p. 1


# OAR Box 

# 1490 Prepped by Charmelle Mathews



### Document

Number: 

# 4 ) IV-B- 4 Docket Number: 

# A-94-5 2

Printed 8/4/2008 11:51:46

AM Sheet 4 of 273P. 2
I , ••«• ' 

### RESEARC H TRIANGL E INSTITUT E A-^-£2
. 

# /UT I
MEMORANDU M TO : FROM : DATE : Keit

h Barnett , EPA/OAQPS/ES D MD-1 3 Mar k Bahne r /yi/j g Septembe r

24,200 1 SUBJECT : Determinatio n o f Exhaus t Concentrations fromF WFarfiP&ffPgg ^
Pe r you r telephon e reques t

o f las t week , I'v e looke da

t RT I file s t o fin ddocumentatio n o f ou r cooperatio n wit

h Pacifi c Environmenta l Service s (PES ) i n determinin g exhaus t concentration s fro mFR P facilities
. I t appear s that

RT I ha dlimite dinpu t

in determinin g th e concentrations
. I'v e attache da

t facsimil e fromMelani e Procto r a t PES , date dSeptembe r

10 , 1996
. Th e facsimil e ha s adraf

t table , date d9/9/96 , titled , "Contro l Cost s for Ne w Ge l Coatin g an d Ope n Moldin g Facilitie s wit h Combine dResi n an dGe l Coat Usag e Abov e 100 0 tpy. " Th e tabl e i s missin g dat afor

Aqu aGlas s i n Klamat

h Fall s (Oregon)
. I'v e attache dacorrespondin g memorandu mwit

h th e subject , "Sourc e Tes t Revie w Report, " fro mth e Stat e of Orego n Departmen t

o f Environmenta l (date dJanuary 10 , 1995)
. It ha s cloude dRT I comments , showin g "measure demission s = 117 5 ton/year , se e pag e 5 " an d"permitte doperatio n = 500 0 hours/yr , se e pag e 4. " I'v e als o attache dacop y o f alette r fro mth e Ohi o EPA , wit

h aforwardin g mem o t o Madelein e Stru mfromth e Canto n (OH ) City Health Department , date d7/26/95
. Th e lette r concern s th e A.R.E
. facilit y in Massillon , Ohio
. Thi s mem o ha s cloude dRT I comment s notin g aflo w rat e o f

55,00 0 cfm , 748 8 hour s o f operation , an demission s o f 63 4 tpy . Fro mthes e records , i t

appear s that

RT I onl y provide dth e dat afor thes e tw o plant s (i.e. , Aqu aGlas s in Klamat h Falls , OR , an dA.R.E
. i n Massillon , OH)
. Th e othe r dat ain th e PE S tabl e wer e apparentl y determine db y PES
. I f I can b e o f

furthe r assistance , pleas e contac t m e a t 541-6016 , o r

bahner@rti.org
. Attachment s (3 )P. 3

SU M o f Ohi o Environmenta l P.O . Bo x 1049,160 0 WaterMark • * Cohitnbus . Ohi o 43266-014 9 , L*fi -"r- r (614)644-302 0 3 Ci£i_f£_OR C P FA X (614 ) 644-232 9 4._

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## CoPY

Georg e V . Voinovic h

Governo r 4L££J~ H Re tPermi tr

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## itar k C °"*» « Applic a ° 0B 

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_ _ ugust12r^==^ r -__J 3s,G ''^ « n """"""trm .4AI L

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A.R.E. , i r CLYD E R I MASSILLO

N whic h wil l allo w indicate d i n th e ition s an d Enclose d yo u t o i : permit . TM°"

—,._,_ __, c restric t,».,

_- - Th e Ohi o isr/* an d energ yconservation . energ yconsumption , bu t i t ca n ais v - _ lik e t o lear n way s yo u ca n sav e mone ywhil e promotin g th e environment , pleas e contac t ou r Offic e o f Pollutio n Preventio n a t (614 ) 644-3469 . **«'«4«t, M M ' " jllutio n preventio n

c e pollutio n an d ey . I f yo u woul d

Yo u ar e herebynotifie d tha t thi s actio n b yth e Directo r i s fina l an d ma yb e appeale d t o th e Ohi o Environmenta l Boar d o f Revie w pursuan t t o Chapte r 3745.0 4 o f th e Ohi o Revise d Code . Th e appea l mus t b e i n writin g and se t fort h th e actio n complaine d o f an d th e ground s upo n whic h th e appea l i s based . I t mus t b e file d wit h th e Environmenta l Boar d o f Revie w withi n thirt y(30 ) day s afte r notic e o f th e Director' s action . Acop yo f th e appea l mus t b e serve d o n th e Directo r o f th e Ohi o Environmenta l Protectio n Agenc ywithi n thre e (3 ) day s o f filin g wit h th e Board . A n appea l ma yb e file d wit h th e Environmenta l Boar d o f Revie w a t th e followin g address :

Environmenta l Boar d o f Revie w 23 6 Eas t Town Street , Roo m30 0 Columbus , Ohi o 4321 5 

### ifi. vJ . Ver ytrul yyours , Thoma s G . Rigo , Hanage r Fiel d Operation s & Permi t Sectio n Divisio n o f Ai r Pollutio n Contro l & 

### \\0\J 

## <,£ £ pp.(st\ 

### oogcf*

& 

## PA<> J 

### l \

cc : D S EP A CANTO NAI R POLLUTIO NCONTRO L 

## ( 3£ £ PA6 £ 3 6 '

&>> • 

## 2 - 0.P. 4 

### TABL E 1 . MAXIMUM MATERIALU S AG E /

II O TP Y £*'TT_E.f i J



### P L 

### TP y &ELI CofiT ExTeK\ofL~ 2^ 5 &-L/VS S ^-fl* 5 ** * •*•*** / r^ &LASS - RoDrv" * -B

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### ^3 4P. 5P. 6 

### Kls e Ko . •Qrc e No . ppllcltio n /

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## J 

# V o0 \ APPENDI XD SURFAC E COATIN G O R PRINTIN G OPERATIO N 1 . Thi s appendi xi s subaitte d fo r a : C B Surfac e coatin g operatio n (chec k on e belov) : XPain t spra y

boot hFlo w coatin g

. , :-. . . Di p tan k Rolle r coatin g Spra y Coatin g (Othe r tha n pain t spra y booth ) Othe r surfac e coatin g operation , describ e 

# ii u 

# r JU N 2 3 199 4
•*i ; ?- . CIT Y H£ALf H *L»»'T J

2
. 3
. 4
.

6 . 7 . 8 . 9 . QPrintin g o r lithographi c operation . Nao e o f operatio n PAIN T & CUR E BOOT H # 1 Yea r Installe d N/ A ; You r identiflcationPAIN T BOOT H ifl 

### QN o I s thi s operatio n succeede d b y a heate d dryin g o r bakin g operation ? E Ye s I f yes , indicat e operatin g temperatur e o f ove n 14 0 °F . Norma l operatin g schedule ; 2 4 hours/day,J > days/wk. , 5 2 vks./ye a PAIN T SPRA YBOOT H
• Downdraf t Typ e o f spra y

booth : Qf l Enclose d QConveyo r • Other , describ e Boot h manufacture r T O B E DESIGNE

D Typ e o f spraying : Mak e o r Mode l No . C D Ai r gu n • Airles s O Electrostati c O Other , describ e ^ ^ Sprayin g operatio a is : 0Manua l Fa n manufacture r T O B E DESIGNE D O Automati c Mak e o r Mode l No . 10 . Booth' s exhaus t i s equippe d vith :

11 . Vate r vash : • Vate r vas h(Complet e ite m 11 ) B Exhaus t filter s (Complet e ite m 12 ) O Baffle s D Other , describ e • Non e (a ) I s vate r re c irculated ? QYe s D N o (b ) I s a chemica l adde d t o th e vater ? QYe s Q N o (c ) I s materia l reclaime d fro m vas hvater . QYe s Q N o (d ) Describ e metho d fo r disposa l o f vast e materials :

* Doe s no t includ e ceta l platin g

EPA-310 3 D- l 

# S >trtti M * f *+ • i rc<Mt«uua t»o-ft* » •,**,•» « ***-»

• r« ^ I l o ••••*•* •P. 7


### Stat e o f Orego n 

# Departmen

t of Environmenta

l Qualit y (4

A 

# jte>i; P copy Memorandu

m

To : From : Subject : Fran k

Messina : ER-Bend Than e Jenning s Sourc e Tes t

Revie w Report . Aqu aGlas s Klamat h Count y Sourc e Testers : AGI Process : Fiberglas s Manufacturer Tvp e of Facilit v Source s no t

liste dwhic h woul demi t

1 0 o r - •

Permi t Number : Tes t Date : Repor t Received :

..,; . Date : Januar

y 10 , 199 5



# . > ; 

# si

'. +•-•'•• , v - 18-009 3 October 24-27 , 1994 Januar y 9 , 1995

: SIC 308 8 mor e tons/y r

VO C uncontrolled , mediumcos t Particulate Emission s fromAau aGlas s Sourc e

Ge l Coa t # 1 Gel Coa t # 2 Firs t Choppe r Bas e Chopper FoamCoa

t Cover Coa t Total (gr/dscf ) Measure d 0.000 2 0.000 2 0.000 2 0.000 3 0.000 7 0.000 2 Limi t 0.001 1



### ll^^iillPlllill^Hil l Particulate Emission s lb/h r
0.020 0 0.0178 : 0.0437 ; 0.042 3 0.049 4 0.015 0 0.188 2 lb/bathtu

b uni t
0.0017 ; 

## ; o.oo n
* •••:•:.• • ^ 0:001 5 x •':: *'r *0.001 8 0.001 6 0.000 5 0.006 8 lb/l b bathtu

b uni t " :j * xl3.35E- 6 • ; U ?.63E # ro;12.61E ^

' '14;04E^6 S 13.36E- 6 4.41E- 6 67.4E- 6 I t shoul db e note dtha

t su mof th e lbs/uni t

i n th e tw o tables , Particulate Emission s fromAqu aGlas s an dStyren e Emission s fromAqu aGlas s ar e no t asimpl e sumo

f the lbs/uni t

fo r each spra y booth
. Gel Coa t # 1 an dGel Coa

t #2 are paralle l processes , tha t i s each bathtub uni t

wil l pas s throug h only on e o f the Ge l Coa t booths
. Th e attache dproces s diagra mshow s th e flow of

bathtu b units
. Th e Th e sumo

f the particulat

e an dstyren e fo r

th e spra y booth s i n Lbs/uni t

i s calculate db y averagin g the lbs/uni t

fromGe l Coa t # 1 an dGel Coa t

# 2 £ASu'fe£-- 0 p £ R M \ TTE D O PEKATfd/ J 5 & 

# e pf&e.*

»«>•= . tH*sJ*£)H

^

— _
i * e^^n-^rtr'^wa -j

- JT » . j.- * 

# <eP. 8

* " %

J

- Mem

o To : Fran k

Messin a Januar y 10 , 199 5 Pag e 3
Roofto p Exhaus t Fa n Styrene Concentratio n Exhaus t Fa n EF- 2 EF- 3 EF- 4 EF-1 1 EF-3 4 EF- ? Maintenanc e Concentratio n

(pp mv/v ) 30-5 0 1 5 2 0 1 3 7 0 7 0 100 Stvrene Emission s fromAqu aGlas s Soiuc e Gel Coa t # 1 Ge l Coa t # 2 Firs t Choppe r Bas e Choppe

r Foa mCoa t Cover Coa t Hea t Room Tota l Flowrate

(DSCFM )

a q 1333 5 %
. 1346 7 ( 3 2621 4

•• ^ 1806 9 q 750 2 3L ( 1032 6 5 818 4 |J> S $*«<•*•*•)** - ppm(v/v )

21 0 22 3 23 3 6 5 5 0 19 3 6 5 Styren e Emission s

lb/h r 45. 5 48. 8 99. 2 19. 0 6. 1 32. 5 8. 6 259. 7 lb/bathtu

b uni t 3.9 1 3.2 3 3.4 2 0.7 8 0.2 0 1.1 1 0.2 9 9. 4 lb/l b bathtub uni t

0.03 1 0.02 7 0.02 8 0.00 6 0.00 2 0.00 9 0.00 2 0.10 5



## -to !$$&*/.• ;TKA . 

## \$.% xV 

## o l 

## * 14 3 (p ^ i r <=)-) , i)\* > 

# 7P. 9

To : Fran k

Messin a anuar y 10 , 199 5 Pag e 4
Summar y of Ambient Stvren e Sampling Productio n Are aLocatio n 1
. Touch-u p Are a 2
. Maintenanc e Are a 3
. Shippin g an dReceivin g 4
. Woo dSho p 5
. Exhaus t

Fa n # 3 Averag e Ambien t Concentratio n (pp mv/v ) 5. 4

4 3 3. 4 1 5 7. 6 1 5 

### C^c^c * 247 ) 2 

### *o ^

Durin g th e mont

h o f October , th e productio n rat e wa s 8,24 0 bathtub unit s whic h i s roughl y 40 % of th e planne dproductio n capacity
. Durin g th e ai r sourc e test , productio n was?40%-;t o 50 % o f th e desig n capacity
. Th e PSEL s show n in th e tabl e ar e calculate dusin g the emissio n factor s fromthe ai r sourc e tes t

andth e desig n capacit

y o f 250,00 0 bathtub units^pe r year . Actua

l emission s fo

r 199 4 are a s follows :

. •L'-F O oo o u/UxT S
_ZSO DAY S ( Particulate % « f\%,ottfeb (54,13 7 bathtu b unit s yea

r * 0.006 8 lb s P M unit)/(25 0 days/year^ * 2£hrs/d^ ) = 0.0 7 lbs/h r &* $ £ & 54,13 7 bathtub unit s * 0.006 8 lb s P M unit/200 0 Ibs7fi3n" = TH f tons/yea r *»]^Stvren e A-JLf ^ (54,13 7 bathtub units/25 0 days ) * 9. 4 lbs/uni t = 203 5 lbs/da

y \j,is/f E 54,13 7 bathtu b unit s * 9. 4 lb s styrene/unit/200 0 lbs/to n = 25 4 tons/year I f Aqu aGlas s wer

e t o continu e operatin g a t

40 % of capacit y i n 199 5 they woul dexcee dthei r lon g termPSE L for

styren e i n 5 0 day s o

f operation
. (9 3 ton s styren e * 200 0 lbs/ton)/(1000'unit/dat y * 0.4 0 capacit

y * 9. 4 lb s styrene/unit ) = 5 0 day s Particulat e emission s ar

e controlle db y awater

curtai n an dadr

y disposabl e filter
. Styrene
. and VO C emission s are uncontrolle d

%P.1 0

Mem o To : Frank

Messin a Januar y 10 , 199 5 Pag e 5
Shor t an dLong Ter

mPSEL s Pollutant PSE L Measure d Limi t Particulate Matter

< 1 0 / z lbs/hour tons/yea r 0.2 8

0.8 5 1.65

4. 9 Styren e lbs/da y tons/yea r 9,40 0



## <Xl7 p 74 4

<*) • Aqu aGlas s i s out

o f complianc e wit

h th e shor t andlon g termstyrene PSEL s fo r tw o reasons ; emissio n factor s measureddurin g thi s sourc e tes t are higher

tha n thos e value s reporte dt

o DE Q b y Aqu aGlass , andAqu aGlas s seem s t o hav e underestimate dth e amoun t of resi n an dgel coa t use dto produc e abath/showe

r unit
. T o illustrat

e th e deficiencie s i n the informatio n use dt o calculat e th e styren e PSELs , I will us e th e 199 3 annua l report andEP A AP-4 2 emissio n factor s to calculat e 199 3 emission s fo

r th e Aqu aGlas s facility
. 199 3 Stvrene Emission s EP A AP-4 2 use s the followin g rang e o f emissio n factor s for

spra y layu p i n th e polyeste

r resi n jroduc t fabricatio n r

. Proces s Spra y Layu p rocess . Resi n Non-Vapo r Suppresse d 0.09-0.1 3 Vapor

Suppresse d 0.03-0.0 9 Gel Coa t Non-Vapo r Suppresse d 0.26-0.3 5 Vapo

r Suppresse d 0.08-0.2 5 The following calculatio n use s th e higher rang e o f EP A AP-4 2 styrene emissio n factors fo r vapo r suppresse dresin s -qficTgelcoSfr , which woul dseemto mor e closely matc h th e Aqu aGlas s styren e emission s tha

n the lowe

r rang e o f emissio n factors
. Resi n styrene content o f 0.3 1 i s taken fromth e 199 3 Aqu aGlas s annua

l report , EP

A AP-4 2 report s avalu e o f 0.43
. Gel coat , resi n andstyren e usag e ar e all taken fromthe 199 3 Aqu aGlas s annua l report .



# < fP.1 1

Memo To : Frank

Messin a Januar y 10 , 199 5 Pag e 7 Fugitiv e emission s wer

e not taken int o accoun t durin g the ai r

dispersio n modelin g originally performe da

t the Aqu aGlas s facility
. I t i s obviou s fromth e odor

complaints , th e air

sourc e tes t performe dby AG

I an dfro mthe surve

y performe db y DE Q tha

t fugitive emission s ar

e aproblema

t Aqu aGlass
. Facilit

y emission s shouldb e modele dagai n wit h the fugitive einissio n source s include d i n th e ai r dispersio n model
. T o maintai n indoor

ai r quality , the Aqu aGlas s facilit y wa s designe dfo

r acombine ddischarg e flowrat e o f 175,00 0 dscf

m( 7 stack s x 25,00 0 dscftn)
. However , the sourc e tes t dat ashow a combine ddischarg e flowrat e o f 97,00 0 dscfm
. On

e wa y for Aqu aGlas s to improv e their styren e capture efficiency an

ddecreas e the ambien

t styren e concentratio n wouldb e to increas e fa n speed , a t eac h o f the 7 stack s excep t

fo r th e first choppe r spra y boot h stac k which ha dastac

k flowrat e of 26,00 0 dscfm
. Thi s wouldnot , however , decreas e overal l styren e emissions
.

cc : John Hector : DEQ : ER-Bend Dav e Kauth : DEQ

r ER-Bend Peter Brewer : DEQ : ER-Ben

d Al i Nikukar : DEQ : H Q



## 10Tabl e 5-1
. Styren e Exhaus t Concentration s a t

Existin g Ope n Moldin g Plant s wit h Resin/Ge l Coa t

Usag e Greate r

tha n 1,00 0 tons/y r

PLAN T NAM E AQU A GLAS S A.R.E. , INC
. LASC O BATHWAR E UNIVERSA L RUNDL E AMERICA N STANDAR D A.R.E. , INC
. MILLENIU M PRODUCT S AQU A GLAS S Arithmeti c mea n CIT Y KLAMAT H FALL S MASILLO N MOAP A OTTUMW A SALE M MOUNTEATO N ELKHAR T ADAMSVILL E
Media n S T O R O H N V I A O H O H I N T N UNCONTROLLE D EMISSION S (ton/yr )

1,17 5 77 0 73 9 32 8 5 3 10 8 12 3 1,15 1 OPERATIN G HOUR S (h/yr )

6,00 0 7,48 8 4,29 0 4,16 0 2,50 0 3,12 0 2,00 0 6,00 0 PLANT-WID E FLO W RAT E (fG/min ) 97,00 0 55,00 0 155,40 0 110,70 0 35,00 0 70,00 0 125,00 0 390,00 0 AVERAG E STYREN E CONCENTRATIO N (ppm ) 24 9

23 1 13 7 8 8 7 5 6 1 6 1 6 1 120 8 2 O

toP.1 3

10/9 6 12:1 2 ©1919941023 4 PE§..FSP'« C 

# FAX C O ®00l/00 3

Datfe:- ' FROM :

Reseatc n A

(919 ) 941-033 3 ^ER
- <*» > 941-023 4 F A XNUMBER . ^ 

### TO : Name : Address :

Pfcon e Number :

F A X NUMBER : 

# Z±i-jrsjL

REFERENC

E CODE : 

## \% OJy£jS.

THI S co :

liaiaSI C*TI° « COMPRIS E 3 PAGE S UJCLUDIN

G THI S ** GE "

COMMENTS :

I To o C M o o § 1 Contro l Cost s fo r Ne wGe l Coatin g an d Ope n Moldin g Facilitie s wit h Combine d Resi n an d Ge l Coat Usag e Above 100 0 tp y DRAF T

Contro l Cos

t (Won ) Facilit y Infonnaiio n of HA P Remove d Numbe * Resi n Resi n OMHA P Gel Coa l Ge l Coa t Gel HA P HA P Operaiin g o f Spfar y Ai r Flo

w Usag e MA P Emission * Usag e HA P Emission s Emission s Concentratio n Hou n Conoenlalo r / Plan t Nam e (Cftn l (tov ) 

### m ton) o a jai . (ta g {Baa l ISltoni A . R . E. , lnc.(Mas5illon } / y j. Aqu B Glas s Corparallof * (Adamsville ) Aqu a Glas s Corporatio n (Klamat h Falls ) 65.00 0 5,88 6 4 2 43 6 1,54 1 4 0 33 4 77 0 23 1 69 1 I S 190,00 0 12,00 0 4 3 91 3 1,17 0 3 8 23 7 1.15 1 6 1 / 1.71 8

97.00 0 1,175 24 9 6.00 0 63 7 I f nlversat-Riundl e Corp - (Ottumwa ) 110,70 0 2.S0 0 4 7 20 6 59 3 3 6 12 2 32 8 8 6 4.18 0 2.36 8 Tompkin s - Lasc o Bathwar e (Moapa ) 155.40 0 6.25 9 4 7 1,5» 6 4 0 73 0 13 7 

## ~r 4.29 0 1/0 6 America n Standai d 35,00 0 cb l cb l Cb l cb i 6 3 7 5 2.50 0 5.595 U 0 ,

OL , Milleniu m Product s 125.00 C 63 4 4 1 0 6 16 7 3 0 2 7 12 3 7 5 2.00 0 8,34 3 A . R . E . (Moun t Eaton ) 

## Lmmmms t 70.00 0 98 7 3 4 5 0 26 2 3 4 4 8 10 8 7 5 3.12 0 4.76 6

n M O
3 0

rs . y-i M
3 D 3 » C A

Pag e 1Contro l Cost s fo r Ne wGe l Coatin g an d Ope n Moldin g Facilitie s wit h Combine d Resi n an d Ge l Coa t Usag e Above 100 0 tpy DRAF T 09/10/9 6

Plan t Nam e A . R . E. . Inc-(Masslllon ) Aqu a Glas s Coiporatio n (Klamat h Falls ) Universal-Rundl e Corp . (Ottumwa ) Tompkin s - Lasc o Baihwai e (Moapa ) America n Standai d Milleniu m Product s A . R . E . (Moun t Eaton ) 

### smSS^k^^^issssM^sfi Numbe r o f Spra y Booth s 4
6 n n 5 i

Ai r Fle w

(Etu i 55.00 0 07,00 0 110.70 0 155,40 0 35,00 0 125.00 0 70,00 0 1 Resi n

Usag e (Ha d 5,88 6 2,50 0 6,25 9 cb l 63 4 98 7 Resi n

HA P (54 1 4 2
4 7 4 7 cb l 4 1 3 4 OMHA P

Emission s (tot ) 43 6
20 6 cb l 9 6 5 9 I

i Facilit y Infonmatio n Ge i Coa l Usag e flex} 1,54 1 59 3 1.59 8 0 16 7 26 2 Gel Coa t

HA P m 4 0
3 8 4 0 0 3 0 3 4 Ge t HA P

Emission s im 33 4
12 2 cb i 2 7 4 8 HA P

Emission s iSEA 77 0 1,17 5 32 8 73 8 S 3 12 3 10 8 Concentratio n

(ppm l 23 1 24 9 6 8 13 7 7 5 7 5 7 5 Operatin g

Hours fhrfyr t 7.46 B 6,00 0 4,16 0 4,29 0 2,50 0 2,00 0 3.12 0 Contro l Cos ! (J/ton )

of HA P Remove d
Conoenlatn r (SflQfl l 69 1 63 7 2.36 6 1.40 8 5,59 5 8,34 3 4.76 6

Pag e 1