plaatlca , Inc

. Breme n Glas , In c TompMf4 a •Laac o Bathwar a (Moapa ) TompMn a •Laac o Bathwar a (Cordala ) TompMn a - Laac o Bathwar a (Anahtlm ) TompMn a •Laac o Bathwar a (Thra a Rlvara ) Bathcraft , In c Untvental-Rundl e Corp

. (Ottumwa ) Caraml c Coolin g Towa rCompan y TompMn a •Laac o Bathwar a (Yelm ) (ak a Hyta c Inc ) Warminste rFberglas s Compan y(Jacksonville) Warminste rFberglas s Compan y(Southampton ) CB I Plan t # 7 CD R System s Corporatio n (Corcoran ) CD R System s Corporatio n (Palatka ) Centur yManufacturin g Compan y Ct4tto m Ffereglas s Manufacturin g Co

. Nationa l Fbe rGlas s Products , In c America n Reinforce d Plastic s Prestigiou s Accessories , In c Grea t Dan a Traitor s Indiana

. In c (FR P Plant ) Acm e Ffcerglass , Inc

. Diamon d Coac h Corporatio n Sunse t Plaatlc a In c Bristo l 4

T feorfJt e Industrie s Hes s CountyIndustrie s o fVW , In c Fowle rManufacturing , In c StytoCms t Products 0

. W

. Ftoergtass

. Inc

. (K G Industrie s Lee rEas t Inc

. Gtatstae

. Inc

. PtastJ c Composite s Corporatio n Monarc h Plasti c In c Universa l Plastic s in c Johnso n Truc k

Bodies Proces s Dose

. 

### Cad s

13*1 7

4~

8 4-1 3 1 6 1 6

1 3 1 2

8*1 3

Sknon-Talelac t In c | 1 4 Ras h {__ 6886 2 J78. 0 •0. 6 2124. 8 180. 0 2271. 3 184. 7 300. 0 2310. 1 2770 2 3(7. 0 277. 0 1168. 0 •288. 6 1878. 8 1138 4 2818. 4 944. 8 2500. 0 110. 0 2783. 8 121. 0 139. 3 1017. 0 152. 0 125. 0 74. 5 553. 0 640. 0 288. 0 432. 0 375. 0 165. 0 138. 0 254. 0 247. 0 494. 0 439. 0 S4. 0 1850. 0 127. 9 534. 0 330. 0 100. 0 87. 5 164. 3 390. 0 65. 5 % Styrvn o

A a Sue d tod 42. 0 46. 0 24. 1 47. 7 38. 0 47. 7 36. 0 36. 0 36. 0 48. 1 38. 0 46. 0 44. 0 47. 0 47. 8 47. 7 47. 7 41. 2 46. 6 32. 0 47. 8 40. 0 40. 0 43. 5 34. 0 34. 0 48. 0 44. 9 48. 0 40. 7 35. 0 39. 0 43. 0 40. 0 43. 0 38. 2 35. 0 50. 5 24. 0 45. 0 45. 0 35. 0 3S. 0 40. 0 44. 0 35. 0 35. 0 35. 4 Fille r

(tra ) 0. 0 0. 0 11. 4 3304. 8 0. 0 3864. 7 180. 6 300. 0 2378. 7 407 M 38* 4 

## a o 1868. 0 ••44. 6 3082 2 4880. 8 4388. 6 •86. 6 3276. 0 0. 0 4216. 6 0. 0 0. 0 603. 0 0. 0 0. 0 60. 0 266. 0 570. 0 121. 0 0. 0 0. 0 75. 0 0. 0 215. 0 0. 0 494. 0 151. 0 0. 0 395. 0 0. 0 437. 0 245. 0 40. 0 0. 0 0. 0 0. 0 0. 0 R

) ttyrvns / 

### B8LB M 3.8 8 4 2 2 2.0 3 2.8 1 

## M t 2.6 1 2.1 7 2.1 7 2 * 1 2 4 * 2 4 8 4.1 3 14 6 2 4 8 16 1 2.8 1 2.6 1 1 6 2 2.8 2 24 4 2.8 4 3.6 7 3.6 7 3.1 1 3.1 2 3.1 2 3.1 8 3.3 5 3.0 9 3.1 1 3.2 1 3.5 8 3.3 1 3.6 7 2.6 1 3.5 1 2.1 7 3.9 8 2.2 0 3.7 6 4.1 3 2.3 1 2.3 7 3.0 8 4.0 4 32 1 32 1 32 5 Applicatio n

Efc& t 1.0 0 1.0 0 0.8 6 1.0 0 0.6 6 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.8 6 1.0 0 0.7 8 0.7 8 0.5 5 • 0.5 5 0.5 5 0.5 5 0.9 1 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 0.7 8 0.7 8 0.7 8 0.7 8 0.7 8 VS R 

### Easts* 1.0 0 0. M 1.0 0 0.8 0 0.6 0 0.6 0 0.8 0 0.8 0 0.6 0 0.7 2 0.8 0 0.8 0 0.8 0 0.6 0 0.8 0 0.8 0 0.8 0 0.6 0 0.6 0 1.0 0 0.6 4 0.6 0 0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 0.6 0 0.6 0 0.6 0 0.6 0 1.0 0 0.6 0 1.0 0 0.7 2 0.6 0 1.0 0 1.0 0 1.0 0 0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 Contro l 

### East a 0.0 8 0.1 1 1.0 0 0.7 6 14 0 0.7 8 1.0 0 1XN ) 1.0 0 0.7 8 1.0 0 1.0 0 1.0 0 1.0 0 14 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.S 5 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 8 1.0 0 1.0 0 1.0 0 Contro l

Statu s 18 4 HAP/oa l RM 1 0.1 8 0.4 8 1.1 2 1.1 4 1.1 6 1.1 7 1.3 0 1.3 0 14 3 14 8

14 7 14 8 14 8 1.( 0 1.6 1 14 1 1.8 1 14 7 14 2 14 2 1.7 1 1.7 1 1.7 1 1.7 2 1.7 2 1.75 1.8 3 1.8 5 1.87 1.9 3 1.97 1.9 8 2.0 2 2.0 2 2.1 0 2.1 7 2.1 9 2.2 0 22 5 22 7 2.3 1 2.3 7 2.3 9 2.4 3 2.4 9 Z4 9 2.5 2 Curran t Emis

.



### (tax) 31. 2 6. 0 2. 0 118. 1 8. 0 128. 0 

## ». o 16 4 128 2 1(0 4 21 2 11. 3 77. 4 446 4 143. 3 227. 1 203 4 69. 1 178. 8 4 4 213. 3 5. 7 6. 6 61. 6 7. 2 5. 9 6. 0 34. 3 46. 6 17. 6 23. 0 20. 4 12. 1 7. 7 19. 9 14. 3 43. 7 30. 8 5. 1 126. 4 8. 0 47. 3 29. 2 7. 8 5. 9 11 4 26. 8 4. 5 MAC TEmis

.

(KB ) 3 1 2 6. 0 2. 0 116. 1 6. 0 126. 0

• 4 16 4 126 2 180. 9 21 2 10 4 74. 8 430. 8 138. 7 216. 1 103. 0 88. 7 169. 8 4. 3 167. 4 4. 6 5. 5 51. 3 6. 0 4. 9 4. 1 26. 7 35. 9 13. 6 17. 0 14. 7 8. 7 5. 4 14. 0 9. 7 28. 7 20. 1 3. 3

. 80. 1 5. 0 2 9 2 17. 6 4. 7 3. 4 6. 5 15. 3 2. 6 Reductio n



### IvXrvfun Incinerato r C Altera , VS R Han d (100% ) Incinerator , VS R VSR , Han d (100% ) Incinerator , VS R VS R VS R VS R Incinerator , VS R (72% )

VS R VSR , Han d (80% ) 6 , Spra y (10% )

VS R VS R VS R VS R VS R VS R VS R Han d (100% )

. VS R (80% ) VSR , Han d 6 Spra y VSR , Han d & Spra y Han d (100% ) Han d (100% ) Han d (100% ) Han d (100% ) VSR , Han d (20% ) VS R VS R VS R Vacuu m boggin g VS R Appfl M wffrofl m VS R (70% ) VS R

Han d (100% )

VS R Han d (100% )

Han d & Spra y Han d (50%)

. Va c Ba g (50% ) Han d 8

. Spra y Han d 4 Spra y Han d 4 Spra y 

# Page l

oo c o

# Ope n Moldin g

4 9 5 0 5 1 5 2 5 3 5 4 5 5 5 6 5 7 5 8 5 9 6 0 6 1 6 2 6 3 6 4 6 5 6 6 6 7 6 8 6 9 7 0 7 1 7 2 7 3 7 4 7 5 7 8 7 7 7 8 7 9 6 0 6 1 8 2 6 3 6 4 8 5 8 8 8 7 8 8 8 9 9 0 9 1 9 2 9 3 9 4 9 5 9 6 9 7 9 8 9 9 10 0 Fberglas s Products , In c Universa l Rundl e Corp

. (Unio n Point ) KeameyArVeste m Powe rProducts Blu e Dolphi n Fberglas s Pool s Kohle rCompan y Austi n Countertops , In c Mr

. Tubs , In c Aqu a Glas s Corporatio n Elje rManufacturlngfVeldosta ) Crnrtom a Fiberglass

. Inc

. Ershigs , tne.(Bellirigham ) Carolin a Counter s 20t h CenturyFiberglass , In c (Plan t Four ) M

. C.Gil l Corporatio n An-Co rIndustria l Plastics , In c Beetl e Plastics

. In c Fberglas s Industries , In c Newartesla n Managemen t C o (Artesia n Plumbin g Products ) Gol d Shiel d Fberglas s tn e (Decatur ) Gol d Shiel d Fiberglass , Inc(Fontana ) Clar k Manufacturin g Hasting s Reinforce d Plastlcs-Viate c (Hastings ) Oasi s Industrie s In c Baj a Product s Ltd.(SaHsoury) LaValle y Constructio n Compan y(Biloxl ) Arrowhea d Plasti c Engineering

. In c McCture Industrie s In c MF G - Molde d Fibe rGlas s Compan y(Adalanto ) Kreide rManufacturin g Inc

. Accurat e Glass , In c Eagl e Craft , In c Grayso n Too l Compan y Nordi c Fberglas s lnc(DevD s Lake) Armorcast Product s Compan y Owens-Comin g (Moun t Union ) Owens-Comin g Tank s (Valparaiso ) ACM E Reinforce d Plastics , In c Newpor t Laminate s Marte y Coolin g Towe rCompan y VM C Fberglas s Products , In c /Tri-Gla s Nordi c Fiberglas s lnc(Warran ) Mowe d Plasti c Industries , In c Classi c Moto rCarriage s Comtec h Systems , In c Fbr e Bod yIndustries

. In c MF G Justi n Tanks , In c Continenta l Campe rCompany , In c Grea t Lake s Plastic s Corporatio n A- 1 Fberglass , Inc

. Electric-Glass , Inc

. Murph yBod yCo

. Fberglas s Sytems , Inc

. 1 4

1 1 3 1 2 1 2

1 3 1 3

1 3

1 3

1 3 1 2 1 2

1+ 8

1 2

1 3 120. 0

1410. 0 168. 0
n ' 550. 0 480. 0 137. 0 12000. 0 363. 0 344. 0 104. 5 159. 0 95. 3 79. 0 190. 0 115. 0 60. 0 250. 0 1989. 7 716. 0 681. 0 160. 0 145. 0 100. 0 134. 0 140. 0 140. 0 209. 0 210. 0 114. 0 60. 0 157. 0 316. 2 126. 5
n "
n " 133. 0 180. 0 634. 0 1156. 0 246. 3 102. 0 142. 1 166. 0 250. 0 176. 4 164. 5 306. 0 395. 0 320. 0 114. 7 235. 0 35. 0

40. 0 38. 0 50. 0 40. 0 28. 0 40. 0 43. 0 47. 0 41. 0 38. 5 35. 0 40. 0 57. 4 53. 0 41. 0 41. 0 47. 0 32. 0 32. 0 40. 0 42. 0 49. 0 47. 5 43. 0 43. 0 45. 0 35. 0 33. 7 50. 0 34. 0 34. 0 48. 5 43. 0 45. 0 45. 0 35. 0 35. 0 35. 0 35. 0 48. 5 36. 0 37. 0 37. 0 37. 0 48. 7 38. 0 50. 0 40. 0 42. 0 39 5 49. 0 66. 0

1347. 0 148. 0 0. 0 520. 0 15. 0 110. 0 12000. 0 467. 0 80. 0 0. 0 53. 3 57 2 0. 0 0. 0 0. 0 0. 0 260. 0 0. 0 0. 0 325. 0 0. 0 145. 0 0. 0 0. 0 0. 0 101. 0 20. 0 0. 0 114. 0 0. 0 0. 0 270. 0 62. 5 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 198. 5 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 200. 0 40. 0 45. 0 0. 0 117. 5 2.5 2

2.5 2 2.5 3 4.6 0 2.5 3 2.5 3 2.6 5 2.6 7 2.6 7 3.3 9 3.5 3 2.7 7 2.6 5 6.2 7 4.6 7 3.7 6 3.7 6 2.9 2 2.9 4 2.9 4 2.9 7 3.8 8 3.0 4 4.3 6 3.9 5 3.6 5 3.0 7 3.0 7 3.0 9 3.1 1 3.1 2 3.1 2 3.1 6 3.2 0 4.1 4 4.1 4 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.3 0 3.4 0 3.4 0 3.4 0 4.4 7 3.4 9 3.5 0 3.5 0 3.6 1 3.6 3 3.6 3 1.0 0

1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 8 1.0 0 1.0 0 OS S 0.6 6 0.7 6 0.7 6 1.0 0 1.0 0 1.0 0 1.0 0 0.7 8 1.0 0 1.0 0 0.7 6 0.7 6 1.0 0 ' 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 8 0.7 8 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 6 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.8 0 1.0 0 1.0 0 1.0 0 1.0 0 0.9 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 | 1.0 0 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 | 1.0 0 2.5 2

2.5 2 2.5 3 2.5 3 2.5 3 2.5 3 2.6 5 2.6 7 2.6 7 2.7 1 2.7 4 2.7 7 2.6 5 2.9 0 2.9 0 2.9 2 2.9 2 2.9 2 2.9 4 2.9 4 2.9 7 2.9 9 3.0 4 3 0 5 3.0 6 3.0 6 3.0 7 3.0 7 3.0 9 3.1 1 3.1 2 3.1 2 3.1 6 3.2 0 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.3 0 3.4 0 3.4 0 3.4 0 3.4 6 3.4 9 3.5 0 3.5 0 3.6 1 3.6 3 3.6 3 10. 6

142. 7 17. 9
n * 55. 7 34. 0 13. 9 1305. 5 43. 2 28. 5 7. 9 14. 1 9. 6 6. 3 15. 2 9. 2 6. 4 29. 7 161. 1 58. 0 66. 9 13. 2 18. 0 8. 4 11. 3 11. 8 15. 9 18. 5 17. 9 14. 4 5. 2 13. 5 38. 8 14. 0
n '
n * 11. 8 15. 9 58. 1 102. 4 30. 2 9. 3 13. 3 15. 5 23. 4 16. 7 17. 7 36. 7 40. 0 34. 0 11. 5 29. 1 6. 0

80. 7 10. 1
n * 31. 4 19. 1 7. 4 696. 9 23. 0 15. 0 4. 1 7. 2 4. 8 3. 1 7. 5 4. 5 3. 1 14. 5 78. 2 28. 1 32. 1 6. 3 6. 4 3. 9 5. 3 5. 5 7. 4 8. 6 8. 3 8. 6 2. 4 6. 2 17. 5 6. 2
n *
n * 5. 2 7. 1 24. 9 45. 4 13. 4 4. 0 5. 6 6. 5 9. 6 6. 9 7. 2 15. 8 16. 3 13. 4 4. 5 11. 4 Applie s w/roller s

VS R (50% ) Han d & Spra y

Han d (100% ) VS R (25%)

. Han d (75% ) Spra y (25% )

Han d 4 Spra y Han d & Spra y

Han d 8

. Spra y

VS R (75% ) Han d & Spra y Han d 4 Spra y

Han d & Spra y Han d & Spra y

Han d 4 Spra y



# Pag e 2

o o ^ i

## Ope n Moldin g

10 1 10 2 10 3 104 10 5 10 6 107 10 8 10 9 11 0 11 1 11 2 11 3 11 4 11 5 11 6 11 7 11 8 11 9 12 0 12 1 12 2 12 3 12 4 12 8 12 6 12 7 12 8 12 9 13 0 13 1 13 2 13 3 13 4 13 5 13 6 13 7 13 8 13 9 14 0 14 1 14 2 14 3 14 4 14 5 14 6 14 7 14 8 14 9 15 0 1S 1 15 2 H 6 R Industrie s In c Fberglas s Specialties , In c Florid a Lin e ofAstatula , Inc

. Covermester , Inc

. Fberglas s Forms , Inc

. Livingsto n Ine

. Piedmon t Fberglas s Inc

. Syntachnlc s PlasWabln c HolidayRamble rCorp. , Plan t 3 6 an d 3 7 Millenniu m Products , In c Delt a Fberglas s Structures , In c Kruege rInternationa l In c Lun d Industries

. In c Norlhwaat Bodie s In c UmversaUtundl e Corp

. (Ne wCastle ) Globa l Glass

. In c Standar d Glas , In c Fbordomo , In c -Plan t # 1 Marrajt s Corporatio n SpecialtyPlastic s Associates , In c B*MV*J TMOtO TCOaMn M Mtloho rMflnufMSurin Q Contptn y Inc

. Prodea n Corporatio n (Catawb a Facility) Fbanjass s Engineerin g Corporatio n Owens-Cornin g (Auburndale ) Owens-Comin g Fbergla s (Cornea ) Re d Ewald , Inc

. KB KIndustries Incorporate d GP I Corporatio n Attba rPlastics , In c Fbe rPad , In c Peart Baths , In c Amtoct i Corporatio n Plasti c Developmen t Compan y Iffira/GlaaorLakevill e MF G - Molde d Fbe rGlas s Compan y(Unio n City ) ARE.

. IncfMountEaton ) Aer o Transportatio n Pioduct s AKE R Plastie s Company , In e (Martinsburg ) Aoptacrda n Plastics , In c Associate d Plastics , In c Bettin g Tan k

Technolog y(F.K A D 4 R Fabrication , Inc ) Boaki g Wichit a C 6 KFberglas a Plaatlca , In c CBIPtort#1 1 Concept Plasllca , In e Diamon d Fberglas s Fabricators , In c E D Industrie s tn e (Sportsma n Picku p Covers ) Ersrsgs , IncfVrtson ) FmbtrcMXl

CornpaWi

y Fsbra xCorporatio n 1 3 1 3

1 2 1 2 1 4

1 4

1 4

1 4

1 3 J 1 4

1 4

•11*13*B M 1 2 85. 5

77. 0 130. 6 131. 0 120. 0 612. 0 120. 0 513. 0 92. 0 700. 0 634. 0 295. 0 252. 0 493. 4 147. 3 3585. 0 276. 0 125. 0 100. 0 105. 0 641. 0 181. 5 134. 0 161. 0 75. 0
n *
n " 105. 0 562. 0 129. 0 500. 0 95. 0 325. 0 46. 9 140. 0 154. 0 520. 0 987. 4 1094. 0
n * 62. 0 161. 0
n * 1155. 6 102. 0
n * 707. 7
n "
n " 54. 0 67. 0
n « 48. 0

40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 3 42. 0 40. 7 41. 0 41. 0 41. 0 41. 5 60. 2 42. 0 42. 0 43. 0 44. 0 44. 0 45. 0 45. 0 45. 0 45. 0 45. 0 45. 0 45. 5 46. 0 46. 0 48. 0 48. 0 48. 7 50. 0 50. 0 50. 0 80. 0 34. 0
n 43. 0
n
n
n ' 20. 0
n n * 3Z 0
n '
n n n n 38. 0

0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 56. 0 0. 0 0. 0 0. 0 0. 0 0. 0 3256. 6 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 y k 0. 0 y k 0. 0
n '
n " 0. 0 0. 0
n " y ' n '
n * 0. 0 2 0
n * 3.6 7

3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.7 0 3.7 1 3.7 4 3.7 6 3.7 6 3.7 6 3.8 1 3.8 5 3.8 6 3.8 6 3.9 5 4.0 4 4.0 4 4.1 3 4.1 3 4.1 3 4.1 3 4.1 4 4.1 4 4.1 6 4.2 2 4.2 2 4.4 1 4.4 1 4.4 7 4.5 9 4.5 9 4.5 9 7.3 4
n '
n '
n *
n '
n *
n *
n '
n "
n '
n « n *
n *
n '
n *
n " 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 10 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.7 8
n " 0.7 6 1.0 0 0.7 8 0.5 5 1.0 0 1.0 0 0.5 5 1.0 0 0.7 6 0.7 8 0.5 5 0.5 5 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

0.6 0

1.0 0 10 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 10 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 

## to o 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

1.0 0

1.0 0 3.6 7

3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.7 0 3.7 1 3.7 4 3.7 6 3.7 6 3.7 6 3.8 1 3.8 5 3.8 6 3.6 6 3.9 5 4.0 4 4.0 4 4.1 3 4.1 3 4.1 3 4.1 3 4.1 4 4.1 4 4.1 6 42 2 4.2 2 4.4 1 4.4 1 4.4 7 4.5 9 4.5 9 4.5 9 7.3 4
n '
n "
n '
n *
n '
n *
n "
n *
n *
n *
n '
n "
n "
n *
n * 10. 4

7. 8 13. 2 13. 3 12. 1 51 6 12. 1 51. 9 9. 4 74. 4 85. 9 30. 6 26. 1 51. 2 15. 5 546. 0 29. 3 13. 3 10. 9 11. 7 93. 6 20. 7 15. 3 16. 3 8. 5
n *
n « 12. 1 67. 7 15. 0 60. 7 11. 5 40. 0 5. 9 17. 7 19. 5 105. 2
n "
n '
n *
n *
n '
n *
n *
n "
n *
n '
n *
n '
n *
n '
n * 4. 0

3. 0 5. 1 5. 1 4. 7 20. 1 4. 7 2 0 2 3. 6 28. 6 32. 8 11. 6 9. 9 16. 4 6. 6 202. 0 10. 8 4. 9 3. 9 4. 1 33. 0 7. 1 5. 3 6. 3 2. 9
n *
n ' 4. 1 22. 9 5. 1 19. 6 3. 7 12. 6 1. 8 5. 5 6. 1 20. 4
n '
n "
n '
n *
n *
n *
n *
n '
n *
n *

. n *
n *
n '
n '
n * 

## -

Han d 4 Spra y VS R Han d 4 Spra y

Han d 4 Spra y Han d (100% )

Han d (100% )

Han d 4 Spra y Han d 4 Spra y Han d (100% ) Han d (100% )



# _ 3 Pag e 3

o o o o

# -£ Ope n Moldin g

15 3 15 4 15 5 15 6 15 7 15 8 15 9 16 0 161 16 2 16 3 16 4 16 5 16 6 16 7 16 6 16 9 17 0 17 1 17 2 (mage s Product s Cor p Jone s 6 Hun t In c Lea rMidwes t Miracl e Recreatio n Compan y Newartesla n Limite d Partnershi p (Marbl e Plant ) Owens-Comin g Fbergla a (Bakersfield ) Ranc h Fbarglas , In c Rave n Industries , In c (Siou xFads ) Rubbe r6 Plasti c Applicators S

. R

. Smith , In c Smit h Fiberglas s Product s In c (Littl e Rock ) CB I Plan t * 1 0 CB I Plant * 1 2 CB I Plan t #1 3 CB I Plan t #1 4 CB I Plan t #1 5 CB I Plan t #1 6 Countr yCoach

. In c Glasg o Plastic s In c McClsri n Plastic s Inc

.
Totals : Average : Projecte d Total : 1

1 2 1 1 1 1 2 1 14* 7 1 2 1 1 5 + 1 3 1 1 1 1 3 6 + 1 3 1 2 1 1 1

Bes t performin g 1 2 % o fef t ope n moldin g facilitie s ar e highlighte d i n bol d type

. MAC TFloo r« media n "styren e contro l status " o fto p 12 % (21 ) o

fal l facilitie s • 

## 1 Baselin e emission s •Su m ofactua l curren t calculate d emission s fo rel l facilitie s 109. 0 n ' 600. 0 n ' 1000. 0 n " 342. 0 n * n " n ' n * n ' n ' n " n ' n " n ' 99. 0 n * n '

94152. 9 644. 9 110919. 8

1.4 3 n

n n n ' 34. 0 50. 0 35. 0 n " n 

## • n " n * 46. 0 46. 0 46. 0 n * 50. 0 45. 9 n * n "

6249. 5 41. 1 n "

n 4 500. 0 n ' y * y k y k n ' n " n * n ' n * n ' n " n * n " n ' n ' n * n *

70708. 2 494. 5 85047. 6 n *

n " n ' n " n " n * n * n * n * n * n * 0.5 0 0.4 6 0.4 6 0.4 6 0.4 6 0.5 0 0.4 6 0.4 0 0.5 0

474. 7 3. 3

MAC Temission s * Su m o fcurran t emission s fo rfacilitie s wit h styren e contro l statu s (SCS ) value s equa l t o o rles s tha n th e media n plu s th e su m ofemission s equa l t o (resi n * fiDer)vor*(media n styren e contro l status)*(AP-4 2 midpoin t fo rspraylayup)*(2-3 ) fo reac h fadlit ywit h a SC S valu e greate rtha n th e median

. | II I Therefore , MAC Tcontro l wou M produc e a 37. 2 percen t reductio n i n emission s c fHA P fro m ope n moldin g operations

. n ' •Fadlit ydi d not provid e thi s infonnation

. | y' « FacilityIndicate d th a us e offiller bu t di d no t quantif yth e amount

.
Contro l Statu s Dat a an d AasumrjOons : A R

. E

. ha s a n overal l captur e efficiencyo t 100 % en d e destructio n efficiencyo f95%

. U.S

. Fberglas s Product s ha s a n ovara l captur e efficiencyof90 % an d a destructio n efficiencyo f90%

. Tompkin s - Laac o (Ellzabathtown ) vent s 50 % t o a n Incinerato rwit h a n overal l captur e efficienc yof50 % an d a destructio n efficiencyof98%

. Tompkin s - Lasc o (Lancastar ) vent s 46 % t o a n incinerato rwit h a n overa S captur e efficiencyo f50 % an d a destructio n efficiencyo f98%

. Tompkin s - Lasc o (Sout h Boston ) vant a 50 % t o a n Incinerato rwit h a n overa n captur e effiC4W4C y of50 % an d a destnx ^ efficiericy of98%

. Us e ofVS R fo ral l resin s receive d a 40 % amissio n reductio n credi t | Ifal l ras h i s applie d b y hand , th e faoVty receive d a 45 % emissio n reduction credi t Th a us e ofvacuu m baggin g fo rth e entir e productio n proces s receive d a 45 % emtoslo n reductio n credi t Fille rdensitywa s assume d t o b e 19. 2 b e pa rgallon

. Resi n densit ywa a assume d t o b e 9. 2 b a pe rgallon

.



## _ ^ 2/22/199 6 1.0 0 0.7 6 1.0 0 1.0 0 1.0 0 1.0 0 n " 0.7 8 0.5 5 0.7 8 0.7 8 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.78 - 1.0 0 1.0 0 0.7 6 0.6 0

0.6 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 n *

n * n ' n n n n n n n n n n n n n n n n n

392. 8 2. 7 n '

n ' n * n ' n ' n n n n n n n n n n n n n n n

7131. 2 54. 0 9292. 2

Proces s Descriptio n Codes : 1 » Ge t Coatin g an d Ope n Moldin g 2 •Ge l Coatin g an d Polyme rCoatin g 3 •RTM , Ga l Coating , an d Ope n Moldin g 4 •Compressio n Molding

. Ge l Coating , an d Ope n Moldin g 5 •Injectio n Moldin g | | 6 » Centrifuga l Castin g an d Filamen t Windin g 7 « Centrifuga l Castin g 8 m Puflrusio n n * n ' n * n n ' n n n n n n n' n' n ' n n ' n n n n

4475. 7 33. 9 5832. 0 Han d 4 Spra y

VS R Han d 6 Spra y Han d (100% ) Han d 4 Spra y Han d 6 Spra y VS R

Han d 4 Spra y

Han d 4 Spra y

9 •BMC , Compressio n Molding , an d Puflrusio n 1 0 •SM C an d Compressio n Moldin g 1 1 •Compressio n Moldin g 1 2 •Filamen t Windin g an d Ope n Moldin g 13-Ope n Moldin g 1 4 •Filamen t Winding

. Ga l Coating , an d Ope n Moldin g 1 5 « Compressio n Moldin g an d Filamen t Windin g 1 8 "Polyme rCostin g en d Ope n Moldin g 1 7 •Continuou s Laminatio n



# Pag e 4

# Ge l Coatin g

Ban k
i 2 3 4 S 

## • 7 8 9 1 0 1 1 1 2 1 3 1 4 1 8 1 8 1 7 1 8 1 9 2 0 2 1 2 2 23 2 4 25 2 6 27 2 8 2 9 3 0 3 1 3 2 3 3 3 4 3 5 3 6 3 7 3 8 39 4 0 4 1 4 2 43 4 4 

# I « Plan t nam e
A. R

. R , Inc(Maaalllon ) U.8

. Flberglss s Product a Inc

. Tompkln a - Lasc o Bathwar e (Ellzabathtown ) Tompkin s - Lasc o Bathwar a (Lancaster ) Tompkin s •Lasc o Bathwar e (Sout h Boston ) Styl e Cres t Products A- 1 Fiberglass , In c Breme n Glas , Inc

. Ceda rManufacturing , lnc.(Breme n Glas ) Grea t Dan e Trailer s Indiana , Inc

. (FR P Plant ) Millenniu m Products , Inc

. Prodell n Corporatio n (Catawb a Facility ) Globa l Glass , In c VM C Fiberglas s Products , Inc/Trl-Gla s Classi c Moto rCarriage s Johnso n Truc k

Bodie s Prestigiou s Accesaortaa , Inc

. Fiberglas s Industries , In c Gol d Shiel d Fiberglas s In c (Decatur) UrtTa/GlasofLakevill e A

. R

. E.

. lnc(Moun t Eaton ) Bathcraf l In c MF G - Molde d Fibe rGlas s Compan y(Unio n City) Newartesla n Managemen t C o (Artesia n Plumbin g Product Countr yCoach , Inc

. Beave rMoto rCoache s Pear l Baths , In c 20t h Centur

yFiberglass , Inc

. (Plan t Four ) AKE R Plastic s Company , Inc.(Plymouth ) Attba rPlastics , In c C 4 KFiberglas s Plastics

. Inc

. Kruege rInternationa l In c Picken s Plastics

. In c Plasti c DeveJopment Compan y Aer o Transportatio n Products AKE R Plastic s Company

. In c (Martinsburg ) Centur y Manufacturin g Compan y Ccvexnsntsr , Inc

. Eagl e Craft , tn e Ershigs , lqc(BeUngham )

. Ershigs , IncfWBson ) Hberdome

. Inc.-Plan t # 1 Grea t Lake s Plastic s Corporatio n HoMa y Ramble rCorp. , Plan t 3 6 an d 3 7 iXoNerComparty Proces s Des c 

### Cede

.

1 4 1 4 Resi n



### Any)

1641. 2 23. 6 499. 0 328. 0 468. 0 36. 0 96. 0 369. 0 105. 3 105. 0 167. 0 38. 0 69. 6 291. 0 41. 0 66. 0 64. 0 16. 0 673. 7 41. 0 261. 6 242. 1 102. 0 75. 0 13. 5 

### 0. 5 3. 3 15. 0 33. 7 76. 0 43. 0 61. 7 45. 0 

### 1.0 93. 0 124. 6 25. 5 70. 0 20. 0 

### 3. 5 5. 6 30. 0 80. 0 150. 0 10. 0 % Styren e

A s Supplie d

40. 0 37.6 3 40. 0 40. 0 40. 0 22. 0 30. 0 30. 0 30. 0 30. 0 30. 0 30. 0 30. 0 30. 3 30. 6 30. 6 31. 0 32. 0 32. 0 32. 0 34. 0 34. 0 34. 0 34. 0 34. 6 34. 7 34. 9 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 I b stryene

/ gaIR M

3.6 7 

### 34 6 3.6 7 3.6 7 3.6 7 2.0 2 2.7 6 2.7 5 2.7 6 2.7 6 2.7 6 2.7 6 2.7 6 2.7 6 2.8 1 2.6 1 2.8 5 2.94 2.9 4 2.9 4 3.1 2 3.1 2 3.1 2 3.1 2 3.1 8 3.1 9 3.2 0 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 Contro l

FBCtor

0.0 6 0.1 9 0.6 3 0.6 3 0.6 3 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 Contro l

Statu s (l b sty/pa l RM )

0.1 8 0.6 6 1.9 3 1.9 3 1.9 3 2.0 2 2.7 5 2.7 6 2.7 5 2.7 6 2.7 6 2.7 6 2.7 6 2.7 8 2.8 1 2.8 1 2.8 5 2.9 4 2.9 4 2.9 4 3.1 2 3.1 2 3.1 2 3.1 2 3.1 8 3.1 9 3.2 0 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 Curren t Emis

.

rjpy i

21. 6 

### 1.2 73. 6 48. 3 68. 6 

### 5. 4 20. 0 77. 6 22. 2 22. 1 36. 1 

### 8. 0 14. 6 61. 8 

### 8. 8 13. 9 13. 9 

### 3. 4 151. 2 

### 9. 2 62. 4 57. 7 24. 3 17. 9 

### 3. 3 0. 1 0. 8 3. 7 8. 3 19. 4 10. 8 15. 1 11. 0 

### 0. 2 22. 8 30. 6 

### 6. 3 17. 2 

### 4. 9 0. 9 1. 4 7. 4 19. 6 36. 8 

### 2. 5 MAC TEmis

.



# and

21. 6 

### 1.2 73. 6 48. 3 68. 6 

### SA 20. 0 77. 6 

### 22 J 22. 1 36. 1 

### 8. 0 14. 6 61. 8 

### 8. 8 13. 9 13. 9 

### 3. 4 151. 2 

### 9. 2 62. 4 57. 7 24. 3 17. 9 

### 3. 3 0. 1 0. 8 3. 7 8. 3 19. 4 10. 6 15.1 11. 0 

### 0. 2 22. 8 30. 6 

### 6. 3 17. 2 

### 4. 9 0. 9 1.4 7. 4 19. 6 38. 8 

### 2. 5 Reductio n

Techniqu e
Incinerato r C filter , VSGelcoa t Incinerato r Incinerato r Incinerato r
VSGelcoa t appl

. w/brush , VSGelcoa t

applie s wit h brus h

Acryli c sheet s als o



# *5 >

- 0 Page l 

# I

# •B Ge l Coatin g

4 6 4 7 4 8 4 9 5 0 5 1 5 2 5 3 5 4 5 5 5 6 5 7 5 8 5 9 6 0 6 1 6 2 6 3 6 4 6 5 6 6 6 7 6 8 6 9 7 0 7 1 7 2 7 3 7 4 7 5 7 6 7 7 7 8 7 9 6 0 8 1 8 2 8 3 8 4 8 5 8 6 8 7 8 8 8 9 9 0 9 1 9 2 9 3 9 4 9 5 LaValleyConsbuctio n Compan y(Biioxi ) Lee rEas t In c Lee rMidwes t McClart n Plastic s In c Melche rManufacturin g Compan yInc

. Molde d Plasti c Industries , Inc

. Piedmon t Fiberglas s In c Ranc h Fiberglas , In c Simon-Teleiect In c Standar d Glas , Inc

. Universa l Plastic s In c Universa l Rundl e Corp

. (Unio n Point) UniversaJ-Rundl e Corp

. (Ne wCastle ) Nordi c Fiberglas s lnc(Devil s Lake ) Nordi c Fiberglas s lnc.(Warren ) America n Reinforce d Plastic s Northwest Bodie s In c Oasi s Industrie s In c Elje rManufacturtng(Valdosta) Florid a Un a o fAstatula , In c GP I Corporatio n Kretde rManufacturin g In c Newpor t Laminate s Sunset Plastic s Inc

. Arrowhea d Plasti c Engineering , Inc

. Accurat e Glass , In c KB KIndustrie s Incorporate d Monarc h Plasti c Inc

. Nationa l Fibe rGlas s Products , Inc

. Fibre Bod yIndustries , Inc

. H & R Industrie s In c Livingsto n In c Plasti-Fa b Inc

. Lun d Industries , Inc

. Aqu a Glas s Corporatio n Chariom a Fiberglass , In c Gol d Shiel d Fiberglass

. Inc(Fontana ) Applachla n Plastics , In c Associate d Plastics , In c (^temporar y Products , Inc

. Rave n Industries , lnc(Sfou xFalls ) linage s Products Cor p Plasti c C43rnposite

s Corporatio n Betdln c CBIP U Tan k

Technolog y(F.ICA

. D & R Fabrication , Inc. ) int*1 0 CB I Plan t #1 3 CB I Plan t 81 1 Diamon d Fiberglas s Fabricators , Inc

.E-TM Enterprises , In c E D Industrie s In c (Sportsma n Picku p Covers ) 1 I

1

1 4

1 4

3 3

1 4 3 3 6 * 1 1 4 1 4 1 1



## ... . 1 4 RT M + Gel 1 4. 9 |

.;; : i24*'-'.- ' 200. 0 ..;-:i24.6"y

y 14. 0 49. 0 2. 3 70. 8 24. 0 15. 0 46. 6 300. 0 607. 5 23. 5 13. 5 56. 0 22. 8 16. 2 93. 0 50.1 15. 0 102. 0 30. 0 50. 0 28. 9 37. 0 9. 0 13.1 3 167. 3 70. 0 5. 0 60. 0 20. 5 111. 4 1170. 0 86. 0 158. 0 2. 0 12. 5 42. 0 9. 5 30. 0 15.0 0 124. 6 124. 8 124. 6 124. 6 124. 6 124. 6 124. 6 35. 0

35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 0 35. 2 35. 5 36. 0 36. 0 36. 0 36. 0 36. 0 36. 0 36. 0 36. 0 36. 0 36. 6 37. 0 37. 0 37. 0 37. 0 37. 0 37. 0 37. 0 37. 4 37. 4 37. 5 37.5 3 37.5 3 37.6 3 37.5 3 37.5 3 37.5 3 37.5 3 37.5 3 37 A 37. 6 37. 6 37. 6 37. 6 37. 6 37. 6 3.2 1

3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.21 ' 3.2 1 3.2 1 3.2 1 3.2 3 3.2 6 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 6 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 3 3.4 4 3.4 4 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.45 " 3.4 5 3.4 5 3.4 5 1.0 0

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 

## i.bo 1.0 0 1.0 0 1.0 0 3.2 1

3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 1 3.2 3 3.2 6 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 0 3.3 6 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 0 3.4 3 3.4 4 3.4 4 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 5 1. 2

30. 6 49. 1 30. 6 3. 4 12. 0 0. 6 17. 4 5. 9 3. 7 11. 4 73. 6 149. 1 5. 8 3. 4 14. 1 5. 7 4. 1 23. 5 12. 7 3. 8 25. 8 7. 6 12. 6 7. 4 9. 6 2. 3 3. 4 43. 4 18. 2 1. 3 15. 6 5. 4 29. 2 307. 7 22. 6 41. 6 0. 5 3. 3 11. 1 2. 5 7. 9 3. 9 32. 8 32. 8 32. 8 32. 8 32. 8 32. 8 32. 8 1. 2

30. 6 49. 1 30. 6 3. 4 12. 0 0. 6 17. 4 5. 9 3. 7 11. 4 73. 6 149. 1 5. 8 3. 4 14. 1 5. 7 4. 1 23. 5 12. 7 3. 8 25. 6 7. 6 12. 6 7. 4 9. 8 2. 3 3. 4 43. 4 16. 2 1. 3 15. 6 5. 4 29. 2 307. 7 22. 6 41. 6 0. 5 3. 3 11.1 2. 5 7. 9 3. 9 32. 8 32. 8 32. 8 32.8 ' 32. 8 32. 8 32. 8 

## •



# Pag e 2

T J CO

# Ge l Coatin g

9 6 9 7 9 8 9 9 10 0 10 1 10 2 10 3 10 4 10 5 10 6 10 7 10 8 10 9 11 0 11 1 11 2 11 3 11 4 11 5 11 6 11 7 11 8 11 9 12 0 12 1 12 2 12 3 12 4 12 5 12 6 12 7 12 8 12 9 13 0 13 1 13 2 13 3 13 4 13 5 13 6 13 7 13 8 13 9 14 0 14 1 14 2 14 3 14 4 14 5 Genera l Marbl e Compan y(Guasti ) Genera l Marbl e Compan y(Homed ) Genera l Marbl e Compan y(Uncolnton ) GlasstJte , In c Miracl e Recreatio n Compan y 6

. R

. Smith , Inc

. Universal-Rundl e Corp

. (Ottumwa ) Fibe rPad , Inc

. Murph yBodyCo

. Cerami c Coolin g Towe rCompan y Fiberglas s Sytems , Inc

. Tompkin s - Lasco Bathwar e (Anaheim ) Blu e Dolphi n Fiberglas s Pool s Comtec h Systems , Inc

. Continenta l Campe rCompany , In c Custo m Fibreglas s (Manufacturin g Co

. Delt a Fiberglas s Structures , In c Diamon d Coac h Corporatio n Fiberglas s Forms , In c Fiberglas s Products , Inc

. Fiberglas s Specialties , in c G

. W

. Fiberglass

. Inc

. Glasg o Plastic s In c Grayso n Too l Compan y Maile y Coolin g Towe rCompan y MF G - Molde d Fibe rGlas s Compan y(Adelanto ) Newartesla n Limited Partnershi p (Marbl e Plant ) Re d Ewald , In c Syntechnic s Tompkin s - Lasco Bathwar e (Cordele ) Tompkin s - Lasc o Bathwar e (Moapa ) Tompkin s - Lasc o Bathwar e (Thre e Rivers ) Tompkin s •Lasco Bathwar e (Yelm ) (aka Hyte c Inc ) Unite d Pane l In c VVarminste rFiberglas s Compan y(Jacksonville) VVairninsta rFiberglas s Compan y(Southampton ) Acm e Frbergtass , In c ACM E Relnforoe d Plastics

. In c KeatTiey/VVesle m Powe rProducts Bristo l Fibertt e Industries MarbeHts Corporatio n Austi n Countartops , In c Fiberglas s Engineerin g Corporatio n S.VV.C

. Industries , In c (Swirl-WayDiv. ) Carolin a Counters Upper ! Corporatio n SchrrWrrlarblef'roduct s Nova Enterprises , In c Superio rHom e Products

a\*mttt*\%%\s*t\Ats

sf * m .*m m mma\ m *%\ •jiwc n corporatio n 2 2 2

1 * 8

1 4

- •• —

1 7 +Ge l 1 4 4 4 1 1 2 1 1 1 1 2 + RT M 2 2 2 1 124 6

12 4 6 12 4 6 124. 6 124. 8 124. 6 59 3 0 20. 0 17.2 1 17. 6 77. 0 616. 0 124. 6 27. 0 72. 5 124. 0 23. 0 24. 0 6. 0 30. 0 20. 0 113. 7 .::::;j124>8:sy ; 45. 0 110. 0 46. 0 135. 0 11. 0 140. 0 405. 0 1596. 0 580. 0 525. 0 22. 0 30. 0 37. 3 37. 5 21. 0 42. 0 15. 8 20. 0 26. 0 13. 5 0. 3 10. 5 60. 0 50. 0 13. 0 39. 0 17. 3 37. 6

3 7 6 3 7 6 37. 6 37. 6 37. 6 38. 0 38. 8 39. 1 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 40. 0 41. 4 43. 0 45. 0 45. 0 45. 0 45. 0 45. 0 45. 0 47. 0 48. 0 50. 0 3 4 5

34 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 9 3.5 6 3.5 9 3.6 7 3.6 7 3.6 7 3.6 7 3.8 7 3.8 7 3.8 7 3.8 7 3.8 7 3.8 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.8 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.8 7 3.6 7 3.8 0 3.9 5 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.3 1 4.4 1 4.5 9 1 0 0

10 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 3 4 5

34 5 3.4 5 3.4 5 3.4 5 3.4 5 3.4 9 3.5 6 3.5 9 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.8 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.6 7 3.8 0 3.9 5 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.3 1 4.4 1 4.5 9 3 2 8

32. 8 32. 8 32. 8 32. 8 32. 8 158. 0 5. 4 4. 7 4. 9 21. 6 172. 8 35. 0 7. 8 20. 3 34. 8 6. 5 6. 7 2. 2 8. 4 5. 8 31. 9 35. 0 12. 6 30. 9 12. 9 37. 9 3. 1 39. 3 113. 6 447. 7 162. 7 147. 3 6. 2 8. 4 10. 5 10. 5 5. 9 11. 8 4. 5 6. 0 8. 2 4. 3 0. 1 3. 3 18. 9 15. 8 4. 3 13. 1 6. 1 3 2 8

32. 8 32. 8 32. 8 32. 8 32. 8 158. 0 5. 4 4. 7 4. 9 21. 6 172. 8 35. 0 7. 6 20. 3 34. 8 6. 5 6. 7 2. 2 8. 4 5. 6 31. 9 35. 0 12. 6 30. 9 12. 9 37. 9 3. 1 39. 3 113. 6 447. 7 162. 7 147. 3 6. 2 8. 4 10. 5 10. 5 5. 9 11. 8 4. 5 6. 0 8. 2 4. 3 0. 1 3. 3 18. 6 15. 8 4. 3 13.1 6. 1 Applie s wit h roller s

Applie s wit h roller s

VSGelcoa t



# _ o Pag e 3

e o r o

# f
Ge l Coatin g

14 6 14 7 14 8 14 9 150 Internationa l Marbl e Inc

. 2 Marbtocas t Products In c Partheno n Marbl e Products Inc

. Rynon e Manufacturin g Corporation-Sayre Plan t Came o Marbl e
Tota l Averag e Projecte d Tota l fo r15 0 facilitie s 

### 2 2 2 2 10 0

124 6 35. 6 50. 0 j47. 2

16323. 4 124. 6 18690. 9

Bes t performin g 1 2 % ofai l compoundin g facilitie s are highlighte d i n bol d type

. MAC TFloor •media n "styren e contro l statusl " ofto p 12 % (18 ) ofal l facilitie s « 

## I I Baselin e emission s = Su m o factua l curren t calculate d emission s fo ral l facilitie s 50. 0 50. 0 50. 0 50. 0 55. 0

5146. 4 37. 6

n o contro l 4.5 9 1.0 0 4 5 9

4.5 9 4.5 9 4.5 9 5.0 5

450. 9 

### 3.4 516. 3 1.0 0

1.0 0 1.0 0 1.0 0 4.5 9

4.5 9 4.5 9 5.0 5

505. 8 

### 3. 9

(MACTemission s « Su m o fcurren t emission s fo rfacilitie s wit h styren e contro l statu s (SCS ) value s equa l t o o rles s tha n th e media n SC S valu e plu s th e su m ofemission s equa l t o (resin)vol*(l b sty/ga l RM)*(media n styren e contro l statu s value)*(0.7013 ) fo reac h facilit

y"wit h a SC S valu e greate rtha n th e median

. Therefore , implementin g MAC Twoul d produce a 0 percen t reduction I n emission s ofHA P fro m compoundin g operations

. Contro l Statu s Dat a an d AtsumptJoni ; A

. R

. E

. ha s a n overal l capture efficiencyo f100 % an d a destructio n efficiencyo f95%

. U.S

. Fiberglas s Products ha s a n overal l capture efficienc yo f90 % an d a destructio n efficienc yo f90%

. Tompkin s - Lasco (Elizabethtown ) vent s 50 % to a n incinerato rwit h a n overal l capture efficiencyof50 % an d a destructio n efficiencyo f98%

. Tompkin s - Lasc o (Lancaster) vent s 46 % t o a n incinerato rwit h a n overal l capture efficienc yo f50 % an d a destructio n efficiencyof98%

. Tompkin s •Lasc o (Sout h Boston ) vent s 50 % to a n incinerato rwit h a n overal l capture efficienc yof50 % an d a destructio n efficiencyof98%

. ;iG4iw^l**>wur444^ ; ^ues - — y •• 

## I I I Fille rdensit

ywa s assume d t o b e 19. 2 lb s pe rgallon

. Resi n densit ywa s assume d t o b e 9. 2 lb s pe rgallon

.

1 » Ge l Coatin g an d Ope n Moldin g 2 = Ge l Coatin g an d Polyme rCastin g 3 = RTM , Ge l Coating , an d Ope n Moldin g 4 •Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 •Injectio n Moldin g 6 « Centrifuga l Castin g an d Filamen t Windin g 7 •Centrifuga l Castin g 8 "Pultrusio n
2/22/9 6 

## | Proces s Descriptio n Codes ;

9 •BMC , Compressio n Molding , an d Pultrusio n 1 0 = SM C an d Compressio n Moldin g 1 1 = Compressio n Moldin g | 1 2 = Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Moldin g | j 1 4 = Filamen t Winding , Gel Coating , an d Ope n Moldin g 1 5 = Compressio n Moldin g an d Filamen t Windin g 1 6 = Polyme rCastin g an d Ope n Moldin g 1 7 = Continuou s Laminatio n 

## I I 3 5 , 43. 7 12. 5 17. 5 18. 2

4339. 6 33. 1 

### 3.5

43. 7 12. 5 17. 5 18.2 '

4339. 6 33. 1 • - -



## Pag e 4

T J CO CO

## Polyme rCastin g

Ban k 1 2 3 4 6 6 7 8 8 1 0 1 1 1 2 1 3 1 4 1 5 1 8 1 7 1 8 1 6



# _ Plan t Nam e Upper t Corporatio n Came o UrUrtol

e Schmlt t Marbl e Product s Internationa l Marbl e Inc

. Nov a Enterprises , Inc

. Marbeiit e Corporatio n CD R System s Corporatio n (Paiatka ) Superio rHom e Products Co rTe c Compan y Partheno n Marbl e Products Inc

. CD R System s Corporatio n (Corcoran ) Genera l Marbl e Compan y(Guasti ) Genera l Marbl e Compan y(Homed ) Genera l Marbl e Compan y(Lincolnton ) Marblecas t Products Inc

. CB I Plan t 8 4 Fsbal l Enterprise s ofUtah , Inc

. (se e Atec ) Rynon e Manufacturin g Corporation-Sayre Plan t Structura l Nort h Americ a
Tota l Averag e Projecte d Tota l Proces s Desc

.



## Cod a 2 +RT M 2 2 2 2 2 1 6 2 1 7 + Pol

. Cas t 2 1 6 2 Resi n



## asui 666. 9 433. 8 34. 6 145. 0 111. 0 228. 0 457. 0 448. 0 2100. 0 303. 0 351. 0 % Styren e

A s SuDplied 27. 2 29. 0 35. 0 33. 0 33. 0 30. 0 32. 7 32. 6 33. 0 35. 0 32. 7 Fille r 

# am 6059. 0 1353. 5 138. 4 600. 0 330. 0 561. 0 1147. 0 1076. 0 776. 0 789. 0 726. 0 I b stryene / gaIR M 0.5 3 1.0 7 1.1 0 1.1 4 1.2 6 1.2 7 1.3 6 1.3 9 2.5 7 1.4 3 1.5 1 423. 7 34. 0 909. 0 1.5 4 2 423. 7 34. 0 909. 0 1.5 4 VS R Eacjg x 1. 0 0. 6 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 2 423. 7 34. 0 909. 0 1.5 4 1. 0 2 423. 7 34. 0 909. 0 1.5 4 1. 0 Pol

. Cast

. 423. 7 34. 0 cb i 5 •Pol

. Cas t 2 Pol

. Cast

.

—• • - -

• - • To p 5 performin g facilitie s ar e highlighted i n bol d type

. (MAC TFloo r•media n "styren e contro l status " o fto p 5 facilities = 

# 1 238. 1 409. 2 16. 5

5932. 1 423. 7 8050. 7

Baselin e emission s = Su m ofactua l curren t calculate d emission s fo ral l facilitie s 39. 5 40. 0 43. 2

475. 9 33.9 9

MAC Temission s = Su m o fcurren t emission s fo rfacilities wit h styren e contro l statu s (SCS ) value s eq u th e su m o

femission s equa l t o (resi n * filler)vol*(l b s t Therefore , implementin g MAC Twoul d produce a 26

. Emissio n Reductio n Dat a an d Assumptions ; y/ga l RM)*(media n S ( 2 percen t reductio n i n



# - : S value)*(> emission s

A 4 0 % emissio n reductio n credi t wa s give n (o rth e us e o fvapo rsuppresse d resin

. Facilitie s usin g Vacuu m baggin g receive d a 45 % e m Grey cell s = assume d value s Fine rdensit

ywa s assume d to b e 19. 2 lbs pe rgallon

.

1 = Ge l Coatin g an d Ope n Moldin g 2 = Ge l Coatin g an d Polyme rCastin g 3 = RTM

. Gel Coaling , an d Ope n Moldin g 4 = Compressio n Molding , Gel Coating , an d Ope n M 5 = Injectio n Moldin g 6 = Centrifuga l Castin g an d Filamen t Windin g 7 = Centrifuga l Castin g 8 •Pultrusio n 02/13/199 6 ssio n reductio n credi t

Resi n densit

ywa s a 164. 1 105. 0 0. 9

12725. 9

" 909. 0 17270. 9 18 0

2.7 3 "'" " 3.2 7 3.6 6

32. 5 ' 2 2

i

i7i o

l 1. 0 "1. 0 " 1. 0 1. 0



# —... .

... - 

# . _ a l to o rles s tha n th e media n SC S valu e \P-4 2 midpoint

) fo reac h facilit

ywit h a SC S valu e greate r o fHA P fro m polyme rcastin g operations

. j



## _I i

ssume d t o be 9. 2 lb s pe rga l

Proces s Descriotio n Codes :

oldin g

•- •• - 

# •- : :• . ';•.[•

. '

on . 

# : :
9 = BMC , Com p 1 0 = SM C an d C ressio n Molding , an d Pultrusio n

ompressio n Moldin g 11 = Compressio n Moldin g 1 2 = Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Mol d 1 4 = Filamen t W 1 5 = Compres s i i 1 6 = Polyme rC

< ing tnding

. Ge l Coating , an d Ope n Moldin g i n Moldin g an d Filamen t Windin g islin g an d Ope n Moldin g 1 7 * Continuou s Laminatio n "Contro l Facto r 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 0.5 5 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 

## Too " 1 d o 1.0 0 1.0 0

plu s tha n th e r

r



# - Contro l

Statu s (Ibstv/oalRM ) 0.5 3 0.6 4 

## li^Tiio'Slis ? 1.1 4 1.2 5 1.2 7 1.3 6 1.3 9 1.4 2 1.4 3 1.5 1 1.5 4 1.5 4 1.54 V5 4 

## Te o 2.7 3 ' " 3.2 7 3.8 6

30.8 7 1.6 2



# -

ledia n Curren t Emis

.



# am 3.6 7 1.5 1 0.2 4 0.9 6 0.7 3 1.3 7 2.9 9 2.9 2 7.6 2 2.1 2 2.3 0 MB:?-:-:
- 2.8 8 2.8 8 2.8 8 2.8 8 1.8 8 3.2 7 0.1 4

46.0 3 2. 4



# . MAC TEmis

.

fltryj 3.5 7 1.5 1 0.2 4 0.9 2 0.6 5 1.1 9 2.4 2 2.3 1 5.9 4 1.6 3 1.6 8 2.0 6 2.0 6 2.0 6 2.0 6 1.7 7 ' 0.7 6 1.1 0 0.0 4

33.9 9 1. 9

• Reductio n

Technique s
VS R (100% )

Vac

. Ba g

••• -



# -

. :

-

- •



## Pag e 1

T J CO

## Pultrusio n

Ban k 1 2 3 4 5 6 7 8 9 1 0 1 1 1 2 1 3 1 4 1 5 1 8 1 7 1 8

i



## ; P|antjiam e Endur o Fiberglas s (formerl yW

. R

. Grace ) Tscto n (Fargo ) CB I Plan t # 6 Clasti c Corp.(8out h Euclid ) Industria l Dielectric s Hayslte Reinforce d Plastic s CB I Plan t # 7 Creative Pultruslons , In c (Alu m Bank ) Carsonite Internationa l Corporatio n Dom-Fa b (DF I Puttrude d Composites ) Shakespear e Compan y Omeg a Pultruslon s Incorporate d Enduro Fiberglas s Systems , In c R

. 0

. Werne rCompany , In c Martey Coolin g Towe rCompan y IK G Industrie s Glasforms , In c Flberftex , In c
Tota l Averag e Projecte d Tota l Proces s Desc

. Cfidf l 1 7 + 8


### 8 9 9 +SM C 9 •SM C •1 7 8 + 1 3 

### 8 8 + 1 1 

### 8 8 •Rl

. Wind

. 

### 8 RTM+1 1 + 8 

### 8 1+ 8 8 + 1 3 

### 8 8

To p 5 performin g facilitie s ar e highlighted i n bol d type

. MAC TFloo r= media n "contro l statu s factor " ofto p 5 facilitie s = 

## 1 Resi n



# am 62 472. 0 472. 0 472. 0 49. 0 42. 5 55. 5 1560. 0 554. 0 144. 0 200. 0 1269. 0 390. 0 1744. 0 117. 0 207. 2 256. 0 440. 0

7080. 2 472. 0 8024. 2

Baselin e emission s •Su m ofactua l curren t calculate d emission s fo ral l facilities

. % Styren e A s Suoolie d 41.2 1 45.0 0 41. 3 

### 41 4 40. 7 41. 0 43. 5 35. 0 40. 0 41. 3 42. 0 42. 6 44. 0 40. 0 40. 0 41. 6 41. 5 45. 0

619. 3 41. 3 Fille r

(toy) 

### 6 168. 6 

## n 165. 5 70. 0 54. 0 33. 1 62. 0 190. 0 45. 0 70. 1 408. 0 117. 0 76. 0 

### 0. 0 0. 0 0. 0 60. 5

1121. 6 80. 1 1442. 1

1.1 6 l b styrene

/ 

### galB M 3.685284 1 3.5 4 2.2 0 3.2 5 2.2 2 2.3 4 3.1 1 3. 1 S 3.1 5 3.3 0 3.3 0 3.3 9 3.5 3 3.6 0 3.6 7 3.8 1 3.8 1 3.8 8

58. 8 Contro l



### EaEto x 0.0 5 0.0 5 0.5 3

1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

15. 2

MAC Temission s * Su m ofcurren t emission s fo rfacilitie s wit h contro l statu s (CS ) value s equa l to o rles s tha n th e media n plu s Contro l Statu s (Ibstv/oalRM ) 0.17926420 4 0.1 8 1.1 6 1.7 9 2,2 2 2.3 4 3.1 1 3.1 5 3.1 5 3.3 0 3.3 0 3.3 9 3.5 3 3.6 0 3.6 7 3.8 1 3.8 1 3.8 8 Curren t Emis

. 

# am 0.0 8 0.5 8 5.6 3 5.9 0 1.1 0 0.9 6 1.3 3 30.0 3 12.1 9 3.2 7 4.6 2 29.7 3 9.4 4 38.3 7 2.5 7 4.7 3 5.8 4 10.8 9

167. 2 

### 9. 3

th e su m o femission s equa l t o (resi n •filler)vol*(1b sty/ga l RM)*(media n C S value)*(AP-4 2 midpoint ) fo reac h facilit

ywit h a C S valu e greate rtha n th e median

. 

## 1 lll l Therefore , implementin g MAC Twoul d produce a 61. 0 percen t reductio n i n emission s ofHA P fro m pultrusio n operations

. 

### Emissio n Reductio n Dat a an d Assumptions ; Endur o Fiberglas s vent s 100 % t o Incinerator , whic h ha s 100 % capture an d 85 % destructio n efficiency

. Di e resi n injectio n receive d n o emissio n reduction credi t | CB I Plan t # 5 ha s a n ovara l capture o f50 % an d a 95 % destructio n efficiency

. Glasti c Corp

. vtrtt s 100 % to carbo n filter , whic h ha s 90 % capture an d 90 % destructio n efficiency

. R

. P

. Werner' s fum e oolBClo rreceive d n o emissio n reductio n credi t | J Facilitie s wit h a temperature controlle d environmen t received n o emissio n reduction credi t Cover«oV4»nclc«edrsslnsrea s received r » ensssio n reductio n credi t | | FBe rdensit

y wa s assume d t o b e 19. 2 lb s pe rgallon

. Resi n densit y wa s assume d t o b e 9. 2 lb s pe rgallon

.



## . ' MAC TEmis

. 

# am 0.058930 3 0.6 8 S.6 3 6.9 0 0.5 7 0.4 7 0.4 9 11.0 0 4.4 6 1.1 5 1.6 2 10.1 3 3.0 9 12.3 2 0.8 1 1.4 3 1.7 7 3.2 4

64. 7 

### 3. 6 Reductio n 

### Technique s Incinerator , di e i s resin injecte d

Incinerato r Incinerato r C Alter , covered/enclose d resi n bat h

Temperatur e controlle d env . Temperatur e controlle d env .

Covered/enclose d resi n bat h

Fum e collector , Temp , controlle d env .

covered/enclose d resi n bat h Temperatur e controlle d env .



## Page l

CO c n

# - &

. Pultrusio n

1 •Ge l Coatin g an d Ope n Moldin g 2 » Ge l Coatin g an d Polyme rCastin g 3 » RTM , Ge l Coating , an d Ope n Moldin g Proces s Descriotio n Codes :

4 « Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 « = Injectio n Moldin g 6 •Centrifuga l Castin g an d Filamen t Windin g 7 •Centrifuga l Castin g 8 •Pultrusio n
2/22/9 6 

# I I I 9 = BMC , Compressio n Molding , an d Pultrusio n 1 0 = SM C an d Compressio n Moldin g 1 1 = Compressio n Moldin g 12 » Filamen t Windin g an d Ope n Moldin g 1 3 - Ope n Moldin g | | 1 4 * Filamen t Winding , Gel Coating , an d Ope n Moldin g 1 5 •Compressio n (Moldin g an d Filamen t Windin g 1 6 " Polyme rCastin g an d Ope n Moldin g | 17 » Continuou s Laminatio n

1 1 

# 1

Pag e 2

# Continuou s Lamination , Castin g

Ban k 1 2 3 4 6 i 6 

### 7 8

•9 

### 1 0 1 1 1 2 1 3



## < Plan t nam e Endur o Fiberglas s (formall yW

. R

. Grace ) Co rTe c Compan y CB I Plan t # 4 Cran e Kemllt e (formerl yB P Chemicals ) Resettl e Haysit e Reinforce d Plastic s Keml'rt e Co. , In c Unite d Pane l Inc

. Tompkin s - Lasc o Pane l Products (KY ) Kalwaf l Corporatio n SequentJa

. Inc.(Grandview) Sequentla , lnc(Gran d Junction ) Brad yUS A (W

. H

. Brad yCo.
- Milwaukee )

Tota l Averag e Projecte d Tota l Proces s Desc

. fiOJjfi 8 + 1 7 1 7 + Pol

. Cas t 

### 1 7 1 7 1 7 + 1 3 9 + SM C + 1 7 

### 1 7 1 7 •Ge l 

### 1 7 1 7 1 7 1 7 1 7

To p 5 performin g facilitie s ar e highlighted i n bol d type

. MAC TFloo r- media n "styren e contro l status " oftop 5 facilitie s = 

## | Resi n



## jam 1287. 0 350. 0 

### cb l 7592. 8 1182. 0 927. 0 12218. 0 199. 0 9890. 0 1881. 0 4188. 0 11106. 0 376. 0

51194.5 0 4266.2 1 55460.7 1

Baselin e emission s » Su m o factua l curren t calculate d emission s fo rsl l facilities

. % Styren e /\ 8 Supplied

. 41.4 0 31.0 0 

### Cbl 42. 0 25. 8 41. 0 41. 3 58. 1 40. 0 41. 0 42. 7 41.4 0 50. 0

495.4 0 41.2 8

0.9 1 Fille r



## iBa) 8. 0 0. 0 cb l 0. 0 50. 0 1170. 0 6497. 0 264. 0 2380. 0 477. 0 1258. 8 2459. 0 

### 0. 0

14583.8 0 1215.3 2 15799.1 2 lbs Styrene / 

## aaLB M 3.7 9 2.8 5 

# uw 3.8 6 2-2 9 2.3 5 3.0 2 3.1 7 3.2 9 3.3 8 3.4 3 3.4 4 4.5 9

41.2 3 3.4 4 Contro l

Easto i 0.0 6 0.0 9 0.5 1 0.6 3 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0

10.1 7 0.7 8 Styren e Contro l

Statu s (l b Sty/ga l RM ) 0.1 9 0.2 5 

# aw « 2.0 2 2.2 9 2.3 5 3.0 2 3.1 7 3.2 9 3.3 6 3.4 3 3.4 4 4.6 9

MAC Temission s * Su m ofcurren t emission s fo rfacilitie s wit h styren e contro l statu s (SCS ) value s equa l to o rles s tha n th e media n SC S valu e plu s Curren t Emis

. 

# am 1.4 7 0.5 3 

### Cb l 92.0 8 16.6 8 20.9 0 277.4 9 6.3 6 217.5 8 42.4 2 98.3 6 252.8 8 10.3 4

1036.9 8 88.4 1 1123.3 9

th e su m ofemission s equa l to (resi n + flller)voT(l b sty/ga l RM)*(media n SC S value)*(AP-4 2 midpoint) fo reac h facilit ywit h a SC S valu e greate rtha n th e median

. Therefore , irrtplementln g MAC Twoul d produce a 65. 2 percen t reduction i n emission s o fHA P fro m continuou s laminatio n operations

. Contro l facto rDat a an d Assjflrjffllgns ; Enduro Fiberglas s ha s a n overal l capture efficienc yof100 % an d a destructio n efficiencyof95%

. Cran e Kemlite ha s a n overal l captur e efficienc

yo f50 % an d a destructio n efficienc yof95%

. Co rTe c ha s a n overal l capture efficienc yo f94 % an d a destructio n efficienc yo f96.9%

. | CB I Plan t #4 ha s a condense rwit h a n overal l capture efficienc yof50 % an d a destructio n efficiencyof99%

. Covered/enclose d resi n area s received n o contro l facto raedi t Covere d mixers received n o contro l facto rcredi t | Partiall ycovere d mixers received n o contro l facto rcredi t Covere d holdin g tank

s receive d n o contro l facto rcredi t Rlte rdensit

ywa s assume d to b e 19. 2 lb s pe rgallon

. Resi n densit ywa s assume d t o b e 9. 2 lb s pe rgallon

.

1 •Ge l Coatin g an d Ope n Moldin g 2 •Gel Coatin g an d F"olyme rCastin g 3 « RIM , Gel Coating ; an d Ope n Moldin g 

# I Proces s Descriptio n Codes :

4 = Compressio n Molding , Gel Coating , an d Ope n Moldin g 5-lnJrjctionMoldiii g 6 • = Centrifuga l Castin g an d Fllamerr l Windin g 7 •Centrifuga l Castin g 8 » Pulbusio n 02/13/9 0 9 > BMC , Compressio n Molding , an d Pultrusio n 10 = SM C an d Compressio n Moldin g 1 1 » Compressio n iMoldin g | 1 2 a Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Moldin g | | 1 4 = Filamen t Winding

. Ge l Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 8 = Polyme rCastin g an d Ope n Moldin g 17' a Continuou s Laminatio n 1 MAC TEmis

. 

## atar i 1.4 7 0.5 3 

### cb l 92.0 8 6.6 7 8.1 0 83.4 5 1.8 2 80.0 6 11.4 9 26.0 9 66.8 9 2.0 5

360.5 7 30.0 5 390.6 2 Reductio n Techniaue s Incinerato r Incinerato r Condenser/ C filte r Incinerato r Covere d mixer s Partiall ycovere d mixer s
Covere d mixer s

Covered/enclose d resin are a Covered/enclose d resi n are a Covere d holdin g tanks



## -



# 6 ^ Page l

T J CO

^ l

# Centrifuga l Castin g

Ran k 1 2 3 4 5

- • • Plant , nam e Emsi g Manufacturin g Corporatio n Fibercas t Compan y Rave n Industries , lnc.(Siou xFalls ) CB I Plan t #1 5 CB I Plan t # 2

Tota l Averag e Projecte d Tota l Proces s Descriptio n Cod e 7 6 + 1 1 + 1 3 +BM C 6 + 1 6+1 3 7

tMAC TFloo r= media n styren e contro l statu s ofto p 5 Facilitie s = 

## | Resi n 

## Mil 487. 3 318. 0 117. 0 

## iWMismm. 192. 6

1114. 3 278. 6 1392. 9

Baselin e emission s = Su m ofactua l curren t calculate d emission s fo ral l facilities

. % Styren e A s SuoDlied 35. 1 42. 6 42.5 0 46. 0 50. 0

216. 2 43. 2 Contro l

Facto r 0. 6 0.51 5 1. 0 1. 0 1. 0

0.42 5 Contro l

Statu s (Ibsty/qaIRM ) 0.21 1 0 21 9 

## '^y^jfrifpr-'- 0.46 0 0.50 0

1.8 1 0.3 6 1.8 1 Curren t Emis

.



# am 17.7 0 12.0 3 8.5 8 MAC TEmis

.

(toy) 17.7 0 12.0 3 8.5 8 22.1 0 20.4 2 16.5 6

77. 0 19. 2 96. 2

MAC Temission s = Su m o fcurren t emission s fo rfacilities wit h styren e contro l statu s (SCS ) value s equa l t o o rles s tha n th e media n SC S valu e plu s th e su m o femission s equa l t o (resin)'(media n styren e contro l status)*(E F of0.075)*2. 3 fo reac h facilit ywit h a SC S valu e greate rtha n th e median

. Therefore , implementin g MAC Twoul d produce a 4. 5 percen t reductio n i n emission s o fHA P fro m centrifuga l castin g operations

. Emissio n Reductio n Assumptions : Fibercast' s incinerato rha s a n overal l capture efficiencyo f50 % an d a destructio n efficienc yo f97%

. A 4 0 % emissio n reductio n credi t wa s give n fo rth e us e o fvapo rsuppressed resin

. Gre ycell s = assume d values :

1 = Ge l Coatin g an d Ope n Moldin g 2 = Ge l Coatin g an d Polyme rCastin g Proces s Descriotio n Cod e



## - - 3 = RTM , Gel Coating , an d Ope n Moldin g 4 = Compressio n Molding

. Ge l Coating , an d Ope n Moldin g 5 = injectio n Moldin g | 6 = Centrifuga l Castin g an d Filamen t Windin g J 7 = Centrifuga l Castin g ! 8 = PuUrusio n
2/22/9 6 

## . . . . 5 1 

## . .

. . _.

_H 9 = BMC , Compressio n Moldin g 1 0 = SM C an d Compressio n M o 11 = Compres s 1 2 ="Filamen t W 1 3 = Ope n Mol d 1 4 a Filamen t V

I o n Moldin g /indin g an d Ope r in g an d Pultrusio n

din g
i Moldin g /inding

. Ge l Coating , an d Ope n Moldin g 1 5 = Compressio n Moldin g an d 1 6 = Polyme rCastin g an d Ope n 1 7 = Continuou s Laminatio n : ilamen t Windin g Moldin g 

## -- • 

## - - 14.0 8

72. 8 18. 2 91. 0



## -— Reductio n Techniaue s VS R (100% ) Incinerato r

- - —• •



# Pag e 1

CO o o

# Compoundin g - SM C

Ban k i 2 3 4 5 6 7 8 9 1 0 1 1 1 2 1 3 1 4 Sftrl C

Plan t nam e Navista rInternationa l Transportation(Columbus) E^le-Pid wIndustrie s Inc(Grabill ) Industria l Dielectric s Bud d Company(Va n Wert ) GenCor p Automotive , Inc

. (Marion ) Applie d Composites , Cor p Mertash a Corporatio n (Watertown ) Columbi a Specialties , Inc

. Haysit e Reinforce d Plastic s BaileyTransportatio n Products , In c Goodyea rTir e & Rubbe rCo

. Rockwel l Internationa l MF G •Molde d Fibe rGlas s Companie s (Unesville ) CB I Plan t 8 6

MAC TFloo r= media n "styren e contro l status " o fto p 5 facilitie s » Proces s Descriptio n Cflflf i 1 0 1 0 9 +SM C 1 0 1 0 1 0 10 1 0 9 + SM C •1 7 1 0 1 0 1 0 1 0 + BM C 1 0 +BM C



## ,
n o numerica l limi t
Baselin e emission s a Su m ofactua l curren t calculate d emission s fo ral l facilitie s Compoun d SM C SM C SMC/BM C SM C SM C SM C SM C SM C SMC/BM C SM C SMC/XM C O M w SM C SMC/BMC/TM C

Total : Average : 

## . . . .

Resi n 

# am 2817. 0 3190. 0 1574. 0 5192. 0 4910. 0 2469. 0 2540. 1 1208. 0 112. 4 970. 0 2498. 3 2498. 3 2498. 3 2498. 3

24982. 5 2498.2 5



## . . .. . 

## .

% Styren e A s Supplie d 44. 7 25. 9 41. 6 43. 6 41. 7 40. 5 41. 3 45. 0 40. 6 47. 9 41. 3 41. 3 41. 3 41 : 3

412. 8 41.2 8



## - Fille r

(tpy) 8224. 0 7810. 0 4773. 0 15410. 0 12894. 0 6103. 0 5371. 4 297 4 213. 0 1980. 0 6575. 2 6575. 2 6575. 2 6575. 2

65752. 4 6575.2 4 I b styrene

/ 

### gaLB M 1.7 1 1.1 0 1.5 6 1.6 5 1.7 0 1.7 0 1.8 9 1.9 0 1.9 6 2.2 3 1.6 8 1.6 8 1.6 8 1.6 8

MAC Temission s a Su m ofcunen t emission s fo rfacilitie s wit h styren e contro l statu s (SCS ) value s equa l to o rles s tha n th e media n SC S valu e plu s th e su m o f emission s equa l t o (resi n + filler)voi*(media n styren e contro l status)*(AP-4 2 midpoint ) fo reac h fadliity wit h a SC S valu e greate rtha n Ih e median

. Therefore , implementin g MAC Twoul d produce a 0 percen t reductio n i n emission s o fHA P fro m compoundin g operations

.

Contro l Statu s Dat a an d Assumptions : Navistar' s s incinerato rha s a n overal l capture efficiencyo f80 % a Fille rdensit

ywa s assume d t o b e 19. 2 lb s pe rgallon

. Resi n den s

1 = Gel Coatin g an d Ope n Moldin g 2 a Ge l Coatin g an d Polyme rCastin g 3 » RTM , Ge l Coating , an d Ope n Moldin g 4 a Compressio n Molding , Gel Coating , an d Ope n Moldin g 5 = Injectio n Moldin g 6 = Centrifuga l Castin g an d Filamen t Windin g 7 a Centrifuga l Castin g 8 a Pultrusio n
2/14/9 6 

## -

n d a destructio n efficienc yof90%

. t ywa s assume d t

o b e 9. 2 lb s pe rgallon

.
4 5fo^sll)"escriDtion"Codes :



## . . . 9 = BMC , Compres s 1 0 = SM C an d Comr

. 1 1 = Compression' M

o n Molding , an d Pultrusio n iressio n Moldin g Oldin g I 1 2 = Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Moldin g ; f 

## . -

1 4 = Filamen t Winding , Gel Coating , an d Ope n Moldin g 1 5 = Compressio n r

V 1 6 = Polyme rCastir u Contro l Facto r 0.2 8

otdin g an d Filamen t Windin g 3 an d Ope n Moldin g Contro l Statu s 

### (l b sty/ga l RM ) 0.4 8 1.1 0 1.5 6 1.6 5 1.7 0 1.7 0 1.8 9 1.9 0 1.9 6 2.2 3 1.6 8 1.8 8 1.6 8 1.6 8



## - '



# 'JJE:

1 7 = Continuou s Lamination ' ~ T! • r Curren t Emis

. 

# am 7.0 5 16.5 2 13.1 0 45.2 7 40.9 5 20.0 0 20.9 8 10.8 7 0.9 1 9.2 9 20.6 3 20.6 3 20.6 3 20.6 3

267.4 5 19. 1



## - - -

—•-•- • MAC TEmis

. 

# am 7.0 5 16.5 2 13.1 0 45.2 7 40.6 5 20.0 0 20.9 8 10.8 7 0.9 1 9.2 9 20.6 3 20.6 3 20.6 3 20;63 ^

267.4 5 19.1



## - Reductio n



### Technique s Incinerato r



# Pag e 1

# Compoundin g - BM C

Ran k 1 2 3 4 5 6 7 8 9 BM C

Plan t nam e Fibercas t Compan y CB I Plan t # 9 MF G •Plan t 1 •Ashtabula Industria l Dielectric s Haysit e Reinforce d Plastic s MF G - Molde d Fibe rGlas s Compan y(Linesville) Allie d Moulde d Products , Inc

. CB I Plan t # 6 Glasti c Corp.(Sout h Euclid ) Proces s Descriptio n Cod e 6 + 1 1 +BMC + 1 3 BM C 11+We t Mi x 9 +SM C 9 + SM C + 1 7 1 0 +We t Mi x 1 1 +BM C 1 0 + BMC/TM C 9

Total : Average : Projecte d Total :
To p 5 performin g facilitie s ar e highlighte d i n bol d type

. MAC TFloo r= media n "styren e contro l status " ofto p 5 facilitie s = n o numerica l limi t 

## | Baselin e emission s = Su m ofactua l curren t calculate d emission s fo ral l facilitie s Resi n 

# am 127. 0 1009. 0 2012. 0 1574. 0 112. 4 425. 0 1254. 4 cb i n
6513. 8 930. 5 % Styren e

A s SuDDlied 14. 1 28. 7 16. 2 41. 6 40. 6 15.2 5 28. 9 

## * n
185. 4 26. 5 Fille r



### (toy) 302. 0 8347. 0 810. 0 4773. 0 213. 0 2689. 0 2889. 0 

## • n
14445. 0 2889. 0 l b styrene

/ oalR M 0.6 1 0.5 3 1.2 5 1.5 6 1.9 6 0.3 3 1.2 6

8.2 6 0.9 8 Contro l

Facto r 0.51 5

0.1 9

MAC Temission s = Su m o fcurren t emission s tor facilitie s wit h contro l statu s (CS ) value s equa l t o o rles s tha n th e media n C S valu e plu s th e su m of emission s equa l t o (resi n + filler)vol*(media n contro l status)*(AP-4 2 midpoint ) fo reac h fadliitywit h a C S valu e greate rtha n th e median

. Therefore , implementin g MAC Twoul d produce a 0 percen t reductio n i n emission s ofHA P fro m compoundin g operations

. Contro l Statu s Dat a an d Assumptions : Fibercast 1 s incinerato rha s a n overal l capture efficienc yof50 % an d a destructio n efficienc yof97%

. Glastjc' s carbo n filte rha s a n overal l capture efficienc yo f90 % an d a destructio n efficienc yo f90%

. Fille rdensit

ywa s assume d t o b e 19. 2 lb s pe rgallon

. Greycell s = assume d value s

1 = Gel Coatin g an d Ope n Moldin g 2 = Gel Coatin g an d Polyme rCastin g 3 = RTM , Gel Coating , an d Ope n Moldin g Resi n densit ywa s assume d t o b e 9. 2 lb s

Proces s Descrirjtio n Codes :

4 = Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 a injectio n Moldin g 6 a Centrifuga l Castin g an d Filamen t Windin g 7 a Centrifuga l Castin g 8 = Pultrusio n
2/22/9 6 pe rgallon

.

9 = BMC , Compressio n Molding , an d Pultrusio n 1 0 = SM C an d Compressio n Moldin g 1 1 a Compressio n Moldin g 1 2 a Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Moldin g | ( 1 4 = Filamen t Winding , Gel Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 6 a Polyme rCastin g an d Ope n Moldin g 1 7 a Continuou s Laminatio n 

## I I Contro l Statu s (l b stv/aa l RM ) 0.3 1 0.5 3 1.2 5 1.5 6 1.9 6 n n n n Curren t Emis

.



### (toy) 0.1 8 5.7 8 6.5 2 13.1 0 0.9 1 1.3 0 7.3 0 n n
35.1 0 5. 0 45. 1 MAC TEmis

.



# am 0.1 8 5.7 9 6.5 2 13.1 0 0.9 1 1.3 0 7.3 0 n n
35.1 0 5. 0 45. 1 Reductio n



## Technique s Incinerato r

Carbo n Filte r



# Pag e 1

# RT M

Ban * 1 2 3 4 5 6 7 6 9 R I M

Plan t nam e Livingsto n Inc

. Plasti-Fa b Inc

. (Millenniu m Products , In c Associate d Plastics , In c Contemporar

yProducts , In c E-T- M Enterprises , In c Lipper t Corporatio n Enduro Fiberglas s Systems , Inc

. Centur yManufacturin g Compan y

MAC TFloo r= media n "styren e cont i Proces s Des c 

## Cod a 3 3 3 3 3 RT M •Gel 2 +RT M RTM+1 1 + 8 3

Total : Average :

rol status " ofto p 5 Resi n



## ito* ) 170. 0 29. 0 30. 0 140. 0 % Styren e

A s Supplie d 40. 8 40. S Fille r 

# om 75. 0 0. 0 43. 6 0. 0 43. 6 0 0 73. 8 43. 8 0. 0 73. 8 43. 8 0. 0 73. 8 43. 8 0. 0 63. 4 10. 5

442. 9 73. 8 43.7 9

50. 0

175. 1 43. 8
facilitie s a n o numerica l limi t 

# 1 1 1 Baselin e emission s = Su m o factua l curren t calculate d emission s fo ral l facilitie s 

## Assumptions ; Gre y oeii s = assume d value s Fille rdensit

ywa s assume d to b e 1 9

1 a Gel Coatin g an d Ope n Moldin g 2 a Ge l Coatin g an d Polyme rCasti n 3 a RTM , Ge l Coating , an d Ope n M < 4 a Compressio n Molding

. Ge l Coa t 5 a Injectio n Moldin g 6 a Centrifuga l Castin g an d Filame n 7 = Centrifuga l Castin g 8 a Pultrusio n
2/13/9 6 

# • • •— 0 0 l b styrene

/ oilfi M 3.0 9 3.7 2 4.0 2 4.0 2 4.0 2 4.0 2 4.0 2 4.0 2 4.5 9

2 lb s pe rgallon

. Resi n densit ywa s assume d t o b e 8. 2 lb s pe rgallon

.
Proces s Descript

9 sidin g ng , an d Ope n M o

t Windin g 

# _ _

o n Codes :

din g 

# ' "

-

•• •i — 

# ! Contro l Fjcto r 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1 i

9 a BMC

. Compressio n Molding , an d Pultrusio n 10 a SM C an d Compressio n Moldin g 1 1 = Compressio n Moldin g | 1 2 = Filamen t Windin g an d Ope n Moldin g 1 3 = Ope n Moldin g | 1 4 = Filamen t Winding , Ge l Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 6 = Polyme rCastin g an d O f 1 7 a Continuou s Laminatio n >e n Moldin g



# .. . 

# _ Styren e Contro l Statu s 

## (lostWaalRM ) 3.0 9 3.7 2 4.0 2 4.0 2 4.0 2 4.0 2 4.0 2 4.0 2 4.5 9



# -

— Curren t Emis

. OCtf ) 1.3 9 0.2 3 0.2 6 1.2 3 0.8 5 0.6 5 0.6 5 0.5 6 0.1 1

5.7 1



# . iMAC TEmis

.



# am 1.3 9 0.2 3 0.2 6 1.2 3 0.6 5 0.6 5 0.6 5 0.5 6 0.0 9

5.7 0 Reductio n



## Technique s



# —

o

Pag e 1

T J r o1 s



## Bac k

i 2 3 4 S 6 7 8 9 1 0 1 1 1 2 1 3 1 4 1 6 1 6 1 7 1 8 1 9 2 0 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 8 2 9 3 0 3 1 3 2 3 3 3 4 3 5 3 8 3 7 3 8 3 9 4 0 4 1 4 2 Compressio n Moldin g



## PtanLnam e Fibercas t Compan y Bud d C4jmpany(Nort h Baltimore ) Bud d Company(Carey ) Bud d CompanyfVa n Wart ) Eagle-Piche rIndustries , Inc.(Huntlngton ) Eagle-Piche rPlastic s Dtv.(Ashley) MF G •Molde d Rbe rGlas s Compan y(Plan t 2 •Ashtabula ) Applie d C4jmposites , Cor p GenCor p Automotive , In c (Marion ) Navista rInternationa l Transportation(Columbus ) Picken' s Plastics , In c Menash a Corporatio n (Watertown ) Columbi a Specialties

. In c MF G - (Molde

d Fibe rGlas s Compan y (F»1an t 1 - Astitabuta ) Nordi c Rberglas s lnc(Devil s Lake ) Prodeti n terporatton (Catawb a Facility) Men Industrie s Eagle-Piche rIndustrie s Inc(GrebiH ) Warminste rFiberglas s Compan y(Southampton ) a Haysit e Reinforce d Plastic s Allie d Moulde d Products , Inc

. ACM E Reinforce d Plastics , Inc

. Kruege rInternationa l In c Industria l Dielectric s BaileyTransportatio n Products , In c Molde d Plasti c Industries , In c Carsontt e Internationa l Corporatio n Endur o Fiberglas s Systems

. Inc

. MF G •Molde d Fibe rGlas s Compan y(Unio n City ) Allie d Signa l Laminat e System s Amero n Inc

. (Burkburnett) Berin g Wichit a CBIPtant« 6 Gencor p Automotive , Reinforce d Plasti c Div

. (Ionia ) Ghnti c Corp.(Sout h Euclid ) Goodyaa rTir e & Rubbe rCo

. MF O •Molde d Fibe rGlas s Compan y(Llnesville ) Plastk } CpmfjXMlte

s Corporatio n Oft_*_r____\

_f*j__tt_-1ljtJ\a\\\ Smit h (tfcargtas s Product s lnc(Uttj e Rock ) Spautdtn g C4xnposites Co

. (SpecialtyPlastic s Div. ) Sterlin g Plumbin g Group , Inc

. Proces s Descriptio n Cod a 6 + 11+BM C + 8 1 1 1 1 10 1 1 1 1 1 1 10 1 0 10 4 10 10 1 1 + B4M C 4 4 1 1 + 5 1 0 4 9 + SM C + 1 7 11+BM C 4 4 9 +SM C 10 4 1 1 + 8 1 1 +RTM + 8 4 1 1 1 5 1 1 + 1 3 1 0 + BM C 1 1 9 10 1 0 +BM C 4 10 15+1 3 1 5 1 1

Total : Average : Projecte d Total : 

## Compressio n Moldin g

Resi n .(toy) 178. 0 7060. 0 7860. 0 660. 0 600 0 500 0 2577. 0 8700. 0 17800. 0 2760. 0 13. 0 8000. 0 367 2 2012. 0 75. 0 860. 0 193. 0 11000. 0 97. 0 28 9 1207. 0 63. 0 65. 0 157. 0 934. 0 143. 2 1 1 71. 5 42. 0 n n n cb l n n n 1112. 0 n n n n n % Styren e A s Supplie d 10. 1 11. 0 114 ) 11. 0 11.1 1 11.1 1 12. 8 11. 5 11. 5 21.5 0 12. 0 13. 1 13. 2 16. 2 14. 5 15. 0 21. 5 20. 0 20. 0 4 1 30. 0 30. 0 30. 0 41. 6 51. 0 33. 5 4 0 43. 1 54. 9 n n n cb l n n n 21.5 0 n n n n 50. 0



## Page l •Titer-

(tpy) 222. 0 0. 0 0. 0 0. 0 0 0 799. 0 0. 0 0. 0 4912. 0 0. 0 0. 0 0 810. 0 0. 0 0. 0 13 2 0. 0 0. 0 37 0 34. 0 0. 0 0. 0 125. 0 1150. 0 0. 0 3 0. 0 0. 0 n n n cb l n n n y n n n n y i b styrene

/ galR M 0.5 8 1.0 1 1.0 1 1.0 1 1.0 2 1.0 2 1.0 3 1.0 6 1.0 6 1.07 1.1 0 1.2 0 1.2 1 1.2 5 1.3 3 1.3 8 1.4 9 1.84 1.8 4 2.3 3 2.7 2 2.7 5 2.7 5 2.7 7 2.9 5 3.0 8 3.2 5 3.9 6 5.0 4 n n n cb l n n n n n n n n n Contro l



## Eaflo x 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 1. 0 Contro l

Statu s fi b sty/ga l RM ) 0.5 8 1.0 1 1.0 1 

# S » 1.0 2 1.0 2 1.0 3 1.0 8 1.0 6 1.0 7 1.1 0 1.2 0 1.2 1 1.2 5 1.3 3 1.3 8 1.4 9 1.8 4 1.8 4 2.3 3 2.7 2 2.7 5 2.7 5 2.7 7 2.8 5 3.0 8 3.2 5 3.9 8 5.0 4 n n n n n n n n n n n n n Curren t Emis

.

ftov) 0.3 6 15.5 3 17.2 9 1.2 3 11.1 1 11.1 1 6.6 1 20.0 1 40.9 4 11.8 7 0.0 3 20.9 9 9.6 9 6.5 2 0.2 2 2.5 8 0.8 3 44.0 0 0.3 9 2.3 7 7.2 4 0.3 2 0.3 9 1.3 1 9.5 3 0.9 6 0.0 9 0.6 2 0.4 6 n n n n n n n n n n n n n
244.6 0 8.4 3 354.2 4 MAC TEmis

.



# am 0.3 6 15.5 3 17.2 9 1.2 3 11.1 1 11.1 1

. 6.6 1 20.0 1 40.9 4 11.6 7 0.0 3 20.9 9 9.6 9 6.5 2 0.2 2 2.5 8 0.8 3 44.0 0 0.3 9 2.3 7 7.2 4 0.3 2 0.3 9 1.3 1 9.5 3 0.9 6 0.0 9 0.8 2 0.4 6 n n n n n n n n n n n n n
244.6 0 8.4 3 354.2 4

# 9 Compressio n Moldin g

Assumption ; | | | Fille rdensitywa s assume d t o b e 19. 2 lb s pe rgallon

. Resi n densit ywa s assume d t o b e 9. 2 lb s pe rgallon

.

1 > Ge l Coatin g an d Ope n Moldin g 2 a Ge l Coatin g an d Polyme rCastin g 3 > RTM , Ge l Coating , an d Ope n Moldin g 4 a Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 > Injectio n Moldin g 6 » Centrifuga l Castin g an d Filamen t Windin g 7 a Centrifuga l Castin g 8 a Pultrusio n
02/13/9 6 

# 1 Proces s Descriptio n Codes ; 9 a BMC , Compressio n Molding , an d Pultrusio n 10 > SM C an d C4xnpresslo n Moldin g 1 1 •C«Tipressio n (Molding 1 2 > Filamen t Windin g an d Ope n Moldin g 13-Ope n Moldin g | | 1 4 a Filamen t Winding , Ge l Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 6 a Polyme rCastin g an d Ope n Moldin g 1 7 a Continuou s Laminatio n | 

# 1 1 1

Pag e 2

T J

## Injectio n Moldin g

Ran k 1 2

. 3 4 5



# I Plant_nam n

tte n Industrie s GM C (Inlan d Fishe rGuid e Div. ) Squar e D Compan y(Lincoln ) Glasti c Corp.(Jefferson ) Fabal l Enterprise s o fUtah , In c (se e At e Proces s Descriptio n Cod a 5 + 1 1 5 5 5 5 + Polyme rCastin g

Total : Resi n

itov ) 19 3 485 0 4750. 0 % Styren e

A s Supplie d 21. 5 1 7 15.2 5 4800. 0 16.1 4800. 0 16. 1

9793. 0
MAC TFloo ra media n "styren e contro l status " o fto p 5 facilitie s = n o numerica l limi t 

## I I BasePn e emission s a Su m ofactua l cunen t calculate d emission s fo ral l facilitie s Assumptions : Greyt^'asMWiedvSru M Rlle rdensit

ywa s assume d t o b e 19. 2 lb s

1 a Ge l Coatin g an d Ope n Moldin g 2 a Gel Coatin g an d Polyme rCastin g 3 B RTM , Ge l Coating , an d Ope n MokJin j Fille r (1BV J 13 2 0 10 0 0. 0 0. 0

pe rgallon

. Resi n densit ywa s assume d to b e 9. 2 lb s pe rgallon

. 

## I proces s Descriptiq n Codes ;

4 a Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 a injectio n Moldin g | 8 a Centrifuga l Castin g an d Filamen t Windin g 7 a Centrifuga l Castin g 8 = Pultrusio n

2/13/9 6 9 a BMC , Compressio n Molding , an d Pultrusio n 10 a SM C an d Compressio n Moldin g 1 1 a compressio n Moldin g | 12 a Filamen t Windin g an d Ope n Moldin g 1 3 a Ope n Moldin g [ I b styrene / gaLB M 1.4 9 1.5 6 1.3 9 1.4 6 1.4 8

1 4 a Filamen t Winding , Ge l Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 6 a Polyme rCastin g an d Ope n Moldin g 1 7 a Continuou s Laminatio n Contro l Facto r 1 1 1. 0 1. 0 1. 0 Styren e Contro l

Statu s (ibstv/galRM l 1.4 9 1.5 6 1.3 9 1.4 8 1.4 8 Curren t Emis

. 

# am 0.8 3 16.4 9 14.4 9 15.4 8 15.4 8

62.7 8 MAC TEmis

.



# am 0.8 3 16.4 9 14.4 9 15.4 6 15.4 8

62.7 8 Reductio n

Techniaue s



# o . Page l

T J CJ I

# Filamen t Windin g

Ban k i 2 3 4 5 8 7 8 9 

### 1 0 

# "ii " "1 2 1 3 1 4 1 5 1 6 1 7 1 6 1 9 2 0 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 B 2 9 30 3 1 Plan t Nam e Shakespear e Compan y Baldin g Tan k

Technolog y(F.K.A

. D & R Fabr i BaaMa Plastics , Inc

. Rave n Industries , lnc.(Slou xFalls ) Owens-Comin g (Aubumdale ) Owens-Cornin g (Moun t Union ) Owens-Comin g Fibergla s (Conroe ) Owens-Comin g Tank

s (Valparaiso ) Re d Ewald

. Inc

. Rubbe r& Plasti c Applicators Amero n Inc

. (Burkbumett) Fowle rManufacturing , Inc

. GP I Corporatio n CB I Plant * 1 5 Hasting s Group , Inc-Viate c (Belding ) Ershigs , Inc(Bellingham ) Ecowate rSystem s MF G Justi n Tanks , Inc

. Diamon d Fiberglas s Fabricators

. Inc

. Owens-Comin g Fibergla s (Bakersfield ) Spauldin g Composite s Co

. (SpecialtyPlastic s D i Applachia n Plastics , Inc

. Fibercast Compan y Ershigs

. Inc.fWUson ) Slmon-Telelec t Inc

. An-Co rIndustria l Plastics , Inc

. FibrexCorporatio n Jone s 4 Hunt , Inc

. Smit h Fiberglas s Products lnc.(Littl e Rock ) Smit h Fiberglas s Products lnc.(Wichila ) CB I Plan t * 1 6

Total s Proces s besc

. Cod a 8 + FU

. Wind

. 1 4 1 2 6 + 1 1 2 1 2 1 2 1 2 1 4 1 2 1 5 1 2 1 4 6+1 3 Fil

. Wind

. 1 4 Fil

. Wind

. 1 2 1 4 1 2 1 5 1 4 6+1 1 •BM C + 1 3 1 4 1 4 1 2 1 2 1 2 1 2 + 1 1 Fil

. Wind

. 1 2

Average ; Projecte d Tota l i

To p 6 performin g faciltie s ar e highlighted i n bol d type

. MAC TFloo ra media n styren e conten t a s supplied o f(o p
Baseli i MAC T (resin ) 

## L

. . . 5 facilities =
i e emission s a actua l curren t projecte d emission s fo ral l facilities Resi n jim 739. 4 n 177. 3 21. 2 n n n n 294. 7 146. 0 " _2. 5 n 131. 5 n 400. 0 226. 1 122. 0 153. 3 254. 0 n 

## • 100. 0 83. 0 87. 0 65. 0 n n n n n n
3003. 0 187. 7 5818. 3

"42. 2 % Styren e

A s supplie d 33. 0 40. 0 42. 2 42. 7 L

_45. 0 45. 0 45. 0 45. 0 45. 0 45. 0 "45. 0 45. 0 46. 0 46. 0 46. 3 47. 6 48. 0 49. 0 49. 0 50. 0 

## • 7 7 ? ? 

## -
n n n n t i n
899. 8 45. 0 Filte r

(tttt ) y 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 

## 9-?

. n 0. 0 n 0. 0 0. 0 0. 0 0. 0 0. 0 y 

## * 20. 0 1. 0

" 0. 0 

## a o n n n 

## "o o A s aoolied %

7 40. 0 42 J 42. 7 

## 4if i 45. 0 45. 0 45. 0 45. 0 45. 0 45. 0

46. 0 7 46. 3 47. 6 48. 0 49. 0 49. 0 7 ? 7 43. 0 43. 8 "' " 43. 6 " 7 7 7 ? n i 7 

## n j 7

21. 0 ' 855.9TM" " 1. 0 ! 42.8 " 31. 0 !

- 3.8 7 l b styrene/ga l R M

i

i • emission s * Su m ofcurren t emission s fro m al l facilities usin g les s tha n 42.2 % styren e resins a s supplie d plu s th e su m •(3.8 7 l b styrene/ga l RM)*(0.075)'(2.3 ) fo ral l facilities usin g resin s wit h mor e tha n 42.2 % styren e a s supplied

. 

# i " :::.. r. ; 

# ~: : MAC Tproduces a 7 2 percen t reductio n i n emission s ofHAP s fro m filamen t windin g operations

. ! ' • - | : •• JAsajmotign , j i iFitle rdensitywa s assume d t o b e 19. 2 lb s pe rga n on . Resi n densit

y«rasassu m

sd to b e 9. 2 it e

i pe rgallo n I b stryene / gaIR M 3.0 3 3.6 7 3.8 7 3.9 2 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.13 " 4.1 3 4.2 2 4.2 2 4.2 5 4.3 7 4.4 1 4.5 0 4.5 0 4.5 9 

## • ? ?

'" ? ? n n n n n n
82. 6



## ..... . "128. 0

ofemission s



## • Contro l

Facto r 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 

## i.o o 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 1.0 0 

# iM ' 1.0 0

equa l t o Contro l

_ .

Statu s (l b sty/ga l RM ) 3.0 3 3.6 7 3.8 7 3.9 2 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.1 3 4.13" " 4.2 2 4.2 2 4.2 5 4.3 7 4.4 1 4.5 0 4.5 0 4.5 9 

## • 7 7 7 7 n n n n n n



## - - -•

• Curren t Emis

. 

# am 42. 1 n 12. 9 1. 6 n n n n 22. 9 11. 3 6. 2 __'_ n 10. 4 n 31. 9 18. 6 10.1 13. 0 21. 5 n 

## • 7 7 7 7 n n n n n n
196. 4 16. 4 507. 5



## . MAC TEmis

.



# am 42. 1 n 12. 9 1. 5 n n n n 21. 4 10. 6

" n 6. 6 n 29. 1 16. 4 8. 9 11. 1 18. 5 n 

## * ? 7 ? 7 n n n n n n
182. 3 15. 2 471. 0



## . . . . .

_ Reductio n

Technique s

• — som e enclose d mixer s



## .... .



# Pag e 1
T J

## C 7 

# e n Filamen t Windin g

n a Facilit

ydi d no t provid e thi s information

. ya Facilit

yindicated th e use o

ffiller bu t di d no

t quantif yth e amount

.

1 a Gel Coatin g an d Ope n Moldin g 2 a Gel Coatin g an d Polyme rCastin g 3 a RTM , Gel Coating , an d Ope n Moldin g Proces s Descriptio n Codes ;

4 a Compressio n Molding , Ge l Coating , an d Ope n Moldin g 5 a injectio n Moldin g 6 a Centrifuga l Castin g an d Filamen t Windin g 7 a Centrifuga l Castin g 8 = Pultrusio n
2/22/9 6 

## • • - -- - 9 a BMC , Compressio n Molding , an d Pultrusio n 1 0 a SM C an d Compressio n Moldin g 11 a Compressio n Moldin g 1 2 a Filamen t Windin g an d Ope n Moldin g 1 3 a ope n Moldin g | | 1 4 a Filamen t Winding , Ge l Coating , an d Ope n Moldin g 1 5 a Compressio n Moldin g an d Filamen t Windin g 1 6 a Polyme rCastin g an d Ope n Moldin g 1 7 a Continuou s Laminatio n



## I I •



## _ _ i



## - — i



## Pag e 2

XI