• NVIRONM6NTA L S€RVIC£ 5 (Fed-X'ed ) Apri l 4 , 201 3 A!Rfc !FO?C Q ^ , - , Mr . Georg e Czerniak , Directo rL ~ Ai ran d Radiatio n Divisio n Unite d State s Environmenta l Protectio n Agenc y Regio n 5 7 7 Wes t Jackso n Blvd . (R-19J ) Chicago , I L 60604-359 0 R E : Veoli a E S Technica l Solutions , L.L.C . Sauget , I L 4 0 CF R Par t 7 1 Titl e V Permi t Renewa l Applicatio n Dea rMr . Czerniak , Enclose d fo ryou rrevie wi s Veoli a E S Technica l Solutions , L.L.C . Sauget , I L facility' s Titl e V permi t renewa l applicatio n prepare d i n accordanc e Wit h 4 0 C.F.R . Par t 71 . Thi s i s a renewa l applicatio n t o th e Titl e V permi t tha t wa s issue s o n Septembe r12 , 200 8 an d expire s o n Octobe r12 , 2013 . I fyo u hav e an yquestion s o n thi s submitta l o rwoul d lik e t o mee t t o discus s thi s application , pleas e cal l Denni s Warcho l o rm e a t (618 ) 271-2804 .

Dou g raarris Genera l Manage r Att . cc : EP AFil e Sincerely ,

# 7 Mobil e Avenue , Sauget , I L 6220 1 (618 ) 271-280 4 www.veoliaes.co mAPPLICATIO N FO R RENEWA L O F A MAJO R SOURC E OPERATIN G PERMI T

Veoli a E S Technica l Solution s

# 7 Mobil e Avenu e Sauget , Illinoi s 6220 1



## APRI L 201 3

### TABL E O F CONTENT S

TABL EO FCONTENT S 2 I . IDENTIFICATIO NINFORMATIO N3 A . Facilit y Informatio n 3 B . Sourc e Descriptio n 3 II . EMISSION S INFORMATIO N5 A . Hazardou s Wast

e Combustor s 5 B . Materia l Processin g Area s 5 C . Dru mCrushe

r 6 D . Storage Tan

k Unit s 6 E . Bul k

Fee dBuildin g 6 F . Gasolin e Storage Tank 7 G . Boile r

#1 - 7 H . Fugitiv e Organi c Emission s 7 I . Emergenc y Generators 7 J . Insignifican t

Emissio nUnit s 7 K . Actua l Emissio nRate s , 8 III . APPLICABL EREQUIREMENT S 9 A . 4 0 CF R63 Subpar t DDDD D Nationa l Emissio n Standards fo r Hazardou s Ai r

Pollutant s fo r Majo r Sources : Industrial , Commercial , andInstitutiona l Boiler s andProces s Heaters 9 B . Removal o f

Obsolet e Requirement s Relate dt o Complianc e Date s i n 4 0 CF R63 Subpar t EE ENational Emissio n Standard s fo r Hazardou s Ai r

Pollutant s Fro mHazardou s Wast e Combustor s 1 0 C . Adjustment

o f B asi s fo r VO M Emissio n Calculation s fo r Dru mCrushe

r 1 0 D . Transfer

o f Combustors ' Operatin g Permi t Limit s fromMai nBod y o f Permi t to Appendi x tha

t Contain s Mos t

Recent Notificatio no f

Complianc e Summar

y Tabl e 1 1 E . 4 0 CF R63 Subpar t ZZZ ZNationa l Emissio n Standard s fo r Hazardou s Ai r

Pollutant s fo r Stationar y Reciprocatin g Interna

l Combustio n Engine s 1 1 F . 3 5 IA C 219.58 5 Gasolin e Volatilit y Standard s 1 2 IV . DEMONSTRATIO NO FCOMPLIANC E1 5 V . COMPLIANC ESTATU S AN D CERTIFICATIO N1 6 VI . STANDAR D APPLICATIO NFORM S 1 7 APPENDI X A : EMISSIO NCALCULATION S 1 8 APPENDI X B : CURREN T NOTIFICATIO NO FCOMPLIANC E(NOC ) OP LSUMMARY . 2 1 2

### I . IDENTIFICATIO N INFORMATIO N

Veoli aE S Technical Solution s (Veolia ) own s an doperate s aResourc e Conservatio n and Recovery Ac t

(RCRA ) treatment, storage an ddisposa l facilit y i n Sauget, Illinois . Th e primary facilit y activitie s includ e receip t o f bul k wast e or wast e i n containers , wast

e processing , wast

e storage , an

dwast e incineratio n i n on

e o f three combustio n units . The facilit y operate s i n accordanc e wit haTitl e V permi t t o operate , Permi t

No . V-IL-12716300103-08-0 1 issue di n accordanc e wit h4 0 CF RPar t 7 1 b y USEP ARegion 5 an dth e most recen t Notificatio n o f Complianc e (NOC ) tha t contain s operatin g limit s fo r the combustors . I n addition , Veoli a operate s i n accordanc e withahazardou s wast e Par t B penni t fo r treatment, storage , an

ddisposal o f hazardou s waste . A . Facilit

y Informatio

n Facilit y Name : Plan tID : Address : Geographical : Permi tContact : Veoli aE S Technica l Solution s (Veolia )

171630010 3 # 7 Mobil e Avenu e Sauget, I L62201-106 9 St . Clai r County Latitud e 38.5944 7 Longitude-90.185 4 Dougla s Harris , Genera

l Manager Pleas e refer

t o FormGI S o f

the standar

dapplicatio n form s fo r

additional specifi c facilit y information . Th e form s ar e containe di n Sectio n V I o f thi s document . B . Sourc

e Descriptio

n The Veoli afacilit y i s comprise do f emissio n unit s tha

t have bee

n groupedinto twelv e define dsourc e emissio n points . Ther e have been no physica l change s t o th e existin g emissio n unit s a

s describe di n th

e origina l Titl e V permit application . N o emissio n unit s have bee n adde

dsinc e the origina l Titl e V permit becam e effectiv e (Octobe

r 12 , 2008) . Th e groupedsources , therefore , ar e provide dbelo w a

s they ar e liste di n Permit

#V-IL 1716300103-08-01 , Sectio n (1.0)(B) . Emission Unit Description Manufacturer /Model Dat

e o f Constructio

n Emission Contro l

Equipmen

t Hazardou s Wast e Combustor s Incineratio n Uni t # 2 (1 6 mmBtu/hr) Trad e Waste

Incineratio n TWI-2000 , Serie s 2 9/198 6 Joy-Nir o Spray Drye r Absorbe r (SDA-2) , Puls e Fl o Fabri c Filte r (BH-2 ) Hazardou s Wast e Combustor s Incineratio n Uni t # 3 (1 6 mmBtu/hr) Trad e Wast e Incineratio n TWI-2000 , Serie s 2 9/198 6 Joy-Nir o Spra y Drye r Absorbe r (SDA-3) , Puls e Fl o Fabri c Filte r (BH-3 )



### 3Emission Unit Descriptio n Manufacture r

/Mode l Dat e o f Construction Emissio n Contro l Equipmen

t Incineratio n Uni t

# 4 (5 0 mmBtu/hr) International

Waste Energy , PY*RO X 6/198 8 Temperin g Chamber , Activate dCarbo n Injection , Spra y Drye r Absorbe r (SDA-4) , Fabri c Filte r

(BH-4 ) Materia l Processin g Area s Materia l Processin g

Area s # 1 an

d# 2 (MP- 1 andMP-2 ) 198 8 Non e Materia l Processin g Area s Lab Pac k Repac k Are a 198 8 Non e Dru mCrusher Crushin g o f RCRA empt y container s 1984 None Storag e Tank s fo r Liqui d Waste s Tanlcs : #2 , #4 , #6 ,

#8 , #10 , #20 , #30 , #40 , #50 , #60 , #300 , #302 , #304 , #306 , #308 , #310 , #312 , #31 4 Moder nWeldin g 198 8 2&4 replace

d in - kind4/200

2 10&2 0 replace d in-kin d6/200

4 3 0 replace din kin d3/200

9 Activate dCarbo n Adsorber s on eac h

Storag e Tan k fo r # 2 Fue l Oi l Tank s #390 Moder nWeldin g 198 8 Non e Bul k Fee d Buildin g (B FBldg ) Temporar y storag e o f bul k soli dwaste s i npit s prio r

to bein g fe dt o Incineratio n Uni t # 4 198 8 Cyclone , Airto l Baghous e (B FBldg-BH-1) , Activate d Carbo n Adsorptio n Uni t (BFBldg-CA ) Gasolin e Storag e Tan k 550-gallo n tank with submerge dloadin g pip e 199 2 replace d in-kin d6/201 2 Non e Diese l Fue l Tan k (Insignificant

) 550-gallo n tan

k 199 2 replace d i nkin d6/201 2 Non e Kerosen e Tan k (Insignificant

) 550-gallo n tan

k 199 2 replace d i nkin d6/201 2 Non e Boile r #1 Natura l gas-fire d

Boile r (10. 6 mmBtu/hr) Cleave r Brooks , 25 0 11/199 5 Non e Emergenc y Generator s - 2 #

2 Fue l oil-fire d (0. 4 MMBtu/h r

ea. ) 198 8 Non e Fugitiv e Emission s Pumps , Valves ,

Flanges , Open endedLines , Compressor s N / A Non e 

### Description s o f

emissio n unit s an

dcontro l equipmen

t ar e provide do n the standar d applicatio n form s EUD- 1 an dEUD- 2 foun di n Sectio n V I o f thi s document .

4

### II . EMISSION S INFORMATIO N

Th e emissio n source s a

t th e Veoli afacilit y have th e potential t

o emit particulate matte

r (PM) , volatil e organi c material s (VOM) , sulfu r dioxid e (S0 2 

### ) , nitrogen oxide s (NOx) , carbon monoxid e (CO) , andorganic/inorgani c hazardou s air pollutant s (HAPs) . Emission s ar e generatedfromth

e storage andhandlin g o f wast e i n material processin g areas , breathing an d workin g losse s fro mstorage tanks , combustio n o f waste , combustio n o f

natura l ga s an dorgani c liqui dtransfe

r i n piping . Th e proces s flow , emissio n uni t description s andemissio n contro l infonnatio n has not

changedfromtha

t provide di n th

e origina l Titl e V penni t application . The followin g section s provid e brie f summarie s o f

th e pertinen

t proces s andemissio n rat e infonnation . A . Hazardou

s Wast e Combustor

s Incineratio n unit s #

2 and# 3 ar e identical fixed-hearthincinerator s withatwo-stage combustio n proces s andmaximu mhea t input capacit y o f 1 6 MMBtu/h r

each . Ignitio n o f wast e material take s plac e i n th e primar y (lower ) combustio n chambe

r a t temperature s i n exces s o f 1,70 0 degree s F . A secondar y (upper ) combustio n chambe

r serve s a s a n "after burner " fo r

proces s gases . Th e secondar y combustio n chambe

r temperatur

e i s maintaine d a t aminimu mtemperatur e o f 1,80 0 degree s F . Natura l ga s i s use da

s auxiliary fue l i n bot hchambers to maintai n minimu mcombustio n chambe r temperatures . Eac huni t i s equippe dwithaspra

y dryer adsorbe r an dfabri c filte r

air pollutio n contro l system . The fabri c filter

fo r uni t # 2 has fou r

baghous e chambers whil e th e fabri c filte r

fo r unit # 3 has three baghous e chambers . Incineratio n uni t

# 4 i s arotar

y kil nequippedwithasecondar y combustio n chambe

r an da maximu mhea

t input capacit y o f 5 0 MMBtu/hr . Ignitio n o f wast e material take s plac e i n th e primary kil na

t temperature s i n exces s o f 1,50 0 degree s F . Th e secondar y combustion chambe r temperatur

e i s maintaine dabove 1,88 0 degree s F . Natural ga s i s useda

s auxiliary fue l t

o maintai n minimu mcombustio n temperatures . Thi s uni t i s equippedwith a n air pollutio n contro l syste

mtha t consist s o f

atemperin g chamber , activatedcarbon injection , aspra

y drye r adsorber, an

dafabri c filter. Th e incineratio n unit s generat e emission s o f

PM , S0 2 

### , NOx , CO , VO M an d organic/inorgani c HAPs . B . Material Processin g Area s Materia l processin g involve s repackaging o f containerize dsoli dwaste s int o smaller , mor e manageable container s fo r incineration . Som

e soli dwaste s ma

y be receive d containin g free liquid s tha t ma y b e aqueous or

organic . Durin g material processing , free liquid s ar e fixedwitha

n iner t absorben

t t o facilitat e repackaging . Materia l processing occur s a t MP-1 , MP-2 , andth

e La b Pac k Repac k Facilit y i n Buildin g 2B . Thes e operation s emit

fugitiv e emission s i n a

n enclosedbuilding . VOM s andorgani c HAP s ar e emitte dto th

e atmospher

e throughbuilding/are aexhaust fans . 5

### C . Dru m Crusher Dram s receive dtha

t ar e unsuitabl e fo r

reus e ar e crusheda

t th e Dru mCrushe

r after bein g emptied . Thes e empt

y drum s ma

y contai n residual organi c material . Crushe ddrums ar e transporte doff-sit e fo r

disposal . Fugitiv e emission s o f VO M an

dorgani c HA Par

e emitte dto th

e atmosphere . D . Storag

e TankUnit

s Bul k liqui dwaste s ar

e storeda

t Tank Farm#1 andTank

Farm#3 . Al l bul k

liqui dwast

e tanks ar e vertical , fixed-roo f

tanks equippedwit hcarbo n canisters fo r contro l o f emissions . In addition , No . 2 fue l oil , kerosene , an dgasolin e ar

e als o storedonsit

e i n tanks . Emission s fro mth e liqui dbul k

storage andhandlin g unit s ar e VOM s andorgani c HAPs . Storage tan

k emissio n unit s andtheir

capacitie s ar

e liste dbelow . Tan kI D Location Capacit y (gallons ) Tan k # 2 Tan k

Far m# 1 4,93 1 Tan k # 4 Tan k

Far m#1 4,93 1 Tank # 6 Tan k

Far m# 1 7,20 0 Tank # 8 Tan k

Far m#1 5,28 0 Tank #1 0 Tan k

Far m# 1 12,86 9 Tank #2 0 Tan k

Far m#1 12,86 9 Tan k #3 0 Tan k

Far m# 1 12,86 9 Tank #4 0 Tan k

Far m# 1 12,86 9 Tan k #5 0 Tan k

Far m# 1 12,86 9 Tank #6 0 Tan k

Far m# 1 12,86 9 Tan k #30 0 Tan k

Far m# 3 30,00 0 Tank #302 Tan k

Far m# 3 30,00 0 Tan k #30 4 Tan k

Far m# 3 30,00 0 Tan k #30 6 Tan k

Far m# 3 30,00 0 Tan k #30 8 Tan k

Far m# 3 30,00 0 Tank #31 0 Tan k

Far m# 3 30,00 0 Tan k #31 2 Tan k

Far m# 3 10,00 0 Tan k #31 4 Tan k

Far m# 3 10,00 0 Tank #39 0 Tan k

Far m# 3 30,00 0 Kerosen e Sout

ho f Parkin g Lo t 55 0 No . 2 Fue l Oi l Sout

ho f Parkin g Lo t 55 0 Gasolin e Sout

ho f Parkin g Lo t 55 0 No . 2 Fue l Oi l Fir e Pum p Hous e 55 0 

### E . Bul kFee

d Building Bul k soli dwaste s ar

e store di n fou r

pit s i n th e Bul k Fee dBuilding . Solid s storedi n thes e pit s ar e incinerate di n Uni t

4 . Bul k soli dwaste s ar

e move dfro mth

e pit s to Uni t

4 b y a clamshel l througha

n enclose dgallery . Th e activitie s withi n th e buildin g generat

e emission s o f

PM , VO M andorganic/inorgani c HAPs . Th e buildin g exhaust i s equipped witha n ai r pollutio n contro l systemtha t consist s o f

acyclone , tw o baghouses , anda carbo n adsorptio n system . 6

### F . Gasolin e Storag e Tan k Gasolin e i s storedi n a550-gallo n horizontal tan k fo r utilizatio nb y compan

y vehicles . Th e tan k i s equippedwithasubmergedloadin g pipe . VO M emission s ar e generated fro mthe tank . G . Boiler#

1 Ther e i s 10. 6 MMBtu/h r

natura l gas boile r

locate dnort

ho f Tank Far m#1 . Th e boile r

i s use dto generat

e hea t an dsteain fo r

on-sit e uses . Th e natura

l ga s combustio n i nthe boile r generate s emission s o f

PM , SO2 , NOx , CO , VO M andorganic/inorgani c HAPs . Ther e i s n o emissio n contro l device s associate dwit hthi s unit . H . Fugitiv

e Organi cEmission

s Fugitiv e VO M an

dorgani c HA Pemission s ar e generatedb y leakin g equipmen t lik e valves , flanges , andpumps . Equipment components ar

e inspectedandmonitore dto minimiz e fugitiv e emission s fro mthes e sources . I . Emergenc

y Generator

s A nemergenc y generato

r tha t combusts #

2 fue l oi l i s use dfo r

emergenc

y power/energ y requirements . The generato r ratin g i s les s tha

n 11 2 kilowatt s or

150. 2 horsepower . Th e maximu mhourl y design rat e i s approximately 0. 4 MMBtu/hr . The generato r i s onl y use d i nth e cas e o f

apowe r outage or

natura l ga s curtailment . Nonemergency operatio n i s limite dto maintenanc e andtestin g tha t i s necessar

y t o maintai n th

e readines s o f

the unit . Asecondemergency generato r i s use dto operat

e the fir e wate

r pum p i n th e even t o f a n onsit e fire . Thi s generato

r als o combusts #

2 fue l oi l andhas amaximu mhourl y desig n rat e o f approximately 0. 4 MMBtu/h r ( < 11 2 kilowatt

rating) . Whe n operated , th

e # 2 fue l oi l combustio n generate s emission s o f PM , SO2 , NOx , CO , V O M andorganic/inorgani c HAPs . Ther e ar e no emissio n contro l device s associate d withthes e units . J . Insignifican

tEmissio n Unit s Th e lis t o f insignifican t

emissio n unit s containe di n the origina l Titl e V permi t no . V-IL 1716300103-08-0 1 i s provide dbelow . N o insignifican t emissio n unit s have been adde d sinc e the original Titl e V permit becam e effectiv e (Octobe

r 12 , 2008) . 2. 5 mmBtu/hr

Tiog aportabl e boile r As hhandlin g Handlin g o f

spen t dr y scrubbe r solid s Lim e unloadin g an

dproportionin g Gasolin e storage tan

k Kerosen e storage tan

k 7

### Diese l fue l storag e tan k Us e o f absorben t material General vehicl e maintenanc e an dservicin g (assume

dt o includ e diese l fue l handling ) Laborator

y Pipin g andstorag e systemfo r natura l ga s Non-halogenate dcol dcleanin g degreasers Interna l combustio n engine s o f

motor vehicle s Storage andhandlin g o f

close ddrums K . Actual Emissio

n Rate s Pollutan t Annua l Emission

s (tons ) Pollutan t 200

7 200

8 200

9 201

0 201 1 C O 1.93 1.95 1.6 7 1.4 1 1.2 1 N O x 54.7 7 54.7 6 55.2 3 57.1 0 58.1 6 P M 1.0

4 1.0

4 1.0

7 1.1 0 1.1 2 so 2 0.59 8 0.49 6 0.52 0 0.49 0 0.4 9 V O M 1.6

0 1.70 1.7 4 1.6

2 1.5 1 HC 1 2.6 9 3.5 6 2.0 9 2.0 3 1.89



### 8

### III . APPLICABL E REQUIREMENT S

Th e existin g Titl e V permit no . V-IL-1716300103-08-0 1 detail s th e requirements tha

t ar e applicabl e t

o Veolia . However , Veoli arequests severa l change s t

o permit requirements base d upo n ne w regulation s comin g into effect , obsolet e requirements tha

t hav e been supersede

dand th e collectio n o f

informatio n durin g the permi t ter mtha t affect s th

e basi s i n th

e origina l application . Th e requeste dchange s ar

e describe dbelow . A . 4 0 CF R6

3 Subpar

tDDDD D Nationa

l Emissio

n Standard

s fo rHazardou

s Ai r Pollutant

s fo rMajo rSources : Industrial , Commercial , an d Institutiona

l Boiler s an d Proces s Heaters. Th e facilit y operate s anatura l gas-fire dboile r

(Boile r #1 ) withamaximu mhea t input rat e o f 10. 6 MMBtu/hour . O n Januar y 13 , 2013 , USEP Apublishe dth e final standards fo r HAP s fro mth

e combustio n o f

fue l i n boiler s andproces s heaters . Sinc e th e facilit y i s a majo r sourc e o f

HAPs , the requirement s o f 4 0 CF R63 Subpar

t DDDD D (Boile r

MACT ) appl y t o Boile r #1 . Veoli amus t

provid e initia l notificatio n i n accordanc e wit h4 0 CF R 63.9(b)(2 ) b y Ma y 31 , 2013 . Th e boile r mus t b e i ncomplianc e b y Januar y 31 , 2016 . Ther e ar e n o applicabl e numerical emission s limits , operatin g limit s or performanc e testin g requirements i n th e majo r sourc e Boile r

MAC T fo r

unit s designe dt

o burn natura

l ga s (Ga s 1) . A s describe di n Tabl e 3 to Subpar t DDDDD , Boile r

# 1 mus t mee t the wor k practic e standards liste dbelow .

• Performanc e o f

a n annua l tune-u p addressing al l regulate demissions . Th e tune-u p shal l includ e th

e followin g a

s describe di n4 0 CF R63.7540(10) : 1 . Inspectio n o f

the burner , the flame patter n andth e air-to-fue l rati o control s fo r operation h i accordanc e wit hmanufacturer' s specification s an dperfonnanc e o f adjustments a

s necessary . 2 . Optimizatio n o f

total C O emission s i n coordinatio n withNO x limitations . 3 . Measuremen

t o f C O concentration s an

doxygen concentratio n i n the boile r exhaust . 4 . Productio n o f

awritte n repor

t documenting C O concentrations , correctiv e action s andth

e amoun t o f fue l combusteddurin g the year . Performanc e o f

aone-tim

e energy assessmen

t b y aqualifie denergy assessor . Submissio n o f

aNotificatio no f

Complianc e Statu s withi n60 day s o f th e initia l tune up . Th e applicabl e informatio n liste di n 4 0 CF R63.7545(e)(1 ) through(8 ) mus t b e provide di nth

e Notificatio no f

Complianc e Status . Submissio n o f

an Annua l Complianc e Repor t a s describe di n 4 0 CF R63.755 0 b y Januar y 31 s t 

### o f eachyear . Th e existin g Permit

#V-IL-1716300103-08-0 1 i n Sectio n 2. 7 Unit-Specifi c Operatin g Requirement

fo r Boiler s require s tha

t Boile r #1 C O concentration s not exceed10

0 pp m o n adry basi s correctedt o 3 % oxygen . I n addition , th e facilit y i s reqrjire dt

o conduct annua l perfonnanc e testin g fo r C O andmonito r

monthl y natura

l ga s consumption . Th e 9

### result s fro mth e las t fou r years o f performanc e testin g o f

the boile r

fo r C O concentration s ar e provide di nthe table below .

Dat e o f Tes t Highes

tC O Concentration 1 (ppm ) 

### June 25,200

9 0.0

6 June 17 , 201 0 <0.01 June 9,201 1 <0.01 June 8,2012 0.1 3 Th e C O concentratio n o f th e boile r exhaust i s ver y smal l an

dmuc hles s tha

n the limi t

o f 10 0 ppm . Th e desig n o f the Cleaver

Brook s boile r

i s conduciv e t

o minimizin g C O emission s b y achievin g goo dcombustion . Veoli arequests tha t the requiremen

t to conduct aperformanc e test

fo r C O i n Sectio n 2.7(D)(2 ) b e remove dan

dreplace dwithth

e requiremen

t t o conduc t

a n annua l tune-u p o f th e boile r a s containe di n th

e Boile r MAC T discusse dabove . Th e annua l tune-u p wil l includ e measuremen t an doptimizatio n o f

th e C O concentratio n i nthe boile r exhaust whic hachieve s th e sam

e result a s th e performanc e test - demonstrating complianc e wit hth e C O emissio n limitation s o f th e pennit . B . Remova

l o f Obsolet e Requirement

s Relate d t o Complianc

e Date s i n 4 0 CF R6

3 Subpar tEE E Nationa

l Emissio

n Standard

s fo rHazardou

s Ai rPollutant

s Fro m Hazardou

s Wast e Combustors. Veoli arequests tha

t peiTni t condition s i n whic hth e complianc e dat

e has passedb e remove dfro mth e Par

t 7 1 permit . Prio r

t o Octobe r 14 , 2008 , th e combustors wer

e require dto compl y wit hdifferent emissio n limitation s tha n thos e tha

t becam e applicabl e after tha t dat e andcontinue t

o b e applicable . Th e facilit y demonstratedcomplianc e with thes e limitation s a

t th e time ; however , they ar

e not relevant t o facilit y requirement s i n the Par t 7 1 permi t goin g forward . C . Adjustmen

to fBasi s fo rVO M Emission Calculation s fo rDrum Crusher. Th e Par t 7 1 permi t contain s recordkeepin g requirement s fo r th e drumcrushe

r VO M emission s tha

t mus t b e calculate dusin g th e emissio n facto r

o f 0.091 4 l b VOM/dru m crushed . Thi s emissio n facto r was calculate dbase do n th e conservativ e assumptio n tha t onl y methano l residu e i s i n th e container s t

o b e crushe dandtha

t methano l i s the onl y V O M release da

s the containers ar

e crushed . Thi s wa s conservativ e becaus e methano l has ahigher

vapor pressur e tha n mos t o f th e volatile s foun di n containe r residues , therefore , assuming the emission s wer e al l methano l maximize dthe potential VO M emissio n rate . I

t wa s understoo dtha

t thi s assumptio n significantl y overestimate dthe V O M emission s fro mth e drumcrusher ; however , th e absence o f

dat afo r the drum crushe r operatio n require daconservativ e approach . Veoli ahas collecte ddat afo r th e fiv e years sinc e th

e penni t was issue dincluding : the numbe r o f container s crushed , th

e typ e o f volatil e constituent s likel y t o be i n containe

r residu e andth

e amoun t o f these volatil e constituents processe do n a n annua l basis . A C O concentratio n i npp ma t 3 % oxygen . 

### 1 0

### new VO M emissio n facto r wa s calculate dutilizin g thi s dat afro mactua

l operations . Th e containe r residu e was characterize da s containin g th

e to p organic s a

t thei r overal l concentration s i n th

e wast e receive di n 2007 - 2011 . Th e remainde r o f th e wast e wa s representeda

s wate r andiner t solids . Thi s approachyielde daVO M emissio n factor o f 0.022 1 pound s VO M pe

r drumcrushed . Wit hamaximu mcrushin g rat e o f 4 0 drams per hour , the potentia

l to emit fo r th e dra mcrashe r was calculate dt

o b e 0.883 3 pound s VO M per hour an d3.8 7 ton s VO M pe

r year . The detaile dcalculation s ar e provide di n Appendi x A . D . Transfero

f Combustors ' Operatin g Permi tLimit s from Mai n Bod

y o f Permi tt o Appendi x tha tContain

s Mos tRecen tNotification o

f Complianc

e Summar

y Table . Th e existin g Permi t

#V-IL-1716300103-08-0 1 i n Sectio n 2.1(C ) Hazardou s Wast e Combustors , Unit s 2 , 3 and4 contain s wor k practic e standards andoperationa l requirements . Conditio n2 o f thi s Sectio n list s th

e operatin g paramete

r limit s (OPLs ) fo r the combustors tha

t ar e use dt o demonstrat

e complianc e with4 0 CF R6 3 Subpar t EEE . Veoli arequests tha

t the tabl e containin g th e specifi c OP Llimit s b e removedfro m Conditio n2 . Instead , w e propos e tha t Conditio n2 rea

da s follows . "2. The Permittee must operate Units 2, 3, and

4 under the operating parameter limits (OPLs) listed

in the Current

NOC a summary of

which is provided

in Attachment

A to this permit

document. Operation in accordance with the NOC limits is used to demonstrate compliance with Subpart EEE." Th e tabl e summarizin g th e OPL s fro mthe curren t NO C woul db e movedt o a n attachmen

t a t the bac k o f th e pennit . Thi s eliminate s th e needt o change table s withi n permit condition s an

dallow s th

e NO C infonnatio n to b e updatedeasily . E . 4 0 CF R6

3 Subpar

tZZZ Z Nationa

l Emissio

n Standard

s fo rHazardou

s Ai r Pollutant

s fo rStationar

y Reciprocatin

g Interna

l Combustio

n Engines . Tw o emergenc y generators ar e locate da

t th e facility . The y ar

e stationar

y reciprocatin g interna l combustio n engine s (RICE ) wit hasit e ratin g o f

les s tha n 500 brak

e H Pused onl y fo r emergency purpose s tha t operat e a t amajo r sourc e o f

HA Pemissions . Th e emergency RIC Emust

compl y withth

e requirements o f

40 CF R63.6640(f

) i n orde r t o b e considere demergency stationar y RICE . Thes e requirement s ar e liste dbelow . (1 ) Fo r owner s an doperator s o f emergenc y engines , any operatio n othe r tha n emergenc y operation , maintenanc e an d testing , an doperatio n i n nonemergenc y situation s fo r 5 0 hour s per

year , a s permitte di n thi s section , i s prohibited . (2 ) There i s n o tim e limi t o n the us e o f

emergenc y stationar

y RIC Ei n emergenc y situations . (3 ) Yo u may operat

e you r emergenc y stationar

y RIC Efo r

th e purpos e o f

maintenanc e check s an dreadines s testing , provide dtha

t the tests ar

e recommende db y Federal , Stat e o r loca l government , the manufacturer , the vendor , or th e insuranc e compan y associate dwit hth e engine . Maintenanc e check s an dreadines s testin g o f suc hunit s i s limite dt

o 10 0 hour s per

year . Th e owner

or operator may petitio n the Administrato r fo r approval o f

additiona l hours t

o b e use dfo r maintenanc e check s an dreadines s testing , bu t apetitio n i s no t

require di f

th e owner

o r operator maintain s record s indicatin g tha

t Federal , State , o r

loca l standard s require maintenanc e an dtestin g o f emergenc y RIC Ebeyon d10 0 hour s pe r year . 

### 1 1(4 ) Yo u ma y operat e you r emergenc y stationar

y RIC Eup t

o 5 0 hour s pe r

yea r i n non-emergenc y situations , hut thos e 5 0 hour s ar

e counte dtoward s th e 10 0 hour s per

yea r provide dfo r

maintenanc e an dtesting . Th e 5 0 hour s per yea r fo r non-emergenc y situation s canno t b e use dfo r

pea k shavin g o r

t o generat e incom e fo r

afacilit y t

o suppl y powe

r to a n electri c gri do r

otherwis e suppl y powe r a s par t o f afinancia l arrangemen

t wit hanothe

r entity ; excep t

tha t owner s and operator s may operat

e the emergenc y engin e fo r amaximu mo f

1 5 hour s per

yea r a s par t o f ademandrespons e programi f

th e regiona l transmissio n organizatio n or equivalent

balancin g authorit

y an dtransmissio n operator has determine dther

e ar e emergenc y condition s tha t coul dlea dt

o apotential electrica l blackout , suc ha s unusuall y lo w frequency , equipment

overload , capacity o r

energ y deficiency , or

unacceptabl e voltag e level . Th e engin e ma y no t b e operate dfo r

mor e tha n 3 0 minute s prio r

t o th e tim e whe n the emergenc y conditio n i s expecte dt o occur , andthe engin e operatio n mus t

b e terminate dimmediatel y afte r the facilit y i s notifie dtha t the emergenc y conditio n i s no longer imminent . Th e 1 5 hour s pe r yea r o f demandrespons e operatio n ar e counte da

s par t o f the 5 0 hour s o f

operatio n per yea r provide dfo r

nonemergenc y situations . Hi e suppl y o f emergenc y powe r

t o anothe r entit y o r entitie s pursuan

t t o financia l arrangemen

t i s no t limite db y thi s paragraph(f)(4) , a s lon g as th e power

provide db y the financial arrangemen

t i s limite dt

o emergenc y power . 

### Eac hemergency RIC Emust compl y withth

e followin g requirement s b y Ma y 3 , 201 3 an d a t al l time s thereafter . 1 . Durin g normal operations : a . Chang e oi l andfilter

ever y 50 0 hour s o f

operatio n o r

annually , whicheve r

come s first; b . Inspect

ai r cleaner ever y 1,00 0 hour s o f

operatio n o r

annually , whicheve r

come s first ; c . Inspec t al l hose s an dbelt s ever y 50 0 hour s o f

operatio n or

annually , whicheve r

come s first, an dreplac e as necessary . d . Durin g startup : minimiz e th e engine' s time spen t a t idl e andminimiz e th e engine' s startu p tim e a t startu p t o aperio d neede dfo r

appropriate an dsaf

e loadin g o f

th e engine , not

t o excee d3 0 minutes , after whic htim e the non-startu p emissio n limitation s apply . 2 . Operat e an dmaintai n the stationar y RIC Eandafter-treatmen t contro l devic e (i f

any ) accordin g to the manufacturer' s emission-relate dwritte n instruction s o r develo p andfollo w you r ow n maintenanc e pla n whic hmus t provid e t

o the exten t practicabl e fo r

the maintenanc e andoperatio n o f the engin e i n amanne r consistent

wit hgoo dai r

pollutio n contro l practic e fo r

minimizin g emissions . 3 . Instal l anon-resettabl e hou r mete r i f on e i s no t

alread y installed . 4 . Maintai nth e followin g records :

• Descriptio n o f

eachmalfunctio n o f

operation/monitorin g equipment ; • Descriptio n o f

al l maintenanc e performed ; • Descriptio n o f

action s taken durin g malfunctio n t o minimiz e emissions ; • Descriptio n o f

correctiv e actions ; • Lis t o f maintenanc e conducte dto demonstrat e tha t RIC Ewa s operate dan dmaintaine di n accordanc e withthe maintenanc e plan/manufacturer s recommendations ; • Th e hour s o f

operatio n a

s monitore db y the non-resettabl e hour meter ; an d • Descriptio n o f

purpos e o f

operatio n hour s spent . 5 . Source s mus t

repor t an y failur e t

o performthe wor

k practice s o n the require dschedule . 

### 3 5 IA C 219.58

5 Gasolin

e Volatilit

y Standards. Effectiv e Januar

y 28 , 2013 , th

e requirements o f

Illinoi s regulatio n 3 5 IA C 219.58 5 wer e repealed . Veoli arequests tha t Sectio n 2. 6 Unit-Specific Operatin g Requirement

s fo r Gasolin e Storag e Tank s be revise dt

o remove th

e item s relate dt

o th e repeale drale. Thes e item s ar

e liste dbelow .

1 2

### Conditio n2.6(A)(3 ) The Permittee shall

not sell, offer for sale, dispense, supply, offer for supply, or

transport for use in Illinois gasoline whose Reid vapor pressure exceeds the applicable limitations set forth in 35IAC

219.585(b) and

(c) below during the regulatory control periods, which shall

be June 1 to September

15. [35IAC

219.585(a)]. Conditio n2.6(A)(4 ) The Reid vapor pressure of

gasoline, a measure of

its volatility, shall

not exceed 7.2 psi (49.68kPa) during the regulatory control period in 1995and

each year

thereafter. [35 IAC 219.585(b)]. Conditio n2.6(A)(5 ) The Reid vapor pressure of

ethanol blend gasolines having at

least nine percent

(9%) bid not more than ten percent

(10%) ethyl

alcohol by volume of

the blended

mixture, shall not exceed the limitations

for gasoline set

forth in subsection (b) of 35IAC 219.585 by more than 1.0pounds per square inch (psi)(6.9kilopascals). 35IAC 219.585(c)]. Conditio n2.6(C)(1 ) The Permittee shall

have gasoline stored

in the affected

tank sampled and analyzed for Reid vapor pressure. Samples shall

be conducted

at least once per calendar year or within 15days of

a written request

from EPA. [40C.F.R. § 71.6(a)(3)(i)(B)]. Conditio n2.6(C)(2 ) The Permittee shall

conduct all sampling (testing) of

gasoline required

by 35IAC 219.585in accordance with the procedures contained in 40C.F.R. part

80, appendix

D, "Sampling Procedures for Fuel Volatility. " Conditio n2.6(C)(3 ) The Permittee shall

measure Reid

vapor pressure of

gasoline in accordance with the procedures contained

in "Tests for Determining Reid

Vapor Pressure (RVP) of

Gasoline and Gasoline-Oxygenate Blends," as set forth in 40C.F.R. part

80, appendix

E. Conditio n2.6(C)(4 ) The Permittee shall

determine the ethanol

content of ethanol blend gasolines using one of the approved

testing methodologies specified in 40C.F.R. part

80, appendix

F. Conditio n2.6(C)(5 ) Any alternate to the sampling or testing methods or

procedures contained

in 35IAC 219.585(d), (e), and

(f ) must be approved

by the IEPA, which shall consider data comparing the performance of the proposed

alternative to the performance of one or more approved

test methods or

procedures. Such data shall accompany any request

for IEPA approval

of any alternate test

procedure. If

the IEPA determines that such data demonstrates that

the proposed

alternative will

achieve results equivalent to the approved test methods or

will achieve results equivalent to the approved

test methods or procedures, IEPA shall

approve the proposed

alternative.

1 3

### Conditio n2.6(0(6 ) On an annual

basis, the Permittee shall conduct an inspection of

the gasoline storage tank to review its physical

condition and

ability to comply with 35IAC 219.585. [40 C.F.R. § 71.6(a)(i)(3)(B)]. Conditio n2.6(D)(3 ) The Permittee shall

maintain records

for each shipment

of material loaded into the gasoline storage tank

that include copies of

the invoice, bill

of lading or

other documentation from the supplier that provides the type of

material, the amount

of shipment, date of

delivery, and

the Reid vapor pressure (psi) of

the gasoline. The Permittee shall

keep these records

for three years. [40C.F.R. § 71.6(a)(3)(i)(B)J. Conditio n2.6(D)(4 ) The Permittee must

maintain records of

results of

any testing samples. [40C.F.R. § 71.6(a)(3)(i)(B)J.

### IV . DEMONSTRATIO N O F COMPLIANC E

Complianc e demonstratio n methods , monitoring , recordkeepin g an dreportin g fo r the source s operatin g a

t Veoli aar

e a s require di n Penni t

#V-IL-1716300103-08-01 . A n Annua l Complianc e Certificatio ni s submitte deac hyear fo r al l applicabl e requirement s as the y are describe di n th e Part 7 1 permit .

1 5

### V . COMPLIANC E STATU S AN D CERTIFICATIO N

Veoli ai s i n complianc e withth e permi t andregulator

y requirement s a

s the y apply t

o th e emission s source s operating a t th e facility . Th e statemen t o f completenes s andcertificatio n o f complianc e b y th

e facility' s responsibl e officia l i s provide don th e CTA C Form5900- 2 i n Sectio n V I o f

thi s document .

1 6

### VI . STANDAR D APPLICATIO NFORM S

Thi s sectio n contain s the complete dapplicabl e standardpermi t applicatio n form s a

s publishe db y the Unite dState s Environmenta l Protectio n Agency .

1 7JPf e Sf^lFTl AUnite d State s

-^^|m : ^PL % Environmenta l Protectio n ^IJrlHi i * m Agenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) GENERA L INFORMATIO N AN D SUMMAR Y(GIS ) A . Mailin g Addres s an d Contact Informatio n Facilit ynam e Veoli a E S Technica l Solution s Mailin g address : Stree t o rP.O . Bo x# 7 Mobil e Avenu e Cit vSauqe t Stat e I L ZIP 6220 1 - 106 9 Contac t person : Dougla s Harri s Titl e Genera l Manage r Telephon e ( 61 8 ) 27 1 - 280 4 Ext . Facsimil e ( 61 8 ) 27 1 - 212 8 B . Facility Locatio n Temporar ysource ? Ye s X N o Plan t sit e locatio n # 7 Mobil e Avenu e Cit vSauge t Stat e I L Count ySt . Clai rEP ARegio n 5 I s th e facilit ylocate d within : India n lands ? YE S _X

_N O OC S waters ? YE S _X

_N O Non-attainmen t area ? X YE S N O If yes , fo rwha t ai rpollutants ? Ozone , PM2. 5 Withi n 5 0 mile s of affecte d State ? __X YE S _N O If yes , Wha t State(s) ? M O C . Owne r Nam e Veoli a E S Technica l Solution s Street/P.O . Bo x70 0 Eas t Butterfiel d Road , Suit e 20 1 Cit vLombar d Stat e I L ZI P 6014 8 - Telephon e ( 63 0 ) 21 8 - 175 6 Ext D. Operato r Nam e Veoli a E S Technica l Solution s Street/P.O . Bo x# 7 Mobil e Avenu e Cit vSauge t Stat e I L ZI P 6220 1 - 106 9 Telephon e ( 61 8 ) 27 1 - 280 4 Ext E P AFor m 5900-7 9GI S E . Applicatio n Typ e

Mar k onl yon e permi t applicatio n typ e an d answe rth e supplementaryquestio n appropriat e fo rth e typ e marked . Initia l Permi t X Renewa l Significan t Mo d Mino rPermi t Mod(MPM ) Grou p Processing , MP M Administrativ e Amendmen t Fo rinitia l permits , whe n di d operation s commence ? / / Fo rpermi t renewal , wha t i s th e expiratio n dat e o f curren t permit ? 1 0 / 1 2 / 201 3 F . Applicabl e Requiremen t Summar y Mar k al l type s o f applicabl e requirement s tha t apply . J<_SI P FIP/TI P PS D Non-attainmen t NS R X Mino rsourc e NS R Sectio n 11 1 Phas e I aci d rai n Phas e I I aci d rai n Stratospheri cozon e OC S regulation s _X

_ NESHA P Sec . 112(d ) MAC T Sec . 112(g ) MAC TEarl yreductio n o f HA P Se c112(j ) MAC TRM P [Sec.112(r) ] Tan k Vesse l requirements , sec . 183(f) ) Sectio n 12 9 Standards/Requiremen t Consume r/

comm. . products , § 183(e ) NAAQS , increment s o rvisibilit y(temp , sources ) Ha s a ris k

managemen t pla n bee n registered ? YE S N O Regulatoryagenc y_ _ Phas e I I aci d rai n applicatio n submitted ? YE S X N O If yes , Permittin g authorit y G . Source-Wid e PT E Restriction s an d Generi c Applicabl e Requirements Cit e an d describ e an yemissions-limitin g requirement s and/o rfacility-wid e "generic " applicabl e requirements . 4 0 CF R71.6(a)(3)(ii ) Genera l Par t 7 1 Recordkeeping . 4 0 CF R71.6(a)(3)(iii ) Genera l Par t 7 1 Reporting . 4 0 CF R71.6(a)(3)(I ) Perfonnanc e Testin g Facilitie s Provided . 3 5 IA C 212.30 1 Fugitiv e particulat e emission s beyon dth e propert y lin e prohibited . 35 IA C 237.10 2 Ope n burnin g i s prohibite dexcep t as provide db y regulation . 35 IA C 212.123(a ) Opacit y i s limite dt o les s than 30 % fro man y emissio n uni t unles s subjec t

t o othe r requirements . 4 0 CF RPar t

8 2 Standard s fo r

recyclin g an demission s reductio n o f ozon e depletin g substances . 35 IA C 24 4 Subpart

C Maintai nonsit e awritte n Episod e Actio nPlan . 4 0 CF R6 1 Subpart

F FCalculatio no f

tota l annua l benzen e quantity an dan y applicabl e requirement s as indicated .

E P AFor m 5900-7 9GI S 

### 3

H . Proces s Descriptio n Lis t processes , products , an d SI C code s fo rth e facility . Proces s Product s SI C Refus e System s No t applicabl e 495 3

I . Emissio n Uni t Identificatio n Assig n a n emission s uni t I D an d describ e eac h emission s uni t a t th e facility . Contro l equipmen t and/o ralternativ e operatin g scenario s associate d wit h emission s unit s shoul d b yliste d o n a separat e line . Applicant s ma yexclud e fro m thi s lis t an yinsignifican t emission s unit s o ractivities . Emission s Uni t I D Descriptio n o f Uni t Incineratio n Uni t

# 2 Fixe dHeart hIncinerato r wit hMaximu mHea t

Capacit y o f

1 6 mmBtu/hr . SDA- 2 Spra y Drye r Absorbe r

ai r pollutio ncontro l devic e fo r Uni t #2 . BH- 2 Fabri c Filte r ai r pollutio ncontro l devic e fo r Uni t #2 . Incineratio n Uni t

# 3 Fixe dHeart hIncinerato r wit hMaximu mHea t

Capacit y o f

1 6 mmBtu/hr . SDA- 3 Spra y Drye r Absorbe r

ai r pollutio ncontro l devic e fo r Uni t #3 . BH- 3 Fabri c Filte r ai r pollutio ncontro l devic e fo r Uni t #3 . Incineratio n Uni t

# 4 Rotar y Kil nIncinerato r (transportable ) wit hMaximu mHea t Capacit y o f

5 0 mmBtu/hr . Temperin g Chambe r

fo r Uni t #4 . Activate dCarbo n Injectio n i n Uni t #4 . SDA- 4 Spra y Drye r Absorbe r

ai r pollutio ncontro l devic e fo r Uni t #4 . BH- 4 Fabri c Filte r ai r pollutio ncontro l devic e fo r Uni t #4 . Materia l Processin g Are a # 1 (MP-1 ) Wast e Processin g Area s # 1 fo r processing/packagin g o f waste an drepackagin g o f containerize dwaste . Materia l Processin g Are a # 2 (MP-2 ) Wast e Processin g Area s # 2 fo r processing/packagin g o f waste an drepackagin g o f containerize dwaste . Activate dCarbo n Absorptio n pollutio ncontro l devic e fo r MP-2 . La b Pac k

Repac k Are a Wast e Processin g processing/packagin g an drepackagin g o f lab pac k wastes . Dru mCrushe r Empt y drum s are crushe di n athree-side dpartia l enclosure . Storag e Tank s fo r

Liquid Waste s an d#

2 Fue l Oi l Tanks : # 2 (4,39 1 gals.) , #

4 (4,93 1 gals.) , #

6 (7,20 0 gals.) , #

8 (5,82 0 gals.) , #1 0 (12,86 9 gals.) , #2 0 (12,86 9 gals.) , #3 0 (12,86 9 gals.) , #40 (12,86 9 gals.) , #5 0 (12,86 9 gals.) , #6 0 (12,86 9 gals.) , #30 0 (19,85 0 gals.) , #30 2 (30,00 0 gals.) , #30 4 (30,00 0 gals.) , #30 6 (30,00 0 gals.) , #30 8 (30,00 0 gals.) , #31 0 (30,00 0 gals.) , #31 2 (10,00 0 gals.) , #31 4 (10,00 0 gals.) . Activate dCarbo n Absorptio n pollution , contro l device s fo r Storag e Tan k

Vents . Storag e Tan k

fo r # 2 Fue l O i l Tan k #39 0 (30,00 0 gals.) . E P AFor m 5900-7 9GI S 

### 4

Bul k Fee dBuildin g Temporar y storag e o f bul k soli dwaste s befor e bein g fe dt o Incineratio n Uni t #4 . B FBld g - C A Activate dCarbo n Absorptio n Syste mpollutio ncontro l device s fo r Bul k Fee dBuilding . B FBldg-BH- 1 Baghous e wit hcyclon e precleane r ai r pollutio n contro l device s fo r Bul k Fee dBuilding . Boile r # 1 Natura l gas-fire dBoile r wit hMaximu mHea t

Capacit y o f

10. 6 mmBtu/h r

use dfo r generatin g steamfo r

the facility . EGEN1 , EGEN 2 # 2 Fue l oil-fire dEmergenc y Generator s wit hMaximu mHea t Capacit y o f

0.4 0 mmBtu/hr . Fugitiv e Emission s Pumps , valves , open-en dline s an dcompressors .

P P AFnr m qQOfW QGI S J . Facility Emission s Summar y Ente rpotentia l t o emi t (PTE ) fo rth e facilit ya s a whol e fo reac h ai rpollutan t liste d below . Ente rth e nam e o f th e singl e HA P emitte d i n th e greates t amoun t an d its PTE . Fo ral l pollutant s stipulation s to majo rsourc e statu s ma yb e indicate d byenterin g "major " i n th e spac e fo rPTE . Indicat e th e tota l actua l emission s fo rfe e purpose s fo rth e facilit yi n the spac e provided . Application s fo rpermi t modification s nee d not includ e actua l emission s information . NO x74.1 1 tons/y rVO C 23.5 4 tons/y rS0 2 67.1 9 tons/y r PM-1 0 14.8 7 tons/y rC O 30.8 5 tons/y rLea d 0.113 7 tons/y r Tota l HA P 32.6 2 tons/y r Singl e HA P emitte d i n th e greates t amoun t Benzen e PT E 0.3 8 tons/y r Tota l o f regulate d pollutant s (fo rfe e calculation) , Sec . F , lin e 5 o f for m FE E N/

Atons/y r K. Existin g Federally-Enforceabl e Permits Permi t number(s ) V-IL-1716300103-08-0 1 Permi t typ e Titl e V Permittin g authorityEP A Permi t number(s ) Permi t typ e Permittin g authority . L . Emissio n Unit(s) Covere d b y Genera l Permits Emissio n unit(s ) subject t o genera l permi t No t applicabl e Chec k one : Applicatio n mad e Coverag e grante d Genera l permi t identifie rExpiratio n Dat e ___!__] _

• M . Cross-reference d Informatio n Doe s thi s applicatio n cross-referenc e information ? X YE S N O (I f yes , se e instructions )

E P AFor m 5900-7 9

# SEP A Unite d State s £ n vi r0 n rTI 0 r1 1 

### u \ P r o t e G U o n Afjenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) INSIGNIFICAN TEMISSION S (IE ) O n thi s pag e lis t eac h insignifican t activit yo remissio n unit . I n th e "number " column , indicat e the numbe r o f unit s i n thi s category . Description s shoul d b e brie f bu t unique . Indicat e whic h emission s criterio n o f Numbe r Descriptio n o f Activitie s o rEmission s Unit s RAP , excep t HA P HA P 1 2. 5 mmBtu/h rTiog a portabl e boile r 1 A s h Handlin g 1 Handlin g o f Spen t Dr yScrubbe rSolid s 1 Lim e Unloadin g an d Proportionin g 1 Gasolin e Storag e Tan k 

### V 1 Diese l Fue l Storag e Tan k 1 Kerosen e Storag e Tan k </ 1 Us e o f Absorben t Materia l </ 1 Genera l Vehicl e Maintenanc e an d

Servicin g (assume d t o includ e diese l fue l handling ) 1 Laborator y 

### Y 1 Pipin g an d Storag e Syste m fo rNatura l

G a s 1 Non-halogenate d Col d Cleanin g

Degreaser s 

### / 1 Interna l Combustio n Engine s i n Moto r

Vehicle s N/ A Storag e an d Handlin g o f Close d Drum s

E P AFor m 5900-8 3jpb

iff - |^J i Unite d State s j^i^l^jL m Environmenta l Protectio n I r!• ! Agenc yOM B No . 2060-D336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D Incineratio n Uni t # 2 . Descriptio n Fixe d Heart h Incinerato r(1 6 mmBtu/hr ) , SI C Cod e (4-digit ) 495 3 . SC C Cod e 5030010 1 B . Emission s Uni t Descriptio n Primar yus e Hazardou s Wast e Incineratio n . Temporar ySourc e Ye s X N o Manufacture rTrad e Wast e Incineration . Inc . Mode l No . TWI-2000 . Serie s 2 . Seria l Numbe rN A ; ; Installatio n Dat e 9 / / 198 6 Boile rType : Industria l boile rProces s burne rElectri cutilit yboile r

X Othe r(describe ) Incinerato r. Boile rhorsepowe rratin g N ABoile rstea m flo w(Ib/h rN A. Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e . _Pulverized , we t be d Pulverized , dr ybe d Actua l Hea t Inpu t M M BTU/h rMax . Desig n Hea t Inpu t M M BTU/h r

E P AFor m 5900-8 0EUD- 1 C . Fue l Dat a

Primar yfue l tvpe(s ) Natura l Ga s Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%

) Max . As h Conten t (%) BT U Valu e (cf , gal. , o rlb. ) Natura l Ga s N A N A 105 0 BTU/c f

D . Fue l Usag e Rate s Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Natura l Ga s 5 2 mmcf t 0.015 2 13 3 mmcf t

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D SDA- 2 Devic e typ e Spra yDrye rAbsorbe r Ai rpollutant(s ) Controlle d HC I an d SQ 2 Manufacture rJov-Nir o Mode l No . Custo m , Seria l No . Installatio n dat e 9 / / 198 6 Contro l efficienc y(%) 99 % Efficienc yestimatio n metho d Performanc e Tes t

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D BH- 2 Devic e typ e Baghous e Ai rpollutant(s ) Controlle d PM/PM10/Lea d . Manufacturer , Mode l No . Custo m . Seria l No . Puls e Fl o

Installatio n dat e 9 / / 198 6 Contro l efficienc y(% ) < 0.0 8 grain s E P AFor m 5900-8 0EUD- 1 Efficienc yestimatio n metho d Performanc e Tes t

F . Ambien t Impac t Assessmen t No t Applicable . Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) Insid e stac k diamete r(ft ) Stac k temp(°F ) Desiq n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0Unite d State s Environmenta l Protectio n iAgenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D Incineratio n Uni t # 3 . Descriptio n Fixe d Heart h Incinerato r(1 6 mmBtu/hr ) . SI C Cod e (4-digit ) 495 3 . SC C Cod e 5030010 1 B . Emission s Uni t Descriptio n Primar yus e Hazardou s Wast e Incineratio n _ . Temporar ySourc e Ye s X N o Manufacture rTrad e Wast e Incineration . Inc . Mode l No . TWI-2000 . Serie s 2 . Seria l Numbe r_N A, Installatio n Dat e 9 / / 1986 Boile rType : Industria l boile rProces s burne rElectri cutilit yboile r

X Othe r(describe ) Incinerato r. Boile rhorsepowe rratin g N ABoile rstea m flo w(Ib/h rN A. Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e _Pulverized , we t be d Pulverized , dr ybe d Actua l Hea t Inpu t M M BTU/h rMax . Desig n Hea t Inpu t M M BTU/h r

E P AFor m 5900-8 0EUD C . Fue l Dat a

Primar yfue l tvpefs ) Natura l Ga s Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%

) Max . As h Conten t (%

) BT U Valu e

(cf , gal. , o rlb. ) Natura l Ga s N A N A 105 0 BTU/c f

Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Natura l Ga s 6 4 mmcft 0.009 5 8 3 mmcft

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D SDA- 3 . Devic e typ e Spra yDrve rAbsorbe r Ai rpollutant(s ) Controlle d HC I an d SQ 2 Manufacture rJov-Nir o Mode l No . Custo m . Seria l No. _ Installatio n dat e 9 / / 198 6 Contro l efficienc y(% ) 99 % Efficienc yestimatio n metho d Performanc e Tes t

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D BH- 3

_ . Devic e typ e Baghous e Ai rpollutant(s ) Controlle d PM/PM10/Lea d . Manufacturer , Mode l No . Custo m . Seria l No . Puls e Fl o

Installatio n dat e 9 / / 198 6 Contro l efficienc y(% ) < O.Q 8 grain s E P AFor m 5900-8 0EUD- 1 3

Efficienc yestimatio n metho d Performanc e Tes t

F . Ambien t Impac t Assessmen t No t Applicable . Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heiqh t (ft ) Insid e stac k diamete r(ft ) Stac k temp(°F ) Desig n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D Incineratio n Uni t # 4 . Descriptio n Rotar yKil n (5 0 mmBtu/hr ) SI C Cod e (4-digit ) 495 3 . SC C Cod e 5030010 1 B . Emission s Uni t Descriptio n Primar yus e Hazardou s Wast e Incineratio n Temporar ySourc e Ye s X N o Manufacture rInternationa l Wast e Energ yMode l No . PY*RQ X , Seria l Numbe r_N A tInstallatio n Dat e 9 / / 198 6 Boile rType : Industria l boile rProces s burne rElectri cutilit yboile r

XOthe r(describe ) Incinerato r= . Boile rhorsepowe rratin g N ABoile rstea m flo w(Ib/h rN A Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e Pulverized , we t be d Pulverized , dr ybe d Actua l Hea t Inpu t M M BTU/h rMax . Desig n Hea t Inpu t M M BTU/h r

E P AFor m 5900-8 0C . Fue l Dat a

Primar yfue l tvpefs ) Natura l Ga s Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%) Max . As h

Conten t (%) BT U Valu e (cf , gal. , o rlb. ) Natura l Ga s N A N A 105 0 BTU/c f

D . Fue l Usag e Rate s Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Natura l Ga s 13 7 mmcft 0.015 2 133. 5 mmcft

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D SDA- 4 . Devic e typ e Spra yDrve rAbsorbe r Ai rpollutant(s ) Controlle d HC I an d SQ 2 Manufacture r Mode l No . Custo m . Seria l No . Installatio n dat e 6 / / 1988 Contro l efficienc y(%) 99 % Efficienc yestimatio n metho d Performanc e Tes t

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D BH- 4 . Devic e typ e Baghous e Ai rpollutant(s ) Controlle d PM/PM10/Lea d . Manufacturer , Mode l No . Custo m . Seria l No . Wheelabrato r

Installatio n dat e 6 / / 1988 Contro l efficienc y(%) 99 % E P AFor m 5900-8 0EUD- 1 3

Efficienc yestimatio n metho d Performanc e Tes t

F . Ambien t Impac t Assessmen t No t Applicable . Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heiqh t (ft ) Insid e stac k diamete r(ft ) Stac k temp(°F ) Desig n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0<ff c•^•"IJI t Unite d State s

»g*gf » w ^W

&ffuk Environmenta l Protectio n JmAgenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D EGEN 1 Descriptio n Emergenc yGenerato r< 11 2 k W (150. 2 HP ) SI C Cod e (4-digit ) SC C Cod e . B . Emission s Uni t Descriptio n Primar yus e Emergenc yPowe rfo rPlan t Operation s Temporar ySourc e Ye s X N o Manufacture r: Mode l No . Seria l Numbe rInstallatio n Dat e / / Boile rType : Industria l boile rProces s burne rElectri cutilit yboile r Othe r(describe ) Boile rhorsepowe rratin g Boile rstea m flo w(Ib/hr ) Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e Pulverized , we t be d Pulverized , dr ybe d Actua l Hea t Inpu t M M BTU/h rMax . Desig n Hea t Inpu t M M BTU/h r

E P AFor m 5900-8 0EUD- 1 C . Fue l Dat a

Primar yfue l type(s ) Diese l Fue l Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%

) Max . As h Conten t (%) BT U Valu e (cf , gal. , o rlb. ) Diese l Fue l 0.0 5 0.013 7 MMBtu/ga l

D . Fue l Usag e Rate s Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Diese l Fue l 28 gallon s 13,96 0 gallon s

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e Devic e typ e Ai rpollutant(s ) Controlle d Manufacture r Mode l No . Seria l No . Installatio n dat e / / Contro l efficienc y(%) Efficienc vestimatio n metho d

E P AFor m 5900-8 0EUD- 1 3

F . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heiqh t (ft ) N A Insid e stac k diamete r(ft ) Stac k temp(°F ) Desiq n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D EGEN 2 Descriptio n Emergenc yGenerato r< 11 2 k W (150. 2 HP ) SI C Cod e (4-digit ) SC C Cod e B . Emission s Uni t Descriptio n Primar yus e Emergenc yFir e Wate rPum p Temporar ySourc e Ye s X N o Manufacture rMode l No . Seria l Numbe rInstallatio n Dat e / / Boile rType : Industria l boile rProces s burne rElectri cutilit yboile r Othe r(describe ) Boile rhorsepowe rrating

_ Boile rstea m flo w(Ib/hr ) Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e Pulverized , we t be d . Pulverized , dr ybe d Actua l Hea t Inpu t M M BTU/h rMax . Desig n Hea t Inpu t M M BTU/h r

E P AFor m 5900-8 0EUD- 1 

### 2

C . Fue l Dat a Primar yfue l type(s ) Diese l Fue l Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%

) Max . As h Conten t (%

) BT U Valu e

(cf , gal. , o rlb. ) Diese l Fue l 0.0 5 0.013 7 MMBtu/ga l

D . Fue l Usag e Rate s Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Diese l Fue l 2 8 gallon s 13,96 0 gallon s

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e Devic e typ e Ai rpollutant(s ) Controlle d Manufacture r Mode l No . Seria l No . Installatio n dat e / / Contro l efficienc y(%) Efficienc vestimatio n metho d

E P AFor m 5900-8 0EUD- 1 3

F . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) N A Insid e stac k diamete r(ft ) Stac k temp(°F ) Desig n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0

# EF W Unite d State s Environmenta l Protectio n Agenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Bul k Fee d Bld q (B F Bldo ) Descriptio n Temporar yStorag e i n pit s prio rt o feedin g int o Incineratio n Uni t # 4 SI C Cod e (4-dioi n 495 3 S C C Cod e 5030083 0 B . Emission s Uni t Descriptio n Equipmen t typ e N A Manufacture rN A _ . Temporar ySourc e Ye s X N o

. Mode l No . N A Seria l Numbe r Installatio n Dat e 51 I 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d • Overspra y(surfac e coating ) (%) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D B F Bldo . BH- 1 . Devic e tvp e Baghous e Manufacture rAirto l Inc . . Mode l No . 49AS0 7 Seria l Numbe r . Installatio n Dat e 1 1 / / 198 8 Contro l efficienc v(%

) Captur e efficienc y(%) Ai rpollutant s controlle d PM/PM1 0 . Efficienc yestimatio n metho d C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D B F Bldo . C A Devic e tvo e Activate d Carbo n Adsorptio n Svste m Manufacture r . Mode l No . Seria l Numbe r Installatio n Dat e 1 1 / / 198 8 Contro l efficienc v(%

) Captur e efficienc y(%) Ai rpollutant s controlle d VO M . Efficienc yestimatio n metho d D . Ambien t Impac t Assessmen t E P AFor m 5900-8 1EUD- 2 2

Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 7 0 Insid e stac k diamete r(ft ) . Stac k tem p (F ) ambien t . Desig n stac k flo wrat e (ACFM ) 5,00 0 . Actua l stac k

flo wrat e (ACFM ) 2.50 0 . Velocit y(ft/sec ) .

E . VOC-containin g Substanc e Dat a Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i f providin g a bran d name , includ e th e nam e o f th e manufacture ; i f th e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1

## Sir 

# EPA Unite d State s Environmenta l Protectio n Agenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Dru m Crushe r. Descriptio n Crushe r SI C Cod e (4-digit ) 495 3 . SC C Cod e 3018000 1 B . Emission s Uni t Descriptio n Equipmen t tvp e Crushe rwit h hoppe r Manufacture rCusto m Buil t Seria l Numbe r . Temporar ySourc e .Ye s X N o Mode l No . N A ; Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (% ) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e . Devic e tvp e Manufacture r . Mode l No . Seria l Numbe r Installatio n Dat e / / Contro l efficienc v(%) Captur e efficienc v(%) Ai rpollutant s controlle d . Efficienc yestimatio n metho d D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) Stac k tem p (F ) Insid e stac k diamete r(ft ) Actua l stac k

flo wrat e (ACFM) . Desig n stac k flo wrat e (ACFM) ,

. Velocit y(ft/sec )

E P AFor m 5900-8 1EUD- 2 2

E . VOC-containin g Substanc e Dat a Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1Unite d State s Ff^F^kAgen& V • OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 

# -ew— — Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D La b Pac k Repac k Are a . Descriptio n Reoackin a o f La b Pac k Wast e . SI C Cod e (4-digit ) 495 3 . SC C Cod e 3018000 1

(4-digit B . Emission s Uni t Descriptio n Equipmen t tvp e Openin g containers / transfe rt o containers . Temporar ySourc e Ye s X N o Manufacture rN A^ Mode l No . N A t Seria l Numbe r_N A, Installatio n Dat e / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d ; Overspra y(surfac e coating ) (% ) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e . Devic e typ e Manufacture rMode l N o Seria l No . Installatio n dat e Contro l efficienc y(%

) . Captur e efficienc y(%) Ai rpollutant(s ) controlle d Efficienc yestimatio n metho d D . Ambien t Impac t Assessmen t No t Applicabl e Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) . Insid e stac k diamete r(ft ) . Stac k tem p (F ) . Desig n stac k flo wrat e (ACFM) . Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec ) _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1Unite d State s Environmenta l Protectio n Agenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Materia l Processin g Are a # 1 (MP-1 1 Descriptio n Processing/Repackin g Waste . SI C Cod e (4-digit ) 495 3 . SC C Cod e 5030081 0 B . Emission s Uni t Descriptio n Equipmen t tvp e Openin g containers / transfe rt o containers . Temporar ySourc e Ye s XN o Manufacture rN A. Mode l No . N A. Seria l Numbe r_N A, Installatio n Dat e / / 198 8 Article s bein g coate d o rdegrease d ; Applicatio n metho d : Overspra y(surfac e coating ) (%) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e Devic e tvp e Manufacture r Mode l N o Seria l No . Installatio n dat e / / Contro l efficienc y(%) Captur e efficienc y(%) Ai rpollutant(s ) controlle d Efficienc yestimatio n metho d D . Ambien t Impac t Assessmen t No t Applicabl e Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) . Insid e stac k diamete r(ft ) . Stac k tem p (F ) . Desig n stac k flo wrat e (ACFM ) _ Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec ) _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Materia l Processin a Are a # 2 (MP-2) . Descriptio n Processing/Repackin g Waste . SI C Cod e (4-diait t 495 3 . SC C Cod e 5030081 0 B . Emission s Uni t Descriptio n Equipmen t tvp e Openin g containers / transfe rt o containers . Temporar ySourc e Ye s XN o Manufacture rN A ; Mode l No . N A Seria l Numbe r_N A. . Installatio n Dat e / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (% ) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e . Devic e tvp e Manufacture r Mode l N o Seria l No . Installatio n dat e / / Contro l efficienc y(%) Captur e efficienc v(%) Ai rpollutant(s ) controlle d Efficienc yestimatio n metho d D . Ambien t Impac t Assessmen t No t Applicabl e Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) . Insid e stac k diamete r(ft ) . Stac k tem p (F ) . Desig n stac k flo wrat e (ACFM) . Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec ) _ E . VOC-containin g Substanc e Dat a F P AFnr m RqOO-R IEUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) CA S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1A|"*"f% * Unite d State s

^^MMjayjrj ^

Enviro n menta l Protectio n L - l jffmAgeno yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N UNI TDESCRIPTIO N FO R FUE L COMBUSTIO N SOURCE S (EUD-1 ) A . Genera l Informatio n Emission s uni t I D Boile r# 1 Descriptio n Boile rfo rStea m Generatio n SI C Cod e (4-digit ) 495 3 . S C C Cod e 1030060 2

(4-digit B . Emission s Uni t Descriptio n Primar yus e Stea m Generation/Fue l Combustio n Temporar ySourc e Ye s XN o Manufacture rCleave rBrook s . Mode l No . 25 0 _ . Seria l Numbe rN A, Installatio n Dat e 1 1 / / 199 5 Boile rType : XIndustria l boile rProces s burne rElectri cutilit yboile r

, Othe r(describe ) " Boile rhorsepowe rratin g Boile rstea m flo w(Ib/h r_ . Typ e o f Fuel-Burnin g Equipmen t (coa l burnin g only) : Han d fire d Spreade rstoke rUnderfee d stoke rOverfee d stoke r Travelin g grat e Shakin g grat e Pulverized , we t be d Pulverized , drybe d Actua l Hea t Inpu t 10. 6 M M BTU/h rMax . Desig n Hea t Inpu t 10. 6 M M BTU/h r

E P AFor m 5900-8 0

### ;ud- i C . Fue l Dat a

Primar yfue l type(s ) Natura l Ga s Standb yfue l type(s) _ Describ e eac h fue l yo u expecte d t o us e durin g th e ter m o f th e permit .

Fue l Typ e Max . Sulfu r Conten t (%

) Max . As h Conten t (%

) BT U Valu e

(cf , gal. , o rlb. ) Natura l Ga s N A N A 105 0 BTU/c f

Fue l Typ e Annua l Actua l Usag e Maximu m Usag e

Hourl yAnnua l Natura l Ga s 1 3 mmcft 0.009 5 83.4 3 mmcf t

E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e Devic e typ e Ai rpollutant(s ) Controlled . Mode l No . Manufacture r Seria l No . Installatio n dat e / / _ Contro l efficienc y(%) _ Efficienc yestimatio n metho d E . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Devic e type , Ai rpollutant(s ) Controlled . Mode l No . Manufacture r Seria l No . Installatio n dat e



## _

/ / _ Contro l efficienc y(%) _ Efficienc yestimatio n metho d

E P AFor m 5900-8 0EUD- 1 3

Efficienc yestimatio n metho d

F . Ambien t Impac t Assessmen t No t Applicable . Thi s informatio n mus t b e complete d b ytemporar ysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heiqh t (ft ) Insid e stac k diamete r(ft ) Stac k temp(°F ) Desig n stac k flo wrat e (ACFM ) Actua l stac k

flo wrat e (ACFM ) Velocit y(ft/sec )

E P AFor m 5900-8 0A l^lf^ AUnite d State s

^ggjgS yj M i B ^ p % Enviro n menta l Protectio n ^IJ rIm f JltAgertC Y OM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k # 2 . Descriptio n 4.93 1 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s X N o Manufacture rModer n Weldin g tMode l No . N A Seria l Numbe rS-4869-TK 2 k Installatio n Dat e 4 / / 200 2 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method _ No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC# 2 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n , Mode l No . N-100X P o reouivalen t Seria l Numbe rN A, Installatio n Dat e 4 / / 200 2 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % , Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) __ 4 . Insid e stac k diamete r(ft ) 0.3 3 , Stac k tem p (F ) 62. 4 , Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1-fl k

rHFlJf c ynite d State s • 

# « '*hw ^r^W^LEnvironmenta l Protectio n yfca l rtAgeng yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k # 4 __ _Descriptio n 4.93 1 gallo n capacit y SI C Cod e (4 -diait i 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Linui d Storag e Tan k _Temporar ySourc e Ye s _X _N o Manufacture rModer n Weldin g . Mode l No . N A__ , Seria l Numbe rS-4869-TK 4 _Installatio n Dat e 4 / / 200 2 Article s bein g coate d ordegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method _ No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC# 4 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe rN A. Installatio n Dat e 4 / / 200 2 Contro l efficienc y(%) 95-98 % Captur e efficienc y(%) 100 % , Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) __ 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a

E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

F P AFnr m RqnO-8 1

### i*%Jf cUnite d State s m^MM Environmenta l Protectio n

.. . I JTHIlAgenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k # 6 . Descriptio n 7.20 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s _JL .N o Manufacture rModer n Weldin g . Mode l No . N A. Seria l Numbe rS-4869-TK 6 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o fdryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai rPollutio n Contro l Equipmen t Emission s uni t I D C C #6 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . . Mode l No . N-100X P o requivalen t Seria l Numbe rJ_ \

. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(%) 100 % Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) 4 , Insid e stac k diamete r(ft ) 0.3 3 _ Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) .. _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

F=P AFnr m c;qnn-R 14%1JTM1T| AUnite d State s 

# f %^lT % H t

Environmenta l Protectio n WmmmM M m Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k # 8 tDescriptio n 5.28 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvo e Lioui d Storag e Tan k Temporar ySourc e Ye s JL.N o Manufacture rModer n Weldin g Mode l No . N A. Seria l Numbe rS-4869-TK 8 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d : ; Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D C C # 8 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n , Mode l No . N-100X P o requivalen t Seria l Numbe rN A. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%) 95-98 % Captur e efficienc y(%) 100 % Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 , Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . . E . VOC-containin g Substanc e Dat a

—:r> AI--- TM rnm_0 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

F P AFnr m ^QDO-R IUnite d State s

^fFmamW

M m Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 jjjji&Sm^"^^^^

Environmenta l Protectio n Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #1 0 . Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvo e Liqui d Storag e Tan k Temporar ySourc e Ye s _X__N o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK1 0 . Installatio n Dat e 6 / / 200 4 Article s bein g coate d o rdegrease d \ . Applicatio n metho d Overspra y(surfac e coating ) (% ) Dryin g method _ No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#1 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n Mode l No . N-100X P o requivalen t Seria l Numbe rN A, , Installatio n Dat e 6 / / 200 4 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % . Ai rpollutant(s ) controlle d VOM/Qmani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) ______ _ Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a F D AFnr m ^QOO-R IEUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t the emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e the nam e o fthe manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1

# S CD A Unite d State s Environmenta l Protectio n Agenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #2 0 . Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g , Mode l No . N A, . Seria l Numbe rS-4869-TK2 0 - . Installatio n Dat e 6 / / 200 4 Article s bein g coate d ordegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#2 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe rJ_ A_Installatio n Dat e 6 / / 200 4 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % . Ai rpollutant(s ) controlle d VOM/Oraani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 tDesig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) ________ _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1^"N-f

r ^^^ ^ |_P S8^

_f _P_

_W U I

I IV. ! •_tM\«^- J ^j^|«-ip^^^Erivimnrrienta l Protectio n Unite d State s Environment . Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #3 0 . Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-dioit t 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Lioui d Storag e Tan k Temporar ySourc e Ye s _X_.N o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK3 0 , . Installatio n Dat e 3 / / 200 9 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D C C #3 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o requivalen t Seria l Numbe rN A. Installatio n Dat e 3 / / 200 9 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(%) 100 % . Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a F P AFor m ^QOD-R IEUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1H . l^jpiyp t Unite d State s irmAgenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #4 0 Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k ; . Temporar ySourc e Ye s ____N o Manufacture rModer n Weldin g . Mode l No . N A. Seria l Numbe rS-4869-TK4 0 , . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D C C #4 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o requivalen t Seria l Numbe r_N A. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%) 95-98 % Captur e efficienc y(% ) 100 % _ Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e the nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1AW mm^%Mk Unite d State s Environmenta l Protectio n M _Agenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #5 0 Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k Temporar ySourc e Ye s ___N o Manufacture rModer n Weldin g . Mode l No . N A. Seria l Numbe rS-4869-TK5 0 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d ; Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#5 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n Mode l No . N-100X P o reouivalen t Seria l Numbe rJ_ A. Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) ___

4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 , Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e the nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

F P AFor m 5900-8 1%T^T%£k Ursite d State s I_!_#_P"I III _H_ . Environmenta l Protectio n |__| M »Agenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #6 0 . Descriptio n 12.86 9 gallo n capacit y SI C Cod e (4-diait ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g Mode l No . N A. Seria l Numbe rS-4869-TK6 0 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d . Overspra y(surfac e coating ) (% ) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D C C #6 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe r____

_. Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(%) 100 % . Ai rpollutant(s ) controlle d VQM/Qrgani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1___D A Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #30 0 . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Lioui d Storag e Tan k . Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g . Mode l No . N A. Seria l Numbe rS-4869-TK30 0 Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d : Applicatio n metho d Overspra y(surfac e coating ) (% ) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#30 0 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n Mode l No . N-100X P o reouivalen t Seria l Numbe r_N A. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%) 95-98 % Captur e efficienc y(% ) 100 % . Ai rpollutant(s ) controlle d VOM/Oraani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 , Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) __. _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

F P AFor m ^QDO-R Ijff % ip - ^%Jf k Unite d State s ^gj^lMp^L! | Environmenta l Protectio n ^ / F ___ J ifmAgeno V OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #30 2 . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvn e Liqui d Storag e Tan k Temporar ySourc e Ye s _X_N o Manufacture rModer n Weldin g _Mode l No . N A. Seria l Numbe rS-4869-TK30 2 Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d . Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#30 2 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l Nn . N-100X P o reouivalen t Seria l Numbe rJ_ A. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%) 95-98 % Captur e efficienc y(%) 100 % . Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . lnfo__ D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) 4 , Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t the emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (ib/gal )

N A

E P AFor m 5900-8 1Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #30 4 . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s _J__.N o Manufacture rModer n Weldin g . Mode l No . N A. _ Seria l Numbe rS-4869-TK30 4 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#30 4 Devic e typ e Activate d Carbo n Caniste r• Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe r_N AInstallatio n Dat e 5 / / 1988 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % . Ai rpollutant(s ) controlle d VOM/Qroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 , Insid e stac k diamete r(ft ) 0.3 3 __ . Stac k tem p (F ) 62. 4 , Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a

P P AFrvr m ^QDO-R !EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (lb/gal )

N A

E P AFor m 5900-8 1W%M l Unite d State s 

### fc^&A Environmenta l Protectio n 

### „ I _rT

_Ag&liey OM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #30 6 . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Lioui d Storag e Tan k . Temporar ySourc e Ye s JL .N o Manufacture rModer n Weldin g . Mode l No . N A. Seria l Numbe rS-4869-TK30 6 .. . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d ; Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#30 6 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe rJ_ A, Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%) 95-98 % Captur e efficienc y(%) 100 % , Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fthe manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

-

E P AFor m 5900-8 1

# EP A

J % %_§

_

Unite d State s Environmenta l Protectio n .Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #30 8 . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-diait . 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Lioui d Storag e Tan k . Temporar ySourc e Ye s ____N o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK30 8 . Installatio n Dat e 5 / / 1988 Article s bein g coate d o rdegrease d [ Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#30 8 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n Mode l No . N-100X P o requivalen t . Seria l Numbe rJ_ A. Installatio n Dat e 5 / / 1988 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(%) 100 % . Ai rpollutant(s ) controlle d VOM/Qroani cHA P . Efficienc yestimatio n metho d Mfo . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 , Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat aEUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) CA S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1Unite d State s Environmenta l Protectio n Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #31 0 ; . Descriptio n 30.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Lioui d Storag e Tan k , Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK31 0 Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (% ) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal) . C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#31 0 Devic e typ e Activate d Carbo n Caniste r. Manufacture rTIG G Corporatio n Mode l No . N-100X P o reouivalen t Seria l Numbe r_N A, Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%) 95-98 % Captur e efficienc y(%) 100 % . Ai rpollutant(s ) controlle d VOM/Oraani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a F P AFnr m 5 900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1

### £%

W

m 

### W%i

l 

### (k ' Unite d State s Environmenta l Protectio n i Agenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #31 2 , Descriptio n 10.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s X N o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK31 2 . Installatio n Dat e 5 / / 1988 Article s bein g coate d o rdegrease d ; Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#31 2 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe rJ

_. Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%

) 95-98 % Captur e efficienc y(% ) 100 % . Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 . Insid e stac k diamete r(ft ) 0.3 3 Stac k tem p (F ) 62. 4 Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) <10 0 . Velocit y(ft/sec ) . _ E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1

## 0%

T m 

## W%Mk

Unite d State s *^^:W^V^^M

Environmenta l Protectio n 

## mWlLm*

_F m Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #31 4 , Descriptio n 10.00 0 gallo n capacit y SI C Cod e (4-digit ) 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t tvp e Liqui d Storag e Tan k . Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g . Mode l No . N A Seria l Numbe rS-4869-TK31 4 . Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g method . No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D CC#31 4 Devic e typ e Activate d Carbo n Caniste r Manufacture rTIG G Corporatio n . Mode l No . N-100X P o reouivalen t Seria l Numbe rJ_ A, . Installatio n Dat e 5 / / 198 8 Contro l efficienc y(%) 95-98 % Captur e efficienc y(% ) 100 % , Ai rpollutant(s ) controlle d VOM/Oroani cHA P . Efficienc yestimatio n metho d Mfg . Info . D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d b ytemporarysource s o rwhe n ambien t impact assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s not common) . Stac k heigh t (ft ) 4 tInsid e stac k diamete r(ft ) 0.3 3 . Stac k tem p (F ) 62. 4 . Desig n stac k flo wrat e (ACFM ) 10 0 Actua l stac k

flo wrat e (ACFM ) < 10 0 Velocit y(ft/sec ) . E . VOC-containin g Substanc e Dat a E P AFor m 5900-8 1EUD- 2 2

Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t the emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e the nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) CA S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

N A

E P AFor m 5900-8 1

### W0 

# EP A Unite d State s Environmenta l Protectio n Agenc y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSION S UNI TDESCRIPTIO N FO R VO C EMITTIN G SOURCE S (EUD-2 ) A . Genera l Informatio n Emission s uni t I D Tan k #39 0 Descriptio n 30.00 0 gallo n capacit y SICCode.4-dic.it . 495 3 . SC C Cod e 3019999 8 B . Emission s Uni t Descriptio n Equipmen t typ e Liqui d Storag e Tan k

_Temporar ySourc e Ye s XN o Manufacture rModer n Weldin g Seria l Numbe rS-4869-TK39 0 Mode l No . N A Installatio n Dat e 5 / / 198 8 Article s bein g coate d o rdegrease d Applicatio n metho d Overspra y(surfac e coating ) (%) Dryin g metho d No . o f dryer s Tan k capacit y(degreasers ) (gal ) C . Associate d Ai r Pollutio n Contro l Equipmen t Emission s uni t I D Non e . Devic e tvp e Manufacture r . Mode l No . Seria l Numbe r Installatio n Dat e / / Contro l efficienc v(% ) Captur e efficienc v(% ) Ai rpollutant s controlle d . Efficienc vestimatio n metho d D . Ambien t Impac t Assessmen t Thi s informatio n mus t b e complete d bytemporarysource s o rwhe n ambien t impac t assessmen t i s a n applicabl e requiremen t fo rthi s emission s uni t (thi s i s no t common) . Stac k heigh t (ft ) Stac k tem p (F ) Insid e stac k diamete r(ft ) Actua l stac k

flo wrat e (ACFM) , Desig n stac k flo wrat e (ACFM) ,

. Velocit y(ft/sec )

E P AFor m 5900-8 1EUD- 2 2

E . VOC-containin g Substanc e Dat a Lis t eac h VOC-containin g substanc e consumed , processe d o rproduce d a t th e emission s uni t tha t i s emitte d int o th e air . I n th e nam e column , i fprovidin g a bran d name , includ e th e nam e o fth e manufacture ; i fth e substanc e contain s HAP , lis t th e constituen t HAP . Substanc e Nam e (Chemical , Bran d Name ) C A S No . Substanc e Typ e Actua l

Usag e (gal/yr ) Ma x

Usag e (gal/day ) Ma x

Usag e (gal/year ) V O C

Conten t (Ib/gal )

Diese l Fue l N A

E P AFor m 5900-8 1

### £%

J^W^kgk

Unite d State s _*_ f i^lr_^ % Ew'TOnmenta l Protectio n ^UFfc-f l W \ Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Uni t # 2 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . C O 2.5 5 6. 6 VO M 8. 0 0. 9 NO x 3.2 6 4. 0 PM2. 5 0.140 5 0.615 6 PM1 0 0.638 8 2. 8 Par t 0.638 8 2. 8 SO x 1.2 1 7. 7 HCI/CI 2 2.1 9 9.9 2

E P AFor m 5900-8 4Ai rPollutant s Emissio n Rate s CA S No .

Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l to Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr ) CA S No . H g 0.002 8 0.012 5 7439-97- 6 A s 0.002 0 0.008 8 7440-38- 2 B e 0.002 0 0.008 8 7440-41- 7 C d 0.005 0 0.022 1 7440-43- 9 C r 0.002 0 0.008 8 7440-47- 3 S b 0.002 0 0.008 8 7440-31- 5 P b 0.005 0 0.022 1 7439-92- 1 N i 0.002 0 0.008 8 7440-02- 0 Dioxin/Fura n 4.3 8 x10" 9 1.9 2 x10" 8

E P AFor m 5900-8 4A

# W m 

# W%ik Unite d State s 

# m^^ J^W^Mm

Environmenta l Protectio n ^UFIwJ - J~"H.Ageno ¥OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Uni t # 3 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No , Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No , Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No , C O 2.6 5 6. 6 VO M 8. 0 0. 9 NO x 3.2 6 4. 0 PM2. 5 0.146 2 0.640 4 PM1 0 0.664 6 2.9 1 Part 0.664 6 2.9 1 SO x 1.2 1 7. 7 HCI/CI 2 2.2 2 10.0 3

E P AFor m 5900-8 4Ai rPollutant s Emissio n Rate s CA S No .

Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . H g 0.002 9 0.013 0 7439-97- 6 A s 0.002 1 0.009 2 7440-38- 2 B e 0.002 1 0.009 2 7440-41-7 C d 0.005 2 0.022 9 7440-43- 9 C r 0.002 1 0.009 2 7440-47- 3 S b 0.002 1 0.009 2 7440-31- 5 P b 0.005 2 0.022 9 7439-92- 1 N i 0.002 1 0.009 2 7440-02- 0 Dioxin/Fura n 2.7 3 x10" 8 1.2 0 x10" 7

E P AFor m 5900-8 4£%WP*W%gk Unite d State s l8_fl^iif ^

Environmenta l Protectio n ^#lwJ

_f l Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Uni t # 4 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . C O 8.0 3 13.8 6 VO M 8 3. 1 NO x 14.6 1 61. 6 PM2. 5 0.443 2 1.94 PM1 0 2.0 1 16.9 2 Part 2.0 1 16.9 2 SO x 4.2 3 50.7 6 HCI/CI 2 2.3 8 10.4 0

E P AFor m 5900-8 4Ai rPollutant s Emissio n Rate s CA S No .

Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . H g 0.009 0 0.039 3 7439-97- 6 A s 0.006 4 0.027 8 7440-38- 2 B e 0.006 4 0.027 8 7440-41-7 C d 0.015 9 0.069 5 7440-43- 9 C r 0.006 4 0.027 8 7440-47- 3 S b 0.006 4 0.027 8 7440-31- 5 P b 0.015 9 0.069 5 7439-92- 1 N i 0.006 4 0.027 8 7440-02- 0 Dioxin/Fura n 1.5 2 x10" 7 6.6 5 x10' 7

E P AFor m 5900-8 4

# _% T m 

# W%M

l 

# k Unite d 

### State

s 

### 1— 1 -PmAgftno y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Bul k Fee d Buildin g (B F Bldg ) B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l to Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . VO M 0.583 6 2.5 6 Benzen e 0.004 3 0.018 8 71-43- 2

E P AFor m 5900-8 44 f h Unite d State s

^%f*^^p3l k

Environmenta l Protectio n ^yM__

_-T%Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h the application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Dru m Crushe r B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . VO M 0.88 3 3.8 7 Benzen e 0.05 7 0.24 8 71-43- 2

E P AFor m 5900-8 4jp| l |P"r^|J k Unite d State s _l!^i^_r^W

_Environmenta l Protectio n ^jF-L- M __TT.Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D LabPac k Repac k B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . VO M 0.332 1 1.4 5 Benzen e 0.055 2 0.241 8 71-43- 2

E P AFor m 5900-8 4•*%Ji

_Unite d State s IpffijU h Environmenta l Protectio n I J r mAgene yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D MP- 1 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l

(tons/yr) CA S No . VO M 0.054 5 0.238 7 Benzen e 0.036 6 0.049 5 71-43- 2

E P AFor m 5900-8 4W^F^jSk Unite d State s Environmenta l Protectio n " M Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . i f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D MP- 2 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l

(tons/yr ) CA S No . VO M 0.054 5 0.238 7 Benzen e 0.036 6 0.049 5 71-43- 2

E P AFor m 5900-8 40%}^W %Mk Unite d State s sgi^yTMi«^L AEnvironmenta l Protectio n ^ F l— l J r m Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D Boile r# 1 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . C O 0.86 3 3.7 9 VO M 0.05 7 0.24 8 NO x 1.0 3 4.5 1 PM2. 5 0.07 8 0.34 3 PM1 0 0.07 8 0.34 3 Part 0.07 8 0.34 3 NH 3 0.03 3 0.14 4 SO x 0.00 6 0.02 7

E P AFor m 5900-8 4W%ik Unite d State s W ^£L\ Environmenta l Protectio n 

### 1 J m Agenc

y OM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D EGE N 1 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l to Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l (tons/yr) CA S No . C O 0.3 6 0.0 9 VO M 0.1 3 0.0 3 NO x 1.6 9 0.4 2 PM2. 5 0.1 2 0.0 3 PM1 0 0.1 2 0.0 3 Par t 0.1 2 0.0 3 SO x 0.1. 1 0.0 3 HA P 0.000 5 0.000 1

E P AFor m 5900-8 4

## g%

w**w*%Mk

Unite d State s ^ppfl l Environmenta l Protectio n

Agenc yOM B No . 2060-0336 , Approva l Expire s 06/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) EMISSIO N CALCULATION S (EMISS ) Calculat e potentia l t o emi t (PTE ) fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo r eac h emission s unit , contro l device , o ralternativ e operatin g scenari o identifie d i n sectio n I o f for m GIS . I f for m FE E doe s no t nee d t o b e submitte d wit h th e application , d o no t calculat e actua l emissions . A . Emission s Uni t I D EGE N 2 B . Identificatio n an d Quantificatio n o fEmission s First , lis t eac h ai rpollutan t tha t i s eithe rregulate d a t th e uni t o rpresen t i n majo ramounts , the n lis t an yothe r regulate d pollutan t (fo rfe e calculation ) no t alread ylisted . HA P ma yb e simpl yliste d a s "HAP. " Next , calculat e PT E fo rapplicabilit ypurpose s an d actua l emission s fo rfe e purpose s fo reac h pollutant . D o no t calculat e PT E fo rai rpollutant s liste d solel yfo rfe e purposes . Includ e al l fugitive s fo rfe e purposes . Yo u ma y roun d t o th e neares t tent h o f a to n fo ryearl yvalue s o rtent h o f a poun d fo rhourl yvalues .

Ai rPollutant s Emissio n Rate s CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Potentia l t o Emi t CA S No . Ai rPollutant s Actua l Annua l Emission s (tons/yr) Hourl y

(Ib/hr ) Annua l

(tons/yr) CA S No . C O 0.3 6 0.0 9 VO M 0.1 3 0.0 3 NO x 1.6 9 0.4 2 PM2. 5 0.1 2 0.0 3 PM1 0 0.1 2 0.0 3 Part 0.1 2 0.0 3 SO x 0.1 1 0.0 3 HA P 0.000 5 0.000 1

E P AFor m 5900-8 4

### W m 

### W%gk Unite d State s lit^l^B^^ - Environmenta l Protectio n ^#_L_t l Agenc yOM B NO . 2060-0336 , Approva l Expire s 06/30/201 5 

## Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) POTENTIA L T O EMI T(PTE ) Fo reac h uni t wit h emission s tha t coun t toward s applicability , lis t th e emission s uni t I D an d th e PT E fo r th e ai rpollutant s liste d belo wan d su m the m u p t o sho wtotal s fo rth e facility . Yo u ma yfin d i t helpfu l t o complet e for m EMIS S befor e completin g thi s form . Sho wothe rpollutant s no t liste d tha t ar e presen t i n majo ramount s a t th e facilit yo n attachmen t i n a simila rfashion . Yo u ma yroun d value s t o th e neares t tent h o fa ton . Als o repor t fac i it ytotal s i n sectio n J o ffor m GIS . Emission s Uni t I D Regulate d Ai rPollutant s an d Pollutant s fo rwhic h th e Sourc e i s Majo r (tons/yr ) NO x V O C S 0 2 PM1 0 C O Lea d HA P UNI T# 2 4. 0 0. 9 7. 7 2.8 0 6. 6 0.022 1 11.0 4 UNI T#3 4. 0 0. 9 7. 7 2.9 1 6. 6 0.022 1 10.4 0 UNI T# 4 61. 6 3. 1 51.7 6 8.8 2 13.8 6 0.069 5 11.4 9 LABPAC KREPAC K 1.4 5 0.241 8 MP- 1 0.238 7 0.049 5 MP- 2 0.238 7 0.049 5 DRU M CRUSHE R 3.8 7 0.24 8 TAN K# 2 0.134 8 0.000 2 TAN K# 4 0.020 3 3.6 5 X 10" 5 

### TAN K# 6 0.013 3 2.4 0 X10" 5



### E P AFor m 5900-8 5Emission s Uni t I D Regulate d Ai rPollutant s an d Pollutant s fo rwhic h th e Sourc e i s Majo r (tons/yr ) NO x V O C S 0 2 PM1 0 C O Lea d H A P TAN K# 8 0.025 6 4.6 1 X 10~ 5 TAN K#1 0 0.012 5 2.2 5 X10" 5 TAN K#2 0 0.046 0 0.000 1 TAN K#3 0 0.020 3 3.6 5 X10" 5 TAN K#40 0.014 3 2.5 8 X 10" 5 TAN K#5 0 0.008 5 1.5 3 X10" 5 TAN K#6 0 - 0.025 7 4.6 2 X 10~ 5 TAN K#30 0 0.145 4 0.000 3 TAN K#30 2 0.422 4 0.000 8 TAN K#30 4 0.309 4 0.000 6 TAN K#30 6 1.2 9 0.002 3 TAN K#30 8 1.6 2 0.002 9 TAN K#31 0 2.1 8 0.003 9 TAN K#31 2 3.2 3 0.005 8 TAN K#31 4 0.473 6 0.000 9

EP AFor m 5900-8 5Emission s Uni t I D Regulate d Ai rPollutant s an d Pollutant s fo rwhic h th e Sourc e i s Majo r (tons/yr ) NO x V O C S 0 2 PM1 0 C O Lea d HA P B F BLD G 2.5 6 0.018 8 BOILE R # 1 4.5 1 0.24 8 0.02 7 0.34 3 3.7 9 FUGITIV E EQUI P LEAK S 0.039 0 0.001 4 EGEN 1 0.4 2 0.0 3 0.0 3 0.0 3 0.0 9 0. 0 0.000 1 EGEN 2 0.4 2 0.0 3 0.0 3 0.0 3 0.0 9 0. 0 0.000 1

FACULT YTOTAL S 74.9 5 23.6 0 67.2 5 14.9 3 30.9 4 0.113 7 33.4 0

E P AFor m 5900-8 5A|T"|f% * Unite d State s ^^1^1*^ % Environmenta l Protectio n ^jFli I JfmAgeno y OM B NO . 2060-0336 , Approva l Expire s 6/30/201 5 Federa l Operatin g Permi t Progra m (4 0 CF R Par t 71 ) CERTIFICATIO N O F TRUTH , ACCURACY , AN D COMPLETENES S (CTAC ) Thi s for m mus t b e completed , signe d b yth e "Responsibl e Official " designate d fo rth e facilit yo remissio n unit , an d sen t wit h eac h submissio n o f document s (i.e. , applicatio n forms , update s t o applications , reports , o ran yinformatio n require d b ya par t 7 1 permit) . A . Responsibl e Officia l Name : (Last ) Harri s (First ) Dougla s . (Ml ) Titl e Genera l Manage r Stree t o rP.O . Bo x# 7 Mobil e Avenu e Cit vSauge t . Stat e I L . ZI P 6220 1 . - 1069 . Telephon e (618. 1 27 1 . - 2804 . Ext . Facsimil e ( 618. 1 27 1 . - 2128 . B . Certificatio n o fTruth , Accurac y an d Completenes s (t o b e signe d b yth e responsibl e official ) I certif yunde rpenalt yo f law , base d o n informatio n an d belie f forme d afte r reasonabl e inquiry , th e statement s an d informatio n containe d i n thes e document s ar e true , accurat e and-complete . Nam e (signed ) ^wOu^J}/-jj\ \ \ OAAA Q Nam e (typed ) Dougla s Harri s . Date : 4 / H / \ _ S

E P AFor m 5900-0 2

### APPENDI X A : EMISSIO NCALCULATION SVesse l Content s Analysi s Vesse l volum e (ft3 ) = 7.352 4 R = 998. 9 (mmHg)(ft3)/(lbmole)(K )

Assumptions : 1 . Eac h containe rcontent s i s uniforml yrepresentativ e o f th e overal l wast e mixtur e receive d a t th e plant . 2 . Th e overal l wast e mixtur e a t th e plan t i s characterize d b yth e to p organi cconstituent s i n wast e receive d fo r200 7 - 2011 . 

### A B C D E 

### F G H i J VO C M W

(lb/Ibmole ) Weigh t

(lbs ) Ibmole s X i Psat i P i Vapo r (Ibmoles ) Vapo r

(lbs ) Comment s acetonitril e 41.0 5 3,361,22 8 81,88 1 0.010 0 86.3 7 0.8 6 0.0000 2 0.0008 7 acrylonitril e 53. 1 804,31 6 15,14 7 0.001 8 105.8 3 0.2 0 4.83E-0 6 0.0002 6 atrazin e 215.6 8 356,14 8 1,65 1 0.000 2 0.0 0 0.0 0 1.44E-1 5 3.10E-1 3 cyanid e compound s 27.0 3 138,87 9 5,13 8 0.000 6 1.0 0 0.0 0 1.55E-0 8 4.19E-0 7 ethylbenzen e 106.1 7 633,27 4 5,96 5 0.000 7 9.5 1 0.0 1 1.71E-0 7 0.0000 2 hydrazin e 32.0 5 180,23 8 5,62 4 0.000 7 10.0 0 0.0 1 1.69E-0 7 0.0000 1 methano l 32.0 4 6,070,50 1 189,46 6 0.023 1 126.9 4 2.9 3 0.0000 7 0.0023 2 methy l isobuty l keton e 100.1 6 3,042,48 3 30,37 6 0.003 7 19.2 8 0.0 7 1.77E-0 6 0.0001 8 methy l tert-buty l ethe r 88.1 5 405,41 3 4,59 9 0.000 6 273.7 1 0.1 5 3.79E-0 6 0.0003 3 n-buty l alcoho l 74.1 2 1,503,98 6 20,29 1 0.002 5 6.1 6 0.0 2 3.77E-0 7 0.0000 3 n-hexan e 86.1 8 747,61 4 8,67 5 0.001 1 151.5 4 0.1 6 3.96E-0 6 0.0003 4 nitrat e compound s 84.9 9 181,23 9 2,13 2 0.000 3 0.0 0 0.0 0 0.00E+0 0 0.00E+0 0 Non e i n vapo r pthali canhydrid e 148. 1 154,63 5 1,04 4 0.000 1 0.0 0 0.0 0 0.00E+0 0 0.00E+0 0 Non e i n vapo r pyridin e 79. 1 169,55 4 2,14 4 0.000 3 45.0 9 0.0 1 2.9 1 E-0 7 0.0000 2 styren e 104.1 5 1,915,48 7 18,39 2 0.002 2 6.1 8 0.0 1 3.43E-0 7 0.0000 4 toluen e 92.1 3 8,657,46 8 93,97 0 0.011 5 28.4 4 0.3 3 0.0000 1 0.0007 4 triethylamin e 101. 2 850,75 2 8,40 7 0.001 0 67.7 8 0.0 7 1.72E-0 6 0.0001 7 xylen e 106.1 7 2,328,68 8 21,93 4 0.002 7 8.3 0 0.0 2 5.49E-0 7 0.0000 6

a s ethano l 46.0 7 93,612,15 0 2,031,95 5 0.247 9 59.1 6 14.6 7 0.0003 6 0.0166 9 Av g volatilityfo r smalle r amount s VO M i n wast e a s wate r 18.0 2 93,612,15 0 5,194,90 3 0.633 9 23.6 9 15.0 1 0.0003 7 0.0066 8 solid s (a s lead ) 207. 2 93,612,15 0 451,79 6 0.055 1 Non e i n vapo rV O M Emissio n Facto rCalculatio n fo rDru m Crushe r

Emissio n Facto r= Summatio n o f Pound s VO M fro m Colum n J abov e

= 0.022 1 pound s pe rdru m Maximu m rat e o f crushin g = 4 0 drum s pe rhou r Maximu m VO M emissio n rat e = 0.022 1 x4 0 = 0.883 3 pound s VO M pe rhou r Maximu m annua l VO M rat e = 0.883 3 x8,760/2,00 0 = 3.8 7 ton s VO M pe ryea r

2 0

### APPENDI X B : CURREN T NOTIFICATIO N O F COMPLIANC E (NOC ) 

### O P L SUMMAR Y

2 1

### UNIT S 2/ 3 OPERATIN G PARAMETE RLIMIT S 1

Performanc e Operatin g Parameter

Unit s Limit s Tes t Dat e Standard s Maximu mTota l Pumpabl e Lb/h r 310 7 Wast e (Hourl y Rollin g Total ) Maximu mTota l Hazardou s Lb/h r - 401 7 Wast e (Hourl y Rollin g Total ) Maximu mStac k

Ga s Flo w Acf m15,147 Rat e (Hourl y Rollin g Average ) Minimu mPrimar y Combustio nDeg F168 6 Chambe r Temperature (Hourl y Rollin g Average ) Minimu mSecondary Combustio nDeg F187 7 Chambe r Temperature (Hourl y Rollin g Average ) Maximu mBaghous e Inlet Deg F42 0 Temperatur

e (Hourl y Rollin g verage ) Max . Pump . Lo w Volatil e Metal s Lb/h r 4 6 Feedrat e (1 2 Hou r

Rollin g Total ) Max . Tota l Lo w Volatil e Metal s Lb/h r 4 7 Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mSem i Volatil e Metal s Lb/h r 6 3 Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mMercur y Feedrat e Lb/h r

0.001 9 (1 2 Hou r Rollin g Total ) Maximu mChlorin e Feedrat e Lb/h r

21 8 (1 2 Hou r Rollin g Total ) Maximu mAs hFeedrate (1 2 Lb/h r 61 7 Hour Rollin g Total ) Minimu mSorben t

Feedrat e Lb/l b Cl 21.57 (Hourl y Rollin g Average ) Minimu mCarrie r

Flui dFlowrat e Gal/l b Cl 21.4 6 (Hourl y Rollin g Average ) Jan , 1993 Jan , 1993 Jan , 199 3

Dec , 200 9

Dec , 200 9

Dec , 200 9 Sep , 200 8 Sep , 200 8 Sep , 200 8 Aug , 200 8 Aug , 200 8 Dec , 200 9 Dec , 200 9 Dec , 200 9 DRE , D/ F DRE , D/ F DRE , D/F , Part. , SVM , L V M DRE , D/ F

DRE , D/ F

D/F , SVM , L V M L V M L V M S V M H g SVM , LV M HC1/C1 2 Part . HC1/G1 2 HC1/C1 2 t Operatin g parameter

limit s i ntabl e reflec t

mor e conservativ e valu e betwee n Uni t 2 andUni t

3 test data .

### UNI T 4 OPERATIN G PARAMETE RLIMIT S

Operatin g Parameter Unit s Limit s Tes t Dat e Performanc e

Standard s Maximu mTota l Pumpabl e Lb/h r Wast e (Hourl y Rollin g Total ) Maximu mTota l Hazardou s Lb/h r Waste (Hourl y Rollin g Total ) Maximu mStac k

Ga s Flo w Acf m Rate (Hourl y Rollin g Average ) Minimu mPrimar y Combustio n De g F Chamber Temperature (Hourl y Rollin g Average ) Minimu mSecondary Combustio n Deg F Chamber Temperature (Hourl y Rollin g Average ) Maximu mBaghous e Inle t De g F Temperatur

e (Hourl y Rollin g Average ) Max . Pump . Lo w Volatil e Metal s Lb/h r sedrat e (1 2 Hou r

Rollin g Total ) Max . Total Lo w Volatil e Metal s Lb/h r Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mSemi Volatil e Metal s Lb/h r Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mMercur y Fee drat e Lb/h r (1 2 Hou r Rollin g Total ) Maximu mChlorin e Fee drat e Lb/h r (1 2 Hou r Rollin g Total ) Maximu mAs hFee dRate (1 2 Lb/h r Hou r Rollin g Total ) Carbo n Injectio n Feedrate Lb/h r (Hourl y Rollin g Average ) PCC-329 1 SCC-117 6 PCC-12,89 7 SC C - 117 6 37,43 2

149 9

188 6

40 0

4 7 5 0 6 4 0.02 6 22 9 644 4 6. 2 Dec , 200 9

Dec , 200 9 Dec , 200 9

Dec , 200 9

Dec , 200 9

Dec , 200 9 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Dec , 200 9 Dec , 200 9 Dec , 200 9 DRE , D/ F

DRE , D/ F DRE , D/F , Part , SVM , L V M DRE , D/ F

DRE , D/ F

D/F , SVM , L V M L V M L V M S V M H g • SVM , LVM , HC1/C1 2 Part . D/F , H g Minimu mSorbent

Feedrate Lb/l b Cl 22.2 5 (Hourl y Rollin g Average ) Minimu mCarrie r

Flui dFlowrat e Gal/l b Cl 23.1 0 (Hourl y Rollin g Average ) Dec , 200 9 Dec , 200 9 HC1/C1 2 HC1/C1 2