## APPENDI X C FIGURE SSTACK-2
- • LIM ESIL O SPEN T LIM E RECOVER Y 

# x x l l i l l I X



## < .

x < EQUIPMEN T

STORAG E BLD G NORT H EN D

MAINTENANC E SHO PBLD G 

# d E g o o S " i g^ * UNI T 2 UNI T CRUSHE D DRU M 4 TRAILE R' • MP- 2 DRUMCRUSHE R 

# L Z P DRU M STORAG E1 A TAN K 8 TAN K 6

DRU M STORAG EI B SUPPLIE S STORAG E a Om O



# D 2 4 

## a D 3 0 2 0 1 0 

# O O O E B B

GAT E HOUS E
ADMINISTRATIV EOFFICE S BUL K TANKE RUNLOADIN G 10.6m mBTU/h r BOILE R—

VEHICL EREFUELIN G 

## ARE A"A " SIT E MA P -TAN K 10 0

10.6m m BTU/h r BOILER iPROPOSED )

SCALE : 1 " 30

"

SIT E MA P SCAL E l"=80f! ' 

# FIGUR El a FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward-Clyd e Consultant s SHEET 1 O F 4 

# SCHREIBE R Q YONLE Y (X , ASSOCIATE S 

# FIGUR El a FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward-Clyd e Consultant s APPROX . SCALE : NON E 

# SCHREIBE R Q YONLE Y (X , ASSOCIATE S CHECKE D BY> DRAW NBY : DAT EDRAWN i PROJEC T ft : REVISIO N * ENVIRONMENTA L ENGINEER S 

# KM S BAH 04-20-0 7 070063

# B
X X X X X I I I I I I I I I 

## T-r T SALVAG E YAR D EQUIPMEN T STORAG E NON-HAZARDOU S STORAG EUNI T EXPLOSIV EMAGAZIN E
DRU M STORAG E UNI T N o 2 BUILDIN GC DRU M STORAG ELA B UNI T N o 2 PAC K BUILDIN GB REPAC K DRU M STORAG E UNI T N o 2 BUILDIN GA



# J " TRUC K SCAL E



# B TRAILER S • TRANSFORME R

ARE A "ff

SIT EMA P FUE L TANK S PARKIN G

WATE RTAN K
PORTABL EBOILE R 

### ELECTRICA

L SCAL E 1 " - 3B '



### SIT E MA P SCAL E r=8ea * 

# xn :



# FIGUR El b FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward—Clyde Consultant s SHEE T 2 O F 4 

# SCHREIBE R C > YONLE Y O C ASSOCIATE S 

# FIGUR El b FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward—Clyde Consultant s APPROX . SCALE : NON E 

# SCHREIBE R C > YONLE Y O C ASSOCIATE S CHECKE D BY ' DRAW NBY . DAT EDRAWN r PROJEC T S i REVISIO N8 ENVIRONMENTA L ENGINEER S 

# KMS BA H 04-20-0 7 070063 -

## ARE A * C SIT E MA P SCAlf i 1" m 3g

SIT EMA P SCAL E 1"=6B0

' 

# FIGUR El c FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward—Clyde Consultant s SHEE T 3 O F 4 

# SCHREIBE R O YONLE Y 

# (3C ASS0CIATE S 

# FIGUR El c FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward—Clyde Consultant s APPROX . SCALE : NON E 

# SCHREIBE R O YONLE Y 

# (3C ASS0CIATE S
CHECKE D BY< DRAW NBY . DAT EDRAWN . PROJEC T # i REVISIO N# ENVIRONMENTA L ENGINEER S 

# KM S BA H 04-20-0 7 070063 -

# D LIM ESIL O



# x x



# D AI RPOLLUTIO NCONTRO LEQUIPMEN T • BH 1 • BH 2 • C I

SIT EMA P SCAL E 1"=B0B 

# FIGUR EI d FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward-Clyd e Consultant s SHEE T 4 O F 4 

# SCHREIBE R O YONLE Y O C ASSOCIATE S 

# FIGUR EI d FACILIT Y LAYOU T VEOLI A ES ; SAUGET , I L Base d o n Figur e b y Woodward-Clyd e Consultant s APPROX . SCALE : NON E 

# SCHREIBE R O YONLE Y O C ASSOCIATE S CHECKE D BY i DRAW NBY ' DAT EDRAWN . PROJEC T # . REVISIO Nft ENVIRONMENTA L ENGINEER S 

# KM S BA H 04-20-0 7 07006 3STORAG ETANK S BLEN D TANK S

p a 

### a

u a LIQUI D WAST EFEE D

TAN K #1 0 C12 a 86 9 GAL ) I | [ CARBO N CANISTERCS ) «1 0 LIQUI D WAST EFEE D TAN K ttHO C12,B6 9 GAL ) | 1 CARBO N CANISTERCS ) «2 D LIQUI D WAST EFEE D TAN K «3 0 C12,BG 9 GAL ) | [ CARBO N CANISTERCS ) 83 0
LIQUI D WAST EFEE D TAN K 84 0 C12,B6 9 GAL ) If— | CARBO N CANISTERCS ) #4 0 LIQUI D WAST EFEE D TAN K 85 0 (12,86 9 GAL ) L__ j [ CARBO N CANISTERCS ) §5 0
LIQUI D WAST EFEE D TAN K 36 0 C12,B6 9 GAL ) T - ] CARBO N CANISTERCS ) 86 0 LIQUI D WAST EFEE D TAN K 8 2 C4,93 1 GAL ) | 1 CARBO N CANISTERCS ) # 2 LIQUI D WAST EFEE D TAN K « 4 C4.93 1 GAL ) [ [ CARBO N CANISTERCS ) #4

LIQUI D WAST EFEE D TAN K 8 6 C7,20 0 GAL ) IT— | CARBO N CANISTERCS ) 8 6
LIQUI D WAST EFEE D TAN K 8 8 C5,2B 0 GAL ) | 1 CARBO N CANISTERCS ) 8 8 INCINERATIO N UNIT S # 2 & # 3
FUE LOI L No . 2 TAN K #100 C9,1S 0 GAL ) 

### ClnslgnlFlcan

tactivity )


# FIGUR E2 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L TAN K FAR M # 1 Base d o n Figur e b y Woodward—Clyd e Consultant s 

# SCHREIBE R YONLE Y ASSOCIATE S CHECKE D BY i DRAW NBY i DAT EDRAWN ' PROJEC T # i ENVIRONMENTA LENGINEER S 

## K S BA H 04-19-0 7 07006 3STORAGE/BLEN D TANK S LIQUI D WAST EFEE D TAN K 830 0 (30,00 0 GAL ) 1 1 CARBO N 1 ICANISTER(S ) 830 0 LIQUI D WAST EFEE D TAN K 830 0 (30,00 0 GAL ) 1 1 CARBO N 1 ICANISTER(S ) 830 0 1 1 CARBO N 1 ICANISTER(S ) 830 0 LIQUI D WAST EFEE D TAN K 830 2 (30,00 0 GAL ) 1 1 CARBO N 1 1 CANISTERCS ) #30 2 LIQUI D WAST EFEE D TAN K 830 2 (30,00 0 GAL ) 1 1 CARBO N 1 1 CANISTERCS ) #30 2 1 1 CARBO N 1 1 CANISTERCS ) #30 2 LIQUI D WAST EFEE D TAN K 830 4 00,00 0 GAL ) 1 1 CARBO N 1 1 CANISTERCS ) 830 4 LIQUI D WAST EFEE D TAN K 831 H (12,00 0 GAL ) I | 1 CARBO N CANISTERCS ) 831 2 LIQUI D WAST EFEE D TAN K 831 4 C12,00 0 GA D | j CARBO N CANISTERCS ) 831 4
FUE LOI L TAN K 839 0 C30,00 0 GAL ) LIQUI D WAST EFEE D TAN K 830 6 C30,00 0 GAL ) | [CARBO N CANISTERCS ) 830 6 LIQUI D WAST EFEE D TAN K 330 B (30,00 0 GAL ) | J CARBO N CANISTERCS ) 830 8 INCINERATIO N UNI T 8 4
LIQUI D WAST EFEE D TAN K 831 0 (30,00 0 GAL ) l [ 1 CARBO N CANISTERCS ) 831 0


# FIGUR E3

PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L TAN K FAR M # 3 Base d o n Figur e b y Woodward—Clyd e Consultant s 

# SCHREIBE R -YONLE Y
, ASSOCIATE S CHECKE D BY ' DRAW NBY ' DAT EDRAWN ' PROJEC T 8 1 ENVIRONMENTA LENGINEER S 

## K S BA H 04-19-0 7 07006 3OPE NVEN T

OUTLE T FLANG E TEMPERATUR E GAUG E FLAM E

ARRESTE R CARBO N CANISTE R VEN T W/RAINSH1EL D

CARBO N CANISTE R

2 " NP T MAL E FITTIN G OUTLE T FLANG E 

# FIGUR E4 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L TAN K T O CARBO NCANISTE R Base d o n Figur e b y Wood-ward—Clyde Consultant s 

# SCHREIBE R YONLE Y ASSOCIATE S CHECKE D BY

< DRAV NBY
- DAT EDRAWN ' PROJEC T ii > ENVIRONMENTA LENGINEER S 

## KS BA H 04-19-0 7 07006 3Specialty ] | WaBt e „Feede r Secondar y Fue l Storag e Tan k



### Relie f Stac k

Natural Gas Secondary^ ) ^ Fuel Secondary Fue l (Hazardou s Wast

e Derived Fuel )

Primary Fue

l (Naturo l Gaa ) , _Wate r Lime Slurr

y

Dro p Ou t Chambe r

Drumme d Solid s Stagin g Are a Enclose d Conveyors I.D . Fa n 

# V I To Pneumati c Tanke rTruc

k 

# FIGUR E5 

# SCHREIBE R PROCES S FLO WDIAGRA M 

# O r 

# YONLE Y VEOLI A ES ; SAUGET , I L r 

# YONLE Y INCINERATO RUNIT S 2 & 3 ASSOCIATE S Base d o n ]

Figur e b y Woodward—Clyd e Consultant s CHECKE D BY

< DRAW NBY i DAT EDRAWN . PROJEC T 11 . ENVIRONMENTA LENGINEER S 

## KS BA H 04-19-0 7 07006 3Lim e Slurr y Spent(Partiall

y Reacted ) Lime
AuxUlor v Gravit y Foo dRa mFoe d Containerize dContainerize d Solid s Solid s

Hig hBt u Liqui d Temperin g Aa h Ai rPollutio n Contro l Residue (Spen tLime )



# FIGUR E6 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L INCINERATO RUNI T 4 Base d o n Figur e b y Wood-ward—Clyde Consultant s 

# SCHREIBE R YONLE Y ASSOCIATE S CHECKE D BY i DRAW NBY i DAT EDRAWN i PROJEC T « i ENVIRONMENTA LENGINEER S 

## KS BA H 04-19-0 7 07006 3CONTAINERIZE D SOLI D WAST E INER T ABSORBEN T

CONTAINERIZE D SOLI D WAST E

INER T ABSORBEN T



### _ J

CONTAINERIZE D SOLI D WAST E

INER T ABSORBEN T VOLATIL EORGANI C MATERIA L

•SOLI D WAST E'CHARGES ' MP- 1 - e ^ EMPT Y DRUM S

VOLATIL EORGANI C MATERIA L

• SOLI D WAST E'CHARGES ' HP- 2 - B
—EMPT Y DRUM S

VOLATIL EORGANI C MATERIA L

LA B PAC K REPAC K FACILIT Y SOLI D WAST E'CHARGES ' - B

—EMPT Y DRUM S



# FIGUR E7 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L MATERIA LPROCESSIN G Base d o n Figur e b y Woochyard—Clyde Consultant s 

# SCHREIBE R -YONLE Y ASSOCIATE S CHECKE D BY i DRAW NBY i DAT EDRAWN i PRDJEC T ii i ENVIRONMENTA LENGINEER S 

## KS BA H 04-19-0 7 07006 3

## PARTICULAT E MATTER , VOLATIL E ORGANI C MATERIAL
CARBO N ADSORPTIDN SYSTE M
BH-2/C- 1

INCINERATION UNI

T # 4 BUL KFEE D BUILDING 'PITS ' TARPED ROLL-OF F /DUMPTRAILE R BUL KSOLI

D WAST E x BATC H DRO

P sr * CLA M SHELL THRDUG

H A N ENCLOSED GALLERY •Ha * WHIL

E DOOR

S TO BUL KFEE D BUILDING AR E CLOSED , SINGL E BAGHDUSE CBH- D OPERATES , WHILE DOOR

S AR E OPE N (UNLOADING) , THE COMBINE D CYCLDNE/BAGHDUS E (BH-2/C- D OPERATES . 

# FIGUR E8 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L BUL K FEE D BUILDIN G Base d o n Figur e b y Woodward—Clyd e Consultant s 

# SCHREIBE R O YONLE Y O C ASSOCIATE S CHECKE D BY ' DRAW NBY . DAT EDRAWN . PROJEC T ft. ENVIRONMENTA LENGINEER S 

## K S BA H 04-19-0 7 07006 3

## VOLATIL E ORGANI C MATERIA L

'EMPTY ' DRUM

S WIT H RESIDUA L WAST E DRU M CRUSHER CRUSHE D DRUM

S WIT H RESIDUA L WAST E



# FIGUR E9 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L DRU M CRUSHE R Base d o n Figur e b y Woodward—Clyd e Consultant s 

# SCHREIBE R 0 7 

# YONLE Y ^J^ , ASSOCIATE S CHECKE D BY . DRAW NBY i DAT EDRAWN ' PROJEC T # : ENVIRONMENTA LENGINEER S 

## K S BA H 04-19-0 7 07006 3

## COMBUSTIO N GASE S
PROPOSED NATURA L GA S * ~ 10. 6 M M BTU/H R BOILER
COMBUSTIO

N GASE S

NATURA L GA S 10. 6 M M BTU/H R BOILER



# FIGUR E1 0 PROCES S FLO WDIAGRA M VEOLI A ES ; SAUGET , I L EXISTIN GAN D PROPOSE D BOILER S Base d o n Figur e b y Woodward-Clyd e Consultant s 

# SCHREIBE R O r

# YONLEY ASSOCIATE S CHECKE D BY i DRAW NBY i DAT EDRAWN i PROJEC T iU ENVIRONMENTA LENGINEER S 

## K S BA H 04-19-0 7 07006 3