# OAR Box 1413 Prepped by Ollie Stewart



## Document

Number: 

# 54 ) 11-1-5 4 Docket Number: 

# A-94-5 2

Printed 7/9/2008 3:11:22 PM Sheet 54 of 114 P. 1P. 2 $<** ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N

. . , P.O . BO X1950 6 SPRINGFIELD . ILLINOI S 62794-950 6 •kfiVJdlM-jJkiwn H Revision?*- ° Date : Pag e b f Sourc e Designation : 

# /HV--TL JE~rt'5*\

APPUCATION

FOR CAAPP PERMIT (CHECK ONLY ONE) 

### X X INITIA L APPLICATIO N RENEWA L APPLICATIO N SIGNIFICAN TMODIFICATIO N 

# "PEKrarnr T5CTE T SOURCE

INFORMATION no - "-57T 7 

### r o i > nr



### rj
th"/ AAI H ULN-Mr." ' 1 ) SOURC E NAME : 

## Gran e Keml'ite Compan yInc
. 3 ) SOURC E STREETADDRESS : 

## 2352 5 W.Eame s Stree t 2) BAT E FOR M COMPLETED : Novembe r30,199 5
"3TCIT7 : ~ 

## Channaho n 5 ) I S TH E SOURC E LOCATE D WITHI N CIT V UMITS ? 

## N o "57ZIP T 

## 6041 0 YE S XXXN O 1\ TOWNSHI P NAME : 

## Channaho n h) COUNTY : 

## Wil l ib) ILUNOI S AI R POLLUTIO N 50URCE'I D KI0 . (I F KNOWN) : 

## 197800AA

X § , TYPICA L NO . O F EMPLOYEE S A TTH E SOURCE : 

## 27 5 i\) FEDERA L EMPLOYE R IDENTIFICATIO N NO . (FEIN) : 

## 06-138000 5 il) TYP E O F SOURC E ANDPRODUCT S PRODUCED: — 

## Reinforce d Plasti cComposite s Production ; Fiberglas s reinforce d plasti cpanel s \i) PRIMAR YSTANDAR D INDUSTRIA L CLASSIFICATIO N (SIC ) CATE50RV : 

## Miscellaneou s Plastic s 15a ) LATITUD E (DD:MM:5S) : 

## 4 1 - 2 7 - 4 5 16a ) UT M ZONE : 17a > COORDINAT E METHOD : 

# I 14) PRIMARYSI C NO. : 

## 308 9 b . LONGITUD E (DD:MM:55. : 

## 88-11-1 5 b ) UT M VERTICA L (RM) : b , REFERENC E LOCATION : 

## cente ro f plan t 16) SOURC E ENVIRONMENTA L CONTAC TPERSON : 

## Pau l Margherio , CHM M c) UT M HORIZONTA L (KMJ :
15 ) CONTAC T 

## 815-467-865 6

c) COORDINAT E ACCURACY : 

## +/- 2.5000SE C PERSON' S TELEPHON E I



## nro : _ i

THI S AGENC

YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R ILLINOI S REVISE D STATUES . 1991 . AS AMENDE D 1992 , CHA P 1111/2 . PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E T O D O S O MA Y PREVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPLICATIO N BEIN G DENIED . THI S FOR M HA S BEE N APPROVE D B

YTH E FORM S MANAGEMENTCENTER . 

## APPLICATIO N PAG E CAAP P - 20 0 

## 1.1- 1 FO R APPLICANT S US E PAG E 1 O F 5

### 197800AA X Cran e Kemlit e



# c . . P. 3 

## TABL EO FCONTENT S rt 

## Pag e ITEM

Introductio n 200-CAAPP , Applicatio nfo r CAAP PPermi t Tabl e o f Content s Plo t Plan/Map Roofto p ven t location s gri d Sit e Locatio nma p Source-wide Proces s flo

w diagram Proces s descriptio nOvervie w Lis t o f Item s for whic hapermi t

i s bein g sough t 297-CAAP

Pform , Listin g o

f Insignifican t

Activitie s Mixin g Roo m# 1 & # 2 Proces s description , mixin g room s 1 & 2 220-CAAP

Pform , Mixin g Room s # 1 & # 2 Exhibi t 220- 1 Exhibi t 220- 5 & 6 260-CAAP

Pform , Receiver

Filte r 260C-CAAP

Pform , FDV-20 1 260-CAAP

Pform , Dr y weig htan k

I A Filte r 260C-CAAP

Pform , FDV-70 1 260-CAAP

Pform , Dr y weigh t

tan k I B Filte r 260C-CAAP

Pform , FDV-70 2 Lon g Pane l Proces s Line s Proces s description , Lon g Pane l Proces s Line s Proces s flow diagrams : LP-3 , LP-6 , LP- 7 220-CAAP

Pform , Lon g Pane l Proces s Line s Exhibi t 220- 1 Exhibi t 220- 5 & 6 Exhibi t 220- 8 Sil o # 1 & Sil o # 2 220-CAAP

Pform , Sil o # 1 & Sil o # 2 Exhibi t 220- 1 Exhibi t 220- 5 260-CAAP

Pform , Sil o # 1 filter 260C-CAAP

Pform , FDV-10 1 260-CAAP

Pform , Sil o # 2 filter 260C-CAAP

Pform , FDV-10 3 1.1- 1 t o 1.1- 5 1.2- 1 t o 1.2- 2 1.3- 1 1.3- 2 1.3- 3 1. 4 1. 5 1. 6 1.7- 1 t o 1.7- 6 1.1- i 1.1- 1 t o 1.1-1 0 1.1.1- 1 t o 1.1.1- 2 1.1.2- 1 to 1.1.2- 5 1.2- 1 t o 1.2-1 0 1.3- 1 t o 1.3- 2 1.4- 1 t o 1.4-1 0 1.5- 1 t o 1.5- 2 1.6- 1 t o 1.6-1 0 1.7- 1 t o 1.7- 2 2.1- i 2.1-ii t o 2.1-i

v 2.1- 1 t o 2.1-1 2 2.2- 1 t o 2.2- 2 2.3- 1 t o 2.3- 4 2.4- 1 t o 2.4- 3 3.1- 1 t o 3.1-1 0 3. 2 3. 3 3.4- 1 t o 3.4-1 0 3.5- 1 t o 3.5- 2 3.6- 1 t o 3.6-1 0 3.7- 1 to 3.7- 2



## Applicatio n Pag e 1.2- 1P. 4



## 197800AA X Cran e Kemlit e TAB ! _T

? O FCONTENT S Pag e ITEM

Storag e Tank s (9) : R Rcar ; F300 ; X501 ; MlOO ; S400 ; X500 ; M101 ; S401 ; Spare . 4 . l- i Proces s description , Storag e Tank s (9 ) 4.1- 1 t o 4.1-1 0 23 2 CAAP Pform , Storag e Tank s (9 ) 4.1. 1 Exhibi t 232- 1 4.1. 2 Exhibi t 232- 4 & 5 4.2- 1 t o 4.2- 5 Dat afo r Tan k R Rca r (NV-1 0 GPR) 4,3- 1 t o 4.3- 5 Dat afo r Tan k F30 0 (NV-1 1 FXR) 4.4- 1 t o 4.4- 5 Dat afo r Tan k X50 1 (NV-1 2 Flex ) 4.5- 1 t o 4.5- 5 Dat afo r Tan k MlO O (NV-1 3 MMA

) 4.6- 1 t o 4.6- 5 Dat afo r Tan k S40 0 (NV-1 4 Sty. ) 4.7- 1 t o 4.7- 5 Dat afo r Tan k X50 0 (NV-1 5 Flex ) 4.8- 1 t o 4.8- 5 Dat afo r Tan k M10 1 (NV-1 6 MMA

) 4.9- 1 t o 4.9- 5 Dat afo r Tan k S40 1 (NV-1 7 STY) 4.10- 1 t o 4.10- 5 Dat afo r Tan k Spar e (NV-18 A Nad ) Natura l ga s fired ai rmake-u p heater s #1 ; #2 ; #3 ; # 4 5.1- 1 t o 5.1-1 1 240-CAAPPform , natura l ga s firedai r make-u p heater s 5.1. 1 Exhibi t 240- 1 5.1. 2 Exhibi t 240- 3 5.1. 3 Exhibi t 240- 5 Fugitiv e Emissions - Roa d dus tan d Clean-u p 6 . l- i Proces s description , Clean-u p operation s 6.1- 1 t o 6.1-1 1 391-CAAPPform , Fugitiv e Emission s - Clean-u p operation s an dPave dSurface s emission s 6.1. 1 Exhibi t 391- 1 6.1.2- 1 t o 6.1.2- 2 Exhibi t 391- 5 Summar y Materia l S.l-ltoS.1- 2 215-CAAPPform , HA PEmission s Summar y S.2- 1 t o S.2- 5 296-CAAPPform , Complianc e Certificatio n S.3- 1 t o S.3- 2 292-CAAPPform , Fe e Determinatio n S.4- 1 t o S.4- 4 293-CAAPPform , Complianc e Pla n

Applicatio n Pag e 1.2-1 .P. 5P. 6

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# wk 8 - jilfft t 1 Jssltf & A i *!*-»• ? T*»?-?TT?-» e *2ga*»«»'a*?*? 5 'Nn.m o K-DC_ O —<MO-» * > I D •.•>« © —flJS X <*" * * ^ ^ •"•••••••"••'•»»•»••• •ir* * •*••-» O l O l OlOtO i 

### Applicatio n Pag e 1.3- 2 

# J SP. 7

CHANNAHON
. I L 7. 5 MINUT E USG S TOPOGRAPHI C QUADRANGL E MA P 1993
. T34N
. R9E
. SEC
. 3 CRAN E KEMUT E CO
. JOLIET , I L 6043 4 I.D
. * 197800AA X najBTNQ . ORMMGM . 

# I.3- 3 

# (oP. 8



### ID#197800AA X Cran e Kemlite 

## Proces s Descriptio n Overvie w Kemlit e Compan y operate s afacility i nJoliet , Illinoi s t o manufactur e fiberglass reinforce dplasti c panel s fo r us e i ntransportatio nan drecreationa l vehicles ; an d commercial , industria l an dspecialty installatio napplications . Polyeste r resi nmi x an dfiberglass reinforcement s ar e th e tw o majo r component s ofth e panels . Th e facility occupie s approximatel y 126,00 0 squar e fee t unde r one roof o nathirt y four acr e sit e annexe dt o th e City o f Jolie t outsid e th e corporat e boundar y i n Channaho nTownshi p alon g U.S . highway 6 , nea r Interstat e 55 . Whil e th e sit e i s legall y i nJolie t

fo r purpose s of

al l municipa l services , th e mailin g addres s i s Channahon , Illinoi s b y directio no f th e local postmaster . Th e manufacturin g are ao f th e facilit

y include s thre e proces s line s tha t produc e a continuou s fiberglass reinforce dplasti c (FRP ) panel . Ther e ar e tw o mixin g room s wher e ra w material s ar e mixedan dpumpe dt o th e productio nlines . Ther e ar e tw o conversio nprocesse s i nth e manufacturin g area . On e proces s adhere s finishede 

## panel s (fromth e pane l lines ) t o othe r substrates , suc ha s plywood . Th e othe r conversio nproces s i s th e cut-dow nlin e wher e finishedpanel s ar e reworke dt o smalle r sizes . Bul k liqui dra w materials , resin s an dmonomers , ar e store di ntanke r truck s permanentl y parke dt o for matan k far mi nalo t

a t th e Southwes t

en dof th e site . Bul k dr y fillers ar e store di ntw o silo s o napa dadjacen t t o th e manufacturin g building . Fou r gas-fire dunit s hea t

th e make-u p ai r

fo r th e manufacturin g are ao f th e plant . Al l roadways , parkin g lots , loadin g docks , an dothe r drivin g surface s ar e payed , excep t for tiie fire lan e alon g th e Nort hperimete r of th e manufacturin g area .

Applicatio n Pag e 1. 5 

# 1P. 9 

## Lis to f Item s fo rWhic h aPermi ti s Bein g Sough t Tan k Far m 8 Raw Materia l Tanke r

Truc k Storag e Tanks : 2 Styren e 2 Methy l Methacrylat e 4 Polyeste r

Resi n 1 Genera l Purpos e Polyeste r Resi nRai l Ca r

Storag e Tan k Mi x Room# 1 an d# 2 Mi x # 1 2 Dry Materia l Weig hTank s

1 Filte r receive r bi n 2 Alumin aHopper s 2 We t Materia l Weig hTank s 2 Mi x Tank s 3 Fee dTank s Mi x # 2 2 Dry Materia l Weig hTank s w/ particulat e filters 1 We t Materia l Weig hTan k 1 Mi x Tan k 2 Fee dTank s 

## Lon g Pane l line s LP-3 . LP-6 , JJP- 7 LP- 3 1 Resi nDispense r e 

## 1 Fiberglas s Choppe r

w/ particulat e filter

(a s insignificant

activity ) 1 Curin g Ove n LP- 6 1 Resi nDispense r

1 Fiberglas s Choppe r

w / particulat e filter

(a s insignifican t

activity ) 1 Curin g Ove n LP- 7 1 Resi nDispense r

1 Fiberglas s Choppe r

w / particulat e filter

(a s insignifican t

activity ) 1 Curin g Ove n 

## Kempl y Hn e 1 Adhesiv e Spreade r

( a s a ninsignifican t

activit y ) Dr v Materia l Storag e Silo s 1 Calciu mCarbonat e Powde r Sil o (Silo#l ) w /

bi nven t filter 1 Alumin aPowde r

Sil o (Silo#2 ) w/

bi nven t filter 

## Natura l gas-fire d ai rmakeu p heater s #1 , #2 , #3 , #4 Fugitiv e emission s driveway s an dparkin g lot s clean-u p operation s Insignifican t

activitie s aaaddresse di n297-CAAP Pfor m
Applicatio n Pag e 1. 6P.1 0

¥ ' ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O . BO X1950 6 SPRINGFIELD , ILLINOI S 62794-950 6 -M:¥M»[*U , k*HM = Revisio n # : Date : Pag e of Sourc e Designation : 

### LISTING OF INSIGNIFICANT ACTIVITIES iTTOragET C PERMIT S T5KTE THI S FOR M MUS TB E COMPLETE

D FO R AL L ACTIVITIE

S THA TAR E "IMSI-SHH-leAUT

" ACCORDIN

G T O 5 5 IL L ABM. CODE

. SECTIO N 201.21 0 AN O 201.21 1 FO R WHIC H DETAILE D DAT AAN O INFORMATION
. AS REQUESTE D I N OTHE R FORMS , I S NO TPROVIDED
. 

### i) SOURC E NAME : Cran e Kemlit e Compan yInc
. SOURCE INFORMATION 1) BAT E FOR M PREPARED
. Novembe 

### r30,199 5 i) SOURC E I B NO
. (I F KNOWN) : 1978()0AA X 

### INSIGNIFICANT

ACTIVITIES T) AR E AN VON E O R AL LO F TH E FOLLOWIN G ACTIVITIES
. A S IBENTIFIE B I N 5 5 IL L ADM . COD E 201.210(b) , PRESEN TATTH E SOURCE ? CHEC KTH E APPROPRIAT E BOX . ACTIVITIES

IN 3 5 ILLADM . COD E 201.210(b): 

### 0 YE S N O

ii ) i« ) iv ) v) vi ) AI R CONDITIONIN G O R VENTILATIN G EQUIPMEN TNO TDESIGNE D T O REMOV E AI R CONTAMINANT S GENERATEDf BYO R RELEASE D FRO M ASSOCIATE D EQUIPMENT ; PHOTOGRAPHI C PROCES S EQUIPMEN TB YWHIC H A N IMAG E I S REPRODUCE D UPO N MATERIA L SENSITIZE D T O RADIAN TENERGY ; EQUIPMEN TUSE D FO R HYDRAUU C O R HYDROSTATI C TESTING ; GENERA L VEHICL E MAINTENANC E AN D SERVICIN G ACTIVITIE S A TTH E SOURCE , OTHE R THAN GASOUN E FUE L HANDLING ; CAFETERIAS , KITCHEN S AN D OTHE R FACILITIE S USE D FO R PREPARIN G FOO D O R BEVERAGES PRIMARIL YFO R CONSUMPTIO N A

TTH E SOURCE ; EQUIPMEN TUSIN G A WATER , WATE R AN D SOA P O R DETERGENT, O R A SUSPENSIO N O F ABRASIVES I N WATE R FO R PURPOSE S O F CLEANIN G O R FINISHIN G PROVIDE D N O ORGANI C SOLVENTHA S BEE N ADDE D T O TH E WATER ; vii ) ADMINISTRATIV E ACTIVITIE S INCLUDING , BU TNOTLIMITE D TO . PAPE R SHREDDING . COPYING , PHOTOGRAPHI C ACTIVITIES , AN D BLUEPRINTIN G MACHINES . THI S DOE S NOTINCLUD E INCINERATORS ; viii ) LAUNDR

YDRYERS . EXTRACTORS , AN D TUMBLERS PROCESSIN G CLOTHING . BEDDING . AN D OTHE R FABRI C ITEM S USE D A

TTH E SOURC E THA

THAVE BEE N CLEANE D WIT H WATE R SOLUTION S O F BLEAC H O R DETERGENt S PROVIDE D THA

TAN YORGANI C SOLVEN TPRESEN TI N SUC H ITEM S BEFOR E PROCESSIN G THA TI S RETAINE D FRO M CLEAN-U P OPERATION S SHAL L B E ADDRESSE D AS PAR TO F TH E VO M EMISSION S FRO M US E O F CLEANIN G MATERIALS ;

THI S AGENC

YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R ILLINOI S REVISE D STATUES , 1991 , AS AMENDE D 1992 . 2HMP 11 1 1/2 , PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E TO D O S O MA Y PREVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPLICATIO N BEIN G DENIED . THI S FOR M HA S BEE N APPROVE D B

YTH E FORM S MANAGEMENTCENTER .



### APPLICATIO N PAGE . 297-CAAP P 

### 1.7- 1 

# 9 &l:«3;_:H[«HZifcV M PAG E 1 O F 6P.1 1

INSIGNIFICANT

ACTIVITIES

(continued}

_7c , , ix) HOUSEKEEPIN G ACTIVITIE S FO R CLEANIN G PURPOSES . INCLUblN C COLLECTIN G SKILLE D AN B ACCUMULATE D MATERIAL

S A TTH E SOURCE/INCLUDIN G OPERATIO N O F FIXE D VACUU M CLEANIN G SYSTEM S SPECIFICAU YF C SUC H PURPOSES , BU

TNO TINCLUDIN G US E O F CLEANIN G MATERIAL S THA TCONTAI N ORGANI C SOLVENT ; x ) REFRIGERATIO N SYSTEMS , INCLUDIN G STORAG E TANK S USE D I N REFRIGERATIO N SYSTEMS , BU TEXCLUDIN G AN YCOMBUSTIO N EQUIPMENTASSOCIATE D WIT H SUC H SYSTEMS ; xi) BENC H SCAL E LABORATOR YEQUIPMEN TAN D LABORATOR YEQUIPMENTUSE D EXCLUSIVEL YFO R CHEMICAL ' AN D PHYSICA L ANALYSIS . INCLUDIN G ASSOCIATE D LABORATOR YFUM E HOODS . VACUU M PRODUCIN G DEVIC E AN D CONTRO L DEVICE S INSTALLE D PRIMARIL YT O ADDRESS POTENTIAL ACCIDENTA L RELEASES ; xii) RESTROO M FACILITIE S AN D ASSOCIATE D CLEANU P OPERATIONS . AN D STACK S O R VENTS USE D T O PREVENT TH E ESCAP E O F SEWE R GASE S THROUG H PLUMBIN G TRAPS ; xiii ) ACTIVmE S ASSOCIATE D WIT H TH E CONSTRUCTION , ONSIT E REPAIR . MAINTENANC E O R DISMANTLEMEN TO F BUILDINGS . UTILIT

YLINES . PIPELINES . WELLS . EXCAVATIONS . EARTHWORK S AN D OTHE R STRUCTURE S THA TOj O NOTCONSTITUT E EMISSIO N UNITS ; xiv ) STORAG E TANK

S O F ORGANIC UQUID S WIT H A CAPACIT YO F LES

S THA N 50 0 GALLONS . PROVIDE D TH E TAN KI ! NOTUSE D FO R STORAG E O F ANYMATERIA L LISTE D AS A HAZARDOU S AI R POLLUTANTPURSUAN TT O SECTlO h 112(b ) OFTH E CLEA N AIRACT ; xv ) PIPIN G AN D STORAG E SYSTEM S FO R NATURA L GAS . PROPANE , AN D LIQUEFIE D PETROLEU M GAS ; xvi ) WATE R TREATMEN TO R STORAG E SYSTEM S A S FOLLOWS : (A ) SYSTEM S FO R POTABL E WATE R O R BOILE R FEEDWATER , (B l SYSTEMS , INCLUDIN G COOLIN G TOWERS , FO R PROCES S WATE R PROVIDE D THA TSUC H WATE R HAS NO TBEE N I N DIREC TO R INDIRECTCONTAC TWIT H PROCES

S STREAM S THA

TCONTAI N VOLATIL E ^ ORGANI C MATERIA L O R MATERIAL S LISTE D A S HAZARDOU S AI R POLLUTANT S PURSUAN TT O SECTIO N 112(b ) O l TH E CLEA N AI R ACT ; xvii) LAW N CARE , LANDSCAP E MAINTENANCE , AN D GROUNDSKEEPIN G ACTIVITIES ; xviii ) CONTAINERS . RESERVOIRS , O R TANK S USE D EXCLUSIVEL

YI N DIPPIN G OPERATION S T O COA TOBJECT

S WIT H •OILS , WAXES , O R GREASES , PROVIDE D N O ORGANI C SOLVENTHA S BEE N MIXE D WIT H SUC H MATERIALS ; xix ) COL D CLEANIN G DEGREASER S THA TAR E NO TINJN E CLEANIN G MACHINES , WHER E TH E VAPO R PRESSUR E O F TH E SOLVENTS USE D NEVE R EXCEE D 2kP a MEASURE D A T38 C O R 0.7kPa AT20C ; xx ) MANUALL

YOPERATE D EQUIPMENTUSE D FO R BUFFING , POUSHING , CARVING . CUTTING . DRILLING , MACHININ G ROUTING , SANDING , SAWING , SCARFING , SURFAC E GRINDING , O R TURNING ; xxi ) US E O F CONSUME R PRODUCTS . INCLUDIN G HAZARDOU S SUBSTANCES A S THA TTER M I S DEFINE D I N TH E FEDERA L HAZARDOU S SUBSTANCES ACT , WHER E TH E PRODUC TI S USE D A

TA SOURC E I N TH E SAM E MANNE R AS NORMA L CONSUME R USE ; xxii ) ACTIVITIE S DIRECTL YUSE D I N TH E DIAGNOSI S AN D TREATMENTO F DISEASE . INJUR YO R OTHE R MEDICA L CONDITION ; xxiH ) FIREFIGHTIN G ACTIVITIE S AN D TRAININ G I N PREPARATIO N FO R FIGHTIN G FIRE S CONDUCTE D ATTH E SOURCE ; XXiv ) INTERNA L COMBUSTIO N ENGIN E O R BOILE R (INCLUDIN G TH E FUE L SYSTEM ) O F MOTO R VEHICLES , LOCOMOTIVES , AI R CRAFT. WATERCRAFT . UFTTRUCKS . AN D OTHE R VEHICLE S POWERE D B YNONROA D ENGINES ; xxv ) ACTIVITIE S ASSOCIATE D WIT H TH E CONSTRUCTION , REPAI R O R MAINTENANC E O F ROAD S O R OTHE R PAVE D O h OPE N AREAS , INCLUDIN G OPERATIO N O F STREETSWEEPERS . VACUU M TRUCKS , SPRA YTRUCKS . AN D OTHE R VEHICLE S RELATE D TO TH E CONTRO L O F FUGITIV E EMISSLQNS O F SUC H ROAD S O R OTHE R AREAS ; xxvi) STORAG E AN D HANDLIN G O F DRUM S O R OTHE R TRANSPORTABL E CONTAINERS WHER E TH E CONTAINERS AR E SEALE D DURIN G STORAG E AN D HANDLING ;



## APPLICATIO N PAGE . 297-CAAP P 

## 1.7-

2 a»];r_.vj:_u*tf__iL:i-£iii>
_ PAG E 2 O F 6 

# inP.1 2


# l^^y^jyi^.^^^P?^?' 1 

# ^ . xxvit yINBMBUA L POINT S O F EMISSIO N O R ACTIVITIE S A S FOLLOWS : (A j INPIVIbOA L FLANGES , VALVES , PUM P SEAL ! PRESSUR E RELIE F VALVE S AN D OTHE R INDIVIDUA L COMPONENT S THA THAVE TH E POTENTIA L FO R LEAKS , (B) INDIVIDUA L SAMPLIN G POINTS . ANALYZERS . AN D PROCES S INSTRUMENTATION , WHOS E OPERATIO N MA Y RESUL TI N EMISSIONS , (C) INDIVIDUA L FEATURES O F A N EMISSIO N UNITSUC H A S EAC H BURNE R AN D SOOTBLOWER S I N A BOILE R O R EAC H US E O F CLEANIN G MATERIAL S O N A COATIN G O R PRINTIN G LINE , (D ) INDIVIDUA L EQUIPMEN TTHA TI S TRANSPORTABL E O R ACTIVITIE S WITHI N A FACILIT YESTABUSHE D FO R TESTlfl G UNITS PRIO R T O SAL E O R DISTRIBUTIO N O R FO R PURPOSE S O F RESEARCH , AN D (E) INDIVIDUA L EQUIPMEN TO l ACTMTIE S WITHI N A PILO TPLANTFACILIT

YTHA TI S USE D FO R RESEARC H O R TRAINING ; xxviii) ACTTVITIE

S A TA SOURC E ASSOCIATE D WIT H TH E MODIFICATIO N ONL YO R CONSTRUCTIO N ONL YO F A FACILITY . A N EMISSIO N UNI TO R OTHE R EQUIPMENTA TTH E SOURCE ; xxix ) ACTIVITIE S A TA SOURC E ASSOCIATE D WIT H TH E MAINTENANCE . REPAIR . O R DISMANTLEMENTO F A N EMISSIO N UNI TO R OTHE R EQUIPMEN TINSTALLE D A TTH E SOURCE , NO

TINCLUDIN G TH E SHUTDOW N O F TH E UNI TO R EQUIPMENT , INCLUDIN G PREPARATIO N FO R MAINTENANCE , REPAI R O R DISMANTLEMENT. AN D PREPARATIO N FO R SUBSEQUEN TSTARTUP . INCLUDIN G PREPARATIO N O F A SHUTDOWN VESSE L FO R ENTRY . REPLACEMEN TO F INSULATION . WELDIN G AN D CUTTING . AN D STEA M PURGIN G O F A VESSE L PRIO R T O STARTUP . IS) AR E AN V EMISSIO N UNIT S A TTH E SOURC E C0N5IBEREBIN5ICKIIFICAN TACTIVITIE S BECAUS E THE V FAL L UNDE R ON E O F TH E ACTIVITIE S O R EMISSIO N LEVEL S LISTE D I N 3 5 ILL . ADM . COD E 201.210(a)(1 ) THROUG H (18) 7 I YES , IDENTIF

YTH E EMISSIO N UNITS I N TH E "US TO F INSIGNIFICAN TACTTVITIE S PURSUANTT O 201.210(a)(1 ) THROUG H (18) " AN D PROVID E TH E REQUESTE D INFORMATION . I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L AS EXHIBI T297-1 . ACTIVITIES

AND EMISSION

LEVELS

IN 3 5 ILLADM. CODE

201.210(a) I ) AN YEMISSIO N UNI TDETERMINE D T O B E A N INSIGNIFICAN TACTIVIT YB YTH E AGENC YPURSUAN TT O 3 5 IL L ADM . COD E 201.21 1 (SE E ITE M #6) ; II ) EMISSIO N UNITS WIT H EMISSION S THA TNEVE R EXCEE D 0. 1 LBS/H R O F ANY REGULATE D AI R POLLUTANTI N TTH E ABSENC E O F AI R POLLUTIO N CONTRO L EQUIPMEN TAN D THA

TD O NOTEMI TANYAI R POLLUTANTLISTE D AS HAZARDOU S PURSUAN TT O SECTIO N 112(b ) O F TH E CLEA

N AI R ACT ; iii ) EMISSIO N UNITS WIT H EMISSION S THA TNEVE R EXCEE D 0.44 TONS/Y R O F ANY REGULATE D AI R POLLUTAN TI N TH E ABSENC E O F AI R POLLUTIO N CONTRO L EQUIPMEN TAN D THA

TD O NO TEMI TANYAI R POLLUTANTLISTE D AS HAZARDOU S PURSUAN TT O SECTIO N 112(b ) O F TH E CLEA

N AI R ACT ; iv )



### v )

vi ) 

# •

• • YE S YE S
YE S 

### XN

O N O
N O DIRECTCOMBUSTIO N UNITS DESIGNE D AN D USE D FO R COMFOR THEATIN G PURPOSE S AN D FUE L COMBUSTIO N EMISSIO N UNITS AS FOLLOWS : (A ) UNIT S WIT H A RATE D HEA

TINPU TCAPACIT

YO F LESS THAN 2. 5 MMBTU/H R THA TFIR E ONL

Y NATURA L GAS , PROPAN E O R UQUEFIE D PETROLEU M GAS , (B ) UNITS WIT H A RATE D HEA TINPU TCAPACIT

YO F LESS THA N 1.

0 MMBTU/H R THA

TFIR E ONL

YOI L O R OI L I N COMBINATIO N WIT H NATURA L GAS , PROPAN E O R UQUEFIE D PETROLEU M GAS , AN D (C) UNITS WIT H A RATE D HEA TINPU TCAPACIT

YO F LESS THA N 200,000 BTU/H R WHIC H NEVE R BUR N REFUSE , O R TREATE D O R CHEMICALL YCONTAMINATE D WOOD ; YE S 

# D N O
EXTRUDER S USE D FORTH E EXTRUSIO N O F METALS , MINERALS , PLASTICS . RUBBER . O R WOOD , EXCLUDIN G EXTRUDER S USE D I N TH E MANUFACTUR E O F POLYMERS . PROVIDE D THA

TVOLATIL E ORGANI C MATERIAL S O R CLASS I O R l l SUBSTANCES i— i SUBJEC TT O TH E REQUIREMENTS O F TITL E VI O F TH E CLEA N AI R AC TAR E NO

TUSE D YE S AS FOAMIN G AGENTS O R RELEAS E AGENT S O R WER E NOTUSE D AS FOAMIN G <— > AGENT S I N TH E CAS E O F EXTRUDER S PROCESSIN G SCRA P MATERIAt T FURNACES USE D FO R MELTIN G METAL S OTHE R THA N BERYLLIU M WIT H A BRI M FULL I I CAPACIT YO F LES S THA N 45 0 CUBI C INCHES B YVOLUME ; | | YE S N O
N O vii ) EQUIPMEN TUSE D FO R TH E MELTIN G O R APPUCATIO N O F LES S THA N 50,00 0 LBS/YR O F WA XT O WHIC H N O ORGANI C SOLVENTHA S BEE N ADDED ; 

# • YE S 

### XN O



## APPLICATIO N PAGE . 297-CAAP P 1.7-3 FO R APPLICANT S US E
PAG E 3 O F 6


# IIP.1 3

viii ) INSIGNIFICANT ACTIVITIES

(continued) EQUIPMEN TUSE D FO R FILLIN 6 BRUMS , PAIL S O R OTHE R PACKA6IN G CONTAINERS ; EXCLUDIN G AEROSO L CANS , WIT H SOAPS , DETERGENTS , SURFACTANTS , l 1 LUBRICATIN G OILS . WAXES . VEGETABL E OILS , GREASES , ANIMA L FATS , GLYCERIN . YE S SWEETENERS . COR N SYRUP . AQUEOU S SAL TSOLUTIONS , O R AQUEOU S CAUSTI C ' ' SOLUTIONS ; ix ) EQUIPMEN TUSE D FO R TH E MIXIN G AN D BLENDIN G O F MATERIAL S A TAMBIENT TEMPERATUR E TO MAK E WATE R BASE D ADHESIVE S PROVIDE D EAC H MATERIAL CONTAIN S LESS THA N 5 % ORGANI C SOLVENTB YWEIGHT ; 

# • YE S
x )
xi ) STORAG E TANK

S O F ORGANI C LIQUIDS WIT H A CAPACIT YO F LES

S THAN 10.000 GALLON S AN D A N ANNUA L THROUGHPU TO F LES S THA N 100,000 GALLONS PROVIDE D TH E TAN KI S NO

TUSE D FO R TH E STORAG E O F GASOUN E O R ANYLISTE D I I YE S HAZARDOU S AI R POLLUTANTPURSUANTT O SECTIO N 112(b

) O F TH E CLEAN AI R ACT; ' ' 

# T l STORAG E TANK

S O F VIRGI N O R REREFINE D DISTILLAT E OIL , HYDROCARBO N I 1 CONDENSAT E FRO M NATURAL GA S PIPELIN E O R STORAG E SYSTEMS . LUBRICATIN G OIL . O R RESIDUA L FUE L OILS ; ' ' xii ) DI E CASTIN G MACHINES WHER E A META L O R PLASTI C I S FORME D UNDE R PRESSURS I iNAniP - 1 I N A DIE ; xiii ) COATIN G OPERATION S (EXCLUDIN G POWDER , ARCHITECTURA L AN D INDUSTRIA L MAINTENANC E COATING ) WIT H AGGREGATE VO M USAG E THA TNEVE R EXCEEDS 1 5 LBS/DA YFRO M ALL COATIN G LINE S A TTH E SOURCE , INCLUDIN G VO M FRO M COATING . DILUTENTS . AN D CLEANIN G MATERIALS ; 

# • YE S YE S YE S Xiv ) PRINTIN G OPERATION S WIT H AGGREGAT E ORGANI C SOLVENTUSAG E THA TNEVE R EXCEEDS 75 0 GAUON S PE R YEA R FRO M ALL PRINTIN G LINE S A TTH E SOURCE . I 1 INCLUDIN G ORGANI C SOLVEN TFRO M INKS , DILUTENTS , FOUNTAI N SOLUTIONS , AN D YE S CLEANIN G MATERIALS ; '— J XV ) GAS TURBINE S AN D STATIONAR YRECIPROCATIN G INTERNA L COMBUSTIO N ENGINEST n O F LES S THA N 11 2 K

W(15 0 HORSEPOWER

) POWE R OUTPUT ; ]X J YE S xvl ) GAS TURBINE S AN D STATIONAR YRECIPROCATIN G INTERNA L COMBUSTIO N ENGINE S 1 O F BETWEE N 11 2 K

WAN D 1.111 8 K

W (150 AN D 1.50

0 HORSEPOWER

) POWE R OUTPU TYE S THA TAR E EMERGENC

YO R STANDB

YUNITS ; ' ' xvl! ) STORAG E TANK

S O F ANYSIZ E CONTAININ G EXCLUSIVEL YSOAPS , DETERGENTS . SURFACTANTS , GLYCERIN , WAXES , VEGETABL E OILS , GREASES , ANIMA L FATS , SWEETENERS . COR N SYRUP . AQUEOU S SAL TSOLUTIONS . O R AQUEOU S CAUSTI C SOLUTION S PROVIDE D A N ORGANI C SOLVENTHA S NOTBEE N MIXE D WIT H SUC H MATERIALS ; 

# • YE S 

## X X X X X X N O
N O
N O N O N O N O ^]N O 

## D N O ^]N O 

## X N O

YE S

YE S N O

N O xviii) LOADIN G AN D UNLOADIN G SYSTEM S FO R RAILCARS , TAN KTRUCKS , O R WATERCRAF

TTHA THANDL E ONL

YTH E FOLLOWIN G UQUI D MATERIAL S PROVIDE D A N ORGANI C SOLVENTHA S NO TBEE N MIXE D WIT H SUC H MATERIALS : SOAPS , i 1 DETERGENTS , SURFACTANTS , LUBRICATIN G OILS , WAXES , GLYCERIN . VEGETABL E OILS . GREASES . ANIMA L FATS . SWEETENER . COR N SYRUP , AQUEOU S SAL T> > SOLUTIONS , O R AQUEOU S CAUSTI C SOLUTIONS . 6 ) AR E AN YEMISSIO N UNIT S A TTH E SOURC E PROPOSE D T O B E CONSIDERE D INSIGNIFICAN TACTIVITIE S THA TMEETTH E CRITERIA USTE D I N 3 5 IL L ADM . COD E 201.211(a) ? I F YES . LIS TTH E EMISSIO N UNIT

S I N TH E "US

TO F ACTIVITIE S FO R WHIC H STATU S A

S A N INSIGNIFICAN TACTIVITIE S I S PROPOSE D PURSUANTT O 201.211(a) " AN D PROVID E TH E REQUESTE D INFORMATION . I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T297-2 . CRITERIA IN

3 5 ILLADM. CODE

201.211(a) i ) TH E EMISSIO N UNI TWOUL D NO TEMI TMOR E THA N 1. 0 LBS/H R O F AN YREGULATE D AI R POLLUTANTNO TUSTE E AS HAZARDOU S PURSUANTT O SECTIO N 112(b ) O F TH E CLEAN AI R AC TI N TH E ABSENC E O F AI R POUUTIO N CONTRO L EQUIPMENT ; ii ) TH E EMISSIO N UNI TWOUL D NO TEMI TMOR E THA N 0. 1 LB/H R O F ANYREGULATE D AI R POLLUTANTUSTE D A S HAZARDOU S PURSUANTT O SECTIO N 11 2 (b ) O F TH E CLEAN AI R AC TI N TH E ABSENC E O F AI R POUUTIO N CONTRO L EQUIPMENT ; AN D iii ) TH E EMISSIO N UNI TI S NOTA PROCESS UNIT . 

# •

1 - APPLICATIO N PAGE . 297-CAAP P 1.7- 4 FO R APPLICANT S US E
PAG E 4 O F 6 

# 10.

## LIS TO F INSIGNIFICAN TACTIVITIE S PURSUAN TT O 201.21 0 (a)(1 ) THROUG H po j



# C 5 EMISSION UNI T" " AN D DESIGNATIO N Electricit y generato r wate r tan k

heate r wate r heate r "#0 F UNITS 

### 2 1 1 DESCRIPTIO N O F UNI TINCLUDIN G AN YCONTRO L

8K wan d 5K

wfor i emergency powe r onl y 200,00 0 inpu t Btu ; propan e fue l bU.oo u inpu t btu ; propan e tue l

• BA51STO R INSIGNIFICANCE SECTIO N 201.210(a) 1 5 (les s tha n 112Kw ) 4 (les s tha n 2.5MMBTU/hr. ) 4 (les s tha n 2.5MMBTU/hr. ) 1 BASI S FO R DETERMINATIO N O F EMISSION S 

### N A NA N A

1 1 F CONSIDERE D INSIGNIFICAN TBASE D O N EMISSIO N LEVEL . TH E DETERMINATIO N METHO O O F EMISSIO N MUSTfl E PROVIDE D (EG. , 1 ) STAC K TEST , 2 ) MATERIA L BALANCE . 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) , 4 ) ENGINEERIN G ESTIMATE , 5 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS)) .


## APPLICATIO N PAGEl-7-5 ,297-CAAP P 

### i»]:¥J_J__l[^Mt*il W
PAG E 5 O F 6

T J

## LIS TO F ACTIVITIE S FO R WHIC H STATU S A S A N INSIGNIFICAN TACTIVITIE S I S PROPOSE D PURSUAN TT O 201.21 1 (a )

EMISSIO N UNI T AN D DESIGNATIO N 

## LP-3 ; LP-6 : LP-7 fiberglass chopper

s Dru m mixin g o f colo r tint s Ti0 2 Slurr y Sys . Tank s Kempl y Lin e 1| U



## 3
1 2
1 DESCRIPTIO N O F UNI T

INCLUDIN G AN Y CONTRO L fiberglas s choppe r o n eac h line ; particulate filte r exhauste d t o th e insid e o fth e buildin g Dru m mi xstatio n t p blen d material s fo r pane l colo r tinting . i On e mi xtan k

an d on e fee d tan k t o delive r white tin t t o mixin g rooms . Laminat e fr p panel s t o plywood . Adhesive spreader , conveyor , an d press . Us e water-base d adhesive . OPERATIN G HOUR S w 

## W i U&BJ K| " W DISCUSSION : 9A 

### h I M Th e filter operatin g hour s correspon d to lin e oper . hn * 1 5 1 3 1 5 2 Thi s operatio n i s don e only a s neede d i n 5 5 gal . drum s 2 1 3 1 5 2 On e cycl e o

foperatio n ever y othe r da

y o fth e wk. 8 1 5 I 52 4 cycle s o f3 0 min s pe r 8 hr . o fadhesiv e spreading . 1 1 

## 1 1 EMISSION S 1 L B PE R POLLUTANT| HOU R HOOPE R YEA R DETERMINATIO N METHOD : PAR T . 1 . 4

4 Engineerin g estimat e an d equipmen t ratin g Styren e Methy l Metttacrylat e .01 5

.0 6 .001 7

.00 7 4 Engineerin g estimat e Styren e . 1 01S 6

4 . Engineerin g estimat e .ygM . .,.,.__. . .0 1 .0 1

assum e negligibl e VO M emissio n rate . (.01 ) OTHE R SUPPORTIN G INFORMATIO N Filte r collect s stra y 2 " lengt h glas s fiber s an d glas s lin t Very lo wvolum e an d frequenc y fo r thi s operation . Very lowfrequenc y o fthi s operation . Negligibl e VO M conten t i n adhesive .

,I U - TOTA L NUMBE R O F UNIT S (EMISSION RATE S SHOUL D B E PROVIDE D O N A PE R UNI TBASIS) . DISCUSSIO N - PROVID E A N EXPLANATIO N O F OPERATIN G HOUR S (E.G. . TH E UNI TI S O N EMERGENC YSTANDB Y- THEREFOR E r TONL YOPERATE S ON E DA YPE R MONTH. ) -"DETERMINATIO N METHOD : 1 ) STAC K TEST . 2 ) MATERIA L BALANCE , 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) . 4 ) ENGINEERIN G ESTIMATE . 5 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS) .

ADD I 

## ir.ATIO N PAG E 17- 6 Mlfaa^WanT.-ll HP.1 6



### DD#197800AA X Crane Kemlit e 

## Proces s Descriptio n Mixin g Room# 1 an d# 2 Th e mixin g roo mproces s i s abatc hoperatio nfo r th e combinatio no

f th e ra w materials , resins , monomers , fillers, an dadditive s tha t become th e polyeste r

resi nmi x use do nth e lon g pane l productio nlines . Th e mixin g operation s ar e compute r controlle dwit h100 % . redundanc y for

manua l operation , i f

necessary . Ther e ar e thre e separat e set s o f batc h equipment , on e se t

for eac hproductio nline . Producin g mi x fo r eac hlin e i s independen t of th e activit y of

th e othe r

system s withi nth e constraint s of share dsuppl y of

ra w materials . Eac ho f

th e thre e system s operat e o nth e sam e schedul e o f operatin g hour s of th e lon g pane l lin e fo r

whic hi t i s supplyin g resi nmix . Th e mixin g proces s consist s of successiv e iteration s o

f thre e basi c step s repeate dfor th e lengt ho f th e productio nru no nth e lon g pane l line . I nth e first ste p th e bul k

ingredients , resins , monomers , an dfiller ar e weighe di nth e weig htanks . Next , thes e ar e charge dt o amixin g tan k

an dagitate dunti l homogenous . Othe r mino r component s ma y b e adde da t thi s time . Whe nth e mixin g cycle i s complete , th e resi nmi x i s transferre dt o th e fee d tan k tha t i s supplyin g th e lon g pane l lin e wit hacontinuou s sourc e of polyeste r resi n mix . Resi nmi x i s formulate di ndiscret e batc hamount s tha t ar e blende dwit hth e previou s an dsuccessiv e batche s t o simulat e acontinuous flow of materia l t o th e pane l line . Th e weight s of

ever y ingredien t

ar e recorde dfo

r eac hdiscret e batch . Th e recor dals o include s th e identificatio nof th e mi x type, date , time , monomer percentage , an dth e VO M emission s create dfor

tha t batc hactivity .

Applicatio nPag e 1,1-i

l* sP.1 7



# m ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O
. BO X 1950 6 SPRINGFIELD , ILLINOI S 62794-950 6 FO R APPLICANT S US E Revisio n # : J > Date : _Septembe r15,199 5 Pag e o f Sourc e Designation : Kemlit e Jolie t
PROCESS

EMISSION

UNIT DATA AND

INFORMATION EMI55I0 N POIN T# : •BATE T
^SOURC E NAME : Cran e Kemlit e 2 ) DAT E FOR M SOURCE INFORMATION
PREPARED*
. Novembe r30,199 5 3 ) SOURC E I D NO
. An -, ann „ AX , (I F KNOWN) : 197800AA X 4) NAM E O P EMISSIO N UNIT : Mixin g Roo m # 1 an d 5 ) NAM E O P PROCESS : Mi xRoo m # 1 an d # 2 GENERALINFORMATION # 2 6 ) DESCRIPTIO N O F PROCESS : Ra w materia l batchin g an d mixin g 7) DESCRIPTIO N O F ITE M O R MATERIA L PRODUCE D O R ACTIVIT YACCOMPUSHED : Polyeste rresi n mi xprepare d an d pumpe d to Lon g Pane l proces s line s 6 ) FLO W DIAGRA

M DESIGNATIO

N 6 F EMISSIONUNIT

: 5 ) FLO WDIAGRA M DESIGNATIO N O F EMISSIO N Mi xroo m # 1 an d # 2 § , MANUFACTURE R O F EMISSIO N UNI T(I F KNOWN) : N A 10 ) MODE L NUMBE R (I F KNOWN) : N A 1 2 DATE S O F COMMENCIN G CONSTRUCTION
. OPERATIO N AND/O R MOS TRECEN TMODIFICATIO N O F THI S EMISSIO N UNI T(ACTUA L O R PLANNED )
ii) DESCRIPTIO N O F MODIFICATIO N (I F APPLICABLE) : ii) SERIA L NUMBE R (I F KNOWN) : N A a) CONSTRUCTIO N (MONTHA/EAR) : N A b ) OPERATIO N (MONTVWEAR) : (#1)05/8 0 (#2 ) 05/8 5 c) LATES TMODIFICATIO N (MONTH/VEAR) : non e

THI S AGENC

YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R ILLINOI S REVISE D STATUES
. 1991
. A S AMENDE D 1992
. CHA P 11 1 1/2 , PAR
. 1039.5
. DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION
. FAILUR E T O DO S O MA Y PREVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPLICATIO N BEJN G DENIED
. THI S FOR M HA S BEE N APPROVE D B YTH E FORM S MANAGEMENTCENTER
.

APPLICATIO N PAGE . 220-CAAP P 1.1- 1 PAG E 1 O F 1 0 

# WnP.1 8

14) DOE S TH E EMISSIO N UNI THAV E MOR E THA N ON E MOD E O F OPERATION ? I F YES , EXPLAI N AN D IDENTIF YWHIC H MOD E I S COVERE D B YTHI S FOR M (NOTE : A SEPARAT E PROCES S EMISSIO N UNI TFOR M 220-CAAP P MUS TB E COMPLETE D FO R EAC H MODE) : JYE S

15 ) PROVID E TH E NAM E AN D DESIGNATIO N O P AL L AI R POLLUTIO N CONTRO L EQUIPMEN TCONTROLLIN G THI S EMISSIO N UNIT , I F APPUCABL E (FOR M 260-CAAP P AN D TH E APPROPRIAT E 260-CAAP P ADDENDU M FOR M MUS TB E COMPLETE D FO R EAC H ITE M O F AI R POLLUTIO N CONTRO L EQUIPMENT) : 

### bi n filters : FDV-701 ; FDV-702 ; FDV-20 1 16 ) WIL L EMISSION S DURIN G STARTU P EXCEE D EITHE R TH E ALLOWABL E EMISSIO N T OK „ RAT E PURSUAN TT O A SPECIFI C RULE . O R TH E ALLOWABL E EMISSIO N LIMI TA S YE S ESTABUSHE D B YA N EXISTIN G O R PROPOSE D PERMI TCONDITION ? I F YES , COMPLET E AN D ATTAC H FOR M 203-CAAPP , "REQUES TT O OPERAT E WIT H EXCES S EMISSION S DURIN G STARTU P O F EQUIPMENT . 1? ) PROVID E AN V LIMITATION S O N SOURC E OPERATIO N AFFECTIN G EMISSION S O R AN YWOR K PRACTIC E STANDARD S (E.G. . ONL YON E UNI TI S OPERATE D A TA TIME) : 

### Maximu m annua l materia l usag e limit s fo r (unit s i n TPY ) Polyeste r resin , 38318 ; Styrene , 5962 ; Methy l Methacrylate , 1721 . Maximu m annua l outpu t ofpolyeste r resi n mix , 72000 . OPERATING INFORMATION 1fl ) ATTAC H TH E CALCULATIONS . T O TH E EXTEN TTHE V AR E AI R EMISSIO N RELATED . FRO M WHIC H TH E FOLLOWIN G OPERATIN G INFORMATION . MATERIA L USAG E INFORMATIO N AN D FUE L USAG E DAT A WER E BASED AN D LABE L A S EXHIBI T220-1 . REFE R T O SPECIA L NOTE S O F FOR M 202-CAAPP . X X NO

19a ) MAXIMU M OPERATIN G HOUR S 

### 750 0 b ) TYPICA L OPERATIN G HOUR S 

### 624 0 Sfl ) ANNUA L THROUGHPU T HOURS/DAY : 

### 2 4 DAV5M1EEK :



### 6 WEEK5WEAR :



### 5 2 HOURS/DAY : 

### 2 4 DEC-FEBM : 

## 2 5 BAYS/WEEK : WEEKS/YEAR : 

### 5 2 MAR-MAYM : 2 5 JUN-AUG(ft) :



### 2 5 SEP-NOV(%) :



### 2 5 MATERIALUSAGE

INFORMATION

21a ) RA WMATERIAL S 

### Polyeste r Resi n Stvren e monome r Methv l methacrylat e Calciu m Carbonat e Alumin a Trihydrat e * se e exhibi t 22 0 - 1 LBS/H R MAXIMU M RATE S



### TON5/VEA R 

### 3831 8 

## 596 2 172 1 1900 0 700 0 TYPICA L RATE S LB5/H R 

## 2049 2

TONS/YEA R 

### 302 4 

## 73 6 707 3 

## 80 2

APPLICATIO N PAG E 11- 2

220-CAAP P PAG E 2 O F 1 0



# inP.1 9

21b ) PRODUCT

S 

## polyeste r resi n mi

x

* tota l suppl

y rat e to lon g pane l line

s LP-3 , LP-6 , LP-

7

2 1 c ) BY-PRODUC

TMATERIAL

S 

## N A MAXIMU M RATE S LBS/H R 

### 1920 0 * TONS/YEA R



## 7200 0

MAXIMU M RATE S LBS/H R 

## N A TONS/YEA R



## N A TYPICA L RATE S LBS/H R 

## 694 3 * TONS/YEA R



## 2166 2

TYPICA L RATE S LBS/H R 

## N A TONS/YEA R



## N A

FUELUSAGE

DATA lit,) MAXIMU M FIRIN G RATE (MILLIO N BTU/HR) : 

# "W TOEnTPE : b ) TYPICA L FIRIN G RAT E (MILUO N BTU/HR) : c) DESIG N CAPACIT YFIRIN G RAT E (MILUO N BTU/HR) : 

### N A
Q ] NATURA L GA

S QFUE L OIL : GRAD E NUMBE R j_JcOA L [_JoTHE R I F MOR E THA N ON E FUE L I S USED , ATTAC H A N EXPLANATIO N AN D LABE L A S EXHIBI T220- 2 •e j TYPICA L HEA

TCONTEN TO F FUE L (BTU/LB . BTU/GA L O R BTU/SCF) : g ) TYPICA L AS H CONTEN T(WTK..KI A FO R NATURA L GAS) : T J TYPICA L SULFU R CONTEN T(W T%.. N AFO R NATURAL GAS) : h ) ANNUA L FUE L USAG E (SPECIF YUNITS . E.G. . SCF/YEAR . GAL/YEAR , TON/YEAR) : li) AR E COMBUSTIO N EMISSION S DUCTE D T O TH E SAM E STAC KO R CONTRO L A S PROCESS UNI TEMISSIONS ? I F NO . IDENTIF

YTH E EXHAUS

TPOIN TFO R COMBUSTIO N EMISSIONS : YE S N

O



### APPLICATIO N PAGE 1 

### - 1 

### ' 3

220-CAAPP 

# If. PAG E 3 O F 1 0.nrrvjw-.^y.w.. . _»%« »

24) PROVID E AN

V SPECIFI C EMISSIO N STANDARD^ ) AN D UMITATION(S) SETB YRULE(S) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T(E.G. , VOM , IA C 2l8.204(j)(4) . 3. 5 LBS/GAL) : REGULATE D AI R POLLUTANT(S ) EMISSIO N STANDARD'S ) REQUIREMENTS ) 

## VO M 218.666(c )

~25 ) PROVID E AN YSPECIFI C RECORDKEEPIN G RULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T REGULATE D AI R POLLUTANT(S ) RECORDKEEPIN G RULE(S ) 

## VO M 218.672(c)(2 )

~5B ) PROVID E ANYSPECIFI C REPORTIN G RULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT : REGULATE D AI R POLLUTANT(S) REPORTIN G RULE(S )



### 1 7 

## VO M
) PROVID E AN YSPECIFI C MONITORIN G RULE( S

REGULATE D A KPOLLUTANT(S ) 

## non e |W I 

## IAC 201.302(a ) j
•IIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

MONITORIN G RULE(S ) : 

## wor k practice s

REQUIREMENTS ) 

## inspectio n lo g (covere d i n maint
. log )

REQUIREMENT(S ) 

## Annua l Emission s Repor t

REQUIREMENT(S )

~2B ) PROVID E ANYSPECIFI C TESTIN G RULES AND/O R PROCEDURE S WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POLLUTANT(S) TESTIN G RULE(S ) REQUIREMENT(S ) 

## non e
\


## APPUCATIO N PAGE . 220-CAAP P 

## 1.1-4 PAG E 4 O F 1 0P.2 1

25 ) DOE S TH E EMISSIO N UNI TQUALIF YFO R A N EXEMPTIO N FRO M A N OTHERWIS E APPLICABL E RULE ? YE S XX . N O I F YES . THE N LIS TBOT H TH E RUL E FRO M WHIC H I TI S EXEMP TAN D TH E RUL E WHIC H ALLOW S TH E EXEMPTION . PROVID E A DETAILE D EXPLANATIO N JUSTIFYIN G TH E EXEMPTION . INCLUD E DETAILED SUPPORTIN G DATA AN D CALCULATIONS . ATTAC H AN D LABE L A S EXHIBI T220-3 . O R REFE R T O OTHE R ATTACHMENT(S ) WHIC H ADDRES S AN D JUSTIF YTHI S EXEMPTION . COMPUANCE INFORMATION 30) I S TH E EMISSIO N UNI TI N COMPLIANC E W l f H AL L APPLICABL E REQUIREMENTS ? X X YE S N O I F NO . THE N FOR M 294-CAAP P "COMPLIANC E PLAN/SCHEDUL E O F COMPLIANC E - ADDENDU M FO R NO N COMPLYIN G EMISSIO N UNITS " MUS TB E COMPLETE D AN D SUBMITTE D WIT H THI S APPUCATION . 31 ) EXPLANATIO N O F HO WINITIA L COMPLIANC E I S T O BE
. O R WA S PREVIOUSLY
. DEMONSTRATED : 

### Calculatio n o femission s metho d approve d by IEPA . (se e exhibi t 22 0 -5 ) Implemente d wor k

practic e standard s o fIA C 218.666(c) .

il) EXPLANATIO N O F HO

WONGOIN G COMPLIANC E WIL L B E DEMONSTRATED : 

### Us e approve d metho d t o calculate emission s o fVOM , an d kee p appropriat e record s o fth e results o fthes e calculations . Followin g wor k

practic e standard s ofIA C 218.666(c) .

TESTING, MONITORING, RECORDKEEPING aAND REPORTING" 33a LISTTH E PARAMETER S THA TRELAT E T O AI R EMISSION S FO R WHIC H RECORD S AR E BEIN G MAINTAINE D T O DETERMIN E FEES , RUL E APPUCABIUT YO R COMPLIANCE . INCLUD E TH E UNI TO F MEASUREMENT , TH E METHO t O F MEASUREMENT , AN D TH E FREQUENC YO F SUC H RECORD S (E.G. . HOURLY . DAILY . WEEKLY) : PARAMETE R materia l usag e 

### Tan k lid s emission s UNI TO F MEASUREMEN T METHO D O F MEASUREMEN T 

## lbs . NA 

## lbs . mi xrepor t visua l inspectio n compute rcalc . FREQUENC Y 

### dail y weekl y 

## monthl y

APPLICATIO N PAG E 1 

### ' 1 

### ' 5

220-CAAP P FO R APPLICANT S US E
PAG E 5 O F 1 0 

# 3dP.2 2

T3B ) BRIEFL

YDESCRIB E TH E METHO D B V WHIC H RECORD S WIL L B E CREATE D AN D MAINTAINED . FO R EAC H RECORDE D PARAMETE R INCLUD E TH E METHO D O F RECORDKEEPING . TITL E O F PERSO N RESPONSIBL E FO R RECORDKEEPING . AN D TITL E O F PERSO N T O CONTAC TFO R REVIE WO F RECORDS : PARAMETE R materia l usag e 

### emission s tan k lid s METHO D O F RECORDKEEPIN G 

### mi xreport s compute rcal c 

### inspectio n lo g TITL E O F PERSO N RESPONSIBL E TITL E O F CONTAC TPERSO N 

### mixsuperviso r mi xsuperviso r mi xsuperviso r Env./Safet yEng . Envi/Safet yEng . Env./Safet yEng .

c ) I S COMPLIANC E O F TH E EMISSIO N UNI TREADIL YDEMONSTRATE D B

V REVIE WO F TH E RECORDS ? I F NO , EXPLAIN : XX YE S N O

d ) AR E A U RECORD S READIL YAVAILABL E FO R INSPECTION . COPYIN G AN D SUBMITTA L T O TH E AGENC YUPO N REQUEST ? I F NO , EXPLAIN : X XYE S N O

34a ) DESCRIB E AN V MONITOR S O R MONITORIN G ACTIVITIE S USE D T O DETERMIN E FEES . RUL E APPUCABIUT V O R COMPLIANCE : ... .



### N/ A

T J WHATPARAMETER ® IS(ARE ) BEIN G MONITORE D (E.G. . VO M EMISSION S T O ATMOSPHERE) ? 

### N/ A

c ) DESCRIB E TH E LOCATIO N O F EAC H MONITO R (E.G. , I N STAC KMONITO R 3 FEE TFRO M EXIT) :



### N/ A

APPLICATIO N PAGE .

220-CAAP P 

### 1.1- 6 PAG E 6 O F 1 0



# J3IP.2 3

34d ) I S EAC H MONITO R EQUIPPE D WIT H A RECORDIN G DEVICE ? I F NO , US TAL L MONITOR S WITHOU TA RECORDIN G DEVICE : 

## NA YE S N

O

e ) I S EACH-MONITO R REVIEWE D FO R ACCURAC YO N A TLEAS TA QUARTERL YBASIS ? I F NO , EXPLAIN : 

## NA YE S 

### N

O

TJ I S EAC H MONITO R OPERATE D A TAL L TIME S TH E ASSOCIATE D EMISSIO N UNI T I S I N OPERATION ? I F NO , EXPLAIN : 

## NA YE S N

O

3 5 PROVID E INFORMATIO N O N TH E MOS TRECEN TTESTS , I F ANV. I N WHIC H TH E RESULT S AR E USE D FO R PURPOSE S O F TH E DETERMINATIO N O F FEES . RUL E APPLICABILIT YO R COMPLIANCE . INCLUD E TH E TESTDATE TES TMETHO D USED , TESTIN G COMPANY. OPERATIN G CONDITION S EXISTIN G DURIN G TH E TES TAN D A SUMMAR

YO F RESULTS . I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T220-4 : TES TDAT E TES TMETHO D 

## none TESTIN G COMPAN Y OPERATIN G

CONDITION S SUMMAR YO F RESULT

S

36 ) DESCRIB E AL L REPORTIN G REQUIREMENT S AND PROVID E TH E TITL E AN D FREQUENC YO F REPOR T SUBMITTALS T O TH E AGENCY : REPORTIN G REQUIREMENT S TITL E O F REPOR T FREQUENC Y 

## materia l usag e VO M emission s Name , ID#
. VO M conten t Mi xrepor t Annua l Emission s repor

t 

## Mi xrepor t annua l

annua l annua l

APPLICATIO N PAG E

220-CAAP P 

## 1.1-

7 PAG E 7 O F 1 0 

# 33REGULATE D AI R

POUUTAN T CARBO N MONOXID E (CO ) LEA D
NITROGE N OXIDE S (NOx ) PARTICULAT E MATTE R (PART ) PARTICULAT E MATTE R <-1 0 MICROMETER S (PM10 ) SULFU R DIOXID E (SOZ ) VOLATIL E ORGANI C MATERIA L (VOM ) OTHER , SPECIFY :

EXAMPLE: PARTICULAT E MATTE R MAXMUM : TYPICAL : MAXIMUM TYPICAL : MAXMUM : TYPICAL : MlMflMUM t TYPICAL : MAXIMUM : TYPICAL : MAXMUM : TYPICAL : MAXMUM E TYPICAL : MftXmUM " TYPICAL :
MAXMUU : TYPCA L • till-EMISSIM 2 L * ACTUA L E

W 'UNCONTRO I HOU R (LBSfHR )

- -



### 1. 5 .549 4

5.0 0 4.00 lUNSPt K

YEAR (TONS/YR .



### 5. 6 1.71 4

21 9 14.4 SSIO N RAT E

.LE O EMISSIO N RATE •-OTHE R TERM S ! ' :

1

GFVDSCF 0.24 GfVOSCF MOTHE R

TERM S «D M



### 4 4 .

i 4 

## m MMUN0 M

ALLOWABL E B YRUL E EMISSIO N RAT E
S RAT E (UNITS)

a.OILBS/HR) 5.5 (LBSMR) APPLICABL E RULES

212.321 212.321 YEA R (TONS/VR)

26.2 8 19.80 'PERMITTE O EMISSIO N RAT E

RATE (UNITS)



### 1.5lbs./hr .

S.5 LBSMR ION S PfcH YEAR (TONS/YR)



### 5. 6

2 2
IMPORTANT : AnACHCAIXUUTIt_Wt % TO'TH E EXTENT"fflE V AR E AI R __WSS_ON

S RELATES , M JcHEC KUNCONTROLLE D EMISSIO N RAT E BO XI F CONTRO L EQUIPMEN Tt S USED . OTHERWIS E CHEC KAN O PROVID E TH E ACTUAL EMISSIO N RATE T O ATMOSPHERE . INCLUDIN G INDOORS . SE E INSTRUCTIONS . "-PROVIDE TH E EMISSIO N RAT E THA TWI U B E USE D A

S A PERMITSPECIAL CONDITION . THI S UH_rTWUJ.B E USEO T O DETERMIN E TH E PERMITFE E -VlEAS E PROVID E AN

YOTHE R EMISSIO N RATE WWC H I S COMMONL YUSED . REQUIRE

O B YA SPECIFI C UOTAT10 N OR-DiA TWA S MI*ASURa> (E. & PH^GRTOSCF . CTC.) 4 D M •DETERMINATIO N METHOD : 1 ) STAC KTEST . 2 ) MATERIAL BALANCE. 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) . 4 ) ENGINEERIN G ESTIMATE . S) SPECIAL EMISSIO N FACTO R (NOTAP-4 2 O R AIRS) •fcATE - AUOWABL E EMISSIO N RAT E SPECIFIE D B

YMOS TSTRMGENTAPPUCABLE RULE .



### APPUCATIO N PAGE . 220-CAAP P 

### 1.1- 8 FQ R APPLICANT

S USE
PAG E 8 O F 1 0 

# J

# - T # 

### (38) HAZARDOUS

AIR POLLUTANT

EMISSION

INFORMAT

ON HA P INFORMATIO N
NAM E O F HA P EMITTE D 

### Styren e (STY

) Methy l (MMA

) Methacrylat e

- 

### -EUMPLE: Benzene •-CA S NUMBE R 

### 100-42- 5 

## 80-62- 6

71432 ""ITWICTL " " '

"TOTUMUH F •ITPICAL"' " "'RUUUMDM r

ITHUJAL "

ITHILAL! "

--««•» » "ITWCWT " X 1 

### ACTUA L EMISSIO N RAT E

UNCONTROLLE D EMISSIO N RATE POUND S PE R 1 HOU R (LBS/HR ) 

## 1.5-(MMA ) .343 1 1.5-(STY ) .206 3

i

i

7<5.( 5 

### 4. 6 TON S PE R

YEA R CTONS/YR

) 

## 5. 6 - (MMA

) 1.0 7 5. 6 - (STY) .643 4

•



### 1.2 " " o i 30THE R

TERM S *D M



## 4 4 4 4

2 

### I ALLOWABL E B Y RUL E

^ T E O R STANDAR D

98%by wt control device leak-tight

trucks APPLICABL E RUL E



### CPRM 61.302(b).(d) IMPORTANT : ATTAC H CALCULATIONS , T O TH E EXTENTTHEYAR E AI R EMISSION S RELATED , O N WHIC H EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T220-6 . ' PROVID E UNCONTROLLE D EMISSION S I F CONTRO L EQUIPMENTI S USED . OTHERWISE . PROVID E ACTUA L EMISSION S T O TH E ATMOSPHERE . INCLUDIN G INDOORS . CHEC K80 XT O SPECIFY . tCAS-CHEMICA L ABSTRAC TSERVIC E NUMBER . TLEAS E PROVID E ANYOTHE R EMISSIO N RATE WHIC H I S COMMONL YUSED . REQUIRE D B

YASPECIFI C LMfTATIO N O R THA TWA S MEASURE D (E.G. . PPM . GR/DSCF . ETC.) . T) M - DETERMINATIO N METHOD : 1 ) STAC KTEST . 2 ) MATERIAL BALANCE . 3 ) STANDAR D EMISSIO N FACTO R (AP-42 O R AIRS . 4 ) ENGINEERIN G ESTIMATE . S) SPECIA L EMISSIO N FACTO R (NOTAP-4 2 O R AIRS) . --RAT E - AUOWABL E EMISSIO N RATE O R STANDAR D SPECIFIE D B YMOS TSTRINGEN TAPPLICABL E RULE . 

## APPLICATIO N PAGE .

1.1-9

rOP.2 6

EXHAUST

POINT INFORMATION THI 5 SECTION SHOUL

D NO TB E COMPLETE D I F EMISSIONS AR E EXHAUSTE D THROUO H AI R POLLUTION CONTRO

L EQUIPMENT

. ii.) PLOWDIAGRA M 0E5I5NATIO N O F EXHAUS TPOINT : 

## mix#1 : NV-1.NV-2 . NV-19 . NV-20 : mix#2:NDV-4andNDV- 5 Ad) PE5CRIPTIO N O F EXHAUS TPOIN T(STACK
. VENT
. ROO F MONITOR , INPOOR5 , ETC.)
. I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS , D O NO TCOMPLET E TH E REMAININ G ITEMS
. 

## vent Ai) PISTANC E T O NEARES TPLAN TBOUNPAR V FRO M EXHAUS TPOIN TDISCHARG E (FT) : 

## NV-1 . NV-2 . NV-19 . NV-20 : 8 0 ft. Al) DISCHARG E HEIGH TABOV E GRAD E (FT) : 

## 43 ) J^kM^ftRfci&T^tff i r\\Wtt, I F KNOW N (FT") : NV-4 . NV-5 :20 0 ft . IV- 4 NIV.fi-9 8 ft 44 ) PIAMETE R O F EXHAUSTPOIN T(FT) : NOTE : FO R ANO N CIRCULA R EXHAUS TPOINT
. TH E PIAMETE R I S 1.128 TIME S TH E SQUAR E ROOTO F TH E ARE An 4S ) EXI TGAS FLO

WRAT E N / A (natura l vents ) 46 ) EXI TOAS TEMPERATUR E 

## ambient a ) MAXIMU M (ACFM) : a ) MAXIMU M fF) : b)TVPICAL(ACFM) : b ) TYPICA L (*F) : IT) DIRECTIO N O F EXHAU5 T(VERTICAL , LATERAL , DOWNWARD,: — 

## latera l 46 ) US TAL L EMISSIO N UNIT S AN P CONTRO L DEVICE S SERVE P B V THI S EXHAUS TPOINT : NAM E FLO WDIAGRA M DESIGNATIO N 

## a T * T 

## Mi x# 2 we t weig h tan k Mix# 2 Mixan d fee d tank s 

## T Mix# 1 we

t weig h tank

s 

# w Mix# 1 Mixan d fee d tank s 

## "S T Mix # 1 Mi x tan k tank2 C toNDV- 5 tank s 3C ; 4C ; 5 C to NDV-4 tan k 2 to NV-20 ; tan k

4 to NV-1 9 tank s 5,6,7, 8 to NV- 1 tan k 9 to NV- 2 TH E FOLLOWINC INFORMATION NEE D ONL V B E SUPPLIE D I F READIL

YAVAILABLE
. 4§a } LATITUDE : 

## 4 1 - 2 7 - 4 5 5fl ) UT M ZONE : ~ b ) UT M VERTICA L b ) LONGITUDE : 

### 88-11-1 5

c ) UT M HORIZONTA L (KM) :



### APPLICATIO N PAGE 1/M 0 220-CAAP P PAG E 1 0 O F 1 0



# •2 5P.2 7



### 197800AA X Cran e Kemlit e 

## Exhibi t220- 1 Mixin g Room s Usag e Mix roo musag e i s create di nth e Kemlit e Mix Report i nth e manufacturin g compute r system . Eac hbatc ho ncompletio ncreate s arecor di nth e repor t tha t include s th e date , time , mi x type , individua l weigh t o f al l ingredients , tota l batc h weight , monome r

percen t o f mix , an demission s create dfromtha t batch . Thes e record s ca nb e sorte dfor individua l batche s i non e day , o r a s asummar y fo

r multipl e date s (ie . month , year) . Dat afor th e for m22 0 typica l operatin g informatio nan dmateria l usag e informatio nwer e 199 4 actua l totals . Actua l maximu musag e i nlbsVhr . ma y excee dsuppl y rat e t o lin e pe r hou r ( ie. : mi x roo m usag e i s batc hprocess ; lin e i s continou s process ) an dshoul dno t b e apermi t condition . Th e maximu musag e i nTon s Pe r Year i s propose dt o b e apermi t condition . Exhibi t 220- 1 (p . 1.1.1-2) attache di s a nexampl e o f th e Kemlit e Mi x Report .

Applicatio n Pag e 1.1.1- 1 

# ao>

### Exhibi t 220- 1

3 1 

### § * * *

•* > ** S Q n 8 i t H « - j h M ri r-

i WW M c i rt 8 R 8 t 8 8 R

oooooo o

ooooo o
C B tf O C

O C D C D O l "*

• 

## si s

Kh N N N N (N t "J J 

### 888888 8 8 060606 6 8 8 8 8 8 8 8 bo o bc

i o o 

### 8 88888 8 o 6 e e be b 8 8 8 8 8 8 8 066066 6 S i 888888 8 1 606600 6 

## s i i aR

## s ; 5 5 s R

« 8

—a, 1 0 IM N P

J N N N t

M

OOOOOO O 

# f i v••vv• « * n 

### i UKU U



## - I I g i 2 S s s g » g 8 8

8

9a o 6 OOOO - 

## » i

- 1 OOO O OaaOaalfllHinfln



# 8i£18§ s

oooooooo o

OOOOOOOO O
CDOODOtBOttiBC O 

### 88888888 8 dddddddd d 

### 88888888 8 88888888 8 ddddddd d 

### K B

K l R£ I



## - fi I
« 8 8 - 3 

# « 1 S S 

# m 

# i

I oooooo o 

### E !

w l OOOOOO O 

## 1 ; M l oooooo o 

# ^iiiiiii i i J 9 * * RK8 ^ S . 8 8 & c S 8 8 i O j O • 3

i n 

### 88888888 8 bbbbbbbb b 

### 88888888 8 dddddddd d R-5*3RRn*3R R 60666060 6

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K I O I

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### 88£8888888 8 K-^noo o 6666 0 

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### 8888888888 8 8 8 dddodddddd d W i



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8 8 o j 6 8 8

8888888888 8 dddddddddd d



### 8 

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# « i 8888888888 8

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### 8888888888 8 6666666666 6 R<823S888S3 8 dddriririritiririri 

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s s o - f . r» . •» n i 3 3 8 8 8 8 6 6 

### 8 8 5 8 ft 

# 5 8 s !

!



## s a 

# i i °Sii 5 - » • • U-R B C RS. RI

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# uui

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ooooo o 8 8 8 88 8 8 0 d d d d d d 8 8 8 8 8 8 8 d d d o d o d 888888 8 o ^ivitiS ^ o 8 8 8 8 8 8 8 d d d d d d d 8 8 8 8 88 8 d d d d o o d

ra .a ra m **_* « • * ooo o oC S o K i K i Ki K i K i Kl Ki 

### SE8U U wiw vi» W w W M W W W rt rt rtl

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1 IIRSSBKR* : r ! 8 5 S S S 5 8 Applicatio n Pag e 1.1.1- 2 

# 5 PP.2 9



### 197800AA X Crane Kemlit

e 

## Exhibi t220- 5 & 6 Mixin g RoomEmission s calculation s Mi x roo memission s ar e base do nth e vapo r displacemen t

of ai r i nth e tank s a s th e VOM containin g material s ar e introduce dint o them . Raoult' s Law an dAntoine' s Equation , an dth e Idea l Ga s La w ar e used . Emissio ncalculation s ar e base do nth e following assumptions : 1 . Styren e monomer

an dmethy l methacrylat e ar e th e onl y material s presen t i nresi nmi x emissions . 2 . Styren e monome r

an dmethy l methacrylat e ar e th e onl y polyeste r resi n mixtur e constituent s wit happreciabl e partia l pressures . 3 . Partia l pressur e an dmonome r mole s ar e directl y proportiona l t o VOM emissions . 4 . Temperatur e i s average dt o 20 ° C . fo r us e i ncalculations . 5 . Monomer

percen t of resin s receive dfromsuppUer s ar e base do ntes t certificate s o

f analysi s fromth e supplier . Th e monome r

percen t i nvendo r

supplie dresin s ar e state do nth e certificat e of analysi s whe nashipmen t i s receive dfromth e supplier . Thi s dat ai s inpu t t o a tabl e i nth e compute r

syste mtha t

make s th e emission s calculation . O neac h subsequen t

delivery , th e tabl e i s updated . Thi s tabl e provide s value s t o detennin e th e amoun t

of monomer i neac hmix . Othe r

value s use dt o calculat e emission s ar e include di nth e formulation s (recipe ) dat abas e use dt o mak e batches , o r ar e result s recorde dfromth e weighin g transaction s o f th e batchin g process . Th e remainde r

of th e value s ar e derive da s outline dbelow . Followin g ar e th e step s use dt o detennin e VO M emission s fo

r aresi nmi x batch : Individua l weigh t

o f ingredient s an dtota l weigh t of mi x i s use dt o determin e tota l weigh t an dpercen t

of monome r components . 1 ) (R

x

## * r x

## ) + CR** r 2 

## ) + (R, , * r n

## ) + Sty ! = St y Where : R j n

## s s Resi ningredien t

weigh t (lbs. ) r 

## i..j » - percen t

styren e monome r

i nresi na s supplie d Sty ! s Styren e ingredien t weigh t a s acomponent

(lbs. ) St y = Tota l weigh t

o f al l styren e i nmi x (lbs. )
Applicatio n Pag e 1.1.2- 1 

# 39.P.3 0



## 197800AA X Cran e Kemlit e Exhibi t

220- 5 & 6 2 ) (R

x

## * r t 

## ) + (R

2 * r 2 

## ) + (R* *r B 

## ) + MMA X

## = MM A Where : Ri...n = Resi ningredien t

weigh t (lbs. ) r 

## i.._ n = 

## percen t

MM A monomer

i nresi na s suppUe d MMA X

## = MM A ingredien t

weigh t a s acomponen t

(lbs. ) MMA = Tota l weigh t

o f al l MM A i nmi x (lbs. ) 3 ) TotL = R-- ^ + St y + MM A Where : Ri...n ~ toteA resi ningredien t weight s (lbs. ) St y = tota l styren e weigh t (lbs. ) MMA = tota l MMA weigh t (lbs. ) Tot t = Tota l Uqui dweigh t

(lbs. ) 4a. ) Th e volum e of

ai r displace di nweig htan k

i s calculate dusin g thes e constants : specifi c gravit y o f

Uqui donly = 1.0 8 ( 9 lbs./gal. ) cubi c fee t of ai r pe r gallo n= 7.4 7 V a

## = TotL/9/7.4 7 Where : V a

## = Volum e of

ai r displace d Tot t = Tota l Uqui dweigh t

Obs. ) 4b. ) Th e volum e of

ai r displace di nth e mi x an dfee dtank s i s calculated : V b 

## =-* • Totj , / mix,, , / 7.4 7 Where : V b 

## = Volum e of

ai r displace d Totjj » Tota l mi x weigh t mix a g 

## = Specifi c gravit y conversio n(weigh t pe r gallo nfo r tha t mi x fromth e formulation s dat abase ) 4c. ) V TM = V a

## + V b 

## Where : Vr * = Tota l volum e o

f ai r displace dby th e mi x throug hth e complet e cycl e i nth e mixin g room . AppUcatio nPag e 1.1.2- 2



# MP.3 1

( . 

## 197800AA

X Cran e Kemlit e Exhibi t220- 5 & 6 5. ) Percen t

monomer , moles , an dmol e fractions ar e calculated : S = Sty/Totj j M = MMA/Tot w mole s styren e *

= S / 104.1 4 mole s MM

A =M/100.1 1 mol e fractionstyren e = mole s styren e / (mole s styren e + mole s MMA ) mol e fractionMM

A = mole s MM

A / (mole s styren e + mole s MMA ) Where : S = percen t

styren e i nmi x M = percen t

MM A i nmi x (molecular

weigh t o f styren e = 104.14 ) (molecular

weigh t o f MM A= 100.11 ) 6. ) Partia l pressur e derivatio nusin g Raoult' s Law an dAntoine' s Equation : Raoult' s La w P s 

## = X j * VP t 

## Where : P { 

## = partia l pressur e of component " i " fromresi nmi x ^ = mol e fractiono

f componen t

" i " i nresi nmi x VP i = vapo r

pressur e of

component " i " fromresi nmi x i = styren e o r

methy l methacrylat e Antoine' s Equatio nlog 10 

## VP i = A - B/(C+T) Where : VP j = vapo r

pressur e of

componen t

" i " i nresi nmi x A , B , & C = Constant s fromth e Uteratur e (se e below ) T = 2 0 (fromassumption s above ) 

## Antoine' s Equatio nConstant s A Styren e (C 8 

## H 8 

## ) 6.9240 9 Methy l Methacrylat e (C 5 

## H 8 

## 0 2 

## ) 10.31 1 B 1420. 0 3764. 0 C 20 6

406.45 4 AppUcatio n Pag e 1,1,2- 3 

# mP.3 2



### 197800AA X Cran e Kemlit e 

## Exhibi t220- 5 & 6 7. ) Emissio nof

eac hcomponen t

VO M i s calculate dusin g thes e constants : atmospheri c pressur e = 76 0 mmH g lbs . moles/c.f

. conversio n= .0027 8 E st y 

## = 104.1 4 * .0027 8 * ( P st y 

## / 760 ) * V Tot 

## E ^ = * 100.1 1 * .0027 8 * (?„

_/ 760 ) * V m
Evta a~ -^Sty + Enun a 

## where : P st y 

## = partia l pressur e o f styren e fromresi nmi x P-am a= partia l pressur e o

f methy l methacrylat e fromresi nmi x E sty 

## = Emissio nof

styren e (lbs. ) Emm a= 

## Emissio nof

methy l methacrylat e (lbs. ) e 

## E ^ * = Tota l emission s (lbs. ) Note : Th e 1. 5 lbThr . hourl y an d5. 6 TPY annua l VOM ( HAP) emissio nUmit s ar e propose dpermi t

conditio nlimit s fo

r acombinatio no

f bot hStyren e an dMethy l Methacrylat e monomers . Th e combinatio no f Styren e an dMethy l Methacrylat e emission s wi

U no t excee dth e emissio nlimi t total . Particulat e emissions : Emission s for

th e filter receiver an ddr y weig htan k

filter operations , base d o nth e 99 + % efficienc y o f th e filters use dan dth e close dsyste mof operation , ar e assume dt o b e a t

th e negUgibl e leve l of

. 1 lbVhr . an d.4 4 TP

Y each . Thi s i s th e permi t limitatio nof

th e curren t

IEPA operatin g permit . I t i s als o th e propose d penni t Umitation .

Applicatio n Pag e 1.1.2- 4



# « l

### |09-nov t I 

### Mxv I d 660 0 669 0 Tota l
Mx v I d 330 0 Tota l
Mx v I d 730 0 760 0 797 2 Tota l Exhibit 220-5& 6

-199 5 KEMLIT E 11/07/95 -
Emissio nStyren e 1.852762704 9 • 0.966254541 3 2.819017246 2
Emissio nStyren e 4.215423746 7 • 4.215423746 7 Emissio nStyren e 1.036000000 0 0.476000000 0 0.649000000 0 2.161000000 0 MI XEMISSIO N REPOR T 11:25:0 5 1 •11/07/9 5 | Mi xStationA EmissionMm

a 3.898362564 9 0.009837695 9 3.908200260 8 Mi xStatio nB Emissio nMma 0.063571940 5 0.063571940 5 Mi xStatio nC Emissio nMm

a 0.040000000 0 1.030000000 0 0.817000000 0 1.887000000 0 Emissio nTota l 5.751125269 8 0.976092237 2 6.727217507 0
Emissio nTota l 4.278995687 3 4.278995687 3 Emissio nTota l 1.076000000 0 1.506000000 0 e 

### 1.466000000 0 4.048000000 0 P3 3

,



## Mxv I d Emissio n Styren e Mi x Station s A , B Emissio n Mm a & C 

## Emissio n Tota l 330 0 660 0 669 0 730 0 760 0 797 2 Tota l al l 4.215423746 7

1.852762704 9 0.966254541 3 1.036000000 0 0.476000000 0 0.649000000 0 9.195440993 0 0.063571940 5 3.89836256*4 9 0.009837695 9 0.040000000 0 1.030000000 0 0.817000000 0 5.858772201 3 4.278995687 3 5.751125269 8 0.976092237 2 1.076000000 0 1.506000000 0 1.466000000 0 15.054213194 3

Applicatio n Pag e 1.1.2- 5 

# Jd.P.3 4

ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O . BO X 1950 6 SPRINGFIELD , ILLINOI S 62794-950 6 

### 5J3H3inMUkri4 i Revisio n # : Date : Pag e o f Sourc e Designation : 

## AIR POLLUTION

CONTROL EQUIPMENT DATA AND

INFORMATION CONTRO L EQUIPMENT * TSRTS T THI S FOR M MUS

TB E COMPLETE D FOR EACH AI R POLLUTION CONTROL EQUIPMENT
. COMPLET

k AM B PROVID E THI S EOR M I M ADDITIO N T O TH E APPUCABL E ADDENDU M FOR M 260- A THROUG H 260-K. A SEPARAT E FORM MUS

TB E COMPLETE D FO R EAC H MOD E O F OPERATIO N O F AI R POUUTIO N CONTRO L EQUIPMENTFO R WHIC H A PERMI TI S BEING SOUGHT. SOURCE

INFORMATION 1 ) SOURC E NAME : Cran e Kemlit e 2 ) DAT E FOR M PREPARED : Novembe r 30,199 5 3 SOURC E I D NO . (I F KNOWN)

: 197800AA X GENERALINFORMATION 4 ) NAM E O F AI R POLLUTIO N CONTRO L EQUIPMEN TAND/O R CONTRO L SYSTEM : 

## Receive rFilte r 5 ) FLO W DIAGRA M DESIGNATIO N O F CONTRO L EQUIPMEN TANDJO R CONTRO L SYSTEM : 

## FDV-20 1 6 ) MANUFACTURE R O F CONTRO L EQUIPMEN T(I F KNOWN, : Chicag o Conveyo r 

## 7 ) MODE L NUMBE R(I

F KNOWN) : 58BC1 6 DATE S O F COMMENCIN G CONSTRUCTION
. 9 ) OPERATIO N AND/O R MOS TRECEN TMODIFICATIO N O F THI S EQUIPMEN T(ACTUA L O R PLANNED )

ifl ) BRIEFLYDESCRIB E MODIFICATIO N (I F APPUCABLE) : fl) SERIA L NUMBE R (I F KNOWN) : 

## N/ A a ) CONSTRUCTIO N (MONTWYEAR) : 

## 10/7 9 b ) OPERATIO N (MONTH/YEAR) : 

## 5/80
. c ) LATES TMODIFICATIO N (MONTkWEAR) : 

## non e

HI S AGENC YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R ILLINOI S REVISE D STATUES . 1991 . A S AMENDE D 1992 . :HA P 11 1 1/2 . PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E T O D O S O MA Y 1EVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPUCATIO N BEIN G DENIED . THI S FOR M HA S BEE N 'PROVE D B YTH E FORM S MANAGEMEN TCENTER .

APPLICATIO N PAGE . 260-CAAP P 1.2- 1 FO R APPLICANT S US E
PAG E 1 O F 1 0 

# PAP.3 5

11 ) LI5 TA U EMI55I0 N UNIT S AN D OTHE R CONTRO L EQUIPMEN TDUCTIN G EMISSION S T O THI S CONTRO L EQUIPMENT : NAM E DESIGNATIO N O R COD E NUMBE R 

### Filte r receive r FDV-20 1

il) DOE S TH E CONTRO L EQUIPMEN THAV E MOR E THA N ON E MOD E O F OPERATION ? I F YES . EXPLAI N AN D IDENTIF YWHIC H MOD E I S COVERE D B YTHI S FOR M (NOTE : A SEPARAT E AI R POLLUTIO N CONTRO L EQUIPMEN TFOR M 260-CAAP P MUS TB E COMPLETE D FO R EAC H MODE) : YE S N O

15 ) IDENTIF V AL L ATTACHMENT S T O THI S FOR M REUTE D T O THI S AI R POLLUTIO N CONTRO L EOUIPMENT(E.G. , TECHNICA L DRAWINGS) :



### OPERATING SCHEDULE 14 ) IDENTIF YAN V PERIO D WHE N TH E CONTRO L EQUIPMEN TWIL L NO TB E OPERATIN G DU E T O SCHEDULE D MAINTENANC E AND/O R REPAIR S WHE N TH E FEEDIN G EMISSIO N UNIT(S ) T O THI S CONTRO L EQUIPMEN TIS/AR E II I OPERATION : 

### Non e
T53 J IDENTIF V AN V PERIOD S DURIN G OPERATIO N O F TH E FEEDIN G EMISSIO N UNIT(S ) WHE N TH E CONTRO L EQUIPMEN TIS/AR E NO TUSED : 

### Non e (
b , 1 5 THI 5 CONTRO L EQUIPMEN TI N OPERATIO N A TAL L OTHE R TIME S THATTH E FEEDIN G EMISSIO N UNIT(S ) IS/AR E I N OPERATION ? I F NO . EXPLAI N AN D PROVID E TH E DURATIO N O F TH E CONTRO L EQUIPMEN T DOWNTIME : YE S N O



# r APPLICATIO N PAGE . 260-CAAP P 1.2- 2 PAG E 2 O F 1 0



# 5 V

### APPUCABLE RULES 16 ) PROVID E AN V SPECIFIC EMISSIO N STANDARD^ ) AN D UMITATION(S

) SE TB V RULE(S ) WHICH ARE APPUCABL E T O THIS EMISSION UNI

T(E.G. . VOM . IA

C 21fl.!HW(b)(1)

. 61 % OVERAL L & 90 % CONTRO L DEVIC E EFF.) :

REGULATE D AI R POLLUTANT(S ) EMISSIO N STANDARDS ) REQUIREMENT'S ) Particulat e 

### IA C 212.32 2

71) PROVID E AN YSPECIFI C RECORDKEEPIN G RULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T

REGULATE D AI R POU.UTANT(S ) RECORDKEEPIN G RULE(S )



### i d

"T 8 non e 

### i ) PROVIDE AN

YSPECIFIC REPORTING RULE(5 ) WHICH ARE APPUCABL E T O THIS EMISSIO N UNIT: REGULATE D AI R POLLUTANT(S ) REPORTIN G RULE(S ) Particulat e
) PROVIDE AN

YSPECIFIC MONITORING RDLE( S REGULATE D AI R POLLUTANT(S) 

### non e i



### .Wl IA C 201.302(a )

•IICH AR E APPUCABL

E T O THI S EMISSIO N UNIT : MONITORIN G RULE(S ) 

### N/ A Proces s weigh t rat e limi t fo r existin g source s

REQUIREMENT(S )

REQUIREMENTS ) 

### Annua l Emission s Report

REQUIREMENT(S )

TO ) PROVID E AN YSPECIFI C TESTIN G RULE S AND/O R PROCEDURE S WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POLLUTANT(S ) ' TESTIN G RUUE(S) REQUIREMENTS ) 

### non e N/ A



## APPUCATIO N PAGE . 260-CAAP P 

## 1.2-3 PAG E 3 OF 1 0P.3 7 COMPUANCE

INFORMATION 21 ) I S TH E CONTRO

L SYSTE M I N COMPLIANCE WITH ALL APPUCABL E REQUIREMENTS ? 

# M YE S !N O I F NO . THE N FOR M 294-CAAP P "COMPLIANC E PLAN/SCHEDUL E O F COMPLIANC E - ADDENDU M FO R NO N COMPLYIN G EMISSIO N UNITS " MUS TB E COMPLETE D AN D SUBMITTE D WIT H THI S APPLICATION . li) EXPLANATION O

F HO WINITIA L COMPLIANCE I S T

O BE
. O R WA S PREVIOUSLY

. DEMONSTRATED : 

### Installatio n met manufacturers standar d fo r rate d efficiency o ffilte r uni t

23 ) EXPLANATION O

F HO WONGOIN

G COMPLIANCE WILL BE DEMONSTRATED: 

### Filte r uni t wil l b e kept i n goo d operatin g condition :

TESTING, MONITORING, RECORDKEEPING AND REPORTING 24a ) LIS TTH E PARAMETER S THATRELAT E T O AI R EMISSION S FO R WHIC H RECORD S AR E BEIN G MAINTAINE D T O DETERMIN E FEES , RUL E APPLICABILIT YO R COMPLIANCE . INCLUD E TH E UNI TO F MEASUREMENT , TH E METHO I O F MEASUREMENT . AN D TH E FREQUENC YO F SUC H RECORD S (E.G. , HOURLY , DAILY , WEEKLY) : PARAMETE R UNITO F MEASUREMENTMETHO D O F MEASUREMEN TFREQUENC Y 

### ba g maint . 

## NA

_... 

### maint . lo g semi-annua l

_.. .



## 1.2- 4 APPLICATIO N PAGE . 26 0 - CAAP P PAG E 4 O F 1 0



# 3/ / nP.3 8

24b) BRIEFL

YDESCRIB E TH E METHO D B YWHIC H RECORD S WIL L B E CREATE D AN D MAINTAINED . FO R EAC H RECORDE D PARAMETE R INCLUD E TH E METHO D O F RECORDKEEPING , TITL E O F PERSO N RESPONSIBL E FO R RECORDKEEPING . AN D TITL E O F PERSO N T O CONTAC TFO R REVIE WO F RECORDS : PARAMETE R 

## bag maint . METHO D O F RECORDKEEPIN G 

## maint . log TITLEO F PERSO N RESPONSIBL E 

## Maint . superviso r

c ) I S COMPLIANC E O F TH E CONTRO L EQUIPMEN TREADIL YDEMONSTRATE D B

V REVIE WO F TH E RECORDS ? I F NO . EXPLAIN : TITI E O F CONTAC TPERSO N 

## Env. Eng .

YE S N O

d ) AR E AL L RECORD S READIL YAVAILABL E FO R INSPECTION . COPYIN G ANB.O R SUBMITTA L T O TH E AGENC YUPO N REQUEST ? I F NO , EXPLAIN : XYE S N O

25a . DESCRIB E AN V MONITOR S O R MONITORIN G ACTIVITIE S USE D T O DETERMIN E FEES . RUL E APPUCABIUT V O R COMPLIANCE : 

## N/ A

b ) WHATOPERATIN G PARAMETERS ) I5(ARE ) BEIN G MONITORE D (E.G. , COMBUSTIO N CHAMBE R TEMPERATURE) ? 

## N/ A

c) DESCRIB E TH E LOCATIO N O F EAC H MONITO R (E.G. . EXI TO F COMBUSTIO N CHAMBER) : 

## N/ A

APPLICATIO N PAGE .

26 0 r CAAP P 

## 1.2-

5 PAG E 5 O F 1 0 

# hiP.3 9

25d ) I S EAC H MONITO R EQUIPPE D WIT H ARLCORDIN G DEVICE ? I F NO . LIS TAL L MONITOR S WITHOU TA RECORDIN G DEVICE : N/ A YE S J X JN O

s ) 1 5 EAC H MONITO R REVIEWE D FO R ACCURAC YO N ATLEAS

TAQUARTERL

YBASIS ? I F NO . EXPLAIN : N/ A YE S N O

f, I S EAC H MONITO R OPERATE D ATAL L TIME S TH E CONTRO L EQUIPMEN TI S I N OPERATION ? I F NO , EXPLAIN : N/ A YE S N O

2 6 PROVID E INFORMATIO N O N TH E MOSTRECEN TTESTS
. I F ANY
. I N WHIC H TH E RESULTS AR E USE D FO R
, PURPOSE S O F TH E DETERMINATIO N O F FEES , RUL E APPUCABIUT YO R COMPLIANCE . INCLUD E TH E TES TDAT E TES TMETHO D USED , TESTIN G COMPANY , OPERATIN G CONDITION S EXISTIN G DURIN G TH E TES TAN D A SUMMAR YO F RESULTS . I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T260-1 : TESTDAT E TESTMETHO D



### non e TESTIN G COMPAN Y OPERATIN G

CONDITION S SUMMAR YO F RESULT

S

27 ) DESCRIB E AL L REPORTIN G REQUIREMENTS AN D PROVID E TH E TITL E AN D FREQUENC YO F REPORT SUBMITTAL S T O TH E AGENCY : REPORTIN G REQUIREMENT S TITL E O F REPOR T FREQUENC Y 

### Actua l emission s Annua l emission s repor t 

### Annua l

CAPTURE

AND CONTROL 25 ) DESCRIB E TH E CAPTUR E SYSTE M USE D T O CONTAIN , COLLEC TAN D TRANSPORTEMISSION S T O TH E CONTRO L EQUIPMENT . INCLUD E A U HOODS . DUCTS , FANS , ETC . ALS O INCLUD E TH E METHO D O F CAPTUR E USE D A TEA C H EMISSIO N POINT . (I F ADDITIONA L SPAC E I S NEEDED , ATTAC H AN D LABE L A S EXHIBI T260-2) : 

### Close d tub e conveyin g syste m

APPLICATIO N PAGE . 26 0 - CAAP P 

## 1.2- 6 FO R APPLICANT ? US E
PAG E 6 O F 1 0 

# 2. KP.4 0

25 ) AR E FEATURE S O F TH E CAPTUR E SYSTE M ACCURATELYDEPICTE D I N TH E FLO W DIAGRA M CONTAINE D I N THI S APPLICATION ? I F NO . A SKETC H SHOWIN G TH E FEATURE S O F TH E CAPTUR E SYSTE M SHOUL D B E ATTACHE D AN D LABELE D A S EXHIBI T260-3 : 

## X YE S N O So ) PROVID E TH E ACTUA L MINIMU M AN D TYPICAL^CAPTUR E SYSTE M EFFICIENCY
. CONTRO L EQUIPMEN T DESTRUCTION/REMOVA L EFFICIENCY . AN D TH E OVERAL L REDUCTIO N EFFICIENC YPROVIDE D B YTH E COMBINATIO N O F TH E CAPTUR E SYSTE M AN D CONTRO L EQUIPMEN TFO R EAC H REGULATE D AI R POLLUTAN TT C B E CONTROLLED . ATTAC H TH E CALCULATIONS . T O TH E EXTEN TTHE YAR E AI R EMISSION S REUTED . O N WHIC H THES E EFFICIENCIE S WER E BASE D AN D LABE L A S EXHIBI T260-4 :
• 1 CONTRO L PERFORMANCE :

REGULATE D AI R POLLUTANT CAPTUR E SYSTE M EFFICIENC

Y(% ) 

### •pn j ~~T CONTRO L EQUIPMENT EFFICIENC

Y(% ) 

### —-miIT7PT " OVERAL L REDUCTIO N EFFICIENC

Y{% ) 

## im ITTPJ — Particulat e 

## 10

0 10 0 

## 99 + 99 + 99 + 99 +

EXPLAI N ANYOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMENTPERFORMANC E SUC H A S OUTLE TCONCENTRATION , COOLANTTEMPERATURE . ETC. :

b ) METHO D USE D T O DETERMIN E EAC H O F TH E ABOV E EFFICIENCIE S (E.G.
. STAC KTEST , MATERIA L BALANCE
. MANUFACTURER' S GUARANTEE . ETC. ) AN D TH E DAT E US TTESTED . I F APPLICABLE : EFFICIENC

YDETERMINATIO N METHO D DAT E LAS T TESTE D CAPTURE : CONTRO L OVERAL L 

### mfr . guarante e

mfr . guarante e mfr . guarante e 

# st rl_J»ll|| r dilj_d : a«]:),f,M: W REGULATE D AI R POLLUTANT CAPTUR E CONTRO L SYSTE M EQUIPMEN T EFFICIENC

Y(% ) EFFICIENC

Y(% ) OVERALL REDUCTIO N EFFICIENC

Y <%) APPLICABL E RUL E

EXPLAI N AN YOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMENTPERFORMANC E SUC H A S OUTLE TCONCENTRATION , COOLANTTEMPERATURE . ETC. :



## 1.2-7 APPLICATIO N PAG E 26 0 - CAAP P FO R APPLICANT S US E PAG E 7 O F 1 0 

# * 9REGULATE D AI R

POLLUTAN T CARBO N MONOXID E (CO ) LEA D
NITROGE N OXIDE S (NOx ) PARTICULAT E MATTE R (PART ) PARTICULAT E MATTE R <-1 0 MICROMETER S (PM10 ) SULFUR DIOXID E (S02 ) VOLAYiU S ORGANI C MATERIA L (VOM ) OTHER , SPECIFY : EXAMPLE: PARTICULATE MATTER TYPICAL : MAXMUM : TYPICAL : MAXIMUM : TYPICAL : MAXIMUM : TYPICAL : M/SXMUM : TYPICA L MAXIMUM : TYPICA L HAXMUM : TYPICA L MlTJfJMU M TYPICAL : MAXMUM : TYPICAL : LB

S PER HOU R (LBS/HR )



## 0. 1 0. 1

S.M ~ 

### 4M (3DEMISSIO

1 ACTUA L EMISSIO N RAT E i TON S PER YEAR (TONS/YR

)



### '


## .44 .4 4

"-n.tr - """14:4"' i

'OTHE R TERM S j 

### !

i

GR/DSCF \ 6.14 GR/DSCF 3 OTHE R

TERM S 4 D M



## 4 4

1 4 

# m ^FORMATION

ALLOWABL E B YRUL E EMISSIO N RAT E
5 RAT E (UNITS )



## 10. 4 lb/h r 0. 1

HdlLBsWR) 5.5 (LBSA.Fi) APPUCABL E

RULE S



## 212.32 1 212.32 1

272.32 T 111.511 TON S PE R

YEA R (TONS/YR)



## 3 9 .4 4

26.2 6 19.80 'PERMITTE D EMISSIO N RAT E

RATE (UNITS) TON S PE R YEA R (TONS/YR)



## 0. 1 lb./hr
. .4 4

"'•• ' ' s.SLbSAb

I il

I

IMPORTANT : ATTAC H CALCULATIONS . T O TH E EXTEN T THEY AR E AI REMISSION S RELATED , O N WHIC H EMISSKMI S WER E DETERMINE D AN D LABE L A S EXHIBI T 2604 . ^PROVID E CONTROLLED EMISSION S (E.G. , TH E EMISSION S THA T WOUL D RESUL T AFTE RAL L CONTRO L AN D CAPTUR E EFFICIENCIE S AR E ACCOUNTE D FOR) . 'PROVID E THE EMISSIO N RAT E THA T WIL L B E USE D A S A PERMIT SPECIA L CONDITION . THI S UMI T WU X B E USE D T O DETERMIN E TH E PERMI T FEE . 'PLEAS E PROVID E AN Y OTHE REMISSIO N RAT E WHIC H I S COMMONL Y USED . REQUIRE O B Y A SPECIFI C UMITATION O RTHA T WA S MEASURE D (E.G . PPM , GR/DSCF . ETC. ) *D M - DETERMINATION METHOD : 1 ) STAC KTEST . 2 ) MATERIA L BALANCE . 3 ) STANDAR D EMISSIO N FACTO R(AP-4 2 O RAIRS) . 4 ) ENGINEERIN G ESTIMATE . 5 ) SPECIA L EMISSIO N FACTO R(NO T AP-4 2 O RAIRS ) 5 RAT E • ALLOWABLE EMISSIO N RAT E SPECIFIE D B Y MOS T STRINGEN T APPUCABL E RULE . 

## 1.2- 8 

## £«3%__d9iri&weius r

* •

# •£ : ~ (32) HAZARDOUS

AIR POniTrMrrmiSSlON INFORMATION HA P INFORMATIO N NAM E O F HA P EMITTE D

EXAMPLE: Betuana 2cA S

NUMBE R

71432 1 ACTUA L EMISSIO N RAT E

Twn«o» r POUND S PE R

HOU R (LBS/HR )

10.6 B.6 TON S PE R

YEA R (TONS/YR )

1.2 6.8 30THE R

TERM S ''D M

1 ' 1 ALLOWABL E B YRUL E

-'RAT E O R STANDAR D

98% by wt control device leek-tight

tmcka APPLICABL E

RUL E

&F&61 61.302(b),(d) IMPORTANT : ATTAC H CALCULATIONS , T O TH E EXTEN TTHE YAR E AI R EMISSION S REUTED , O N WHIC H EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T2604 . ^PROVID E CONTROLLE D EMISSION S (E.G „ TH E EMISSION S THA TWOUL D RESUL TAFTE R AL L CONTRO L AN D CAI-mJR E EFFICIENCIE S AR E ACCOUNTE D FOR) . X A S - CHEMICA L ABSTRAC TSERVIC E NUMBER . ^PLEAS E PROVID E AN YOTHE R EMISSIO N RAT E WHIC H I S COMMONL YUSED . REQUIRE D B YA SPECIFI C UMITATIO N O R THA TWA S MEASURE D (E.G. . PPM . GR/DSCF . ETC.) . !D M - DETERMINATIO N METHOD : 1 ) STAC KTEST . 2 ) MATERIA L BALANCE . 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS . 4 ) ENGINEERIN G ESTIMATE , 5 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS) . TFJAT E - ALLOWABL E OMISSIO N RAT E O R STANDAR D SPECIFIE D B YMOS TSTRINGEN TAPPUCABL E RUL E 

### APPUCATIO N PAGE . 260-CAAP P 

### 1.2-9 PAG E 9 O F 1 0

r oP.4 3


## EXHAUST

POINT INFORMATION 33 ) PESCRIPTIO N O F EXHAUS TPOIN T(STACK . VENT . ROO F MONITOR . INDOORS . ETC.. . I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS . D O NO TCOMPLET E TH E REMAINING ITEMS . 

## ven t 34 ) DISTANC E T O NEARES TPLAN TBOUNPAR VFRO M EXHAUS TPOIN TDI5CHARC E (FT) : 

## 6 0 3$ ) DISCHARGE HEIOHT ABOVE CRAPE (FT) : 

## 32 36 ) OOO P ENGINEERIN G PRACTIC E (OEP ) HEIGHT . I F KNOW N (FT) : 37 ) PIAMETE R O F EXHAUS TPOIN T(FT) : NOTE : FO R A NO N CIRCULA R EXHAUS TPOINT , TH E PIAMETE R I S 1.12 8 TIME S TH E SQUAR E ROO TO F TH E AREA . Q g 36 ) EXI TOA S FLO WRAT E a ) MAXIMU M (ACFM) : 

## 40 0 b ) TYPICA L (ACFM) : 

## 40 0 35 ) EXI T OA S TEMPERATUR

E a ) MAXIMU M ('F) :



## ambien t b)TVPICAL('F) : 

## ambien t "TO J DIRECTIO N O F EXHAUS T(VERTICAL . LATERAL . POWNWARP): — 

## Latera l 4 1 ) US TAL L EMISSIO N UNIT S AN P CONTRO L OEVICE S SERVE P B VTHI S EXHAUS TPOINT :

NAM E FLO WDIAGRA M DESIGNATIO N 

### a ) 

## W Filterreceive r

•s r g ) 

## FDV-20 1

"35 5 WHA TPERCENTAC E O F TH E CONTRO L EQUIPMEN TEMISSION S AR E BEIN 5 PUCTE B T O THI S EXHAUS TPOIN T(%) ? 

## 10 0 43 ) I F TH E PERCENTAC E O F TH E CONTRO L EQUIPMEN TEMISSION S BEIN O DUCTE D T O TH E EXHAUS TPOIN TI S NO T 100% . THE N EXPLAI N WHER E TH E REMAININ G EMISSION S AR E BEIN G EXHAUSTE D TO :

TH E FOLLOWING " IHFORMATIO N NEE P ONL V BE SUPPUE D I P READIL

YAVAILABLE. 44a)LATITUPE : 

## 41-27-4 5 45 ) UT M ZONE : b ) LONGITUDE : 

## 88-11-1 5 b ) UT M VERTICA L (KM) : c ) UT M HORIZONTA L (KM) :



## APPLICATIO N PAGE . 260-CAAP P 

## 1.2-1 0 PAG E 1 0 O F 1 0 

# -V AP.4 4
ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O . BOX1950 6 SPRINGFIELD , ILLINOI S 62794-950 6 

### *M:liTa«l«f_j_k*jli M Revisio n # : Date : Pag e , o f Sourc e Designation : 

### SUPPLEMENTALFORM AIR POLLUTION

CONTROL EQUIPMENT FILTER (260C) I D NUMB E CONTRO L EQUIPMENT * T33TO T 

### DATA AND

INFORMATION i) FLOWDIAGRA M DESIGNATIO N O F FILTER : 

## FDV-20 1 2 ) FILTE R CONFIGURATIO N (CHEC KONE) : 

# R OPE N PRESSUR E CLOSE D PRESSUR E • OTHER . SPECIFY : CLOSE D SUCTIO N
3 ) OESCRIB E FILTE R MATERIA L 

### 1 6 oz . Dacro n fel t 4 ) FILTERIN G ARE A (SQUAR E FEET) : 

## 11 7 S ) AI R T O CLOT H RATI O (FEET/MIN) : 

### 3. 4 6 ) CLEANIN G METHO P SHAKE R REVERS E AI R 

# • PULS E AI R 

# • PULS E JE T OTHER . SPECIFY : 7 ) NORMA L RANO E O F PRESSUR E DROP : 2 T 0 6 da) INLE TEMISSIO N STREA M PARAMETERS : (INCHH 2 0 ) MA X TYPICAL MOISTUR E CONTEN T( % B YVOLUME) : PARTICULAT E INLE TLOADIN G (GRAINS/SCF) : 

## N/ A N/

A

b) MEA N PARTICL E PIAMETE R (MICRONS) : 

### 16 8 1.3- 1

APPLICATIO N PAGE .

260C-CAAP P PAG E 1 O F 2



# U*sP.4 5



### § ) FILTE R OPERATIN O PARAMETERS :
INLE TFLO WRAT E (SCFM) : DURIN G MAXMU M OPERATIO N O F FEEDIN G UNIT(S

)

INLE TGA S TEMPERATUR E (DEGREE S FAHRENHEIT) : EFFICIENC Y(P M REDUCTION) : EFFICIENC Y(PM1 0 REDUCTION) : 

## 40 0 N/ A 99 + % 99 + % W

(% ) DURIN G TYPICA L

OPERATIO N O F FEEDIN G UNIT(S ) 

## 40 0 N/ A 99 + % 99 + % W



# m ib) HO W1 5 FILTE R MONITORE D FO R INDICATION S O F DETERIORATIO N (E.G. , BROKE N BAGS) ? CONTINUOU S OPACIT Y PRESSUR E 1 —'DRO P 

# • 0 ALARMS-AUDIBL E T O PROCES S OPERATO R VISUA L OPACIT YREADINGS , FREQUENCY : 

### OTHER , SPECIFY

: v 

## j sua 

## | performanc e chec k i l ) DESCRIB E AN YRECORDIN O DEVIC E AN D FREQUENC YO F LOO ENTRIES : 

## N/ A

tt) DESCRIB E AN YFILTE R 5EEDIN 6 BEIN Q PERFORMED : N / A (



### APPLICATIO N PAG E 13- 2 260C-CAAP P PAG E 2 O F 2



# mP.4 6

ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O . BO X1950 6 SPRINGFIELD , ILLINOI S 62794-950 6 i»kfJJJ*WJ_kikli M Revisio n # : Date : Pag e _ o f Sourc e Designation : 

### AIR POLLUTION

CONTROL EQUIPMENT DATA AND

INFORMATION CONTRO L EQUIPMEN

Tft •RAT E IHIt . POR M MUS

TB E COMPLETE D PO H EAC H AI R POLLUTIO N CONTRO L EQUIPMENT . COMPLET E AN B PROVID E THI S FOR M I H ADDITIO N TO TH E APPUCABL E ADDENDU M FOR M 260- A THROUG H 260-K

. A SEPARAT

E FOR M MUS

TB E COMPLETE D FO R EAC H MOD E O F OPERATIO N O F AI R POUUTIO N CONTRO L EQUIPMENTFO R WHIC H A PERMITI S BEIN G SOUGHT. SOURCE

INFORMATION i) SOURCE NAME : 

### Cran e Kemlit e l) DAT E FOR M PREPARED : 3 ) SOURC E I D NO
. (I F KNOWN) : Novembe r30,199 5 

### 197800AA X

GENERALINFORMATION 4 ) NAM E O F AI R POLLUTION CONTRO L EQUIPMEN

TAND/OR CONTRO

L SYSTEM : 

### Dr yWeig h Tan k

1 AFilte r 5) FLO W DIAGRA

M DESIGNATION O F CONTROL EQUIPMEN TAND/OR CONTRO

L SYSTE M 

## FDV-70 1 6) MANUFACTURE R O F CONTRO L EQUIPMEN

T(I F KNOWN) : 

### Shic k 7) MODE L NUMBE R (I F KNOWN) : 

### 3 6 A- J 3 6 DATES O F COMMENCING CONSTRUCTION
. i) SERIA L NUMBE R (I F KNOWN) : a ) CONSTRUCTIO

N (MONTH/YEAR) : 

### 2/8 5 9 ) OPERATIO N AND/O R MOS TRECEN TMODIFICATIO N O F THI S EQUIPMEN T(ACTUA L O R PLANNED ) b ) OPERATIO

N (MONTH/YEAR) : 

### 5/85
. c ) LATES TMODIFICATION (MONTH/YEAR) : 

### non e Ifl ) BRIEFL

YDESCRIB E MODIFICATION (I F APPUCABLE) :

mi S AGENC YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R lUINOI S REVISE D STATUES , 1991 , A S AMENDE D 1992 , :HA P 1111/2 , PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E T O O O S O MA Y REVENTTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N THE APPLICATIO N BEIN G DENIED . THI S FOR M HA S BEE N 'PROVE D B YTH E FORM S MANAGEMEN TCENTER . 

### 1.4- 1 APPLICATIO N PAGE . 26 0 - CAAP P FO R APPLICANT S US E PAG E 1 O F 1 0 

# H*.P.4 7

i i ) LIS TAL L EMISSIO N UNIT S AN D OTHE R CONTRO L EQUIPMEN TDUCTIN G EMISSION S I O THI S CONTRO L EQUIPMENT : NAM E DESIGNATIO N O R COD E NUMBE R 

### Dr y weig h Tan k

1 A 

## 1 A

i i ) DOE S TH E CONTRO L EQUIPMEN THAV E MOR E THA N ON E MOD E O F OPERATION ? I F YES , EXPLAI N AN D IDENTIF YWHIC H MOD E I S COVERE D B YTHI S FOR M (NOTE : A SEPARAT E AI R POUUTIO N CONTRO L EQUIPMEN TFOR M 260-CAAP P MUS TB E COMPLETE D FO R EAC H MODE) : YE S N O

13 ) IDENTIF V AL L ATTACHMENT S T O THI S FOR M RELATE D T O THI S AI R POLLUTIO N CONTRO L EQU1PMENT(E.6 „ TECHNICA L DRAWINGS) :



### OPERATING SCHEDULE U IDENTIF V AN V PERIO D WHE N TH E CONTRO L EQUIPMEN TWIL L NO TB E OPERATIN G DU E T O SCHEDULE D MAINTENANC E AND/O R REPAIR S WHE N TH E FEEDIN G EMISSIO N UNIT(S ) T O THI S CONTRO L EQUIPMEN TIS/AR E II I OPERATION : 

### Non e
T51 J IDENTIF V AN V PERIOD S DURIN G OPERATIO N O F TH E FEEDIN G EMISSIO N UNIT(S ) WHE N TH E CONTRO L EQUIPMEN TIS/AR E NO TUSED : 

### Non e
b) I S THI S CONTRO L EQUIPMEN TI N OPERATIO N A TAL L OTHE R TIME S THATTH E FEEDIN G EMISSIO N UNIT(S ) IS/AR E I N OPERATION ? I F NO , EXPLAI N AN D PROVID E TH E DURATIO N O F TH E CONTRO L EQUIPMEN T DOWNTIME : YE S N O



### APPLICATIO N PAGE . 260-CAAP P 1.4- 2 PAG E 2 O F 1 0 

## f)

### APPUCABLE RULES i6 ) PROVIP E AMV SPECIFI C EMISSIO N STANDARD ® AN D LIMITATIONS ) SE TBV RULE(5 ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T(E.G. , VOM , IA C 216.207(b)(1) . 61 % OVERAL L & 90 % CONTRO L DEVIC E EFF.) : EMISSIO N STANDARD^ ) REQUIREMENT(S ) REGULATE D AI R POLLUTANT(S) 

## Particulat e IAC 212.32 2 Proces s weigh t rat e Hmi t fo rexistin g source s

17 ) PROVIP E AN V SPECIFI C RECORDKEEPIN G RUU-.(S) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT*.

REGULATE D AI R POUUTANT(S ) RECORDKEEPIN G RULE(S) REQUIREMENTS ) 

## non e

ifl ) PROVID E AN V SPECIFI C REPORTIN G RULE(S) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POLLUTANT(S) 

## Particulat e REPORTIN G RULE(S ) REQUIREMENT(S ) 

### IA C 201.302(a ) Annua l Emission s Repor t

ifl ) PROVID E AN V SPECIFI C MONITORIN G RULE(S) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POLLUTANT'S ) 

## non e MONITORIN G RULE(S) REQUIREMENT(S )

20 ) PROVID E AN V SPECIFI C TESTIN G RULE S AND/O R PROCEOURE S WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POUUTANT(S ) 

## non e TESTIN G RULE(S ) REQUIREMENT^ )



## APPUCATIO N PAGE . 26 0 - CAAP P 

## 1.4- 3 PAG E 3 O F 1 0
o oP.4 9 COMPUANCE

INFORMATION Si ) I S TH E CONTRO L SYSTE M I N COMPLIANC E WIT H AL L APPUCABL E REQUIREMENTS ? 

# i x YE S N O I F NO . THE N FOR M 294-CAAP P "COMPLIANC E PLAN/SCHEDUL E O F COMPLIANC E - ADDENDU M FO R NO N COMPLYIN G EMISSIO N UNITS " MUS TB E COMPLETE D AN D SUBMITTE D WIT H THI S APPUCATION . il) EXPLANATIO N O F HO

WINITIA L COMPLIANC E I S T O BE
. Of t WAS PREVIOUSLY
. DEMONSTRATED : 

### Installatio n me t manufacturers standard fo r rate d efficiency offilte r uni t

23 ) EXPLANATIO N O F HO

WONGOIN G COMPLIANC E WIL L B E DEMONSTRATED : 

### Filte r uni t wil l b e kep t i n goo d operatin g condition .

TESTING, MONITORING, RECORDKEEPING AND REPORTING 24a US TTH E PARAMETER S THA TRELAT E T O AI R EMISSION S FO R WHIC H RECORD S AR E BEIN G MAINTAINE D T O DETERMIN E FEES , RUL E APPUCABILIT YO R COMPLIANCE . INCLUD E TH E UNI TO F MEASUREMENT , TH E METHO t O F MEASUREMENT , AN D TH E FREQUENC YO F SUC H RECORD S (EG. , HOURLY , DAILY , WEEKLY) : PARAMETE R 

### ba g maint . UNITO F MEASUREMEN T 

### N A METHO D O F MEASUREMEN T 

### maint . lo g FREQUENC Y 

### semi-annua l

APPLICATIO N PAGE . 26 0 -CAAP P 1.4- 4 PAG E 4 O F 1 0



# HiP.5 0

24 b BRIEFL YDESCRIB E TH E METHO D BV WHIC H RECORD S WIL L B E CREATE D AN D MAINTAINED . FO R EAC H RECORDE D PARAMETE R INCLUD E TH E METHO D O F RECORDKEEPING , TITL E O F PERSO N RESPONSIBL E FO R RECORDKEEPING . AN D TITL E O F PERSO N T O CONTAC TFO R REVIE WO F RECORDS : PARAMETE R METHO D O F RECORDKEEPIN G 

## bag maint . maint . lo g TITL E O F PERSO N RESPONSIBL E 

## Maint. superviso r

c ) I S COMPLIANC E O F TH E CONTRO L EQUIPMEN TREADIL YDEMONSTRATE D B

V REVIE WO F TH E RECORDS ? I F NO . EXPLAIN : TITL E O F CONTAC TPERSO N 

## Env. Eng .

YE S N

O

d ) AR E AL L RECORD S READIL YAVAILABL E FO R INSPECTION . COPYIN G AND/O R SUBMITTA L T O TH E AGENC YUPO N REQUEST ? I F NO , EXPLAIN : YE S N O

25a ) DESCRIB E AN V MONITOR S O R MONITORIN G ACTIVITIE S USE D T O DETERMIN E FEES . RUL E APPUCABIUT V O R COMPLIANCE : 

## N A

b ) WHA TOPERATIN G PARAMETER ® IS(ARE ) BEIN G MONITORE D (E.G. . COMBUSTIO N CHAMBE R TEMPERATURE) ? 

## N A

c ) DESCRIB E TH E LOCATIO N O F EAC H MONITO R (E.G. . EXI TO F COMBUSTIO N CHAMBER) : 

## N A

APPLICATIO N PAGE .

260-CAAP P 

## 1.4-

5 PAG E 5 O F 1 0 

# wP.5 1

SSd ) I S EACH MONITOR EQUIPPE D WITH ARECORDIN G DEVICE ? I F NO . LIS TAL L MONITOR S WITHOU TA RECORDIN G DEVICE : N A YE S N O

e) I S EACH MONITOR REVIEWE D FO R ACCURAC

YON A TLEAS TAQUARTERL

YBASIS? I F NO , EXPLAIN : N A 

# n YE S N O

f) I S EACH MONITOR OPERATE D A TAL L TIME S TH E CONTRO L EQUIPMEN

TI S I N OPERATION ? I F NO . EXPLAIN : N A YE S N O

26 ) PROVID E INFORMATION ON TH E MOS TRECEN TTESTS
. I F ANY
. I N WHICH TH E RESULT S AR E USE D FO R •PURPOSE S O F TH E DETERMINATIO N O F FEES . RUL E APPLICABILITYO R COMPLIANCE . INCLUD E TH E TES TDAT E TES TMETHO D USED , TESTIN G COMPANY , OPERATIN G CONDITION S EXISTIN G DURIN G TH E TES TAN D A SUMMAR YO F RESULTS . I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T260-1 : TES TDATE TES TMETHO D TESTIN G COMPAN Y 

## non e OPERATIN G CONDITION S SUMMAR YO F RESULT

S

27 ) PESCRIB E AL L REPORTING REQUIREMENT S AN P PROVID E TH E TITLE AN P FREQUENC YO F REPOR

T SUBMITTAL S T O TH E AGENCY : REPORTIN G REQUIREMENT S TTTL E O F REPOR

T FREQUENC Y 

## Actua l emission s Annua l emission s repor t 

## Annua l

CAPTURE

AND CONTROL li) PESCRIB E TH E CAPTURE SYSTE M U5E P T O CONTAIN , COLLEC

TAN P TRANSPOR

TEMISSION S T

O TH E CONTRO

L EQUIPMENT . INCLUD E AL L HOODS , DUCTS . FANS . ETC . ALS O INCLUD E TH E METHO D O F CAPTUR E USE D A TEACJ H EMISSIO N POINT . (I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T280-2) : 

## Close d tub e conveyin g syste m

APPLICATIO N PAGE . 260-CAAP P 1.4- 6 

## FQ R APPLICANT S US E
PAG E 6 O F 1 0 

### </)

_P.5 2



### 2fl ) AR E FEATURE S O F TH E CAPTUR E SYSTE M ACCURATEL YPEPICTE P I

N TH E FLO W DIAGRA M CONTAINE D I N THI S APPLICATION ? I F NO , A SKETC H SHOWIN G TH E FEATURE S O F TH E CAPTUR E SYSTE M SHOUL D B E ATTACHE D AN D LABELE D A S EXHIBI T260-3 : YE S IN O ib) PROVIP E TH E ACTUA L (MINIMU M AN P



# P AL I CAPTUR E SYSTE M EFFICIENCY . CONTRO L EQUIPMEN T COMBINATIO N O F TH E CAPTUR E SYSTE M AN D CONTRO L EQUIPMEN TFO R EAC H REGULATE D AI R POLLUTAN TT C B E CONTROLLED . ATTAC H TH E CALCULATIONS . T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N WHICI * THES E EFFICIENCIE S WER E BASE D AN D LABE L A S EXHIBI T260-4 : a . CONTRO L PERFORMANCE :

REGULATE D AI R POUUTAN T CAPTUR E SYSTE M EFFICIENC

Y(% ) •PR J TT-7P

T CONTRO L EQUIPMENT

EFFICIENC

Y(% ) 

### •pu r 

# nw OVERA U REDUCTIO N EFFICIENC

Y(% ) 

### -PR J [TW 

## Particulat e 

## 10 0 10 0 99 + 99 + 99 + 99 +

iv . EXPLAI N AN YOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMENTPERFORMANC E SUC H AS OUTLE TCONCENTRATION . COOLANTTEMPERATURE . ETC. :

b ) METHO O USE P T O DETERMIN E EAC H O F TH E ABOV E EFFICIENCIE S (E.G. , STAC KTEST . MATERIA L BALANCE , ED . r MANUFACTURER' S GUARANTEE , ETC. ) AN D TH E DAT E LAS TTESTED , I F APPUCABLE : EFFICIENC

YDETERMINATIO N METHO D DATE LAS T TESTE D CAPTURE : CONTRO L 

## mfr. guarante

e OVERALL 

## mfr . guarante

e mfr. guarante

e "HT . : _f»i i : -iilid : _r»:*.',-.!*• « REGULATE D AI R POUUTAN T CAPTUR E SYSTE M EFFICIENC

Y(% ) CONTRO L

EQUIPMEN

T EFFICIENC

Y(% ) OVERAL L REDUCTIO N EFFICIENC

Y W APPUCABL E RUL E I

EXPLAI N AN YOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMEN TPERFORMANC E SUC H A S OUTLE TCONCENTRATION . COOLANTTEMPERATURE . ETC. :



## 1.4- 7 APPLICATIO N PAGE . 26 0 - CAAP P FQ R APPLICANT S US E PAG E 7 O F 1 0 

# -S IREGULATE D AI R

POLLUTAN T CARBO N MONOXID E (CO )
LEA D

NITROGE N OXIDE S (NOx ) PARTICULAT E MATTE R (PART ) PARTICULAT E MATTE R < ° 1 0 MICROMETER S (PM10 ) SULFU R DIOXID E (S02 ) VOLATIL E ORGANI C MATERIA L (VOM ) OTHER , SPECIFY :

EXAMPLE : PARTICULATE MATTER TYPICA L
Mnm%lflM_Mfl a TYPICAL : MAXMUM : TYPICA L MAXIMUM : TYPICA L MAXMU M TYPICA L MftXIMUM : TYPICA L MAXMU * TYPICA L MAXIMU M TYPICA L MAXMU M TYPICA L LB

S PER HOU R (LBS/HR )

0. 1 0. 1

S.66 4.66 (3DEMISSIO

1 ACTUA L EMISSIO N RAT E "TONSPE R YEA R (TONS/YR )

.4 4 .4 4

11.6 " 17.4 3 OTHE R

TERM S

!

I A i GR/DSC F i 6.14 GR/DSCF 3 OTHE R

TERM S 4 D M

4 4

1 4 % (if l 

## \w VFORMATidN ALLOWABL E B Y RUL E EMISSIO N RAT E
S RAT E (UNITS)

10. 4 Ib/h r , 0. 1

>

—6.6{LBSA.R) 5.5 (LB&HR) APPUCABL E RULE S

212.32 1 212.32 1

111.511 111.511 TON S PE R

YEA R (TONS/YR )

3 9 .4 4

2ki8 1Mb 'PERMITTE D EMISSIO N RAT E

RAT E (UNITS ) TON S PE R YEA R (TONS/YR )

0. 1 Ib./hr . .4 4



# ^^i^^m ^ 1 tLsLbyrlt. I 11 1

IMPORTANT : ATTAC H CALCULATIONS . T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N WHIC H EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T260-6 . 1 PROVID E CONTROLLE D EMISSION S (E.G. , TH E EMISSION S THA TWOUL D RESUL TAFTE R A U CONTRO L AN D CAPTUR E EFFICIENCIE S AR E ACCOUNTE D FOR) . ••PROVID E TH E EMISSIO N RAT E THA TWI U B E USE D A S A PERMI TSPECIA L CONDITION . THI S UMI TWIL L B E USE D T O DETERMIN E TH E PERMI TFE E 'PLEAS E PROVID E AN YOTHE R EMISSIO N RAT E WHIC H I S COMMONL YUSEO , REQUIRE D B YA SPECIFI C UMITATIO N O R THA TWA S MEASURE D (EG . PPM , GR/DSCF . ETC. ) «D M •DETERMINATIO N METHOD : 1 ) STAC KTEST . 2 ) MATERIA L BALANCE , 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) . 4 ) ENGINEERIN G ESTIMATE . S ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS ) 5 RAT E •AUOWABL E EMISSIO N RAT E SPECIFIE D B YMOS TSTRINGEN TAPPLICABL E RULE . 

## 1.4-8 

## i»]:r.vj-jir^:it--ii w k M I"* * A^ ^

• a

## > A ^ 

### (32) HAZARDOUS MR POUUTANT

EMISSION

INFORMATION HA P INFORMATIO N NAM E O F HA P EMITTE D

• EXAMPLE: Benzene ^CA S NUMBE R

71432 1 ACTUA L EMISSIO N RAT E

"""" a *"**"_*"M"""""""'_M_l
_ ROUND S PE R

: HOU R (LBS/HR )

I

__

,

16.6 

### 6.6 TON

S PER YEA R (TONS/YR )



### 1.1 ~ 6.6 •-OTHE R

TERM S *D M

• • ^ 2 ALLOWABL E B Y RUL E

SRAT E O R STANDAR D

98 % by wt control device leak-light

trucks APPLICABL E RUL E



### CM61 61.302(b),(d) IMPORTANT : ATTAC H CALCULATIONS , T O TH E EXTEN T THEY AR E AI REMISSION S RELATED . O N WHICH EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T 2604 . ^PROVID E CONTROLLED EMISSION S (E.G. . TH E EMISSION S THA T WOUL D RESUL T AFTE RA U CONTRO L AN D CAPTUR E EFFICIENCIE S AR E ACCOUNTE D FOR) . $CA S - CHEMICA

L ABSTRAC T SERVIC E NUMBER . TLEAS E PROVID E ANY OTHE REMISSIO N RAT E WHICH I S COMMONL Y USED , REQUIRE O B Y A SPECIFI C UMITATION O RTHA T WA S MEASURE D (E.G. . PPM . GR/DSCF . ETC.) . ZD M - DETERMINATIO

N METHOD : 1 ) STAC KTEST , 2 ) MATERIA L BALANCE , 3 ) STANDAR D EMISSIO N FACTO R(AP-4 2 O RAIRS , 4 ) ENGINEERIN G ESTIMATE . 5 ) SPECIA L EMISSIO N FACTO R(NO T AP-4 2 O RAIRS) . 7IAT E -AUOWABL E EMISSIO N RAT E O RSTANDARD SPECIFIE D B Y MOS T STRINGEN T APPLICABL E RULE . 

### APPUCATIO N PAGE . 260-CAAP P 

## 1.4- 9 PAG E 9 O F 1 0

U l 41 .P.5 5


### EXHAUST POINT INFORMATION 35 ) DESCRIPTIO N O F EXHAUS TPOIN T(STACK

, VENT . ROO F MONITOR . INDOORS . ETC.) . I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS , DO NO TCOMPLET E TH E REMAININ G ITEMS . 

## ven t (discharge

s indoors ) 34 ) DISTANC E T O NEARESTPLANTBOUNDAR VFRO M EXHAUS

TPOIN TDISCHARG E (FT) : 3S ) DISCHARG E HEIGH TABOV E GRAD E (FT) : 36 ) GOO P ENGINEERIN G PRACTIC E (GEP) HEIGHT . I F KNOW N (FT) : 57) DIAMETE R O F EXHAUS

TPOIN T(FT VNOTE : FO R ANO N CIRCULA R EXHAUS TPOINT . TH E DIAMETE R I S 1.128 TIME S TH E SQUAR E ROO TO F TH E AREA . 

### 36) EXI TGAS FLOWRAT E 35) EXI TGAS TEMPERATUR E a ) MAXIMU M (ACFM) : a ) MAXIMU M ('F) : I® DIRECTIO N O F EXHAUS T(VERTICA L LATERAL, DOWNWARD) : b ) TYPICA L (ACFM) : b) TYPICA L ('F) :
41 ) LISTAL L EMISSIO N UNITS AN D CONTRO L DEVICE S SERVE D B VTHI S EXHAUS

TPOINT : NAM E FLO WDIAGRAM DESIGNATIO N a j : 

## W $ 

## W
9 T T% WHA TPERCENTAG E O F TH E CONTRO L EQUIPMEN TEMISSION S AR E BEIN G DUCTE D T O THI S EXHAUS TPOIN T(%) ? \ 

### 45 ) I F TH E PERCENTAG E O F TH E CONTRO L EQUIPMEN TEMISSION S BEIN G DUCTE D T O TH E EXHAUS TPOIN TI S NOT 100% . THE N EXPLAI N WHER E TH E REMAININ G EMISSION S AR E BEIN Q EXHAUSTE D TO :

TH E FOLLOWIN G INFORMATIO N NEE D ONL YB E SUPPLIE D I P READIL

YAVAILABLE . 44a ) LATITUDE : 45 ) UT M ZONE : b ) LONGITUDE : b ) UT M VERTICA L (KM) : c ) UT M HORIZONTA L (KM) :



## APPLICATIO N PAGE . 260-CAAP P 

## 1.4-1 0 PAG E 1 0 O F 1 0

^P.5 6
ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N P.O . BO X1950 8 SPRINGFIELD , ILLINOI S 62794-950 6 

### asraEraaiHonisii H Revisio n # : Date : Pag e o f Sourc e Designation : 

## SUPPLEMENTALFORM AIR POLLUTION

CONTROL EQUIPMENT FILTER (260C) CONTRO L EQUIPMEN Tft T5ATE ! 

### DATA AND

INFORMATION i) FLO WDIAGRA M DESIGNATIO N O F FILTER : 

## FDV-70 1 1) FILTE R CONFIGURATIO N (CHEC KONE) : OPE N PRESSUR E l2_L_ i CLOSE D PRESSUR E OTHER , SPECIFY : 

# • CLOSE D SUCTIO N
3 ) DESCRIB E FILTE R MATERIA L 

### Polyeste r 4 ) FILTERIN G ARE A (SQUAR E FEET) : 

## 14 9 5 ) AIRT O CLOT HRATI O (FEET/MIN) : 

## 4 6 ) CLEANIN G METHO D SHAKE R REVERS E AI R 

# • PULS E AI R 

# • PULS E JE T OTHER . SPECIFY : 7 ) NORMA L RANG E O F PRESSUR E DROP : 2 T 0 6 6a ) INLE TEMISSIO N STREA M PARAMETERS : (INC H H 2 0 )

MOISTUR E CONTEN T( % B YVOLUME) : PARTICULAT E INLETLOADIN G (GRAINS/SCF) : 

## N/ A MA

X TYPICAL



## N/ A

b ) MEA N PARTICL E DIAMETE R (MICRONS) : 

## 16 8 1.5- 1

APPLICATIO N PAGE .

260C-CAAP P PAG E 1 O F 2



# /S 5P.5 7

;'



# c "5

) FILTER-OPERATIN G PARAMETERS : INLE TFLO WRAT E (SCFM) : INLE TGA S TEMPERATUR E (DEGREES FAHRENHEIT) : EFFICIENC

Y(P M REDUCTION) : EFFICIENC

Y(PM1 0 REDUCTION) :
10 ) HOWI S FILTE R MONITORE D FO R INDICATION S O F I I DETERIORATIO N CONTINUOU S (E.G. , BROKE N BAGS) ? OPACIT Y j (VISUA L OPACIT Y R THER . SPECIFY : DURIN G MAXIMU M OPERATIO N O F FEEDIN G UNIT(S

) 

## 600 N/ A 99+ % w 

## 99 + % w DURIN G TYPICA L OPERATIO N O F FEEDIN G UNIT'S ) 

## 600 N/ A 99 + % TO 

## 99+ % l% )

I PRESSUR E ALARMS-AUDIBL E 'DRO P T O PROCES S OPERATO R EADINGS . FREQUENCY : 

## visua l performanc

e chec k 11 ) DESCRIB E AN YRECORDIN G DEVIC E AN D FREQUENC YO F LO G ENTRIES : 

## N/ A e

12) DESCRIB E AN YFILTE R SEEDIN G BEIN G PERFORMED : 

## N/ A

-



## APPLICATIO N PAG E 15- 2 260C-CAAP P 

## sjitMsir-tfsziPii M
PAG E 2 O F 2 

# <toP.5 8
ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N

P.O . BO X1950 6 SPRINGFIELD . ILLINOI S 62794-950 6 •kfJ_J_JIWJ:k*li M Revisio n it. Date : Pag e o f Sourc e Designation :


### AIR POLLUTION

CONTROL EQUIPMENT DATA AND

INFORMATION CONTRO L EQUIPMENT * DATE : THIS FOR M MUS

TB E COMPLETE D K) R EAC H AI R POLLUTIO N CONTRO L EQUIPMENT . COMPLETE AN D PROVID E THI S FOR M I N ADDITIO N T O TH E APPUCABL E ADDENDU M FOR M 260- A THROUG H 260- K

A SEPARATE FOR M MUS TB E COMPLETE D FO R EAC H MOD E O F OPERATIO N O F AI R POUUTIO N CONTRO L EQUIPMENTFO R WHIC H A PERMI TI S BEIN G SOUGHT . 

### SOURCE

INFORMATION i) SOURC E NAME : Cran e Kemlit e l) DAT E FOR M PREPARED : 5) SOURC E I D NO . (I F KNOWN) : 

### Novembe r30,199 5 

## 197800AA X GENERALINFORMATION A) NAM E O F AI R POLLUTIO N CONTRO L EQUIPMEN TAND/O R CONTRO L SYSTEM : 

### Dr yWeig h Tan k

1 B Filte r 5 ) FLO WDIAGRA M DESIGNATIO N O F CONTRO L EQUIPMEN TAND/O R CONTRO L SYSTEM : 

## FDV-70 2 6 ) MANUFACTURE R O F CONTRO L EQUIPMEN T(I F KNOWN) : 

### Shic k 7 ) MODE L NUMBE R (I F KNOWN) : 

## 36A-J3 6 fl) SERIA L NUMBE R (I F KNOWN) : DATE S O F COMMENCIN G CONSTRUCTION . OPERATIO N AND/O R MOS TRECEN TMODIFICATIO N O F THI S EQUIPMEN T(ACTUA L O R PLANNED ) a ) CONSTRUCTIO N (MONTH/YEAR) : 

### 2/8 5 b) OPERATIO N (MONTH/YEAR) : 

### 5/85
. c ) LATES TMODIFICATIO N (MONTH/YEAR) : 

### non e 10 ) BRIEFLYDESCRIB E MODIFICATIO N (I F APPUCABLE) :

HI S AGENC YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R ILUNOI S REVISE D STATUES . 1991 . A S AMENDE D 1992 . HA P 11 1 1/2 . PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E T O D O S O MA Y •-•EVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPLICATIO N BEIN G DENIED . THI S FOR M HA S BEE N PPROVE D B YTH E FORM S MANAGEMEN TCENTER .



### APPLICATIO N PAGE . 26 0 - CAAP P 

## 1.6- 1 FC1 R APPLICANT S US E PAG E 1 O F 1 0
. < !P.5 9



## lm \.)

LISTAL L EMISSIO N UNIT S AN D OTHE R CONTRO L EQUIPMEN TDUCTIN G EMISSION S TO THI S CONTRO L EQUIPMENT : NAM E DESIGNATIO N O R COD E NUMBE R 

## Dr yweig h Tan k

1 B 

## 1 B

12 ) DOE S TH E CONTRO L EQUIPMEN THAV E MOR E THA N ON E MOD E O F OPERATION ? I F YES . EXPLAI N AN D IDENTIF YWHIC H MOD E I S COVERE D B YTHI S FOR M (NOTE : A SEPARAT E AI R POUUTIO N CONTRO L EQUIPMEN TFOR M 260-CAAP P MUS TB E COMPLETE D FO R EAC H MODE) : YE S N O

J3 ) IDENTIF

YAL L ATTACHMENT S T

O THI S FOR M RELATE D T O THI S AI R POLLUTIO N CONTRO L EQUIPMENTS
. TECHNICA L DRAWINGS) :

OPERATING SCHEDULE 1 4 IDENTIFV AN V PERIO D WHE N TH E CONTRO L EQUIPMEN TWIL L NO TB E OPERATIN G DU E T O SCHEDULE D MAINTENANC E AND/O R REPAIR S WHE N TH E FEEDIN G EMISSIO N UNIT(S ) T O THI S CONTRO L EQUIPMEN TIS/AR E II I OPERATION : 

## Non e
TS5 J IDENTIFV AN V PERIOD S DURIN G OPERATIO N O F TH E FEEDIN G EMISSIO N UNIT(S ) WHE N TH E CONTRO L EQUIPMEN TIS/AR E NO TUSED : 

## Non e
b ) I S THI S CONTRO L EQUIPMEN TI N OPERATIO N A TAL L OTHE R TIME S THA TTH E FEEDIN G EMISSIO N UNIT(S ) IS/AR E I N OPERATION ? I F NO , EXPLAI N AN D PROVID E TH E DURATIO N O F TH E CONTRO L EQUIPMEN T DOWNTIME : -YE S N O



### APPLICATIO N PAGE .

260-CAAP P 

## 1.6- 2 PAG E 2 O F 1 0



# <A

## APPUCABLE RuLts 16 ) PROVID E AN YSPECIFI C EMISSIO N STANDARDS ) AN D UMITAT(ON(5 ) SE TB YRULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T(E.G. . VOM . IA C 216.207(b)(1) , 61 % OVERAL L & 90 % CONTRO L DEVIC E EFF.) : !

REGULATE D AI R POLLUTANT'S ) EMISSIO N STANDARO(S ) REQUIREMENTS )



### 1 7 

## Particulat e 1 IA C 212.32 2 i I i ) PROVID E AN YSPECIFI C RECORDKEEPIN G RULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T

REGULATE D AI R POLLUTANTS ) ' RECORDKEEPIN G RULE(S ) 

## non e

IS) PROVID E AN YSPECIFI C REPORTIN G RULE(S ) WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE

O AI R POLLUTANT(S

) REPORTIN G RULE(S )



### "T C

T B 

## Particulat e
) PROVID E AN YSPECIFI C MONITORIN G RULE( 5

REGULATE D AI R POU_UTANT(S ) 

## non e
) PROVID E AN YSPECIFI C TESTIN G RULE S AND / REGULATE D AI R POLLUTANT(S ) 

## non e 

## iw i
i



### O R 

## IA C 201.302(a )

-HC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

MONITORIN G RULE(S

) 

## Proces s weigh t rat e limi t fo rexistin g source s

REQUIREMENT'S)

REQUIREMENTS) 

## Annua l Emission s Repor t

REQUIREMENT(S

)

PROCEDURE S WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

TESTIN G RULE(S

) REQUIREMENT(S )



## APPUCATIO N PAGE . 260-CAAP P 

## 1.6-

3 PAG E 3 O F 1 0P.6 1 COMPUANCE

INFORMATION 21 ) I S TH E CONTRO L SYSTE M I N COMPLIANC E WIT H ALL APPLICABL E REQUIREMENTS ? 

# W YE S 

## LJN O I F NO . THE N FOR M 294-CAAP P "COMPLIANC E PLAN/SCHEDUL E O F COMPLIANC E - ADDENDU M FO R NO N COMPLYIN G EMISSIO N UNITS " MUS TB E COMPLETE D AN D SUBMITTE D WIT H THI S APPLICATION . 11) EXPLANATIO N O F HOWINITIA L COMPLIANC E I S T O BE . O R WA

S PREVIOUSLY . DEMONSTRATED : 

### Installatio n me t manufacturer s standard fo r rate d efficiency offilte r uni t

35) EXPLANATIO N O F HO WONGOIN G COMPLIANC E WIL L B E DEMONSTRATED : 

### Filte r uni t wil l b e kep t i n goo d operatin g condition .

TESTING, MONITORING, RECORDKEEPING AND REPORTING 24a) LISTTH E PARAMETER S THA TRELATE T

O AI R EMISSION S FO R WHIC H RECORD S AR E BEIN G MAINTAINE D T O DETERMIN E FEES , RUL E APPLICABIUT YO R COMPLIANCE . INCLUD E TH E UNI TO F MEASUREMENT . TH E METHO C O F MEASUREMENT . AN D TH E FREQUENC YO F SUC H RECORD S (E.G. . HOURLY , DAILY , WEEKLY) : PARAMETE R UNI TO F MEASUREMEN TMETHO D O F MEASUREMEN TFREQUENC Y 

### ba g maint . 

## NA

. „ _ _.. . 

### maint . lo g

.. _ 

### semi-annua l



## 1.6- 4 APPLICATIO N PAGE . 260-CAAP P PAG E 4 O F 1 0



# /ef)P.6 2

24b ) BRIEFLYDESCRIB E TH E METHO D B V WHIC H RECORD S WIL L B E CREATE D AN D MAIN ! AINED . FO R EAC H RECORDE D PARAMETE R INCLUD E TH E METHO D O F RECORDKEEPING . TITL E O F PERSO N RESPONSIBL E FO R RECORDKEEPING . AN D TITL E O F PERSO N T O CONTAC TFO R REVIE WO F RECORDS : PARAMETE R METHO D O F RECORDKEEPIN G 

## ba g maint . maint . lo g TITI E O F PERSO N RESPONSIBLE 

## Maint . supervisor

c ) I S COMPLIANC E O F TH E CONTRO L EQUIPMEN TREADILYDEMONSTRATE D BV REVIE WO F TH E RECORDS ? I F NO . EXPLAIN : TITL E O F CONTAC TPERSO N 

## Env . Eng .

YE S N

O

d ) AR E AL L RECORD S READIL YAVAILABL E FO R INSPECTION . COPYIN G AND/O R SUBMITTA L T O TH E AGENC YUPO N REQUEST ? I F NO . EXPLAIN : YE S N O

25a ) DESCRIB E AN V MONITOR S O R MONITORIN G ACTIVITIE S USE D T O DETERMIN E FEES . RUL E APPUCABIUT V O R COMPLIANCE : 

## N A

b) WHA TOPERATIN G PARAMETER^ ) I5(ARE ) BEIN G MONITORE D (E.G. . COMBUSTIO N CHAMBE R TEMPERATURE) ? 

## N A

c ) DESCRIB E TH E LOCATIO N O F EAC H MONITO R (E.G. , EXI TO F COMBUSTIO N CHAMBER) : 

## NA

APPLICATIO N PAGE .

260-CAAP P 

## 1.6- 5 PAG E 5 O F 1 0



# /olP.6 3

25d) I S EAC

H MONITOR EQUIPPE D WITH ARECORDIN G DEVICE ? I F NO . LIS TAL L MONITOR S WITHOU TA RECORDIN G DEVICE : N A 

# U YE S | X'N O

B ) I S EACH MONITO R REVIEWE D FO R ACCURAC YO N A TLEAS TA QUARTERL

YBASIS ? I F NO . EXPLAIN : N A YE S 

# B U N O

f ) I S EAC H MONITOR OPERATE D A TAL L TIMES TH E CONTRO L EQUIPMEN

TI S I N OPERATION ? I F NO . EXPLAIN : 

### NA YE S N O

25 , PROVIDE INFORMATION O N TH E MOS TRECEN TTESTS
. I F ANV
. I N WHIC H TH E RESULT S AR E USE D FOR PURPOSE S O F TH E DETERMINATIO N O F FEES , RUL E APPLICABILIT YO R COMPLIANCE . INCLUD E TH E TES TDAT E TES TMETHO D USED , TESTIN G COMPANY , OPERATIN G CONDITION S EXISTIN G DURIN G TH E TES TAN D A SUMMAR YO F RESULTS . I F ADDITIONA L SPAC E I S NEEDED , ATTAC H AN D LABE L A S EXHIBI T260-1 : TES TDATE TES TMETHO D TESTIN G COMPAN Y OPERATIN G

CONDITION S 

### non e SUMMAR YO F RESULT

S

27 ) DESCRIBE AL L REPORTING REQUIREMENT S AN D PROVID E TH E TITL E AN D FREQUENC YO F REPOR

T SUBMITTAL S T O TH E AGENCY : REPORTIN G REQUIREMENT S TITLE O F REPOR T FREQUENC Y 

### Actua l emission s Annua l emission s repor t 

### Annua l

CAPTURE

AND CONTROL 26 ) DESCRIB

E TH E CAPTURE SYSTE M USE D T O CONTAIN , COLLEC

TAN D TRANSPOR

TEMISSIONS T

O TH E CONTROL EQUIPMENT . INCLUD E A U HOODS . DUCTS , FANS . ETC . ALS O INCLUD E TH E METHO D O F CAPTUR E USE D A TEAd H EMISSIO N POINT . (I F ADDITIONA L SPAC E I S NEEDED . ATTAC H AN D LABE L A S EXHIBI T260-2) : 

### Close d tub e conveyin g syste m

APPLICATIO N PAGE . 260-CAAP P 

### 1.6-6 

## FO R APPLICANT S US E
PAG E 6 O F 1 0 

# fJP.6 4

25 ) AR E FEATURE S O F TH E CAPTUR E SYSTE M ACCURATEL YDEPICTE D I N TH E FLO W DIAGRA M CONTAINE D I N THI S APPLICATION ? I F NO , A SKETC H SHOWIN G TH E FEATURE S O F TH E CAPTUR E SYSTE M SHOUL D B E ATTACHE D AN D LABELE D A S EXHIBI T260-3 : YE S 

## QN O
30 ) PROVID E TH E ACTUA L (MINIMU M AN D TYPICAL ) CAPTUR E SYSTE M EFFICIENCY , CONTRO L EQUIPMEN T DESTRUCTION/REMOVA L EFFICIENCY . AN D TH E OVERAL L REDUCTIO N EFFICIENC YPROVIDE D B YTH E COMBINATIO N O F TH E CAPTUR E SYSTE M AN D CONTRO L EQUIPMEN TFO R EAC H REGULATE D AI R POUUTAN TT C B E CONTROLLED . ATTAC H TH E CALCULATIONS . T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N WHIC H THES E EFFICIENCIE S WER E BASED AN D LABE L A S EXHIBI T260-4 : a ) CONTRO L PERFORMANCE ;

REGULATE D AI R POLLUTANT CAPTUR E SYSTE M EFFICIENC

Y(% ) (MIN ) (TYP) CONTROL EQUIPMENT EFFICIENC

Y(% ) -WH (TYP

) OVERA U REDUCTIO N

EFFICIENC

Y(% ) 

### "PR I \TW~ 

### Particulat e 

## 10 0 10 0 99 + 99 + 99 + 99 +

EXPLAI N AN YOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMENTPERFORMANC E SUC H A S OUTLE TCONCENTRATION . COOLANTTEMPERATURE . ETC. :

b ) METHO D USE D T O DETERMIN E EAC H O F TH E ABOV E EFFICIENCIE S (E.G. , STAC KTEST , MATERIA L BALANCE , MANUFACTURER' S GUARANTEE . ETC. ) AN D TH E DAT E LAS TTESTED . I F APPUCABLE : EFFICIENC

YDETERMINATIO N METHO D OAT E LAS T TESTE D CAPTURE : CONTRO L 

### mfr . guarante e OVERAL L 

### mfr . guarante e

mfr . guarante e



## " 3 :U» H l : -*iI-J-4:"_f » :i,VJ

_ « H REGULATE D AI R POLLUTANT CAPTUR E SYSTE M EFFICIENC

Y<% ) CONTRO L

EQUIPMENT EFFICIENC

Y(% ) OVERA U REDUCTIO N EFFICIENC

Y 

### W APPUCABL E RUL E

EXPLAI N ANYOTHE R REQUIRE D LIMIT S O N CONTRO L EQUIPMENTPERFORMANCE SUC H A S OUTLE TCONCENTRATION , COOLANTTEMPERATURE . ETC. :



## 1.6- 7 APPLICATIO N PAGE . 260-CAAP P FO R APPLICANT S US E PAG E 7 O F 1 0 

# /oS/

REGULATE D AI R POLLUTAN T CARBO N MONOXID E (CO )
LEA D

NITROGE N OXIDE S (NOx ) PARTICULAT E MATTE R (PART ) PARTICULAT E MATTE R « •1 0 MICROMETER S (PM10 ) SULFU R DIOXID E (S02 ) VOLAYILl * ORGANI C MATERIA L (VOM ) OTHER , SPECIFY : EXAMPLE: PARTICULATE MATTER TYPICAL MAXIMUM : TYPICA L MAXIMUM : TYPICAL : MAXIMUM : TYPICA L MAXIMUM : TYPICA L MAXIMUM : TYPICA L MAXIMUM : TYPICA L MAXIMUM : TYPICA L MAMMUM : TYPICA L LB S PE R

HOU R (LBS/HR )



## 0. 1 0. 1

8.66 4.66 (31)£MISS)6

1 ACTUA L EMISSIO N RAT E TON S PER YEA R (TONS/YR )



## .4 4 .4 4

11.6 ' TR — MOTHE R

TERM S

i

!

d. 3 " • GR0SCF 6.14 GR/DSCF 3 OTHE R

TERM S

V
. 4 D M



## 4 4

1 • 4 

# m VtdRMATlON ALLOWABL E B YRUL E EMISSIO N RAT E

6 RAT E (UNITS )

10. 4 Ib/h r 0. 1

—8.37/J&WA

) 5.5 (LBS/HR) APPLICABL E RULE S



## 212.32 1 212.32 1

11x511 111.511 TON S PE R

YEA R (TONS/YR )



## 3 9 .4 4

11.18 19.80 'PERMITTE D EMISSIO N RAT E

RAT E (UNITS ) TON S PE R YEA R (TONS/YR )

0. 1 lb./hr . | .4 4



# I^HHBBHI H MIMSMR

I 11 1

IMPORTANT : ATTAC H CALCULATIONS , T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N WHIC H EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T280-5 . 1 PROVID E CONTROUE D EMISSION S (E.G. . TH E EMISSION S THA TWOUL D RESUL TAFTE R AL L CONTRO L AN D CAPTUR E EFFICIENCIE S AR E ACCOUNTE D FOR) . --PROVID E TH E EMISSIO N RAT E THA TWIL L B E USE D A S A PERMI TSPECIA L CONDITION . THI S UMI TWU L B E USE D T O DETERMIN E TH E PERMT TFE E 3 PLEAS E PROVID E AN YOTHE R EMISSIO N RAT E WHIC H I S COMMONL YUSED . REQUIRE D B YA SPECIFI C UMITATIO N O R THA TWA S MEASURE D (E.G . PPM , GR/DSCF . ETC. ) 4 D M - DETERMINATIO N METHOO : 1 ) STAC KTEST . 2 ) MATERIA L BALANCE . 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) , 4 ) ENGINEERIN G ESTIMATE . 6 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS ) 5 RAT E - ALLOWABL E EMISSIO N RAT E SPECIFIE D B YMOS TSTRINGEN TAPPUCABL E RULE . 

## 1.6- 8 *• ] iWA di ) I W : I KHM : ADD I tr. ATtnM PAft F- " " (32) HAZARDOUS

AIR POnVTAnTTMISSlON INFORMATION HA P INFORMATIO N NAM E O F HA P EMITTE D

1 EXAMPLE: Benzene "*CA S NUMBE R

7143 2 1 ACTUA L EMISSIO N RAT E

UAUMUI C

MJ"l-JU_Ml_MH » POUND S PE R

HOU R (LBS/HR )

i

f

16.6 

### 6.6 TON S PE R

YEA R (TONS/YR ) •



### 1.1 6.6 30THE R

TERM S ^ M



### 1 2 ALLOWABL E B YRUL E
5RAT E O R STANDAR D

98 % by wt oontroi device leek-tight

trucks APPLICABL E RUL E

CFR 61 61.302(b).(d) IMPORTANT : ATTAC H CALCULATIONS , T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N VIMIC H EMISSION S WER E DETERMINE D AN D LABE L A S EXHIBI T260-6 . ^PROVID E CONTROLLE D EMISSION S (EG. . TH E EMISSION S THA TWOUL D RESUL TAFTE R A U CONTRO L AN D CAPTUR E EFFICIENCIE S AR E ACCOUNTE D FOR) . 5CA S •CHBfflCA L ABSTRAC TSERVIC E NUMBE R ""PLEAS E PROVID E AN YOTHE R EMISSIO N RAT E WHIC H I S COMMONL YUSEO . REQUIRE D B YA SPECIFI C LIMITATIO N O R THA TWA S MEASURE D (E.G. , PPM . GR/DSCF . ETC.) . ?D M •DETERMINATIO N METHOD : 1 ) STAC KTEST , 2 ) MATERIA L BALANCE . 3 ) STANDAR D BWSSIO N FACTO R (AP-4 2 O R AIRS . 4 ) ENGINEERIN G ESTIMATE . 5 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS) . -"RAT E •AUOWABL E EMISSIO N RAT E O R STANDAR D SPECIFIE D B YMOS TSTRINGEN TAPPLICABL E RULE . 

## APPUCATIO N PAGE . 260-CAAP P 

## 1.6-9 PAG E 9 O F 1 0P.6 7

EXHAUST

POINT INFORMATION 33 , BE5CRIPTI0 N O F EXHAUS TPOIN T(STACK
. VENT
. ROO F MONITOR
. INPOOR5
. ETC.)
. I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS , D O NO TCOMPLET E TH E REMAININ G ITEMS
. 

## ven t 34 ) BISTANC E T O NEARES TPUW TBOUNBAR V FRO M EXHAUS TPOIN TBI5CHARG E (FT) : 

## 20 0 3S ) BISCHARG E HEIGH TABOV E GRAB E (FT) : 

## 2 8 36 ) GOO B ENGINEERIN G PRACTIC E (GEP ) HEIGHT
. I F KNOW N (FT) : 37 ) BIAMETE R O F EXHAUS TPOIN T(FT) : NOTE : FO R ANO N CIRCULA R EXHAUS TPOINT
. TH E BIAMETE R I S 1.12 8 TIME S TH E SQUAR E ROO TO F TH E AREA
. a- Q 46
. EXI TGA S FLO WRAT E 33 ) EXI TGA S TEMPERATUR E a ) MAXIMU M (ACFM) : 

## 60 0 a ) MAXIMU M ('F) : 

## ambient TRJ J DIRECTIO N O F EXHAUS T(VERTICAL
. LATERA LBOWNWARB) :



## - latera l b ) TYPICA L(ACFM) : 

## 60 0 b ) TYPICA L('F) : 

## ambient
41 ) US TAL LEMISSIO N UNIT S AN B CONTRO LBEVICE S SERVE B B V THI S EXHAUS TPOINT :

NAM E FLO WDIAGRA M DESIGNATIO N 

## i y Dr y weig h tan k

1 B 

## W ST 

## W 1 B (FPV-702 )

"E J WHA

TPERCENTAG E O F TH E CONTROL EQUIPMEN TEMISSIONS AR E BEIN G BUCTE B T O THI S EXHAUS TPOIN T(%)? 

## 10 0 43 ) I F TH E PERCENTAG E O F TH E CONTRO LEQUIPMEN TEMISSION S BEIN G BUCTE B T O TH E EXHAUS TPOIN TI S NO T 100%
. THE N EXPLAI N WHER E TH E REMAININ G EMISSION S AR E BEIN G EXHAUSTE D T a

TH E FOLLOWIH e INFORMATIO N HEE D OML V B E SUPPLIE D I F EEAPIL

V AVAILABLE
. 44a ) LATITUDE : 

## 41-27-4 5 45 ) UT M ZONE:
. b , LONGITUDE : 

## 88-11-1 5 b ) UT M VERTICA L(KM) : c ) UT M HORIZONTA L(KM) :



## APPLICATIO N PAGE . 260-CAAP P 

## 1.6-1 0 PAG E 1 0 O F 1 0



# u>P.6 8 ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N

P O BO X1950 6 SPRINGFIELD.'ILLINOI S 62794-950 6 ••;fJ__-_H_»«_k_fcJiR : Revisio n # : Date : Pag e o f Sourc e Designation : 

### SUPPLEMENTALFORM /UR POLLUTION

CONTROL EQUIPMENT FILTER (260C) CONTRO L EQUIPMENT * TJATE T 

### DATA AND

INFORMATION i) FLO WDIAGRA M DESIGNATIO N O F FILTER : 

## FDV-70 2 2 ) FILTE R CONFIGURATIO N (CHEC KONE) : OPE N PRESSUR E | X| CLOSE D PRESSUR E OTHER . SPECIFY : 

# • CLOSE D SUCTIO N 3) DESCRIB E FILTE R MATERIA L 

### Polyeste r 4 ) FILTERIN G AREA (SQUAR E FEET) : 

## 14 9 5 ) AI R T O CLOTH RATI O (FEET/MIN) : 4 i) CLEANIN G METHO B SHAKE R REVERS E AI R 

# • PULS E AI R 

# • PULS E JE T OTHER , SPECIFY : 7 ) NORMA L RANG E O F PRESSUR E DROP : 2 TO g 6a ) INLE TEMISSIO N STREA M PARAMETERS : (INC H H 2 0 )

MOISTUR E CONTEN T( % B YVOLUME) : PARTICULAT E INLETLOADIN G (GRAINS/SCF) : 

## N/ A MA

X TYPICA L



## N/ A

b ) MEA N PARTICL E BIAMETE R (MICRONS) : 

### 6 0 1.7- 1

APPLICATIO N PAGE . 260C-CAAP P PAG E 1 O F 2



# f/>7P.6 9

( • S

) FILTE R OPERATIN G PARAMETERS :
INLE TFLO WRAT E (SCFM) : INLE TGA S TEMPERATUR E (DEGREE S FAHRENHEIT) : EFFICIENC Y(P M REDUCTION) : EFFICIENC Y(PM1 0 REDUCTION) : DURIN G MAXIMU M OPERATIO N O F 

## 60 0 N/ A 99 + % 

## 99 + % (%

) (% ) DURIN G TYPICA L

OPERATIO N O F FEEDIN G UNIT.S ) 

## 60 0 N/ A 99 + 

## % 99+ % 

## W

W
1 0 HO WI S FILTE R MONITORE B FO R INDICATIONS O F I I DETERIORATIO N CONTINUOU S (E.G. , BROKE N BAGS) ? ' 'OPACIT Y JPRESSUR E '—'DRO P 

# • 0 ALARMS-AUDIBL E T O PROCES S OPERATO R VISUA L OPACIT YREADINGS . FREQUENCY : OTHE R SPECIFY: v 

### j sua 

### j performanc e chec k 11 ) BESCRIB E AN YRECORBIN GBEVIC E AN P FREQUENC V O F LO GENTRIES : 

# N/ A

12 ) PESCRIB E AN

V FILTE RSEEPINGBEIN

GPERFORMEB : 

# N/ A

APPLICATIO N PAG E 1-7- 2 260C-CAAP P PAG E 2 O F 2



# JaP.7 0



### I D #197800AA

X Cran e Kemlit e 

## Proces s Descriptio n Lon g Pane l Productio nLine s Al l thre e lines , LP-3 , LP-6 , an dLP- 7 manufactur e fiberglass reinforce dplasti c panel s i nessentiall y identica l proces s methods . Th e line s ar e compute r controlle d an dproces s activit y i s monitore dan drecorde delectronically . Ther e ar e smal l difference s i neac hmachine , bu t th e following proces s descriptio nappUe s t o al l thre e productio nlines . Polyeste r resi nmi x i s pumpe dfromon e o f th e mixin g room s i naclose dpipin g syste mt o th e lin e fo

r processing . I naclose dsystem , on e o r mor e component s includin g catalyst , promoter , o r pigmen t ar e pumpe dint o th e mixture . Th e mi x i s the n allowe dt o flo

w ont o amovin g shee t

of polyeste r film. A doctorin g blad e level s th e resi nt o adesire dthicknes s a s i t travel s underneat hth e blade . Immediatel y beyon dth e docto r

blad e choppe dfiberglass i s distribute do nto p th e resi nmix , coverin g it . Thi s materia l the ntravel s thoug hcompressio nroll s fo r desire d thickness , an dwher e anothe r laye r of polyeste r filmi s appHe dt o for

ma "sandwich " of

resi nmi x an dfiberglass whic hbecome s th e finishedpanel . e Th e pane l the ntravel s throug hase t o f electri c oven s wher e controlle dhea t allow s th e pane l t o cur e (harden ) t o th e desire dpropertie s fo r tha t product . After

th e pane l travel s ou t

o f th e oven , i t

cool s o nth e way t o th e en dof th e lin e wher e th e filmi s removed , th e edge s ar e trimme dan di t i s cu t t b th e prope r

length . Th e fiberglass tha t

i s adde dt o th e pane l a s describe dabov e i s don e b y pullin g individua l rovin g throug hclose dtubin g t o achopper device . A lin t

exhaus t syste m collect s loos e strand s an drecirculate s th e ai r int o th e plant . Kemlit e propose s th e lin t exhaus t syste mt o b e a ninsignifican t activity a s demonstrate do nFor m29 7 i n thi s permi t

application . Proces s activit y i s continuousl y monitored . Record s o f th e proces s parameter s ar e mad e severa l time s a n hou r dunn g th e productio nrun . Record s ar e mad e fo r totalize damount s o

f materia l provide dt o th e process . Th e emission s rat e i s calculate dcontinuousl y wit hinformatio nfromth e proces s parameter s an d monome r percen t informatio nfromth e mi x areas . Thi s rat e i s monitoredb y th e compute r contro l syste mt o alar mi f rat e limit s ar e approached . Record s fo r totalize demission s ar e mad e firomthi s sam e calculate dinformation . Record s includ e date , time , produc t type , usag e information , proces s parameters , emission s parameters , an dtota l emissions . Applicatio n Pag e 2.1- i 

# fflP.7 1



# Wm 

# I

v . 

# i

C M CN J srou Ttn-ttBrato

C D


# in

# - a 2.2 DISPLAY

OF EQUIPMENT



# LP-6 LINE

pttooucr COILER 

# g^x ROVING RACKS

TOP FILM MZNDU P OOOOOOOO O ROLLER^ CONVEYOR OOO O ROLLER CONVEYOR BOTTOM

FUJI UXNOUP \ ROVINQ lt€ATB»lHEATB_

BELT COOUNB

BOX IIB"

tOOE STAOLSTEELBELT 1 1/.U1 . A _/UD
_ 6LASS ROVINB
BOTTOM FILM UMNO (VIRGIN)

Applicatio n Pag e 2.1-ii i 

## KP.7 3

»..•-• » 

# IrOP.7 4 ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F AI R POLLUTIO N CONTRO L - PERMI TSECTIO N

P.O . BO X1950 6 SPRINGFIELD . ILLINOI S 62794-950 6 FO R APPLICANT S US E Revision s 0
__ _ Date : _September 15.199 5 Pag e o

f Sourc e Designation : Kemlit e Jolie t 

## PROCESS

EMISSION

UNIT DATAAND

INFORMATION EMISSIO N POIN T« : T5CTE T 

### SOURCE

INFORMATION 1 ) SOURCE NAME : Cran e Kemlit e 2 ) DATE FOR M 5 ) SOURC E I P NO . <ft 

### , flnfttt v 

### (I F KNOWN) : 197800AA X PREPARED : Novembe r30,199 5 GENERALINFORMATION 4 ) NAM E O P EMISSIO N UNIT : : L p 

### ~j. ; 

### _*-^~f rjj 3-7 

### ' Lon 

### 9 Pane l 

### P roce 

### s s Line s 5 ) NAM E O F PROCES S Continuou s Laminatio n 6) DESCRIPTIO N O F PROCESS : Continuou s wet-ou t an d ove n curin g o f resi n mi x 7 ) DESCRIPTIO N O F ITE M O R MATERIAL PRODUCE D O R ACTIVIT V ACCOMPUSHED : Fiberglas s reinforce d plasti c pane l eri i 37715 1 

### plasti c p a

IO N O F EMIS ! i) FL0WBIA5RA M DESI5NATI0 N O F EMISSIO N UNIT : 

## LP-3 ; LP-6 ; LP- 7 5 ) MANUFACTURE R O F EMISSIO N UNI T(I F KNOWN) : 10 ) MODE L NUMBE R (I F KNOWN) : 

## N A i i) SERIAL NUMBE R (I F KNOWN) : 

## NA 1 2 DATE S O F COMMENCIN G CONSTRUCTION . OPERATIO N AND/O R MOS TRECEN TMODIFICATIO N O F THI S EMISSIO N UNI T(ACTUA L O R PLANNED ) a ) CONSTRUCTIO N (MONTWVEAR) : 

## 1979 ; 1980 ; 1985 b ) OPERATIO N (MONTWVEAR) : 

## 5/80 ; 10/80 ; 5/8 5 c) LATES TMODIFICATIO N (MONTH/YEAR) : 

### non e 13 ) DESCRIPTIO N O F MODIFICATIO N (IFAPPLICABLE) :

THI S AGENC

YI S AUTHORIZE D T O REQUIR E THI S INFORMATIO N UNDE R lUINOI S REVISE D STATUES . 1991 . A S AMENDE D 1992 . CHA P 11 1 1/2 . PAR . 1039.5 . DISCLOSUR E O F THI S INFORMATIO N I S REQUIRE D UNDE R THA TSECTION . FAILUR E T O D O S O MA Y. PREVEN TTHI S FOR M FRO M BEIN G PROCESSE D AN D COUL D RESUL TI N TH E APPLICATIO N BEIN G OENIED . THI S FOR M HA S BEE N APPROVE D B

YTH E FORM S MANAGEMENTCENTER . 

## APPLICATIO N PAG E 220-CAAP P 

## 2.1- 1 PAG E 1 O F 1 0



# 7 ^ ^P.7 5

U ) DOE S TH E EMISSIO N UNI THAV E MOR E THA N ON E MOD E O F OPERATION ? I F YES . EXPLAI N AN D IDENTIF YWHIC H MOD E I S COVERE D B YTHI S FOR M (NOTE : A SEPARAT E PROCESS EMISSIO N UNI TFOR M 220-CAAP P MUS TB E COMPLETE D FO R EAC H MODE) : YE S X XN O

15 ) PROVID E TH E NAM E AN D DESIGNATIO N O F AL L AI R POLLUTIO N CONTRO L EQUIPMEN TCONTROLLIN G THI S EMISSIO N UNIT . I F APPLICABL E (FOR M 260-CAAP P AN D TH E APPROPRIATE 260-CAAP P ADDENDU M FOR M •MUSTB E COMPLETE D FO R EAC H ITE M O F AI R POLLUTIO N CONTRO L EQUIPMENT) :
1 6 WIL L EMISSION S DURIN O STARTU P EXCEE D EITHE R TH E ALLOWABL E EMISSIO N RAT E PURSUAN TT

O A SPECIFI C RULE , O R TH E ALLOWABLE EMISSIO N LIMITA S ESTABLISHE D B

YA N EXISTIN G O R PROPOSE D PERMI TCONDITION ? I F YES . COMPLET E AN D ATTAC H FOR M 203-CAAPP , "REQUES TTO OPERAT E WIT H EXCES S EMISSION S DURIN G STARTU P O F EQUIPMENT . YE S X X >
17 ) PROVID E AN V UMITATION S O N SOURC E OPERATIO N AFFECTIN 5 EMISSION S O R AN V WOR KPRACTIC E STANDARD S (E.G. . ONL YON E UNI TI S OPERATE D A TA TIME) : 

## se e exhibi

t220 - 6

OPERATING INFORMATION

~ " i i) ATTAC H TH E CALCULATIONS
. T O TH E EXTEN TTHE V AR E AI R EMISSIO N RELATED
. FRO M WHIC H TH E FOLLOWIN G OPERATIN G INFORMATION . MATERIAL USAG E INFORMATIO N AN D FUE L USAG E OAT A WER E BASE D AN D LABE L AS EXHIBI T220-1 . REFE R T O SPECIA L NOTE S O F FOR M 202-CAAPP . 1§a , MAXIMU M 0PERATIN 5 HOUR S 

## 7500 ; 7500 ; 750 0 HOURS/DAY : 

## 24 ; 24 ; 2 4 BAYS/WEEK :
•WHHM I WEEKS/YEAR :



## 52 ; 52 ; 5 2 b . 1YPICA L OPERATIN G HOUR S 

## 5020 ; 5818 ; 3145 HOURS/DAY : 

## 19.3.22.4 ; 12. 1 BXYSWEEK :



### 5 ; 5 ; 5 

### WEEKsflkAR :



## 52 ; 52 ; 5 2 20 ) ANNUA L THROUGHPU T BEC-FEBM : 

## 25 ; 25 ; 2 5 MAR-MAV(K) :



## 25 ; 25 ; 2 5 JUN-AUG(%) :



## 25 ; 25 ; 2 5 SEP-NOV(%) :



## 25 ; 25 ; 2 5 MATERIALUSAGE

INFORMATION

21a ) RA W MATERIAL

S Polyeste rresi n mixtur e MAXIMU M RATE S LBS/H R 

## 1920 0 TONS/YEA R



## 7200 0 TYPICA L RATE S LBS/H R 

## 9141. 6 21660. 2

TONSflEA R



## APPLICATIO N PAG E 2.1-2 220-CAAP P PAG E 2 O F 1 0



# nuP.7 6

21b ) PRODUCT

S 

### FR P Pane l

21c ) BY-PRODUC

TMATERIALS MAXIMU M RATE S

^ LBS/H R 

### N A TONS/YEA R



## N A

MAXIMU M RATE S LBS/H R TONS/YEA R TYPICA L RATE S LBS/H R 

## N A TONS/YEA R



## N A

TYPICA L RATE S LBS/H R TONS/YEA R

FUELUSAGE

DATA 22a ) MAXIMU M FIRIN G RAT E (MILLIO N BTU/HR) : b ) TYPICA L FIRIN G RAT E (MILUO N BTU/HR) : c | DESIG N CAPACIT YFIRIN G RATE (MILUO N BTU/HR) : 

### T T FUELTYPE : j _ J NATURA L GAS | [FUE L OI L GRAD E NUMBE R [TjcOA L [[OTHE R
_ _ I F MOR E THA N ON E FUE L I S USED . ATTAC H A N EXPLANATIO N AN D LABEL A S EXHIBIT220-2 . "e i TYPICA L HEATCONTEN TO F FUE L (BTU/LB
. BTU/GA L O R BTU/SCF) : T j ' TYPICA L SULFU R CONTEN T(W T%.
. N AFO R NATURA L GAS) : 9 , TYPICA L AS H CONTEN T(WTK..N AFO R NATURA L GAS) : h , ANNUA L FUE L USAG E (SPECIFYUNITS
. E.G. , SCF/YEAR . GAL/YEAR . TON/YEAR) : 25 ) AR E COMBUSTIO N EMISSION S DUCTE D T O TH E SAM E STAC KO R CONTRO L A S PROCES S UNI TEMISSIONS ? I F NO . IDENTIF

YTH E EXHAUS

TPOIN TFO R COMBUSTIO N EMISSIONS : YE S N

O



### APPLICATIO N PAGE 2 

### - 1 

### " 3 220-CAAP P PAG E 3 O F 1 0

! < ,

### :'~ > Stkx .- " —N , 

### APPUO^g.RULES 24 ) PROVIb t AN YSPECIFI C EMISSIO N STANDARD ® AN D UMITATION(S ) SE TBYRULE(Sy$HIC H AR E APPUCABL E T O THI S EMISSIO N UNI T(E.G.
. VOM , IA C 216.204(j)(4) , a. S LBS/GAL) : REGULATE D AI R POLLUTANT'S ) EMISSIO N STANDARDS ) REQUIREMENT(S ) 

## VO M VO M IA C 218.30 1 (A C 218.66 0 | i ~55 ) PROVID E AN YSPECIFI C RECORDKEEPIN G RULE(S ) jWHIC H AR E APPUCABL E T O THI S EMISSIO N UNI T REGULATE D AI R POLLUTANTS ) | RECORDKEEPIN G RULE(S ) 

## VO M !IA C 218.672(a ) «
1 5 ) PROVID E AN

YSPECIFI C REPORTIN G RULE(S ) WHIC H AR E APPUCABL E TO THI S EMISSIO N UNIT : REGULATE D AI R POUUTANT(S ) REPORTIN G RULE(S )



### Tf V O M
) PROVID E AN YSPECIFI C MONITORIN G RULE( 5

REGULATE D AI R POLLUTANT(S ) 

### non e IW I ; IA C 201.302(a )

'v.
. -IIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

MONITORIN G RULE(S ) • I

i . 

### Us e o f organi cmateria l (se e exhibi t 220-8 )

REQUIREMENT(S ) 

### Name , ID# , an d VO M conten t of each polyeste rresi n used
.

REQUIREMENT(S ) 

### Annua l Emission s Repor t

REQUIREMENTS )

TB ) PROVID E ANYSPECIFI C TESTIN G RULES AND/O R PROCEDURE S WHIC H AR E APPUCABL E T O THI S EMISSIO N UNIT :

REGULATE D AI R POLLUTANT(S ) TESTIN G RULE(S ) REQUIREMENTS ) 

### non e



## 2.1* 4 

# MtFjasir-tfrcrfcii H;TT _W'"?! r- P.7 8

25 ) DOE S TH E EMISSIO N UNI TQUALIF YFOR AN EXEMPTION FRO M AN OTHERWIS E APPLICABL E RULE ? YE S XX i N O I F YES , THE N LIS TBOT H TH E RUL E FRO M WHIC H I TI S EXEMP TAN D TH E RUL E WHIC H ALLOW S TH E EXEMPTION . PROVID E A DETAILE D EXPLANATIO N JUSTIFYIN G TH E EXEMPTION . INCLUD E DETAILE D SUPPORTIN G DAT A AN D CALCULATIONS . ATTAC H AN D LABE L A S EXHIBI T220-3 , O R REFE R T O OTHE R ATTACHMENT(S ) WHIC H ADDRES S AN D JUSTIF YTHI S EXEMPTION . COMPUANCE INFORMATION 50 ) I S TH E EMISSIO N UNI

TI N COMPLIANCE WITH AL L APPUCABL E 

# B REQUIREMENTS ? X XYE S 

### N O I F NO , THE N FOR M 294-CAAP P "COMPLIANC E PLAN/SCHEDUL E O F COMPLIANC E - ADDENDU M FO R NO N COMPLYIN G EMISSIO N UNITS " MUS TB E COMPLETE D AN D SUBMITTE D WIT H THI S APPLICATION . 51 ) EXPLANATION O F HO W INITIAL COMPLIANCE I S T O BE
. O R WA S PREVIOUSLY

. DEMONSTRATED: 

### Engineerin g calculation s wer e develope d to estimate an d recor d emission s dat a tha t wer e subsequentl y validate d throug h a stac k tes t procedure performe d i n Apri l 199 2 base d o n a protoco l approve d b y th e IEP A i n Jan . 1992 . Th e result s o f th e stac k

tes t wer e submitte d t o th e agency i n Ma y 1992 . Thes e calculation s wer e the n incorporate d into Illinoi s Ai r permi t # 80050016 .

32 ) EXPLANATIO

N OF HO W ONGOIN

G COMPUANC

E WIL L B E DEMONSTRATED

: 

### Calculation s validate d fro m th e stac k tes t wil l b e use d t o record emissio n rate s fro m proces s an d supplie r data . Thes e calculation s an d record s ar e mad e an d

. store d i n th e manufacturin g compute r syste m an d dat a base , respectively .

TESTING:

MONITORING, RECORDKEEPING AND REPORTING 33a ) US TTH E PARAMETER

S THA TRELAT E T O AI R EMISSIONS FO

R WHICH RECORD

S AR E BEING MAINTAINE D T O DETERMIN E FEES , RUL E APPLICABILIT YO R COMPLIANCE . INCLUD E TH E UNI TO F MEASUREMENT . TH E METHO C O F MEASUREMENT , AN D TH E FREQUENC YO F SUC H RECORD S (E.G. , HOURLY , DAILY , WEEKLY) : PARAMETE R UNITO F MEASUREMENTMETHO D O F MEASUREMEN TFREQUENC Y 

### Proces s data : temperatur e E facto r _ emissio n rat e resi n mi xvolum e 

### degree s F .

realnumber.. . lbs . / hr . lbs . / min . PLC

/ dat a collectio n calculatio n calculatio n PLC / dat a collectio n hourl y

hourl y hourl y hourl y

APPLICATIO N PAG E 21 

### " 5

220-CAAP P FO R APPLICANT S US E
PAG E 5 O F 1 0 

# 7 7P.7 9

T3 $ BRIEFL

YDESCRIBE TH E METHO D B V WHIC H RECORD

S WIL L B E CREATE

D AN D MAINTAINED

. FO R EAC H RECORDE D PARAMETE R INCLUD E TH E METHO D O F RECORDKEEPING . TITL E O F PERSO N RESPONSIBL E FO R RECORDKEEPING , AN D TITL E O F PERSO N T O CONTAC TFO R REVIE WO F RECORDS : PARAMETE R Proces s dat a Supplie r dat a METHO D O F RECORDKEEPIN G electroni c dat

a bas e electroni c dat

a bas e TITLEO F

PERSO N RESPONSIBL E Syste m Administrato r 

## Mi xSuperviso r nTLEO F CONTAC TPERSO N EnvVSafet

y Eng . Env./Safety Eng .

c ) I S COMPLIANC

E OF TH E EMISSION UNI TREADIL YDEMONSTRATE

D B V REVIE WOF TH E RECORDS ? I F NO , EXPLAIN : X X YE S 

# • N O

d ) ARE AL

L RECORD

S READIL YAVAILABL

E FO R INSPECTION , COPYIN

G AN D SUBMITTA L T O TH E AGENC YUPO N REQUEST ? I F NO , EXPLAIN : X X YE S N O

54a ) DESCRIBE AN

V MONITOR

S O R MONITORIN

G ACTIVITIE

S USE D T O DETERMIN E FEES. RUL E APPUCABIUT

V OR COMPLIANCE : ... .

N/ A

b ) wHA

TPARAMETER^

) IJ>(AkE ) BEIN G MONITORED 1 (E.G. , VO M EMISSION S T O ATMOSPHERE) ? 

## N/ A

c ) BESCRIBE TH E LOCATIO N OF EAC

H MONITO

R (E.G. . I N STAC

KMONITO

R 3 FEE TFRO M EXIT) : 

## N/ A

APPLICATIO N PAGE .

220-CAAP P 

## 2.1- 6 PAG E 6 O F 1 0



# 7 *P.8 0

54d ) I S EAC H MONITO R EQUIPPE D WIT H A RECORDIN G DEVICE ? I F NO . LIS TAL L MONITOR S WITHOU TA RECORDIN G DEVICE : 

## N A YE S N O

e ) I S EAC H MONITO R REVIEWE D FO R ACCURAC YO N A TLEAS TA QUARTERL

YBA515 7 I F NO , EXPLAIN : 

## N A YE S N O

1 5 I S EAC H MONITO R OPERATE D ATAL L TIME S TH E ASSOCIATE D EMI5SIO N UNI T I S I N OPERATION ? I F NO . EXPLAIN : 

## N A 

# • YE S N O

3 5 PROVID E INFORMATIO N O N TH E MOSTRECEN TTESTS . I F ANV . I N WHIC H TH E RESULT S AR E USE D FO R PURPOSE S O F TH E DETERMINATIO N O F FEES . RUL E APPLICABILIT YO R COMPLIANCE . INCLUD E TH E TES TOAT E TES TMETHO D USED , TESTIN G COMPANY , OPERATIN G CONDITION S EXISTIN G DURIN G TH E TES TAN D A SUMMAR YO F RESULTS . I F ADDITIONA L SPAC E I S NEEDED , ATTAC H AN D LABE L A S EXHIBI T2204 : TESTDATE 

## 4/28/9 2 TES TMETHO D TESTIN G COMPAN Y 

## 1 8 OPERATIN G CONDITION S 

## Almeg a Maximu m SUMMAR YO F RESULT

S Complianc e

36 ) DESCRIB E AL L REPORTIN G REQUIREMENTS AN D PROVID E TH E TITL E AN D FREQUENCV O F REPORT SUBMITTAL S T O TH E AGENCY : REPORTIN G REQUIREMENT S TITL E O F REPOR T FREQUENC Y 

## VO M emissio n rat e VO M emission s Name , ID# , VO M conten t 

## Lin e emission s Annua l emission s repor t 

## Mi xrepor t annua l

annua l annua l

APPLICATIO N PAGE ;

220-CAAP P 

## 2.1-7 PAG E 7 O F 1 0



# 7 ?^ ^ REGULATE D AI R

POLLUTAN T
CARBO N MONOXID E (CO )
LEA D

NITROGE N OXIDE S (NOx )
PARTICULAT E MATTE R (PART ) PARTICULAT E MATTE R <-1 0 MICROMETER S (PM10 ) SULFU R DIOXID E (S02 ) VOLATIL E ORGANI C MATERIA L (VOM ) OTHER , SPECIFY : EXAMPLE: " PARTICULATE MATTER MAXMUM :

TYPICA L MAXMUM : TYPICAL : MAXMUM ; TYPICAL : MflXIMI M TYPICAL : MAXMUM : TYPICAl : MAXMUM : TYPICAL : MAXMUM : TYPICAL : MAXIMHM " TYPICAL :
MAXMUM : TYPICAL ; X

. HOU R (LBS/HR )

23.0 1 8.37 4

SOO 4.00 " ' '!'• " tf WEMttS/fi A INF6RUATI6N

- , ACTUA L EMISSIO N RAT E •UNCONTROLLE D EMISSIO N RAT E ION S f fcH YEA R (TONS/YR )

86.2 8 19.8 3

2f. 9 f«. 4 \>THE R

TERM S 1

i !

! | 

## i I

— ; ftj " GRA3SCF : 0.2 4 GR/DSC F MOTHE R

TERM S "D M

1 5 .

i 4 ALLOWABL E B YRUL E EMISSIO N RAT E

8 RAT E (UNITS )

8 lb/h r (x3 )

6.0 (LBS/HR) 5.5 (LBS/HR) APPLICABL E RULE S

218.30 1

212.321 212.321 YEA R

(TONS/YR )

.

3 0 (x3 )

26.2 8 19.60 'PERMITTE D EMISSIO N RAT E

RAT E (UNITS )

23.0 1 lbs/hr . * *se e exhibi t 220- 6

5.5 LBSMR TONSPE R YEA R (TONS/YR )

86.2 8 *

22
IMPORTANT : ATTAC H CAl_CUU-nON8 . T O TH E EXTEN T THEY AR E A«EMISSICi4SRE-_ATED , O N V^ ^ ^CHEC KUNCONTROLLE D EMISSIO N RAT E BO XI F CONTRO L EQUIPMEN TI S USED , OTHERWIS E CHEC K AN D PROVlO E TH E ACTUA L EMISSIO N RAT E T O ATMOSPHERE , INCLUDIN G INDOORS . SE E INSTRUCTIONS . W>\flO £TH E ILMISSIO N RAT E THA TWI U B E USE O A S A PERO TSPEClALi^ ^ THI S LBM TWIL L B E USE D T O DETERMIN E TH E PERMI TFEE . -"PLEAS E PROVlO E AN YOTHE R EMISSIO N RAT E WHIC H I S COMMONL YUSED . REQUIRE D B V A SPECIFI C LIMITATIO N O R THA TWA S MEASURE D (E. a PPM . GR/DSCF . ETC. ) <O M - DETERMINATIO N METHOO : 1 ) STAC KTEST . 2 ) MATERIA L BALANCE . 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS) , 4 ) ENQINEERIN O ESTIMATE . S ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS ) -•RAT E - ALLOWABL E EMISSIO N RAT E SPECIFIE O B YMOS TSTRINGEN TAPPLICABL E RUL E APPLICATIO N PAGE . 220-CAAP

P 2.1- 8 FO R APPLICANT S US E
PAG E 8 O F 1 0

0 0

## X i I3B) HAZARDOUS

AIR POLLUTANT

EMISSION

INFORM AT ON HA P INFORMATIO N NAM E O F HA P EMITTE D 

## Styren e (STY

) Methy l (MMA

) Methacrylat e

EXAMPLE: Benzene *^CA S NUMBE R 

## 100-42- 5 80-62- 6

71432 

### E 1 

### ACTUA L EMISSIO N RAT E \_\ UNCONTROLLE D EMISSIO N RAT E POUND S PE R HOU R (LBS/HR ) 

## 2 3 - (MMA ) 5.134 6 23-(STY ) 3.239 1 1
!

i

i

i ! 10.0 

### 6.6 TON S PE R

YEA R (TONS/YR ) 

## 8 6 - (MMA ) 12.61 4 8 6 - (STY ) 7.218 5

•

1.2 

### 6.6 •-bTHE R

TERM S "D M



## 5 5 5 5

2 2 ALLOWABL E B YRUL E

5RAT E O R STANDAR D 

## 8. 0 lbs/h rVO M * se e exhibi t 220- 6 8. 0 lbs/h rVO M * se e exhibi t 220- 6

98 % by wt control device leak-tight trucks APPUCABL E RUL E 

## IA C 218.30 1 IA C 218.30 1

CFH 61 • 61.302(b).(d) IMPORTANT : ATTAC H CALCULATIONS . T O TH E EXTEN TTHE YAR E AI R EMISSION S RELATED , O N VITHIC H EMISSION S ItlTER E DETERMINE D AI 0 U ^ 'PROVID E UNCONTROLLE D EMISSION S ( F CONTRO L EQUIPMEN TI S USED . OTHERWISE . PROVID E ACTUA L EMISSION S T O TH E ATMOSPHERE . INCLUDIN G INDOORS . CHEC KBO XT O SPECIFY . X A S - CHEMICA L ABSTRAC TSERVIC E NUMBE R *PLEAS E PROVlO E AN YOTHE R EMISSIO N RAT E WHIC H I S COMytONL YUSED . REQUIRE D B YA SPECIFI C LIMITATIO N O R THA TWA S MEASURE D (E.G. , PPM . GR/DSCF . ETC.) . ?** » •DETERMINATIO N METHOD : 1 ) STAC KTEST . 2 ) MATERIA L BALANC E 3 ) STANDAR D EMISSIO N FACTO R (AP-4 2 O R AIRS . 4 ) ENGINEERIN G ESTIMATE . 5 ) SPECIA L EMISSIO N FACTO R (NO TAP-4 2 O R AIRS) . -RAT E -ALLOWABL E EMISSIO N RAT E O R STANDAR D SPECIFIE D B YMOS TSTRINGEN TAPPUCABL E RULE . 

## APPUCATIO N PAGE . 220-CAAP P 

## 2.1- 9 PAG E 9 O F 1 0

c oP.8 3



## — : EXHAUST POINT INFORMATION— THI S SECTIO N SHOULD NO

TBE COMPLETED I P LMIS3ION S AR E EXHAUSTED THROUG H AI R POLLUTION CONTRO L EQUIPMENT . m FLO WDIAGRA M DESIGNATIO N O F EXHAUS TPOlNT : 

## PDV-2 : PDV-2 6 46 ) DESCRIPTIO N O F EXHAUSTPOIN T(STACK . VENT . ROO F MONITOR . INDOORS . ETC.) . I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS . D O NO TCOMPLET E TH E REMAININ G ITEMS . 

## ven t 41 ) DISTANC E T O NEARES TPLAN TBOUNPAR VFRO M EXHAUS TPOIN TDISCHARS E (FT) : 

## 23 0 42 ) DISCHARG E HEIGH TABOV E GRAD E (FT) : 45 ) GOO D ENGINEERIN G PRACTIC E (OEP ) HEIGHT . I F KNOW N (FT) : 44 ) DIAMETE R O F EXHAUS TPOIN T(FT) : NOTE : FO R ANO N CIRCULA R EXHAUS TPOINT . TH E DIAMETE R I S 1.12 8 TIME S TH E SQUAR E ROO TO F TH E AREApQy_ 2 (2.66 ) PD V -2 6 (1.70 ) 4S ) EXI TOA S FLO WRAT E 

## PDV- 2 (6950 ) * 46 ) EXI TGA S TEMPERATUR E 

## PDV- 2 (ambient ) *

_ « a ) MAXIMU M (ACFM) :



## N A a ) MAXIMU M ('F) : 

## N A 77 ) DIRECTIO N O F EXHAUS T(VERTICA L LATERAL . DOWNWARD) : 

## Latera l b ) TYPICA L (ACFM) : 

## PDV-2 6 (1350 ) • * b ) TYPICA L ('F) : 

## PDV-2 6 (ambient ) 4fl ) US TAL L EMISSIO N UNIT S AN D CONTRO L DEVICE S SERVE D B VTHI S EXHAUS TPOINT : NAM E FLO WDIAGRA M DESIGNATIO N 

### a T 

## LP- 3 B ) 

## •3T note : al l rate s i n #4 5 an d temp s i n ST 

## #4 6 ar e typica l values
. LP- 3 lin e (PDV-2 ) (PDV-26 )

TH E FOLLOWIN C INFORMATIO N NEE D ONL V B E SUPPUE D I F READIL YAVAILABLE. 

### 48a ) LATITUDE : 

## 41:27:45.000 0 50 ) UT M ZONE : b , LONGITUDE : 

## 88:11:15.000 0 b) UT M VERTICA L (KM ) c ) UT M HORIZONTA L (KM) :



## APPLICATIO N PAGE 2 

## - 1 

## " 1 0 220-CAAP P PAG E 1 0 O F 1 0

&P.8 4



### " EXHAUST POINT INFORMATION THIS SECTION SHOUL

D NO TBE COMPLETE D I F EMISSION S ARE EXHAUSTED THROUG H AIR POLLUTIO N CONTRO L EQUIPMENT

. ii) FLOWDIAGRA M DESIGNATIO N O F EXHAUSTPOINT : PDV- 3 PDV-2 5 46 ) DESCRIPTIO N O F EXHAUS TPOIN T(STAC KVENT . ROO F MONITO R INDOORS . ETC.) . I F TH E EXHAUSTPOIN T DISCHARGE S INDOORS . D O NOTCOMPLETE TH E REMAININ G ITEMS . 

## * y Ven t DISTANC E T O NEARES TPLAN TBOUNDARYFRO M EXHAUSTPOIN TDI5CHAR5 E (FT) : 23 0 42 ) DISCHARG E HEIGH TABOV E GRAD E (FT) : 43 ) G?S D 

### ENGINEERIN G PRACTIC E (GEP ) HEIGHT , I F KNOW N (FT) : 44 ) DIAMETE R O F EXHAUS TPOIN T(FT) : NOTE : FO R A NO N CIRCULA R EXHAUSTPOINT . TH E DIAMETE R I S 1.128TIMESTHESQUAREROOTOFTHEAREApQY. 3 /n QQ) PDV-2 5 (1.70 ) 45 ) EXI TGA S FLOWRAT E PDV- 3 (695 0



# 2 L ITD F Ai) EXI TGAS TEMPERATUR E PDV- 3 (ambient ) a ) MAXIMU M (ACFM) : N A a ) MAXIMU M ('F) : N A b) TYPICA L (ACFM) : PDV-2 5 (1350 ) b) TYPICA L (T) : PDV-2 5 (ambient ) 77 ) DIRECTIO N O F EXHAUS T(VERTICA L LATERA L DOWNWARD): — latera l 46 ) US TAL L EMISSIO N UNIT S AN D CONTRO L DEVICE S SERVE D B VTHI S EXHAUSTPOINT : 

# I NAM E FLO W DIAGRA

M DESIGNATIO N 

## I T LP- 6


# -sr * note : al l rate s i n #4 5 an d temp s i n •5 7 #4 6 ar e typica l values . LP- 6 lin e (PDV-3 ) (PDV-25 )

THE FOLLOWIN

C INFORMATIO

N NEE D ONL V B E SUPPUE

D I F RLADIL

V AVAILABLE

. 

### 45a ) LATITUDE : 

## 41-27-4 5 56 ) UT M ZONE : b) LONGITUDE : 88-11-1 5 b)UTMVERTICAL'(KM) : c) UT M HORIZONTA L (KM) :

APPLICATIO N PAGE 2 

### - 1 

### " 1 1 220-CAAP P PAG E 1 0 O F 1 0



# £ SP.8 5



### EXHAUST

POINT INFORMATION THI S 5ECTI0 N SHOULD NO

TB E COMPLETED I F EMISSIONS AR E EXHAUSTED THROUG H AI R POLLUTIO N CONTRO L EQUIPMENT . ii) FLO WDIAGRA M DESIGNATIO N O F EXHAUS TPOINT : 

### PDV- 5 PDV- 6 PDV-1 2 40 ) DESCRIPTIO N O F EXHAUSTPOIN T(STACK . VENT . ROO F MONITO R INDOORS . ETC.) . I F TH E EXHAUS TPOIN T DISCHARGE S INDOORS . D O NO TCOMPLET E TH E REMAININ G ITEMS . 

### ven t 41 ) DISTANC E T O NEARES TPLAN TBOUNDAR V FRO M EXHAUS TPOIN TDISCHARG E (FT) : 

### 23 0 42 ) DISCHARG E HEIGH TABOV E GRAD E (FT) : 43 ) GOO D ENGINEERIN G PRACTIC E (GEP ) HEIGHT . I F KNOW N (FT) : 44 ) DIAMETE R O F EXHAUS TPOIN T(FH : NOTE : FO R A NO N CIRCULA R EXHAUS TPOINT . TH E DIAMETE R I S 1.12 8 TIME S TH E SQUAR E ROO TO F TH E AREApQ^. 5 (- j 7 ) p[)\/- 6 (2.25 ) PDV-1 2 (1.6 ) 45 ) EXI TGA S FLO WRAT E 

### PD V j (3600) i * a ) MAXIMU M (ACFM) : 

### PDV- 6 <" innn m 

### * b ) TYPICA L (ACFM) : 

### PPy-1 2 (300 ) * 4S ) EXI TGA S TEMPERATUR E 

### PDV- 5 (ambient ) * (10000 ) a ) MAXIMU M ('F) : 

### PDV- 6 (ambient ) b ) TYPICA L ( 5 F) : 

### PDV-1 2 (ambient ) * 77 ) DIRECTIO N O F EXHAUS T(VERTICAL . LATERAL . DOWNWARD) : 

### latera l 46 ) US TAL L EMISSIO N UNIT S AN D CONTRO L DEVICE S SERVE D BV THI S EXHAUS TPOINT :

NAM E FLO WDIAGRA M DESIGNATIO N 

### LP- 7 

## W note : al l rate s i n #4 5 an d temp s i n 

## er #4 6 ar e typica l values . LP- 7 lin e (PDV-5 ) (PDV-6 ) ( PDV-12 )

TH E FOLLOWING INFORMATION NEED ONL V B E SUPPLIE D I F READIL

YAVAILABLE

. 49a ) LATITUDE : 

## 41-27-4 5 56) UT M ZONE : b ) LONGITUDE : 

### 88-11-1 5 b ) UT M VERTICAL '



### IRH F c ) UT M HORIZONTA L (KM) :



### APPLICATIO N PAGE 2 

### - 1 

### " 1 2 220-CAAP P PAG E 1 0 O F 1 0 

# mP.8 6



## 197800AA X Cran e Kemlit e Exhibi t_22Q__1 _ Long pane l lin e Usag e Th e manufacturin g compute r syste mcontrollin g th e Un e create s aLin e Usag e repor t for th e resi nmi x an dothe r ra w materia l usag e fo

r eac hpane l line . Th e recor dinclude s date , time , produc t type , an dtotalize dvalues (weigh t o r othe r amount ) for

material s delivere dt o th e line . Exhibi t 220-1 A attache di s a nexampl e o f thi s report .

Applicatio n Pag e 2.2- 1



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## 197800AA X Cran e Kemlit e Exhibi t220- 5 & 6 Lon g Pane l lin e Emission s Calculation s Th e compute r

controllin g th e operatin g parameter s of eac hlin e calculate s a n operatin g facto r

(K) , emissio nrat e ( EH

R, a s lbsThr.VOM) , an dtotalize dVO M emission s fo r

eac hhou r

of operation . Th e operatin g parameter s use di nth e calculatio ninclud e th e resi nflow volum e (MRF : mas s fee drate ) an dresi n temperatur e (T) . Th e mi x roo memissio ncalculatio nvalue s for Styren e %, Methy l Methacrylat e (MMA

) %, Styren e mol e fraction, an dMM A mol e fractionfo

r th e mi x typ e processin g o nth e lin e ar e electronicall y passe dint o th e dat abas e a s variable s for

calculatin g th e lin e emission s o f tha t mi x (product ) type . Th e hourl y rat e i s monitore db y th e compute r t o war na noperato r

if th e rat e approache s th e maximu mrate . Th e totalize demission s ai*e th e cumulativ e tota l o f th e rat e fo

r eac hhou r

of operation . Th e emissio nrat e i s calculate dbase donth e following : EH Ra s ( K * 7.6 7 lbs . pe r

hr. ) / ( 20,10 4 lbs . monome r

* m mH g pe r

hr. ) Where : e 

### EJJ H 

## = Hourl y VO

M emissio nrat e K = Hourl y operatin g facto r a s define dbelo w '7.67 = Th e maximu mhourl y emissio nrat e 20,10 4 = Th e maximu moperatin g factor Th e totalize demission s ar e calculate da s acumulativ e tota l of th e rat e fo

r a nhou r of operatio na s demonstrate dbelow : E-fc t = ( ( E m* (t j - t

^ ) ) / 36(00 ) + E ^ Where : • E ^ = Cumulativ e emission s (lbsThr. ) EJJ R

## = Hourl y VO

M emissio nrat e '''''''t£'''-''t2 

## ''''-'' : 

## elaps'ed''tim'e'(seconds)' ' 360 0 = second s i na nhou r Eac hhou r

E ^ i s recorde dan dreinitialize dt o zero fo r ane w tota l calculation .

Applicatio n Pag e 2.3- 1 

# £ 7—: . P.8 9



## Maximu mlon g panel lin e emission s ar e base dupo nth e followin g assumptions : 1 . Styren e monome

r an dmethy l methacrylat e ar e th e only material s presen t i n th e lon g panel line s VO

M emissions . / 2 . Styren e monome r an dmethy l methacrylat e ar e th e only polyeste r resi n ( mixture constituent s wit happreciabl e partia l pressures . 3 . Partia l pressur e an

dmonome r (i.e.,styren e monome

r an dmethy l methacrylate ) mass feed rat e are directl y proportiona l t o VO M emissions . 4 . Th e scenari o fo r

maximizin

g emission s i s define db y maximizin

g polyeste r resi nmixture proces s partia l pressure , an dstyren e monome

r an dmethyl methacrylat e feedrates . Th e operatin g factor , base d upo n productio n temperature s an d mas s fee d rate , an d utilizin g Raoult' s la

wan d Antoine' s Equatio

n i s derived a

s follows :
* 4 

## Raoult' s Law

:

- " P i - X i * VP f Where : 

## P- i «* » Partial pressur

e o f componen

t"i " i n th e polyeste rresi n mixtur e X* j « Mol e fractio n of

componen

tm 

## \ m 

## i n th e polyeste rresi n mixture VP < • Vapo

rpressur e of componen

t"1 " a tth e resi n feed temperatur e 1 - Styren

e and/ormethy

l methacrylate (Molecula rWeigh tStyren e - 104.1 1 lb/lb-mole ) " (Molecula

rWeigh to f Methy l Hethacrylat

e - 100.1 1 lb/lb-mole )
« 

## Antoine' s Equation : logi o V P - A - B/(C+T ) 

## Where : V P- Vapo rpressur e o f th e specifie d polyeste rresi n mixtur e constituen ta tth e resi n mixtur e proces s feed temperature . A , B , , & C • Constant

s eithe robtaine d fro

m th e literatur e orderive d throug h use of acompute

rgenerated curv

e fittin g program

. T - Specifie d resi n mixture proces s feed temperatur e (*C) . Antoin e Equatio

n Constants Styren e (CaHg

) Methy l Methacrylat

e (C5H

8 

## 0 2 

## ) A 6.9240 9 10.31 1 B

1420. 0 3764. 0 

# c

# ""•

" 206 406.45 4 •
• 

## Th e operatin g facto r(K

) i s th e su

m o f th e produc

to f the individual monome

r mas s fee d rat e (MFR-j

) an d th e individua l monome

rpartial pressur

e (P-j ) o f th e polyeste rresi n mixture .

K- «£(MFR

f * 9\) (poun

d monome r* m m H g pe rhour ) Applicatio n Pag e 2.3- 2P.9 0 T'r. U NC V 5 :i:4S:5 6 *.39 5 _ • se-ec c * frc m«pa_emiss_ 3 

### Exhibi t220-5& 6 Ipr3d_:;emissio n ; hour s j 3OC30 9 j 30032 4 J300332 1 53.395 1

0.463 1 2.229 1 22.94 8

0.16 5 0.80 S

. 3 rows ) En d o f Reques t

_VV,,, Vrxxia\\..Vl..a\') 199 5 l > selec c sum(emission) , sum(hours ) fro m epa_emiss_ 3 |col l |col 2 I ] 6i"687i " 23.918 | ( 1 row ) En do f Reques t

_Th u No v

9 ll:48i4 1 199 5 _ 1 > selec t * fro

m epa_emiss_ 6 prod_c|emissio n|hour s 60060 0 18.52 2 11.38 2 60060 6 16.05 0 7.13 8 60069 0 8.17 4 3.02 6 ( 3 rows ) En do f Reques t Th uHo v

9 11:49=1 1 199 5 1 > selec tsum(emission) , sum(hours ) fro m epa_emiss_ 6 |col l |col 2 | l " 42.747 | 21.S46 | • + . • ( 1 row ) En do f Reques t
Th uNo v

9 11:49:5 2 199 5 1 > selec c * +..... . + ..... . .....4.... . |prod_c|emis s io n|hour s 70031 7 70060 6 70097 2 10.719 1

12.53 5 9.12 4 5.91 7

5.77 0 1.90 9 ( 3 rows ) En do f Reques t fro m epa_eraisa_ 7

Th uNo v

9 11:50:1 5 199 5 1 > selecc.sum(emisaion) , sum(hours ) fro m epa_emisa_7 ' I col l |co! 2 | 32.378 | ( 1 row ) En do f Reques t 13.596 |



### Applicatio n Pag e 2.3- 3 

# 29P.9 1



## ID#197800AA

X Cran e Kemlit e Exhibi t220- 5 & 6 Rational e fo

r Form22 0 Proces s Emissio nUnit : LP-3 , LP-6 , LP- 7 Fo r purpose s o

f utilizin g optimu mflexibility , Kemlit e ha s presente dth e thre e line s a s on e emissio npoint . Th e typica l operatio no f thes e line s ha s adistributiv e rathe r tha ncumulativ e effect : ie. ) i f on e lin e run s more , anothe r run s less . T o avoi drestrictin g th e capacity of an y on e line , Kemlite propose s acontro l strateg y tha t woul doperat e th e thre e line s collectivel y unde r a naggregat e emission s cap equa l t o atota l les s tha nth e maximu mindividua l allowabl e rate s fo r eac h line.Thi s strateg y woul dremov e th e individua l emissio nlimit s fo r eac hUne . forample! 

## Curren t maximu mallowabl e emissio nrat e fo r LP- 3 lin e = x = 8 lbsVhr . Curren t maximu mallowabl e emissio nrat e fo r LP- 6 lin e = y = 8 lbsVh r Curren t maximu mallowabl e emissio nrat e fo r LP- 7 lin e -

= z = 8 lbsVh

r Tota l =

* 2 4 lbs/hr . Note : 8 lbsVhr . fromIAC 218.30 1 Curren t operatin g permi t

limi t i s 7.6 7 lbsVhr . pe r

line ; 23.0 1 lb s total . Thi s permi t

applicatio npropose s maximu mtota l allowabl e emission s o f 23.0 1 lbsVhr . usin g th e followin g formulas : ( x , y , z value s ar e lbsVh

r VO M ) LP- 3 lin e = x =*

• 23.0 1 - ( y + z ) LP- 6 lin e = y = 23.01- ( x + z ) LP- 7 lin e = z = 23.01- ( x + y ) Tota l s ax + y + z = 23.0 1 lbsVhr Th e us e of

a nemission s capL_unde

r tMscon^ l strateg y woiil dallo w th e Une s t o operat withi nth e variable s ofth e function s ofth e emissio ncalculation : resi nvolume , monom t content , an dtemperature . A s state di nth e proces s descriptio nfo r th e pane l Unes , th e compute r contro l o f lin e parameter s woul dmonito r th e propose dcalculation s continuousl y t o assur e tha t th e maximu mhourl y Umi t aggregat e tota l i s no t

exceeded . Th e propose dcap i s fo

r th e combinatio nof

Styren e an dMethy l Methacrylat e monome x emission s i nth e tota l Umi t fo r VOM lbs/hr . Th e combinatio no f emission s fo

r Styren e an dMethy l Methacrylat e wil l no t excee dth e Umi

t total .
Applicatio n Pag e 2.3- 4 

# 90P.9 2



### Crane Kemlit

e 197800AA

X 

### Exhibi t220 - 8 Complianc e with th e requirement s o f 3 5 111 . Adm . Cod e Par

t218.66 0 ( Subpar

tCC ) i s met as follows : • Al l buton e typ e o f polyeste rresi

n materia l mixture use d meets th e criteri ao f 218.66 6 (a)(l)(A)(v ) (ie.) .. . amonomercontento f n o mor e tha n 35 % b y weigh tas applied . • Th e on e othermixture typ e (lightweigh tfillermodifie d resin) meet s th e criteri ao f

218.66 6 (a)(1)(C ) (ie.) Us e vapo rsuppressed polyeste rresi n approved b y th e Agenc y in th e source' s penni tsuch tha tweigh tlos s fro

m VO M emission s doe s no texcee d 6 0 grams persquar e metero f

expose d surfac e areaduring molding ; I hav e include d calculatio n results t o suppor tthi s determination o n the nextpag e o f Exhibi t220-8 .

Applicatio n Pag e 2. 4 - 1



# 91P.9 3



### Cran e Kemlite 197800AA X 

## Exhibi t220- 8 Lightweigh t

Fille r Modifie dResi nCalculation s (Resi nmi x i nexces s of

35 % VO M conten t

a s appUed ) Background ; .• • Th e histor y of

thi s resi nmi x wa s presente dfo r th e renewa l o

f th e previou s permit . SpecificaUy , thi s mi x ha s th e sam e volume percentag e o f monome r conten t a s th e coronary typ e tha t

doe s no t hav e th e Ughtweight

filler added . Bu t

becaus e ofth e weigh t differenc e i nth e fiUers, th e tota l weigh t percen t o f a U th e ingredient s i s shifte di nrelatio nt o eac hothe r i ntota l weight . Th e Ughtweight filler modifie d mi x ha s a naverag e monomer conten t (b y weight ) o

f 41% . Sinc e thi s figure wil l no t satisf y th e criteri afo

r Subpar t CC , 218.66 6 a.lA.v . (ie.) ".. . les s tha n35 % b y weight..." , i t

wa s discusse dwit hMr . Davidso n(IEPA ) tha t emission s calculation s coul dsatisf

y th e criteri afo

r Subpar t CC , 218.66 6 a.l.C . "...tha t weigh t los s from VO M emission s doe s no t

excee d6 0 gram s pe r

squar e mete r

o f expose dsurfac e area... " Th e followin g calculation s demonstrat e compUanc e wit hSubpar t CC , 218.66 6 a.l.C : Emission s Calculations ; A tabl e wa s prepare dusin g th e emission s calculation s include din , operatin g permit , ( se e pag e 2. 4 -3) . Varyin g temperature s and(Hn e ratesj use dt o creat e thi s EFacto r emission s table . Th e maximu m EFacto r calculate di s 6.9 6 lb/hr . a t 95 ° F . an d22 0 inVmin . fo r a n8 ft. wid e panel . Thi s i s converte dt o grams/meter 2 

## i nth e following calculation . 

# g.96 Ih . x m x Ibr

, x _l

_x 12

m x _teg x ift 2

# = 3 . hr . 22 0 in . 6 0 min . 8 ft. ft. lib . .0929m2 

## Th e value"o f

3. 9 g/m2 

## i s significantl y les s tha nth e 6 0 g/m 2 

## aUowedi nSubpar t

GG;T ] resul t shoul dsatisf

y th e criteri aspecified .

( AppUcatio n Pag e 2. 4 - 2 

# 92P.9 4 

### Exhibi t 220- 8 Th e E Factor calculatio n yield s the following results : Mi x Temperatur

e 

### (°F ) 

## 8 0 8 1 8 2 8 3 8 4 8 5 8 6 8 7 8 8 8 9 9 0 9 1 9 2 9 3 9 4 9 5 0.060 "

Pane l 1.990 2.05 8 2.12 7 2.19 9 2.27 3 2.34 9 2.42 7 2.50 7 2.59 0 2.675 2.76 2 2.85 1 2.94 3 3.03 8 3.135 323 5 E Factor (lin e rat e constan t a t 22 0 ipm ) 0.070 " Pane l 2.41 9 2.50 1 2.586 2.673 2.763 2.855 2.95 0 3.048 3.148 3.25 1 3.357 3.466 3:57 8 3.69 3 3.81 1 3.933 0.080 "

Pane l 2.85 7 2.95 4 3.05 5 3.15 8 3.26 3 3.372 3.485 3.60 0 3.71 8 3.84 0 3.965 4.09 4 4.22 6 4.36 2 4.50 2 4.645 0.085 "

Pane l 2.985 3.087 3.19 1 3.29 9 3.40 9 3.52 3 3.64 0 3.76 1 3.885 4.01 2 4.14 3 4.277 4.41 5 4.55 7 4.70 3 4.85 3 0.100 '

Pane l 3.63 3 3.75 7 3.884 4.01 5 4.15 0 4.28 8 4.43 1 4.577 4.72 8 4.88 3 5.042 5.206 5.37 4 5.547 5.72 4 5.906 0.115 "

Pane l 4.28 1 4.42 7 4.57 7 4.73 1 4.89 0 5.05 3 5.22 1 5.39 4 5.57 1 5.75 4 5.94 1 6.13 4 6.33 2 6.53 6 6.74 5 6.96 0

Applicatio n Pag e 2.4- 3 

# 9%