p. 1



# OAR Box 1394 Prepped by Ollie Stewart



### Document

Number: 

# 31 ) II-C- 1
Docket Number: 

# A-94-5 2

Printed 7/3/2008 7:52:00 AM

Sheet 31 of 56P. 2

-*S> sr « > 

# kWr! UNITE D STATE S ENVIRONMENTA L PROTECTIO N AGENC Y Offic e o f Ai rQualit yPlannin g an d Standard s Researc h Triangl e Park , Nort h Carolin a 2771 1


### MA R3- 1 l" 3 Mr . Joh n Schweitze r Technica l Directo r Composite s Institut e 35 5 Lexingto n Avenu e Ne wYork , Ne wYor k 1001 7 Dea r Mr . Schweitzer : Than k yo u fo r comin g t o Durhamt o mee t wit h u s las t week
. A t tha t meeting , yo u informe d u s o f th e Composit e Institute' s plan s t o surve yth e industry , and you r willingnes s t o shar e th e ra wdat a wit h th e Environmenta l Protectio n Agenc y(EPA ) . A s discussed , I a msendin g a summar yan d thre e questionnaire s tha t illustrat e th e typ e o f dat a EP Arequest s fo r th e purpos e o f regulator ydevelopment
. Thes e questionnaire s wer e sen t t o th e magneti c tap e an d woo d furnitur e industrie s fo r th e developmen t o f nationa l emissio n standard s fo r hazardou s ai r pollutant s (NESHAP's ) an d t o th e aerospac e industry , fo r th e developmen t o f bot h a NESHA P and a contro l technique s guidelin e fo r th e reductio n o f volatil e organi c compounds
. . I loo k forwar d t o reviewin g th e draf t questionnair e tha t yo u develo p fo r th e composite s industry
. I n addition , pleas e le t m e kno wth e tim e fram e fo r sendin g th e questionnaire s and receivin g th e data
. I f yo u hav e anyquestion s o r comment s regardin g thi s lette r o r th e enclosures , fee l fre e t o cal l m e a t (919 ) 541-2383 . 

### Sincerely , 

# -nhL 

# L * Madelein e L
. Stru m Chemica l Applicatio n Sectio n Chemical s an dPetroleu mBranc h Enclosure s

V ''•""» «P. 3

Summar yo f Dat a Need s GENE.RA L

* Plan t FA

X numbe r i s no t importan t

* Latitud e and longitud e no t importan t

* Al l dat a shoul d b e requeste d fo r 1992 . * Employe e coun t i s importan t

* Informatio n tha t woul d allo wclassificatio n o f th e facilit yint o a distinc t subcategory PRODUCT S & PROCES S

* Informatio n regardin g typ e o f product s manufacture d and productio n rat e o f eac h product
. Proces s informatio n (eg : Par t II"B " o f pag e 8 i n woo d furnitur e questionnaire. )

* Informatio n regarding solven t cuttin g o f resin s o r othe r raw material s (eg : Par t i n F " o n pag e 7 o f woo d furnitur e questionnaire )

* Proces s descriptio n fo r eac h produc t (eg : bloc k diagra mo n pag e 8 o f aerospac e questionnaire ) Provid e example
. * Quantif yHA P emission s fo r eac h operatio n (eg : Tabl e 6 o n pag e 2 3 o f aerospac e questionnaire ) i n proces s
* Tabl e fo r usag e o f ra wmaterial s and HA P conten t o f eac h raw materia l

* MSD S sheet s o f rawmaterial s
* Tes t report s fro memissio n testin g
* Materia l (HA

P containing ) storag e procedure s (drums , tanks , ho w ar e ra wmaterial s transfere d fromstorag e t o process? )

* Spra yboot h dat a (eg : Par t II"C " o n pag e 9 o f woo d furnitur e questionnaire )

* Ove n dat a (eg : Par t I I "D " o n pag e 9 o f woo d furnitur e questionnaire )

* I f gluin g i s applicable , dat a o n glue s suc h a s quantitie s used , HA P conten t WAST E HANDLING & CLEANU P
* Type , quantit yan d disposa l practice s o f wast e material
. Wast e wate r characteristics
.



# ZP. 4

* Cleanin g operation s and material s (chemicals ) use d fo r cleanin g
CONTRO L TECHNIQUE S / Pollutio n Preventio n Measure s
* Pollutio n preventio n measure s (reformulation/materia l substitution , proces s changes , others ) - example s provide d i n al l questionnaire s
* Contro l devic e informatio n - example s provide d i n al l questionnaire s
* Genera l informatio n regardin g Ai r handlin g (flo wrates )

* Regulation s t o whic h plan t i s subjec t
COS T AN D ECONOMIC S

* Economi c and cos t informatio n - example s provide d i n al l questionnaire s OTHE R OPERATION S
* Wha t beside s composite s production , result s i n HA P emission s

^P. 5

Enclosur e 1 No t subjec t t o th e requirement s o f Sectio n3507 , Paperwork ReductionAc t o f 1980 .

MAGNETI C TAP E MANUFACTURIN GFACILITY INFORMATIO

N REQUES T FO

R Verbatim Sunnyvale , Californi a Pleas e answe r thi s informatio nreques t a s completel y a s possible . I f you ar e unabl e t o respon d t o anite

m a s i t i s stated , pleas e provid e an y informatio

nyou believe ma

y be related . Us e additiona l sheet s o r the back s o f th e reques t page s for your responses , i f necessary . I nsom e case s you ma

y wan t t o cop y blan k table s t o provid e response s for multipl e units . Thi s informatio

nreques t i s designed t o gathe r informatio n for the developmen t o f a nationa l emissionstandard for hazardou s ai r pollutant s (NESHAP ) fo r the magneti c tap e manufacturing industry . (Th

e lis t o f hazardou s ai r pollutant s [HAP's ] i s foun d i nAttachmen t 1. ) T o do so , w e nee d t o gathe r informationon bot hHAP' s an

d contro l technologies . Eveninformationconcernin g non-HA P solvent s (e.g. , cyclohexanone an d tetrahydrofuran ) tha t ar e used a t your facility wil l be usefu l i nthi s effort . Therefore , pleas e complet e al l applicabl e part s o f thi s informatio

nreques t for al l solvent s an d HAP' s (liqui d an d particulate) , wit hthe exceptiono f Par t F . Thi s reques t pertain s t o al l processe s related t o magneti c tap e manufacturing an d related activities . I f you provid e informationi nunit s othe r thanthos e requested , pleas e specif y thos e unit s i nyou r response . Thi s informatio

nreques t ha s beenseparated int o th e followin

g sections : Pag e Par t I : A . Genera l Information3 B . Overvie

w o f Solvent s an

d Particulat e HAP' s . . 3 C . Deliver

y an d Storag e 5 D . Mi xRoo

m 7 E . Coatin

g Operation8 F . Packagin

g an d Labeling o f Product s 1 2 G . Cleanin

g 1 3 H . Fugitiv

e Emission s 1 6 I . Contro l Device s 1 6 J . Wastewate r an

d Soli d Wast e Treatmen t an d Disposa l 2 4 K . Retrofit , Replacement , an d Modification... . 2 5 L . Othe r 2 5P. 6 

## h Pag e Par t II : M . Economi c Informatio n 2 6 N . Cos t Informatio n 2 7 Pleas e retur n thi s informatio n reques t and an yadditiona l informatio n yo u wis h to :

Emissio n Standard s Divisio n (MD-13 ) Unite d State s Environmenta l Protectio n Agenc y Offic e o f Ai r Qualit yPlannin g an d Standard s Researc h Triangl e Park , Nort h Carolin a 2771 1 Attention : Bruc e Jordan , Actin g Directo rP. 7

3 

## PART I
A . Genera l Information 1 . Nam e o f lega l owne r o f plant : 2 . Addres s o f lega l owner : 3 . Numbe r o f employee s attached t o the magneti c tap e productiondivisio no f the plant : 4 . Nam e o f respondent(s) : 5 . Title(s) : 6 . Telephone Number : 7 . Fa xNumber : 8 . Latitude an

d longitude (o

r UT M coordinates) : 9 . Th e actua l operatin g schedul e for 1990 : hr/d ; d/wk ; wk/y r B . Overvie

w o f Solvent s an

d Particulat e HAP' s 1 . Pleas e complet e Tabl e 1 . 2 . Wha t plans , i f any , d o you have t o furthe r reduc e HA P emission s (e.g. , fugitiv e emission s reduction , switch t o low-solven t coatings , etc.) ?

3 . Pleas e provid e a diagra m o r blueprin t tha t shows th e layou t o f the magneti c tape productionproces s t o include the deliver y poin t o f the solvent s an d particulat e HAP' s t o the plan t site , storag e area , mi x room , coatin

g room , contro l device , packagin g area , an

d produc t storag e area . Pleas e als o sho w the locationo f the majo r equipmen t i nthes e areas . 4 . Wha t percen t o f tota l VO C emission s fro m a coating line i s fro m eacho f the followin g areas : (a ) coate r hea d ; (b ) dryin

g oven; an d (c ) coatin

g preparation? Pleas e indicat e i f thes e value s ar e estimate s or ar e based o n actua l measurement s . I f measurement s wer e taken , pleas e provide a cop y o f the protoco l an d results . 5 . Have emissiontest s beenconducted fo r an y o f th e majo r emissio nsource s a t thi s facility (includin

g vents , stacks , etc. , a s wel l a s contro l devices) ? I f yes , pleas e attacha cop y o f al l complet e tes t reports , includin

g problems encountered wit hth e test s an d an y step s takent o resolv e th e problems .



### (oTABL E 1 . SOLVEN T AN D PARTICULAT E HA

P US E 

# 1

Name ' 

### illiliiiiiPiiiBiiliil i Emissions , lb/yi * Tota l amount

purchased , gal/yi * 1

Amountuse d i n th e following" : l Applie d coatings , gal/y r(lb/yr ) Purchas e Recycl e Cleanin g o rmaintenance , gal/y r Purchas e Recycl e Packagin g process , gal/y r Purchas e Recycl e

a Al l solvent s an

d an y particulat e HAP's . 

## K

•^ i

0 0P. 9

6 . I f the followin g informationi s no t included i nyour respons e t o Question5 , pleas e provid e the information belo w for eachsolven t fro m eachmajo r emissionsource .

Emission Sourc e Stac k concen tratio no f eac hsolvent , Plum

e temp. , Exi t

velocity , ft/se c Stac k

height , f t Stac k diameter , f t

C . Deliver

y an d Storaqe 1 . Pleas e provid e the informatio nrequested i nTabl e 2 o n the storag e vessel s used t o stor e virgi nan d recovered solvent . 2 . I f a vapo r balanc e syste m i s used for tanke r deliverie s i nwhic hthe solven t vapor s i nthe head spac e o f the tan k ar e vented bac k t o the tanke r during delivery , pleas e describe .

3 . I f som

e type o f particulat e contro l syste m (e.g. , filters ) exist s for deliver y an d storag e o f particulat e HAP's , pleas e identify .



## 3P.1 0

/ 4 . Wit h respec t t o th e bul k solven t storag e tanks , doe s a syste m exis t t o contai n (capture ) emission s fo r deliver yt o a contro l device ? I f yes , pleas e describ e thi s syste m(includ e pipin g diamete r an d length , ai r flows , etc.) .

5 . I f N 2 i s use d a s par t o f th e storag e tan k and/o r mi x equipmen t emission s contro l syste m(a s oppose d t o othe r reasons , suc h a s safety) , pleas e provid e a descriptio n o f th e system , including : (a ) I f i t i s bough t a s liqui d o r ga s (b ) siz e o f cylinder s o r tank s use d - (c ) Flo wrate , acfm , (i f applicable)
. (d ) Annua l N 2 use , ft 3 (e ) Solven t concentratio n i n N 2 discharg e t o th e atmosphere , pp m. D . Mi x roo m 1 . Pleas e complet e th e applicabl e statement : numbe r o f coatin g line s serve d b yeac h mi x room : ; o r th e percentag e o f mi x equipmen t tha t i s dedicate d t o a specifi c lin e . 2 . Pleas e describ e an d attac h a diagra mo f th e emissio n captur e system/ventilatio n syste muse d i n eac h coatin g mi x preparatio n area . Indicat e wha t system s ar e use d an d t o wher e th e emission s ar e vented
. Includ e ai r flo wrate s durin g mi x preparatio n an d a t othe r times , HA P concentratio n maintaine d i n th e ductwork , and , i f tank s ar e close d an d emission s ducte d t o a contro l device , ho wth e ai r i s supplie d t o th e tanks
.

I f an yo f th e mi x equipmen t i s covered , pleas e provid e a descriptio n o f th e cove r an d th e seal s use d (e.g. , fla t stee l plat e extendin g a n inc h beyon d th e edg e o f th e mixer , n o gaskets , bolte d i n place) , ho wofte n th e cove r i s opened , an d ho wth e constituent s ar e adde d t o th e tank
.

OaP.1 1 

# i 4 . Ar e an

y wast e coating s produced ? I f yes , ho

w much , gal/y

r I f yes , describe ho w the y ar e treate d an

d disposed an

d provide the amoun t o f fina l treate d wast e tha t i s disposed eachyear . .

5 . For eachmi xroom , pleas e provid e th e dat a requested i n Tabl e 3 . E . Coatin

g Operation 1 . Pleas e provide the informatio nrequeste d inTable s 4 an d 5 for eachcoatin g line . 2 . Pleas e provid e th e followin g coating characteristic s for eachtype o f tape produced on.th e magneti c tap e manufacturin

g lines , eveni f som e product s ar e no t magnetic .

1 Coating parameter s j Wha t percen t o f the | coating i s solvent O f th e tota l liqui d J solvent , wha t | volum e an d weigh t 1 percen t i s eac

h I solven t 1 Particulat e matte r | (PM ) HAP' s i n I coating O f tota l P

M i n coating , % o f each HAP volum e % weigh t % Solvent : Solvent : Solvent : volum e % weigh t % HAP: HAP : HAP : Densit y o f coating , lb/ga l 1 Densit y

o f coatin

g solids , | lb/ga l Produc t cod e (se e Attachmen t 2 )



### 10TABL E 3 . PHYSICA L AN D OPERATIN G PARAMETER S FO RMI X ROO M EQUIPMEN T ' Numbe r Capacity , ga l Operatin g time , hours/da y an d hr/batch o f

coatin g Metho d o f

solven tand solid s addition 8
Operated unde rpressure , ye s o rn o Ho w i s pressur e applied ? Open o rcovered ? Solven tconcentratio n i n headspace , specif y unit s Us e o f breathe rvalves/conservatio n vents ; If yes , valv e diameter , in. ; Valv e pressur e setting , specif y unit s Valv e vacuu m setting , specif y units Mixer s Mill s

" Polishin g tanks Holdin g tanks Othe r(specify )

* \

a Fo r example , piped , poured b y han d throug

hhatch , hopper .

S 3TABL E 4 . COATIN GLINE INFORMATIO

N

^ Lin e

I D Dat e instaUed * Width , in . Averag e lin e speed , ft/min Hour s o f

coating , hr/y r Percent

utilizatio n o f lin e Ai rdrawn from Ih e coate r

hea d

• LE L Flowrate ,

scfi n Ai rdraw n firom th e ove n

*LE L Flowrate ,

scfi n Temp , # F

*If partia l replacemen toccurred , pleas e complet e Sectio n Ko f thi s infonnatio n request . If thes e da u ar

e significantl y differen tfo reac h zon e o f th e oven , pleas e provid e informatio n foreac h zone .

TABL E 5 . COATING LIN E PRODUC T INFORMATION 

# X

Lin e I D Productcode * Productfor m Amounto f coatin g applied , lb/f

t We tthickness , mil s Singl e o rdoubl e side d coatin g

'Pleas e se e Attachment2 tot produc tcode . I f

mor e than on e typ e i s produce d pe rline , pleas e circl e Ihe typ e lhati s produce d i n greates tamounts . I s th e final productshippe d ttom Ihe plas tunalitweb , pancakes , blan ktape , prerecofde d tape , other ?

T lP. M

3 . Pleas e writ e th e lin e I D unde r eac h o f th e followin g type s o f ventilatio n system s use d t o captur e emission s a t th e coate r hea d fo r eac h coatin g line
. Tota l enclosur e Pick- u

point s Canop yhoo d Othe r Roo m H ventilatio n I

a Pick-u p point s ar e smal l vents , ofte n locate d nea r th e floor , tha t ar e no t withi n a n enclosur e an d provid e localize d ventilation
. 4 . Pleas e provid e th e followin g informatio n o n th e ai r handlin g syste mfo r eac h coatin g line
. a . b
. c . d
. e . Aschemati c and/o r descriptio n o f th e ai r handlin g system , includin g recirculatio n Indicat e location s o f captur e syste mpickups , dimensions , an

d volumetri c flowrates
. Makeup ai r requirements , acf mo r scf m Provid e a copyo f th e results ' o f an yresult s o f any captur e syste mtestin g Ha s recirculatio n bee n considered ? Fo r whic h operations ? Wh

ywa s i t o r wasn' t i t installed ?

f
. I f ther e i s a n enclosur e tha t completel ysurround s th e coater , provide : (1 ) Relativ e are a o f natura l draf t opening s (NDO's ) (2 ) Location s o f NDO' s relativ e t o emissio n point s (3 ) Locatio n o f NDO' s relativ e t o exhaust s (4 ) Averag e facia l velocit ythroug h and/o r pressur e dro p acros s NDO' s



### \"hP.1 5

5 . Pleas e provid e the followin g informatio

nfor each coatin g line .

Lin e I D Ove n

pressure 3 Coate r head

pressure a Coatin g roo m pressure 3 "Clean

room " condition s f (Y/N ) 

# I

a Provid e actua l unit s o f pressure , i f available . A t a minimum , indicat e whethe r are a i s operatin g a t positive or negative pressure . F . Packagin

g an d Labelin

g o f Product s NOTE : Complet e thi s sectio nonl y i f liqui d or particulat e HAP' s ar e used . 1 . Pleas e provid e the followin g informatio

nfor al l activitie s performed for finished magneti c tap e products .

Activit y Nam e o f HAP' s used Quantit y o f HA P used or emitted/y

r (indicat e which ) Contro l syste m (Y/N ) Plasti c molding Printin g (label s or directl y

o n boxes ) Gluin g (label s or boxes ) Shrin k wrapping Othe r (specify )



## | fP.1 6

^ 2 . I f HA P emission s fro mpackagin g o r labelin g ar e capture d an

d controlled , pleas e provid e a detaile d descriptio n o f th e process , includin g ventilatio n rates , concentrations , etc .

I f solvent-lade n ai r fromcleanin g o r treatmen t and disposa l o f cleanin g solvent s i s vente d t o a contro l device , complet e Tabl e 8 . Indicat e i f tha t contro l devic e i s dedicate d onl yi n Sectio n I t o cleanin g operation s o r als o control s othe r emissio n source s

(indicat e whic h ones) . G . Cleanin g 1 . I n Tabl e 6 , indicat e al l proces s step s i n th e productio n o f magneti c tap e tha t requir e th e us e o f cleanin g materials
. Pleas e identif yth e particula r typ e o f cleanin g operatio n (e.g. , wiping , dipping , spraying , o r flushing ) tha t i s use d i n eac h proces s step . 2 . Ho wmanywas h sink s ar e use d fo r cleaning ? Ho w ofte n ar e the yused ? Wha t i s th e surfac e are a o f each ?


### 3 . Ho wman

ywas h tank s ar e use d fo r cleaning ? Ho w ofte n ar e the yused ? Wha t i s th e surfac e are a o f each ?
4 . I f an

yothe r equipmen t i s use d fo r cleaning , pleas e lis t an d describ e wher e an d ho wi t i s used
.



### I *TABL E 6 . GENERA L INFORMATIO

N O N CLEANIN

GOPERATION S

<T- . Cleanu

p description Mi xtank (example ) Mi xequipmen t Filte r housing s Pum p part s Coate r hea

d Calendarin

g roll s Blade s onslitte r Spill s Othe r (pleas e specify ) Cleanu p operatio

n flushin g Solvent use d MEK Frequenc y o f operatio

n 2/week Volum e o f solven t pe r operation , ga l 1 0



# X

T lP.1 8 

## tf Usin g th e followin g table , indicat e ho wventilatio n i s provide d t o th e area s i n whic h th e cleanin g i s performe d (provid e numbers , locations , airflo wrates , concentrations , destination , etc.) .

Hood s
Floo r sweep s

Roo mai r change s (no . pe r hour ) othe r (specify ) Storag e

are a Mi x roo m Coate r Packagin g are a

6 . Ho war e th e mops/rags/sponges/brushes , etc. , treate d an d dispose d of ? D o the yente r a manifes t program ?

Ho wmuc h dirt ycleanin g solven t i s generate d eac h year , an d ho wi t i s handle d an d disposed ? Ar e yo u require d t o manifest ?

8 . I f solvent-lade n ai r fromcleanin g o r treatmen t and disposa l o f cleanin g solvent s i s vente d t o a contro l device , complet e Tabl e 8 i n Sectio n I . Indicat e i f tha t contro l devic e i s dedicate d onl yt o cleanin g operation s o r als o control s othe r emissio n source s

(indicat e whic h ones) .



# nP.1 9

* H . Fugitive Emission s 1 . Pleas e provide the followin g informatio

nonthe tota l number s o f component s for the equipmen t tha t transport s HAP' s an

d the coatin

g durin g the manufactur e o f magneti c tape . Componen t Pum p seals 3 Packe d Mechanica l 1 Doubl e mechanical* 3 I Compresso r seals 3 1 Flange s Valve s Sampl e connection s 1 Open-ende d line s (e.g. , purge , 

### B vent) c 1 Tota l numbe r

•

'

3 Lis t numbe r o f seals , no t numbe r o f pump s an d compressors . b I f doubl e mechanica l seal s ar e operated wit hth e barrie r flui d (B ) a t a pressur e greate r thanthe pum p stuffin

g boxpressur e and/o r ar e equipped wit ha senso r (S ) tha t wil l detec t failur e o f the sea l system , the barrie r system , o r both, , indicat e wit ha "B " and/o r an"S" . c Line s closed durin g norma l operationtha t woul d b e used during maintenanc e operations . 2 . I f a forma l lea k detectionan

d repai r progra

m for reducin g fugitiv

e emission s fro

m thes e source s i s i n place , pleas e complet e Tabl e 7 . I . Contro l Device s 1 . Pleas e specif y

the type , manufacturer , an d dat e o f installatio

nfor eachcontro l device .

«TABL E 7 . EQUIPMENT LEA KEMISSION S DETECTIO N AN D REPAI R
Equipmen t typ e Pum p seal s Compresso r seal s Flange s Valve s Pressur e relie f device s Sampl e connection s Open-ende d line s Lea k detection Concentration , pp m Wher e

measured Detection

devic e Frequenc y o f lea k monitorin

g Repair s initiated (days afte r detection ) Repair s |

complete

d | (day s afte r [ initiated )



# fcv

t o oP.2 1

^ 2 . Contro l devic e efficienc y a . Pleas e provide monthl y averag e contro l efficiency (e.g. , bed o

r destructionefficiency ) for th e contro l device . I f applicable , als o provid e th e averag e lin

e HA P recover

y efficiency

(HA P recovered/HA

P use d at coaters ) an

d tota l HAP recover y efficienc

y for the plan t for the las t 1 2 months . I f yo

u do no t have operatin g dat a for anentir e year , pleas e provid e an y dat a tha t ar e available .

Mont h 9 Jan . Feb . Mar . Apr . Ma y Jun . 

### I Jul . Aug . Sep . Oct . Nov . Dec . | Averag e 9 fo r yea r Efficiency \

Contro l devic e 1 Contro l

devic e 2 Averag e o f

eachline (provid e lin e ID ) Plan t

averag e

.

| Ho w wer e th

e contro l devic e efficiencie s determine d (e.g. , liqui d materia l balance , contro l devic e inlet/outle t ratio) ?

c . Ho w wer e the averag e line efficiencie s determined ?



## ZoP.2 2

^ d . Ho w wa s the plan t averag e contro l efficiency determined ?
3 . Pleas e attacha description , includin g a flo w diagram , o f the HA

P recover

y syste m (e.g. , distillationsystem) . 4 . Wha t amoun t (indicat e units ) o f the recovered HAP' s are : a . Use d i ncoatin g mix ? b . Use d i ncleaning ? c . Fired i non-sit e boilers ? ~ d . Shipped off-sit e permanentl y (provid

e destina tion) ? f e . Shipped off-sit e for reclamationan d returned (provid e use) ? f . Othe r (specify) ? . 5 . Pleas e complet e Tabl e 8 for eachcontro l devic e yo u operate . I f you wis ht o us e measuremen t unit s othe r thanthos e specified for the parameters , pleas e indicat e the unit s used . 6 . D o you continuousl y monito r inle t or outle t concentrationo f solvent s or HAP' s fo r an y contro l device ? . I f yes , pleas e specif y eachHA

P monitored , the type s o f monitors , an

d the samplin

g systems use

d for each contro l device .

7 . Additiona l question s regardin g fabri c filters : a . Describe the bag cleanin g cycle . Indicat e ho w th e cleanin g frequenc

y i s controlled an

d estimat e th e typica l frequency .

b . I f ther e have an y particula r problems wit hbag failure , pleas e describe .



## t lTABL E 8 . CONTRO L

Typ e device/paramete r Operation s serve d b y thi s contro l devic e DEVIC E SPECIFICATION S Contro l devic e No . 1 Desig n Actual Control devic e No . 2 Desig n Actual

CARBO N ADSORBE R Sectio n 1 . Thi s sectio n applie s t o both fixed and fluidized be d units . * SLA * flow rate , nominal , acf m maximum , acf

m

• SLA inle ttemperature , ° F

• SL A inle tpercentR

H

• SLA inle tconcentration , ppmv o rppmC :
* SLA outle tconcentration , ppmv o rppmC : Typica l Maximu m

• Carbo n lifetime , m o

• Total carbo n charge , l b .

•

Sectio n 2 . Th e followin g sectio n applie s only t o fixe d beds .

• No . o f

bed s

• No . o f

bed s use d a

ton e tim e

• Stea m rate , lb/h r lb/l b charcoa

l lb / (specify ) Contro l devic e No . 3 I Desig n Actual

- 

# XTABL E 8 .

Type device/paramete

r Sectio n 3 . This section applie

s only t o fluidized beds .

• No . o f tray s

• Carbo n flow rate

, lb/h r

• Pressur

e dro p pe rtray , in . wate r

• Regeneratio

n agent—N

2 orsteam?

• Regeneratio

n temperature

, ° F

• N2 orstea

m rate , lb/h rorft^/hr CONDENSATIO

N SYSTE M

• SL A flow rate, nominal, acf

m maximum , acf m

• SL A inle ttemperature

, ° F

• SL A inletgas composition, percen tLE L

• N 2 consumptio

n rate, ft 3/yr (continued ) Contro l device No . 1 Design Actua

l Contro

l device No . 2 Design Actua

l Contro

l device No . 3 Desig n Actua

l

\^

- ^ TABL E 8 .
Typ e device/paramete r INCINERATO R

• Catalyti c( Q o rtherma l (T )

• SL A flow rate, nominal , acf m minimum , acf

m maximum , acf

m

• SLA inle ttemperature , ° F

• Incinerato rtemperature , ° F

• Destructio n efficiency , percent

• Residenc e time , se c

• Fuel consumption : Typ e fuel Annua l amount

• Hea trecovery : Wit h primar y heatexchange ? Ye s o rN o With secondary heatexchange ? Ye s o rN o FABRI C FILTE R(giv e both averag e and typical range values )

• Gas temperature , ° F

• Gas flow rate, acf

m

• Moistur e content , percent (continued ) Control devic e No . 1 Desig n Actua

l

• Contro l devic e No . 2

Desig n Actua l Contro l devic e No . 3 Desig n Actual

\TABL E 8 .

Typ e device/paramete r

• Inletparticulate loading , gr/dsc f

• Cleanin g mechanis m (e.g. , shaker , revers e air , puls e jet )

• Ga s t o cloth ratio, acfm/ft 2

• Bag length , ft

• No . o f

bag s * No . o f

compartment

s

• Outletparticulat

e loading , gr/dsc f

• Pressure drop acros s baghouse , in . w.c .

• Ba g life , m o 

### (conti n ued ) Contro l devic e No . 1 Desig n Actual Control devic e No . 2 Desig n Actua l Control devic e No . 3 Desig n Actual

FLARE

• Maximum heatconten to f ven tstream , BTU/scf

m

• Exi tvelocity , ft/s

• Averag e HA Pconten to f ven tstream , percent 

# X

a SL A i s solven tladen air .P.2 7 

# p Pleas e provide dat a o nbaghous e dus t characteristics .

d . Describe the baghous e dus t collectionsyste m an d dus t disposa l practices .

e . Do yo

u pretrea t the ai r strea m o r ar e reagent s injected t o enhanc e performance ? I f yes , pleas e describe the process .

8 . Additiona l flar e question : I s the flar e steam-assisted

, air-assisted , or nonassisted ? J . Wastewate r an d Soli d Wast e Treatmen t an d Disposa l Pleas e provid e the followin g informationo

nan y soli d waste s o r wastewate r generated b y (1 ) the HAP contro l devices , (2 ) the HA

P recover

y system s (e.g. , distillation) , an d (3 ) othe r (specify) . I f magneti c tape wast e i s combined wit hth e tota l plan t waste , pleas e estimat e quantitie s tha t resul t fro m magneti c tap e productionan d control .

Descriptionan

d sourc e o f wast e EXAMPL E Stil l bottoms fro m solven t recover y Amount , gal/yr ; lb/y r 1,00 0 gal/y

r On-sit e treatmen t methods , i f an

y none Disposa l method s Reclaime r HA P concentrationi n wast e fro

m eachsource , PP m 1,00 0 pp m

Rat e o f discharg e fro m plant , gal/yr ; lb/y r N/ A



### lbP.2 8 

# S
K . Retrofit
. Replacement , an d Modificatio n 1 . Pleas e lis t an

ymodification s o r replacement s o f th e coatin g line(s ) and th e associate d costs . 

### j Yea r Lin e

I D Descriptio n o f

modificatio n Reaso n fo r modificatio n Cost , $

2 . Ar e ther e plan s t o replac e existin g equipment ?
I f yes , why , and wha t equipmen t i s t o b e replaced ?

3 . I f emission s fromth e storag e tanks , mi x equipment , o r coate r ar e no t alread ycontrolled , pleas e discus s th e feasibilit yo f retrofittin g control
. Pleas e b e specifi c (e.g. , distances , access , configuration , etc.) .

L . Othe r 1 . I s th e facilit ysubjec t t o an yStat e o r loca l agenc y ai r pollutio n contro l requirements ? I f yes , pleas e provid e a copyo f th e permit
. 2 . Ar e ther e an

yothe r regulatoryrequirement s (e.g. , OSHA , RCRA ) tha t woul d affec t you r abilit yt o compl y wit h additiona l ai r pollutio n contro l requirements ?
I f yes , pleas e discuss :



## 2 7P.2 9



## PART E M . Economi c Information 1 . Pleas e provid e th e followin

g estimate s o f your expansionplan s for the next 5 years . No . o f ne

w line s added t o existin g plan t No . o f ne

w plant s buil t
2 . No . o f line s a t th e ne w plan t I f installationo f ne w line s i s anticipated , pleas e provid e the followin g informatio

nabou t eachprobabl e line .
Lin e Lin e width , in . Lin

e speed , ft/mi n Coatin

g metho d Produc

t cod e

3 . Pleas e provid e the followin g informatio

nfor you r products .

9 Produc t 1 code Annua l production

or annua l sale s (indicat e which) a Averag e pric e pe r unit b Productio n cost , $/ft 2 c Averag e fl

percen t I pretaxH 

### profi t fl 

# 1 

# 1 

# 1

aNumbe r o f cassettes , disks , ft 2 o f coated product , etc . ^Provide th e averag e pric e for eachuni t o f outpu t for eac hmajo r categor y o f product . Giv

e price , lo t size , an d t o who

m sol d (e.g. , wholesale , distributor ) or attac hpric e list . ^ota l productioncost , includin g line operation , contro l device , etc . 4 . Ar e your product s sol d inregional , national , and/o r

internationa l markets ? 5 . Th e Smal l Busines s Administrationdefinitiono f a smal l busines s for SI C Code s 357 3 an d 367 9 i s a fir

m tha t employ s 50 0 person s or fewer . Canyour fir m an d paren t compan y be considered a smal l busines s b y thi s definition ? I f yes , pleas e provide the tota l numbe r o f employee s i n your fir

m (parent company ) (i.e. , no t jus t th e magneti c tap e productionfacility or your individua l plan t site) . '. : — 

### 1%P.3 0 

# rf
N . Cos t Informatio n

Pleas e provid e tota l capita l and curren t annua l operatin g cost s fo r th e magneti c tap e productio n operation s (fro

mdeliver yo f ra wmaterial s t o shipmen t o f fina l product)
. Tota l capita l cos t Tota l annua l operatin g cos t (yea r

. ) Capita l and annua l cost s shoul d b e provide d fo r proces s equipment
. Annua l operatin g cost s shoul d include , fo r example , labo r (production , maintenance , and super visory ) , supplies , energy , and wast e disposa l costs . Pleas e documen t al l assumptions , includin g cos t referenc e yea r and discoun t factors
. Provid e wor k sheets/table s showin g ho wthes e cost s wer e calculated
. I f i t i s simple r t o provid e capita l and annua l operatin g cost s fo r th e combinatio n o f productio n an d contro l equipmen t rathe r tha n jus t fo r th e proces s equipment , pleas e d o so . Wha t i s th e cos t o f eac h HA P used ? 

# IHA P 

# 1 1 

# 1 $/uni t (specify ) HA P 

### $/uni t

(specify )

Pleas e provid e th e capita l cos t informatio n i n Tabl e 9 fo r th e ventilatio n system s fo r th e variou s emissio n source s indicated , i f th e ventilatio n i s par t o f th e emission s contro l system . I f an yo f th e equipmen t wa s retrofitted , pleas e indicat e o n th e tabl e wit h a n asterisk
. I f ther e ar e an

yannua l operatin g cost s fo r thes e ventilatio n system s othe r tha n th e energycosts , pleas e describ e and quantif yhere
. (B e sur e tha t th e airflo w rat e informatio n ha s bee n supplie d wher e requeste d i n Question s C.4 , D.2 , E.4 , F.2 , an d G.5. )



### Z< ?P.3 1



# s

T.ABL E 9 . INSTALLE D COST S FOR VENTILATIO NEQUIPMENT j • ' 9 Emissio n | sourc e 1 Deliver y and storag e
Mi x room

Qeanin g

Packaging

/ labelin g
Fugitiv e emission s Equipmentinclude d i n th e

cos testimate

Coate rhead s fo reach lin e Lin e ID : Lin e ID : Lin e ED : Lin e ID : Purchas e cost , $ Installatio n

cost 1 , $

• Referenc e

yea r Depreciabl e

life , y r

a Includin g start-up , engineering , contingenc yfees , etc .



### 3> oP.3 2



# X 5 . Th e followin g question s as k fo r cos t dat a o n th e contro l device(s) ; complet e on e colum n fo r eac h contro l device
. I f dat a ar e no t available , pleas e estimat e replacemen t cost s i n 199 1 dollars
. Pleas e provid e annua l operatin g cost s i n 199 0 dollars
. I f absolut e amount s ar e no t available , pleas e respond wit h dat a tha t bes t fi t tha t specifi c bloc k o f th e table
. I f any o f th e cost s ar e fo r retrofitte d equipment , pleas e indicat e wit h a n asterisk
. a . Installe d Capita l Cost s o f Contro l Device (s ) Typ e o f contro l system : Materia l o f constructio n (e.g. , stainles s steel) : Purchase d cost , $ : Referenc e year : Depreciabl e life , yr : Initia l carbo n charg e Tota l charge , lb : Carbo n cost , $/lb : Initia l N 2 charg e (fo r condensatio n systems ) Amount , ft3 : N 2 cost , $/ft 3 : _ Othe r installatio n cost s (specify) : TOTA L installe d cost , $ : b
. Pleas e lis t th e majo r equipmen t include d i n th e abov e capita l cos t estimate(s)
.

c . Annua l Operatin g Cost s fo r Contro l Device (s ) Typ e o f contro l devic e Direc t labo r Labo r hours : Cost , $/hr. : Supervisor ylabo r Labo r hours : Cost , $/hr. :


### 3 /P.3 3

Repair s and maintenanc e Part s and supplies , $/yr. : Labo r hours : Labo r cost , $/hr. : Electricit y(fans , etc. ) Use , kWh : Cost , $/kWh : Activate d carbo n replacemen t Cost , $ : $/lb : _ _ Carbo n regeneratio n Rate , lb : Cost , $/lb : Steam/N 2 fo r carbo n adsorbe r Units : $/unit : Fue l fo r steamgeneratio n Type : Use , units : Cost , $/unit : ~ Wate r (bed quenching , etc. ) Use , 1,00 0 gal : Cost , $/l,00 0 gal : ~ N 2 consumptio n fo r condensatio n syste m Use , ft 3 : Cost , $/ft 3 : Incinerator/flar e fue l Cost , $ : type : $/unit : $/yr. : Othe r annua l operatin g cost s (pleas e specify )
TOTA L annua l operatin g costs , 199 0 $ :



### !>lP.3 4



## 7* 6 . Pleas e provid e th e followin g cos t informatio n fo r th e distillation , soli d waste , wastewater , and othe r (e.g. , wast e coating ) treatmen t system s a t you r facility
. a . Installe d Capita l Cost s Distil

- Soli d Waste
latio n wast e wate r Othe r Purchase d cost , $ : Materia l o f contruction : Referenc e yr : Depreciabl e life , yr : Othe r instal

latio n cost s (specify) : TOTA L installe d cost , $ : b
. Pleas e lis t th e majo r equipmen t include d i n th e abov e capita l cos t estimate(s)
.

Annua l Operatin g Cost s Electricit y Use , kWh : Cost , $/kWh : Steamgeneratio n Use , lb : Cost , $/lb : Fue l fo r steam generatio n Type : Use , No . units : Cost , $/unit : TOTA L annua l operatin g cost , $/yr : b5304-l/DI S 

## " 3 3P.3 5

Attachmen t 2

Pleas e us e th e followin g produc t code s i n respons e t o th e questions
. Produc t cod e A- C A-O R A- P V-VH S V- P C-O R C- D I D- M M- I L Typ e o f tap e produce d

audi o cassett e (consumer ) audi o ope n ree l audi o - professiona l vide o VH S vide o - professiona l compute r ope n ree l compute r flopp

ydisk s instrumentatio n tap e compute r magneti c car d medi a magneti c ink s no t applie d a t thi s facilit y leade r tap e (nonmagnetic ) Pleas e specif yother s



# ^ f