p. 1 

# OAR Box 

# 1413 Prepped by Ollie Stewart



### Document

Number: 

# 34 ) 11-1-3 4 Docket Number: 

# A-94-5 2

Printed 7/9/2008 3:11:21 PM

Sheet 34 of 114Jul y 11 , 199 5 DEPARTMEN T O F ENVIRONMENTA

L Richard Nielsen Clar k Count y Healt h Distric t Ai r Pollutio n Contro l P.O . Bo x 442 6 La s Vegas , N

V 8912 7 QUALIT Y EASTER N REGIO N Ben d Offic e

Re : Styren e Sourc e Tes t Informatio n Dea r Mr . Nielsen : Enclose d pleas e fin

d the Sourc e Tes t

Review Report s (2 ) fo

r th e Aqu aGlass , Klamat

h Fall s facilit y a s prepare d b

y our sourc e tes t

coordinator , Than e Jennings . Th e sourc e tes t document s themselve s are rathe r larg e s o I di dno t

attemp t to copy them . I hop e tha t yo u wil l fm d thi s informatio n useful . Th e sourc e tes t

protoco l fo

r the Octobe

r 24-2 7 tes t

(tes t #1 ) i s describe din th e Septembe r 7 , 199 4 letter

t o Mr . Gantenbei n o f

BW R(consultant) . Th e initial sourc e tes t protoco l fro

m BWR , als o enclosed , was foun d to b e deficien

t i n man y areas . Tes t

# 1 was conducte d t o fulfi l asourc e tes t

requirement

i n the Air

Contaminant

Discharg e Permi t

(ACDP) . Th e DE Q receive d th e protoco l fo r tes t #2 month s afte

r th e tes t wa s conducted . W

e hav e no t formally reviewe d o r

approve d th e protocol . Th e tes t was conducte dt

o develop styren e emission s infonnatio n fo

r Aqu aGlass , but

wa s late r submitte dt

o the DE Q as additiona

l emission s informatio n fo

r PS D permittin g purposes . Ihav e enclose dacop y o f th e protoco l fo r tes t # 2 for you r information . Th e DE Q i s expectin g th e ful l PS D applicatio n fro mAqu aGlas s o n o r abou t Augus t 15 , 1995 . W e hav e alread

y receive d th

e BAC T analysi s andhav e mad

e apreliminar

y BAC T decisio n whic h incorporate s acombinatio n of proces s modification s an

dtherma l oxidation . However , the BAC

T determinatio n will no t

become fina

l unti l the propose dpermi t ha s gon e throug h publi c notic e and forma l revie w b y th e EP A Regio n X a s par t of th e PS D process . I hop e th e recent

tes t event a t th e LASC O facilit

y i n Moap awen

t well . I wouldlik

e to discus s thi s wit

h you , a t leas t when yo u receiv e th e tes t

result s if no t earlier . If yo u o r your sourc e tes t

coordinator , Maso n McNinch , wouldlik e to discus s testin g methodolog y and result s determination , don' t hesitate to contac t

Thane Jenning s o

f ou r office . H e ca

n b e reachedat

extensio n 247 . A s w e foun d wit h tes t #2 a t Aqu aGlass , th e result s wer e no t alway s presente di n a conservativ e manner . Than e essentially recalculate dth e emissio n rate s fro m scratc h to verif

y th e reporte d results . 214 6 N E 4t h Stree t Suit e 10 4 Bend . O R9770 1 (503 ) 388-614 6 DEQ/CR-10 1 /P. 3

Richar d Nielse n Jul y 11 , 199 5 Pag e 2 I f yo u hav e an y question s o r

would lik e additional infonnatio n yo u ma y reac h m e a t 503
- 388-6146 , extensio n 243 . Sincerely ,
Pete r J . Brewe r Air Qualit y PJB:n s Enclosur e cc : S7 < Madelein e Strum U S Environmenta

l Protectio n Agency MD-1 3 Researc h Triangl e Park , N C 2771 1 Than e Jennings : DEQ:Bend/fil e

^

# BWR ASSOCIATES, INC. P. 4
ENVIRONMENTA L CONSULTANT S WNmswSmSSu,, ^ Jul y 22 , 1994 L r? 6 1994 Joh n Hector , P.E . CENTRA L REGIO N Orego n Departmen t

o f Environmenta l Qualit y aEH D 214 6 N.E . Fourth , #10

4 Bend , O R9770 1 REGARDING

: Sourc e Tes t

Pla n fo r

Conpliamr

p Bnissicn . Testing , AquaGlass , Klamat h Falls , Orego n Dea r Mr . Hector : Thi s correspondenc e i s t o notif yth e Agenc yo f th e pendin g sourc e tes t fo r th e above-reference d facility , schedule d fo r Septembe r 23-25,"1994 . Unles s change d b yth e Agency , thi s uotic e als o serve s a s th e approve d sourc e tes t plan . 1 . Source s t o b e Tested :

Coltics tjtore> SOURC E I.D . 

## —*-c . v D . 

### H . J . L . P . X . DESCRIPTIO N

Firs t gel-coa t cubicl e nort h Firs t gel-coa t cubicl e sout h Firs t cho p booths , combine d Cove r coa t cubicl e Foa m cubicl e Bas e cho p booths , combine d Hea t roo m 2 . Sourc e Description : Th e e-xhaust s o f th e abov e processe s (excep t X ) ar e controlle d b yfoam/pape r filtratio n an d wate r fal l impingemen t particulat e remova l systems , an d exi t throug h vertica l stack s locate d abov e th e roof . 3 . Pollutant(s ) t o b e Monitored : Particulat e matte r (Tota l & JM 10 ) an d styrene . 4 . Method s Approved : Particulat e Matter - CDE Q Method s 1-4, 8 & 9 . (Tota l S e EMJQ ) assumin g al l particulat e

t o b e FM,g . Styrene - EP AMetho d TO-14 , verball y pre-approve d byMar k Fishe r o f CDEQ . 5 . Numbe r o f Samplin g Replicates :

Particulat e Matter - Thre e (3 ) M 8 fo r th e sourc e wit h rh e highes t potentia l t o emit . Aqu a Glas s ha s determine d tha t Sourc e H i s th e larges t particulat e emittin g source . Method s 1- 4 & 9 wil l b e utilize d i n duplicat e o n th e remainin g sources .
;A V » MEDFORD . OREGO N37501-134 3 • [503 ] 779-2646



# 3P. 5 /



# 9 —BWR ASSOCIATES, INC. ENVIRONMENTA L CONSULTANT S Styrene - Thre e integrate d sample s pe r source . extende d ove r a on e hou r period . 6 . Sourc e Testin g Personnel : "RJ O BW R Associates , Inc . representative s 7 . Sourc e Sit e Personne l Contact : Scot t Dickson . Facilitie s Manage r Telephone : (503 ) 882-771 1 8 . Applicabl e Process/Productio n Informatio n a s specifie d i n sectio n 1 3 o f th e ACD P i s t o b e Collecte d b yAqu a Glas s fo r BW R Associates ; Inc . an d wil l include : A ) Productio n rat e i n fiberglas s bat h tu b units . B ) Pressur e dro p acros s th e boot h boundary . C ) Weigh t o f al l fiberglas s bat h tu b -.tni.t s produce d witr-to* * testin g fro mproductio n dat a c r b yphysicall yweighin g eac h uni t t o withi n on e pound . ( V* D ) Interio r styren e i n ai r testing , utilizin g th e averag.- . 

# V y* 0 o f thre e randoml ylocate d detecto r tub e sanple s durin g

o n e hou r whe n stac k styren e sample s ar e bein g taken . \Q . Thes e sample s ar e t o b e take n fro mth e ai r fiv e fee t .^ 7 _/h abov e th e mai n manufacturin g roo mfloor . Detecto r tube s v l , 0 shal l hav e a styren e rang e o f 2-10 0 ppm . / n *9 . I t i s assume d today , bu t i t shoul d b e confirme d o n o r befor a th e A^y ^ » tes t da ytha t duc t airflo w measurin g meet s th e •cri.ceria.-in.-CDSQ ' Method s 1 an d 2 . Othe r specia l samplin g considerations, . inriudi-:_ g

samplin g sit e configurations , equipmen t limitations , specia l methods , etc. : A ) CDE Q Metho d 8 wil l b e modifie d t o increas e tii e sampl e rat e t o decreas e th e sanpl e tim e t o tw o hour s pe r sampl e o r less . B ) Th e particulat e concentration s obtaine d fro mSourc e H wil l b e utilize d i n combinatio n wit h th e individua l measure d flow s t o determin e mas s emissio n rates . 10 . Othe r Proces s Considerations , includin g intermitten t production , specia l fee d o r product , etc. : proces s operation s a t 33 % o r mor e o f capacity . I n n o cas e wil l samplin g replicate(s ) b e accepte d i f separate d b ya tim e duratio n o f twenty-fou r (24 ) o r mor e hours , unles s prio r authorizatio n i s grante d b yth e Agency . Th e sourc e t o b e teste d mus t operat e a t a nomina l rat e durin g testing . Rate s ne t i n agreemen t wit h thos e stipulate d i n th e Ai r Contaminan t Discharg e Permi t ca n resul t i n tes t rejectio n fo r applicatio n t o detennin e compliance . Impose d proces s limitation s coul d als o resul t i n tes t repor t rejection . Sourc e tes t report s mus t b e suhnitte d t o th e Agenc ywithi n thirt y(30 ) day s o f th e tes t dates , unles s anothe r deadlin e ha s bee n stipulated , eithe r b ypermi t condition , o r th e Departmen t lette r approval . 

# 0 ' k?

92 0 MASO N WA Y • MEDFORD
. OREGON 37501- 1 34 3 • [503 ] 779-264 6

# :"_.__

_BW 

# ft j ASSOCIATES, INC. ^ ENVIRONMENTA L CONSULTANT S Aqu a Glas s wil l sen d on e (1 ) cop yo f th e complete d sourc e tes t repor t t o th e Departmen t o f Environmenta l Quality , Attn : Joh n Hector , 214 6 N E Fourth , #104 , Bend , Orego n 97701 . I f yo u hav e an

yquestions , o r nee d additiona l infonnation , pleas e let'm e know . Sincerely ,
R . L . Gantenbein , Jr . T.E . Genera l Manage r

cc : Scot t Dickson , Aqu a Glas s Sourc e Tes t Coordinator , CDE Q Portlan d RLG/c b 93-0895 X

- 5S C VASC^.-A'A Y • MEDFORD
. OREGO N 37501-134 3 • [503 ] 779-264 6



# 5P. 7



### State o f Orego n 

## Departmen t

o f Environmental Qualit

y Memorandu m

To : Fran

k Messina : ER-Ben

d From : 'Thane Jenni n Subject : Sourc e Tes t Revie w Repo n Permit

Number :

. Aqu aGlas s Tes t Date : ' Klamat h Count y Repor t Received : Sourc e Testers : Engineerin g Environmenta l : Process : Fiberglas s Manufacturer A •': 18-009 3 Marc h 7 , 199 5 Apri l 3 . 199 5 Tvp e o f Facilit v Source s no

t liste d whic h wouldemit

1 0 o r mor e tons/y r

VO C uncontrolled , mediumcos t SIC 308 8 O n Marc h 7 . 1995 a

n ai r sourc e tes t

wa s performe da

t Aqu aGlas s t

o verif y result s fro

ma previou s sourc e tes t

performe di

n Octobe r 1994 . The Departmen

t ha s no t receive d asourc e tes t protoco l nor

wa s notificatio n receive dunti l afte r th e tes t hadbeen performed , therefor e Department

personnel were not

presen t durin g th e testing , an dn o revie w andapprova l o f tes t protoco l i s possible . Th e current

tes t wa s designe dt

o calculate astyren e unit

emissio n facto

r usin g th e styren e emission s fro

mbot h point an dfugitiv e sources . T o simplif y th e styren e fugitiv e emissio n measuremen

t the door s opening o n th e mai n productio n are awer e kep t closed , a s muc

h a s possibl e during th

e test . Also , certai n exhaus t fan s wer e turne dof

f to restric t

th e fugitive emissio n point s t

o a n easily measurabl e number . During th e origina l tes t onl y point

source s wer e use d t o calculat e th e styrene uni t

emissio n factor . Fugitiv e emission s wer e quantifie d indirectly durin g th

e origina l tes t b y measurin g th e ambien t styren e concentration s a

t possibl e fugitive emission point s suc h as doorway s an dexhaus t fans . Th e mos t recen t tes t wa s perfonne dusin g longer sampl e period s andadifferent collectio n medi athe n th e Octobe r 199 4 test . Styren e concentratio n wa s measure dusin g duplicat e charcoa l tub e sample s taken a

t 8 stack s ove r

a10-hou r period . I n additio n to th e above measurements , sho n ter

mstyrene concentratio n was measure da t th e eigh t stack s durin g 5 consecutiv e 2-hou

r periods . Charcoa

l tub e sample s Jv

e r e als o usedto quantif

y styrene emission s a

t th e exi t of fiv e exhaus t fan s ove r a10-hou r period . Th e 10-hour

samplin g perio d wa s chose n to approximat

e th e lengt

h of one shif t at the plant .



## ioP. 8

Mem o To : Fran

k Messin a Ma y 4 , 199 5 Pag e 2 Sma U batter y powere d pump s ar e usedto withdra w stac k ga s fro mth e stac k

through the charcoal tube . Thes e pump s are calibrate da t apanicula

r sample flowrat

e befor e th e tes t an d thi s calibratio n i s checke d afte r th e test . Fou r

of th e pump s faile

d the pos t tes t calibratio n an d therefor

e th e result s fo

r thos e sample s are deeme dunacceptabl e b y NIOS H standards . Stac k ga s velocit

y wa s measure d i n th e stack s onc e durin g th e 10-hou r samplin g period . Stac k ga s velocit

y measurement s ar

e normall y performe di

n triplicate . Durin g the previou s sourc e test , stac

k ga s velocit

y measurement s wer

e performe d6 time s a

t eac h site . Data qualit y i s improve d b y increasin g th e numbe r o f flo w measurements . Upstrea mand downstreamdisturbanc e location s wer e no t recorde dfo

r the stac k ga s velocit

y measuremen

t locations . Sourc e tes t

repon s withou t

thi s informatio n ar

e normall y rejecte db

y th e Department . However , sinc e thi s sourc e tes t wa s no t Departmen

t approve dth

e issu e o f data qualit y requirement s i s moot . Th e combine dvolumetri c flowrat e fro mth e point

source s measure d durin g thi s tes t

wa s 15 % highe r

tha n th e volumetri c flowrat

e measure ddurin g th e previou s test . Th e volumetri c flowrat

e o f th e exhaus t

fan s wa s no t

measure ddirectly , bu t

was calculate d usin g the manufacturer' s fa n curve s an

destimatin g th

e rotationa

l rate o f the fa n blades . Exhaus t fa n emission s comprise d 1% of th e tota l styren e emission s by weight . Tw o charcoal tube s wer e spike d wit h liqui dstyren e a

t one-half the highes t

quantitate d standar d concentratio n and one-fift h o f th e highes t

quantitate dstandar

dconcentration . Th e mean spik e recover y wa s 73.1 % andwa s use dt o correc t al l sample concentration s associate d with thi s analysi s event . Th e sourc e tes t repo n di dno t

contai n the laborator

y repo n or

th e sampl e chai n o

f custody . Th e Depanmen t receive dth

e laborator

y repo n i n asubmitta

l from . Seco r o n Apri l 20 , 1995 . Th e repone d styrene emissio n factor , 8.1 1 lb s styrene/bathtub unit , i s actually the lowes t valu e of th e rang e o

f value s measure ddurin g th e sourc e test . Upon furthe r analysi s o

f th e dat ath e Department

ha s determine dtha

t th e styren e emissio n facto r calculate dove

r a10
- hou r shif t shoul d hav e bee n repone da s 8. 1 lb s styrene/bathtu b uni t < factor < 9. 1 lb s styrene/bathtu b unit . Th e styren e emissio n factor calculate dusin g the shor t ter msample i s useful fo

r compariso n with th e emissio n factor

calculate dfrompreviou s sourc e tes t databecaus e it

mor e closely approximate s th

e 30-minut

e samplin g perio duse ddurin g th e firs t test . Th e 2-hou

r sample s ar e use d t o calculat e an hourly styren e emissio n rat e whic h i s multiplie dby 5 anddivide d b y th e facilit y shif t productio n to calculat e asho n ter memissio n factor . A

n averag e of

the 5 sho n ter memissio n factor s yield s avalu e o f 9. 4 lb s styrene/bathtub uni t which i s exactly th e number repone d durin g th

e previou s sourc e test .


# nP. 9

Mem o To : Fran

k Messin a Ma y 4 , 199 5 Pag e 3 Conclusion s Th e styren e emission factor fo r th e 1994 ai r

sourc e tes t

was 9. 4 lb s styrene/bathtub unit . Durin g th e most

recen t ai r sourc e tes t

areductio n in th e emissio n facto r i s achieve db y extendin g th e samplin

g perio d over

on e shif t length , th e mea

n o f the duplicate sample s i s 8. 6 lb s styrene/bathtub unit . 8. 6 lb s styrene/bathtub uni t i s the appropriat

e emissio n facto

r t o predic t futur e emission s o f

styren e fro mAqu aGlass . Enforcemen t action s shoul dbe base d o n th e previou s Departmen t approve dandwitnesse dtes t becaus e o

f proces s andfacilit

y change s i n th e interimbetwee n test s an dth e fac t tha t th e result s o f th e new sourc e tes t

are no t substantially differen

t than th e previou s test .

cc : Joh n Hector: : DEQ : ER-Ben d Pete r Brewer : DEQ : ER-Ben d A H Nikukar : DEQ : H Q Nanc y Couch : DEQ : H Q



## 1 5P.1 0
September

7 , 1994 " 

# Oregon
DEPARTMEN

T O F ENVIRONMENTA

L R . L . Gantenbe mQUALIT Y

- J -n^ BW

RAssociates , Inc . 92 0 Maso n Wa

y EASTER N REGIO N Medford , Orego n 9750 1 Ben dOffic e Re : Sourc e Tes t

o f Spra y Booth s ACD P 18-009 3 Dea r Mr . Gantenbein : Th e BW RSourc e Tes t

Plan fo r conductin g emission s testin g of spra y boot h emission s an d ambien t ai r a t AquaGlass , Klamat

h Falls , Orego n ha s been reviewe dan di s approve d b y th e DE Q wit h th e followin

g conditions : i 1 ) Th e DE Q mus t

b e notifie dof

an y change s in th e sourc e tes t plan prio r

t o testing . Significan t

change s no

t acknowledge db y th e DE Q which coul daffec t accurac y an

d reliability of

result s wil l resul t

i n tes t report rejection . 2 ) Method-specifi c qualit y assurance/qualit

y contro l (QA/QC ) procedure s mus t b e performe d t

o ensur e tha t th e datai s vali dfor

detenninin g sourc e compliance . Documentatio n o

f th e procedure s andresult s shall b e presente di n th e sourc e tes t •repo n for

review . Omissio n o

f thi s critica l infonnatio n will resul t i n rejectio n of

th e data , requirin g aretest . 3 ) Th e ambien

t ai r concentratio n of

styren e shall b e measure dat fiv e differen

t location s insid

e th e plant usin g EP A Metho dTO-14 , Determinatio n o f Volatil e Orgam c Compound s (VOCs ) i n Ambient

Air Using Summ

aPassivate dCanister Samplin g and Ga

s Chromatographi c Analysis . Th e fiv e samplin g location s will b e determine d b

y takin g 1 0 indicato r

mb e measurement s prio r

t o th e EP A TO-1 4 measurement . The main productio n are ai s to b e divide dint o 1 0 equa l areas , indicato r mb e sample s ar e t

o b e take n a t

th e centroi do

f each equal are aa

t aheigh t o f fiv e feet . Th e fiv

e centroi d measurement

point s wit

h th e highes t styren e concentration , as determine d by th e detecto r tub e wil l b e use da s th e EP A Metho d TO-1 4 measuremen

t point . The EP

A TO-1 4 measuremen

t wil l b e take n a s a3 0 minut e integrate d sample concurrent with on e o

f th e stac k samplin g tests . 

# m 214 6 N E 4t h Stree t Suite . 10 4 Bend . O R9770 1 (503 ) 388-614 6 OEQ/CR-i

m 

# °lP.1 1

R . L . Gantenbein Septembe r 7 , 1994 Pag e 2

«*"---'."''-»-*«-.s-.'>-»*"7>-« v —?»«-rir>-•-"•—» • s._-+:^.JW . •.f»-r

_«•>•«..•.:*.»•**—:'V_-s. - —->»•«.—•*;<- . • - •__.*._«••« • .-_ • —.••.._»,._ • %_». o J^-Tti.ct^.-.... r -..*_._v-<CT.^-o f f-~^;»>-' t _T_i»—«• . '

4 ) Th e followin g site s wil l b e testedin triplicat e for flowrate , moistur

e content , styren e and paniculat e usin g EP A Metho dTO-1 4 andOrego n Sourc e Tes t Method s 1
- 4 an d 8 : Gel Coa t Cubicl e # 1 Gel Coa t Cubicl e Wl Firs t Cho p booths , combine d Bas e Cho p booths , combine d Foa mCubicl e Cover ! Coat

Cubicl e Hea t Roo m Th e EP A TO-1 4 measurement

wil l b e take n a s a3 0 minut e integrate dsample . Th e Metho d 8 wil l b e performe d fo r aperio dt

o b e determine db y th e sourc e tester s o tha t th e metho d detectio n limi t

i s a t leas t 0.001 1 grains - pe r

dr y standar dft 3

. I f th e filter ^ : > weight s m mbu t

t o b e negativ e i t

will b e assume dthat

an insufficien

t sampl e volum e ''- f?i ' ' wa s measure d an d the tes t result s ma

y b e rejected . Flowrate measurement s mus t b e performe d concurrendy wit h the Metho dTO-1 4 measurements . Molecula r weigh t ma y b e calculate d base d o n a n oxyge n concentratio n o f

20.9 % v/ v andacarbo n dioxide concentratio n o

f 0.04 % v/v . 5 ) Styren e emission s shal l b e presente di n th e followin g units ; ppm , lb s styrene/hr , lb s styrene/bat

h m b uni t an d lb s styrene/lb s bat

h m b uni t fo r each emissio n point . PM l 0 emission s shal l b e presente di n th e followin g units ; grains/dscf , PM 10 /hr , lb s PM 10 /bat h tu b uni t fo r eac h emissio n point . 6 ) PJeas e provid e th e nam e an daddres s of

th e laboratory(s ) performin g the analytica l wor k an d acop y o f

their Statement

o f Qualifications . V



### re* 

# 1 0P.1 2

R . L . Gantenbei n Septembe r 7 , 1994 Pag e 3

When submittin g futur

e sourc e tes t

protocol s pleas e includ e al l the informatio n requeste d in Sourc e Samplin g Manual Volum e I , Stat e o f Orego n DE Q Ai r

Qualit y Division , suc

h a s facilit y address , numbe r

of tes t replicate s includin g blanks , etc . Shoul dyou hav e an y question s regardin g th e abov e condition s pleas e feel fre e t o contac t m e at 388-614 6 extensio n 247 . Sincerely , Than e Jenning s Sourc e Tes t

Coordinato r Eastern Regio n - Bend TJ/n s cc : Joh n Hector , Ai r

Qualit y Manager , Easter n Regio n - Ben d Stev e Crane : DEQ:W R Jac k Herbert : DEQ:NW R Denni s Siivola : DEQ:Medfor d Scot t Dixo n Aqu aGlas s Western , Inc . 585 5 Washbur

n Driv e Klamat h Falls , Orego n 9760 3



# l

l%\

Concentration , ng/L r r\ j o i - j c n o c

n ooo o !>?<_

_"•*^SD?e?V_"efo"(j! ^ O l Q O i o o o r o o i • .

c n o 0 1 0 0 o Aceton e Hexana l Ethylbenzen e _

b m.p-Xylen e to 2-Heptanon e •i"" i • "i " " i < 1 • ' i 1

l ' 1 " ! " •"I"' 1 l"" | * [ • * • * 1 • • • • 1 • • O i o o i

0 0 0 •!.••• • !•••• ! o n c n

0 0 o-Xylen e | b Propylbenzen e p Ethy l 3 - ethoxypropionat e Umonen e |C D 2-(2 - Butoxyethoxy)ethano l Naphthalen e fch-O Pentamethylbenzen e •

Junipen e C D Methy l laurat e _ p 1,1.3,3 - Tetramethoxypropan e Hexy l acetat e IndanlJ ) C3-Benzene s Terpene s C4-Benzene s D- o

C5-Benzenes tl < O O o o 3 o ro 3 o 3 (0 & 

# t
o 3 O 

### y If 3 ro ro 3 a • o u » o ' 5 T t r o » a— 0 D O 

### a —o

o a a

• 0 - o » o ro - »

e i dP. M


### STYREN E SOURCE TES T PLA

N FORTH E AQU A GLAS S FACILITY I N KLAMAT

H FALLS , OREGO

N

prepare dfo

r , th e Stat e of Oregon Department

o f Environmental Qualit

y Air Qualit y Divisio n

o n behalf o f Aqu aGlas s Corporatio n 585 5 Washbur

n Wa y Klamat h Falls , Orego n 9760 3
b y Rober t A . Haberiein , PhJD . Engineerin g Environmental 10 0 A Annapoli s Street

, Annapolis , M

D 2140 1 Nei l P . Juiinski , PhD. , C.I.H . NuChemC o Incorporate d 7008- G Litd e River

Turnpik e Annandale , Virgini a Danie l P . Boyd , PhD . Danie l P . Boy d& Compan y Wy e HaU , Wy e Islan d Queenstown , Marylan d

Februar y 21 , 199 5 MA Y J c 19=

5 CEm Kl__8»_ N 6EM D 

# / 3P.1 5 Engineerin g Environmental Consultin g Service s

! Lis t

o f Figure s 1- * Styren e Concentratio n Profil e a t Typical Bathware Facilit

y H- 3 2 Diagramo f

th e Aqu aGlas s Proces s an dStyren e Emission s H- 4 3 Cross-sectio n View of aTypica l Waterfal l Spra

y Bo o tf i H- 5 4 Diagra

mof EP A Metho d 1 8 Integrate dBa g Samplin g Trai n H- 7 5 Diagra

mof Recommende d Stack

Tes t Setu p 11-1 2

Lis t of Table s 1 Stac k & Fa n Description s - Expecte dFlow s & Concentration s H- 2 2 Sampl e Ro w Rat

e versu s Sampl e Duratio n & Concentratio n 11-1 4 3 Typica l Sampl e Trai n Pum p Specificatio n H-1 7 4 Precisio n Rotamete

r Calibratio n Dat aH-1 8 5 Standar d Charcoa

l Adsorptio n Tube s 11-2 0
Lis t of Appendice s A Roo f Fa n Performanc e Curve s fro

mLore n Coo k

u i 

# HP.1 6 Engineerin g Environmenta l Consultin g Service s I . B . Oregon DE Q Sourc e Tes tPla n Requirements Accordin g t o th e Orego n DE Q Sourc e Samplin g Manual , asourc e tes t pla n shal l include , a s aminimum , th e followin g fifteen items : 1 . Sourc e nam

e an d address . 2 . Sourc e sit

e personnel ; contac t

nam e andphon e number . 3 . Sourc e testin g personnel ; company , contac t nam e andphon e number . 4 . Schedule d date o f

th e sourc e test . 5 . Sourc e description , includin g adescriptio n o f th e pollutio n contro l devic e an dsampl e locations . 6 . Pollutant

t o b e measured . 7 . Tes t

methods . 8 . Numbe

r o f samplin g replicates . 9 . Applicabl e process/productio n information t o b e collecte ddurin g the sourc e tes t 10 . Contro l devic e operatin g parameter s t o b e monitore ddurin g th e testing . 11 . Fue l sample s an d typ e o f analysis ; wh o wil l collec t the mandwho wil l perfor mth e analysis . 12 . Visibl e emission s measurements ; wh o wil l take opacit y reading s durin g th e sourc e tes t andar e they , certified . 13 . Othe

r samplin g considerations . 14 . Othe

r proces s considerations . 15 . Th e sourc e test

pla n shal l include the followin g statements , unles s otherwis e specifie d b y ACD P cc-ndition o r

DE Q lette r a . Th e duc t

ai r flo w measurin g meet s criteri ai n EP A Method s 1 an d2 . b . Th e samplin g replicate s shal l no t b e separate db y atime duratio n greater than twenty-fou

r hours . c . Th e sourc e t o b e teste dmus t b e operate da

t anorma l productio n rat e durin g testing . d . Th e DE Q mus t

b e notifiedo

f an y change s i n sourc e tes t

plan s prio r

t o testing . e . Mediod-specifi c qualit y assurance/qualit

y contro l (QA/QC ) procedure s mus t b e performe d t o ensur e datavalidity . Documentatio n o f th e procedure s an d result s shal l als o b e presente di n the sourc e tes t repor t fo r review . f . Sourc e tes t

report s mus t

b e submitte dt

o th e DE Q within thirt

y days . g . Tw o (2 ) copie s o f

th e complete dsourc e tes t

repor t mus t b e sen t t o th e Department ; on e (1 ) t

o the DE Q Regional Operation s staf f perso n responsibl e fo r th e sourc e an d th e secondcop y t o th e Sourc e Testin g Coordinator , Department

o f Environmenta

l Qualit y Headquarter s i n Portland . Th e followin g section s discus s severa l source-specifi c testin g details , describ e th e logistic s o f the stac k tes t plan an d provide ates t

pla n summar

y i n the Oregon DE Q forma t
1- 2 

# 1 5P.1 7 

### Engineerin g Environmenta

l Consultin g Service s 

### A substantia

l amoun t o f the finer aerosol s pas s through th

e booth' s separation baffle s an d remai n in th e exhaus t Thes e fine aerosol s pos e aspecia l proble mfo r the charcoa

l wbes , becaus e the moistur

e could saturat

e th e carbo n adsorben t an dinterfer

e wit h the sampling . Therefore , i

t i s recommende

dtha t th e wate r leve l i n the boot h pa n shouldb e dropped below the lowe r edge o f the entrainmen

t throa t t o sto p th e formation o

f aerosol s i n the exhaus t durin g th e tes t Thi s actio

n shoul dhav e n o impac

t upo n th e styren e concentration level in th

e exhaust .
TABL E 1 Stac k

& Fan Description s - Expecte dFlow s & Concentration s Stc k I D 1 2 3 4 5 6 7 8
Fa n I D A B C D E Re f I D D (EF-20 ) C (EF-21 ) L (EF-27 ) J (EF-23 ) H (EF-13 , EF-19 , EF-25 ) P (EF-22 , EF-26 ) X

- (EF-31 )
Ref ID EF-1 0 EF- 3 EF- 7 EF-4 3 EF-1 4 Sourc e

Descriptio n Ge l Coa t # 1 ! Ge l Coa

t # 2 FoamCoa

t Cover Coa t Firs t Chop Bas e Chop Roll/Hea t Room Mi x Room
Fan Descriptio n Maintenanc e Are a Finishin g Are a Warehous e Are a Productio n Are a Receivin g Are a Stac k

Diamete r (inches ) 3 4 3 4 2 4 3 4 3 4 3 4 2 8 3 4 Expecte d Flowrate (dscfm) 4,00 0 24,00 0 30,00 0 4,00 0 12,00 0 Expecte d

Howrat e (dscfm) 13,30 0 13,50 0 7,50 0 10,30 0 26,20 0 18,10 0 8,200 N/ A Expecte dRang e Concentratio n (ppm ) 125-25 0 • 125-25 0 20-5 0 100-20 0 125-25 0 25-7 5 25-7 5 N/A Expecte dRang e Concentratio n (ppm) 5-1 0 5-1 0 5-1 0 5-1 0 5-1 0



### n-2 MtP.1 8 Engineering Environmenta l Consultin g Service s FIGUR E 1 Diagra

m o f th e Aqu a Glas s Proces s an d Styren e Emission s

Vent X

_ /

Hea tRoo m Vent D Clea n Mol d w mea

n Mor a ^

Vent C
Ge l Coa t# 1 GerCoa

t#2

Firs tChoppe r Vent H 

# v" Vent V

Ye m

Vent P Bas e Choppe

r Vent L Foa m Coa t
Cove r Coa t Ven tJ

Legen d 

# L Remov

e fro m Moi d Touch-u p 

# 4 * Shipping/Warehous

e i

I Vente d Ai r Emission s > • no w


### n- 4 

# \nP.1 9



# 9 9 9 <? i 9 9 9 ????? ?

BLOCKE D FAN« C

BLOCKE D BLOCKE D

MrHojIIO n BLOCKE D

FAN# D STAC K # 6 fcahH

FAN# E

tota aa raw «E A B*S I OO P STACK « mr - I I I I ' < - 

### T^T ^ f%

> 

# ' ''a^ 1 

# ' W j

STAC K # 7 STAC

K #4 ir * <«- « STAC K # 3 tal Sta , BLOCKE D



# ~ d — 0

— 0 

# —0 '

— 0

- 0

- 0 

# .- 0

- ©

— 0

- 0 STACK . *i 0U_ _ 

# '- 0

- 0 Ihb ,



# r *P.2 0 Engineerin g Environmenta l Consultin g Services FIGUR E 3 Cross-sectio n Vie w o f a Typical Waterfal

l Spra y Boot h 

### S- O

ADJUS T SAWTOOT H O N ITSn © FO R PROPE R UiVbHEf c PSRFORMtMC S



### n- 5 

# \°\P.2 1 Engineerin g Environmenta l Consultin g Service s FIGUR E 4 Diagra

m o f EP A Metho d 1 8 Integrate d Ba g Samplin g Trai n

Stac k Wal l Filte r (glas s wool )

Revers e (3" ) Typ o Pitot Tub e

Rigi d Leakproof Containe r



### n- 7 

## 10P.2 2 Engineerin g Environmenta l Consultin g Service s 7.4.1. 8 Rotameter . O t o 10 0 cc/min , t o detec t change s in flow rate during sampling . 7.4. 2 Samplin g an d Analysis . I t i s suggeste d tha

t th e tester follow th e sampling an d analysi s portio n of th e respectiv e NIOS H metho dsectio n entitle d "Procedure.' ' Calibrate th e pum p and limitin g orific e flow rate throug h adsorptio n tube s wit h th e bubbl e tub e flowmete r befor e sampling . Th e sampl e syste m ca n b e operate d a s a"recirculatin g loop " fo r thi s operation . Recor

d the ambien

t temperatur

e an d barometri c pressure . Then , durin g sampling , us e th e rotameter t o verif y tha t th e pum p an d orific e samplin g rat e remain s constan t Us e asample probe , i

f required . Minimiz e th e lengt h of flexible tubing between th e prob e an d adsorptio n tubes . Severa

l adsorptio n tube s ca

n b e connecte d i n series , i f th e extraadsorptiv e capacit y i s needed . Provide th e ga s sampl e t o the sample syste ma

t apressur e sufficien t fo r th e limitin g orific e t o function a s asoni c orifice . Recor d the tota l tim e an d sampl e flow rate (or th e numbe

r of pum p strokes) , th e barometri c pressure , and ambien t temperature . Obtai n atota l sample volum

e commensurat

e wit h th e expecte d concentration^ ) of th e volatil e organic(s ) present , and recommended sampl e loadin g factor s (weigh t sampl e pe r

weigh t adsorptio n media) . Laboratory * test s prio r t o actua l samplin g ma

y b e necessai y t

o predetermin e thi s volume . Whe n more tha

n on e organi c i s present

in th e emissions , the n develo p relativ e adsorptiv e capacit y information . I f

wate r vapo r i s presen t i n th e sampl e a t concentration s abov e 2 to 3 percent , th e adsorptiv e capacit y ma y b e severel

y reduced . Operat e th e ga s chromatograph accordin g to th e manufacturer' s instructions . Afte r establishin g optimumconditions , verif y and document

thes e condition s durin g al l operations . Analyz e th e audit sample s (se e Sectio n 7.4.43) , then th e emissio n samples . Repea t th e analysi s of

eac h sampl e unti l th e relativ e deviatio n o f tw o consecutiv e injection s doe s no t excee d 5 percen t 7.4 3 Standard s an d Calibration . Th e standard s ca n b e prepare d according to th e respectiv e NIOS H method . Us e aminimu

mof thre e differen

t standards ; selec t

th e concentration s to bracke t th e expecte d averag e sampl e concentration . Perfor mth e calibratio n befor

e an d afte r eac h day' s sampl e analyses . Prepare th e calibratio n curv e b y usin g th e leas t square s method . 7.4. 4 Quality Assurance . 7.4.4. 1 Determinatio n o

f Desorptio n Efficiency . Durin g th e testin g program , determin e th e desorptio n efficiency i

n th e expecte d sampl e concentratio n rang e fo r eac h batc h of

adsorptio n medi at o b e used . Us e an intemal standard . A minimu mdesorptio n efficienc y of S O percent shal l b e obtained . Repea

t th e desorptio n determinatio n unti l th e relativ e deviatio n o f tw o consecutiv e determination s doe s no t excee d S percent . Us e di e averag e desorptio n efficiency o f thes e tw o consecutiv e determination s fo r the correctio n specifie d i

n Sectio n 7.4.4.5 . I f

th e desorptio n efficiency o

f th e compound(s ) o

f interes t i s questionabl e under

acmal samplin g conditions , us e o f th e Metho d of

Standar d Addition s ma

y b e helpfu l to determine thi s value . 7.4.4. 2 Determinatio n o

f Sampl e Collectio n Efficiency . For th e sourc e samples , analyz e th e primar y an d backu p portion s of

th e adsorptio n tube s separately . I f the backu p portio n exceed s 1 0 percen t of th e total amoun

t (primar y and back-up) , repea

t th e samplin g wit

h alarge r sampling portion . 7.4.4. 3 Analysi s Audi t

Immediately befor

e th e sampl e analyses , analyz e the tw o audit s i n accordanc e wit h Section 7.4.2 . Th e analysi s audi t shal l agre e wit

h th e audi t

concentratio n withi n 1 0 percen t 7.4.4. 4 Pum p Lea k

Check s an dVolum e Flo w Rat e Checks . Perfor mbot h of thes e check s immediatel

y afte r samplin g wit

h al l sampling trai n component s i n place . Perfor mal l leak-check s according t

o th e manufacturer' s instructions , an d recor d the results . Us e the bubble-tub e flowmete r to measur e th e pum p volum e flo w rate wit h th e orific e used i

n th e tes t sampling , an d recor d th e resul t I f H- 9 

## 7. 1P.2 3 Engineerin g Environmental Consultin g Service s B L D . Recommende d Tes t Protoco l Th e recommende d styren e vapo r sourc e tes t

protoco l fo

r th e Aqu aGlas s Plan t

i s EP A Metho d 18 , incorporatin g NIOS H Metho d150 1 adsorptio n tub e collectio n a s specifie di n Sectio n 7. 4 an d adjuste d fo r th e expecte dstyrene concentrations . Th e recommende dmetho d i s hencefort

h referre d t o a s th e "Alternate EP A Metho d18. " I

n general , th e Alternat e Metho d 1 8 protoco l use s EP A Metho d 1 8 procedure s to measur e th e exhaus t stac k flo w rate s wit

h a pito t tube/manometer

an d t o measure th e samplin g flow rate s wit h aprecision-metere d an d calibrate d samplin g train . NIOS H Metho d150 1 procedure s ar e use dt o collec t an danalyz e th e styren e vapo r

concentratio n in th e exhaust . Th e actua l flo w rate s throug h th e tube s ar e adjuste d t o preven t

sorben t breakthroug h an dt o ensure tha t th e styrene-to-carbo n mas s loadin g rati o remain s withi n th e validate drange . A diagra mo f th e recommende dtes t

setup i s show n in Figur e 5 . A detaile d descriptio n o f th e testin g equipmen

t specification s i s provide d i n Sectio n II- E below , a s par t o f th e QA/Q C procedures .
Th e followin g thre e (3 ) set s of styren e sample s wer

e include da s par t

o f thi s sourc e tes t fo r th e Aqu aGlas s Plant : * Tw o (2 ) concurren t

ten-hour integrate dcharcoal tub e sample s per stac k fo r the eigh t (8 ) stacks , durin g on e (1 ) ten-hou r productio n shif

t * Fiv e (5 ) consecutiv e two-hour integrate dcharcoa

l tub e sample s pe r

stac k fo r th e eigh t (8 ) stacks , durin g on e (1 ) ten-hou r productio n shift . Not

e tha t thes e sampl e ru n concurrentl y wit

h th e ten-hour

samples . * On e (1 ) ten-hou r

integrate d charcoal tub e sample s pe r roo f fa n fo r th e fiv e (5 ) operational roo f

fan s durin g on e (1 ) ten-hour productio n shif

t Tes t Equipmen t

- Thi s tes t

protoco l use s astandar

dpito t tub e & manometer

to measure exhaus t

duc t velocities , an duse s aprecisio n hot-wir e anemomete

r t o verif y lo w duc t velocit y measurements . Styren e sample s are collecte di n standardcharcoa

l sampl e tube s usin g sampl e flow pump s tha t ar e calibrate dwit

h aprecisio n rotameter

meter . Th e sampl e pump s are activate d b y internal timers , whic h allow s fo r simultaneou s startin g andstoppin g o f al l pumps . A singl e sampl e pum p i s connecte di n serie s to tw o (2 ) charcoal tube s pe r stack (sampl e replicates ) throug h acalibrate dflo w manifold . A standar dcolorimetri c detecto r

tub e i s use d t o measur

e th e approximat

e styren e concentratio n i n di e exhaus t duc t durin g samplings
Atmospheri c pressure i s measure d wit h aportabl e barometer . Th e exhaust' s dr y bul b and wet bulb temperature s are measure d wit h adigital thermomete

r and/o r certifie dglass-bulb thermometers . H-l l 

# 2 tP.2 4 Engineerin g Environmental Consulting Service s Samplin g Locatio n - th e preferre dsamplin g locatio n i s insid e th e plant building , a t th e suction-sid e stack

section s tha t

lea dfiromth e spra

y booth s to th e roof-mounte dexhaus t fans . Thes e indoor

location s hav e auniformly war mambien t

ai r temperature , whic

h ensure s prope r operatio n of

th e samplin g equipmen t

andminimize s calibratio n drif t du e t o temperatur e fluctuations . Th e suctio n side o f th e exhaus t

duc t i s als o mor

e suite dt o th e sampl e pum

p back pressure specification s an doffer s abetter flo w profil e fo

r th e pito t tub e measurements . Stack

# 1 throug h Stac k

# 4 will b e sample dinsid e th e building , usin g a combinatio n o

f floor-mounte d scaffoldin g an dexistin g suspende dequipment catwalks . Not e tha t thes e location s ar

e withi n th e distance-to-flow-disturbanc e guideline s specifiedi n Metho d 1 an d Metho d 2 . However , fou

r (4 ) of th e stack s t o b e teste d(Stac k # 5 t o Stac k #8 ) wil l require outdoo r sampling location s o n th e plan t roof . Roof-top acces s i s neede dbecaus e tw o o f thes e stack s consis t

o f multipl e exhaus t

stream s tha

t are manifolde dtogether

o n th e roo

f (tw o separat e flows fo

r Stack # 6 an d thre e flow s fo

r Stack #5 ) an dtw o o

f th e stack s (Stac

k # 7 an d Stac k #8 ) canno t

b e easil y accesse d fromwithi n th e building . In order to rninimiz e th

e effect s o f col d an d wind

y weather , temporar

y heate denclosure s wil l b e constructe daroun d eac h o f thes e outdoor

stacks . Thes e enclosure s will b e constructe dfromstee l scaffoldin g covere d wit

h polyethylen e plasti c fil man dheate dwit h smal l electri c heaters , i

f necessary . Not e tha t thes e location s ar e als o withi n th e distance-to-flow-disturbanc e guideline s specifie d i n Metiio d 1 and Metho d 2 . Sampl e Flo w Rat e - base d upo n a800/20 0 m g charcoal tube , th e sample flo w rat e fo r eac h stac k

sampl e wil l b e se t

betwee n 30 0 an d75 0 ml/min . Th e flo w rat e i s adjuste d withi n thi s rang e to ensure tha t th e styrene-to-carbo n mas s loadin g rati o remain s within th e validate d rang e specifie d i n Metho d 150 1 fo r th e expecte dstyren e concentration s and samplin g intervals . Th e approximat e samplin g concentration s wil l b e checke ddurin g eac h da y o f testin g usin g one-minute gra b sample s take n wit

h standardcolorimetri c detector tubes . NuChemC o ha s prepare d atabl e o f recommende dsampl e flow rate s base dupo n sample duratio n an d styrene concentration s i n th e exhaus t Thi s tabl e i s show n i n Tabl e 2 belo w [Re f

- NuChemCo] . Th e following six (6 ) agencie s hav e adopte do r accepte dth e recommende dMetho d 1 8 procedure s fo

r stack testin g o f styren e emission s from fiberglass manufacturin g facilities : Virgini aDAP C - styren e vapo r stack testin g a t thre e (3 ) fiberglass manufacturing facilitie s [re f

- EES Reports ] Pennsylvani aDE Q - styren e vapo r stac k testin g to sho w complianc e wit h operatin g penni t fo r afiberglass par t

facilit y [re f - EE S Reports] . Missouri DNR- styren e vapo r stack testin g fo r fiberglass truc k

manufacturing facilit

y [re f - EE S Report] . E-1 3



# 2 3P.2 5 Engineerin g Environmenta l Consultin g Service s Californi aSCAQM D - styren e stac k testin g fo r afiberglass manufacturer [re f -EES] . i Ohi o EP A - styrene vapo r stac k testin g at tw o (2 ) fiberglass par

t manufacturin g facilitie s [re

f - EE S Reports] . EP A Offic e of

Ai r an d Energ y Engineerin g Researc h Laboratory , Researc h Triangl e Par k

- Metho d 1 8 i s currentl y use dt o measur e styren e emission s at

aNort h Carolin abathwar

e facilit y [re f - Bobb y Daniels, Tas

k Officer , EPA , AEERL] . II . E . QA/Q C Procedure s & Analysi s of Testin g Erro r Th e qualit y assuranc e an d qualit

y contro l (QA/QC ) procedure s an dcalculatio n of measurement

erro r fo r si x (6 ) important

tes t variable s ar

e liste di n th e followin g sections . E L E . 1 . Exhaus t

Flo w Rate s PITOT TUBE & MANOMETER Th e tes t protoco l will us e aDwye r Instrument s Mode l #125-A V incline dmanometer , o r it s equivalent , wit

h a0.0 " t o 1.00 " wate r

column stati c pressure an da0.005 " scal e precision , o r

aDwyer Instrument s Mode l #125-A V incline dmanometer , o r it s equivalent , wit h a0.0 " t o 2.00 " wate

r colum n stati c pressure anda0.02 " scal e precision . The pito t

tub e i s aDwye r

mode l #160-36 , o r

equivalent , stainles s stee l pito t tub e wit h a36 " insertio n lengt

h tha t complie s wit

h ASHRA E an d AMC A specifications . An equivalent "S-type " manometer ma y b e substituted
- The equatio n t o calculat e ai r velocit y fro mth e pito t

pressur e differenc e readin g is : ai r velocity (fpni ) = 1096 2 x A pressure (i n wg) 0 5 ai r density 0- 5 [e q 1 ] wher e th e dry air

densit y i s given by : air densit y = : 1.32

5 x barometri c pres s (i n Hg ) ai r temperatur

e (°R) [e q 2 ] Th e ASHRA

E psychometri c table s wil l b e use dt o correc t th e dr y ai r densit y du e t o th e relative humidit

y o f th e exhaus t Assumin g standardcondition s (usin g adr y air densit y o f 0.075) , th e reading s provide d b y th e pito t tube/manometer

in th e lowes t expecte dvelocit

y rang e of abou t 1,06 0 fp mis : H-1 5



# itP.2 6 Engineerin g Environmental Consultin g Service s I L E . 2 . Sampl e Flo w Rat e Th e samplin g trai n wil l us e aSKC Mode l #224-PCXR 8 precisio n samplin g pump , o r it s equivalent , t

o dra w aprecis e sampl e volum e throug h th e charcoal adsorptio n tube . Accordin g t o th e SK

C performanc e specifications , th e Model #224-PCXR 8 pum p ha s th e followin g characteristic s [re f - SKC; Operatin

g Instruction

s fo r Universa l Sampl e Pump , Mode l 224-PCXR8; For m#37713 ; Au

g 92] : TABL E 3 Typica l Sampl e Trai n Pum p Specificatio n Flo w rang e - , 1,00

0 to 5,00 0 ml/mi n ; 10 0 t o 50 0 ml/mi n wit

h lo w flow contro l Flo w contro l - ± 5 % set poin t constan t flow Flo w compensatio n range : 75 0 ml/mi n 1,00 0 2,00 0 2,50 0 3,00 0 4,000 ; RunTim e - 5 " to 40 " water bac k 0 " t o 40 " 0 " to 40 " 0 " to 40 " 0 " t o 35 " 0 " to 20 " 8 h r minimu ma t

4,00 0 ml/ n pressur e

tin an d 2 Operatin g Temperature - -20° C t o 45° C (-4° F to 113°F ) Th e combine d exhaus t

duc t stati c pressure an dcharcoa l tub e pressure dro p shoul dno t excee d thes e compensatio n ratings . Th e sampl e pum p flo w accurac y a

t asamplin g rat e o f

on e (1 ) lite r pe r minute wil l b e ± 5 0 ml/minute . Thi s tes t samplin g trai n wil l als o us e aCole-Parme r Instrument

Company , Chicago , EL , Mode l 3216-4 5 precisio n rotameter , o r it s equivalent , t

o QA/Q C th e flo w rate caUbration o f th e sampl e pumps . Cole-Palme r provide s flow mete

r caUbratio n dat atable s [re

f - Cole-Palme

r Documen t No . 217 ] for several combination s o f

tub e an dfloat

whic h include s flow meter tub e #N112-0 2 a

t standard condition s o

f 70° F an d14.7 0 psi ausin g a n 1/8 " diamete r

carbolo y float (stoc k #ZC 2 wit

h adensit y of 14.9 8 g/ml) , a#N082-0 3 a t standar dcondition s of

70° F an d 14.7 0 psi ausin g a

n 1/8 " diameter

glas s floa t wit h adensit y of 2.5 3 g/ml , an d#N082-0 3 at standard condition s of

70° F an d 14.7 0 psi ausin g a n 1/8 " diamete

r stainles s stee l float

wit h a densit y of 8.04 g/ml . Thes e calibratio n curve s are Uste di n Tabl e 4 below . E-1 7 

# Z$P.2 7 "•*** i ^"**** i Engineerin g Environmenta l Consultin g Service s Th e QA/Q C procedure for th e loca l barometri c pressur e reading s i s provide db y comparin g th e local measurement a t th e plan t wit h th e barometri c pressur e reporte da t th e nearb y weathe

r recordin g station , locate da t th e Klamat h Fall s airpor t I L E . 4 . Exhaus t

Temperatur e A digital thermomete

r and/o r glas s bul b thermometer

wil l b e use dt o measur e th e exhaus t temperature . An

y thermometer

wit h a± 1 % accurac y an dadispla y resolutio n of 0.1° C (0.2°F ) i s suitable . Stac k exhaus t temperatur

e readings wil l b e recorde da t th e en d o f eac h duc t traverse . Th e QA/Q C b f

th e temperature measurement s wi U b e perfonne dby comparin g th e simultaneou s steady-state temperature reading s o f th e digita l thermometer

an dafull
immersio n glas s ste

mlaborator

y thermomete

r wit h a0.1° C resolutio n tha

t meet s SAM A an d NIS T requirement s fo

r accuracy . I

f th e exhaus t

exhibit s arang e o

f temperatures , aserie s o f QA/Q C temperatur

e comparison s wil l b e performe d a t th e low , middle , an dhig h temperatur e value s withi n th e exhibite d range . E L E . 5 . Relativ e Humidit y A digital thennomete r

and/o r glas s bul b thermometer

als o wil l b e use dt o measure th e dry-bul b an d wet-bul

b exhaus t temperatures . An

y thermomete r

wit h a± 1 % accurac y an d a displa y resolution of

0.1° C (0.2°F ) i s suitable . Th e we t bul b readin g i s measure dafte r awe t "sock " ha s been place d over th e temperatur

e probe . Wet-bul b temperatur e reading s wil l b e recorde d a

t th e beginnin g o

f eac h duc t

traverse . Th e QA/Q C o

f th e relativ e humidit

y measurement s wi

U b e provide db y comparin g th e simultaneou s steady-state wet-bulb/dry-bulb temperature readings of th e digital thennomete r an d abenc h top wet-bulb/dry-bulb hygromete r that incorporate s tw o (2 ) NIST-certifie d full
immersio n glas s ste

mlaborator

y thermometers . E L E . 6 . Styren e Vapo r

Concentratio n Severa l size s o f charcoa l adsorptio n tube s ar e commerciall y available , a s show n i n Tabl e 5 below . Th e prope r combinatio n o

f flow tub e siz e an dsample flow rate wil l b e dependent upo n th e styren e concentratio n o f th e exhaus t an dthe sampl e duration . Fo r relativel y high-concentratio n stac k samples , th e stac k

tes t protoco l will us e aSK C mode l 26
- 1 6 mb e wit

h a20 0 mg bac k

sorben t sectio n anda80 0 m

g front sorben t section , a s specifie d i n Sectio n 7.4.1. 6 o

f EP A Metho d 18 . However , asmaUe r tube , suc h a s mode l 226-01 , ma y b e use d t o sampl e lo w styren e concentrations . A smalle r tub e generaU

y increase s th e H-1 9 

## 2&P.2 8 Engineerin g Environmenta l Consultin g Service s A detaile d descriptio n of

th e AML G C analysi s procedur e i s availabl e b y phon e fromMr . Chri s Cas e o

f America n Medica l Laboratorie s a

t (800 ) 348-1590 . DETECTOR TUBE

EQUIPMENT Thi s tes t setup use s aKitigaw aMode l #8014-400A detector tub e piston-typ e pump , o r it s equivalent , t o estimate th e sampl e concentratio n durin g th e stack sampling . Th e correspondin g detecto r

tub e for styren e vapo r

i s aMatheso n Mode

l #158 S wit h asampUn

g rang e from5 t o 30 0 pp mwit h on e stroke , 2. 5 to 15 0 ppmwit h tw o strokes , an d1 0 t

o 60 0 pp mwit h one-hal f stroke . E L F . Miscellaneou s Productio n Dat a I n order to correlate th e measure dstyren e emission rate s wit h th e correspondin g productio n activity , th e foUowin g plan t productio n dat awil l b e recorded durin g eac h da y o f testing : * Productio n shif t star t an dsto p times . * Number

o f wor k breaks ; includ e th e star

t an dstop time o f

eac h break . * Numbe

r o f unit s produce dan dlaminat e surfac e are aof

eac h unit . Also , an y modification s t o th e plan t that woul daffect

ventilatio n flo

w rate s durin g th e testin g wi U b e recorded. Thi s includes :

Openin g an d closin g of

exterio r buUdin g doors . Deactivatio n o r

activatio n of

ventilatio n fans . Replacemen

t o r remova l o f

spra y boot h filters. Th e number

o f unit s produce d durin g aten-hour wor k shif t i s the su mof th e foUowin

g thre e values : One-half

of th e number

o f unit s i n proces s at

th e beginnin g o

f th e shif t A U o f the unit s starte d an dcomplete ddurin g th e shif t One-half o f th e numbe

r o f unit s i n proces s a

t th e endo f th e shif t

n-2 1 

# 2. 1P.2 9

Pollutan t t o b e measured : Styren e vapo r

only . Engineerin g Environmental Consultin g Service s Fan I D A B C D E Fa n

Descriptio n Maintenanc e Are a Finishin g Are a Warehous e Are a Productio n Are a Receivin g Are a Expecte d

Flowrate (dscfm ) 4,00 0 24,00 0 30,00 0 4,00 0 12,00 0 Expecte dRang e

Concentratio n (ppm) 5-1 0 5-1 0 5-1 0 5-1 0

. 5-1 0

Tes t method s Exhaus t Ro w Rat e - Barometri c Pressur e - Ai r Temperatur

e - Relativ e Humidit

y - Styren e Concentratio n & Sampl e Flo w Rate EP A Metho d1 & EP A Metho d2 EP A Metho d18 , Sectio n 7.4.1 . NIST-certifie d Thermomete r We t bulb/Di y bulb Thennometer EP A Metho d18 , usin g Sectio n 7. 4 Absorptio n Tub e Procedure , equivalen t

t o NIOS H Metho d150 1 Numbe r o f samplin g repUcate s On e (1 ) da

y o f testing , consistin g of

atypica l ten-hour workshift : Tw o (2 ) simultaneou s integrate dten-hou r sample s per

stack , fo r eight (8 ) stacks . Fiv e (5 ) concurrent

integrate dtwo-hour

sample s pe

r stack , fo r eight (8 ) stacks , taken concurrentl y wit

h th e ten-hour

samples . On e (1 ) integrate d two-hou r

sample s pe r

roo f fan , fo r five (5 ) roo f

fans , take n concurrentl y wit

h th e ten-hou r

stac k samples .



### m-2 

# 21P.3 0 Engineerin g Environmenta l Consultin g Service s d . Th e DE Q sha

U b e notified , i n writing , of an y change s in sourc e tes t

plan s prio r t o testing . e . Method-specifi c quaUt y assurance/quaUt

y contro l (QA/QC ) procedure s sha U b e perfonne d t o ensure dat avaUdity . Fu U documentatio n o

f the procedure s an d results sha U als o b e presente di n th e sourc e tes t report fo r review . f . Th e sourc e tes t

report shal l b e submitte dto , th e DE Q within thirt y day s o f th e las t da y o f testing . g . Tw o (2 ) copie s of

th e complete dsourc e tes t

repor t sha U be sen t t o th e department ; on e (1 ) to th

e DE Q Regional Operation s staf f perso n responsible fo r th e sourc e an d the secon dcop y t o th e Sourc e Testin g Coordinator , Department

of Environmental QuaUt

y Headquarter s in Portland . 16 . Signature s > Fo r th e Aqu aGlas s Corporation :

nam e ^t e titl e Fo r Engineerin g Environmental :

name dat e title


### m- 4



# ii \Engineerin g Environmental Consultin g Service s FIGUR E 6 a Performance Curv e fo r Fa n # A P.3 1

LORE N COO K-COMPAN V MOOE L NO
. 30-LS U TES

T NO
. 88-160 IMPELLER DIA

M 30.1 3 OUTLE

T ARE A 5.07 4

1.7 5

1.2 5 C D X I > 7- : 

### m x o n m T ) 

### o 2s _ m X

3 4 6 6

- 7 8 8 1 0 

### cr i n u tn&&\A \ \ n 

### 1000' S 1 1 1 2P.3 2

Engineerin g Environmenta l Consultin g Service s FIGUR E 6 c Performanc e Curv e fo r Fa n # C

STEE L U P BUS T PROPELLE RVENTILATOR* MODE L SU B HIG H TEMPERATUR E SMOK E CONTRO L VENTILATOR- MODE L SUB H FA N * « £

4 3

M CATALO G

NO .

*»SU 8 •n d 4WU8 H

54-SU B MOTO R

M P S

7-1/ 2

1 0

I S

2 3

5

7-1/ 2

1 0

I S
a RP M SS S 01 0 es s w o 68 5 71 0 73 5 7B0 78 5 SI O S3 5 M O 36 5 39 5 42 2 45 5 O S 51 5 54 5 57 S 80 S S3 S 60 S 89 5 72 3 F

A ch l BM P 3014 5 3.80 S 3143 J 4.42 8 szn i 4.88 5 3400 9 IOC S 3529 7 127 0 3656 6 tsa S767 4 7J4 6 381S 2 156 3 4045 0 8.43 6 4173 9 10J6 7 4302 7 11.35 7 4431 5 1140 6 2803 7 1* 9 3034 1 148 5 3264 5 3.10 8 3485 0 SJ U 3725 4 4.81 9 3855 9 S_S3 1 4106 3 1&S 5 441( 7 7.68 8 4S47 2 is« 4 4877 8 .(Uf a 5108 1 HJ0 7 S338 5 1358 3 5568 9 15.43 0 1/

1 BH P 2B58 1 4.08 8 2984 4 4.81 8 3129 8 5.18 2 3264 2 581 3 3388 4 8.48 2 3532 2 7.20 1 3865 7 7J7 2 37B8 8 8.79 4 3331 7 8.67 7 4064 1 10.81 5 4186 3 11.61 2 4326 4 12.87 0 2481 5 2.12 4 2725 1 166 8 2381 1 szn. S232 6 4.01 2 3480 4 4.83 0 3728 1 5.7S 4 3970 1 8.78 3 4212 2 una 4453 2 8.2S 1 4693 2 10.8* 8 4832 3 12.18 8 5170* . 1X89 6 6408 1 15.74 8 1/

4 CP M BH P 2652 7 4_31 S a m 4.64 2 2SS2 4 5.41 8 3108 3 6.03 9 3252 3 8.71 2 3383 5 7.43 7 3534 0 8.21 2 3872 6 9.04 4 3810 2 9.8J 1 3947 3 10.67 5 4064 0 11.67 8 4220 2 12.84 3 1681 6 2.19 6 2218 6 173 5 2538 2 345 4 2883 6 4.16 7 3194 5 102 3 3470 6 iMi 3735 8 ion. 389S 3 1.18 4 4248 2 149 0 4500 8 1081 8 4750 3 12.48 6 4996 9 14.18 6 8242 4 16J0S 2 1* 1 CP U 8H P 2(02 6 4,48 1 2554 6 S.04 4 2707 2 5.66 7 2865 1 6.32 7 3035 5 7.01 S 3206 1 7.73 3 3366 0 6.50 2 3523 2 9.32 7 3671 2 10i1 4 3817 8 11.15 8 3860 9 1116 8 4102 3 1323 6

2408 3 4.25 8 2731 3 5.05 8 3047 3 5.97 5 3405 2 7.14 8 3727 8 139 8 4016 4 9.72 8 4288 7 11.17 8 4653 9 1178 3 4813 7 14.48 1 5068 5 1U7 0 1/

2 c m BH P 2161 7 4.44 7 2360 7 5.06 3 2520 8 S.71 8 2678 8 6.41 3 2832 4 7.15 6 2964 1 7.84 8 3137 1 6.78 6 3295 6 8.66 6 3464 0 10J7 7 3638 3 11.52 1 3802 0 12.51 6 3S58 3 13.57 7

2644 8 6.17 1 2886 4 7.24 5 3307 1 136 0 3SJ7 7 9.68 4 3966 2 ibi s 4314 8 1180 8 4603 0 14\JS 6 4676 2 16.88 1 V I cn i BH P

22S0 S 5.64 0 2464 1 139 4 2649 6 7.17 1 2818 4 7.89 0 2977 1 8 AS S 3131 0 8.77 8 3282 6 10.75 2 3435 0 11.77 8 3590 2 12.85 5 3752 5 13J7 4

2946 1 L58 7 3306* 1 IJt3 4 3617 0 11.30 2 3835 8 1186 4 4233 2 14.78 2 4634 7 16AS 4 3/ 4 7/ 1

CF M BH P

Z35S 5 7.01 6 2593 2 7.S3 4 2792 0 8.64 8 2869 0 9.79 7 3133 7 10.79 7 3291 3 1145 3 AAAJJt 1234 6 3596 6 14.13 7

3298 0 11J7 8 3645 6 1S.17 S 3936 0 14.82 2 4__ m 16.67 2 CF U

BH P

.

2492 8 8.61 4 2742 3 9.71 0 2947 2 10.76 8 3131 5 11.35 5 3301 0 12.99 8 3461 6 14.19 3

3676 5 15.17 4 4009 1 17X8 6 1 '"CFlT BH P

2S68 1 1146 4 2909 0 11.74 2 3118 1 12.84 8 3305 3 14.16 4

xaU 17.17 3
—• • » • *^« . »k tham u H fo-»

w Mki g (Ert^-M^ob*^"'"* ' kmt . /-arlorrmno a nfrig . a a ne tMud * f n •!-*__

_P.3 3 Engineerin g Environmenta l Consultin g Service s d . Th e DE Q shal l b e notified , i n writing , of an y change s i n sourc e tes t

plan s prio r t o testing . e . Method-specifi c qualit y assurance/qualit

y contro l (QA/QC ) procedure s shal l b e performe d t o ensure datavalidity . Ful l documentatio n of th e procedure s an d results shal l als o b e presente di n th e sourc e tes t report fo r review . f . Th e sourc e tes t

repor t shal l b e submitte dto , th e DE Q withi n thirt y day s o f th e las t da y of testing . g . Tw o (2 ) copie s of

th e complete dsourc e tes t

repor t shal l b e sent

t o th e department ; on e (1 ) to th

e DE Q Regional Operation s staf f perso n responsibl e for th e sourc e an d the secon dcop y t o th e Sourc e Testin g Coordinator , Department

of Environmenta

l Qualit y Headquarter s i n Portland . 16 : Signatures ' . Fo r the Aqu aGlas s Corporation :

nam e dat e titl e Fo r Engineerin g Environmental :

nam e dat e titl e 

### m- 4 

## 3<LP.3 4



### Engineering Environmenta

l Consultin g Service s 

### FIGUR E 6 aPerfonnanc e Curv e fo r Fa n *# A LORE N COO K-COMPAN Y MODE L NO
. 30-LS U TES

T NO
. 88-160 IMPELLER OIA

M 30.1 3 OUTLE

T ARE A 5.07 4

1.7 5

1. 5

1.2 5 C D X I > 

### m x o 1 3 

### to m o *£ _ 

### m

\ * n 1000' SEngineerin g Environmenta l Consultin g Service s FIGUR E 6 c Performanc e Curv e fo r Fa n # C

STEE L UPBLAS T PROPELLE RVEKTILATOR- MODE L SU B HIG H TEMPERATUR E SMOK E COKTROL VENTIUTO R- MODE L SUB H FA M 8C £

4 3

& 4 CATALO

G NO ,

•*su a m d 4MU8 H

S4-SU B an d S4-SU8 H MOTO

R KP
3

7- M

1 0

1 5

2 3

S

7-1/ 2

1 0

I S
a RP U SS S 61 0 O S 64 0 64 5 71 0 73 5 76 0 T U 81 0 SS S s n 3S 3 39 S 42 5 45 S 48 5 S1 S SA S S7 S 60 S SS S 60 S 88 5 7*23 P

A CP U BH P 3014 S 3.B0 S 3143 3 4.4* 3 3271 1 4.99 5 3400 9 5.60 8 3S29 7 127 0 9656 6 a_a a 3787 4 774 6 3916 2 156 3 404S 0 9.43 6 4173 8 1136 7 4SH 7 11.35 7 +451 4 12.40 4 acer 1.96 9 30J4 1 2.4S S 3264 8 110 4 S49S 0 l a u 1725 4 4.81 9 3955 9 153 1 4166 3 lis * 441( 7 7.B8 - 4*47 2 ue * 4877 « io_3e a J1« 1 11J0 7 S33S 5 1158 3 i&«a a 15.43 Q 1/

1 "6W ~ •H P 2S58 1 4.oa a 2994 4 4.61 8 3129 6 5.19 2 3264 2 5JB1 3 3309 4 14* 2 3532 2 720 1 3648 7 7J7 2 3796 9 (.79 6 8931 7 9.67 7 4064 1 10.81 5 41*5 3 1U1 2 4326 4 12.67 0 2481 5 2.12 4 2725 1 2.66 8 2981 1 329 2 3232 6 4.01 2 3460 4 4.83 0 3729 1 175 5 3870 1 179 3 4212 2 744 4 44JJ 2 923 1 4693 2 10.64 « 4832 3 12.19 9 5170 6 1188 8 4408 1 1174 8 I M

CF M BM P _ , 26S2 7 4.51 5 2811 4 4.84 2 2842 4 141 6 3109 3 6.03 9 3252 3 171 2 3383 5 7.43 7 3534 0 121 2 3872 9 9X4 4 3810 2 9.93 1 3947 3 10.67 S 4064 0 11.67 9 4220 2 1194 3 1881 8 2.19 6 2219 8 2.7*1 5 2638 2 136 4 28S3 6 4.16 7 J194 5 102 3 3470 6 196 8 373S 9 )JQ2 2 389S 3 119 4 4248 2 149 0 4500 9 1091 9 47(0 0 12.48 6 4996 9 14.19 6 8242 4 1105 2 3/ 1

CF U BH P 2402 6 4,48 1 2554 6 S.04 4 2707 2 5.66 7 2B6S 1 6.32 7 3035 5 7.01 S 3206 1 7J3 3 3368 0 150 2 •yy)* > 9.32 7 3671 2 10.21 4 3817 9 11.15 8 3960 9 12.18 4 4102 3 1123 6

2406 3 425 8 2731 3 S.0S 8 3047 3 4.97 . 3405 2 7.14 8 3727 8 138 8 401( 4 9.72 8 4288 7 11.17 9 45S3 9 12.76 3 4413 7 14.49 1 SOW S 1137 0 1/

2 CF M BH P 2161 7 4.44 7 23S0 7 S.06 3 2S20 6 171 6 2678 9 6.41 3 2332 4 7. 1 S S 2984 1 7.94 6 3137 1 178 8 3295 4 9.68 6 3444 0 10.57 7 3636 3 11.52 1 3802 0 12.51 6 3858 3 13.57 7

2644 9 117 1 2998 4 724 5 3307 1 136 0 3837 7 9.69 4 3968 2 11J1 4 4314 4 12.90 9 4603 0 14.75 4 4876 2 18.8*1 1 S I

CP M BH P

22SO S 144 0 2444 1 139 4 2*19 6 7.17 1 2816 4 7.89 0 2977 1 8.85 6 3131 0 9.77 8 3282 6 10.75 2 3435 0 11.77 8 3590 2 1185 5 37S2 S 1187 4

2944 1 lis ? 3304 1 9-0 4 36170 (1_ta2 38336 12.64 4 42332 14.78 2 4434 7 1145 5 V 4

CF U BH P

2359 S 7.01 8 2S03 2 7.83 4 2792 0 iMi 2948 0 9.79 7 3133 7 10.79 7 3291 3 11.85 3 M-t-tf l 1234 4 3594 6 14.13 7

3298 0 11.57 8 3445 8 n m 3836 0 1-182 2 4Z72_ l 16.47 2 7/ 1

CF M BH P

.

2462 8 6.61 4 2742 3 9.71 0 2947 2 10.76 6 3131 5 1135 5 3301 0 12.99 6 3461 6 14.19 3

3478 5 15.174 4009 1 17.02 6 1

CF M BH P

2664 1 10.48 4 29090 11.74 2 3118 1 12.94 9 330S 3 14.18 4

<30Q M 17.17 3

—i-vw.it.F M euM . FOB V a*> g &tf) « i >___•_

• attaa tw . Nrtamno * ntrg i <* > no tMut e t» rtrdk,P.3 6

Engineerin g Environmenta l Consultin g Service s FIGUR E 6 e Performanc e Curv e fo r Fan # E LORE N COO KCOMPAN V MODE L NO
. 48-LS U TES

T NO
. 88-16 9 IMPELLE R DIA

M 48.00 OUTLE

T AREA . 12.8 3

C

D D > m 

### I 

## o u (/ ) 

### m T J 

### o * s m n

" 0 2 4 6 3 1 0 I E 1 4 1 6 '*J3r""a 2 2 2 4 °. 5 £ 3 3 0 3 2 3 4 363 7 1 4 I B '^^. ~ -. A r\oc\ • •** ;P.3 7


### Stat e o f Orego n 

## Departmen to f

Environmenta

l Qualit y Memorandum

To : Fran

k Messina : ER-Ben d From : Than e Jenning s Subject : Sourc e Tes t Revie w Repor

t Aqu aGlas s Klamat h Count y Sourc e Testers : AG I Process : Fiberglas s Manufacturer Tvp e o f Facilitv ! Source s no t

liste d which woul d emi t

1 0 o r mor e tons/y r

VO C uncontrolled , mediu mcos t Permi t Number : Tes t Date : Repor t Received : Date : Januar y 10 , 199 5 

# "M - 

# * (
18-009 3 October 24-27 , 199 4 Januar y 9 , 199 5
SI C 308 8 Particulat e Emission

s from Aqu

i Source

Ge l Coa t# 1 Gel Coa t#2 Firs tChoppe

r Bas e Choppe

r Foa m Coa t j Cove r Coa

t | Tota l i Glass

: \ (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



### l^^^§^^.^^B^^ l Particulat e Emission s lb/h r 0.020 0 0.017 8 0.043 7 0.042 3 0.049 4 0.015 0 0.188 2 lb/bathtu

b unit 0.001 7
' 0.001 1 0.001 5 0.001 8 0.001 6 0.000 5 0.006 8 • * — 

# 1

lb/lb bathtu

b uni t 13.35E- 6 9.63E- 6 12.61E- 6 14.04E- 6 13.36E- 6 4.41E- 6 67.4E- 6 I t shoul d b e note d tha

t sumof th e lbs/uni t

i n th e tw o tables , Particulat e Emission s firomAqu aGlas s an d Styren e Emission s fromAqu aGlas s ar e no t asimpl e su mo f

th e lbs/uni t

fo r eac h spra y booth . Ge l Coa t # 1 an d Ge l Coa

t # 2 ar e paralle l processes , tha t i s eac h bathtub uni t

wil l pas s throug h onl y on e o f th e Ge l Coa

t booths . Th e attache d proces s diagra mshow s th e flo w of

bathtu b units . Th e Th e su mof

th e particulat

e an d styren e fo r

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

i s calculate db y averagin g th e lbs/uni t

fromGe l Coa t # 1 an d Ge l Coat

ffl



### 3(o^'P.3 8

Memo To : Fran k

Messin a Januar y 10 , 199 5 Pag e 2 Thi s report

ha s bee n reviewe d an d i t ha s bee n determine dthat

th e tes t method s conducted , dat a provided , and calculation s perfonne d ar e sufficien t fo r evaluatin g th e complianc e o f thi s sourc e fo

r permitte d parameters . Averag e bathtub uni t weight i s 124 lbs/unit . Particulat e emission s fromthi s sourc e ar e assume d t o b e les s than 1 0 / x i n diameter . Particulat e matter wa s belo w th e performanc e standard o f

0.001 1 grains/dscf. Th e particulat e matte r mas s emissio n rat e wa s belo w th e short and lon g ten n PSELs . Th e tes t result s show styren e emission s excee dth e dail y an dannua l Plan t Site Emissio n Limits , (PSELs) . Th e opacit y wa s no t measured , a s i t

i s assume dt o b e zer o becaus e o f th e lo w particulat e concentration , opacit y wa s confirme dt o b e zer o durin g th e sourc e tes t b y th e DE Q observer , Than e Jennings . Thes e sourc e test s wer e conducte d t o satisf y th e requirement s o f

conditio n 10-1 4 fo r

demonstratin g complianc e wit

h condition s 2 , 3 , and 6- 8 o f th e ACD P issue do n Januar y 20 , 1993 . Th e testin g was performe d i n accordanc e wit h th e method s approve din . th e sourc e tes t plan an dQA/Q C documentatio n wa s sufficien t fo r evaluatin g th e validit

y o f th e data . Th e permi t

state s tha t th e averag e ambien

t concentratio n o f

styren e sample s take n from 5 differen t samplin g location s representativ e of fugitive ai r

that woul dsee p ou t

fromth e plant , shal l no t

excee d 5 ppm . Th e averag e o f

th e 5 ambient

sample s wa s 1 5 ppm . Th e shippin g an dreceivin g are awa s th e onl y on e o f

th e fiv e samplin g location s belo w five ppm , a t 3. 4 ppm . A n informal styren e surve y o f th e plan t wa s perfonne d b y DE Q staf f o n Oct . 2 4 usin g aphot o ionizatio n detector , (PID) , th e PI D wa s calibrate d with isobutylene an darespons e factor of 0. 5 wa s use dt o correlat e th e instrumen t

respons e fromisobutylen e to styrene . PI D reading s take n o n th e plan t floo r range d from3 0 t o 140 ppm , th e highes t readin g wa s take n insid e th e hea t room . Rooftop reading s range d from1 pp mt o 1 2 pp mtake n a t th e northeas t

corne r of th e building . PI D reading s wer e take n a t the Gelcoa t # 1 an d il stacks , ffl

stac k varie dfro m25 0 t o 40 0 pp mandffl stac k from25 0 t o 47 0 ppm . Styren e concentratio n wa s measure da t seven exhaus t

fa n outlet s a t

th e rooftop . Th e results ar e show n i n th e tabl e belo w and ama p of th e rooftop showin g th e exhaus t fa n locatio n i s include d wit

h thi s memo .



## 3< l

### Mem

o To : Fran

k Messin a Januar y 10 , 199 5 Pag e 3 P.3 9



### Roofto p Exhaus t Fa n Styren e Concentration Exhaus t Fa n EF- 2 EF- 3 EF- 4 EF-1 1 EF-3 4 EF- ? Maintenanc e Concentration

(pp mv/v ) 30-5 0 1 5 2 0 1 3 7 0 7 0 100 Stvrene Emission s fromAqu aGlas s Sourc e Flowrat

e (DSCFM ) Styrene Emission s pp m(v/v) lb/h

r lb/bathtu

b unit lb/l

b bathtu b unit Ge l Coa t ffl 1333 5 21 0 45. 5 3.9 1 0.03 1 Ge l Coa t ffl 1346

7 223 48. 8 3.2 3 0.02 7 

### Firs t Choppe r 2621 4 23 3 

### 99. 2 3.4 2 0.02 8 

### Bas e Choppe

r 1806

9 65 19. 0 0.7 8 0.00 6 Foa mCoa t 750 2 5 0 6. 1 0.2 0 0.00 2 

### Cove r Coa t 10326 193 32. 5 1.1 1 0.00 9 Hea t Roo m Tota l 818 4 6 5 8. 6 259. 7 0.2 9

9. 4 0.00 2

0.10 5



## 3%P.4 0



### Mem o To : Fran

k Messin a Januar y 10 , 1995 Pag e 4 Summar y o f Ambien t Styren e Samplin g Productio n Are

aLocatio n i 

### 1 . Touch-u p Area 2 . Maintenanc e Are

a 3 . Shipping an

d Receivin g 4 . Woo d Sho

p j 5 . Exhaus t

Fa n # 3 Averag e Ambien t Concentratio

n (pp my/v ) 5. 4 4 3 3. 4 1 5 7. 6 1 5 During the mont

h o f October , th e productio

n rate wa s 8,240 bathtu

b unit s which i s roughl

y 40 % of the planne dproductio

n capacity . Durin

g th e ai r source test , production wa s 40 % t o 50 % o f the desig n capacity . Th

e PSEL s shown in th

e tabl e ar e calculate dusing the emission factor

s fromth e air sourc e tes t

an d th e desig n capacit y o f 250,00 0 bathtu

b unit s pe r year . Actua

l emissions fo

r 199 4 ar e a s follows : Particulat e (54,13 7 bathtu

b units yea r * 0.006 8 lb s P

M unit)/(25 0 days/yea

r * 2 0 hrs/day ) = 0.0 7 lbs/h r 54,13 7 bathtu

b unit s * 0.006 8 lb s P

M unit/2000 lbs/to n = 0.1 8 tons/yea r Stvrene (54,13 7 bathtu

b units/25 0 days ) * 9. 4 lbs/unit = 203 5 lbs/da

y 54,13 7 bathtu

b unit s * 9. 4 lb s styrene/unit/2000 lbs/to n = 25 4 tons/yea r If Aqu aGlas s wer

e t o continu e operatin g a t 40 % o f capacit y i n 199 5 the y wouldexcee

d their long ter mPSE L fo r styren e i n 5 0 day s o

f operation . (9 3 ton s styren

e * 200 0 lbs/ton)/(100 0 unit/da

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 awate r curtain an dadr y disposable filter. . Styrene an d VO C emission s ar

e uncontrolle

d


# 3

VP.4 1

Memo To : Fran k

Messin a Januar y 10 , 199 5 Pag e 5
Shor t and Lon e Ter

mPSEL s Pollutan t PSE L

Measure d Limi t Particulat e Matte r

< 1 0 p. lbs/hou r tons/yea r 0.2 8

0.8 5 1.6 5



### 4. 9 Styren e lbs/day tons/year 9,40 0 1,17 5 

### 74

4 

### 9 3 Aqu aGlas s i s ou t

of complianc e with th e shor t an dlon g ter mstyren e PSEL s fo r tw o reasons ; emissio n factor s measure d durin g thi s sourc e tes t are higher

than thos e value s reporte dt o DE Q b y Aqu aGlass , an d Aqu aGlas s seem s t o hav e underestimate dth e amount o f resi n andge l coa

t use d t o produc e abath/showe r

unit . T o illustrate th e deficiencie s i n th e informatio n use dt o calculat e th e styren e PSELs , I wil l us e th e 199 3 annua l report an dEP A AP-4 2 emissio n factor s to calculate 199 3 emission s fo r

th e Aqu aGlas s facility . 199 3 Stvren e Emission s EP A AP-4 2 use s th e followin g rang e of emissio n factor s fo r

spra y layup i n th e polyeste

r resi n nroduct fabricatio n process . Proces s Spray Layup Resi n

Non-Vapo r Suppresse d 0.09-0.1 3 Vapo r

Suppresse d 0.03-0.0 9 Ge l Coa t Non-Vapo r Suppresse d 0.26-0.3 5 Vapor

Suppresse d 0.08-0.2 5 Th e followin g calculatio n use s th e highe r rang e o f EP A AP-4 2 styren e emissio n factor s fo r vapo r suppresse d resin s an d gelcoat , whic h would , see mt o mor e closel y matc h th e Aqu aGlas s styren e emission s than th e lowe r

rang e o f emissio n factors . Resi n styren e conten t o f 0.3 1 i s take n fromth e 199 3 Aqu aGlas s annua l report, . EP A AP-4 2 report s avalu e o f 0.43 . Ge l coat , resi n ah d styren e usag e ar e al l take n fromth e 199 3 Aqu aGlas s annua l report .



## <-V DP.4 2



### Mem o To : Fran

k Messin a Januar y 10 , 199 5 Pag e 6 22,27 7 lb s ge l coat*(0.3 5 l

b styrene/l b ge l coat)*(0.2 5 lb s styrene emitted/l b styrene) = 1,94 9 lb s 68,90 0 lb s resin*(0.3 1 l

b styrene/l b resin)*(0.09 l

b styren e emitted/l b styrene ) = 1,922 lb s 44 0 lb s styren

e - = 44 0 lb s 68 3 bathtu b units produce

din 199 3 =4,31 1 lb s 4,31 1 lb s styrene/68 3 units = • 6. 3 lb s styrene/unit I f thi s emission facto

r wa s use dt o predic t futur e emissions , Aquaglas s woul demi t 78 9 ton s o

f styren e pe r yea r a t desig n capacity , whic

h i s abou t 8 time s highe

r tha n DE Q predictedfo

r thi s facility . 273 3 tons/yea

r o f styren e pe r yea r i s th e Aqu

aGlas s styren

e usag e containe din th e detai l shee t o f the ai r contaminan

t discharge permit , (ACDP) . Dividing th e styren e usage b y the desig n capacit y yield s valu

e o f 2 2 lb s o f styren e appliedt o eac

h unit . Th e Aqu

aGlas s consultan

t Bill Grigg s statedin atelephon

e conversatio

n tha t AquaGlas s use s a24. 5 lb s o f styrene/bathtu

b unit . Bil l Grigg s als o state

d in the sam

e telephon e conversation tha

t the source tes t

show s 40 % o f

their styren e usag e i s emitte

dt o th e ai r base do n th e sourc e tes t

report . Usin

g Bill' s valu

e o f 40 % styren e emitted/use

d yield s avalu

e o f 23. 4 lbs . o f

styren e appliedt o eac h bathtu b unit . Yet

i n 199 3 Aqu aGlas s applie

d 4 3 lb s o f styren e pe r unit , anumbe

r which i s roughl

y doubl e th e value i n the ACD P detail sheet . 22,27 7 lb s ge

l coa t * 0.3 5 l b styrene/l b ge l coa t = 7,79 7 lb s styren

e 68,90 0 lb s resin * (0.3 1 l

b styrene/l b resin) = 21,35 9 lb s styren e 44 0 lb s styren

e = • 44 0 lb s stvren

e = 29,59 6 lb s styren

e 29,59 6 lb s styrene/68 3 units = 43. 3 lb s styrene/bathtu b uni t Recommendations Th e styrene emissio

n facto r fo r the 199 4 ai r sourc e tes t

wa s 9. 4 lb s styrene/bathtu

b unit , which i s 33 % highe r tha n th e valu e calculate dusin g the 199 3 annua

l repor t an dth e EP A AP-4 2 emission factors . Anothe

r Orego n facilit y tha t produce s hot-tub s an

dshowe r unit s emits 9 lb s styrene/unit . Ther e i s definitel

y roo mfo r improvemen

t a t AquaGlass . Bill Grigg s ha s state dtha t Aqu aGlas s cunenti y use s th

e followin g proces s change s an

dmaterial s substitution t

o reduce styren

e emissions ; vapo r suppresse dresin s an d ge l coat , an dairles s spra

y guns . Sinc e AquaGlas s alread

y use s the abov

e technologies , add-on contro l equipmen t suc h as thennal oxidation seem

s t o b e th e best metho davailabl e t o reduce vapo

r emissions fromstyrene . Aqu a Glas s wouldnee

dt o improv e thei r VO C captur e efficienc y if the y wer e t o receiv e th e benefi t o f installing atherma

l oxidizer . Besides therma

l oxidatio n ther e ar e emergin g technologie s such a s chiller s whic

h recove r th e styren e s o i t ca n b e reused .


### <q- iP.4 3

Memo To : Frank

Messin a Januai y 10 , 199 5 Pag e 7 Fugitiv e emission s were no t take n into accoun

t durin g th e ai r

dispersio n modeling originall y performe d a

t th e Aqu aGlas s facility . It i s obviou s fromth e odo r

complaints , th e air

sourc e tes t performe d by AGI an d fro mth e survey performe db y DE Q tha t fugitiv e emission s are aproble mat Aqu aGlass . FacUit

y emission s shoul d b e modele dagai n wit h th e fugitiv e emissio n source s include d i n th e ai r dispersio n model . T o maintai n indoor

ai r quality , th e Aqu aGlas s facilit y wa s designe dfor

acombine ddischarg e flowrat e of 175,00 0 dscf

m( 7 stack s x 25,00 0 dscfm) . However , th e sourc e tes t datasho w a combine d discharg e flowrat e o f 97,00 0 dscfm . On e wa

y fo r Aqu aGlas s t o improv e thei r styren e captur e efficienc y and ; decreas e th e ambien t styren e concentratio n woul db e t o increas e fa n speed , a t eac h o f th e 7 stack s excep t

fo r th e first chopper spra y booth stac k

whic h hadastac k

flowrate o f 26,000 dscfm . Thi s woul d not , however , decreas e overal l styren e emissions .

cc : Joh n Hector : DEQ : ER-Ben d Dav e Kauth : DEQ r

ER-Ben d Pete r Brewer : DEQ : ER-Bend Ai i Nikukar : DEQ : H Q



## 4< L

# z

Hea t Roo m Clea n Moi d

Ge l Coa t # 1 Ge l Coa t # 2

Firs t Choppe r \ /

Bas e Choppe r

Foa m Coa t
Cove r Coa t
Remove fro m Mol d 

# I
Touch-u p Shipping/Warehous e 

### Legen d Vente d Ai r Emission s -__-________«_____Ba—«"J£ > Proces s Ro w 

# AG I TECHNOLOGIE S 30.-M52.00 1 

### PROCES S DIAGRA M Aqu a Glas s Klamat h Falls , Orego n RO B 1 1 No v 9 4 REVIUd J RGUR E 

# 1 4- 3...a.aa pollutan t Leve l Dat a ••••••• • AQU A GLAS S WESTERN , INC . 24-OCT-9 4 Unit : Ge l Coa t # 2



# 4< V P.4 5

_r

_No . Avg .

.0000 7 .0001 6 .0001 8 .0001 4 gr/dsc f
.000 9 .000 7 .001 5 .00 1 lb/bathtu buni t .011 9 .010 9 .024 6 .015 8 lb/h r tyren e 2.8 5 3.1 1 3.7 4 3.2 3 lb/bathtu buni t Styren e 39. 9 46. 7 59. 8 48. 8 lb/h r Styren e 18 0 22 0 27 0 22 3 pp mP.4 6

Sourc e Tes tRepor tDetai l Shee t Tested : 24-OCT-9 4 b y AG I Technologie t Approve d fo r Agenc y ut e

Source : 1 8 - 009 3 AQU A GLAS S WESTERN. IMC . KLAMAT H PALL S Uni tTested : Ge l Coa t» 2
Uni tType : Spra y Boot h I Ge l Coa t1 Contro l Device(a) : Fabri c Filte r , Hate r Curtai n Scack : Diameter : 34. 0 inche s

Ru n Leve l Dat a

Ru n No . Velocit y (FPM ) Flo w (DSCPM) Temperatur e (F ) %H20 %C0 2 Proces s Rac e Contro l Dat a 1 2S1 7 1365 3 6 6 1 . 3

. 0 1 4 Bathtu b unic/h r 4 . 7 i n H2 0 2 238 9 1309 1 6 6

- 9

. 0 I S Bathtu b unit/h r 4 . 6 i n H2 0 3 2S0 0 1365 6 6 2 1. 0

. 0 1 6 Bathtu b unit/h r 4 . 6 i n H2 0 Av g 246 9 1346 7 I S 1 . 1

. 0 I S



# 4 5P.4 7

Sourc e Tea t Repor t Detai l Shee t Tested : 25-OCT-9 4 b y AG I Technologie s Approved for Agenc y us e

Souree : 1 8 -.009 3 AQ0 A GLAS S WESTERN , INC . KLAMATH FALL S I Uni t Tested : Firs t Choppe r
Uni t Type : Spra

y Boot ht Chopper- ] Contro l Device(s) : Fabri c Filte r , Wate r Curtai n Stack : Diameter : 34. 0 inche s

Ru n Leve l Dat a

Run No . Velocit y

(FPM ) Flo w (DSCFM ) Temperatur e (F ) %H2 0 %C0 2 Proces s Rat e Contro l Dat a 1 495 7 2657 1 7 1 1. 3

. 0 3 1 . Bathtu bunits/hr 4. 9 i n H2 0 2 495 5 ' 2628 0 7 5 1. 7

. 0 2 5 Bathtu b 4. 8 i n H2 0 units/h

r 3

481 2 2579 2 7 0 I. S

. 0 3 2 Bathtu bunits/hr 5 i n H2 0 Av g 490 8 2621 4 7 2 1. 5

. 0 2 9



# 4 4...... . pollutant Leve l Dat a ••••••• • AQU A GLAS S WESTERN , INC . 25-OCT-9 4 Unit : Firs t Choppe r

u n No . . 1 Avg .

M .0001 2 .0002 7 .000 2 .000 2 gr/dsc f

• M .000 8 .002 4 .001 4 .001 5 lb/bathtu

buni t
> M .026 3 .060 8 .043 9 .043 7 lb/h r Styren e 3.3 4 3.9 2 3.0 1 3.4 2 lb/bathtu

buni t Styren e 103. 4 98 . 96. 2 99. 2 lb/h r Styren e 24 0 23 0 23 0 23 3 pp «



# 4- 1P.4 9

Sourc e Tes t Repor t Detai l Shee t Tested : 24-0CT-9 4 byAG I Technologie s Approve d fo r Agenc yus e

Source : 1 8 • 009 3 AQU A GLAS S WESTERN , INC . KLAMAT H FALL S Uni t Tested : Ge l Coa t # 1
Uni t Type : Spra

y Boot h- [ Ge l Coa t ] Contro l Device(s) : Fabri c Filte r , Hate r Curtai n Stack : Diameter : 34. 0 inche s

Ru n Leve l Dat a

Ru n No . Velocity

(FPM ) Flo w (DSCFM ) Temperatur e (F ) UQ O %C0 2 Proces s Rat e Contro l Dat a 1 238 5 1300 7 6 3 1. 2

. 0 1 1 bathtubs/h r S. 5 i n H2 0 2S5 1 1378 3 6 8 1. 3

. 0 1 1 bac hcubs/h r 4. 8 i n H2 0 243 1 1321 5 6 6 1. 1

. 0 1 3 . . bathtubs/hr 4. 9 i n H2 0 Av g 245 6 1333 5 6 6 1. 2

. 0 1 2



## <*T >»«•»• » pollutan t Leve l Dat a ••••••• • AQU A GLAS S WESTERN , INC . 24-OCT-9 4 Unit : Ge l Coa t » 1



# iM\ P.5 0

n No . Avg .

.0001 5 .0002 2 .000 2 .0001 9 gr/dsc f

: 001 5 .002 2 .001 8 .001 8 lb/bathtu

buni t .016 8 .024 3 .023 2 .021 4 lb/h r :yren e 3.6 4 4.4 7 3.6 3 3.9 1 lb/bathtu

buni t -yren e 40. 1 49. 2 47. 2 45. 5 lb/h r tyren e 19 0 22 0 22 0 21 0 pp m>••••• • pollutan t Leve l Dat a •**••*• • AQU A GLAS S HESTERN , INC . 26-OCT-9 4 Unit* . Bas e Choppe r
Iu n No . 1 Avg .

P H .0001 9 .0003 2 .0003 2 .0002 8 gr/dsc f ? M .001 1 .001 7 .002 5 .001 8 lb/bathtu buni t ? M .027 7 .049 9 .049 4 .042 3 lb/h r Styren e .4 8 .8 4 1.0 1 .7 8 lb/bathtu buni t Styren e 12. 5 24. 4 20. 2 1 9 lb/h r Styren e 4 4 8 2 6 8 6 5 pp m



### , ^ D P.5 1P.5 2

. »

Sourc e Tes t Repor t Detai l Shee t Tested : 27-0CT-9 4 b y AG I Technologie s Approve d fo r Agenc y

us e

Source : 1 8 r 009 3 AQU A GLAS S WESTERN , INC . KLAMAT H FALL S Uni t Tested : Hea t Roo m
Uni t Type : Curin

g Roo m [ Fiberglas s 1 Stack : Diameter : 28. 0 inche s

Ru n Leve l Dat a

Ru n No . Velocit y

(PPM ) Flo w (DSCFM ) Temperatur e (F ) %H2 0 %C0 2 Proces s Rat e Contro l Dat a 1 234 9 818 4 9 4 1. 2

. 0 3 0 Bathtu bUnits/hr 2

234 9 818 4 9 4 1. 2

. 0 3 0 Bathtu bUnits/h

r Av

g 234 9 818 4 9 4 1. 2

. 0 3 0



# 5\...... . pollutan t Leve l Dat a ••••••• • AQU A GLAS S WESTERN , INC . 27-OCT-9 4 Unit : Cove r Coa t '.u n No . 1 ' Avg .

.0001 3 .0001 7 .0001 9 .0001 6 gr/dsc f
? M .000 4 .000 5 .000 7 .000 5 lb/bathtu

buni t ? M .011 8 .014 8 .018 4 .01 S lb/h r Styren e . 9 9 .8 3 1.5 2 1.1 1 lb/bathtu

buni t Styren e 31. 7 24. 9 4 1 32. 5 lb/h r Styren e 20 0 15 0 23 0 19 3 pp m



# s' L P.5 3>••••• • pollutan tLeve l Dac a ••••••• « AQU A GLAS S WESTERN. INC . 26-OCT-9 4

Unit : Foa m Coa t Ru n No . Avg .

.0011 3 .000 4 .0004 6 .0006 6 gr/dsc f P M '.002 8 .001 1 .001 1 .001 7 lb/bachtu b uni t P M .083 4 .029 6 .035 1 .049 4 lb/h r Styren e .1 9 . 1 9 .2 3 . 2 lb/bathtu b uni t Styren e 5. 8 7 . 6 6 . 1 lb/h r Styren e 4 8 4 2 6 1 S O pp m



# S 3 P.5 4P.5 5



## 0 - 0 - 0 - 0 - © - 0 - 0 - 0 - © - 0 - © - 0 - 0 - 

# io?^99n??? t

a

I Q V. D i

a

I Q

I a

« _ L J 

### 5 • V

I i ° / i B 

# r SP&
S

o 

# P

•'i t £

. « o $ i 

## 1 $ $ § a



# S UP.5 6

Sourc e Tes tRepor tDetai l Shee t Tested : 26-OCT-9 4 b y AG I Technologie s Approve d fo r Agenc y us e
Source : 1 8 -.009 3 AQU A GLAS S WESTERN

, INC . KLAMAT H FALL S Uni tTested : Bas e Choppe r
Uni c Type : Spra y Boot h [ Choppe r ] Concro l Device(s) : Fabri c Filte r , Wate r Curtai n Stack : Diameter : 34. 0 inche s

Ru n Leve l Dat a

Ru n No . Velocit y

(FPM ) Flo w (DSCFM ) Temperatur e (F ) *H2 0 %C0 2 Proces s Rat e Contro l Dat a 1 321 8 17S8 S 6 1 1. 2

. 0 2 6 Bathtu b- units/h

r 4. 8 i n H2 0 2 338 9 1832 S 6 6 1. 3

. 0 2 9 Bathtu bunits/h

r 5. 3 i n H2 0 Av g 341 3 1829 8 7 0 1. 4

. 0 2 0 Bathcu b 4. 8 i n K2 0 units/hr 334 0 1806 9 6 6 1. 3

. 0 2 5



# S SP.5 7

Sourc e Tes tRepor tDetai l Shee t Tested : 26-OCT-9 4 b y AG I Technologie s Approve d fo r Agenc y us e
Source : 1 8 -.009 3 AQU A GLAS S WESTERN

, INC . KLAMAT H FALL S Urti tTested : Foa

m Coa t
Uni c Type : Spra y Booc h [ Foa m Coa t] Scack : Diameter : 24. 0 inche s

Ru n Leve l Dat a

R u n No . Velocit y (FPM ) Flo w (DSCFM ) Temperatur e (F ) %H2 0 *C0 2 Proces s Rat e Contro l Dat a 1 285 6 744 7 8 7

. 6

. 0 3 0 Bathtu b Units/h r Av g 211 2 297 8 288 2 733 3 772 6 750 2 8 7 8 8 8 7

. 6 . 9 . 7

. 0 . 0 . 0 2 7 3 3 3 0 Bathtu bunits/h

r Bathtu

bUnits/hr



# 5( bP.5 8

Sourc e Tes t Repor c Detai l Shee t Tested : 27-OCT-9 4 b y AG I Technologie s Approve d fo r Agenc y

us e

Source : 1 8 - 009 3 AQU A GLAS S WESTERN , INC . KLAMAT H FALL S Oni c Tested : Cove r Coa t
Ooi C Type : Spra

y Boot h( Cove r Coa t 1 Stack : Diameter : 34. 0 inche s

Ru n Leve l Dat a
Ru n No . Velocit y (FPM

) Flo w (DSCFM

) Temperatur e (F ) %K2 0 %C0 2 Proces a Rat e Concro l Dac a 1 180 4 977 0 6 5 1 . 3

. 0 3 2 BachCu b unics/h r 6 i n H2 0 Av g 189 8 204 2 19X 5 1021 S 1099 3 1032 6 6 7 6 7 6 6 1. 5 I. S 1. 4

. 0 . 0 . 0 3 0 3 0 3 1 Bathtu bunics/h

r BachCu

buniCs/h

r S. 9 5. 4 i n H2 0 i n H2 0



# 5 1P.5 9

...... . Pollutan t Leve l Dat a •«•**•• * AQO A GLAS S WESTERN , INC . 27-OCT-9 4 Unit : Hea t Roo o
N o . Avg .

-_rex» e .2 2 .3 5 .2 9 lb/bathtu buni t

'-cen e 6. 6 10. 5 8. 6 lb/h r
^-ren e S

O 7 9 6 5 pp m



## <£