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# OAR Box 

# 1500 Prepped by Ollie Stewart



# Document

Number: 

# 73 ) ll-C-9 9 Docket Number: 

# A-94-5 2

Printed 8/5/20081:51:30PM

Sheet 73 of 343

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# I ^-19 ^ Centra l Par k Wes t 500 1 Sout h Miam i Boulevard , Suit e 30 0 P.O . Bo x1207 7 Researc h Triangl e Park , N C 27709-207 7 (919 ) 941-033 3 FA X(919 ) 941-023 4 

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^[o-%ri--is3*i REFERENC E CODE : •Qgol.QOl THI S COMMUNICATIO

N COMPRISE

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S INCLUDIN

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. COMMENTS

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## Continuou s Laminatio n DFeAI= T 04/15/9 7



# T * Ran k

1 2 3 4 5 6 7 8 9 1 0 1 1 EXISTIN G SOURCE S Importan t Notes : Th e averag e emission s factor s use d i n thi s sprea d sheet t o calculate emission s shoul d no t b e use d to determin e actua l emission s a t a specifi c facility . A facility' s specifi c emission s show n i n thi s sprea d sheet ma yno t represen t th e facility' s actua l emission s an d shoul d therefore no t b e used . Curren t proces s subcategories ma y change , whic h may chang e th e rankin g offacilities . | | | | Thi s databas e onl ycontain s facilities fo rwhic h th e Administrato rha s information . Othe rfacilitie s tha t shoul d b e par

t ofthi s databas e ar e likel y to exis t

Plan t Nam e Cran e Kemlit e (Jonesbor o - formerl yB P Chemica l Endur o Fiberglas s (formerl yW . R . Grace ) Sequentia , Inc . (Grandvlew ) Sequentia , Inc . (Gran d Junction ) Tompkin s - Lasc o Pane l Product s (KY ) Resolite Kalwal l Corp . Cran e Kemlite (Joliet

) BradyUS A (W . H . BradyCo. - Milwaukee) Glastee l Industria l Laminates Unite d Panel , Inc .

Projecte d Tota l (includin g assume d values) : Averag e Legen d Resi n (tPV ) 7,59 3 1,28 7 4,18 8 11,10 6 9,89 0 1.18 2 1,88 1 12,21 6 37 6 1,20 1 19 9 51,11 9 4,26 0 %HA P

neat resi n Dlu s 42. 0 41. 4 42. 7 41. 4 40. 0 37. 9 41. 0 41. 3 50. 0 51. 5 58. 1

40. 6 Filler/Resi n

Rati o 0. 0 0. 0 0. 3 0. 2 0. 2 0. 0 0. 3 0. 5 0. 0 0. 0 1. 4

0. 3

Endur o Fiberglas s has a captur e efficienc

yof100 % an d a destructio n efficienc yof95% . Cran e Kemlite , Jonesbor o has a captur

e efficienc

yof1 Assume d value s - N o dat a provided 00 % an d a destructio n effidenc yof95% .

Covered/endose d resi n area s receive d n o contro l facto rcredi t Covere d mixer

s receive d n o contro l facto raedit . | Partiall ycovere d mixer

s receive d n o contro l facto rcredi t Covere d holdin g tank

s receive d n o contro l facto rcredi t Fille r (tPV ) 0 8 1,25 9 2,45 9 2,38 0 50 47 7 6,49 7 0 0 28 4 13,41 4 1,11 8 Contro l

Facto r 0.0 5 0.0 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 Curren t Controlle d

Emission s (tpv ) 5.5 8 0.9 3 62.5 9 160.9 3 138.4 6 15.6 8 26.9 9 176.5 8 88.3 6 21.6 5 4.0 5 701. 8 58. 5 Curren t Uncontrolle d Emission s (tpy) 111.6 1 18.6 5 62.5 9 160.9 3 138.4 6 15.6 8 26.9 9 176.5 8 88.3 6 21.6 5 4.0 5 825. 5 68. 8 Reductio n Technique s Therma l Oxidize r Therma l Oxidize r we t are a enclosure s we t are a enclosure s enclosur e o n on e lin e Numbe r o fline s n 1 2 4 3 1 1 3 1 1 1



## c — 1 ' — J t' l I

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## Continuou s Laminatio n DF5AF T 04/15/9 7

Ran k 1 2 Continuou s Castin g EXISTIN G SOURCE S

Importan t Notes : Th e averag e emission s factor s use d i n thi s sprea d sheet t o calculate emission s shoul d no t b e use d t o detennin e actua l emission s a t a specifi c fadlity . A fadlity' s specifi c emission s shown i n thi s sprea d sheet may no t represen t th e fadlity' s actua l emission s an d shoul d therefor e no t b e used . Cunen t process subcategories ma ychange , whic h ma

ychang e th e rankin g offadlities . | | | | Thi s databas e onlycontain s fadlitie s fo rwhic h th e Administrato rha s infonnation . Othe rfadlitie s tha t shoul d b e par t o fthi s databas e ar e likel y t o exist .

Plan t Nam e Internationa l Pape r(Nevamar) Unite d Panel , Inc . Legen d Resi n (tpy) cb i n %HA P

neat resin olu s cb i n Filler/Resi n

Rati o cb i n Fille r

(tpy ) cb l n Contro l

Facto r 0.3 0 n Curren t Controlle d

Emission s (toy) cb i n Curren t Uncontrolle d

Emission s (tpy) cb i n

Internationa l Pape rha s a condense rcombine d wit h carbo n filters wit h a capture effidenc y o f50 % an d a destructio n efficienc y o f99 % (Fountainhea d Shee t line) . Internationa l Pape rha s a fixe d carbo n be d wit h a capture efficiency of92 % an d a destructio n effidenc y o f99 % (Particl e line) . n = N o Availabl e Dat a Reductio n Technique s Condenser/

C filte r n Numbe r

o fline s CB I n



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