# VEOLI A € N V S RO N M E NTA L SERViCE S

TECHNICA L SQIUTION S NORT H AMERIC A 

### Octobe r10 , 200 8 Vi a FedE x Attn : Complianc e Tracker , AE-17 J Ai rEnforcemen t an d Complianc e Assuranc e Branc h Unite d State s Environmenta l Protectio n Agenc y Regio n 5 7 7 W
. Jackso n Blvd. , AE-17 J Chicago , I L 6060 4 RE : Veoli a E S Technica l Solutions , LLC
. 16312 1 AA P 4 0 CF R Par t 6 3 - Subpart EE E Nationa l Emissio n Standard s fo rHazardou s Ai rPollutant s fro m Hazardou s Wast e Combustor s Notificatio n o

f Complianc e (NOC ) Complianc e Tracker , Pursuan t t o Appendi xB , Item s 9,1 1 an d 1 2 o f th e Reques t t o Provid e Informatio n Pursuan t t o th e Clea n Ai rAc t fro m USEPA , Regio n 5 , date d February22 , 2008 , revise d Jun e 5 , 200 8 an d revise d o n Septembe r16 , 2008 , Veoli a E S technica l Solutions , LLC , hereb ysubmit s th e Notificatio n o f Complianc e (NOC) , th e Performanc e Tes t Report s fo rIncinerators 2 , 3 an d 4 an d th e Significan t Modificatio n t o th e Part 7 1 Permit
. Th e NO C document s complianc e wit h th e emissio n standard s an d continuou s monitorin g syste m requirements , an d identifyin g operatin g paramete rlimit s fo rmercury , SV M an d LV M define d i n 4 0 CF R 63-120 9 an d 63.1219
. Veoli a i s nowcomplyin g wit h al l operatin g requirement s specifie d i n thi s NOC
. Th e Performanc e Tes t Report s detai l complianc e wit h thes e standard s an d th e Significan t Modificatio n reques t tha t th e revise d OPL' s b e incorporate d int o Veolia' s Part 7 1 permit
. I certifyunde rpenalt yo f la wthat thi s documen t an d al l attachment s wer e prepare d unde rm ydirectio n o rsupervisio n i n accordanc e wit h a syste m designe d t o assur e that qualifie d personne l properl ygathe ran d evaluat e th e


## Veoli aE S Technica l Solutions , LL.C . # 7 Mobil e Ave , Sauget , I L 6220 1 tel : 61 8 271280 4 - fax : 61 8 271212 8 VE S 00074 3

### informatio n submitted
. Base d o n m yinquir yof th e perso n o rperson s wh o manag e th e system , o rthos e person s directl yresponsibl e fo rgatherin g th e information , th e informatio n submitted , i s t o th e bes t of m yknowledg e an d belief , true , accurate , an d complete
. I a m awar e that ther e ar e significan t penaltie s fo r submittin g fals e information , includin g th e possibilit yo f fin e an d imprisonmen t fo r knowin g violations
. Upo n revie wo f thi s submittal , shoul d th e Agenc yhav e a nee d fo radditiona l informatio n o rquestions , pleas e contac t Denni s Warcho l a t (618 ) 271-280 4 o rvi a e-mai l a t dwarchol@onvxes.co m o rmysel f a t (618 ) 27 1 -280 4 o rvi a e-mai l a t dharri s @ onvxes.com. . Sincerely , VeoUavE S Technica l Solutions , L.L.C
. Dou g Harri s Genera l Manage r Att
. cc : Geneviev e Damico , USEP A(Significan t Modificatio n Only ) USEP AFil e

VE S 00074 4

### Veoli a E S technica l Solutions , LLC - Significan t Modificatio n to Par t 7 1 Permi t titl e V Permit #

: V-IL-1716300103-08-0 1 Pursuan t t o 4 0 CF R 71.7(e)(3) , Veoli a E S technica l Solutibhs , LL.C
. i s submittin g a significan t modificatio n t o ou rPar t 7 1 Permi t numbe rV-IL 1716300103-08-01 , Th e followin g page s detai l th e requeste d modifications , supportin g informatio n an d justificatio n fo rth e modifjcation
. th e requeste d modification s ar e a s followed :

• Sectio n 1 (B ) Date s o f Constructio n fo rIncinerators 2 , 3 an d 4

• Sectio n 2. 1 (C)(2 ) Operatin g Paramete rLimit s fo rUnit s 2 , 3 an d 4

• Sectio n 2. 2 Materia l Processing , Handlin g o f Leve l 2 Container s

• Sectio n 2. 4 Storag e Tanks , Monitorin g an d Testin g fo rtank s Maintaine d a t Atmospheri c

• 55 0 Gasolin e Storage , Insignifican t Activity

• Dru m Sampling , Insignifican t Activity

VE S 00074 5

### Sectio n 1 (B ) Sourc e Emissio n Point s Veoli a request that th e date s of constructio n fo rIncinerators 2 , 3 an d 4 b e modifie d a s followed : Incinerato r # 2 ' # 3 # 4 Thes e revise d date s ar e take n directl yfro m th e constructio n permit s issue d b yIEP A(constructio n permit s attached)
. Dat e of Constructio n 9/198 6 (correct i n permit ) 8/198 8 (permi t state s 9/1986 ) 8/198 8 (permi t state s .6/1988 )

### f A Illinoi s Envirprimenia l ProteGticit tAgency » tlb 'rj ' ^^it f Road , SpirSiigReld

, I L 6270 6 

### 217/782*211 3 GdHSTRUetlO W PERMI T fPSit e Waste
. IneiMritio n ' Attention s James t , (sar y 7 Mobil e Avenu e

Illinoi s 62201-10^

9 

# ?

jftpgT i can t - s D eg?

} gnat i on; ; $mfaW'\'m W1-2UM 0 fodrteytffiofrs pate rmptrnMP iiii ' W^^^TWI Avenue , Sauge t I..D , ..Ng. ? 163121AA P Received : Jun e 9:

^ 1

Permi t i s hereb ygrante d t o th e above-designate d Permitte e t o CONSTRUC T emissio n soufce(s ) and/o rai rpollutio n contro l equipmen t consistin g o f tw o TWI-&G0 Q Serie s 2 Hazardou s Wast e Incinerator s on e wit h a Jo ySpra yDr y Adsorbe ran d fabri cfitter * an d the
. secon d uni t wit h a Ventur i Scrubber , Cycloni cWate rGa

s Separator , Induce d Draf t Fan , an d Exhaus t Expansio n Tan k as . describe d i n th e above-referehce d application
. Thi s Permi t i s subjec t t o standar d condition s attache d heret o an d th e followin g specia l conditions} ; 1 , Th e incinerato rwhe n constructe d shal l includ e a Wast e Fee d Interloc k Syste m t o insur e tha t wast e i s no t fe d t o th e incinerato runles s al l critica l operatin g parameters ar e wit h acceptabl e limits
. As par t o f thi s syste m stac k

monitor s shal l be installe d o n eac h incinerato rfo rOxygen , Carbo n Monoxide , an d Hydrocarbons
. Fo rth e incinerato rwit h th e SD Ath e followin g tw

o additiona l emissio n monitor' s ar e required : Broke n Bag Detecto ran d hydroge n chlorid e tnbnitor
. 2 , Particulat e matte remission s fro m th e incinerato rshal l no t excee d 0.0 8 grain s pe rdrystandar d cubi cfoo t o f ga s discharge d t o th e atmosphere , pursuan t t o 3 5 111 , Adm , Cod e 121.181(b)
. 3 , Carbo n monoxide ; wtsslpn s fro m th e i nethe ra to rsha l 1 no t excee d 50 0 part s pe rmi l 1 ion , correcte d t o SQ percen t .exces s a i rypursuan t t o 35 111
. Adm
. Cod e 216.141 , ' • • 4 , Hydroge n chlorid e emission s fro m incinerator s 2 an d 3 shal l no t eXCe/e' d 4 lbs/h ro rth e contro l device s shal l demonstrat e a minimu m HG L Remova l efficienc yo f 99%
.

D ECEIVE D SE P


### VE S 00074 7

### P a g e t



### i s The ; r! # i-R,!?llfrai0,r. | shal l fee, §o;fjs*ru,ef£ d aB4lfte-T§t^4jsf'$ | a ; 

### wast e cutof f ^ ini;gr1 'OG) < syjs'fer

a vshie h wf] 3 preven t intro^UGfeTO n i f ISff e fcff e th e 1lfe?afl^t e vihs R an yth e l^tl^ M event s hay e peourr.e< k J J
. ft!? : Mtam
. I KWM^iXttg a l rp'res&ure - belowIf f pSi§
.

: 

### © vInqiner:,a^o rchambe rpressur e 2 " W : 

### ..G ., . 

### above aMosphori cfo rwer e tita n 0 seconds

^ d , Emergenc

y.stic k open s . e \ Fai l ar e t o sustai n operatin g parameters speci f iet i i n specia l •f , burne rfailur e i n th e |?rimar yo rsecondar

ycivamher

> g . Whe n prim a if " Camber

- temperatur e f a l I s below1 S^Q^ F o rsecondar

y ehambe rexceeds
. 2£?S°F
. •h , GarbO n monoxid e eoheeft^ratio n exceed s 500 pp m o rexcee d 50 pp

m fo r mor e Ifen , thre e m i nutes ; Fo rThe Incinerato rtyft|i A Veplur i S^rubfee r f
. Quench wjtte^

Mm 10

0 gpm . | , Ventur i scrubbe rWate rbelow3. 7 gpin , pressur e dro p acros s Ventur i scrubbe rIjes s tha n 21 " w.e.., . Scrubbe rp H les s tha n .

6 an d flu e gas temperatur e enterin g th e scrubbe rgreate rtha n iSO^p ; Fo rThe , Iniclirteratoi - g i t h ASpray ; ifep f Adsorbe r k.
. Los s o f slurr yflo w t o SDA
. 1
. ,Hig h hydroge n chlor i de .concentratio n i n th e stack; , ft. Hig h opacit yas iridicate d b yth e broke n ba g detector , ii. Ifig t inle t tem|.erat«r e %};
. th e fabri cfiller
. 6
. The incinerator s an d assc-clate d ai rpollutio n contro l equipmen t shal l b e constructe d suc h tha t th e value s o f th e parameters bein g menitore d ar e displaye d fo roperatin g personnel
. 7
. Operatio n o f th e incinerato rutilizin g auxiliar yfue l wil l b e limite d a s t o compositio n and iocineratp roperatin g condition s whic h wil l mee t al l applicabl e regulations
. Such a reques t shoul d b e incorporate d i n th e tria l bur n plan
.
VE S 00074 8

### flt,Kft^Wcftj*iB^. I?rate*ctio;i i Agenc y- Churchil l Road , Springfiel d it , 6270 S

L r J I , Trad e Wast e incineratio n shal Tsubtntt as -buiT t plan s an d specification s t o

- th e Agenc

yas par t O

f thei roperatin g permi t application
. ff s 

### . Prio rt o operatio n th e ne wunits , 2 an d 3 , shal l b e teste d pursuan t t o a n Ag«np yapprove d tria l bur n plan
. Trad e Wast e Incineratfo n shal l submi t a detaile d tria l bur n pla n fo rAgenc yapprova l prio rt o startup
. Th e tria l bur h p i ah shal l provid e fo rdemonstratio n o f th e incinerators ' destructio n an d remova l efficiency , an d particulat e matter , carbo n Monoxide , organi c material s an d hydroge n chlorid e emission s throughou t th e rang e o f wast e characteristic s an d incinerato roperatin g parameters for'whic h a n " Operatin g permi t wil l b e sought
. Suc h tria l bur n pla n shoul d als o indicat e perio d o f operatio n o t incinerator s durin g shajcedaw n an d testing
. Standar d conditio n 9 'whic h allow s 3 0 days fo rshakedown an d testing , i s hereb ysupercede d b ythi s condition
. A n operatin g permi t wil l onl y-b e issue d fo rthes e incinerator s afte ra tria l bur n ha

s demonstrate d complianc e wit h al l applicabl e regulations
. Base d upo n tria l bur n operatio n an d wast e materia l burned , th e operatin g permi t ma

ylimi t th e incinerato roperatin g parameters an d th e compositio n o f th e incinerator' s wast e feed , TJQ V A s par t o f th e tria l bur n plan,, Trad e Wast e Incineratio n shal l propos e procedure s fp rmaintainin g operatin g records
. Suc h procedure s shal l includ e appropriat e notificatio n t o th e Agenc yan d actio n t o b

e take n by ; operatin g personne l i n th e even t o f equipmen t malfunctio n o rbreakdown
. II , Emission s o f particulat e matte r(TSP) , sulfu roxide s (S02) , nitroge n oxide s fNQX) , organi cmateria l (OM ) an d carbo n monoxid e (CQ ) shal l not excee d th e amount

s specifie d i n th e Tabl e below
. Emissio n Source : Annua l EjmissTon s {Tons/fear ) W> Ul 

### Mo

xo j e g E^Stth g Ineifierato r He wIn^the^ator s Storag e Operation s 30.0 , 7. 7 15. 4 4. 0

8. D 6j,. i

1. 8 6. 9 13-. 2 Thes e limit s ar e base d o n th e potentia l emission s o f th e incinerator s and storag e as indicate d i n th e permi t application
.
Bhara t Mathur , P.E
. Manager , Permi t Sectio n bivisio n o f Ai rPollutio n Contro l BM;JOC:jnrni/1857F/25-2 7 cc ; Regio n 1
VE S 00074 9

### Illinoi s Ewvimnmietl^ l Pfbfcectio n Agenc y i
. / WSf^SS^M PERMI T T#,ad e Vfest e i;fte%e^tJw# - I

S Divisio n 0 t 

### mmicM Wast e l^Hase|in$
. ifcttW i Jame

s u :la ^ f Mobil e Avenu e Sittget , Illinois : 6820Tv W Applicatab n ffHJOo m :l,D , No; g tSIWAA P J6tfl;iiPiW rS; Dgs^gnatioh : iNSp
. a

### pat e Receive d Ha y24 , \$m W$M£V£ TW I 20Q Q .|efies , 2 * ;fffcinera*p r Qa M 'issued ; Augus

t TS S 

### iftSS ; X&mtfms i Mobile ' ftyeotte-, Sallget , 11 1 inoi s
Permi-t i s hereb

ygrante d t o th e afeoje-Msiffftate a Perraftt.e e t b C0NSTM6J 

### attache d heret o and th e fpliQ^R. g Specia l cpnditiorits?5 : 1 * Particulat e matte rgrtti^Moii S fo rthe ; incjhefatO rsha l 1 not , excee d Q-M gftin t pe rdr

ystandotr l cubi cfoo t o f th e ga s discharge d t b th e atmosphere , pursuan t t o 3 5 11 1
. Adm
. Cod

e 121..i8llbJ. ' •2 , 

### Carbo n monoxide emission s fro m th e incinerato rshal l no t excee d .BOO
. part s p e rm i l l i o n MrirmmAW Sf l pr©en t exces s ai r, p&rs^^'Ibio/ S 1 11 , : 

### Adm , Cede 216,14 1 A, , The incinerato rshal l | i equippe d vift h sensor s t o monito rtlie : followin g parameters : % vUppe ranf l lowe rcombustio n chambe rexi t ga s fMptSa^ra * b
. Uppe rand lowe rcombustio n chambe rpressure . Spra ydrye radsorbe rinle t temperature
. d
. Spra

ydrye radsorbe routle t temperature
. e . Lim e slurr yhea

d tan k liqui d level
. f
. Wate rpressure t o slurr yhea d tan k makeup
. g . Baghous

e tub e sheet pressur e drop , h
. Combustio n stac k

ga s flo wrate , i „ Stac k

ga s oxyge n concentration
.



## RECEIVE

D AII 0 2 3 il l VE S 00075 0

### i S£a#f t p § tota l b;0r&mmw 6W«w M W&M; ga s Hit , eoii®l^:onj i - Stack- gat ® opac i ty
. Liquid : anW& rs1uTd|| e waste flo» ffiSe int o tnj e ?a#ifte^a|©;r * *"l;l i WSste cti^gei U ' • ii f fue l preS;s.Ht;e

> iStfdn
. a^ rp;re$su're:
. Pl^toai^ y'Jlawf r$ Nto t flame,
. Siae#niar yepfiei ^

& Pttofs , flames, * £$e/pge^ yst&e k 1 atc h * I , n \ a . P S ~ 4 . Th e incinerato rshal l .b e ^stfh M 4 P

4 e.onst^ucl-eid : t o ape^te , wit h a n •awloijalSfi g waste : fee d fiutpff th^eyim^jk : systefi ' whief i wil l preven tth e introdHCtib n -d f 'Wisj b into ' th e incinerato rwhe

n opeij'atih g outside : th e permftte a raflg e o f parameters , a . Starta p rang e o f parameters ar e establishe d buse d upo n desig n specific-ation s an d performanc e test s conducte d o n Incinerato rUm t 2 an d ca n b e change d afte rsuccessfu l stac k tes t demonstratio n o n Uni t 3
. (1 > primarychambe rMo M 1600PF , 11 1 p^ndar yc.haiw

>e f belowl :0pQd

,F
. |t l P f ftsat*^

o rseMnaa W Chamfe rab.qrtf e aMospheric : pressure , (i t Sb.ra

ydrye radsorbe rinle t greate rt&a n BfoOPF. ' (5 1 Spraydrye radsorbe routle t greate rtha n 40d° F o rbelow ' 370PF V " (6 } Lo wliqui d leve

l i n lim e slurr yhea

d tank , (7 ) Low; , makepp wate rpressur e int o slurry : hea t tank
. W) fiaghbuse |uS

e shee t pressur e dro

p greate rtha n 1 0 i riche s wate r column , (9 ) Combustio n stac k

gas flo wles s tha n 5,00 0 acf m o rgreate rtha n 15,00 0 acfm
. (10 ) Oxyge n concentratio n les s than
. 6% b yvolume
. (11 ) Carbo n monoxid e concentratio n greate rtha n 500 ppm . (12 ) CarJjo n monoxid e concentratio n greate rtha n 5 0 pp m fo r3 minutes
. (13 ) Tota l hydrocarbo n concentratio n greate rtha n 10 0 pp m correcte d t o 7%oxygen * (14 ) HC I concentratio n greate rtha n 100 pp m fo r1 hour
. (15 ) Opacit ygreate rtha n 10% , (16 ) Primaryfue l pressur e below3 0 psig
. (17 ) Combustio n ai rpressur e belo w1 0 inche s - M-X
. (18 ) Primar

yburne rfailure
. (19 ) Secondar

yburne rfailure
. (20 ) Emergenc

ystac k open .

VE S 00075 1

### Pag e 3 ' is,.. o >Bi , 

### aM. ^

jmstititespn «fl l ?&

> ss^itsiiaf
. IW £ ftp* s ^5se^a i «* s ietua l «5&N

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. ,t e G0ns#ac%d l s«e n tha t th e viTHes
. o f tjt e |f

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^ jfijps^ . fo rsptf^ft l ||ri'OTM f li t-^ f

ll i i M vfsul i al.§rii s 6
. Th e Pgj$ttt£ & shal l submi t a s MH I plans , o f th e InGlneratO Tan d a f r p^flutftoi i •G ^jftro l equipifieh t a s par t o f th e operatin g permf t app l f cation; , l :i

### The : permitte e sha l J no t initiat e th e start-up
. o f th e iheineratb' ? withou t wWttef t app^tyit i fP H M e Affeflcf
. Thi s special ' eonliiMon ; sHpk^f& s standar d gawiilfef i 6{b} , §
. stac k

eiflfsloi i test s shal l S i eonjuete d m thi s Uni t 3 ^^m^atM esiiij i isi veiraissip i rsies. - St d ggmpliawcf i W i t h th e applicabl e g$g^k1$fct& . The : require d stac k

tests ' ar

f 1f tM conducte d b

ya n iftdepend f g ^'tss

^el v •a * Emissio n test s ar e require d fo rth e foHiwih g loTfuja&Si f

earlon ; RbfldXide
. C5 ) Principa l organic : hazardou s components:
. a * The Permitte e shal l submi t a stac k tes t pla n at ; leas t 6

8 day s i n advanc e fo rAgenc

yapproval
. Th

e pla n shal 1 contai n detaile d plans , an d procedures
. Writte n notic e o f th e schedule d date s fo rcomplianc e stac k testin g shal l b e give n a t leas t 3

0 day s i n advanc

e t o th e Agency
. Fina l notic e shal l b

e give n verball yno t les s tha n 7 days- befor e emissio n testin g begins
. The require d notic e shal l b e give n t p th e following * Illinoi s Environmenta l Protectio n Agenc y Attn : Permi t Sectio n Manage r Divisio n o f Ai rPollutio n Contro l P.O.
. Bo x1927 6 Springfield , Illinoi s 62794-9276 217/782-211 3 Illinoi s E'nviro.nmenta i Protectio n Agenc y Attn : Sourc

e Emissio n Tes t Specialis t Divisio n o f Ai rPollutio n Contro l The Intercontinenta l Cente r 170 1 Firs t Avenu e Maywood , Illinoi s 6015 3

V E S 00075 2

# & f¥iW ! 

### m g$$r$H & Permitte e sftal; 1 

### ! sitet t ?l§|r«B!pi^c » ari d
. BiWitortri g gpsftflMMMtltt * p^olal : ## rthe ; il|afjs-a # Kefor d feeepifig an d repot * foBnals ' Use d t o sho t tifflpi^i^ vtli e l «tatif| s o f |fi.e
. opBrs^nj f •piWffleas ^

.t^pCt^ l H I s gpn|^e| t f:f t spe^iaTlS^flll W t |fr % eoJiftMctto n perntf t sftal l b e :#ti$nt f feted to : til e Agenc

yfp rapproval
. •m, Th t i|j^i^^^^M--' : 

### @HS4'-^al s Ittggfit p equipmen t sfiaTJ pi^vM e f§ r storag e o f \QQ%

o f th e incinerato rparameters an 4 stac k monitore d results : in : -

£ Olm^uie rpBaJiabl l fd'Mat , Sopie s shal l be madei !a^aijafeii ^

t o th f .Agency ; in ; a : stf i tabf e compute rreadabl e format , b » Ti e dat a Toggin g equijpmeh t shal l als o provid e fo rrecordin g waste: * analysi s piagefe * fo ra l burne d v&st e e ;


### . Th e :4ft a l<Sg|iii g equipmen t snW H provid e fel l time ; acpis s t o th e ineineHate roperatin g parameter s throug h a teTecomrtunfeatio h compute r p*t , *

" Th e proposa l shal l §efe^r|:h„it e hardwar e an d so f tv/are spectf i Ration s fo rthe ; ihfbrftiatio p 

# syste

malon g Wit h availabl e option s i n repor t formats' ari d dat a exchartig e mod i a > e . Th e permitte e Shal l instal l a compute rlinku p syste m wit h IEP A Springfield , I£P

ACollinsviU e an d som e locatio n wit h publi caccess . Suc h a syste m an d locatio n wil l requir e Agenc yapproval
.

. Prio rt o startup , th e Permitte e shal l submi t detail s o f a n operato r trainin g progra m fo rAgenc yapproval
. "

. Prio rt o startup , th e Permitte e shal l submi t fo rAgenc yapproval , specification s fo ron-sit e securit yincludin g vide o cameras , monitorin g cabine t lock s an d seal s an d detail s o f securit yfencing,
.

. Emission s o f particulat e matte r(TSP). , sulfu roxide s (SO^) , nitroge n oxide s (NOy) , organi cmateria l (OM) , an d carbo n monoxid e (CO ) shal l no t excee d the , amount

s speciffe d i n th e Tabl e below
. Illinoi s mffl8mm$fil

PPitectfo' n JjfyiSfoi i o f Ai ri^Htftlo n Gbfltro t jleiiWii
. Office ?

Erir i ssio n Sourc e TS P AnnUa i Emission s (Tons/Year ) SQ 2 

### NO xO M C C O Incinerato rUni t 1 Incinerato rUni t 2 Incinerato rUni t 3 incinerato rUni t 4 * Wast e Storag e 15. 0 7. 7 4. 0 15. 0 7. 7 4. 0 15. 0 7. 7 4. 0 16.9 2 50.7 6 61. 6 0. 9 0. 9 0. 9 3. 1 6. 6 6, 6 6. 6 13.6 8
VE S 00075 3

### Illinoi s Bn\ycqi«mgnt!i l PfoteetioT i 2;20 Q Gh'^rCtti U Road , Spring?fel,a
. Ji , 6&7.Q 6

*Thes e 1 

# ifirits ar i establishe d base d 0: 0 72$ ? hear s e f operate s Bferyea r an d avert s aitsffbft
. rates ; 'give n tf f th e a^«%tii $ B > These : 1 pf e Wil l be ; revi'sStt 

# site * th e s%# ; 

# |is l rem i t s -aire , 

## ^e ^M & A
pleas e not e tha t th e start-u p ari d tria l bur n pla n m subtriitte d wit h th

e applliEiatiQ' h i& ^n%^ss^^% m 

### Pla n 

# del ^iotetg s tffll b e tdehtlfie d a t ft

filViffbn o f Ai r.Pottatlof i COntro l

ce > Regio n 3

VE S 00075 4

### Wm$tCiUM^%$XjPROTECTIO N A&ENG Y

j Jul y 1,198

5

fjisiflipt to f Af r^IJtt^on GatiWl S|>i?iii|fi#d

, BM&ei B 6270 6 ftregiona

l offiti e ij f ttt e j^Mf t Operations Soetiph . Tji: e regiona l dfficeBaM :%ejfcarg&

s sfteBfdiwiiiJij ^ ar e tihawf t<jij t $|£p. . Hfo

e "attilEieBBe

B ^dfeleplip^ e liMipber

e o f I6 e f-egionfi l "S.eg | air e ik s Follows: lUinoi B EPA 1701S, le tAyenii

e

•541i > Naftli Universit

y £iajria , Illiuoi

s 6161 4 691-220 0 Illinoi s El? A 2a &|3Msii l Stree t ^Qp|#8*ilig

, Illinoi K6223 4 '345-Q70 0

VE S 00075 5

### illinoi s Enviro n menta l Protec t io n A$mcy < 22ftf ) ChsfcW H Ro

.a4 . Springfield

, i L 6270 6 CONSTRUGTleN PEgf« T
Trad e Wast

e Incineratio n I t fif^lsojn, W

#amtSa 1 Wast

e Manag^eri i Att n : ? tame s L
. Gar

y 7 M o b i l ft ye n u e ^auge ^ illinois : 6®R1ffMa> * 8801000 1 Ma i ifa»^|1^.djia>^ga | il^Jt l $ 4 •Subfect ; Tra:rrsng.r^tb:l e RotaryKil n Incifierafco r flaterissued, ; Augus t 198 8 Location * /"Mobil e Avenue , SSttps , I L I A
. te> t 16312 1 M&m March 2 % 1988

jerwi i notaryi « i n incinerato rUni t #4 : equippe d #|jh , a dr yscrubbe rand
. a b :a #0.U .S:e s

### as describe d in
. th e abovsrfrefer#:nc -ed application
. I n i s Permi t i s snbpe t t o standar d condition s attache d .fe^i f an

d th e followin g s-peeia l COhditiionis) : | % Particulat e matte r^mission s frolf l th e iircln e rate rshal l no te>?cse d ti,£8 grain s pjfi rdr

ystandar d ciibi e foo t of ; 

### tft« s i p discharge d t o % hie aisno sphere , pursuan t t

o s s in . Adm.

, Met e I2l. : 

### 18?(b)
. < L Carbo n liionoxid e emission s fPom th e fne i iterate * sha l 1 no t excee d 500 part s pe rmillio n correcte d t o 5 0 percen t exfees s air. , pursuan t t o M III * Adm
. (lod e 2.16,141 , ; 

### % The.incinerato rsha l 1 b e equippe d wit h sensor s t o continuousl ymonito rth e \
. foltoW i h g parameters ; a*
. |pf)
. an d seeeodar ycombustio n ehambie rexi t gas temperature,
. ' ;jf
. lllffl
. an d sMIttSdftff ' combustio n oham|f,<E| rpressure ; 

### 0
. Spraydrye radsorbe rinle t teiiipera.ijjtire , 1. Spra y drye radsorbe f bulle tteroper&tu^e *
, f im e slurr yfei 3 tan k liqui d leve l low,
. Wate rpressur e t o slurr yfee d tan k makeup
. Baghouse tub e sfiee t pressur e drop
. Combustio n stac k

ga s flo wrate:
. Stac k ga s oxyge n concentration
. Stac k ga s carbo n monoxid e concentration:
. Stac k ga s tota l hydrocarbo n concentration
. Stac k ga s HC L concentration. , i fri."-
. -tac k

ga s infrare d absorption
. | n.. . i qu i c

i and/o rsludg e waste flo wrat e int o th e incinerator
. I li d wast e charged
.
VE S 00075 6

### ibis ; EttyirQtimehtai Protectio n Agenc y ' 2® 6 ChurcM' U ftoad, Spfingfteid

, I L 62:70 6

§) 

### £o#us$:fe o tit*pr^ssarf.
.

MsEinWI ^

S.wT«i&m * Pilot s flame , 'Eiifeplfe ystael
. latch * The : ifiGiheraito rshal l le : 

### .-tije&f|pw & aa^ , •g#ns« , 

### raete« l t o operat e wjfch an .aylomyil f ^ E S * 6 

## fee i i »lsl f ifil^loc k

sj^Sen i Wht # wil ] preven t 

## Me . piratfle l rang s e t parameters , a . Startu p rang e o f parameter s ar e establ-fehe d base d upo n desig n specification s an d perfo^aiic e tesNsS " esriduete d o h rncinepaio r an d ca n is - change d after- " siucfe^fu l Stac k test , demonstratip n o n tlni t 'i.

b
. chambe rbelo w160 0 F > Secondar ychamber' below ; K i lp , ^^eiggtii ^r y abiav e atmospheri cpressure * f o rbelo w

(12 ) (13 ) IB ) Baghduis

e ttfb e sf!ig $ pi^SS^ s tlrO p |t»^ W tha n 1 Q inche s wate r eoiumru
. Owgm coH ^eflt ;p¥tib.r

t te M tha* i 6

% b yVolume , Garlor i monoxid e elhfeMI;faftTor k greate rtftan : jipl Carbo n monoxid e concentration : greate rthaft 5 0 ppifl ' fo r3 minutes
. Tota l hydrocarbo n concentratio n greate rthat i 1D Q pp m correcte d t o 7% ef^ge n one hou rrunning ; average , lie ! concentratio n gteate rtiVar i 1Q0 pp m fo r1 hou rrurin i n g average , 0pSCii*y ; greMe rthaf

t Wik PritfiaJry ; fiie Tpressur e M s ftQ: ps3g
. Combustio n ai rpressur e belo w1 0 inche s W.C , kil n fotmnerfailure
. SeeMlar yburne rfailure
. Emergenc ystac k open ; Combustio n stac k

gas flo wparameter s wil l be establifheiji , a t a lafe r'stage, ' Operatin g parameters shal l be establishe d base d upo n evaluatio n o f actua l operatio n an d measured emission s durin g a tria l burn
. 5
. The incinerato ran d associate d ai rpol l utio n contro l equipmen t shal l b e constructe d suc h tha t th e value s o f th e parameters monitore d and/o r indicato ro f acceptabl e statu s ar e displaye d fo roperatin g personne l wit h audibl e an d visua l alarms
.

VE S 00075 7

### \ Illinoi s Enyiro ^itteintal PrOteclibt i Agenfi y' 220t f ChureM H Road , Spriffgrteld

i th 62 ^6

6
. Th e Permitte e shal l submi t as : buil t plan s f o rtlje ; feg|i^fe p ,p d ai: r •pji'lulfin : -g^ffi ! equipmen t as : par t o f th e operat f ti | fWffii t ip| l ie&itdh , I * Tt e HmiMee

sftal l ho t inltial e ifj$ j start-ti p p f file ' inelne^tb rwjibjtu i m^ttim

! 

### s^^MWM

ffs m •%< ? Agens^.
. Ihis " socia l cohdilib l supersede s standar d conditio n 6|pj. v 8 , Stac k

gnfisitei
. MIS ' shaf t be : Conducte d o n tlii s i«ci»6pato > t o estab l is h emission / fpg s an d c&fpliBfte e wit h "th e app l l4#X e rejulatidns
. Th e required stac k

tests 1 

### ar e t o fefej'Qo^dM^lejl.^ an independen t tester* , a , Emissio n tests , are : required : fo rth e fotllOiitf g polluisnM? ' | l ) Particulate , matter
. (3 ) ^itr^ge h oxides
. (4 ) ,0arbb:r

i moliOfife;. ! (5 1 .Desijr^to.1 1 ajf ' §riije1|$ t fr^iftif c Mazardou s components ,

. . b ; Tti e Permitte e steal ! submi t a startu p pla n Sho e tria l bu W plan s an d pj*0jrfl!t ^

Sue n I
. WW

bur n ||if t shjM i rSfuir e th e Agency * s approva l 30 ' day

s prip rt o an yst&ft-uo ; afi d testing , c . Writter i notice: , o f li e s:dh;e4ulfe d date s fo rcpmplianc e stac k testing
. jsi'ot i iowin p Illinoi s Environmenta l Protectio n Agenc y Attn: : Permi t Sectio n Manage 1 

### * 1 

### llfvfsip M %fMf-

PMfutio n Contro l Springfield , I L 62794-927 6 217/782-211 3 Illinoi s Environmenta l Protesjfefiaf : j &JBffl^ f Attn : Sourc e Emissio n Tes t Specialis t Divisio n o f Ai rPollutio n Contro l Intercontinenta l Cente r 170 1 Firs t Avenu e MaywDQd , I L 6015 3 312/345-978 0 Illinoi s Environmenta l Protectio n Agenc y Divisio n o f Ai rPollutio n Control-Regiona l Offic e 2Q0 9 Mai l Stree t Collinsville , I L 6223 4 618/345-070 0

VE S 00075 8

### i S - Illinoi s fes&ofi^efllletffroi^#m AgeHc f - g^W^BS J SMwni , fL«| ;



### t , Mol * t o SSftftHfr*
. th e Permittee : ShftY l tgtaai t Ih^lplW W Wt f Ittittopitt g speofffeafiiais f ^ p^pss^ l wShe : ae«&ft e o # recto M 'HMrfe i fft f repot * i|^a# s u^es l ^ Q : eMpTiMe'e ; wit h th e o f #^%t|n § pis^mifef i r^st^l' M te'jflejgf^&»a I W specia l eojilfiga: ^ o f 4g^- : 

### &gi^ ^

fee submitte d t o |fi e fenjyfp rWpWlv -
' a , 'Th e 'imwmm^rm ah f fata ; Toggin g equipmen t shal l proMi§*f6 ¥ st^raf e M'

W($$ -of $h e i^fegj?aii ^ parameter s gsi.^iaieWnii^e i MsuTts / TO a «iiupju|^ rr-ell^W s fswat - espies ; shal l D B wi t availalT e tp - ^fe*lp W tf f a tuitablj e compute rre;a#bl,e ; format,
. • bw ; Tne : tfata lofgifig ; esufprnen t iftai i als p previii e for- reeotdih g wast e •srialfst s paMWe^ei ? fe ri § burne d -vitaste / streams k c.. . Th e #at & loggin g epip^ ^ p Wid e ^ea l tim e acces s k g ih e inefperailo rBBfK^ng : p^ame}ters ; 

### throug h -a. te^eeom|?upieitiQ n eomptife r dj;
. Th e proposa l shal l se t fort h th e hardwar e an d softwar e specification s fo rth e information , syste m alon g wit h availabl e option s i n repor t format s an d dat a exchang e media
. % Th e permitte e shal l instal l a compute rlinku p syste m wit h IEPA Springfield , IEPACollinsvill e an d som e locatio n y/it h publi caccess . Suc h a syste m an d locatio n wil l requir e Agenc yapproval
. iibvPrio rt o startup , th e Permitte e shal l submi t detail s o f an operato r trainin g progra m fo rAgenc yapproval
. 11
. Prio rt o startup , th e Permitte e shal l submi t fo rAgenc yapproval , specification s fo rqa-sit a securit yincludin g vide o cameras , monitorin g cabine t lock s an d seal s an d detail s o f securit yfencing
. 12
. Emission s o f particulat e matte r(TSP) , sulfu roxide s (SOg) , nitroge n oxide s {MO^) , organi cmaterial , (df4) , an d carbo n monoxid e {CO ) shal l no t excee d th e amount

s specifie d i n th e Tabl e below
. Emissio n $pM # W:ssi&n s tfWs/Year) : Sourc e , %W iM IjQx , O

W ..Cj ) Ilicihferatp rUni t 4 11 .9 2 5:0.76 6J ^ 3
. 1 1 $M' Thes e limit s are . estab l ishe d base d o n 72;p 5 hour s o f operatio n per , yea ran d averag e emissio n rate s give n in
. the : application
. Thes e limit s wil l le v revise d afte rth e stac k tes t result s ar e reviewed
. 13.
. Prio rt o startup , the : permitte e shal l provid e deta i 1 s o f th e Qualit y Assurance/Quai i t yContro l program s fo rth e monitorin g system s specifie d i n Specia l Conditio n 3 abov e fo rAgenc

yapproval
.

V E S 00075 9

### Illinoi s Environmenta l PBOte^io n Age^ y' ^PIMttlsiM
. $p*t#eld j It
.

Pag e 5 

## t**tat - torn fii M

uitio n Contro l

sos . Segfpj i I

VE S 00076 0

## mm mM0}mmm

SH #WiR3 @^fr : 

### 4pas^dJi s ar e iapplicafcl e unless a^j^rseded^'^^g i GOH ^I IB »M . 

### yea r 2. . 3Ph £ c£nS!br«#^ fc% Illinoi s Ewfeonrnental-B^ ^ aSopfed'Tj y the Illinoi s feirtlutibn Contro l 

### W<$gx$h §'.-
. iiierB.«faalI|jfi ;H

O #wli3e(|ffl

S i®mi|ig :4 $pj$ ^

r#$Lies. t fsl^^liei^a , ale 'rig ; syitf c.jalkli B -iifia : ^cM ^tti^s , * S ^

r^juirfe * JiMlfee:.#( ^ a^lt ^ a ' W

& an!

4 k :|jj^lera^M l Tfc e j&pfiiifte e shal l allo

wany; ful yauthorize d agen t n f fee i%

e nc yupon , tkt s presentatio n n f credential^ a*- - -reaBgxjalfe
. iifce s s 'whefc e ;any;a'efe|i yia
. t

o p f qondu^ep

t pufcsiSHift

' |^ k |i&r^il; , b „ t p Jiay e acc§S* S |o„^Mo<iicApy^^a; 

### i^'|^ss3g''r^#teeAf a ^ kep t unde rth e term s an d cond i tibn a o f thi s permit , c i to ;iiiBpeGt,ini6ludia

g durin g an ytours af

* i $gBra &3a. ^

Operate d u&der , fnigip ^j^iJt i g «en'%tfij!ffi ^t*a

^/ftftB ' e^aipinen t require d tfrhe : 

## ^Mk, W^GM^m A

## 'MlW^^M^Mi^^^Ms-: Mis d t p obtai n an d temolr

e sample s o f an ydischarg e oremission s o f pollutants , an d e , -t o ente rati d utiliz e anypkotographic , recording , testing ; monitorin g o t otte regnitmiejif

cffc rth e ^purpos

e o f preserving , testing , motatoraig , o t recordin g an yactivity , discharge , o remissio n authorize d b ythi s permi t •5
. Ife : isgu^c g o

f thi s perftiit ; a . shal l no t h

e considered ' a

s i n an ymaime raffectin g th e ti'tf e o f th e premise

s upo n Winch th e pefrnitte d facilitie s ar

e t o b e located , Us. 

### doeB 'rio

t 

### releas e tn e permittee fro m air

yliabilit yfo rdamage : t

o per'soi i d

r

### propert ycause d b yo r

### resultm g fro

m 

### th e construction , maintenance , o roperatio n o

f th e propose

d facilities , • c , doe

s no t releas e th e permittee fro m complianc e wit h othe rapplicabl e statute s an d regulation s o f th e Unite d States , o f th e State o

f Illinois , orwit h applicabl e loca l laws,'orctin&nfce s an d regulatione , d , doie s not take , int o consideratio n o rattes t to , th g structura l stabilityo f an yunits o rp$r£

s Q f th e project , and
. APQ^tS^tllv: , I13/U.S

1 09Q-O0 S 

### VE S 00076 1

### Etesia n of^Afc '

"in s Sfictftra i IBjs - "' '

VE S 00076 2

# m "srtj/siBHsn a mffl f mM &Rtm

AM D fWPS i paiif?
tmd e Ipiii l ittMfieMtioti ; & o f Chepies J Sfes M f ; 

### loMT s Avernje

;

SM&aetefe s TanK ; Far m MdMbe

r% 

### mm 'mums ;auii e s &

t is p 

## iteafieft : 1 fflabif

e ASeinue;, , I t
Permi t i s hereb ygrante d t o th e above-desjgnate d Remitte e t o CONSTRUC Tan d ' OPERAT E emissio n $ouree(s ) «thd/o rai rpollutio n contro l equipment'consistin g o f te n 12*00 0 gal
. an d sixtee n 30^00 0 gaT
. wast e blendin g an d storage " tanks wit h carbo n adsorptio n an d ^sjsociatet i truc k an d rai l ca runloadin g station s wit h va^o rbalanc e as- describe d I n th e above-refereflte d application
. Thi s Permi t is ' subjec t t o standar d condition s attache d heret o an d th e follnynn g specia l conditio n (s\) : U 0pei"#i,o;n ; o f th e emis&la n s^reels i tnclMed
. I'll
. Wis. pgfTfiltshal l not tseft n ucnfS l al l s^^fajag d ai f j ?6 ;Ttoti;£> h contro l equipWeh t has bee n ^nstWt.ed : an d i; s y$^$:$%$Mi f « Wltht h $ 0 dafs : fpo m the * !'gsi#j|e
. <o; f tftf g pMtt i 4 carbon
. §$sf$§ ^ breakthroug h monitorin g progra m sftal l be submitte d fo rAgenc yapproval
. %eraj % n M tM s tan k farm ; s%afj; l no t begi n unti l M^^m^,a^m&i I, s 

### Emissions ; o f $^ani cmateria: ! sJraC l no t excee d 2, 5 tpnt^ear , t# # l;fni £ l i :&asej | a h fh^ria^loj j prjsvlfe d f h th e flp^fea1fro ;ni

Terr y t^K ; Sweitzej^PvIE , f%jia|#, . Permi tSectio n Divisio n of

Ai rPollutio n Contro l TAS:JD£:amm 5 /49a9H /S . i 

### cc : Regio

n 3


### RECEIVE S m

Z $ fl88 VE S 00076 3

### yji e ffinoMfittg-coiiiilbi^j B ire. ^

3(fifi ^ fi$li: gati

s o f Seauaae^

j u^p g f

ij$j^$q % ^rflg^amo f conetruslipp o r4^fopjpa:en to » this j^^t e



### -^pg WMm sa t^ec^bajiSl i W Wj&fa^&iM

hwete « |a|:fE#ep | jig - iM ^meg-m&m n^j^t^MM' 

# 0%. P8e-|iBSB0lJstee ; 

### ^gi' . sssjftp-

' ftgc^eQjy

- njdSna^i * agltt-

i f £ 

### ife iipm

# torn f 

### «e|etft|tfe i 

### «*

f 

### SHU^0M%

- 

## «* •

a . tp)fcnter

; l^ e pef^tt^e' s peojje f t y wlier c ac.tuft l o^ppientt'a

l effi^ ^ hois d sourse s ar e locate d o r j$rgC e aji y activilysi s fo h

e eftftdugje

d fthratianto tlu s 'peradt j \ B . t

o hav e acces s t o an d t o cop y £ny'recqrd' s required t o be j^p tujade

* the.terni

B an d condition

s b| ; thi' s permit

, c . t o i^pf^f s j^fl^ftg-^^u g •aiay;&^fi'^lMffot ' equipmen teona&uete: ! p

rppgi-aie d i|n.de rthi s peraait

, sUcK ^ t o h e fcepf), used,.opetated

i c|ijipfr'a:te

d aii d maintained Un# r'tliif e 

### mmk 

### "' '~ «

### - •• • a . , to ; obtain and retnov e gsiiiipfe

s o f air y d.wcharg

e o rejp|s§jipn6vpf

plUtttanls , and 0>: t o enterand utiliz e an

y photographic

, recording, testing , monitoring o rotherequipmen

tfor th e purpos e o f preseryiftg, testing , monitoring- , o rrecordin g sSi y activity , discharg

e o remisBtG

n authorize

d b y this permit

. Mk< "$h

e issuanc

e o f this penult : .a, shal l no

tb e considere

d a s ii i an y mannerSf%dUn

g th e titl e o f the premise

s upo n Whic h th e permitte

d facilitie s ar

e t o b e located, b . does'no

treleas e th e permitte

e Fro m an y liabilit y fo rdamag e t o perso n orpropert

y cause d h y o rresulting fro

m th e construction , maintenance, o roperatio

n o f th e propose

d facilities ,

. e > doe s no trelease th

e permitte

e from.cotnpliatiij e Wit

h othe rapplicable statutes an d regulation

s o f th e Unite d I Statea

v o f th e Stat e o f Hlinojs , o

rwit h appucfibi

e loca l laws, ordinance

s ari d regulatlolfts, d i doe s nO ttak e int o consideratio

n o rattestt p the structural stabilit y o f art y units o rpart s o f th * project

, ari d 

### Af> G 

### <B 6 tR=v . 10/85 1 G9&00 5 

### VE S 00076 4The Illinois (fll|kq & Ife^sgjl ' iSfiatftteje v -SSteffes

tl&i-tjk, Seetib

a WIU " iSW * th

© BiLviconxoiei^ I ^l^^nj^^ ^ S&t£g^^"feiEgtt ^ ^ffiip^ioafi^a^S : #M^ S iCiasu.es . conaiifon

a at e applteabl

e iinles a si|#ggB|ifeft

. b y specia l permit ; cendjtion® .

% ,|^jLg§^,J ^ 

## *? 8l 

## ? 3 

## 4 . M§/$iiS> & teei upoti , $ie..feTfliroatio

a

## s)ib^^ a bj

r t%e- ' fe 'Eitfi |f^r$S ' th

e jpr-ntff c dteg--iBl#^nS,gjtg % false : ^a|gj&§$j,j i o f ; ttisp «ssen&*!pi i .lid

, *h/e.

: £gpllea#0! i Shal

th e gtopuadfi

r St. . a.. •pleiJ|^^1^fe : , 4^||^^&# , stttorfSg};.aljf^&llf : j^odafioaiion , 'aB; . defllie S in . 36111 . Adin. : @ode

. •M||£$a|L3i ^ fp'r^ievMpp;o|tf e ^ji$j |ag £iw^ ^ tt^piJitoItrQr. revisiet i 'o f ; |i^Meifcinfoget^l^) 1 ltiiB^ed . for-isucl inp;di5c|Liiipri . 'b;- : ^bl a germii vaalj c ^If^S'eaTtiagio

n aetl.tJC6J|

, if d •contro

l ed^uigiiReli

tS?hll e phyEicall

y pr^sM ^ at.th

e indic&ieg

l nd|^illiSMadiii| f

th e expjr#ipn d£.t e specified O n th e p'ecjiiit4 . Th< | prjnitfeee shal l AIIQWaay\duly auihorip d ageS to f th e Agency ^ uppl

i th e presentiatio

h ot . credeHiMs f

al t fcgjgiiiable ; times : ' • . a. t o fen|iefc fhe: : .|«stiBitfcee' s property , tyhere actual o rpotentia l effluent , emission

, p rnoise sources'toeifpgatSd or ; vftere:;fii^a:ctiyit

y i s t o h e conducte

d pursuant,(

a thi s permit, h . ,t^'|ifty

p aeces 8 & :an.d.|b

. gdp^-.aTiy

, woof p* s rgqiiii-g

d t p b e kep ti^d^r' : tb $ tlrjn a ; :an d «Ojiffiia£ 8 o

f thi s permi t •••C i it o inBpee ^ thi s permit, . ;g;q^iprnJi.iii

i an d any-equipffiejtt:£ ^ cfiibr^te d a,n d mainia%e,lj.^fe,|his . perihit , , d ; td , obtain an

d rejtnov e sample s o f an y disc)ia$ge

~ oremission O

f poilu;ta;nts

, an d e, . t o enteran d utilizi

j an y photographic

, recording

s testing ; moriitpring or . othe requipmen

tfo rth e purpos e o f presetViflg

i testing , monitorin

g o rrecording an

y activity , discharg

e o remissio

n authorize

d b y this permit

. ii . The ! issuanc

e o f thi s permit : % shal l no tb e considere d a s i n an y manne

raffectin g thf

e titt e of - th e premise

s upo n whic h th e permitte

d facilitie s ^Lr

e located, b . doe s netrelease thepermitte e from an

y liability fprdamag e t o perso n o rpropert y caused b

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m tli e construction , maintenance , oroperation o

f th e .Facilities , V E S 00076 5

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### Sectio n 2. 1 (C)(2 ) Modificatio n o f operatin g parameter s limit s (OPL's ) Table
. ; Pursuan t t o th e Reques t t o Provid e informatio n Pursuan t t o th e Clea n Ai rAc t date d Jun e 5 , 260 8 an d subsequentl yrevise d o n Septembe r12,2008 , attache d i s a revise d Oper ^

Parameter s Limit s (OPL's ) tabl e tha t reflec t the mercury , S V M an d LV M QfV s define d i n 4 6 CF R 63.1209
. Th e OPU s wer e modifi e o n th e result s orth e performanc e testin g tha t r^re'^i(if^ve6^t^

USEPA , Regio n 5 o n Augus t 8,200 8 an d conducte d i n Augus t an d September , 2008
. Thes e tes t pla n result s hav e bee n submitte d a s par t o f th e Fleques t frori i USEP Adescribe d above
. Veoli a ha s extrapolate d meta l feedrat e limit s fo rmercury , SV M an d LVM
. Thes e feedrate s wer e e ^

usin g th e protoco l provide d b yUSEP A(attached ) an d include d i n th e Performanc e Tes t Plan
. Th e calculatio n sheet s ar e include d wit h thi s request , However, ; base d o n th e extremel yhig h Syste m Remova l Efficiencie s (SRE's ) achieve d durin g thi s testing , Veoli a ha s lowere d th e extrapolate d meta l feedrate s fo rSV M an d LV M a t Unit/ 4 t o accoun t fo rhistorica l ; M Veoh a ha s als o lowere d th e extrapolate d meta l feedrate s fo rSV M an d LV M a t Uni t 2 to matc h thos e value s a t Uni t 3 an d agai n takin g int o accoun t historica l meta l feedrat e dataa s define d i n 4

6 CF R 120 9 (n)(2)(ii)(B)(2)
. Attache d dat a sheet s detai l th e extrapolate d OPL' s compare d t o th e requeste d OPL's
. I n orde rfo rextrapolatio n t o b e utilized , Veoli a conducte d thes e performanc e tes t usin g meta l feedrate s a s define d i n 4 0 CF R 120 7 (f)(1)(x)(B) , tha t wer e greate r tha n "th e historica l rang e o f norma l metal s feedrates " fe d t o th e unit s ove rth e las t year . Include d i s a tabl e tha t define s averag e feedrate s fo rmetal s ove rth e pas t yea rcompare d t o the actua l rate s tha t wer e spike d an d fe d t o th e inciherator s durin g th e performanc e test
. A s i s detailed , th e metal s fe d t o th e incinerator s durin g the performanc e tes t wer e significantl yhighe rtha n th e historica l rang e o f norma l meta l feed s ove rtha t yea ran d i n som e case s wer e highe rtha n th e 1 2 maximu m values
. A s state d above , Veolia' s extrapolate d meta l feedrate s define d i n th e attache d tabl e use d th e extrapolate d metho d define d i n th e Performanc e Tes t Pla n a s require d b y4 0 CF R 120 7 (f)( 1 )(x) (A ) an d give n t o Veoli a b yUSEP ARegio n 5 a s a n approve d metho d bu t als o too k int o accoun t historica l meta l feedrate s fo r eac h uni t i n settin g thes e extrapolate d value s a s require d b ythe 4 0 CF R 120 9 (n)(2)(ii)(B)(2)
. Veoli a i s requestin g approva l of thes e extrapolate d feedrate s no t onl ybecaus e i t followe d th e requirement s o f the Regulation s bu t i t ha s bee n th e Agency' s practic e o f permittin g extrapolatio n wit h othe rRegio n 5 incinerators
. Veoli a reques t tha t extrapolatio n b e approve d base d o n the merit s o f the methodolog yutilized , the meta l federate s a t whic h th e performanc e test s wer e

V E S 00076 8\Ve61ia. ' Environmenta l Service s Page : 1 3 o f 17 6 -

. Permit-No/' : ;'V:-IL-17163001p3-08-0 1 .2 1 .'/.permittee , must'operate " Unit s 2 , 3 , an d 4 unde r thes e '•'- . ... / operating.parameter s limit s (OPL's ) to ' demonstrate. . ^;'..:"«:^p^pliauveei ; with'-.-Subpart ; EEE . - - - • .Operatin g Parameter s . ' . ' • Oni t# 2 . Uni t#3 • Oni t# 4 •• AWFC O • • Minimu m primar y cOnibuStion' -

- • chamber ; temperature . - V6Vl ^ ••/ ' 1,712' F l t 734°F ' "•' . 

### Liy.71 2 . " l r ,50Q° F .



### 1 , 50 7 /•:': . . Minimu

m hourl y rollin g averag e .Minimum ' secondar y .;• '•:_ " . • .. : 'p6mbii.s'tion'"clii^be'r' . • : ' ' ; • ; ' temperatur e ...' ' ., - ' • (63 . i20 9 (j),'{£) ; (k i (2 ) )':•:-.. ' •. . . l: , 8 48° ? 

### li?:845 ' . 1,850-°F ,



### L ,84 5 . . 1,88 6 Minimum hourl y rollin g averag e Maximu m flu e .gas - flowrate''.. ' o rproductio n :.rafce' - •• ' '•: - - :;(63/l '2b5'(j)'f25 ')';-'':.(fc. ) (.3) , : ' 

### (m ) (2 ) V . (ri ) (6) , lp).m)

-. ..'
. 10 > 3GO.acf/ mi n 

### 15,14 7 "- . '1

- 3 > il l acf/. , mi n 

### 15,14 7 . .43,-40 0 ' acf/min . 

### 38,0 8 6 .'''.- . hourl y

rollin g average s Maximum-hazardou s Wast e pumblabl e feedrat e rat e fo r .each / 'combustio n chamber'.. <63.120 9 (j ) (3) , . (k)(4) ) / 3,00 3 ' . " lbs/h r 

### 3,12 3 4ylG0 -

lbs/h r' . ' 

### 3,12 3 W*3,25 6

lbs/h rfo r •PC C an d irW-1,00 6 lbs/h rfo r scc hourl y

-rollin g average s

: Maximu

m , hazardou s '.wast e .'-•; ' total- ' feedrate ; -rat0 ..'.f or- ' .eae n .'combqs.tio h . chamber. ' ., ' • , • ;/6i;:;i'2 : p9/(j ) (?Vr/Ykr/<4f) . '•./ . / ' 4,14 0 , . . lbs/h r 

### 4 ,30 1 5-

, .3 4 4 - . . lbs/h r• 

### 4,30. 1 . •: . 17,-907 , ^ 7 Q ,

..ibs/h rmt 

### E.CC- and ' " . 

### p *f*f. 1,00 6 •lbs/hr . for . . .SC C '. '

• hourl y rollin g .averag e basi s Operatio n o f ':wa$.te/.firin g 'system - fo reac h : locatio n '.wher e waste ' i s fed-to ' the' ' •incinerator ' (6.3 ; 1209 ( j ) (4) ) : Minimum wast e . atomizatio n pressur e fo rlo w BT

O wa s t e - 1

5 ps i Minimum ' .

waste atomizatio n •

• pressur e for-lo w BT U wast e - 1 5 ps i Minimum •

wast e . atom'izatio h ' pressur e for'lo w BTU wast e - I S ps i . " Instanta n

' eou s

Maximu m temperatur e o f

th e gas. , a tth e inlet . .(63;u:09.(k>tij .)v :'lny : (l) ) ,. : .420 ° F 420° F 43 4 hourl y rollin g averag e Minimu m carbon ' injectio n ';.- ' ' .idtji. ' (6

3 . 120 9 (k).:(6r(i)) ' . , N/ A N/ A • -6-'lbs/h r. .6. 2 hourl y

rollin g averag e Minimu m .'carrier. , flui d (ga s o rliquid).'flowrat e o r/*.' / • ' pressur e .dro p . •

' - ' (63.520 9 (k

) (6 ) (.i i ! ).,'. . ,•/'. - ' : N/ A . N/ A , ' ' .miniitiuiA ; ' hig h •- • pressure' ; • 4 psi g Maximu m lo w pressure : ' 1 inc h H 2 0 hourl y

rollin g averag e Th e bran d (i:e. , manufacturer ) an d typ e o f carbo n use d durin g th e comprehensiv e performance ' tes t,(6

3 . 1209 (k

) (6 ) (iii ) ) N/

A N/ A NORI T America s Inc . DARCO ® FGL Tota l feedrat e o f mercur y | 0.017 4 0.017 4 0 . 25 7 12-hou r



### V E S 00077 0'.'Vebli a Environmenta l Service s . • Page : 1 4 o f 17 6 VWrmi t ^o/:.-V 7 IL-1716300i03-08-0 1 "Operating' ' Parameter s , Oni t# 2 • Uni t#

3 Oni t#

4 AWFC

O (G3.1209 ; :(l ) (1 ) (i) > . . • ; rollin g averag e Maximum.-'ash - federat e • "(6l'^1269'jiiv)'{3iV : • . •-./ . • 67 3 ;'. / 9.13. 4 lbs/hr , g 7 3 . 7,CS O

lbs/h r 8,77 7 12-hou r•

rollin g averag e ' •TQta;li-'fe.e_sira'te";'o f '-,.'. ' seM.^yi'a'tiie;Ve.tai. s ^^:^Ql(nf';t2T:i i 1 > •.; v.;-'. ; -/ . V 45'9. ' \ -4S9-. . . 50 0 12-hp.u r rollin g average ' limit s Total , .feedrate-.q.f ' lo w • . •.yoiatile-'me'tal s - : ' . • " • 120.9 (n' V (2. ) (ii ) ) . • . . . 39 9 ' - - 39 9 50 0 . 12-hou r• rollin g averag e limit s ; ' .'Feedrate-limits ! -.fo rlo w •• ' •.volatile " jrietais " i n pumpabl e feedstream s '-'.

- •' : •" • .(e3 -.iZ09-'('nr-(2) (vii ) ) 36 8 36 8 ' -42 7 • 12^-hou r rollin g average ' limit s Feedra-te-xi f

tota l chlorin e • •'and;chlqr'id e .in ' al l • ' •'feWstream's'' <63.i209.(n ) (4) > ;•'(ai :(i).)' : . /-., : •'//. -. • - &5*~ . lbs/h x .

. .22.9 . '; . lbs/h r•

.. . . 22 9 -e^H - lbs/h r 25 2 • 12-hpu r

rollin g average . * Minimum

, sorbent'. ' feedrat e ; .t63'.'li09.;Co)'<4)''(i ) ) . . . 1.7 6 lb/l b



### - • rr-? '- 1.7 6 lb/l b ' : C-l°' r ' 1.0 1 lb/l b

• Minimum" - carrier , flui d • ; . f ipy'rate l o r.hd.zz.le / pressure. . v 'dro p ;;fii rtYis-'-Spray- - dr y

- . ''adsotbcf;'"^6.3 . i'20 9 . . . • • %(o)'(4'j:(-ii) r

:J
- ; • 1.7 0 Gal/ 1

- : : ci - 2 ' . •

> ' 1.7 0 Gal / l b C1 2 1.6 1 -Gal /

l b C1 2 "TEe'.'brand:•-.( , i;'e.'> . manufacturer")''an d typ e o f ' .' - - sdrben't ' used.'/durin g the -

. - cpmpjteh'ensiye /

performanc e " ' .'tes t(63 .12.09 : '(o)'(4 ) '(ii i i ! (AV ) Mississipp i

Lim e Company Hydrate d ' Lim e Cod e MR2O 0 Mississippi •

Lime ' Company Hydrate d Lim e Cod e MR20 0 Mississipp i

Lim e Company. Hydrate d L ime Cod e MR20 0 Maximu m combustio n chambe r •pressure-' ' (63' . 120 9 (p ) ) -0.0 1 inch H 2 0 -0.0 1 inc h

H 2 0 -0.0 1 inc h

H 2 0 5 second s

fo runit' s 2' an d 3 an d iostanta n eou s Co r uni t4 

### .3'. ' - ..'. : 

### C '0 'rttpli.'a'nc

e . v ith standards : 140/'C
. F:.R."••§.'6 3 .120"6.('b] (.1 ] j /.', K /v ' 

### .'T.K'4 : emissio n standard s an d .operatin g requirement s se t ; .-: . '.'....-.--.f o rti i derived ' f rom-.Subpa rt EE E appl y-a t al l time s -' / ;; - . ' - ' except;: - ' ' .' • • (a ) Durin g period s o f startup , shutdown , an d malfunction ; an d (b ) Whe n hazardou s wast e i s no t i n th e combustio n chambe r(i.e. , th e hazardou s wast e fee d t o th e combusto rha s bee n cu t of f fo ra perio d o f tim e no t

V E S 00077 1USEP A Approve d Extrapolatio n Method; - Tota l Tota l

' •- , • LVMEmis . SVMEmis . H g Emis . Stackflo w Oxyge n LV M Fee d . Rat e (ER ) SV M Fee d : Rate(ER ) H g Fee d Rate(ER ) Tes t Dat a Ru n (dscfm ) (%dry ) (Ib/hr

) (Ib/hr

) (Ib/hr

) (IbJhr

) < (Ib/hr

) (Ib/hr

) Uni t 2 (8/08

) 1 549 6 11.7

2 0:005 2 •0:00079 1 2 557

2 . . ii:5 4 0.004 4 0.00082

2 3 535

7 . 11.3 0.004 6 0.00079

9 Uni t 2 (9/08

) 1 469 8 11.2 1 47 ; 0.00012 5 6

2 0.00039

8 , 2 509

9 10.9

1 4

7 0.000043

8 6

4 . 0.00014

4 3 524

8 . 11.3

5 47 . 0.000101 6 3 0.00036

4 Uni t 3 (8/08

) 

### \ 5665 , 11.9 9 5

1 . 0.00038

8 • •6 5 0.00079

9 0.004

5 0.00074

8 2 .5719 , . 10.9 6 51 , .. . 0.00030 8 6

6 0.0010

3 0.005

6 0.00093

8 3 589

0 11.9

8 52- . .0.0002 2 6

5 0.00065

5 •0.005 1 0:00081 8 Uni t 4 (8/08

) 1 1728 0 12.2

7 5

5 0.00021 4 6 5 0.000

9 0:O306. . : 0.0015 3 . . 2 1725

5 12.1 3 55 0.00042 5 6

5 0.001 3 0.030 4 0.00099

6 3 1718

9 11.6

3 5

5 0.00058

6 6

6 0.0011 6 0.030 6 . 0.0010

8



### V E S 00077 2USEP A Approve d Extrapolatio n Metho d [1 ] [2

] [3

] 14

] Propose d Propose d Uni t 2 (LVM ) Remova l Max . E R a t 75 % LV M Feedrate Extrapolatio n Extrapolatio n Em . Std. : 9

2 ug/dsc m Efficienc y (RE ) Stackflow of Standar d OP L Limi t (Total ) Limi t (Pump. ) (9/08 ) (% ) (dscfm.7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) (lb/hr

) 1 99.9997

3 671 8 0.00173 4 65

2 2 99.9999 1 707 5 0.001826 195 9 3 99.9997

9 761 4 0.00196 5 91 4 Av g 99.9998 1 713 6 0.00184 1 117 5 39

9 36

8 [1 ] 12

] [3

] [4

] Propose d Uni t 2 (SVM ) Remova l Max . E R a t 75 % SV M Feedrate Extrapolatio n Em . Std. : 230 ug/dsc m Efficienc y (RE ) Stackflo w of Standar d OP L Limi t

(9/08 ) (% ) (dscfm , 7%02 ) (Ib/hr

) (lb/hr

) (lb/hr

) 1 99.99936 671 8 0.00433 4 67

5 2 99.9997

8 707

5 0.00456

4 2029 3 99.9994

2 761 4 0.00491 2 85 0 Av g 99.99952 7136 0.00460 4 118

5 45 9 [1 ] [2

] [3

] [4

] Propose d Unit2(Hg ) Remova l Max . E R a t 75 % H g Feedrate Extrapolatio n Em . Std. : 13

0 ug/dsc m Efficienc y (RE ) Stackflo w of Standar d OP L Limi t (8/08 ) (% ) (dscfm.7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) 1 84.79 8291 0.00302 4 0.019

9 2 81.32 824 6 0.00300

7 0.016 1 3 82.63 773 2 0.00281 9 0.016 2 Av g 82.9 1 809 0 0.002950 0.017 4 

### I 0.01 7 Extrapolate

d metal s feedrate

s calculated usin g USEP A approve d method .USEP A Approve d Extrapolatio n Metho d [1 ] [2

] P I [4 ] Propose d Propose d Uni t 3 (LVM ) Remova l Max . E R a t 75 % LV M Feedrat

e Extrapolatio n Extrapolatio n Em . Std. : 9

2 ug/dsc m Efficienc y (RE) Stackflow o f Standard OP L Limi t Limi t (Pump. ) (% ) (dscfm,7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) (Ib/hr

) 1 99.9992

4 880

2 0.00227

2 29

9 2 99.9994

0 797

5 0.00205

8 34

1 3 99.9995

8 914

2 0.00235

9 55

8 Av g 99.9994

0 864

0 0.00223

0 39

9 39

9 36

8 [1 ] [2

] P I [4 ] Propose d Uni t 3 (SVM ) Remova l Max . ERat75 % SV M Feedrat e Extrapolatio n Em . Std. : 23

0 ug/dsc m Efficienc y (RE) Stackflow of Standard OP L Limi t (% ) (dscfm,7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) 1 99.9987

7 880

2 0.00567

9 46

2 2 99.9984

4 797

5 0.00514

5 33

0 3 99.9989

9 914

2 0.00589

8 58

5 Av g 99.9987

3 864

0 0.00557

4 45

9 45

9
I U [2

] [3

] [4

] Propose d Unit3(Hg ) Remova l Max . E R a t 75 % H g Feedrat

e Extrapolatio n Em . Std. : 13

0 ug/dsc m Efficienc y (RE ) Stackflow o f Standard OP L Limi t (% ) (dscfm,7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) 1 83.3

8 880

2 0.00321 0 0.019 3 2 83.2

5 797

5 0.00290

8 0.017

4 3 83.9

6 914

2 0.00333

4 0.020

8 Av g 83.5

3 864

0 0.00315 1 0.019 2 0.01 7 I Extrapolate

d metal s feedrate

s calculate

d usin g USEP A approve d method .USEP A Approve d Extrapolatio n Metho d [1 ] [2

] [3

] [4

] Propose d Propose d Uni t 4 (LVM ) Remova l Max . ERat75 % LV M Feedrate Extrapolatio n Extrapolatio n Em . Std. : 9

2 ug/dsc m Efficienc y (RE ) Stackflow o f Standar d OP L Limi t Limi t (Pump. ) (% ) (dscfm,7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) (Ib/hr

) 1 99.9996 1 2771 1 0.00715 1 183 8 2 99.99923 2723 4 0.00702

8 91 0 3 99.9989

3 2568

3 0.00662

8 62

2 Av g 99.99926 2687 6 0.00693

6 112

3 50

0 427 [1 ] [2

] [3

] [4

] Propose d Uni t 4 (SVM ) Remova l Max . E R a t 75 % SV M Feedrate Extrapolatio n Em . Std. : 23

0 ug/dsc m Efficienc y (RE ) Stackflow of Standar d OP L Limi t (% ) (dscfm.7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) 1 99.9986

2 2771 1 0.01787 8 129

1 2 99.9980

0 2723

4 0.017571 87 9 3 99.99824 2568 3 0.01657

0 94

3 Av g 99.99829 2687 6 0.01734

0 103

8 50

0 [1 ] [2

] [3

] [4

] Propose d Unit4(Hg ) Remova l Max . E R a t 75 % H g Feedrate Extrapolatio n Em . Std. : 13

0 ug/dsc m Efficienc y (RE ) Stackflow of Standard OP L Limi t (% ) (dscfm,7%02 ) (Ib/hr ) (Ib/hr

) (Ib/hr

) 1 95.0

0 2771 1 0.01010 5 0.20

2 2 96.7

2 2723

4 0.00993 1 0.30 3 3 96.4

7 2568

3 0.00936

5 0.26

5 Av g 96.0

6 2687

6 0.00980 1 0.25 7 0.25

7 I Extrapolate

d metal s feedrate

s calculate

d usin g USEP A approve d method .1 Yea r Metal s Dat a '
. •• • " -" ' Iv-
. • • | •

_ . /I.."--'. - . 06/01.0 7 thr u 05/31/0 8 .06/01/0 7 thr u 05/31(0 8 • - - . . . - . . 06/01/0 7 thr u 05/31/0 8

.. , ' • • LV M Uni t 2 Uni

t 3 Unit* .

, SV M Uni t 2 ... ' uni t 3 Unlt4. ; H g v:: . Uni t 2 Uni

t 3 Uni

t 4 (lbs/hr ) (lbs/hr

) . (lbs/hr) : (lbs/hr ) : (lbs/hr

) (lbs/hr

) (lbs/hr ) (lbs/hr

) . (lbs/hr

) : '...
. - ••

• '' 12 H r Ma x Valu e 77.7

4 .38.8

8 77.2

9 1

2 H r Ma x Valu e '.90.7

3 -.81.5

9 ' . -58.3 B 12 H

r Ma x Valu e , . ' . ;0.00539

6 0.0041 6 0.0537

3

'
. \ e '
. . . ' 12 H r Av g Valu e •1.8

8 ":',." " 1.1 8 .3.0

3 12 H

r Av g Valu e . i : 1.7

5 . ' ; .1.9

8 . . 3.8 1 12 H

r Av g Valu e - 0.000297

2 .0.000243

3 .0.00723

2 ..''.•••,•' • St d De v . 6.0

0 3.6

9 6.5

S St

d De v . 5.7 1 6.8

0 . 6.0 9 StdDe

v 0.000710

9 0.000568

3 0.00894

3 Avg + 1 StdDe

v 7.8

8 '4.8

7 8.5

8 Av

g + IStdDe

v . ' "

, . 7.4 6 8.7

8 9.9 0 Av

g + 1 StdDe v 0.00100

8 0.00081 2 0.01617

5 Av g + 2StdDe

v '13.8

8 ' 8.5

6 '14.1 3 Av

g + 2 StdDe

v' : 13.1 7 15.5 8 15.9 9 Avg

+ 2 StdDe v 0.00171 9 0.001379 9 0.02511 8 200 8 Tes t Fee d Rate s 4

7 '6

1 5

5 200

B Tes t Fee d Rate s ' 6

3 6

5 - . -6 5 200

8 Tes t Fee d Rate s 0.004

7 0.005

1 0.03

1

V E S 00077 6

### Utilizatio n o f Metho d 2 3 fo rDioxin/Fura

n Emission

s Th e HW C MAC T standar

d a t4 0 CF R§63.l208(b)(l)(i)(A ) specifie s th e us e o f EP A SW-84 6 Metho d 0023 A t o determin

e complianc

e wit h th e emissio n standar d fo rdioxin s ari d furans . Alternatively

, th e standar d provide s i n 4 0 CF R§63.1208(b)(i)(i)(B ) tha tMetho d 2 3 (4 0 CFR, Par t60 , Appendi

x A ) ca n b e used , afte rapprova

l b y th e Administrator

, Lubrizo

l request s approva l t o us e Metho d 2 3 t o detennin

e complianc

e wit h th e emissio n standar d fordioxin

s and . furan s whe n i tconduct s th e WHR I CPT . Furthe

rexplanatio

n an d justificatio

n fo rthi s alternativ

e monitorin

g reques ti s foun d i n Sectio n 6.1 . 3. 3 Mercur

y Feedrat

e LimitDeterminatio

n Lubrizo l requeste d awaive rfrom conductin

g th e performanc

e tes tt o documen

tcomplianc

e wit h th e mercur y emissio n Standar d pe r4 0 CFR-63.1207(m

) an d 63.7(h). Thi

s reques twa s include d i n th e 200 2 CP T Pla

n an d approve

d b y US EP A o n Augus t29 , 2003 . Lubrizo

l wil l utiliz e th e maximu m theoretica

l emission

, concentratio

n (MTEC ) approac

h t o documen

ton-goin

g complianc

e wit h th e mercur y emissio n standar d pe r4 0 CF R63.1207(m)(4)..

. Thi s approac h i s base d o n al l th e mercur y fe d t o th e combusto

rbein g emitte d throug h th e stack . (i.e. , d o no ttak e an y credi tformercur

y remova l i n th e ARCS) . Th

e mercur y concentration

: i n al l feedstream

s wil l b e determine

d pe rth e feedstrea

m analysi

s pla n (FAP ) require d b y 4 0 CFR63.1209(c) ; Th

e mercur y feedrat e o f eac h feedstrea

m will b e determine

d pe rth e discussio

n i n Sectio n 3.1 , Base

d o n historica

l analytica

l an d wast e feedrat e data , th e maximu

m mercur

y feedrat e limi twill b e 0.001 4 lb/hr . Thi s OP L wil l b e monitore

d o n aI2-HR

A basi s an d wil l b e interlocke

d t o th e AWFC O system

. Pe r4 0 CFR63.l207(m)(5

) th e ful l detectio n limi twil l b e assume d fo r feedstream

s wher e mercur y i s no tdetected

. I n addition

, aminimu

m flu e ga s flo w rat e (acfm ) OP L ha s bee n determined

. Base d o n flu e ga s parameter s collecte d i n conjunctio

n wit h th e 200 3 CPT , th

e mercur y emissio n limi to f 13. 0 ug/dsc m a t7 percen

toxyge n an d th e maximu

m mercur

y feedrat e o f 0.001 4 Ib/hr ; th e minimu m flu e ga s flow rat

e o f 773 8 acf m wa s calculated

. Th e flu e ga s flo w rat e i s continuousl

y monitore

d an d th e minimu m OP L wil l b e interlocke

d t o th e AWFC O system

. Th e minimu m flu e ga s flo w rat e OP L will- b e monitore

d o n a12-HR

A basis . Thes e tw o OPLs i

n conjunctio

n assur e complianc

e wit h th e mercur y emissio n limi tpe r4 0 CF R63.1207(m)(4)

. 3. 4 Metals Feedrat

e Extrapolatio

n Procedure

s I n orde rt o establis h a n approac h fo rcontrollin

g meta l hazardou

s ai rpollutants

, U S EP A groupe d th e metal s i n categorie

s b y thei rrelativ e volatility

. Th e categorie

s includ e lo w volatilit

y metal s (LVM) , semi-volatil

e metal s (SVM ) an d volatil e metals . Th e LV M categor

y include s arsenic ,

1 8 V E S 00077 7

### beryllium , an d chromium

. Th e SV M categor

y consist s o f cadmiu m an d lead . Mercur y i s th e onl y volatil e meta l regulate d b y th e MAC T standard

. Fo rth e purpos e o f th e CPT , on

e meta l from eac

h ofth e LV M an

d SV M categorie

s wil l b e spike d t o fh e incinerator

. Th e mercur y feedrat e limi ti s establishe

d an d monitore

d base d o n th e maximu m theoretica

l emissio n concentration

, a s discusse

d i n Sectio n 3.3. The . emissio n limit s fo rth e LV M an

d SV M categorie

s fo rexistin g incinerator

s are:

• LV M (tota

l o f As , Be , an

d Cr ) 9 2 ug/dscm

, correcte d t o 7 % 0 2 

### • SV M (totalo

f C d an d Pb ) 23

0 ug/dscm

, correcte d t o 7 % 0 2 

### Lubrizo l intend s t o spik e metal s durin g th e CP T t o assur e tha tmeta l feedrate s demonstrate

d durin g th e CPT wil

l allo w fo radequat e flexibilit

y base d o n historica

l meta l feedrat e data . However , du e t o variation

s i n wast e feedstreams

, analytica

l uncertainties

, an d othe rfactors , Lubrizo l will continu

e t o utiliz e fh e metal s feedrat e extrapolatio

n procedur

e pe r4 0 CFR 63.1209(n)(2)(ii

) base d o n th e prio rapprova

l o f thi s techniqu

e b y U S EP A Regio n 5 . Th e Technica

l Implementatio

n Documen

t(TID ) fo rU S EPA' s Boile

ran d Industria

l Fumac e (BIF ) Regulation

s (U S EPA , OSWER

, EPA530-R-92-Q11, PB92-15 4 947 , Marc h 1992 ) provide s a detaile d discussio

n o f th e theoretica

l rationale

. fo rupwar d extrapolatio

n o f allowabl e metal s feedrate s base d o n th e relationshi

p of metal s feedrate s an d emission

s rate s demonstrate

d durin g testin g o f a unit . Th e relationshi

p o f metal s feedrate s an d resultin g emissio n rate s i s comple x an d dependen to n anumbe

ro f factor s includin g operatin g conditions

, th e ai rpollutio n contro l system , an d th e meta l feedrat e itself . Thi s guidanc e ha s propose d tha tthre e zone s o f relationshi

p betwee n feedrat e an d emissio n rat e exist . Thes e zone s are : I ) vaporization

, whic h characterize

s condition

s belo w saturatio

n o f th e meta l in th e combustio

n gas , 2 ) entrainment

, whic h describe

s th e condition

s durin g whic h metal s ar e primaril y entraine

d o n th e as h particle s i n th e system , an d 3 ) complex

, whic h include s th e effect s fro m bot h soli d an d liqui d fee d stream s beyon d th e poin ta twhic h metal s concentration

s i h th e liqui d strea m alon e ar e i n exces s o f th e ga s saturatio

n poin tTh e g u idanc e propose s tha twithi n eac h o f thes e zones , th e relationshi

p of feedrat e an d emissio n rat e i s linear . Therefore

, extrapolatio

n o f metal s feedrate

s withi n a zon e i s performe

d simply , b y assumin

g a linea r relationship

. Additionally

, contribution

s o f metal s fro m soli d an d liqui d stream s ar e additive .

1 9 

### VE S 00077 8

### Lubrizo l utilize d th e remova l efficienc

y (RE ) demonstrate

d durin g th e 200 2 CPT fo rLV M an d SV M an d 75 % ofth e HW C MAC T emissio n standar d fo rth e respectiv

e meta l categorie

s t o determin e .th e permitte

d LV M an

d SV M feedrate

. Th e step s fo rutilizin g extrapolatio

n t o calculat e th e LV M an

d SV M feedrat

e limit s ar e detaile d below . 1 . Detennin

e th e demonstrate

d LV M an

d SV M R E base

d o n dat ademonstrate

d durin g th e CPT - (LV M feedrate , lb/h r- LV M emissio

n rat e (ER) , lb/hr

) x 10 0 

### LrV M RJb, /o-— • • — —: ^ LV M feedrat

e lb/h r cir * n, c o, ( S Y M

### feedrate , lb/hr - SV M emissio

n rat e (ER) , lb/hr

) x 10 0 S V M feedrate

, Ib/h r f - . . . . 

### 2. Utiliz e th e flu e ga s flowrate measure

d b y th e stac k tes tcre w (i n dscfrn ) an d correc tt o 7 % oxyge n usin g th e followin

g calculation : dscfm (measured)

* (14 - (21 - dry %Oi)) = dscfm, 7%0 2 

### 3 . Calculat

e th e maximu

m mas s emissio n rat e (ER ) of LV M an d SVM a t7 5 percen tofth e HW C MAC T emissio

n standar d base d o h th e ga s flowrat e demonstrate

d durin g th e CPT : Max LVM

ER, lb/hr = 69 jig/dscm, 7%0 2 

### * dscfm,. 7%0 2 

### * 0.0283 dscm/dscf
* 60 min/hr * 1 lb/453.6g

* 1 g/10

6 

### fxg Max. SVMER; lb/hr

= 173 /Jg/dscm, 7%

0 2 

### * dscfm, 7%0 2 

### * 0.0283 dscm/dscf * 6 0 min/h r* 1 lb/453.

6 g * 1 g/10 6 

### 4. Calculat

e th e permitte

d LV M "an

d SV M feedrat

e OP L base d o h th e mas s emissio n rate s determine d in . ste p 3 an d th e LV M an

d SV M RE' s demonstrate d durin g th e CPT .

rTM? A * * no riu,u Ma x LV M

ER - lb/h r 

### LV M feedrat

e OPL , Ib/h

r=
SV M feedrat

e OPL , lb/h

r= ((100-LVMRE,% ) -100) Ma x SVMER , lb/h

r ((100-SVM RE , %

) -100)

2 0

### Th e LV M calculatio

n applie s t o pumpabl

e LV M an

d tota l LVM , base

d o n th e respectiv

e feedrate s o f pumpabl e an d tota l LV M demonstrate

d during , th e CPT . Th

e U S EP A approve

d thi s extrapolatio

n procedur

e fo rth e LV M an

d SV M feedrat

e OP L in alette

rdate d Augus t29,2003 . 3. 5 Waive

ro f Monitoring m Certai

n Feedstream

s Lubrizo l doe s no tinten d t o perfor m feedstrea

m monitorin

g fornatura

l ga s an d proces s ai rdurin g th e up-comin

g CPT , a s requeste

d i n th e 200 2 CPT pla

n an d approve

d b y U S EP A Regio n 5. Thi s sectio n summarize

s th e justificatio

n o f th e initia l waive rreques t i n 4 0 CF R63.1207(f)(l)(xi ) . an d 63.1209(c)(5

) th e HW C MAC T Standar d require

s documentatio

n o f th e expecte d level s o f th e regulate

d constituent

s i n natura l gas , proces s ai ran d feeastfeam

s fro m vapo rrecover y systems : Th

e WHR I utilize s fue l oil a s th e auxiliar

y fue l Natura l ga s i s onl y utilize d durin g start-u p a s apilo t(se e Sectio n 4.8) . Therefore

, th e natura l ga s discussion

_ i s no tapplicable

. Th e regulate

d constituent

s i n fue l oil ar e determine

d pe rth e Feedstrea m Analysi

s Pla n an d th e feedrat e I s continuousl

y monitored

. Th e contributio

n o f thi s feedstrea m i s include d i n calculatio

n o f th e tota l regulate d constituen

tfeedrat e t o th e WHR I b y th e PLC . Ther e ar e n o feedstream

s from vapo

rrecover y system s associate

d wit h fh e WHRI . Th

e combustio

n ai r(proces s air ) fo rth e uni ti s draw n fro m ambien

tai rnea rth e unit . Sinc e th e WHR I syste m i s operate d , a tles s tha n ambien tpressure

, th e fugitiv e emission

s o f regulate d constituent

s fro m th e uni twill b e negligible

. Additionally

, fugitiv e emission

s from othe

r processin g equipmen

t(tanks , pumps , etc. ) ar e controlle

d pe rRCRA Subpar

tBB . Therefore

, th e feedrat e o f regulate d constituent

s i n th e proces s ai rintroduce

d t o th e WHR I syste m wil l b e considere d negligibl

e a s compare

d t o th e regulate d constituent

s containe

d i n th e wast e an d fue l feedstreams

. 3. 6 Operatio

n o f Wast e Firin g Syste

m I n 4 0 CF R63.1209(j)(4

) th e HW C MAC T Standar d require s tha ta n operato rmus tspecif y operatin g parameter

s an d limit s t o ensur e tha tgoo d operatio

n o f eac h hazardou

s Wast e firin g syste m i s maintaine

d t o ensur e complianc

e wit h th e DR E standards

. Th e require d OPLs pe

r4 0 CFR63.l209(j)(l)-(3)are :

« Minimu

m combustio

n chambe rtemperature

s
• Maximu

m flu e ga s flowrat e
• Maximu

m wast e feedrat e



### 21

### Sectio n 2. 2 Materia l Processin g Area s Ad d provision s fo rth e handlin g o f Leve l 2 container s i n thes e areas . Veoli a manage s container s i n the Materia l Processin g Area s that/excee d th e containe rsiz e limit s fo rLeve l 1 controls
. Th e processin g of Leve l 2 container s a t Veoli a i s identica l t o tha t of Leve l 1 containers : Wast e treatmen t i s no t performe d i n th e Materia l Processin g areas . Leve l 2 container s ar e controlle d accordin g t o th e requirement s a t 4 0 GF R Par t 63 , Subpar t P P "Nationa l Emissio n Standard s fo rContainers; " a s appropriat e fo rLeve l 2 containers
. Metho d 2 1 monitorin g o f Leve l 2 container s i s performe d a s require d t o demonstrat e n o detectabl e emissions
. Pleas e ad d th e Emission s Limitation s an d Standard s a t Sectio n 2.2(A) , Wor k Practic e an d Operationa l Requirement s a t Sectio n 2.2(C) , Monitorin g an d Testin g Requirement s a t Sectio n 2.2(D) , an d Recordkeepin g an d Reportin g requirement s a t Sectio n 2.2(E. ) a s appropriat e fo rmanagemen t o f Leve l 2 container s i n thes e Materia l Processin g Areas
.

### Sectio n 2. 4 Storag e Tank s Modif yMonitorin g an d Testin g sectio n t o reflec t onl ythos e requirement s

- applicabl e t o tanks , whic h ar e no t maintaine d a t les s tha n atmospheri c pressure .

- Non e o f Veolia' s wast e storag e tank s ar e maintaine d belo watmbspheri c pressure . Titl e V Permi t Sectio n 2.4(D)(1 ) contain s a n appropriat e requiremen t fo rannua l testin g o f th e tan k cove ran d al l opening s pursuan t t o Benzen e Wast e Operation s NESHA P 4 0 CF R 61.343(a)(1. ) Followin g th e appropriat e requiremen t i s a n requiremen t derive d fro m 4 0 CF R 61.343(a)( 1 )(C)(3) , whic h reflect s requirement s fo rtank s maintaine d belo watmospheri cpressure . Th e las t sentenc e o f 2.4(D)(1 ) simpl yneed s

. t o b e deleted
.

### Sectio n 2. 9 Insignifican t Activitie s Dru m Samplin g Veoli a propose s tha t emission s fro m dru m samplin g activitie s b e treate d a s insignifican t consisten t with 4 0 CF R 71.5(c)(11 ) an d 3 5 IA C 201.210
. Thi s activit ydoe s no t emi t mor e tha n 2 ton s / yea ro f regulate d ai r. pollutants ^

excludin g HAP , no rdoe s i t emi t an yHA P i n exces s o f 100 0 l b pe ryear . Likewise , i t doe s no t emi t mor e tha n 1. 0 l b / hou rof an y regulate d pollutan t excludin g HAP , no rdoe s i t emi t mor e tha n 0. 1 l b / hou r o f an yHA P i n th e absenc e o f ai rpollutio n contro l equipment
. Th e followin g tex t i s copie d fro m th e Titl e V Permi t Applicatio n (Page s 3 7 ^ 39) discussio n o n the dru m crushin g operation : Accordin g t o previou s TR I report s submitte d b ythe facility , th e majo rregulate d constituent s processe d b yth e facilit ytha t Coul d emi t VO M ar e toluene , methanol , xylen e an d methy l ethy l ketone
. Methano l ha s a muc h highe rvapo rpressur e tha n th e othe rliste d materials
. Fo ra ver yconservativ e estimat e o f VO M emission s fro m dru m crushin g activities , i t wa s assume d tha t methano l residu e wa s the VO M contai n in , an d release d fro m the crushe d drums
. I t wa s als o assume d tha t the n entir e volum e o f th e dru m wa s fille d wit h methano l vapo r Drum s crushe d pe ryea r= 17,00 0 Vapo rpressur e o f methano l a t 20° C = 97.4 8 mmH g = 1.8 8 ps i Molecula rweigh t o f methano l = 32.0 4 Ib/lb-mol e Atmospheri cpressdr e = 14. 7 ps i Densit yo f ai ra t 20° C = 0.074 8 lb/ft 3 

### Molecula rweigh t o f ai r= 28,9 7 Ib/ib-rhoi e Dimension s of a 55-galio n dru m = 2 4 inc h diamete rx3 3 inc h hig h = 2 f t diamete rx2.7 5 ft hig h Volum e o f a 55-gallo n dru m = f l * (radius) 2 

### * heigh t

= 3.14*(1) 2 

### *2.7 5 = 8.635ft 3

### Raoult' s Law : p A= xA* P wher e p A= partia l pressur e o f methano l i n ai r x A= mol e fractio n o f methano l i n ai r P = pressur e 1.8 8 ps i = xA*14.7ps i x A= 0.12 8 = mol e fractio n o f methano l i n ai r lb
. o f ai ri n dru m = 8.63 5 ft 3

### * 0.074 8 lb/ft 3

### = 0.64 6 l b ai r mole s o f ai r= 0.64 6 l b ai r/ 28.9 7 Ib/lb-mo l ai r= 0.022 3 Ib-mo l ai r mol e fractio n o f methano l * Ib-mo l ai r- mole s o f methano l 0.12 8 * 0.022 3 Ib-mo l ai r= 0.0028 5 Ib-mo l methano l 0.0028 5 Ib-mo l methano l * 32.0 4 Ib/lb-mol e methano l = 0.091 4 l b methano l i n dru m Thi s provide s th e basi s fo rdiscussio n o n dru m samplin g emissions ; 0.091 4 f b methano l vapo ri s containe d i n a n empt y5 5 gallo n drum
. I f a n empt ydru m i s fille d wit h 0.091 4 l b methano l vapors , a conservativ e estimat e woul d b e tha t 5 % o f a dru m fille d wit h wast e woul d b e fille d with vapor . I f th e entir e vaporou s conten t o f th e dru m wer e evacuate d durin g th e shor t samplin g time , 0.0045 7 l b o f methano l vapo rwoul d b e emitted
. Not e tha t thi s i s a conservativ e figur e a s man ydrum s o f nori-ha z an d non regulate d waste s ar e sample d whic h woul d no t contai n VOM , Man y drum s sample d ar e les s tha n 5 5 gallon s i n size
. Approximatel yhal f o f th e drum s receive d contai n solids , whic h emi t littl e o rrio vapors . I f 0.0045 7 l b o f methano l i s emitte d wit h ever ydru m sampled , assum e tha t hal f o f tha t i s attribute d t o HA P material ; 0.00228 5 i b HA P pe rdrum
. Veoli a currentl ysample s approximatel y3 0 drum s pe rhour , roughl y3 hour s pe rday , 6 day s pe rweek ; 93 6 hour s / year . 3 0 drum s /

hou r* 0.0045 7 I b methano l / dru m = 0.137 1 I b VO M / hou r 0.137 1 I b VO M /

hou r* 93 6 hour s /

yea r= 12 8 I b VO M /

yea r 3 0 drum s /

hou r* 0.00228 5 I b HA P / dru m = 0.068 6 I b HA P / hou r

V E S 00078 4

### 0.068 6 I b HA P / hou r* 93 6 hour s /

yea r= 6 4 l b HA P /

yea r Th e tim e spen t samplin g i s directl yrelate d t o th e numbe rof samples ; thi s i s t o sa ytha t whe n the wor k loa d i s increased , th e hour s spen t samplin g increases'accordingly
. Th e numbe ro f drum s sample d pe rhourwil l no t fluctuate ; o n th e average , dramatically
. Eve n i f Veoli a sa wa 43 % increas e i n th e samplin g rat e (4 3 drum s / hour ) w e woul d stil l b e belo wthe limit s require d t o b e a n insignifican t activity
. 4 3 drum s /

hou r* 0.0045 7 I b methano l / dru m = 0.19 7 I b VO M / hou r 0.19 7 I b VO M /

hou r* 93 6 hour s /

yea r= 18 4 l b VO M /

yea r 4 3 drum s /

hou r* 0.00228 5 I b HA P / dru m = 0.098 2 i b HA P / hou r 0.098 2 I b HA P /

hou r* 93 6 hour s /

yea r= 9 2 I b HA P /

yea r 4 0 GF R 71.5(c)(11 ) limit s insignifican t activitie s t o 2 TP Yregulate d ai r pollutant
. Eve n i f samplin g th e unlikel y4 3 drums/hour , ther e ar e no t enoug h hour s i n a yea rfo rVeoli a t o excee d the emissio n limit s give n a t 4 0 GFR71.5(c)(11)
. 400 0 l b VO M /

yea r* 1 h r/

0.19 7 I b VO M = 20,30 5 hour s / yea r 100 0 l b HA P /

yea r* 1 h r/

0.098 2 I b HA P = 10,18 3 hour s / yea r Maximu m hour s /

year : 8,73 6

V E S 00078 5

### Sectio n 2. 6 Gasolin e Storag e Tan k 55 0 gallo n Gasolin e Storag e Tan k Veoli a propose s tha t emission s fro m th e 55 0 gallo n gasolin e storag e tan k b e treate d a s insignifican t consisten t wit h 4 0 CF R 71.5(c)(11 ) an d 3 5 IA C • 201.210
. Thi s tan k

doe s no t emi t mor e tha n 2 ton s / yea ro f regulate d ai r "pollutants , excludin g HAP , no rdoe s i t emi t an yHA P i n exces s o f 100 0 l b pe ryear . Likewise , i t doe s no t emi t mor e tha n 1. 0 I b / hou ro f an y regulate d pollutan t excludin g HAP , no rdoe s i t emi t mor e tha n 0. 1 I b / hou r o f an yHA P i n th e absenc e o f ai rpollutio n contro l equipment
. Veoli a operate s on e 55 0 gallo n gasolin e storag e tank
. Historical records indicate that this tank has never had an annual throughput

that exceeded

6,000 gallons;

four of the past 5 years have shown annual throughputs

of less than 5,000 gallons. Eac h year , emission s fro m thi s tan k ar e calculate d usin g th e TANK S softwar e availabl e a t the USEP A website
. Th e versio n mos t recentl yuse d wa s TANK S 4.0.9d
. Th e maximu m annua l gasoline , emission s calculate d b yTANK S fo rthi s specifi c tan k ove rth e pas t 5 year s i s 8 1 lb
. Thi s include s bot h workin g an d breathin g losses
. I n orde rt b approac h th e 2 TP Yregulate d ai rpollutant'limit , Veoii a woul d nee d t o handl e 4 millio n gallon s o f gasolin e i n thi s tan k accordin g t p TANK S calculations
. A t thi s throughput , 3,74 0 I b (1.8 7 T ) o f gasolin e emission s woul d b e release d annually , fh e constituent s o f gasolin e var ysignificantly , bu t resource s agre e tha t toluen e i s th e HA P tha t wil l b e foun d a t th e highes t concentratio n i n gasoline
. Th e mos t conservativ e estimate s indicat e tha t toluen e wil l b e presen t I n gasolin e a t concentration s o f les s tha n 25%
. Again , usin g the annua l throughpu t o f 4 millio n gallons , i f on e quarte ro f th e tota l gasolin e emission s ar e attribute d t o toluene , thi s woul d resul t i n emission s o f 93 5 I b toluen e annually , whic h doe s no t excee d the 1,00 0 I b HA P limit
. Wit h respec t t b th e 1. 0 l b / hou rHmit o n an ynon-HA P pollutant , assum e tha t Veoli a unexplainabl ytriple s the us e o f gasolin e on-sit e an d annua l throughput s becom e 18,00 0 gallons
. Thi s woul d resul t i n annua l gasolin e emission s o f 14 7 l b accordin g t o TANKS
. I f th e entir e year' s emission s wer e t o occu rin

a single week (168 hours) , thi s woul d stil l no t excee d the 1. 0 I b / hou rlimit
.

V E S 00078 6

### Regardin g the : 0. 1 Ib/h rHA P limit , onc e again , us e th e exaggerate d 18,00 0 gallo n throughpu t exampl e wit h toluen e concentratio n bein g 25 % o f th e tota l gasolin e emissions
. Toluen e emission s woul d b e 3 7 I b fo rthe year . I f th e emission s wer e t o occu rin two weeks (33 6 hours ) th e emission s woul d barel yexcee d 0. 1 l b Toluen e pe rhour
. Thes e extremel yexaggerate d scenario s shoul d illustrat e th e fac t tha t i t i s impossibl e fo rVeoli a t o approac h an yo f th e limit s o f a n insignifican t source . Consideratio n o f th e smal l tan k

siz e an d minima l ACTUA L throughput s o f thi s tan k shoul d clearl yqualif yi t a s a n insignifican t source .Uni t # 2 Revise d Run# 1 Date : 09/08/0 8 Tes t Time : 14:3 6 t o 16:46 Ru n Lengt h (minutes ) - 13 0 PP M PP M PP M PP M PP M Wast e Typ e Btu/l b %CWorin e %As h Lea d Cadmiu m Arseni c Berylliu m Chromiu m PC C Hig h Bt u 526 0 1, 3 1.6

3 0.5 8 0. 1 16 0 0.0002 5 1500 PC C Lo wBt u 285 0 0.002 0.66 0.0 3 0.003 0.06 0.0002 5 0,00 6 (Chromiu m Spike ) 0 0 26. 6 0 0 0 0 177000 PC C S p Fd r 800 0.0 1 12. 5 0.005 0.00 1 0.0 1 0.0002 5 0.33 Containerize d Solid s 18 0 0.08 63. 4 313.9 2 196. 2 92.2 1 0.2 5 1177. 2 (Lea d Spike ) 0 0 63. 9 62100 0 0 | 0 0 0 (Chlorin e Spike ) 2 5 89. 8 0. 5 0 0 0 0 0

... . Total s . L i

Chromi c Aci d : Star t Wg t En d Wg t Tota l Wg t Averag e (Batc h CH08H00216 ) L b . L b L b Lb/H r 1124. 8 568 556. 8 25 7
Solids : Numbe r o f Tota l Charge s Averag e P b Spik e CI 2 Spik

e Wast e Charge s Weigh t Pe r Hou r Lb/H r Lb/H r Lb/H r [ Lb/H r 8 3 177

3 38.3 | 81 8 10 0 245 474 2. 6 Ib/ch g 6. 4 Ib/ch g 62.1 % P b 89.8 % CI 2Uni t # 2 Revise d : Ru n # 1 Date : 09/08/08 Tes t Time : 14:36 to 16:4 6 Ru n Lengt h (minutes ) — 13 0 Averag e Therma l Chlorin e As h i Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrat e Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Wast e Typ e (Ib/hr ) (MMBtu/hr) (Ib/hr ) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (lb/hr

) (Ib/hr

) PC C Hig h Bt u 54 9 2.89 7. 1 8. 9 0.0 0 0.00

0 0.088 0.00 0 0,8

2 PC C LowBt u 101 8 2.90 0. 0 6. 7 0.0 0 0.00

0 0.000 0.00 0 0.0

0 (Chromiu m Spike ) 257 0.0 0 0. 0 68. 4 0.0 0 0.00

0 0.000 0.00 0 45,49 PC C S p Fd r 24 4 0.20 0. 0 30. 5 0.0 0 0.000 0.000 0.000 0.0 0 Containerize d Solid s 474 0.0 9 0.4 300. 2 0.1 5 > 0.093 0.04 4 0.00

0 0.5

6 (Lea d Spike ) 10 0 0.00 0. 0 63. 6 61.85 0.000 0.00 0 0.000 0.0 0 (Chlorin e Spike ) 24 5 0.01 220. 2 1. 2 0.00 0:00 0 0.000 0.00 0 0.0

0 ! Total s 288 6 6. 1 228 480 | 62. 0 0.09 0.1 3 0.00 46. 9Uni t # 2 Revise d 

## I Ru n # 2 •I i Date : 09/09/08 l Tes t Time : 12:20 t o 14:30 Ru n Lengt h (minutes ) - 13 0 PP M PP M PP M PP M PP M Wast e Typ e Btu/l b %Chlorin e %As h Lea d Cadmiu m Arseni c Berylliu m Chromiu m 7 I PC C Hig h Bt u 4930 1. 5 1.6

7 0.7

2 0.1 1 16 0 0.00025 140 0 PC C Lo wBt u 176 0 0.00

2 0.0

3 0.0

3 0.00

4 0.0

4 0.00025 0.0025 (Chromiu m Spike ) 0 0 26. 6 0 0 0 0 17700 0 PC C S p Fd r 77 0 0.01 9 9.3 4 0.00

5 0.00 1 0.0 3 0.00025 0.1 2 Containerize d Solid s 320 0.1 6 60. 8 234.96 156.6 4 88.1 1 0.25 949.63 (Lea d Spike ) 0 0 63. 9 621000 0 0 0 0 (Chlorin e Spike ) 2 5 89. 8 0. 5 0 0 0 0 0 1 1 Total s Chromi c Acid : Star t Wg t En d Wg t Tota l Wgt ! Averag e (Batc h CH08H00216) L b L b Lb Lb/H r 1076. 6 522. 9 553. 7 25 6 Solids : Numbe r o f j Tota l Charge s Averag e P b Spik e CI2 Spik

e Waste Charge s ] Weigh t Pe r Hou r Lb/H r Lb/H r Lb/H r Lb/H r 8 5 201 5 39. 2 93 0 102

1 25 1 57 7 

### i ' 2. 6 Ib/ch g 6.4 Ib/ch g 62,1 % P b 89-.8%CI 2Uni t # 2 Revise d Ru n # 2 Date : 09/09/0 8 Tes t Time : 12:2 0 to 14:30 Ru n Lengt h (minutes ) - 13 0 Averag e Therma l Chlorin e As h Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrat e Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Wast e Typ e (Ib/hr ) (MMBtu/hr) (lb/hr ) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) PC C Hig h Bt u •54 9 2.7 1 8.2 9. 2 0.0 0 0.000 0.088 0,000 0.7 7 PC C Lo wBt u 110 3 1.9

4 0; 0 0. 3 0.0 0 0.000 0.000 0.000 0.00 (Chromiu m Spike ) 256 0.00 0. 0 68. 0 . 0.00 0.000 0.000 •0.00 0 45.2 3 PC C S p Fd r 244 0.1 9 0. 0 22. 8 0,0 0 0.000 0.000 0.000 0.00 Containerize d Solid s 57 7 0.1 8 0.9 ! 350. 8 0.1 4 0.090 0.05 1 0.000 0.55 (Lea d Spike ) 10 2 0.00 O.O f 65. 2 63.3 4 0.000 0.00 0 0.00

0 0.00 (Chlorin e Spike ) 25 1 0.0 1 225. 5 1. 3 0.00 0.000 0.000 0.00 0 0.00
Total s 3082 5. 0 235 51 7 63. 5 0.0 9 0.14 | 0.0 0 46. 5Uni t # 2 Revise d Ru n # 3 Date : 09/10/0 8 Tes t Time : 09:44 t o 11:53 Ru n Lengt h (minutes ) — 12 9 PP M PP M PP M PP M PP M Wast e Typ e Btu/l b %Chlorin e %As h Lea d Cadmiu m Arseni c Berylliu m Chromiu m PC C Hig h Bt u 478 0 1. 6 1.0

1 2. 1 0.1 6 240 0.0002 5 63 0 PC C Lo wBt u 148 0 0.002 5 0.01 0.0 3 0.005 0.0 4 0.0002 5 0.002 5 (Chromiu m Spike ) 0 0 26. 6 0 0 0 0 17700 0 PC C S p Fd r 24 0 0.01 6.4 1 0.00 5 0.00

2 0.005 0.0002 5 0.37 Containerize d Solid s 25 0 0. 1 ' 61. 5 234.2 4 165.9 2 87.84 0.25 976 (Lea d Spike ) 0 0 63. 9 621000 0 0 0 0 (Chlorin e Spike ) 25 89. 8 0. 5 0 0 0 0 0
Total s Chromi c Aci d : Star t Wg t En d Wg t Tota l Wg t Averag e (Batc h CH08H00216 ) L b L b L b Lb/H r 1027. 2 465. 6 561. 6 26 1 

### i Solids : Numbe r o f ' Tota l Charge s Averag e P b Spik e CI2 Spik

e Wast e Charge s Weigh t Pe r Hou r Lb/H r Lb/H r Lb/H r Lb/H r 8 4 207 1 39. 1 963 10 2 25 0 61 2 2. 6 Ib/ch g 6. 4 Ib/ch g 62.1 % P b 89.8 % CI2Uni t # 2 Revise d I Ru n # 3 i Date : 09/10/08 Tes t Time : 09:4

4 to 11:5

3 Ru n Lengt h (minutes ) - 12 9 Averag e Therma l Chlorin e As h Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrat e Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Wast e T y p e (Ib/hr ) (MMBtu/hr) (Ib/hr ) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) PC C Hig h Bt u 54 9 2.62 8. 8 5. 5 0.0 0 0.00

0 0.132 0.00 0 0.3

5 PC C Lo wBt u 105 5 1.5

6 0. 0 0. 1 0.0 0 0.00

0 0.000 0.00 0 0.00 (Chromiu m Spike ) I 26 1 0.00 0. 0 69. 5 0.0 0 0.000 0.00 0 0.000 46.2 3 i PC C S p Fd r 234 0.0 6 0. 0 15. 0 0.00 0.000 0.000 0.000 0.00 Containerize d Solid s 61 2 0.1 5 0. 6 376. 2 0.1 4 0.10 1 0.054 0.00 0 0.60 (Lea d Spike ) 10 2 0.0

0 0. 0 64, 9 63.08 0.00 0 0.000 0.00 0 0.00 (Chlorin e Spike ) 250 0.01 224, 5 1. 3 0.00 0.000 0.000 0.000 0.00
Total s 306 2 4. 4 23 4 53

2 63. 2 0.1 0 0.1 9 0,0 0 47. 2Uni t # 2 Revise d Run# 1 Date : 08/11/0

8 Tes t Time : 14:4

0 t o 16:5 0 j Ru n Lengt h (minutes

) — 13 0 / PP M PP M PP M PP M PP M PP M Wast e Typ e Btu/l b |%Chlorin e %As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m PC C Hig h Bt u 131 0 3. 4 6.8 3 0.01 8 1.

4 0. 1 1 2 0.01 5 5.1 PC C Lo wBt u 15 0 0.51 0.1 1 0.006 8 0.0

5 0.0

4 0.5 0.002 5 0.3

9 (Chromiu m Spike

) 0 0 26. 6 0 0 . 0 0 0 18180 0 PCCS p Fd r 35 0 0.03

7 4 0.14

1 0.0

5 0.0

1 0.0

5 0.002

5 0.02

5 Containerize d Solid s 184 0 0.2 6.0

3 5.28

1 947.8 812.4 17.6 0.2 5 5348.3 (Lea d Spike

) 0 0 63. 9 0 62100 0 0 0 0 0 (Chlorin e Spike) 2 5 89. 8 0.5 0 0 0 0 0 0 (Mercur y Spike ) 0 0 0 98 7 0 0 0 0 0
Total s Chromi c Aci d : Star t Wg t En d Wg

t Tota l Wg

t Averag e (Batc h CH08E00643

) Lb Lb L b Lb/H r 1225.6 67

6 549.6 25

4 Solids : Numbe r o f Tota l Charge

s Averag e P b Spik

e H g Spik

e CI 2 Spik e Wast

e Charge s Weigh

t Pe r Hou r Lb/H r Lb/H r Lb/H r Lb/H r Lb/H r 8 6 182

3 39.7 84

1 10

3 1,2

3 23

0 50

7 2.6 Ib/chg 0.031 Ib/chg 5.8 Ib/chg I 62.1 % Pb | 98

7 pp m H g 89.8 % CI 2 jUni t # 2 Revise d | I Ru n # 1 

### I I Date : 08/11/0

8 Tes t Time : 14:4

0 t o 16:5 0 Ru n Lengt h (minutes

) - 13 0 Averag e Therma l Chlorin e As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrat e Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Wast e Typ e (Ib/hr ) (MMBtu/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) PC C Hig h Bt u 50 0 0.6

6 17.0 34.2 0.00001 0.0 0 0.00

0I 0.00

6 0.00

0 0.0

0 PC C Lo wBt u 108 7 0.1 6 5. 5 1.

2 0.00001 0.0

0 0.00

0 0.00

1 0.00

0 0.0

0 (Chromiu m Spike

) 25 4 0.0

0 0.0 67.5 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 46.1 2 PC C S p Fd r 22 5 0.0

8 0. 1 9.0 0.0000 3 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 Containerize d Solid s 50 7 0.9

3 1.

0 30. 6 0.0026

8 0.4

8 0.41 2 0.00 9 0.00

0 2.7

1 (Lead Spike

) 10 3 0.0

0 0.0 65. 9 0.0000 0 64.0

9 0.00

0 0.00

0 0,00

0 0.0

0 (Chlorin e Spike) 23 0 0.0

1 206.7 1.

2 0,0000

0 0,0

0 0,00

0 0.00

0 0.00

0 0.0

0 (Mercur y Spike ) 1.2 3 0.0

0 0.

0 0.0 0.0012 1 0.0 0 0.00

0 0.00

0 0.00

0 0.0

0 Total s 290 7 1.

8 23

0 20

9 0.003

9 64. 6 0.4 1 0.021 0.0 0 48. 8Uni t # 2 Revise d Ru n # 2 Date : 08/12/0

8 Tes t Time : 11:0

5 t o 13:1 6 Ru n Lengt h (minutes) — 13 1

•

i PP M PP M PP M PP M PP M PP M Waste Typ e Btu/l b %Chlorin e %As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m PC C Hig h Bt u 289 0 3. 4 7 0.042 5 1.

3 0. 1 1 1 0.01 5 4. 7 PC C LowBt u 2 5 0. 5 0.0 3 0.001 6 0.0

5 . 0.0.

1 0.2 0.002 5 0.1 2 (Chromiu m Spike) 0 0 26. 6 0 0 0 0 0 18180 0 PC C S p Fd r 84 0 0.00

5 8.4

8 0.00

6 0.0

5 0.01 0.0 5 0.002

5 0.2

2 Containerize d Solid s 169 0 0.3

3 6.0

1 4.871 960. 4 754. 6 9.60 4 0.2

5 5350. 8 (Lea d Spike) 0 0 63. 9 0 62100 0 0 0 0 0 (Chlorin e Spike) 2 5 89. 8 0.5 0 0 0 0 0 0 (Mercur y Spike) 0 0 0 66 7 0 0 0 0 , 0
Total s Chromi c Aci d : Star t Wg t En d Wg

t Tota l Wg

t Averag e (Batc h CH08E00643) L b Lb Lb Lb/H r 812. 9 252. 8 560. 1 25 7 Solids : Number o f Tota l Charges Averag e P b Spik e H g Spik

e CI 2 Spik e Wast

e Charges Weight Pe r Hou r Lb/H r Lb/H r Lb/H r Lb/H r Lb/H r 8 6 180

6 39. 4 82

7 10

2 1.2

2 228 49 5 2. 6 Ib/ch g 0.031 Ib/chg 5.8 Ib/ch g 62.1 % P b 66

7 ppm H g 89.8

% CI 2Uni t # 2 Revise d Ru n # 2 Date : 08/12/0

8 Tes t Time : 11:0

5 t o 13:1 6 Ru n Lengt h (minutes

) - 13 1 Averag e Therma l Chlorin e As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrate Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Waste Typ e (Ib/hr ) (MMBtu/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) PC C Hig h Bt u 49 9 1.4

4 17.0 34. 9 0.0000 2 0.0

0 0.00

0 0.00

5 0.00

0 0.0

0 PC C LowBt u 101 0 0.0 3 5. 1 0.3 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 0,0

0 (Chromiu m Spike) 25 7 0.0

0 0.0 68. 2 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 46.6

4 PC C S p Fd r 21 2 0.1 8 0.0 18.0 0.0000 0 0.0

0 ' 0.00

0 0.00

0 0.00

0 0.0

0 Containerize d Solid s 49 5 0.8

4 1.

6 29. 8 0.00241 0.4 8 0.37

4 0.00

5 0.00

0 2.6

5 (Lea d Spike

) 10 2 0.0

0 0. 0 65. 4 0.0000 0 63.60 0.00 0 0.00

0 0,00

0 0.0

0 (Chlorin e Spike) 22 8 0.0

1 205. 2 1.

1 0.0000

0 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 (Mercur y Spike ) 1.2 2 0.0

0 0. 0 0.0 0.00081 0.0 0 0.00

0 0.00

0 0.00

0 0.0

0 i Total s 280 5 2.5 229 | 21 8 0.003 3 64. 1 0.3 7 0.01 ] 0.00 | 49. 3



### VE S 00079 7Uni t # 2 Revise d ! Ru n # 3 i . .. . Date : 08/13/0

8 Tes t Time : 10:3

9 to 12:4 7 I Ru n Lengt h (minutes

) — 12 8 PP M PP M PP M PP M PP M PP M Waste Typ e Btu/l b %Chlorin e %As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m PC C Hig h Bt u 164 0 3.

2 6.5

4 0.0

4 1.

1 0. 1 1 7 0.01 5 4. 1 PC C LowBt u 200 0 0.4

6 0.0

9 0.001 5 0. 1 0.0 2 0.

2 0.00

5 0.0

5 (Chromiu m Spike) 0 0 26. 6 0 0 | 0 0 0 . 18180 0 PC C S p Fd r 2 5 0.00

5 9.0

5 0.009

2 0.0

5 0.0

1 0.0

5 0.002

5 0.1 8 Containerize d Solid s 148 0 0.1 7 6.6 2 4.8

6 84

0 72

0 9 0.2 5 516

0 (Lea d Spike) 0 0 63. 9 0 62100 0 0 0 0 0 (Chlorin e Spike) 2 5 89.8 .0. 5 0 0 0 0 0 0 (Mercur y Spike) 0 0 0 54 8 0 0 0 0 0 Total s Chromi c Acid : Star t Wg t En d Wg

t Tota l Wg

t Averag e (Batc h CH08E00643

) L

b Lb L b Lb/H r 725. 4 188.2 537.2 25 2 

### I Solids : Number o f Tota l Charge

s Averag e Pb Spik

e H g Spik

e CI 2 Spik e Wast

e Charge s Weigh

t Pe r Hou r Lb/H r Lb/H r Lb/H r Lb/H r Lb/H r 8 2 173

4 38. 4 81 3 10 0 1.1 9 223 48 9 2.6 Ib/chg 0.031 Ib/chg 5.8 Ib/ch g 62.1 % Pb 54

8 pp m H g 89.8

% CI 2Uni t # 2 Revise d Ru n # 3 Date : 08/13/0

8 f Tes t Time : 10:3

9 to 12:4

7 Ru n Lengt h (minutes

) - 12 8 Averag e Therma l Chlorin e As h Mercur y Lea d Cadmiu m Arseni c Berylliu m Chromiu m Feedrat e Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Loadin g Waste Typ e (Ib/hr ) (MMBtu/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (lb/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) (Ib/hr

) PC C Hig h Bt u 50 0 0.8

2 16.

0 32. 7 0.0000

2 0.0

0 0.00

0 0.00

9 0.00

0 0.0

0 PC C LowBt u 103 3 2.0

7 4.8 •0. 9 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 (Chromiu m Spike

) 25 2 0.0

0 0. 0 67. 0 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 45.7

8 PC C S p Fd r 20 8 0.0

1 0.0 18.8 0.0000 0 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 Containerize d Solid s 48 9 0.7

2 0.

8 32. 4 0.0023

8 0.41 0.35

2 0.00

4 0:00

0 .2.5

2 (Lead Spike

) 10 0 0.0

0 0.0 63. 9 0.0000 0 62.0

6 0.00

0 0.00

0 0.00

0 0.0

0 (Chlorin e Spike

) 22 3 0.0

1 200.2 1.

1 0.0000

0 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 (Mercur y Spike) 1.1 9 0.0 0 0. 0 0.0 0.0006 5 0.0

0 0.00

0 0.00

0 0.00

0 0.0

0 I Total s 280 6 3.6 22 2 21 7 0.0031 62. 5 0.3 5 0.01 1 0.0

0 48. 3

V E S 00079 9

### Uni t 2 Operatin g Paramete r [Revised ]

Limit s Se t Durin g Augus t an d September , 200

8 Testin g August , 200 8 — Ru n 1 Ru n 2 Ru n 3 Averag e — Mercur yFee d (Lb/hr

) 0.003 9 0.003 3 0.003 1 0.003 4 (Ave
. o f tes t ru n ave.'s )
September , 200 8 Ru n 1 Ru n 2 Ru n 3 Averag e Baghous e Inle t Temp
. (De g F ) 41 9 42 0 42 0 42 0 (Ave
. of tes t ru n ave.'s ) Stackflo w(ACFM ) 1519 6 1512 0 1512 4 1514 7 (Ave
. o f max . HRA' s o f eac h tes t run ) Pumpabl e LV M Fee d (Lb/hr ) 4 6 4 6 4 7 4 6 (Ave
. o f tes t ru n ave.'s ) Tota l LV M Fee d (Lb/hr ) 4 7 4 7 4 7 4 7 (Ave
. o f tes t ru n ave.'s ) SV M Fee d (Lb

/hr) 6 2 6 4 6 3 6 3 (Ave
. o f tes t ru n ave.'s ) Chlorin e Fee d (Lb/hr

) 22 8 23 5 23 4 23 2 (Ave
. of tes t ru n ave.'s )



### V E S 00080 0Recalculate d Meta l Concentration s i n Soli d Waste s 200 8 Metal s Emissio n Testin g 

### ff. A i . . Uni t 2 Reporte d Metal s Concentratio n o f Soli d Wast

e Feed s Dat e Run * Arseni c Berylliu m Chromiu m Lea d Cadmiu m Mercur y Moisture Soli d (ppm) (ppm ) (ppm ) (ppm) (Ppm ) (ppm) (% ) (%

) 8/11/200 8 1 2 6 0.2 5 790 0 140 0 120 0 7. 8 32. 3 67. 7 8/12/200 8 2 1 4 0.2 5 780 0 140 0 110 0 7. 1 31. 4 68. 6 8/13/200 8 3 1 5 ' 0.2 5 860 0 140 0 120 0 8. 1 4 0 6 0 A s Receive d Metal s Concentratio n o f Soli d Wast

e Feed s Dat e Run # Arseni c Berylliu m Chromiu m Lea d Cadmiu m Mercur y (ppm ) (ppm ) (PPm) (ppm) (PPm ) (ppm ) 8/11/200 8 1 17.60 2 0.2 5 0.2 5 0.2 5 5348, 3 947. 8 812. 4 5.280 6 1/ 2 detectio n limi t 8/12/200 8 2 9.60 4 0.2 5 0.2 5 0.2 5 5350. 8 960. 4 754. 6 4.870 6 8/13/200 8 3 9 0.2 5 0.2 5 0.2 5 516 0 84 0 72 0 4.B 6

. . . Reporte d Metal s Concentratio n of Soli d Wast e Feed s Dat e Run # Arseni c Berylliu m Chromiu m Lea d Cadmiu m Mercur y Moisture Soli d (ppm) (ppm ) (ppm) (ppm) (ppm) (ppm ) (% ) (%

) 9/8/200 8 1 9 4 0.2 5 120 0 32 0 20 0 N A 1. 9 98. 1 9/9/200 8 2 9 0 0.2 5 97 0 24 0 16 0 N A 2. 1 97. 9 9/10/200 8 3 9 0 0.2 5 100 0 24 0 17 0 N A 2. 4 97. 6

_ A s Receive d Metal s Concentratio n o f Soli d Wast

e Feed s Dat e Run # Arseni c Berylliu m Chromiu m Lea d Cadmiu m Mercur y (ppm) (ppm ) (ppm) (ppm) (ppm) (ppm ) 9/8/200 8 1 92.21 4 0.2 5 1177. 2 313.9 2 | 196. 2 N A 1/ 2 detectio n limi t 9/9/200 8 2 88.1 1 0.2 5 949.6 3 234.9 6 156.6 4 N A I 9/10/200 8 3 87.8 4 0.2 5 97 6 234.2 4 165.9 2 N A 

## I

V E S 00080 1Notificatio n o f Complianc e (NOC ) Repor t Veoli a E S Technica l Solutions , L.L.C . hereb y submit s th e Notificatio n of

Complianc e (NOC ) Repor t i n complianc e wit h 4 0 CF R 63.1210(b ) an d 4 0 CF R 63.1207Q) Applicabl e Rule : 4 0 CF R Par t 63.1200 , Subpar

t EE E —Nationa l Emissio n Standard s fo r Hazardou s Ai rPollutant s fo rHazardou s Wast e Combustors
. Thi s NO C i s bein g mad e i n accordanc e wit h §63.9(h)
. SECTIO N I GENERA L INFORMATIO N A
. I f yo u hav e bee n issue d a Titl e V permit , d o not complet e thi s form
. Submi t you rNO C i n accordanc e wit h you rTitl e V permit
. [§63.9(h)(3) ] B
. If yo u hav e no t bee n issue d a Titl e V permit , complet e th e remainin g portion s o f thi s sectio n an d als o complet e Section s ll-IX
. [§63.9(h)(2)(i) ] C
. Prin t o rtyp e th e followin g informatio n fo reach , facilityfo rwhic h yo u ar e makin g notificatio n o f complianc e status : Operatin g Permi

t Numbe r (OPTIONAL

) Facilit y I.D. Number (OPTIONAL ) 

## V-IL-1716300103-08-0 1 ILD09864242 4 Responsibl e Official' s Name/Titl e 

## Dou q Harri s Stree t Addres s 

## # 7 Mobil e Ave
. Cit y Stat e ZI P Cod e 

## Sauge t 62201-106 9 Facilit y Nam e (i

f different from Responsibl e Official' s Name ) 

## VeoliaJE S Technica l Solutions , L.L.C
. Facilit y Stree t Addres s (I

f different tha n Responsibl e Official' s Stree t Address

) Facilit y Loca l Contac

t Name Titl e • \ Phon e (OPTIONAL ) 

## Dou g Harri s Genera l Manage r 618-271-280 4 Cit y Stat e ZlPCod e . 

## Sauge t I L * 62201-106 9 D.. : Indicate th e relevan t standar d o r othe r requiremen t tha t i s th e basi s fo r thi s notificatio n an d th e source' s complianc e date : (§63 .9 (b)(2)(iii) ) Basi s fo r thi s notificatio n (relevant standar d o r other requirement

) Complianc

e Dat e (mm/dd/yy

) 

## 40 CF R 63.120 0 0B& 

## Jun e 30 , 2004

1SECTIO N I I CERTIFICATIO N (Note: you may edit the text in this section as deemed appropriate) Base d upo n informatio n an d belie f forme d afte ra reasonabl e inquiry , I , a s a responsibl e officia l o f th e above-mentione d facility , certifyth e informatio n containe d i n thi s repor t i s accurat e an d tru e t o th e bes t o

f m yknowledge
. Th e above-mentione d facilit yha s complie d wit h th e relevan t standar d o rari d othe rapplicabl e requirement s reference d i n th e relevan t standard
. [§63.9(h)(2)(i)(G) ] Nam e o f Responsibl e Officia l (Prin t or Type ) Titl e Dat e (mm/dd/yy

) 

## Dou g Harri s Genera l Manage r 10/10/200 8 Signatur e o t Responsibl e Officia l ponstbl l , ^
_
SECTIO N III Describ e th e method s yo u use d t o determin e compliance
. [§63.9(h)(2)(i)(A) ] RCR ATria l Bur n Dat a fro m EP Aapprove d testin g a s require d byth e RCR APar t B permi t an d testin g conducte d prio rt o th e complianc e dat e usin g al l approve d EP Amethod s wa s use d t o demonstrat e complianc e wit h al l applicabl e emissio n standard s define d i n 4 0 CF R 6 3 1203
. I n addition , Performanc e Testin g approve d b yUSEPA , Regio q 5 o n Augus t 8 , 200 8 an d conducte d i n Augus t an d Septembe ro f 200 8 Se e th e attache d Operatin g Parameter s Table s an d HW C MAC TEmissio n Standard s fabl e fo rUnit s 2/ 3 an d Uni t 4 , that defin e th e operatin g parameter s establishe d dutm g testin g tha t ensure s complianc e wit h th e performanc e standard s : . SECTIO N I

V Describ e th e result s of an yperformanc e tests , opacityd rvisibl e emissio n observations , continuou s monitorin g syste m (CMS ) performanc e evaluations , and/o rothe rmonitorin g procedure s o rmethod s that wer e conducted
. r §63.9(h)(2)(i)(B) ] Se e attache d tes t result s tha t wer e tile d t o develo p fhe/limit s define d i n th e Operatin g Paramete rTable s reference d i n Sectib n Jl l of thi s repor t Thes e result s als o includ e monitorin g method s an d procedure s Als o attache d ar e th e Facility' s Continuou s Emission s Monitorin g Syste m QualityAssuranc e Pla n an d Continuou s Monitorin g Syste m Qualit yGontrd l Progra m , , . SECTIO N V Describ e tfi e method s yo u wil l us e t o determin e continuou s compliance , includin g a descriptio n o f monitorin g an d reportin g requirement s an d tes t methods
. [§63.9(h)(2)(i)(C) j Continuou s complianc e i s base d o n th e operatin g paramete rlimit s establishe d fro m complianc e testing , tiefined i n th e attache d Operatin g Parameter s Tabl e reference d i n Sectio n 11 1 o f thi s report
. Thes e incinerato roperatin g parameters^aremonitore d continuousl yt o verifycomplianc e bya proces s monitorin g an d contro l syste m Th e detail s o f thes e system s ar e define d i n detai l i n Sectio n 2 0 , Incinerato rProces s descriptio n reference d m Sectio n VII I of thi s repor t an d attache d

2 

### VE S 00080 3SECTIO N V I Describ e th e typ e an d quantityo f hazardou s ai rpollutant s (HAP ) emitte d b yth e sourc e (o r surrogat e pollutant s i f specifie d i n th e relevan t standard) , reporte d i n unit s an d averagin g time s an d i n accordanc e wit h th e tes t method s specifie d i n th e relevan t standard
. [§63.9(h)(2)(i)(D) ] Se e attache d tes t results f rbm'c^ that wa s conducte d t o demonstrat e complianc e wit h th e HAP' s ari d otfre rpollutant s define d in ; Subpar t EEE
. ;.„.^ : SECTIO N VI I I f th e relevan t standar d applie s t p bot h majo ran d are a sources , presen t a n analysi s demonstratin g whethe rth e affecte d sourc e i s a majo rsourc e (usin g th e emission s dat a generate d fp rthi s notification
. [§63.9(h)(2)(i)(E) ] Thi s facilit yis 1 a majo rsourc e du e to it s applicabilit yt o th e NESHA P regulations , specificall ySubpart EE E an d Subpar t .DD
. Regardles s o f the
. facility' s emissio n concentrations , thi s facilityi s a majo rsourc e b y definition
. SECTIO N VII I Describ e th e ai rpollutio n contro l equipmen t (o rmethod ) fo reac h emissio n point , includin g eac h control devic e (o rmethod ) fo reac h hazardou s ai rpollutan t an d th e contro l efficienc y(percent ) fo r eac h contrp l devic e (o rmethod) , [§63.9(h)(2)(i)(F) J Se e attache d Sectio n 2 0 , Incinerato rProces s Descriptio n fro m 2D0 8 Performanc e Tes t Plan s fo r Incinerator s 2 , 3 an d 4 tha t describe s th e ai rpollutio n contro l equipmen t fo reac h emissio n poin t Also , se e attache d th e complianc e testin g dat a define d m Sectio n I V o f thi s repor

t tha t detail s th e contro l efficienc yfo reac h contro l devic e , . . . SECTIO N I

X A
. Di d yo u submi t a n applicatio n fo rconstructio n o rreconstructio n unde r§63.5(d ) that containe d preliminaryo restimate d data ? £§63.9(h)(5) ] •Ye s L
. . /Not "
. , . No t applicabl e I
. (di d no t submi t a n applicatio n fo rconstructio n o r reconstruction)
. B
. :"i f yb u answere d yes , provid e actua l emissio n dat a o rothe rcorrecte d informatio n below
.

EN D O F FORM . A Responsible Official must sign this form - See Sectio n II .

# HW C MAC T Emissio n Standards

Paramete

rUnit s Dioxin/Fura

n (D/F) ng/dsc m TE Q
Mercur y (Hg ) * ug/dsc m Semivolatil

e Metal s (SVM ) ug/dsc m Cadmium, Lea

d * Low Volatile Metal

s (LVM ) ug/dsc m Arsenic, Beryllium , Chromiu m * Carbo n Monoxid

e (CO ) ppm v Hydroge n CMoride/CMorm

e ppm v (HC1/C12

) -i.-articulat

e mg/dsc m Standar

d Metho

d o f Complianc

e 0.2 0 Operatin g Paramete

r Limit s 13 0 Operatin g Paramete

r Limit s 24 0 Operatin g Paramete

r Limit s 9 7 Operatin g Paramete

r Limit s 10 0 Continuou s Emission

s Monito r 7 7 Operatin g Paramete

r Limit s 3 4 Operatin g Paramete

r Limit sUNIT S 2/ 3 OPERATIN G PARAMETER S

Operatin g Paramete

r Unit

s Limit

s Tes

tDat e Performanc

e Standard s Maximu m Tota l Pumpabl

e Lb/h

r312

3 Wast e (Hourl y Rollin g Total ) Maximu m Tota l Hazardou

s Lb/h

r430

1 Wast e (Hourl y Rollin g Total ) Maximu m Stac k Ga s Flo w Acf

m 15,14

7 Rat e (Hourl y Rollin g Average

) Mmimu m Primar y Combustio

n De

g F 171

2 Chambe rTemperatur

e (Hourl y Rollin g Average

) Minimum,Secondar

y Combustio

n Deg

F 184

5 Chambe rTemperatur

e (Hourl y Rollin g Average

) Maximu m Baghous

e Inle tDe

g F 42

0 Temperatur

e (Hourl y Rollin g ..Average ) •-Miax . Pump . Lo w Volatil e Metal s Lb/h

r4

6 Feedrat e (1 2 Hou rRollin g Total ) Max . Tota l Lo w Volatil e Metal s Lb/h

r4

7 Feedrat e (1 2 Hou rRollm g Total ) Maximu m Sem i Volatil e Metal s Lb/h

r6

3 Feedrat e (1 2 Hou rRollin g Total ) Maximu m Mercur

y Feedrat e Lb/h

r0.004

7 (1 2 Hou rRollingTotal

) Maximu m Chlorin

e Feedrat e Lb/h

r22

9 (1 2 Hou rRollin g Total ) V Maximu m As h Feedrat e (1 2 Lb/h

r67

3 Hou rRollin g Total ) Minimu m Sorben tFeedrat e Lb/l

b Cl ? 1.7

6 (Hourl y Rollm g Average

) Minimu m Carrie rFlui d Flowrat e Gal/l

b Cl 21.7

0 (Hourl y Rollin g Average

) May , 200 4 May , 200 4 Sept. , 200 8
May , 200 4
Nov. , 199 6 Aug. , 200 8 Sept. , 200 8 Sept. ; 200

8 Sept. , 200 8 Aug. , 200 8 Aug. , 200

8 Nov., 199 6 Nov., 199 6 Nov; , 199 6 DRE , D/

F DRE , D/ F DRE , D/F , Part. , SVM , LV M DRE , D/ F
DRE , D/ F
D/F , SVM , LV M LV M LV M SV M H g SVM , LV M HCI/C1 2 Part . HC1/C1 2 HC1/C1 2



### VE S 00080 6UNI T 4 OPERATIN G PARAMETER S

Operatin g Paramete

r Unit

s Limit

s Tes

tDat e Performanc

e Standard s Maximu m Tota l Pumpabl e Lb/b

r Wast e (Hourl y Rollin g Total ) Maximu m Tota l Hazardou

s Lb/h

r Wast e (Hourl y Rollin g Total ) Maximu m Stac k Ga s Flo w Acf

m Rat e (Hourl y Rollin g Average ) Minimu m Primar y Combustio

n De

g F Chambe rTemperatur

e (Hourl y Rollin g Average ) Minimu m Secondar

y Combustio

n De g F Chambe rTemperatur

e (Hourl y Rollin g Average ) Maximu m Baghous

e Inle tDe

g F Temperatur

e (Hourl y Rollin g erage ) "Max . Pump . Lo w Volatil e Metal s Lb/h

r Feedrat e (1 2 Hou rRollin g Total ) Max , Tota l Lo w Volatil e Metal s Lb/h

r Feedrat e (1 2 Hou rRollin g Total ) Maximu m Sem i Volatil e Metal s Lb/h

r Feedrat e (1 2 Hou rRollin g Total ) Maximu m Mercur y Fee d rat e Lb/h

r (1 2 Hou rRollin g Total ) Maximu m Chlorin e Fee d rat e Lb/h

r (1 2 Hou rRollin g Total ) Maximu m As h Fee d Rat e (1 2 Lb/h

r Hou rRollin g Total ) Carbo n Ejectio n Feedrat e Lb/h

r (Hourl y Rollin g Average ) PC C - 325 6 SC C -100 6 PC C -13,79 6 SC C -100 6 38,08 6
150 7
188 6
43 4
4 7 5 5 6 5 0.03 1 25 2 877 7 6: 2 Sept

, 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Aug. , 200 8 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Aug. , 200 8 Dec , 199 5 Aug, 200 8 DRE

, D/ F DRE , D/ F DRE , D/F, Part , SVM , LV M DRE , D/ F
DRE , D/ F
D/F , SVM , LV M LV M LV M SV M H g SVM , LVM , HC1/C1 2 Part . D/F , H g
Minimu m Sorben tFeedrat e (Hourl y Rollin g Average ) Minimu m Carrie rpljii d Flowrat e (Hourl y Rollin g Average ) Lb/l

b Cl 2 Gal/l b Cl 2 1.0

1 1.6 1 Dec

, 199 5 Dec , 199 5 HC1/C1

2 HC1/C1 2

# UNI T 2 EMISSIO N RESULT S

c

(

V E S 00080 8Tabl e 3- 3 R M 2 9 Samplin g Parameter s an d Emissio n Result s - Wee k o f Augus t 11 , 

# ENS R

200 8
Ru n No . I 1
_ 2 ) 3 Dat e j r It-AmSS ' t2-Aug-0

3 f t3-Ai/g-0

8 Star t Time "Unit s f 14:4

0

r16:5 0 " ' '11.0 5 ^'13 T 1 6 f 10.3

9 Stop Tim e f 14:4 0

r16:5 0 " ' '11.0 5 ^'13 T 1 6 "ri? : 4 7 AVG S Samplin g Parameter

s — Barometri c Pressur

e in . H g r29

^ 6 0 29.5

5 f 29.5

0 29.6 1 Volume Metere

d de

f f 83'65

0 " 86.04

4 " ' 8

5 61 1 '81J99 6 Sample Volum

e dsc

f \ 7 6 /5 0 8

0 23 3 ]' 78.03

6 78.34

0

...... . Moisture l 0 2 a t Stac k % y/\ T % dr y T 1 1 7

2 ' 40.1" "

711.5 4 "." I III!!.. ' 

### J 11.3 0 11.5

2 Avg . Stac k

Temp . .36 9 f 37

0 r35

8 36

5 Stac k Flowrat e dscfm I 5,49 5 5,57

2 T " 5,35

7 5 ,47

5 Isokinetic s % ? 9 3 "9

6 i 9

7 9

5 Mercun'(Ha ) — pg . ug/m 3 83.5 " \ 89.4 "T_"87.9' Z 87. 0 Stac k Con e @ 7

% 0

7 pg . ug/m 3 

# f

58.0 58. 2 "] ' 57. 4 ' 67. 9 Stac k Emissio n Rat

e Vlb/li r ' g/se c ; y.9TF r0 4 ^ i'a.96E-0 5 8.22 E 0

4 104E-04 7.99I.-0

4 ; 1 01E-0

4 ' 8.04E-0

4 "VotL-0 4 Tota l Chromiu m (Cr)

H LV M ; Quantit y Collecte

d jjg„_„ . | 78.7 5 75.6

6 

# XLZIJI X " 75.8 5 Stac k Cone . @ 7

% 0

2 ug/m 3 1 54.6

6 [ 49.28 47*7 6 " 50.5

7 Stac k Emissio n Rat

e Ib/h r 7.46E-0 4 'o.95h.0 4 j 6.64E-0 4 '7.02E-O 4 j g/sec 1 9.40E-0 5 i 8.76E-0

5 ! 8.37E-0

5 '>784E -u 5 Cadmiu m (Cd) — SV M \ Quantit y Collecte

d j 1.9 9 2.0 6 

# .'. " 

# X jJi . ' r '~i-?l'. ! Stac k Cone . @7%0 2 •Stac k Emissio n Rat

e ug/m 3 ' Jr5h r ' j 1.3

8 ':1.88E-0 5 1.3

4 1.89f;-0 5 T ^'2 1

r 'L68L -6 5 ' 1.3

1

r " l .82E : 0 5 ~ T l g/sec ;2.37E0 6 2.38 E 0 6 " " " 1 2 ;i?F:-0 6 iLead (PM - SV M

r35 6 0 8 fQuantir y Collecte

d £ 9 " j 3?9. 5 ' 36 9 2 '369. 5 ' r35 6 0 8 IStackConc . @7%O s ug/m 3 ! 228.7 240.5 : 241.3 " 236. 8 Stac k Emissio n Rat

e Ib/h r 3.12E-0 3 j 3.3G E 0 3 r 3.29E-0 3

r AML-QA " • T ' " " ' " ' i g/sec 0 4 ''L23K-04 ' r 3.29E-0 3

r AML-QA Arseni c (As)

— Quantit y Collecte

d m. 10.0 8 Stac k Cone . @ 7

% 0 2 pg/m 3 11.8 0 6.5

7 

# f

3/ 0 r " 7.3

6 Stac k Emissio n Rat

e lb/h r 1.61E-0 4 i 9.26E-0

5 ' 1.02E-0 4 g/se c 2.03E-0

5 1.17E-0

5 16~49E-u 6 r 'f.28E -d 5 Berylliu m (Be

) — Quantit y Collecte

d jjg.. . 0.2 0 0.20 j 0.2 0 

# XPJIL X Stack Cone . @ 7

% 0? Stac k Emissio n Rat

e pg/rr r Jb/h r g/se c j 0.1 4

: i.89i : ;-« i

: 2 39E-0 7 0.1 3 1.84H-0 6 2 .32fc

; -0 7 ' 1 0.1 3 j 1.82E-0 6 ' 2 29E-07' " 0.1 3

r i85E-0 6 ' 2.33F-0

7 LVM ! Total. = ug/m 3 j i 58. 0 I 51. S 53. 8 SV M Tota

f = pg/rr

f j 230. 1 : 241 8 242.5 238. 1

C:\DOCUME-1\Marich.TVViU.OCALS--1\Temp\notesD3055 0 3- 4 Octobe r 200 B Weoli a Repor t Uni t 2 final-do c 

### VE S 00080 9

# ENS R

Tabl e 3- 4 Summar yo f HW C MAC TMetal s - Augus t 11,200 8
Lo wVolatil e Metal s Emission s -ug/m 3 @7 % 0 2 Metal s Ru n 1 Ru n 2 Ru n 3 Averag e A s 11.6 0 6.5 7 3.7 0 B e 0.1 4
. 0.1 3 0.1 3 C r 54. 7 49. 3 47. 8 Tota l LV M 66. 6 56. 0 51. 6 58. 1

LV M Regulator

yStandard = 9 7 ug/m 3 Semi-Volatil e Meta l Emission s • VQlm* @ 7 % 0 2 Metal s Ri m 1 Ru n 2 Ru n 3 1 Averag e P b 22 9 24 0 24 1 C d 1.3

8 1.3

4 1.2 1 Tota l SV M 23 0 24 2 24 2 23 8

SV M Regulator

yStandard = 24 0 ug/m 3 I Mercur y Emission s -|jgfm 3 (g > 7 % 0 2 Ru n 1 Ru n 2 Ru n 3 Averag e 58. 0 58. 2 57. 4 57. 9 Mercur yRegulator

yStandard = 130 ug/m 3

C:\DOCUME-1\Warich.TWI\LOCALS-1\Temp\natesD3055 0 Weoli a Report Uni t 2 final.doc 3- 5 Octobe r 200 8 

### VE S 00081 0

# ENS R Tabl e 3- 5 R M 2 9 Samplin g Parameter s an d Emissio n Result s - Wee k o f Septembe r8 , 200 8
Ru n No
. Date Star t Tim e Slop^Tim e Unit s 1

r 08-Sep-0 8
r14:3 6

r16:4 6 2

r 09-Sep-0 8
r12:2 0

r14:3 0 3

r 10-Sep-0 8
r09:44

r11:5 3 AVG S Samplin g Parameter

s — Barometri cPressur e Volum e Metere d Sampl e Volum e Moistur e 0 2 a t Stac k Avg
. Stac k

Temp
. Stac k Flowrate Isokinetic s in
. H g de f dsc f % v/ v % dr y T dscf m % r29.6 0

r77.38 2 75.29 6 41. 4

r11.2 1

r38 5 4,69 8 107 r29.7 5

r79.26 9 78.40 7 41. 2

r10.9 1 " 38 1 5,09 9 103 r29.7 2

r78.90 5 78.65 4 41. 3

r11.3 5

r38 4 524 8 100 ' 29.7 1 " 77.05 9 • 77.45 2 41. 5 711.1 6 ' 38 3 5,01 5 10 4 Tota l Cliromiumt'Cr ) - Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e LV M

pg ug/m 3 Ib/h r g/se c 12.1 6

8.1 6 1 .OOE-0 4 1.26E-0 5 2.7 9

1.7 4 2.40E-0 5 3.02E-0 6 9.1 8

5.9 8 8.10E-0 5 1.02E-0 5 ' 8.04

5.2 9

r 6.85E-0 5 ' 8.63E-0 6 Cadmiu m (Cd ) — Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e SV M

u g ug/m 3 Ib/h r g/se c 2.7 3

1.83 2.25E-0 5 2.83E-0 6 2.7 4

1.7 1 2.35E-0 5 2.96E-0 6 2.2 0

. 1.4 3 1.94E-0 5 2.44E-0 6 " 2.5 5

1.6 6 '2.18E-D 5

r 2.75E-0 6 LeadfPVt Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e SV M

M 9 ug/m 3 Ib/h r g/se c 45. E

30. 6 3.76E-0 4 4.74E-0 5 13. 9

8. 7 1.20E-04 1.5 1 E-0 5 39. 0

25. 4 3.45E-0 4 4.34E-0 5 ' 32.8 4

21. 6

r 2.80E-0 4 " 3.53E-0 5 Arseni c(As)

- Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e M

S ug/m 3 Ib/h r g/sec 2.8 0

1.8 8 2.3 1 E-0 5 2.9 1 E-0 6
. 2.1 0

1.3 1 1.8 1 E-0 5 2.28E-0 6 2.1 0

1.3 7 1.85E-0 5 2.34E-0 6 " 2.3 3
71.5 2 "1.99E-G 5 "2.5 1 E-0 6 Berylliu m (Be) — Quantit yCollecte d Stac k Cone
. @7 % 0 2 Stac k Emissio n Rat e M

S ug/m a Ib/h r g/se c 0.2 0

0.1 3 1.65E-0 6 2.08E-0 7 0.2 0

0.1 2 1.72E-0 6 2.17E-0 7 0.2 0

0.1 3 1.77E-0 6 2.22E-0 7 70.2 0

0.1 3 '1.7 1 E-0 6 '2.16E-0 7 LV M Tota l = ug/m 3 10. 2 3. 2 7. 5 6. 9 SV M Tota l = pg/m 3 32. 4 10. 4 26. 9 23. 2

C:\DOCUME-1\l<larich.TWI\LOCALS-1\Temp\notesD3055 0 3- 6 October200 8 Weoli a Report Uni t 2 final.do c 

### VE S 00081 1

# ENS R Tabl e 3- 6 Summar yo f HW C MAC TMetal s - Septembe r8,200 8 

### Lo wVolatil e Metal s Emission s •|ig/m 3 

### @ 7%0 2 Metal s Ri m 

### 1 Ru n 2 Ru n 3 Averag e A s . 1.8 8 1.3 1 1.3 7 B e 0.1 3 0.1 2 0.1 3 C r 8. 2 1. 7 6. 0 Tota l LV M 10. 2 3. 2 7. 5 6. 9

LV M Regulator

yStandard = 9 2 ug/m 3 

### Semi-Volatil e Meta l Emission s -ugfm 3 

### @7 % Q 2 Metal s Ru n 

### 1 Ru n 2 Ru n 3 Averag e P b 30. 6 8. 7 25. 4 C d 1.83 1.7 1 1.4 3 Tota l SV M 32. 4 10. 4 26. 9 23. 2

SV M Regulator

yStandard = 23 0 ug/m 3

C:\DOCUME~1\klarich.TWI\L0CALS~1\Temp\notesO3055 0 Weoli a Repor t Uni t 2 final-doc 3- 7 Octobe r 200 8 

### VE S 00081 2

# UNIT 3 EMISSIO N RESULT S

# ENS R

Tabl e 3- 1 R M 2 9 Samplin g Parameter s an d Emissio n Result s Ru n No . Dat e Star t Time Stop Tim e Unit

s 1 05-Aufl-0 8 " 12:5 6

r15:1 9 2

06-Aug-0 8 " 12:3 2

r14:4 1 3

07-Aug-0 8

r12:4 5 " 15:0 4 AVG S Samplin g Parameter

s — Barometri c Pressur

e Volum e Metere d Sample Volum

e Moistur e Oz a t Stac k Avg . Stac k

Temp . Stac k Flowrat e Isokinetic s in . H g

de f dsc f % v/ v % dr y ° F dscf m % r29.2

3

r88.53 9 78.48 8 42. 3 11.9 9 " 37 2 5,66 5 9 2 T29.6

5 " 87.45 2 84.25 8 43.6 10.9 6

r37 7 5,71 9 9 8 ' 29.6

5 " 85.94 3 83.93 2 40.6 11.9 8

r37 4 5,89 0 9 5 ' 29.5 1 ' 87.31 1 82.22 6 42. 2 11.6 4 ' 37 4 5,75 8 9 5 Mercurv(He

) — Quantif y Collecte

d Stac k Cone . @ 7

% 0 2 Stac k Emissio n Rat

e p

g pg/m 3 Ib/h r g/se c 78. 5

54. 9 7.49E-0 4 9.44E-0 5 10

5 61. 1 9.39E-0 4 1.18E-0 4 88.

2 57. 6 8.19E-0 4 1.03E-0 4 ' 90.

4 57. 9 ' 8.36E-0 4 ' 1.05E-0 4 Tota l Chromiu m (Cr 1 ) - Quantit y Collecte

d Stac k Cone . @ 7

% 0

2 Stac k Emissio n Rat

e LV M P 9 pg/m 3 Ib/h r g/sec 37.5

0 26.2 2 3.58E-0 4 4.51 E-05 30.4

9 17.8 1 2.74E-0 4 3.45E-0 5 21.7

6 14.2 1 2.02E-0 4 2.55E-0 5 ' 29.9

2 19.4 1 ' 2.78E-0 4 " 3.50E-0

5 Cadmiu m (Cd) — Quantit y Collecte

d Stac k Cone . @ 7

% 0 2 Stac k Emissio n Rat

e SV M p g pg/m 3 Ib/h r g/sec 0.2

4 0.1 7 2.27E-0 6 2.86E-0 7 0.9

0 0.5 3 8.08E-0 6 1.02E-0 6 0.6

3 0.4 1 5.85E-0 6 7.37E-0 7 0.5

9 0.3 7 ' 5.40E-0 6 * 6.80E-0

7 LeadflPb)- - Quantit y Collecte

d Stac k Cone . @ 7

% 0 2 Stac k Emissio n Rat

e SV M p g pg/m 3 Ib/h r g/se c 83. 5

58.4 7.97E-0 4 J.OOE-0 4 11 4

66. 6 1.02E-0 3 1.29E-0 4 70. 1

45. 8 6.50E-0 4 8.19E-0 5 ' 89.1 8 56. 9 " 8.24E-0 4

r1 04E-O

4 Arseni c (As)

— Quantit y Collecte

d

- Stac k Cone . @ 7

% O 2 Stac k Emissio n Rat

e p

g pg/m 3 Ib/h r g/sec 3.1 5

2.20 3.0 1 E-05 3.79E-06 3.7

5 2.1 9 3.37E-05 4.24E-06 1.9

4 1.2 7 1.80E-0 5 2.27E-06 '

2.95 1.8 9 "2.73E-05 " 3.43E-0

6 Berylliu m (Be

) — Quantit y Collecte

d Stac k Cone . @ 7

% 0 2 Stac k Emissio n Rat

e M

9 pg/m 3 Ib/h r g/sec 0.20

0.1 4 1.91E-0 6 2.41.E-0 7 0.2

0 0.1 2 1.80E-0 6 2.26E-07 0.2

0 0.1 3 1.86E-0 8 2.34E-0 7 " 0.20 0.1 3 '1.85E-0 8
" 2.34E-0

7 LV M Tota l = pg/m 3 28. 6 20. 1 15. 6 21. 4 SV M Tota l = pg/m 3 58. 6 67. 1 46.2 57. 3

C:\DOCUME-1\klarlch.TWHLOCALS-1\Temp\notesD30S5 0 3- 2 Ortober200 8 Weoli a Repor t U nit 3 draft-do c 

### VE S 000814

# ENS R

Tabl e 3- 2 Summar yo f HW C MAC TMetal s 

### LowVolatil e Metal s Emission s -ug/m 3 

### <§ > 7 % 0 2 

### Metal s Ru n 1 Ru n 2 Ru n 3 Averag e A s 2.2 0 2.1 9 1:2 7 B e 0.1 4 0.1 2 0.1 3 C r 26. 2 17. 8 14. 2 Tota l LV M 28. 6 20. 1 15. 6 21. 4

LV M Regulator

yStandar d = 92 pg/m 3 

### Semi-Volatil e Meta l Emission s - ug/m 3 

### @ 7 % 0 2 

### Metal s Ru n 1 Ru n 2 Ru n 3 Averag e P b 58. 4 66. 6 45, 8 C d 0.1 7 0.53 0.4 1 Tota l SV M 58. 6 67. 1 46. 2 57. 3

SV M Regulator

yStandar d = 23 0 pg/m 3 

### iVlercur y Emission s -pg/m 3 

### @ 7 % 0 2 

### Ru n 1 Ru n 2 Ru n 3 Averag e 54. 9 61. 1 57. 6 57. 9 Mercur yRegulator

yStandar d = 13 0 pg/m 3

C:\DOCUME-1\klarich.TWHLOCALS-1\Temp\notesD3055 0 Weoli a Repor t Uni t 3 drstt.ioc 3- 3 Octobe r 200 8 

### VE S 00081 5

# UNI T 4 EMISSIO N RESULT S

# ENS R

Tabl e 3- 2 R M 2 9 Samplin g Parameter s an d Emissio n Rate s Ru n No
. Date Star t Tim e Sto p Tim e Unit s 1

r 21-Aug-0 8
r13:2 5
r-15:3 7 2

r 22-Aug-0 8
r10:5 0
r13:0 1 3

r 23-Aug-0 8
r08:5 5 " 10:5 9 AVG S Samplin g Parameter

s — Barometri cPressure Volum e Metere d Sampl e Volum e Moistur e 0 2 a t Stac k Avg
. Stac k

Temp
. Stac k Flowrate Isokinetics in
. H g de f dsc f % v/ v % dr y ° F dscf m % r29.5 4

r90.93 8 89.02 3 39. 0 " 12.2 7

r39 0 17,280 10 1 r29.6 9

" 89.784 88.43 3 39.5
. T12.1 3

r38 8 17,255 10 0 r29.6 4 " 91.42 0 89.264 40. 3

r11.6 3

r39 4 17,18 9 10 2 ' 29.6 2 " 90.71 4 88.90 7 39. 6 12.0 1 ' 39 1 17,24 1 10 1 Mercur y(~H%) - Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat

e pg pg/m 3 Ib/h r g/se c 59. 6

37. 9 1.53E-03 1.93E-04 38. 7

24. 4 9.99E-0 4 1.26E-04 42. 3

25. 0 1.08E-0 3 1.36E-04 ' 46. 9

29. 1

r 1.20E-0 3 " 1.5 1 E-04 Tota l Chromiu m (Cr ) ~ Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rate LV M

p g pg/m a Ib/h r g/se c 3.1 2

1.9 8 8.0 1 E-05 1.0 1 E-05 6.2 B

3.9 6 1.62E-04 2.04E-0 5 6.4 0

3.7 8 1.63E-04 2.05E-0 5 " 5.2 7

3.24 '1.35E-0 4

r1.70E-05 Cadmiu m fCd ) — Quantit yCollecte d Stac k Cone
. @ 7% 0 2 Stac k Emissio n Rat

e SV M p g pg/m 3 Ib/h r g/se c 0.8 0

0.5 1 2.05E-0 5 2.58E-0 6 1.2

7 0.8 0 3.27E-0 5 4.12E-0 6 1.2 9

0.7 6 3.29E-0 5 4.14E-0 6 r1.1 2

0.6 9

r 2.87E-0 5 k 3.6 1 E-0 6 LeadrPhV Quantit yCollecte d Stac k Cone
. @ 7%
. 0 2 Stac k Emissio n Rate SV M

p g pg/m 3 Ib/h r g/se c 34. 3

21. 8 8.8 1 E-0 4 1.11E-04 49. 1

30. 9 1.27E-0 3 1.60E-0 4 44. 5 26. 3 1.13E-Q 3 U3E-0 4 r42.6 3

* 26. 4 "1.09E-0 3

r1.38E-04 Arseni c(As)

— Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rate p

g pg/m 3 Ib/h r g/se c 4.8 2

3.07 1.24E-04 1.56E-0 5 9.82

6.1 9 2.53E-0 4 3.19E-0 5 16.2 2

9.5 9 4.13E-0 4 5.2 1 E-0 5 ' 10.2 9

6.2 8

r 2.63E-0 4 ' 3.32E-0 5 Berylliu m (Bet - Quantit yCollecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rate p

g pg/m 3 Ib/h r g/se c 0.2 0

0.1 3 5.13E-0 B B.47E-0 7 0.2 0

0.1 3 5.16E-0 6 6.50E-0 7 0.2 0

0.1 2 5.09E-0 6 6.42E-0 7 ' 0.2 0

0.1 2 '5.13E-0 6 ' 6.46E-0 7 LV M Tota l = 5. 2 10. 3 13. 5 g. e SV M Tota l = pg/m 3 22. 3 31. 7 27. 1 27. 0 CADOCUME-1\klarich.TWI\LOCALS-1\Temp\noIesD3055 0 3- 3 Octobe r 200 8 \-7902083.do c 

### VE S 00081 7

# ENS R Tabl e 3- 3 Summar yo f HW C MAC TMetal s
Lo wVolatil e Metal s Emission s -ugfm 3 < § 7 % Q 2 Metal s Ru n 1 Ru n 2 Ru n 3 Averag e A s 3.0 7 6.1 9 9.5 9 B e 0.1 3 0.1 3 0.1 2 C r 2. 0 4. 0 3. 8 Tota l LV M 5. 2 10. 3 13. 5 9. 6

LV M Regulator

yStandard = 9 2 pg/m 3 Semi-Volatil e Meta l Emission s -|jg/m 3 @ 7 % O z Metal s Ru n 1 Ru n 2 Ru n 3 Averag e P b 21. 8 30. 9 26. 3 C d 0.5 1 0.8 0 0.7 6 Tota l SV M 22. 3 31. 7 27. 1 27. 0

SV M Regulator

yStandard = 23 0 pg/m 3 Mercur yEmission s -jjg/m 3%7% 0 2 Ru n 1 Ri m 2 Ru n 3 Averag e

r m m m 37. 9 24. 4 25. 0 29. 1

Mercur yRegulator

yStandard = 130 pg/m 3

C:\DOCUME-1\klarich.TWI\LOCALS~1\Temp\notesD3055 0 V-T902083.do c 3- 4 Octobe r 200 8 

### VE S 00081 8

# SYSTE M REMOVA L EFFICIENCY (SRE ) FO R UNIT S 2 , 3 AN D 4200 8 Metal s Testin g Remova l Efficiencies , Uni t 2 (LVM ) Remova l Uni t 3 (LVM ) Remova l Uni t 4 (LVM ) Remova l Em . Std. : 9

2 ug/dsc m Ru n Efficiency (RE) j Em . Std. : 9 2 ug/dsc m Ru n Efficiency (RE) Em . Std. : 9 2 ug/dsc m Ru n Efficienc y (RE ) (9/08 ) (% ) (% ) (% ) 1 99.9997

3 1 99.9992 4 1 99.9996 1 2 99.9999 1 2 99.9994 0 2 99:9992 3 3 .99.99979 . 3 99.9995 8 3 99.9989 3 Av g 99.9998 1 Av g . 99.9994 0 Av g 99.99926

Uni t 2 (SVM ) Remova l Uni t 3 (SVM ) Remova l Uni t 4 (SVM ) Remova l Em . Std. : 23

0 ug/dsc m Ru n Efficienc y (RE) Em . Std. : 23 0 ug/dsc m Ru n Efficiency (RE) Em . Std. : 23 0 ug/dscm - Ru n Efficienc y (RE ) (9/08 ) (% ) (% ) (% ) 1 99.9993

6 1 99.9987 7 1 99.9986 2 . 2 99.9997

8 2 99.9984 4 2 99.9980 0 3 99.9994

2 3 99.9989 9 3 99.9982 4 Av g 99.9995

2 Avg ^ 99.9987 3 Av g 99.99829 Unit2(Hg ) Remova l Unlt3(Hg ) Remova l Unit4(Hg ) Remova l Em . Std. : 13

0 ug/dsc m Ru n Efficienc y (RE) Em . Std. : 13 0 ug/dsc m Ru n Efficiency (RE) Em . Std. : 13 0 ug/dscm . Ru n Efficiency (RE) (8/08 ) (% ) (% ) (% ) 1 84.7

9 1 83.3 8 1 95.0 0 2 81.3

2 2 83.2 5 2 96.7 2 3 82.6

3 3 83.9 6 3 96.4 7 Av g 82.9 1 Av g 83.5 3 Av g 96.0 6Revision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 1 o f 1 2 

## 2. 0 Engineerin g Descriptio n 2. 1 Proces s Overvie w Veoli a operate

s 2 Fixe d Hearth Dual Chambered Incinerator s (Unit s 2 an d 3

) an d one rotar

y kil n incinerato r (Uni t 4 ) a t th e Sauget , I L facility. Th e tw o fixed hearth unit

s ar e rate d a t 1 6 million Btu/h r each . Incineration Uni t No . 3 i s a mirror image o f Uni t No . 2 . Both o

f these unit

s hav e thei r ow

n wast e handlin g system s a s describe d i n th e section s tha

t follow . Th e onl y differenc

e bein g Uni

t No . 2 i s equippe

d wit h fou r (4 ) baghous

e modules , whil e Uni

t No , 3 i s equippe

d wit h thre e (3 ) baghouse modules . However, eac h incinerato r i s operate d identically wit

h onl y thre e baghous

e module

s i n service durin g operation . 2. 2 Wast e Fee d System s [4 0 CF R § 63.1207(f)(1)(ii)(c) an d (f)(1)(iii)(D ) an d (E)] 2.2. 1 Uni t 2 Liqui d Wast e Feed Syste m an d Blendin g Operation s Th e fixe d heart h incinerato r i s designe d t o receiv e containers , aqueou s liqui d wastes , organi c liqui d wastes , specialt y liqui d feeds , gases an d direc t injec t liquids fed throug h th e aqueou s o r organi c liqui d fee d systems . Thes e unit

s ca n receiv

e an y combinatio n o

fwaste s - liquid , semi-solid , soli d or gase s - wit h a hea t valu e o f up t o 1 6 millio n Btu/hr. Uni t 2 i s supporte

d b y storage/blen d tank

s locate d i n Tan k

Farm #1 . Rate

s o f feed ar e controlle

d a t eac h incinerator. Segregated liquid waste s ar e store d unti l utilize

d i n th e wast e blendin g facilities . A

t tha t time , liquids ar e delivere

d t o th e blendin g tank

s wher e the daily liqui d feed t

o th e incinerato r i s formulated , tested , an d released t

o th e incinerator. Blendin g o f store d liqui d waste

s t o achiev e optimu m heatin g valu e an d viscosit y fo r incineratio n take

s plac e i n Tank s 2 , 4 , 6 & 8 . Si x additiona l tank s (10 , 20 , 30 , 40 , 5

0 & 60 ) ar e used t o segregat

e differen

t wast e strea m type

s fo r blendin g o

f liqui d feed t

o the incinerator. Severa l criteri a ar e importan

t i n designin g a blen d from availabl e waste s tha t hav e bee n segregate

d principally b

y physica l an d chemica l properties . These include compatibility , prope r range o

f heatin g value , an d permi t restrictions regardin g elementa l compositio n (base d on emissio n limitations) . Th e materia l i s transferre d throug h abovegroun d pipeline

s from the tan k

farm t o th e incinerator. Pipeline s used t o transfe r liqui d organi c wast e an d aqueou s wast

e ar e equippe

d wit h strainers . I n complianc

e wit h th e Benzen e NESHAP , al l tank s ar e vented t

o individua l carbo n adsorptio n canister s fo r remova l o

f organics befor

e vapo r is discharged t

o the atmosphere . Eac h carbo n adsorbe r caniste r i s essentially equivalent t

o a 5 5 gallo n containe r o r greater, i f necessary . Al l tank

s ar e equippe

d wit h conservatio n vents , i n additio n t o th e carbo n caniste r adsorber . Al l tank s ar e grounded , an d flam e arrestor s ar e installe d betwee n th e carbo n adsorber s an d th e tanks . 2.2.1. 1 Organi c an

d Aqueou s Liqui d Wast e Feed s Th e liqui d waste.injector s used i n th

e combustio n chamber s ar e air-atomizin g injectors . Thes e ar e used fo

r injection o

f hig h Btu , lo

wBtu liquids an d specialt y feed liquids . Dua l flui d injectio n nozzles wil l be use d fo r atomizatio n o

f th e waste . Eac h o

f th e injector s i s rate d a t 0-30 0 gph . Th e liqui d wast e feed nozzles ar

e served b y paralle l redundan

t pump s an d recirculatio n system s wit h bac k pressur e control .

Q.'\mv>07\Pro]ec!s\10DD2D22\Veoli a Performanc e Test Pla n U 2 Revise d O73008.doc


### VE S 00082 1Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 2 o f 1 2 2.2.1. 2 Package d an d Bul k Soli d Container s o f waste s ar e sample d an d analyze d afte rreceipt i n accordanc e wit h th e facility' s Wast e Analysi s Plan
. Thes e waste s ca n the n b e delivere d directl yt o Uni t 2 o rrepacke d into.smal l combustibl e container s a t th e facility
. Fiberboard o rplasti ccontainer s (full yo rpartiall yful l of waste) , u p t o 40-gallo n size , ma yb e charge d directl yt o th e primar ychamber
. Thes e wil l b e receive d a t th e doc k

adjoinin g eac h fixe d heart h incinerator , an d charge d t o th e incinerato rwithi n 2 4 hour s o rreturne d to permitte d storage
. Solids , usuall ypackage d i n plasti co rfiberboar d containers , are introduce d int o th e incinerato rthroug h a PL C controlle d airlock-ra m syste m locate d a t th e lowe rfron t o

f th e primar

ychambe rof th e incinerator
. Th e airloc k i s compose d o

f a refractory-line d door , a doo rinto th e airloc k enclosure , an d two pneumati crams . Th e actio n o f th e feede ri s a s follows :

• Wit h th e incinerato rdoo rclosed , th e airloc k doo ri s opened
. • Th e first pneumati cra m (load ram ) pushe s weighe d charge s o f wast e int o th e airloc k

chamber
. • Th e airloc k

doo ri s closed
. • Aswitc h i s activate d eithe rautomaticall yo rmanually , whic h open s th e doo rto th e incinerato ran d actuate s th e ra m (charg e ram ) tha t pushe s th e wast e into th e incinerator
. Th e ra m the n retract s an d th e incinerato rdoo rcloses
. 2.2.1. 3 Specialt yLiqui d Feed s an d Gase s Specialt yFee d System s associate d wit h Incinerato rNo
. 2 ar e a s follow s

• SpecialtyFeede r
• Compresse d Ga s Cylinde rFee d Syste m
• Direc t Injec t Liqui d Fee d Syste m 2. 3 Manufacturer , Make an d Mode l o f th e Incinerato r [4 0 CF R § 63.1207(f)(1)(iii)(A) ] 2.3. 1 Combustio n Chambe r an d Burner s [4 0 CF R §63.1207(f)( 1 )(iii)(B) an d (C ) Incinerato rNo
. 2 feature s a two-stag e combustio n process . Ignitio n o f wast e materia l take s plac e i n th e primar y(lower ) combustio n chambe r(PCC)
. Asecondar y(upper ) combustio n chambe r(SCC ) serve s a s a n "after-burner " fo rproces s gases . Ignitio n ofth e wast e take s plac e a t temperature s i n exces s o f 170 0 degree s F
. Th e secondar ycombustio n chambe rmaintain s a minimu m temperatur e of approximatel y1800 degree s F
. Th e fixe d heart h incinerato ri s fabricate d o f carbo n steel
. Th e primar ychambe rhas a n externa l diamete ro f 9 fee t an d i s 17. 5 feet long
. Th e interio rwall s o f th e chambe rar e line d wit h approximatel y1 0 inche s o f brick refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y7*2*
. Th e cross sectiona l are a o

f th e chambe ri s thu s 40. 3 square feet
. Tabl e 2- 2 provide s a summar yo f th e incinerato r desig n specifications
. Liqui d an d soli d wast e feed s ente rth e lowe rchambe ro n th e front-fac e o f th e chamber
. Th e primar yburne r an d th e specialtyfee d injecto rar e locate d nea rth e front-face ofth e chambe ran d are mounted tangentially
.
Q:\mw97\Projerts\10002022\veoli a Performanc e Tes t Pla n U 2 Revise d 073008.do c 

### VE S 00082 2Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technical Solution s Uni t 2 HW C MAC TPerformanc

e Tes t Pla n Pag e 3 o f 1 2 Th e primar

yburne ri s a Nort h America n burne rrate d a t 12. 0 millio n Btu/hr
. an d i s use d i n th e lowe rchambe r t o maintai n permitte d temperatures
. I t wil l burn onl ynatura l ga s o rNo
. 2 fue l oil
. Th e burne rsyste m i s supplie d wit h combustio n ai ra t a stati cpressure o

f 30 " wate rcolum n (WC)
. Th e pilo t fo rth e primar

yburne rwil l bur n natura l gas . Th e fue l syste m fo rth e lowe rchambe r(an d secondar ycombustio n chamber

) i s controlle d b

ya Factor yMutua l approve d burne rmanagemen t syste m complete wit h interlock s an d safet

yvalves
. 2.3.2 Secondary Combustio n Chambe r Th e secondar

ycombustio n chambe r(SCC ) i s a horizontal , cylindrica l chambe rtha t ha s a n externa l diamete r o f 9 feet an d i s 17. 5 feet long
. Th e interio rwall s o f th e chambe rare line d wit h approximatel y1 0 inche s o f bric k refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y7'2"
. Th e cross sectiona l are a o

f th e chambe ri s thu s 40. 3 squar e feet
. Followin g ignitio n o

f th e waste materia l unde rcontrolle d o rstarved-ai rcondition s i n th e lowe rchamber , offgase s trave l throug h a refractory-line d flue gas passag e into th e uppe rchamber , whic h acts a s a n afterburner
. Turbulence i s achieve d b

yth e tangentia l introductio n o f ai ran d additiona l fue l i n th e uppe rchamber
. Th e SC C i s equippe d wit h on e burne rmounte d tangentiall yo n th e sid e ofth e chambe rTh e burne ri s a Nort h America n burne rrate d a

t 6. 0 millio n Btu/h ran d i s fuele d wit h natura l ga s o rfue l oil
. A s wit h th e primar

ychambe rburner , th e SC C burne ri s supplie d wit h atomizin g ai ran d i s equippe d wit h a burne rmanagemen t system
. Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof f whe n ther

e i s a los s o f flame , combustio n ai rsupply , fue l pressure , atomizin g ai rpressure , o rpilo t burner
. Leavin g th e uppe rchamber , th e ho t ga s strea m travel s throug h 2 8 fee t o f refractory-line d stac k

section s befor

e reachin g th e star

t o f th e ga s scrubbin g system
. Th e combine d volum e o f th e uppe ran d lowe rchambers , th e flu e ga s passag e an d th e ho t crossove rsectio n i s approximatel y1,567 cubi cfeet
. Th e tota l retentio n tim e o f combustio n gase s withi n th e syste m i s approximatel y5 seconds
. 2.3. 3 Locatio n o f Combustio n Zon e Temperatur e Devic e [4

0 CF R § 63.1207(f)(1)(xix) ] Th e thermocoupl e tha

t monitor s temperatur

e i n th e primar

ycombustio n chambe ri s locate d o n to p ofth e chambe rabou t five fee t fro m th e transition
. Th e thermocoupl e tha t monitor s temperatur

e i n th e SC C i s locate d o n to p o f th e chambe rabove th e transition
. 2.3.4 Hazardou s Waste Residenc e Tim e [4 0 CF R § 63.1207(f)(1)(ix) ] Th e Hazardou s wast e ga s residenc e tim e fo rth e Fixe d Heart h Incinerato ri s calculate d a s follows :

• Primar

yCombustio n Chambe rVolum e - 63 5 ft 3
• Secondar

yCombustio n Chambe rVolum e - 635 ft3
• Tota l Volume-1270ff. 3
• Maximu m Flu e Ga s Flowrate -17,38 2 acf m (29 0 ft 3 /sec ) » Tota l Combustio n Zon e Residenc e Tim e = (127 0 ft3 )/(29 0 ft 3

/sec ) = 4. 4 se c

Q:\mvfi7\Projects\10002022\veoli a Performanc e Tes t Pla n U 2 Revise d 073008.OOC 

### VE S 00082 3Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 4 o f 1 2 2.3. 5 Combustio n Syste m Lea k Combustio n syste m leaks ar e prevente d throug h maintainin g a totall yseale d combustio n chamber , couple d wit h th e us e o

f a n induce d draf

t fa n tha t maintain s a vacuu m of normall y- 4 t o - 6 inche s o

f wate rcolum n i n bot h combustio n chamber s whil e waste s are bein g fe d to th e unit
. 2.3. 6 Emergenc y Safet y Ven t Th e incinerato ri s equippe d wit h a n emergenc ysafet yven t (ESV ) locate d a

t th e to p o f th e secondar

y combustio n chamber
. Thi s ES V i s a refractory-line d emergenc ytherma l relief ven t (TRV) whic h i s hel d i n th e close d positio n bya pneumati ccylinder
. Th e contro l valv e i n th e lin e supplyin g ai rt o th e cylinde ran d th e cylinde rven t valv e whic h open s th e TR V ar e locate d i n th e contro l roo m fo reac h unit
. Valv e lock s (with key

s attached ) are utilize d to dete rindiscriminat e operatio n o f thes e valves
. Openin g of th e TR V allow s ho t combustio n ga s to ven t fro m th e combustio n syste m durin g emergenc yshutdow n events
. Th e purpos e ofth e TR V i s to protec

t th e downstrea m APC S fro m excessiv e temperatur e situations
. Alimi t switc h o n th e TR V shuts of f al l wast e feed s to th e syste m a s it sense s tha t th e ca p i s opening
. 2. 4 Procedure s fo r Rapidl y Stoppin g Hazardou s Wast e Fee d Durin g Equipmen t Malfunctio n [40 CF R §63.1207(f)(1)(viii) ] Equipmen t malfunction s ar e identifie d b

yth e contro l system , observatio n o f proces s contro l variables , o rb y regula rfiel d inspections
. I n th e even t o

f mino requipmen t malfunction s (e.g
. wast e fee d o rscrubbe rleaks) , th e contro l roo m operato r wil l b e notified
. Th e contro l roo m operato rwil l the n clos e th e wast e fee d valve s an d disabl e th e wast e fee d pumps . I n th e even t o

f majo requipmen t malfunction s (e.g
. fire) , th e emergenc ysto p butto n locate d i n th e contro l roo m wil l be pushed
. I f thi s butto n i s pushed , al l equipmen t wil l switc h t o its fail-saf e position
. 2. 5 Ai r Pollutio n Contro l Equipmen t [40 CF R §63.1207(f)(1)(iii)(G) ] 2.5. 1 Ai r Pollutio n Contro l System s Description s Th e ai rpollutio n contro l syste m consist s o f a spraydrye rabsorbe ran d fabri cfilte rbaghous e modules
. Th e ai r pollutio n contro l syste m neutralize s acidi ccompound s an d remove s particulat e fro m th e exhaust gas . Tw o subsystems , th e spraydrye rabsorbe ran d th e fabri cfilter , carr you t th e chemica l neutralizatio n an d particulate remova l functions , respectively
. Athir d subsystem , th e lim e system , i s use d to prepare an d provid e lim e slurr y t o th e spraydrye rabsorbe rfo rus e i n th e chemica l neutralizatio n process . Th e induce d draf t fa n an d stac k provid e th e mechanica l energ yrequire d to transpor t th e flu e ga s throug h th e interconnectin g ductwork , to it s eventua l discharg e poin t t o atmosphere
. 2.5.1. 1 Lime Syste m Th e lim e syste m prepare s lim e slurr yfo rus e i n th e chemica l neutralizatio n proces s i n sufficien t suppl yan d concentratio n to maintai n continuou s flu e ga s treatmen t i n th e spra ydrye rabsorber
. Th e syste m ha s bee n designe d fo rbatc h mixin g to provid e thi s service. Veoli a utilize s hydrate d lim e a s its neutralizin g agen t in f th e ai rpollutio n contro l systems
. Th e keyneutralizatio n paramete ro f th e hydrate d lim e i s th e "Ca O Equivalent"
. Figur e 4- 1 i s th e specificatio n shee t fo rth e hydrate d lim e tha t Veoli a uses . Veoli a ha s use d thi s specifi cproduc

t fo rove r2 0 year s an d plan s t o continu e wit h its use . Although , i f Veoli a doe s chang e Q:Vnvj97\Projects\10002022\Veoli a Performance Tes t Pia n U 2 Revise d 0730DB.do c 

### VE S 000824Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 5 o f 1 2 suppliers o rtyp e o f lim e i n th e future , i t woul d have a "Ca O Equivalent " specificatio n equa l t o o rgreate rtha n th e 72.6 % show n o n Figure 4-1
. Hydrate d lim e i s store d i n a storag e bi n above th e lim e preparatio n area . Th e storag e bi n i s size d to hol d enoug h hydrate d lim e t

o maintai n severa l days o f syste m operatio n a

t th e maximu m combustio n rate ofth e incinerator
. Lim e i s discharge d throug h th e conica l storag e bi n bottom
. Th e flo wo f th e materia l fro m th e bi n i s aide d bya vibratin g "live bottom, " o rbi n activator
. Avariabl e spee d scre wfeede ri s use d to mete rth e hydrate d lim e i n th e proportion s require d fo rbatc h mixin g lim e slurry
. Th e lim e i s mixe d wit h wate ri n a tan k beneat h th e lim e storag e bin
. Th e scre wfeede rspee d an d th e rate tha t wate ri s adde d t

o th e lim e slurr

ytan k are variabl e s o tha

t th e desire d lim e solid s concentratio n ca n be achieve d i n th e tank
. Th e variabl e fee d adjustments allowwate ran d lim e to b e adde d to th e lim e slurr ytan k a t a rate tha

t wil l allowa batc h mod e o f mixing
. A n agitato ri s provide d i n th e slurr ytan k t o mixth e wate ran d lim e an d t o maintai n th e suspensio n o f lim e solids
. Th e mixe d lim e slurr yi s pumpe d at a continuou s rat e of flo wthroug h a recirculatio n loo p to th e atomize ra

t a rate o f u p t o 1 0 gpm . 2.5.1. 2 Spra yDr yAbsorbe r Uni t 2 i s equippe d wit h a Spra yDrye rAbsorbe r(SDA) locate d immediatel ydownstrea m o f th e secondar

y combustio n chamber
. Th e SD Auni t i s fabricate d o f 3/ 8 inc h carbo n steel
. Th e functio n o f th e SD Ai s to :

• Furthe rcoo l th e combustio n gase s fro m 1600-2000o F to 300-500oF , • Neutraliz e an d remove HC I an d othe racid s fro m th e combustio n gases , • Remove a portio n o

f th e particulate (flyash ) fro m thes e gases . Slurr yflowto th e spra

ydrye rabsorbe r(SDA ) i s metere d b ya flowcontro l valve t

o obtai n th e prope rfee d concentratio n to th e spra

ydrye rabsorbe ratomizer
. Automati c(o rmanual ) adjustmen t t o th e flo wi s mad e a s a functio n o

f th e output fro m a hydrochlori caci d (HCI ) analyze ri n th e ga s duc t downstrea m o

f th e fabri cfilter
. Th e amoun t of slurr

ymetere d i s proportiona l to th e amoun t o f HC I monitored
. Th e slurr ypasse s throug h a stationar yswirl-typ e liqui d distributo rint o th e atomize rwhee l wher e induce d centrifuga l forc e fro m th e rapidl yspinnin g whee l discharge s th e slurr ythroug h th e wheel , nozzle s a t hig h velocity
. Th e desig n o

f th e atomize rwheel , its rat e of spin , an d th e discharg e velocit yo f th e slurry , create a clou d o f finel ydivide d droplets aroun d th e peripher yof th e atomize rwheel
. Coolin g wate ri s als o passe d throug h th e atomize rt

o provid e additiona l ga s coolin g t o th e system
. Th e wate rflow i s no t metered , but i s controlle d b

ya feedbac k

signa l fro m th e atomize rpowe rtransmitter
. Thi s provide s verificatio n tha t wate rflo w t o th e atomize rincrease s o rdecrease s i n proportio n t o th e spra ydrye rabsorbe routle

t temperature
. Flu e ga s enter

s fro m th e botto m p

f th e spra ydrye rabsorbe rthroug h a vertical , centrall ylocate d disperser
. Th e disperse rdirect s th e flue ga s throug h th e zon e fille d b yth e atomize d slurr

yclou d wher

e th e flu e ga s an d slurr ymixan d most of th e absorptio n occurs . Th e gase s the n flowdownwar d throug h th e absorbe rchambe r an d exi t throug h a botto m sid e duct
. A s th e gase s contac t an d pas s throug h th e clou d of atomize d lim e slurry , th e wate ri n th e slurr

yevaporates , coolin g th e gases . Simultaneously , th e lim e i n th e slurr yreacts wit h th e hydroge n chlorid e i n th e gase s t o produce calciu m salts
. Som e ofth e resultin g dr ymaterial , consistin g o

f calciu m salts , fl yas h an d exces s lime , fall s to th e conica l botto m o f th e unit
. Th e dr ymateria l fro m eac h unit i s discharge d to a conveyo rsyste m whic h transports i t to a dum p traile ro requivalen t typ e system
.

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### VE S 00082 5Revision : 1 Date : Jul y200 8 Section : 2, 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 6 o f 1 2
2.5.1. 3 Fabri c Filte r Ga s exhauste d fro m th e spra ydrye rabsorbe ri s distribute d b ymanifol d ducts t

o fou rfabri cfilte rmodules
. Th e unit i s operate d wit h onl ythre e module s on-lin e wit h th e fourt h modul e off-lin e i n a standb ymode
. Withi n eac h filte rmodule , th e ga s i s passe d throug h Teflon-coate d fiberglas s clot h bags
. Th e ga s passe s fro m th e outsid e t o th e insid e ofth e filte rbags
. Particulat e entraine d i n th e ga s strea m i s mechanicall ydeposite d o n th e outsid e of th e filte rbag s a s th e ga s passe s throug h th e cloth
. Eac h modul e ha s a clea n ai rplenu m an d housin g sectio n to contai n approximatel y96 bags
. Eac h bag i s approximatel y6 ° i n diamete rb y20 ' long
. Th e baghouse s are fabricate d fro m 3/16 " mil d stee l plate , o f welde d construction , ga s tigh t an d stiffene d t o withstan d th e maximu m operatin g negativ e pressure . Eac h compartmen t ha s a tub e sheet tha t supports th e bag s an d provide s fo rto p bag/cag e removal
. Acces s t o th e clea n ai rplenu m i s vi a a sid e acces s doo ri n th e clea n ai rplenum
. Th e fabri cfilte rcleanin g mechanis m utilize s jets of ai rt o clea n th e filte rbags
. Periodically , th e cleanin g sequenc e wil l b e initiated
. Th e sequenc e i s starte d a t th e en d o

f a 4 hou rtime d cycle , whe n th e differentia l pressure acros s th e filte rreache s a predetermine d setpoin t o f approximatel y7.0 " w.c , o rwhe n th e operato r initiate s a cycle
. Th e controlle rthe n sequence s to eac h rowo f filte rbag s i n eac h module , releasin g a burs t of ai ropposit e t o th e directio n o f ga s flow
. Th e quickl yrelease d burs t o f ai rdislodge s dus

t cake o n th e exterio ro

f eac h bag a s i t travel s fro m th e to p t o th e botto m ofth e bags
. Release d fro m th e bag , th e dus t cake fall s b

y gravit yint o th e hoppe ra

t th e botto m ofth e module
. Fro m ther e i t i s discharge d t

o a conveyo rsyste m whic h transports it t o a dum p trailer , o requivalen t typ e system
. Treate d b yth e spraydrye rabsorbe ran d filtere d b yth e fabri cfilters , th e cleane d flu e ga s exits th e fabri cfilte r module s t o a n outlet manifol d fo rexhaust
. 2.5.1. 4 Induce d Draf t Fa n an d Stac k Th e induce d draf

t fa n an d stac k

are locate d downstrea m o f th e fabri cfilter
. Combustio n gase s ar e draw n throug h th e syste m bya 7 5 h p induce d draf t (ID) fan , rate d a

t 15,00 0 acf m a

t 400 ° F saturated , an d 22 " wate r colum n pressure . Th e induce d draf t fa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s throug h th e spraydrye rabsorber , fabri cfilter , an d al l interconnectin g ducts
. Th e I D fa n include s a n inlet volum e contro l dampe rt o b e use d t o contro l th e velocit

yofth e ga s withi n th e ductin g an d treatmen t devices
. Treate d gase s ar e exhauste d fro m th e induce d draf t fa n to th e atmosphere throug h a 90-ft
. hig h stack
. Th e stac k diamete rfo rUni t 2 i s 3 9 inche s I.D
. Th e stac k i s equippe d wit h instrumen t samplin g port s an d a samplin g platfor m fo remission s testing
. Figure 5- 1 provide s detail s o n th e desig n an d sampl e por t location s an d configuration s fo rth e stack
. 2. 6 Stac k

Emission s Monitorin g [40 CF R §63.1207(f)(1)(iiij(H) ] Th e continuou s emission s monitorin g (CEM ) syste m consist s o f sampl e probes , sampl e deliver yan d conditionin g apparatus , ari d ga s analyzers
. Sample s are extracte d fro m th e samplin g port s o n th e stack
. A CE M performance test an d qualit yassuranc e progra m ha s bee n implemente d i n accordance wit h th e Appendi x t o Subpar t EE E of Par t 63
— Quality Assuranc e Procedure s fo r Continuou s Emission s Monitor s Use d fo r Hazardou s Wast e Combustors . Response s fro m eac h CEM S wil l b e fe d t o th e Contro l Syste m (CS ) wher e th e C O hourl yrollin g averag e i s calculate d an d interlocke d t o th e wast e fee d cutof

f valve s a s par

t of th e Automati cWast e Fee d Cutof f Syste m

Q:\m\v97\ProJects\10002022\veoli a Performanc e Tes t Pla n U 2 Revise d O73O08.doc


### VE S 00082 6Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerfonnanc e Tes t Pla n Pag e 7 o f 1 2 (AWFCO ) discusse d i n Sectio n 2.8 , below
. Th e followin g provide s a brief descriptio n ofth e CEM S instruments includin g th e operatin g rang e an d measuremen t principal
. 2.6. 1 CE M Syste m Descriptio n Th e Continuou s Emission s Monitorin g System s (CEMS ) currentl ybein g utilize d a t Incinerato r2 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , excep t opacity , ar e extractive device s mounted i n samplin g ports o n th e stack
. Th e tabl e belowsummarize s th e analyze rspecifications
. Th e opacit

ymonito rcontinuousl ymeasure s th e stac k ga s opacit

yan d report

s th e measurements to a n indicato ran d a recorder
. A n opacit ytha t exceed s a preset limi t trigger s a n alar m an d interlock
. Carbo n monoxid e an d hydroge n chlorid e ar e monitore d wit h extractive non-dispers e infrare d analyzers
. Tota l hydrocarbo n i s monitore d wit h a n extractive flam e io n detecto ranalyzer
. Oxyge n i s monitored wit h a zirconiu m oxid e cell
. Stac k ga s flo wrate i s continuousl ymonitore d usin g a n anuba rtha t send s a 4-2 0 m Asigna l t o th e PL C whic h converts th e signa l to acfm
. Tabl e 2- 1 Uni t 2 Continuou s Emissio n Monitor s Paramete

r Curren

t Mfg
. Rang e Principl e ] Oxyge n COS A 0-25 % Electrochemica l Carbo n Monoxid e Ecoche m MC 3 0-20 0 ppmv 0-300 0 ppmv Infrared I Tota l hydrocarbon s Thermoelectro n 0-10 0 ppmv FID/lnfrare d | Hydroge n chlorid e Ecoche m MC 3 0-1,00 0 ppmv Infrared Opacity Teledyn e 0-100 % Whit e ligh t Stac k ga s flow PSE/Rosemoun t 0-20,00 0 acf m Pressure dro p |
2. 7 Proces s Monitorin g an d Contro l Th e facilit yi s equippe d wit h a state-of-the-ar t monitorin g an d contro l system , whic h facilitate s complianc e wit h permi t conditions , an d otherwise , collects.proces s contro l information , facilitate s efficien t operatio n an d detect s an d prevent s damag e t

o th e facility
. Th e syste m consist s of thre e majo rcomponents :

• Ahuman-machin e interface (HMI ) system , • Programmabl e logi ccontroller' s (PLC's) , an d
• Ahig h spee d etherne t cabl e connect s al l contro l syste m components Th e desire d contro l function s ar e implemente d throug h th e HM I system
. Al l digita l contro l an d emergenc y interlock s ar e accomplishe d b

yth e PLC
. Th e contro l syste m i s capabl e o f monitorin g th e "operationa l envelope " ofth e incinerato ran d i s capabl e o f performin g a numbe ro

f activitie s including :
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### VE S 00082 7Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veoli a E S Technical Solution s Uni t 2 HW C MAC TPerformanc

e Tes t Pla n Pag e 8 o f 1 2

• Contro l roo m indicatio n o f processo rsensors locate d withi n th e incinerato rsyste m (suc h a s pressur e indicatio n of a fiel d installe d pressure transmitter) ; • Proces s controlle rfo rsingl e instrumen t loop s o ra n individua l sub-system , suc h a s a temperatur e contro l loo p involvin g a senso rreadin g fro m on e temperatur e transmitte raffectin g th e functio n of on e temperatur

e contro l valve ; an d
• Alar m fo ra n exceedanc e o f a designate d setpoint , suc h a s a hig h pressure o rlo wtemperature
. Th e proces s contro l compute rwil l continuousl ycontro l an d monito rth e operatio n ofth e incinerator
. Whe n outof-rang e condition s exist , it wil l notif yth e operato ro

f thos e conditions
. Th e proces s contro l compute ri s programme d t

o shut-dow n equipmen t (i.e. , brin g th e syste m int o a saf e mode ) whe n designate d parameter s ar e exceeded , whic h i s a protectiv e mechanis m agains t potentia l equipmen t damage , operatio n outsid e o f permi t limits , o rcondition s tha t might lea d t

o a releas e to th e environment
. Continuou s monitorin g o f th e incinerato ran d scrubbe rsyste m i s a n importan t aspec t of th e syste m design
. A digita l readou t of al l monitorin g instrumentatio n i s displaye d o n th e mai n contro l screen . A n audibl e an d visua l alar m alert s th e incinerato roperato rto significan t deviation s fro m norma l operatin g conditions
. Thi s syste m allows a n immediate respons e t o advers e condition s b

yth e operator
. Automati cwaste fee d cut-of f an d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m a t o rprio rto reachin g permi t limi t levels
. Monitorin g method s an d calibratio n frequencie s are liste d i n Tabl e 2-3
. Th e Incinerato rha s a n independen t proces s contro l compute rtha t interface s t

o th e Quantu m programmabl e controllers
. Th e proces s compute ri s capabl e o f controllin g th e incinerato ri n cas e o f a failur e i n a HM I server . Thi s compute rrun s a RSVIE W HM I contro l softwar e tha t provide s operato rinterface t o al l instrumentatio n an d controls
. 2. 8 Automati c Wast e Fee d Cut-of f Syste m [40 CF R §63.1207(f)(1)(iii)(F) ] Th e incinerato rha s a n Automati cWast e Fee d Cut-Of f (AWFCO ) Syste m tha

t wil l shu t wast e feed s of

f i n th e even t certai n operatin g parameter s deviat e fro m allowabl e se t points
. Th e PL C continuousl ymonitor s operatin g parameters , makin g adjustments to th e proces s a s neede d fo rprope rcontrol
. Alar m logi ci s incorporate d int

o th e PL C syste m t

o automaticall yinitiat e a n AWFCO
. Tabl e 2-3 summarize s th e curren t AWFC O set points
. AWFC O limits have bee n establishe d base d o n severa l factor s tha t ar e summarize d below
.
• Regulatory/permi t limits - establishe d to compl ywit h existin g permits
. A n exampl e of thi s typ e o f limi t i s th e lowtemperatur

e limit , belowwhic h wast e cannot b e fe d unti l th e prope rlimi t i s re-established
. I n addition , th e HW C MAC Tregulation s requir e tha t th e AWFC O syste m b e interlocke d wit h th e spa n of eac h proces s instrumen t tha t i s par t ofth e Continuou s Monitorin g Syste m (CMS)
. Alistin g o f thes e CM S instruments an d thei rinterlocke d spa n setpoint s i s maintaine d a s par t o f Veolia' s Operatin g Record
. • Proces s safet

ylimit s - establishe d t

o assur e proces s equipmen t i s protecte d an d unsaf e operatin g condition s d o no

t occur . A n exampl e of thi s i s inadequat e exces s ai ri n th e combustio n chambe rtha t ca n lea d t o fue l rich conditions
. • Utilit yo rPowe rfailur

e - establishe d t o facilitat e a controlle d shutdow n o f th e proces s durin g los s o f proces s air , steam , wate ro relectricity
. A n exampl e o f thi s i s th e los s o

f instrumen t ai rtha

t i s necessar yfo rcertai n type s of proces s instruments to functio n properly
. Waste s wil l no t b e re introduce d into th e incinerator s unti l prope roperatio n o f ke yinstruments i s re-established
.
Q:Vnw97\Pro)Bcts\10002022\Veoli a Performanc e Tos t Pla n U 2 Revise d 073008.do c 

### VE S 00082 8Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pia n Pag e 9 o f 1 2 I n additio n t o th e AWFC O system , operator s ca n manuall yshutdow n wast e feed s o rth e entir e proces s shoul d thi s b e needed
. 2.8. 1 AWFC O Syste m Testin g Veoli a test s th e AWFC O system s bi-weekly , a s weekl ytestin g woul d undul yinterfer e wit h operation s b

y ceasin g an d restartin g wast e feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s durin g th e downtime , an d increasin g operatin g costs
. Testin g ofth e AWFC O syste m i s a time-consumin g an d manpowe rintensive process . Th e curren t testin g progra m ha s bee n i n place unde rth e RCR Apermi t fo rove r2 0 years an d ha s prove n t o b e adequat e i n detectin g problems
. Thi s rational e i s include d i n th e facility' s AWFC O Plan
. I n som e case s thi s testin g occurs more frequentl ydependin g o n ho w ofte n actua l AWFCO s occu ra t th e unit
. Pe rth e require d frequency , incinerato rpersonne l chec k th e functionalit

yo f AWFC O logi ctha

t i s par t ofth e incinerator' s PL C syste m to mak e sure tha

t shoul d proces s condition s deviat e fro m allowabl e limits , th e compute rlogi cwil l initiat e wast e fee d shutdown s a s required
. Thi s i s accomplishe d b

ymanuall ysimulatin g proces s condition s tha t are outsid e allowabl e limits an d observin g an d documentin g whe n th e contro l o rbloc k valv e softwar

e logi co n th e wast e fee d lin e begin s t o initiate valve closure
. Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e are documente d b yoperatin g personne l to satisf

yregulator

yrequirements fo rsyste m testing
. Result s of thi s testin g ar e documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par t of th e unit' s Operatin g Record
. 2. 9 Ai r Pollutio n Contro l Equipmen t Maintenanc e Practice s [40 CF R §63.1207(f)(1)(iii)(G) ] 2.9. 1 Progra m Overview Onc e equipmen t i s installe d an d operational , Veoli a utilize s a n extensive preventative maintenance (PM ) progra m to kee p equipmen t operationa l an d preven t breakdown s an d failures
. Base d upo n th e typ e of equipmen t an d historica l operation s an d maintenanc e experience , schedule s fo rvariou s inspectio n an d P M activitie s ar e followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenanc e historie s o n equipment , routin e inspectio n an d lubricatio n program s fo rhig h wea requipmen t an d non-destructive testin g of pipin g an d vessel s usin g technique s like ultrasoun d t o asses s integrity
. Th e frequenc yo f thes e activitie s varie s dependin g upo n th e equipment , P M activit yan d th e incinerator' s shutdow n schedule
. Fo rexample , frequen t (i.e. , weekly) instrumen t an d certai n mechanica l equipmen t checks ar e mad e fo rcritica l proces s items
. Lubrication , vibratio n analysi s an d othe rmechanica l integrit ychecks are . don e a

t longe r frequencie s like monthl yo rquarterly
. An d finally , suc h item s a s inspectin g refractor ybric k fo rwear , are typicall yperforme d whe n th e entir e incinerato ri s shu t dow n fo rmaintenance
. 2.9. 2 Tes t Progra m Preparatio n Activitie s Prio rt o testing , instrumentatio n associate d wit h ke yparameter s o f th e test wil l b e checked , calibrated , o r replaced , a s appropriate , to ensure prope roperatio n ofth e instrumentatio n durin g testin g (i.e. , wast e fee d flowmeter s an d scales , CEM's , pressure transmitters , thermocouples , stac k flowmeters , etc.)
.

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### VE S 00082 9Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technical Solution s Uni t 2 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 0 o f 1 2 Tabl e 2- 2 Technica l Information Summar y o n Incinerator No . 2 Manufacture r Trad e Wast e Incineratio n Mode l No
. TWI-2000 , Serie s 2 Typ e Fixe d Hearth , Dua l Chambe r Dat e o f Manufacture 198 7 Dimension s Primary
. Chambe r Secondar yChambe r Externa l Lengt h 17.5 ' 17.5 ' Externa l Diamete r 9 ' 9 ' Interna l Diamete r 7'2 " 7'2 " Cross-sectiona l are a 40. 3 squar e fee t 40. 3 squar e fee t Burner s Primar yChambe rBurne r SecondaryChambe rBurne r Manufacture r Nort h America n Nort h America n Siz e 12. 0 Millio n Btu/h r 6. 0 Millio n Btu/h r Fue l Natura l Ga s Natura l Ga s Prime rMove r Induce d Draft Fa n 15,00 0 acf m @ 400° F saturated , 2 2 in
. wate rcolum n

Q.-\mw97VProJet:ls\10002022Weoli a Performance Tes t Pla n U 2 Revise d 0730OB.do c 

### VE S 00083 0Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veoli a ES Technica l Solution s Uni t 2 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 1 o f 1 2
Tabl e 2-3 Curren t AWFC O Parameters an d Limit s fo r Incinerato r No . 2 1 Syste m Device Unit s Cutof

f Limit s Calibratio n j

Frequenc

y | J Tota l Pumpable Wast

e Fee d frar. e Mass Flowmeters/Scale s Lb/h r > 3,12 3 (HRA ) Annuall

y Tota l Wast

e Feedrat

e Mass Flowmeters/Scale s Lb/h r >4,30 1 Annually/quarterl y Hig h BT U Liquid feedrat e Mass flo

wmeter lb/h r > 2,01 2 Annuall y Lo wBT U Liquid feedrat

e Mas

s flo wmete r Ib/hr > 1,99 3 Annuall y Specialt y feede r Scal e Ib/hr 5 72 4 Quarterl y Tota l LV M Feedrat

e Mass Flowmeters/Scale s Ib/hr > 1,26 4 (1 2 HRA

) Annually/quarterl y Pumpabl e LVM Feedrat e Mass flo

wmeter/Scale

s Ib/hr > 1,26 4 (1 2 HRA

) Annually/quarterl y SV M Feedrat

e Mass Flowmeters/Scale s Ib/hr >3,477(12HRA ) Annually/quarterl y Mercur y Feedrat

e Mass Flowmeters/Scale s Ib/hr > 0.007 3 (12HRA

) Annually/quarterl y Chlorin e Feedrat

e Mass Flowmeters/Scale s Ib/hr >237 (1 2 HRA ) Annually/quarterl y As h Feedrat

e Mas s Flowmeters/Scale s Ib/hr > 67 3 (1 2 HRA

) Annually/quarterl y Primar y Combustion Chambe r Temperatur

e Type KThermocouple ° F <1,59 0 (one-minut

e average

) <1,71 2 (HRA 1 ) >2,40 0 (instantaneous

) Annuall

y

•Secondar

y Combustio n Chambe r Temperatur

e Type KThermocouple ° F £1,79 4 (one-minut e average

) <1,84 5 (HRA

1 ) >2,40 0 (instantaneous

) Annuall

y
Primar y Combustion Chambe r pressur

e Pressur e transmitte

r in . w.c. >-0. 1 ( 5 secon d delay

) Quarterl

y Secondar

y Combustion Chambe r pressur

e Pressur e transmitte

r in . w.c. 5 -0. 1 ( 5 secon d delay

) Quarterl

y Chlorin e Fee

d t o Slurr y Flo w Rati o Flowmete r rati

o > 33. 5 Annuall y [Spra y Drye r Adsorbe r Outle

t I Temperatur

e Type KThermocoupl e ° F >50 0 (on e minut e average

) >42 0 (HRA ) Annuall y Combustio n Ga s Flo

wRat e Pito

t Tub e acf

m £17,19 8

>15,53 4 (HRA ) Annuall

y Stac k Ga s Excess Oxyge n Zirconiu m Oxide fue l cel l % < 3 (one-minut e avg.) Quarterl y Stac k carbon monoxid

e Infrare d ppm

v >10

0 (HRA ) 250 0 (on e minut e average

) Quarterl

y Stac k Hydrocarbon FI D ppm v >1 0 (on

e minut e average

) Quarterl

y Stac k ga s opacit y Whit e Ligh t % £1 0 (on e minut e average

) Quarterl

y Stac k hydroge n chloride 2 Infrare d ppm

v >10

0 (HRA ) 250 0 (on e minut e average

) Quarterl

y Fabri c filte

r pressur e drop Delt

a P transmitte

r in . w.c . £ 2 or > 1 0 ( 1 min . average

) Quarterl

y

1 HR A mean

s "hourl y rolling average " as calculate d b y averagin g th

e previous 6

0 one-minut

e average values . I z Thi s i s a RCR A permi t limi t only . Q:\mw97\Projects\1O00202Z\Veoli a Performanc e Tes t Pla n U 2 Revise d 073008.do c 

### VE S 00083 1Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC TPerformanc e Tes t Pla n Pag e 1 2 o f 1 2 Figur e 2- 1 Hydrate d Lim e Specification s
Mis8i:&i&%ti

Osa e Compass};
.

.t.t\:t M7SarS5ilP M ROTA VlMiT

' • Hy*i rate d 1..±)i'. e Cod e MB200 . Mset s (SW A an d wat* r .ae-mlcal s Co.tle s 5iwciiJ.C!ttJ-<?s m

O " ' t o 97.2 %

. . .7 2 . a t c 73. 6

.6 5 Jf > 7 4 . 3 c t t c o 3 ...... . . a s t o i.7 5 , 0 5 t o a-.i o S T5<iv

i J.v«l<sa t . . . . . 0 . , Ol E t o Q . 0S 4 ,•3 8 l o o.e s . . 2 0 LO 0.30 - or t o 0,3.1 ?

- . Q . 4 0 IU - 0.£ 6

3 0 l.i l 0.9 5

. .. . - - 0 . o o e L O 0,01 3 OOI S I: a 0.003 5 'i 'VUlCIS- J PtlYEtCft L ACalVfil S lf.Xa.um 10 3 raesb IC O .OS . KXCUJ ; iJO O 9 S . I > Kleue t 3S 5 ne-sh . 32. 0 DtSiirt

l tj - - youod s yai ' it 3 - * o t o 35 > {Depending ; s;po n dejfra e 0

2

Q:\mvfi7\Projecls\10002022\veoll s Performanc e Tes t Pla n U 2 Revise d 073D08.do c


### VE S 00083 2Revision : 1 Date : Jur

y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC TPerformanc e Tes t Pla n Pag e 1 o f 1 2 

## 2. 0 Engineerin g Descriptio n

2. 1 Proces s Overvie w Veoli a operate s 2 Fixe d Heart h Dua l Chambere d Incinerator s (Unit s 2 an d 3 ) an d on e rotar

ykil n incinerato r (Uni t 4) a t th e Sauget , I L facility
. Th e tw o fixe d heart h unit

s ar e rate d a t 1 6 millio n Btu/h reach
. Incineratio n Uni t No
. 3 i s a mirro rimag e o f Unit No
. 2
. Bot h o

f thes e units hav

e thei rown waste handlin g system s a s describe d i n th e section s tha t follow
. Th e onl ydifference bein g Uni t No
. 2 i s equippe d wit h fou r(4 ) baghous e modules , whil e Uni t No
. 3 i s equippe d wit h thre e (3 ) baghous e modules
. However , eac h incinerato ri s operate d identicall ywit h onl ythre e baghous e module s i n service durin g operation
. 2. 2 Wast e Fee d System s [40 CF R § 63.1207(f)(1)(ii)(c) an d (f)(1)(iii)(D) an d (E) ] 2.2. 1 Uni t 3 Liqui d Wast e Fee d Syste m an d Blendin g Operation s Th e fixe d heart h incinerato ri s designe d t o receive containers , aqueou s liqui d wastes , organi cliqui d wastes , specialt yliqui d feed s an d direc

t injec t liquid s fe d throug h th e aqueou s o rorgani cliqui d fee d systems
. Thes e units ca n receive an ycombinatio n of waste s - liquid , semi-soli d o rsoli d - wit h a hea t valu e o f u p t o 1 6 millio n Btu/hr
. Uni t 3 i s supporte d b

ystorage/blen d tank

s locate d i n Tan k

Farm #1
. Rate s o

f fee d ar e controlle d a

t eac h incinerator
. Segregate d liqui d waste s are store d unti l utilize d i n th e wast e blendin g facilities
. A t tha t time , liquid s ar e delivere d t

o th e blendin g tank

s wher e th e dail yliqui d fee d t

o th e incinerato ri s formulated , tested , an d release d t

o th e incinerator
. Blendin g o f store d liqui d waste s t

o achieve optimu m heatin g valu e an d viscosit yfo rincineratio n take s place i n Tank s 2,4, 6 & 8
. Si xadditiona l tank s (10,20 , 30,40 , 5 0 & 60) ar e use d t o segregat e differen t waste strea m type s fo rblendin g o f liqui d fee d t

o th e incinerator
. Severa l criteri a are importan t i n designin g a blen d fro m availabl e waste s tha t hav e bee n segregate d principall yb yphysica l an d chemica l properties
. Thes e includ e compatibility , prope rrang e o f heatin g value , an d permi t restriction s regardin g elementa l compositio n (base d o n emissio n limitations)
. Th e materia l i s transferre d throug h abovegroun d pipeline s fro m th e tan k farm to th e incinerator
. Pipeline s use d t o transfe rliqui d organi cwast e an d aqueou s wast e ar

e equippe d wit h strainers
. I n complianc e wit h th e Benzen e NESHAP , al l tank s ar e vente d t o individua l carbo n adsorptio n canister s fo r remova l of organics befor

e vapo ri s discharge d t

o th e atmosphere
. Eac h carbo n adsorbe rcaniste ri s essentiall yequivalen t to a 55 gallo n containe ro rgreater , i f necessary . Al l tank s ar e equippe d wit h conservatio n vents , i n additio n to th e carbo n caniste radsorber
. Al l tank s ar e grounded , an d flam e arrester s are installe d betwee n th e carbo n adsorber s an d th e tanks
. 2.2.1 . 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui d wast e injector

s use d i n th e combustio n chamber s ar e air-atomizin g injectors
. Thes e ar e use d fo r injectio n o f hig h Btu , lo

wBt u liquid s an d specialt

yfee d liquids
. Dua l flui d injectio n nozzle s wil l b e use d fo r atomization'of th e waste
. Eac h o f th e injector

s i s rate d a

t 0-30 0 gph
. Th e liqui d wast e fee d nozzle s ar e serve d b yparalle l redundan t pumps an d recirculatio n system s wit h bac k pressur e control
.

Q :\mw97\Projects

\1 0002022\veo!i a Performanc e Tes t Pla n U 3 073006 Revlsion.do cRevision : 1 Date: Jul y 200 8 Section : 2.

0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC TPerformanc

e Tes t Plan Pag e 2 o f 1 2 2.2.1.2 Package d an d Bul k Soli d Containers o f waste s ar

e sample d an d analyze d afte rreceip t i n accordanc e wit h th e facility' s Wast e Analysi s Plan
. Thes e waste s ca n the n b e delivere d directl yt o Uni t 3 O

rrepacke d into smal l combustibl e container s a t th e facility
. Fiberboard o rplasti ccontainer s (full yo rpartiall yful l of waste) , u p to 40-gallo n size , ma yb e charge d directl yto th e primar ychamber
. Thes e wil l b e receive d a t th e doc k adjoinin g eac h fixe d heart h incinerator , an d charge d t o th e incinerato rwithi n 2 4 hour s o rreturne d t o permitte d storage
. Solids , usuall ypackage d i n plasti co rfiberboar d containers , are introduce d int o th e incinerato rthroug h a PL C controlle d airlock-ra m syste m locate d a t th e lowe rfron t of th e primar ychambe ro

f th e incinerator
. Th e airloc k i s compose d of a refractory-line d door , a doo rint o th e airloc k

enclosure , an d tw

o pneumati crams . Th e actio n of th e feede ri s a s follows :

• Wit h th e incinerato rdoo rclosed , th e airloc k doo ri s opened
. • Th e first pneumati cram (loa d ram) pushe s weighe d charge s o f wast e int o th e airloc k

chamber
. • Th e airloc k

doo ri s closed
. • Aswitc h i s activate d eithe rautomaticall yo rmanually , whic h open s th e doo rt o th e incinerato ran d actuate s th e ra m (charg e ram ) tha t pushe s th e wast e int o th e incinerator
. Th e ra m the n retracts an d th e incinerato rdoo rcloses
. 2.2.1.3 Specialt yLiqui d Feed s an d Gase s SpecialtyFee d System s associate d with Incinerato rNo
. 3 are a s follows

• Hoode d Specialt

yContaine rFeede r
• Glov e Bo xEmissio n Contro l System s
• Direc t Injec t Liqui d Fee d Syste m 2. 3 Manufacturer , Mak e an d Mode l o f th e Incinerato r [4 0 CF R § 63.1207(f)(1)(iii)(A) ] 2.3. 1 Combustio n Chambe r an d Burner s [4 0 CF R §63.1207(f)(1)(iii)(B) an d (C ) Incinerato rNo
. 3 feature s a two-stag e combustio n process . Ignitio n o f wast e materia l take s plac e i n th e primar y(lower ) combustio n chambe r(PCC)
. Asecondar y(upper ) combustio n chambe r(SCC ) serve s a s a n "after-burner " fo rproces s gases . Ignitio n ofth e wast e take s plac e a t temperature s i n exces s o f 1700 degree s F
. Th e secondar ycombustio n chambe rmaintain s a minimu m temperatur e o f approximatel y1800 degree s F
. Th e fixe d heart h incinerato ri s fabricate d o f carbo n steel
. Th e primar ychambe rha s a n externa l diamete ro f 9 fee t an d i s 17. 5 fee t long
. Th e interio rwall s o f th e chambe rar

e line d wit h approximatel y1 0 inche s o f bric k refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y7'2"
. Th e cross sectiona l are a of th e chambe ri s thu s 40. 3 square feet
. Tabl e 2- 2 provide s a summar yof th e incinerato r desig n specifications
. Liqui d an d soli d wast e feed s ente rth e lowe rchambe ro n th e front-face o f th e chamber
. Th e primar yburne r an d th e specialt

yfee d injecto rare locate d nea rth e front-fac e o f th e chambe ran d are mounted tangentially
.

Q:\mw97\Projectsi10002O22lveolj a Performance Tes t Pla n 0 3 07300 8 Revfeion.do c 

### VE S 000834Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC TPerformance
. Tes t Pla n Pag e 3 o f 1 2 Th e primar

yburne ri s a North America n burne rrate d a t 12. 0 millio n Btu/hr
. an d i s use d i n th e lowe rchambe r t o maintai n permitte d temperatures
. I t wil l burn onl ynatura l ga

s o rNo
. 2 fue l oil
. Th e burne rsyste m i s supplie d wit h combustio n ai ra t a stati cpressur

e o f 30 " wate rcolum n (WC)
. Th e pilo t fo rth e primar

yburne rwil l bur n natura l gas . Th e fue l syste m fo rth e lowe rchambe r(an d secondar ycombustio n chamber

) i s controlle d b

ya Factor yMutua l approve d burne rmanagemen t syste m complete wit h interlock s an d safet

yvalves
. 2.3.2 Secondary Combustio n Chambe r Th e secondar

ycombustio n chambe r(SCC ) i s a horizontal , cylindrica l chambe rtha t has a n externa l diamete ro f 9 feet an d i s 17. 5 fee t long
. Th e interio rwall s o f th e chambe rar

e line d wit h approximatel y1 0 inche s o f bric k refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y 7'2"
. Th e cross-sectiona l are a o f th e chambe ri s thu s 40. 3 squar e feet
. Followin g ignitio n o f th e waste materia l unde rcontrolle d o rstarved-ai rcondition s i n th e lowe rchamber , offgase s trave l throug h a refractory-line d flu e ga s passag e int o th e uppe rchamber , whic h acts a s a n afterburner
. Turbulence i s achieve d b

yth e tangentia l introductio n o f ai ran d additiona l fue l i n th e uppe rchamber
. Th e SC C i s equippe d wit h on e burne rmounted tangentiall yo n th e sid e o f th e chamber
. Th e burne ri s a Nort h America n burne rrate d a

t 6. 0 millio n Btu/h ran d i s fuele d wit h natura l ga s o rfue l oil
. A s wit h th e primar

ychambe rburner , th e SC C burne ri s supplie d wit h atomizin g ai ran d i s equippe d with a burne rmanagemen t system
. Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof f whe n ther

e i s a los s of flame , combustio n ai rsupply , fue l pressure , atomizin g ai rpressure , o rpilot burner
. Leavin g th e uppe rchamber , th e ho t ga s strea m travel s throug h 2 8 fee t of refractory-line d stac k

section s befor

e reachin g th e star

t of th e ga s scrubbin g system
. Th e combine d volum e o f th e uppe ran d lowe rchambers , th e flu e ga s passag e an d th e ho t crossove rsectio n i s approximatel y1,56 7 cubi cfeet
. Th e tota l retentio n tim e o f combustio n gase s withi n th e syste m i s approximatel y5 seconds
. 2.3. 3 Locatio n o f Combustio n Zon e Temperatur e Device [4

0 CF R §63.1207(f)(1)(xix) ] Th e thermocoupl e tha

t monitor s temperatur

e i n th e primar

ycombustio n chambe ri s locate d o n to p ofth e chambe rabou t fiv e fee

t from th e transition
. Th e thermocoupl e tha t monitor s temperatur

e i n th e SC C i s locate d o n to p ofth e chambe rabove th e transition
. 2.3. 4 Hazardou s Waste Residenc e Tim e [4 0 CF R §63.1207(f){ 1 )(ix) ] Th e Hazardou s wast e ga s residence tim e fo rth e Fixe d Heart h Incinerato ri s calculate d a s follows :

• Primar

yCombustio n Chambe rVolum e - 63 5 fr. 3
• Secondar

yCombustio n Chambe rVolum e - 635 ft3

. Tota l Volume-127011 3
• Maximu m Flu e Ga s Flowrate -17,38 2 acf m (29 0 ff/sec )
• Tota l Combustio n Zon e Residence Tim e = (1270 ft 3)/(29 0 ft3 /sec ) = 4. 4 se c

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### VE S 00083 5Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC TPerformanc

e Tes t Plan Pag e 4 o f 1 2 2.3. 5 Combustio n Syste m Lea k Combustio n syste m leaks are prevente d throug h maintainin g a totall yseale d combustio n chamber , couple d wit h th e us e o

f a n induce d draf

t fa n tha t maintain s a vacuu m of normall y- 4 t o - 6 inche s o f wate rcolum n i n bot h combustio n chamber s whil e waste s ar e bein g fe d t o th e unit
. 2.3. 6 Emergenc y Safety Ven t Th e incinerato ri s equippe d wit h a n emergenc ysafet yven t (ESV ) locate d a

t th e to p o

f th e secondar

y combustio n chamber
. Thi s ES V i s a refractory-line d emergenc ytherma l relief ven t (TRV) whic h i s hel d i n th e close d positio n b

ya pneumati ccylinder
. Th e contro l valv e i n th e lin e supplyin g ai rt o th e cylinde ran d th e cylinde rven t valv e whic h open s th e TR V ar e locate d i n th e contro l roo m fo reac h unit
. Valv e lock s (wit h keys attached ) are utilize d to dete rindiscriminat e operatio n o f thes e valves
. Openin g of th e TR V allows ho t combustio n ga s to ven t fro m th e combustio n syste m durin g emergenc yshutdow n events
. Th e purpos e ofth e TR V i s t o protec

t th e downstrea m APC S fro m excessiv e temperature situations
. Alimi t switc h o n th e TR V shut s of f al l wast e feed s to th e syste m a s it sense s tha t th e ca p i s opening
. 2. 4 Procedure s fo r Rapidl y Stoppin g Hazardou s Wast e Fee d Durin g Equipmen t Malfunctio n 14

0 CF R §63.1207(f)(1)(viii) ] Equipmen t malfunction s are identifie d b yth e contro l system , observatio n o f proces s contro l variables , o rb y regula rfiel d inspections
. I n th e even t o

f mino requipmen t malfunction s (e.g
. wast e fee d o rscrubbe rleaks) , th e contro l roo m operato r wil l be notifie d b

yradio
. Th e contro l roo m operato rwil l the n disabl e th e wast e fee d pump s an d clos e th e wast e fee d valves
. I n th e even t of majo requipmen t malfunction s (e.g
. fire) , th e emergenc ysto p butto n locate d i n th e contro l roo m wil l b e pushed
. I f thi s butto n i s pushed , al l equipmen t wil l switc h t o it s fail-saf e position
. 2. 5 Ai r Pollutio n Contro l Equipmen t [4 0 CF R §63.1207(f)(1)(iii)(G) ] 2.5. 1 Ai r Pollutio n Contro l System s Description s Th e ai rpollutio n contro l syste m consist s o f a spraydrye rabsorbe ran d fabri cfilte rbaghouse
. Th e ai rpollutio n contro l syste m neutralize s acidi ccompound s an d remove s particulat e fro m th e exhaust gas . Two subsystems , th e spraydrye rabsorbe ran d th e fabri cfilter , carr you t th e chemica l neutralizatio n an d particulate remova l functions , respectively
. Athir d subsystem , th e lim e system , i s use d to prepar e an d provid e lim e slurr

y t o th e spraydrye rabsorbe rfo rus e i n th e chemica l neutralizatio n process . Th e induce d draf t fa n an d stac k provid e th e mechanica l energ yrequire d t o transpor t th e flu e ga s throug h th e interconnectin g ductwork , t o its eventua l discharg e poin t t o atmosphere
. 2.5.1. 1 Lime Syste m Th e lim e syste m prepare s lim e slurr yfo rus e i n th e chemica l neutralizatio n proces s i n sufficien t suppl yan d concentratio n to maintai n continuou s flu e ga s treatmen t i n th e spraydrye rabsorber
. Th e syste m ha s bee n designe d fo rbatc h mixin g t o provid e thi s service
. Veoli a utilize s hydrate d lim e a s its neutralizin g agen t in f th e ai rpollutio n contro l systems
. Th e ke yneutralizatio n paramete ro f th e hydrate d lim e i s th e "Ca O Equivalent/'
. Figure 4- 1 i s th e specificatio n shee t fo rth e hydrate d lim e tha t Veoli a uses . Veoli a has use d thi s specifi c
Q:\mwG7\Projects\10002022\veoli a Performance Tes t Pla n U 3 07300 B Revisian.do c 

### VE S 00083 6Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technical Solution s Uni t 3 HW C MAC TPerformanc

e Tes t Pla n Pag e 5 o f 1 2 produc t fo rove r2 0 years an d plan s t o continu e wit h its use . Although , i f Veoli a doe s chang e supplier s o rtyp e o f lim e i n th e future , i t woul d hav e a "Ca O Equivalen f specificatio n equa l t o o rgreate rtha n th e 72.6 % shown o n Figur e 4-1
. Hydrate d lim e i s store d i n a storag e bi n above th e lim e preparatio n area . Th e storag e bi n i s size d t o hol d enoug h hydrate d lim e to maintai n severa l day s o f syste m operatio n a

t th e maximu m combustio n rate o f th e incinerator
. Lim e i s discharge d throug h th e conica l storag e bi n bottom
. Th e flo wo f th e materia l fro m th e bi n i s aide d b ya vibratin g "live bottom, " o rbi n activator
. Avariabl e spee d scre wfeede ri s use d t o mete rth e hydrate d lim e i n th e proportion s require d fo rbatc h mixin g lim e slurry
. Th e lim e i s mixe d wit h wate ri n a tan k beneat h th e lim e storag e bin
. Th e screwfeede rspee d an d th e rate tha t wate ri s adde d to th e lim e slurr ytan k ar e variabl e s o tha

t th e desire d lim e solid s concentratio n ca n b e achieve d i n th e tank
. Th e variabl e fee d adjustment

s allo wwate ran d lim e t o b e adde d to th e lim e slurr ytan k a t a rate tha

t wil l allowa batc h mode o f mixing
. A n agitato ri s provide d i n th e slurr ytan k t o mi xth e wate ran d lim e an d to maintai n th e suspensio n o f lim e solids
. Th e mixe d lim e slurr yi s pumpe d a

t a continuou s rat

e o f flo wthroug h a recirculatio n loo p t o th e atomize ra

t a rat e o f u p t o 1 0 gpm . 2.5.1. 2 Spra yDr

yAbsorbe r Uni t 3 i s equippe d wit h a Spra yDrye rAbsorbe r(SDA) locate d immediatel ydownstrea m ofth e secondar y combustio n chamber
. Th e SD Auni t i s fabricate d of 3/ 8 inc h carbo n steel
. Th e functio n ofth e SDAi s to :

• Furthe rcoo l th e combustio n gase s fro m 1600-2000o F t o 300-500oF , • Neutraliz e an d remov e HC I an d othe racid s fro m th e combustio n gases , • Remove a portio n o

f th e particulate (flyash ) fro m thes e gases . Slurr yflo wt o th e spra

ydrye rabsorbe r(SDA) i s metere d b ya flowcontro l valve to obtai n th e prope rfee d concentratio n t

o th e spra

ydrye rabsorbe ratomizer
. Automati c(o rmanual ) adjustmen t t o th e flowi s mad e a s a functio n o

f th e outpu t fro m a hydrochlori caci d (HCI ) analyze ri h th e ga s duc t downstrea m of th e fabri cfilter
. Th e amoun t of slurr

ymetere d i s proportiona l to th e amount o f HC I monitored
. Th e slurr ypasse s throug h a stationar yswirl-typ e liqui d distributo rinto th e atomize rwhee l wher e induce d centrifuga l forc e fro m th e rapidl yspinnin g whee l discharge s th e slurr ythroug h th e whee l nozzle s a t hig h velocity
. Th e desig n ofth e atomize rwheel , its rat e o f spin , an d th e discharg e velocit yof th e slurry , create a clou d o f finel ydivide d droplets aroun d th e peripher yof th e atomize rwheel
. Coolin g wate ri s als o passe d throug h th e atomize rt

o provid e additiona l ga s coolin g t o th e system
. Th e wate rflowi s no t metered , bu

t i s controlle d b

ya feedbac k

signa l fro m th e atomize rpowe rtransmitter
. Thi s provide s verificatio n tha t wate rflo w t o th e atomize rincrease s o rdecrease s i n proportio n t o th e spraydrye rabsorbe routle t temperature
. Flu e ga s enter

s fro m th e botto m o f th e spra ydrye rabsorbe rthroug h a vertical , centrall ylocate d disperser
. Th e disperse rdirects th e flu e ga s throug h th e zon e fille d b ythe : atomize d slurr

yclou d wher

e th e flu e gas an d slurr ymixan d mos

t o f th e absorptio n occurs . Th e gase s the n flowdownwar d throug h th e absorbe rchambe r an d exi t throug h a botto m sid e duct
. A s th e gase s contac t an d pas s throug h th e clou d of atomize d lim e slurry , th e wate ri n th e slurr

yevaporates , coolin g th e gases . Simultaneously , th e lim e i n th e slurr yreacts wit h th e hydroge n chlorid e i n th e gase s t o produce calciu m salts
. Som e of th e resultin g dr ymaterial , consistin g o

f caldu m salts , fl yas h an d exces s lime , fall s t o th e conica l botto m o f th e unit
. Th e dr ymateria l fro m eac h unit i s discharge d t o a conveyo rsyste m whic h transports it t o a dum p traile ro requivalen t typ e system
.

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e Tes t Plan Pag e 6 o f 1 2 2.5.1.3 Fabri c Filte r Ga s exhauste d fro m th e spra ydrye rabsorbe ri s distribute d b ymanifol d duct s to thre e fabri cfilte rmodules
. Withi n eac h filte rmodule , th e ga s i s passe d throug h Teflon-coate d fiberglas s clot h bags
. Th e ga s passe s fro m th e outsid e t o th e insid e ofth e filte rbags
. Particulate , entraine d i n th e ga s stream , i s mechanicall ydeposite d o n th e outsid e ofth e filte rbag s a s th e ga s passe s throug h th e cloth
. Eac h modul e ha s a clea n ai rplenu m an d housin g sectio n t o contai n approximatel y9 6 bags
. Eac h ba g i s approximatel y8 " i n diamete rby20 ' long
. Th e baghouse s are fabricate d fro m 3/16 " mil d stee l plate , o f welde d construction , ga s tigh t an d stiffene d to withstan d th e maximu m operatin g negative pressure . Eac h compartmen t ha s a tub e shee t tha t supports th e bag s an d provide s fo rto p bag/cag e removal
. Acces s t o th e clea n ai rplenu m i s vi a a sid e acces s doo ri n th e clea n ai rplenum
. Th e fabri cfilte rcleanin g mechanis m utilize s jet s o f ai rt o clea n th e filte rbags
. Periodically , th e cleanin g sequenc e wil l b e initiated
. Th e sequenc e i s eithe rstarte d a t th e en d o

f a time d cycle , o rwhe n th e differentia l pressur e acros s th e filte rreache s a predetermine d setpoin t o f approximatel y7.0 " w.c , o rwhe n th e operato r initiate s a cycle
. Th e controlle rthe n sequence s to eac h ro wo f filte rbag s i n eac h module , releasin g a burs t o f ai ropposit e t

o th e directio n of ga s flow
. Th e quickl yrelease d burst of ai rdislodge s dus t cake o n th e exterio ro

f eac h ba g a s it travel s fro m th e to p t o th e botto m ofth e bags
. Release d fro m th e bag , th e dus t cak e fall s b y gravit yinto th e hoppe ra

t th e botto m ofth e module
. Fro m ther e i t i s discharge d t

o a conveyo rsyste m whic h transport s it to a dum p trailer , o requivalen t typ e system
. Treate d byth e spraydrye rabsorbe ran d filtere d b yth e fabri cfilter , th e cleane d flu e gas exits th e Fabri cfilte r module s to a n outlet manifol d fo rexhaust
. 2.5.1.4 Induce

d Draf t Fa n an d Stac k Th e induce d draf

t fa n an d stac k

are locate d downstrea m ofth e fabri cfilter
. Combustio n gase s ar e draw n throug h th e syste m b

ya 7 5 h p induce d draf

t (ID ) fan , rate d a

t 15,00 0 acf m a

t 400 ° F saturated , an d 22 " wate r colum n pressure . Th e induce d draf t fa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s throug h th e spra

ydrye rabsorber , Fabri cfilter , an d al l interconnectin g ducts
. Th e I D fa n include s a n inlet volum e contro l dampe rt

o b e use d t

o contro l th e velocit

yofth e ga s withi n th e ductin g an d treatmen t devices
. Treate d gasse s exhauste d fro m th e induce d draf t fa n to th e atmospher

e throug h a 90-ft
. hig h stack
. Th e stac k diamete ri s 3 9 inche s I.D
. Th e stac k i s equippe d wit h instrumen t samplin g port s an d a samplin g platform fo remission s testing
. Figure 5- 1 provide s detail s o n th e desig n an d sampl e por t location s an d configurations
. 2. 6 Stac k

Emission s Monitorin g [4 0 CF R §63.1207(f)(1)(iii)(H) ] Th e continuou s emission s monitorin g (CEM ) syste m consist s of sampl e probes , sampl e deliver yan d conditionin g apparatus , an d ga s analyzers
. Sample s ar e extracte d fro m th e transitio n ductin g locate d betwee n th e scrubbe ran d stack
. ACE M perfprmance test an d qualit yassuranc e progra m ha s bee n implemente d i n accordanc e wit h th e Appendi x t o Subpar

t EE E o f Par t 63—Qualit

y Assurance Procedure s fo r Continuou s Emission s Monitor s Used fo r Hazardou s Wast e Combustors . Response s fro m eac h CEM S wil l b e fe d to th e Contro l Syste m (CS ) where th e C O hourl yrollin g averag e i s calculate d an d interlocke d to th e wast e fee d cutof f valve s a s par

t o f th e Automati cWast e Fee d Cutof f Syste m (AWFCO ) discusse d i n Sectio n 2.8 , below
. Th e followin g provide s a brief descriptio n o f th e CEM S instruments includin g th e operatin g rang e an d measuremen t principal
.

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e Tes t Plan Pag e 7 o f 1 2 2.6. 1 CE M Syste m Descriptio n Th e Continuou s Emission s Monitorin g System s (CEMS ) currentl ybein g utilize d a t Incinerato r3 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , except opacity , ar e extractive device s mounte d i n samplin g port s o n th e stack
. Th e tabl e belo wsummarize s th e analyze rspecifications
. Th e opacit

ymonito rcontinuousl ymeasure s th e stac k ga s opacit

yan d report

s th e measurements t

o a n indicato ran d a recorder
. A n opacit ytha t exceed s a preset limi t trigger s a n alar m an d interlock
. Carbo n monoxid e an d hydroge n chlorid e are monitore d wit h extractive non-dispers e infrare d analyzers
. Tota l hydrocarbo n i s monitore d wit h a n extractive flam e io n detecto ranalyzer
. Oxyge n i s monitored wit h a zirconiu m oxid e cell
. Stac k ga s flo wrate i s continuousl ymonitore d usin g a n anuba rtha t send s a 4-2 0 m Asigna l t o th e PL C whic h converts th e signa l t

o acfm
. Tabl e 2-

1 Uni t 3 Continuou s Emissio n Monitor s \ "

= Paramete r Curren

t Mfg . Rang e Principl e J Oxyge n COS A 0-25 % Electrochemica l j Carbo n Monoxid e Ecoche m MC 3 0-20 0 ppmv 0-300 0 ppmv Infrare d j Tota l hydrocarbon s Thermoelectro n 0-10 0 ppmv FID/Infrare d j Hydroge n chlorid e Ecoche m MC 3 0-1,00 0 ppmv Infrare d j Opacit y Teledyn e 0-100 % White ligh t I Stac k ga s flo w PSE/Rosemoun t 0-20,00 0 acf m Pressure dro p J
2. 7 Proces s Monitorin g an d Contro l Th e facilit yi s equippe d wit h a state-of-the-ar t monitorin g an d contro l system , whic h facilitate s complianc e wit h permi t conditions , an d otherwise , collect s proces s contro l information , facilitate s efficien t operatio n an d detect s an d prevents damag e to th e facility
. Th e syste m consist s o f thre e majo rcomponents :

• Ahuman-machin e interface (HMI ) system , • Programmabl e logi ccontroller' s (PLC's) , an d 2-7.1. 1 Ahig h spee

d etherne

t cabl e connect

s al l contro l syste m component s Th e desire d contro l function s are implemente d throug h th e HM I system
. Al l digita l contro l an d emergenc y interlock s ar e accomplishe d b

yth e PLC
. Th e contro l syste m i s capabl e of monitorin g th e "operationa l envelope " of th e incinerato ran d i s capabl e o f performin g a numbe ro

f activitie s including :

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e Tes t Pla n Pag e 8 o f 1 2

• Contro l roo m indicatio n o f processo rsensor

s locate d withi n th e incinerato rsyste m (suc h a s pressur e indicatio n o

f a fiel d installe d pressure transmitter) ;
• Proces s controlle rfo rsingl e instrumen t loop s o ra n individua l sub-system , suc h a s a pressure contro l loo p involvin g a senso rreadin g fro m on e pressure transmitte raffectin g th e functio n of on e pressur e contro l valve ; an d
• • Alar m fo ra n exceedanc e o f a designate d setpoint , suc h a s a hig h pressure o rlowtemperature
. Th e proces s contro l compute rwil l continuousl ycontro l an d monito rth e operatio n o f th e incinerator
. Whe n out-of-rang e condition s exist , it wil l notif yth e operato ro

f thos e conditions
. Th e proces s contro l compute ri s programme d to shut-dow n equipmen t (i.e. , brin g th e syste m into a saf e mode) whe n designate d parameter s ar e exceeded , whic h i s a protectiv e mechanis m against potentia l equipmen t damage , operatio n outsid e o f permi t limits , o rcondition s tha t migh t lea d to a releas e to th e environment
. Continuou s monitorin g ofth e incinerato ran d scrubbe rsyste m i s a n importan t aspec t ofth e syste m design
. A digita l readou t of al l monitorin g instrumentatio n i s displaye d o n th e mai n contro l screen . A n audibl e an d visua l alar m alert s th e incinerato roperato rto significan t deviation s fro m norma l operatin g conditions
. Thi s syste m allows a n immediat e respons e t o advers e condition s b

yth e operator
. Automati cwast e fee d cut-of f an d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m a t o rprio rto reachin g permi t limi t levels
. Monitorin g method s an d calibratio n frequencie s are liste d i n Tabl e 2-3
. Th e Incinerato rha s a n independen t proces s contro l compute rtha t interface s t

o th e Quantu m Progammabl e controllers
. Th e proces s compute ri s capabl e o f controllin g th e incinerato ri n cas e o f a failure i n a computer
. Thi s compute rfun s a RSVIE W HM I contro l softwar e tha t provide s operato rinterface t o al l instrumentatio n an d controls
. 

### 2. 8 Automati c Wast

e Fee d Cut-of f Syste m [4

0 CF R §63.1207(f)(1)(iii)(F)] Th e incinerato rha s a n Automati cWast e Fee d Cut-Of f (AWFCO ) Syste m tha

t wil l shu t wast e feed s of

f i n th e even t certai n operatin g parameter s deviat e fro m allowabl e se t points
. Th e PL C continuousl ymonitor s operatin g parameters , makin g adjustments to th e proces s a s neede d fo rprope rcontrol
. Alar m logi ci s incorporate d into th e PL C syste m to automaticall yinitiat e a n AWFCO
. Tabl e 2- 3 summarize s th e curren t AWFC O set points
. AWFC O limit s hav e bee n establishe d base d o n severa l factor s tha t ar e summarize d below
.
• Reoulatorv/permi t limits - establishe d to compl ywit h existin g permits
. A n exampl e of thi s typ e of limi t i s th e lo wtemperatur

e limit , belowwhic h wast e ca n no t b e fe d unti l th e prope rlimi t i s re-established
. I n addition , th e HW C MAC Tregulation s requir e tha t th e AWFC O syste m b e interlocke d wit h th e spa n of eac h proces s instrumen t tha t i s par t ofth e Continuou s Monitorin g Syste m (CMS)
. Alistin g o f thes e CM S instruments an d thei rinterlocke d spa n setpoint s i s maintaine d a s par t o f Veolia' s Operatin g Record
. • Proces s safet

ylimits - establishe d to assure proces s equipmen t i s protecte d an d unsaf e operatin g condition s d o no

t occur . A n exampl e o

f thi s i s inadequat e exces s ai ri h th e combustio n chambe rtha t ca n lea d t o fue l rich conditions
. • Utilit yo rPowe rfailur

e - establishe d to facilitat e a controlle d shutdow n o f th e proces s durin g los s of proces s air , steam , wate ro relectricity
. A n exampl e o f thi s i s th e los s o f instrumen t ai rtha

t i s necessar yfo rcertai n type s proces s instruments to functio n properly
. Waste s wil l no t b e re-introduce d int o th e incinerator

s unti l prope roperatio n of ke yinstrument s i s re-established
.
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0 Veolia E S Technica l Solution s Uni t 3 HW C MAC TPerformanc

e Tes t Plan ' Pag e 9 o f 1 2 I n additio n to th e AWFC O system , operator s ca n manuall yshutdow n wast e feed s o rth e entir e proces s shoul d thi s b e needed
. 2.8. 1 AWFC O Syste m Testin g Veoli a tests th e AWFC O system s bi-weekly , a s weekl ytestin g woul d undul yinterfer e wit h operation s b

y ceasin g an d restartin g wast e feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s durin g th e downtime , an d increasin g operatin g costs
. Testin g ofth e AWFC O syste m i s a time-consumin g an d manpowe rintensive process . Th e curren t testin g progra m ha s bee n i n plac e unde rth e RCR Apermi t fo rove r2 0 year s an d ha s prove n t

o b e adequat e i n detectin g problems
. Thi s rational e i s include d i n th e facility' s AWFC O Plan
. I n som e case s thi s testin g occurs mor e frequentl ydependin g o n ho w ofte n actua l AWFCO s occu ra t th e unit
. Pe rth e require d frequency , incinerato rpersonne l chec k th e functionalit

yo f AWFC O logi ctha

t i s par t o f th e incinerator' s PL C syste m to mak e sur e tha t shoul d proces s condition s deviat e fro m allowabl e limits , th e compute rlogi cwil l initiat e wast e fee d shutdown s a s required
. Thi s i s accomplishe d b

ymanuall ysimulatin g proces s condition s tha t ar e outsid e allowabl e limits an d observin g an d documentin g whe n th e contro l o rbloc k valv e softwar

e logi co n th e wast e fee d lin e begin s t o initiate valv e closure
. Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e are documente d b yoperatin g personne l t o satisf

yregulator

yrequirements fo rsyste m testing
. Result s o f thi s testin g are documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par t ofth e unit' s Operatin g Record
. 2. 9 Ai r Pollutio n Contro l Equipmen t Maintenanc e Practice s [40 CF R §63.1207(f)(1)(iii)(G) ] 2.9. 1 Progra m Overvie w Once equipmen t i s installe d an d operational , Veoli a utilize s a n extensiv e preventativ e maintenance (PM ) progra m t o kee p equipmen t operationa l an d preven t breakdown s an d failures
. Base d upo n th e typ e of equipmen t an d historica l operation s an d maintenance experience , schedule s fo rvariou s inspectio n an d P M activitie s are followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenance historie s o n equipment , routin e inspectio n an d lubricatio n program s fo rhig h wea requipmen t an d non-destructive testin g of pipin g an d vessel s usin g technique s like ultrasoun d t o asses s integrity
. Th e frequenc yo f thes e activitie s varie s dependin g upo n th e equipment , P M activit yan d th e incinerator' s shutdow n schedule
. Fo rexample , frequen t (i.e. , weekly ) instrumen t an d certai n mechanica l equipmen t check s ar e mad e fo rcritica l proces s items
. Lubrication , vibratio n analysi s an d othe rmechanica l integrit ychecks ar e don e a

t longe r frequencie s like monthlyo rquarterly
. An d finally , suc h item s a s inspectin g refractor ybric k fo rwear , are typicall yperforme d whe n th e entir e incinerato ri s shu t dow n fo rmaintenance
. 2.9. 2 Tes t Progra m Preparatio n Activitie s Prio rto testing , instrumentatio n associate d wit h ke yparameter

s of th e tes t wil l b e checked , calibrated , o r replaced , a s appropriate , t o ensur e prope roperatio n o

f th e instrumentatio n durin g testin g (i.e. , wast e fee d flowmeter s an d scales , OEM's , pressure transmitters , thermocouples , stac k flowmeters , etc.)
.

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0 Veoli a E S Technical Solution s Uni t 3 HW C MAC TPerfomianc

e Tes t Pla n Pag e 1 0 o f 1 2 Tabl e 2- 2 Technica l Information Summar y o n Incinerator No . 3 Manufacture r Trad e Wast e Incineratio n Mode l No
. TWI-2000 , Serie s 2 Typ e Fixe d Hearth , Dua l Chambe r Date o f Manufactur

e 198 8 Dimension s Primar yChambe r Secondar yChambe r Externa l Lengt h 17.5 ' 17.5 ' Externa l Diamete r 9 ' 9 ' Interna l Diamete r 7'2 " 7'2 " Cross-sectiona l are a 40. 3 squar e fee t 40. 3 squar e fee t Burner s Primar

yChambe rBurne r SecondaryChambe rBurne r Manufacture r Nort h America n Nort h America n Siz e 12. 0 Millio n Btu/h r 6. 0 Millio n Btu/h r Fue l Natura l Ga s Natura l Ga s Prime rMove r Induce d Draf t Fa n 15,00 0 acf m @ 400° F saturated , 2 2 in
. wate rcolum n

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e Tes t Pla n Pag e 1 1 o f1 2
Tabl e 2- 3 Curren t AWFC O Parameters an d Limit s fo r Incinerato r No . 3 ] Syste m Devic e Unit s Cutof f Limit s Calibratio n

Frequency Tota l Pumpabl e Wast e Fee d rate Mas s Flowmeters/Scale s Lb/h r >3,12 3 (HRA ) Annuall y {Tota l Wast e Feedrat e Mas s Flowmeters/Scale s Lb/h r >4,30 1 Annually/quarterl yi [Hig h BT U Liqui d feedrat e Mas s flo wmete r lb/h r >2,01 2 Annuall y [Lo wBT U Liqui d feedrat e Mas s flowmete r Ib/h r > 1,99 3 Annuall y Specialt yfeede r Scal e Ib/h r £72 4 Quarterly Tota l LV M Feedrat e Mas s Flowmeters/Scale s •Ib/h r > 1,26 4 (1 2 HRA ) Annually/quarterl y Pumpabl e LV M Feedrat e Mas s Flowmeters/Scale s Ib/h r > 1,26 4 (1 2 HRA ) Annually/quarterl y JSV M Feedrat e Mas s Flowmeters/Scale s Ib/h r >3,477 (1 2 HRA ) Annually/quarterl y JMercur y Feedrat e Mas s Flowmeters/Scale s Ib/h r > 0.007 3 (12HRA) Annually/quarterl yj Chlorin e Feedrat e Mas s Flowmeters/Scale s Ib/h r >23 7 (1 2 HRA) Annually/quarterl y As h Feedrat e Mas s Flowmeters/Scale s Ib/h r >67 3 (1 2 HRA ) Annually/quarterl y Primar yCombustio n Chambe rTemperatur

e Typ e KThermocoupl e ° F <1,590 (one-minut e average ) <1,71 2 (HRA 1 ) >2,40 0 (instantaneous ) Annuall y Secondar yCombustio n Chambe rTemperature Typ e KThermocoupl e ° F 51,79 4 (one-minute average ) <1,84 5 (HRA 1 ) >2,40 0 (instantaneous ) Annuall y Primar yCombustio n Chambe rpressure Pressure transmitte r in
. w.c . >-0. 1 ( 5 secon d delay

) Quarterly Secondar yCombustio n Chambe rpressure Pressure transmitte r in
. w.c . £ -0. 1 (5 secon d delay ) Quarterl y Chlorin e Fee d t

o Slurr y FlowRati o Flowmete r rati o >33. 5 Annuall y Spra yDrye rAdsorbe r [Outle t Temperatur

e Typ e KThermocoupl e ° F 250 0 (one minut e average ) >420 (HRA) Annuall yI Combustio n Ga s Flow [Rat e PitotTub e acf m >17,19 8 >15,53 4 (HRA ) Annuall y Stac k Ga s Exces s Oxyge n Zirconiu m Oxid e fue l cel l % < 3 (one-minut e avg. ) Quarterl yj Stac k carbo n monoxid e Infrared ppmv >10 0 (HRA) >50 0 (on e minut

e average ) Quarterlyj Stac k Hydrocarbo n FI D ppm v >1 0 (on e minut e average ) Quarterl y Stac k ga s opacit

y Whit e Light % s1 0 (one minut e average ) Quarterl y Stac k hydroge n chloride 2 Infrared ppm v >10 0 (HRA ) >50 0 (on e minut

e average ) Quarterly Fabri cfilterpressure dro p Delta P transmitte r in
. w.c . < 2 o r> 1 0 ( 1 min . average ) Quarterly
1 HR Amean s "hourl yrollin g average " a s calculate d b yaveragin g th e previou s 6 0 one-minute averag e values
. |
2 Thi s i s a RCR Apermi t limi t only
. J

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( Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC TPerformanc e Tes t Pla n Pag e 1 2 o f 1 2 Figur e 2- 1 Hydrate d Lim e Specification s

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# c Q:VnwS7\ProjectsUOOD2022\Veoli a Pertbimanc e Tes t Pla n U 3 07300 B Revision.do c


### VE S 00084 4Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technical Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 o f 1 5 

## 2. 0 Engineerin g Descriptio n

2. 1 Proces s Overvie w Veoli a operate s 2 Fixe d Heart h Dua l Chambere d Incinerator s (Unit s 2 an d 3 ) an d on e rotar

ykil n incinerato r (Uni t 4 ) a t th e Sauget , I L facility
. Th e tw o fixe d heart h units ar

e rate d a t 1 6 millio n Btu/h reach
. Incineratio n Uni t No
. 3 i s a mirro rimag e of Unit No
. 2
. Bot h o f thes e unit

s have thei row n waste handlin g system s a s describe d i n th e section s tha t follow
. Th e onl ydifference bein g Uni t No
. 2 i s equippe d wit h fou r(4 ) baghous e modules , whil e Uni t No
. 3 i s equippe d wit h thre e (3 ) baghous e modules
. However , eac h incinerato ri s operate d identicall ywit h onl ythre e baghous e module s i n servic e durin g operation
. Uni t 4 i s rate d a t 5 0 millio n Btu/h ran d i s equippe d wit h its ow n tan k farm system , dru m storage , bul k solid s storag e an d fee d systems
. 2. 2 Wast e Fee d System s [4 0 CF R § 63.1207(f)(1)(ii)(c) an d (f)(1)(iii)(D) an d (E) ] 2.2. 1 Uni t 4 Liqui d Waste Fee d Syste m an d Blendin g Operation s Th e Uni t 4 Rotar

yKil n ca n incinerate anyo f th e wast e tha

t Veoli a i s authorize d an d permitted t o receive
. Al l physica l form s o

f waste s wil l b e handle d an d fe d byth e system' s wast e fee d devices
. Liquid s wil l b e fe d t o eithe rth e kil n o rth e Secondar yCombustio n Chambe r(SCC)
. Bul k soli d waste s wil l b e fe d t

o th e kil n throug h eithe rth e ra m feeder
. Containerize d waste s wil l b e fe d t o th e kil n throug h th e ra m feede ro rth e auxiliar yra m feeder
. Thi s unit ca n receive anycombinatio n o f waste s - liquid , semi-solid , o rsoli d - wit h a hea t valu e of u p t o 5 0 millio n Btu/hr
. Uni t 4 i s supporte d b

ystorag e tank

s locate d i n Tan k

Far m #3
. Thes e tank

s ar e use d t o stor e th e liqui d organi c waste , aqueou s wastes , an d pumpabl e sludge s t o b e fe d t o th e system
. Unlik e Tan k Far m #1 , al l o

f th e tank s i n Tan k Far m # 3 ca n b e use d a s fee d tank s to th e incinerator
. Severa l criteri a ar e important i n designin g a blen d fro m receive d wastes
. Thes e includ e compatibility , prope rrang e o f heatin g value , an d permi t restriction s regardin g elementa l compositio n (base d o n emissio n limitations)
. Pump s t o transfe rthes e waste s t o th e syste m ar

e installe d i n th e tan k

farm
. Th e materia l i s transferre d throug h abovegroun d pipeline s fro m th e tan k far m t o th e incinerator
. Pipeline s use d t o transfe rliqui d organi cwast e an d aqueou s wast e ar e equippe d wit h strainers
. I n complianc e wit h th e Benzen e NESHAP , al l tank s ar e vente d to individua l carbo n adsorptio n canister s fo r remova l of organics befor e vapo ri s discharge d t

o th e atmosphere
. Eac h carbo n adsorbe rcaniste ri s essentiall yequivalen t to a 5 5 gallo n containe ro rgreater , i f necessary . Al l tank s ar e equippe d with conservatio n vents , i n additio n to th e carbo n caniste radsorber
. Al l tank s ar e grounded , an d flam e arrestor s ar e installe d betwee n th e carbo n adsorber s an d th e tanks
. 2.2 .1. 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui d wast e injector

s use d i n th e combustio n chamber s are air-atomizin g injectors
. Thes e ar e use d fo r injectio n o f pumpabl e sludges , aqueou s waste s an d organi cliqui d waste s t o th e kil n an d fo rinjectio n o f organi cliqui d wast e to th e SCC
. Dua l flui d injectio n nozzle s wil l b e use d fo ratomizatio n o f th e waste
. Eac h o

f th e injector

s i s rate d a

t 0-30 0 gph
. Th e liqui d wast e fee d nozzle s are serve d b yparalle l redundan t pumps an d recirculatio n system s wit h bac k pressur e control
.

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### VE S 00084 5Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 2 o f 1 5 2.2.1. 2 Package d an d Bul k Soli d Container s o f waste s ar e sample d an d analyze d afte rreceipt i n accordanc e wit h th e facility' s Wast e Analysi s Plan
. Thes e waste s ca n the n b e delivere d directl yto Uni t 4 o rrepacke d int o smal l combustibl e container s a t th e facility
. Repackage d container s ar e delivere d to , an d staged , i n th e Containe rStorag e Uni t No
. 6 adjacen t t o th e Uni t 4 incinerator
. Whe n schedule d fo rfeedin g t o th e system , th e container s o f waste are transferre d b

y forklifts t o th e fee d conveyor

s servin g Uni t 4
. Bul k solid s an d non-pumpabl e waste s ar e delivere d an d discharge d into waste fee d bin s i n th e Bul k Solid s Storag e Buildin g afte rbein g received , sampled , an d analyzed
. Aclamshel l operatin g fro m a n overhead cran e i s use d t o transfe rthes e waste s fro m th e bin s t o th e fee d hopper

s dischargin g t

o th e system' s ra m feeder
. Th e weig h hoppe ri s equippe d with weig h cell s s o eac h charg e o f wast e ca n b e weighe d befor e it i s discharge d int

o th e ra m feeder
. Fugitiv

e emission s ar

e controlle d b

ya baghouse , cyclone , an d carbo n adsorptio n syste m connecte d t o thi s system
. Th e ram feede ri s a 25-inc h wid e b y42 inc h hig h (insid e dimensions ) rectangula rtub e operate d b ya hydraulicall ydrive n ram . Th e ra m tub e i s equippe d wit h a vertical , hydraulicall yoperate d charg e doo rnea rth e kil n end
. Thi s doo ri s opene d befor e th e ra m begin s advancin g to pus h a charg e int o th e kiln
. Afte rth e ra m ha s fullyretracted , a limi t switc h trigger s th e doo rt

o clos e s o a s t

o protec t th e ra m feede rfro m th e kiln' s radian t heat
. Th e ra m i s capabl e o f operatin g fro m 0-30 cycles/hour
. Th e to p fac e o

f th e ra m feede rha

s a 2 ' x2 ' openin g whic h receive s wast e charge s fro m th e hopper
. Th e ram feede risolatio n gate , th e charg e door , an d th e ra m operate i n sequence . A t th e beginnin g o

f a cycle , th e ra m i s full yretracted
. O n a "start " comman d fro m th e operato ro rth e programmabl e controller , th e ra m feede r isolatio n gat e open s t o receive a charg e o f wast e fro m th e hopper
. Th e gat e the n closes , th e charg e doo r opens , an d th e ra m begin s its advance
. Once th e ra m reache s its ful l extension , it begin s t o retract
. Whe n th e ra m i s full yretracted , th e charg e doo ri s close d an d th e cycl e ca n b e repeated
. Thi s system' s sequence d operatio n combine d wit h th e negativ e pressur e i n th e kil n preven t fugitive emission s fro m escapin g th e kil n ra m feede rsystem
. Th e ra m feede rals o receive s container s o f waste s delivere d b

ya n auxiliar

yfee d system
. Th e auxiliar yfee d conveyo ri s capabl e of handlin g charg e weights of 1 t o 10 0 pounds
. Th e syste m i s capabl e of handlin g charg e size s u p to 2 4 inche s i n diamete ran d 2 4 inche s tall
. Th e auxiliar yfee d conveyo ri s capabl e o f makin g 6 0 charge s a n hou ro ron e complete cycl e ever yminute
. 2.2 .1
. 3 Specialt yLiqui d Feed s Th e Specialt

yFee d Syste m associate d wit h Incinerato rNo
. 4 i s a Direc t Injec t Liqui d Fee d System
. 2. 3 Manufacturer , Mak e an d Mode l ofth e Incinerato r [4 0 CF R § 63.1207(f)(1)(iii)(A) ] 2.3. 1 Combustio n Chambe r an d Burner s [4 0 CF R §63.1207(f)(1)(iii)(B ) an d (C ) Incinerato rNo
. 4 feature s a two-stag e combustio n process . Ignitio n o f waste materia l takes plac e i n th e kiln , o rprimar ycombustio n chambe r(PCC)
. Asecondar ycombustio n chambe r(SCC ) serve s as a n "after-burner" fo rproces s gase s an d i s als o permitted t o incinerat e hig h Bt u liqui d waste
. Ignitio n o f th e wast e take s place a

t temperature s i n exces s o f 1600 degree s F
. Th e secondar ycombustio n chambe rmaintain s a minimu m temperatur

e of approximatel y187

5 degree s F
. Th e rotar ykil n i s fabricate d of carbo n steel
. I t ha s approximate dimension s o f 8'8 " O.D
. X 35 ' long
. It i s supporte d o n a one-degre e slop e b ytw o stee l tire s o rridin g rings. Eac h riding rin g rides o n tw o pair s o f stee l Q:taw97\ProJects\10002022\veoli a Performance Tes l Pla n U 4 073008 Revislon.do c


### VE S 00084 6Revision : 1 Date : Jul y 200 8 Section : 2.

0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 3 o f 1 5 trunnion s an d have a n approximate outsid e diamete ro f 9 feet 5 inches
. Th e thicknes s an d fac e widt h ofth e trunnion s are approximatel y6 inche s an d 9 inches , respectively
. Tabl e 2- 2 provide s a summar yofth e incinerato rdesig n specifications
. Th e kil n i s line d wit h approximatel y7 Vz inche s o f dens e abrasion-resistan t high-alumin a firebric k refractory
. Wit h thi s refractor

ysystem , th e kil n ha s a n insid e diamete ro f approximatel y7 feet an d a lengt h of approximatel y35 feet , a n integra l cross-sectio n are a of approximatel y38 square fee t an d a n interna l volum e o f approximatel y1,34

6 cubi cfeet
. Al l kil n feed s wil l ente rthroug h th e uppe rkil n fac e plat e whic h i s locate d o n th e fee d en d o f th e kiln
. Th e plat e contain s a primar

yburner , thre e liqui d fee d nozzle s (fo rpumpabl e sludge , aqueou s waste , an d hig h Bt u liqui d waste) , a ra m feede ran d a surg e vent
. Th e primar

yburne ri s equivalen t t

o a Nort h America n 'Fue l Directed ' burne ro f 2 5 MMBtu/hr
. an d burn s No
. 2 fue l oi l o rnatura l gas . Th e burne rsyste m i s supplie d wit h approximatel y4,00 0 acf m combustio n ai ra t a stati c pressure o f 20 " wate rcolum n (WC)
. Th e pilo t fo rth e primar

yburne rwil l bu m natura l gas . Th e fue l syste m fo rth e kil n (an d secondar ycombustio n chamber

) is.controlle d b

ya Factor

yMutua l approve d burne rmanagemen t syste m complet e wit h interlock s an d safet

yvalves
. 2.3. 2 Secondary Combustio n Chambe r(SCC ) Th e SC C i s a vertical , cylindrica l chambe rhavin g approximat e dimension s o f 10'-6 " O.D
. x71 ' high
. I

t i s fabricate d o f carbo n stee l an d line d wit h a n inne rcours e (ho t face ) o f approximatel ysi xinche s of hig h alumin a refractor yan d a n oute rcours e o f approximatel ytw o inche s o

f insulatin g refractory
. Wit h thi s installe d refractory , th e SC C ha s a n insid e diamete ro f approximatel ynin e feet
. Th e effective lengt h (ga s retentio n length ) ofth e chambe ri s approximatel y48 ' - 6"
. Consequently , th e SC C ha s a cross-sectio n are a of 6 4 squar e fee t an d a n effective volum e o f approximatel y3,08 4 cubi cfeet
. A t maximu m combustio n ga s flows , th e combustio n ga s residenc e tim e i s greate rtha n tw o seconds
. Combustio n gase s fro m th e kil n ente rth e botto m of th e SC C throug h a refractory-line d sid e duc t an d exi t fro m th e to p o f th e SC C throug h a refractory-line d duc t t o th e temperin g chamber
. Th e flooro f th e chambe ri s slope d to facilitat e th e remova l of as h an d solid s throug h a sla g tap
. Th e SC C i s equippe d wit h on e burne rmounte d o n th e sidewal l of th e chambe rnea rth e bottom
. Th e burne ri s a Tran e Therma l Model , o requivalent , wit h a desig n heat releas e o f approximatel y3 0 millio n Btu/hr
. Thi s burne ri s supplie d wit h No
. 2 fue l oi l o rnatura l ga s an d combustio n air
. A s wit h th e kil n burner , th e SC C burne ri s supplie d wit h atomizin g ai ran d i s equippe d wit h a burne r managemen t system
. Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof f whe n there i s a los s of flame , combustio n ai rsupply , fue l pressure , atomizin g ai rpressure , pilo t burne ro rI D fan
. Th e SC C burne ri s a high-intensity , vortextyp e uni t wit h a spi n van e assembly , locate d withi n th e windbo xt o impar t a n intens e rotar

ymotio n t o th e combustio n air
. Thi s rotar ymotio n an d th e burne rdesig n provid e complet e mixin g o

f ai ran d fuel , an d recirculatio n ofth e gase s withi n th e combustio n chambe rpromote s rapi d combustio n an d hig h hea t intensity
.

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### VE S 00084 7Revision : 1 Date : Jul y 200 8 Section : 2.

0 Veoli a ES Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 4 o f 1 5 2.3. 3 Locatio n o

f Combustio n Zon e Temperature Devic e [4 0 CF R §63.1207(f)(1)(xix) ] Th e pyromete rtha

t monitor s temperatur

e i n th e rotar

ykil n i s locate d top-cente ri n th e transitio n sectio n betwee n th e rotar

ykil n an d th e SC C abou t tw o feet downstrea m fro m th e exi t of th e kiln
. Th e thermocoupl e tha t monitor s temperatur

e i n th e SC C i s locate d o n th e wes t sid e ofth e chambe rnea rth e SC C exi t duct
. 2.3. 4 Hazardou s Waste Residenc e Tim e [40 CF R §63.1207(f)( 1 ){ix) ] Th e hazardou s wast e ga s residenc e tim e fo rth e Uni t 4 Rotar yKil n Incinerato ri s calculate d a s follows :

• Rotar yKil n Volum e -134 6 ft3
• Secondar

yCombustio n Chambe rVolum e - 308 4 ft 3
• Tota l Volum e - 443 0 ft 3
• Maximu m Flu e Ga s Flowrat e - 43,00 0 acf m (71 7 ft 3 /sec )
• Tota l Combustio n Zon e Residenc e Tim e = (443 0 ft 3)/(71 7 ff/sec ) = 6. 2 se c 2.3. 5 Combustio n Syste m Lea k Th e kil n itsel f i s equippe d wit h a doubl e sea l syste m that i s comprise d o f overlapping , adjustable , stainles s stee l sprin g plate s o n bot h th e fee d an d discharg e end s of th e kiln
. Th e sealin g edge s o f eac h plate ar e fitte d wit h a sintered-meta l wea rsho e simila rt o a brake sho e wit h th e inne rsea l restin g o n th e kil n shell
. Th e powdere d meta l formulatio n fo rth e sea l shoe s includ e graphite granules , whic h mak e th e shoe s self lubricating
. Th e voi d betwee n th e seal s an d th e oute rshel l ofth e kil n i s pressurize d t o furthe rpreven t fugitive emissions
. I n additio n to th e kil n sea l system , Uni t 4 als o utilize s a n induce d draf t fa n tha t maintain s a vacuu m of - 0. 5 t o -1. 0 inche s wate rcolum n whil e wast e i s bein g fire d int o th e system
. 2.3. 6 Emergenc y Safety Ven t Uni t 4 i s equippe d wit h tw o emergenc

yvents , on e locate d a

t th e kil n inlet whic h act s a s a n emergenc y pressure relief , th e secon d i s locate d a t th e to p ofth e SC C a s a therma l relief vent
. Th e emergenc

yven t a t th e kil n inlet woul d onl yb e require d fo ra n occurrenc e tha t overwhelm s th e abilit

yof th e I D fa n t

o contro l th e pressur e o

f th e kiln
. Th e ven t an d chute openin g i s designe d suc h tha t wast e fro m th e bul k solid s chut e woul d no

t imped e th e escapin g ga s flow
. Adeflecto rseparate s th e fee d flo wfro m th e ven t opening
. Th e entrainmen t of solid s throug h th e surg e ven t i s minimal
. A s a n extra precaution , th e exhaust openin g ofth e ven t i s angle d to provid e a horizonta l exit , therebyminimizin g solid s entrainmen t int o th e air
. Th e ven t i s kept close d b yweighte d louvers
. Thes e louvers wil l ope n onl yi f th e pressure i n th e kil n suddenl y rises beyon d th e compensatin g capacit yo f th e I D fan
. Alimi t switc h o n th e louvers wil l automaticall yshutof f al l wast e feed s to th e kil n an d SC C whe n th e ven t i s opened
. Th e incinerato ri s als o equippe d wit h a n emergenc ysafetyven t (ESV ) locate d a t th e to p o

f th e secondar

y combustio n chamber
. Thi s ES V i s a refractory-line d emergenc ytherma l relief ven t (TRV) whic h i s hel d i n th e close d positio n b

ya pneumati ccylinder
. Th e contro l valv e i n th e lin e supplyin g ai rto th e cylinde ran d th e cylinde rven t valv e whic h open s th e TR V ar e locate d i n th e contro l roo m fo reac h unit
. Valv e locks (wit h keys attached ) are utilize d t o dete rindiscriminat e operatio n o f thes e valves
. Openin g ofth e TR V allows ho t combustio n ga s t

o ven t fro m th e combustio n syste m durin g emergenc yshutdow n events
. Th e purpos e ofth e TR V i s t o protec t th e downstrea m APC S fro m excessiv e temperatur e situations
. Alimi t switc h o n th e TR V shut s of f al l wast e feed s t o th e syste m a s i t sense s tha t th e ca p i s opening
. Q:vTMv97\Projecls\1D002022\Veo!l a Performanc e Tes l Pla n U 4 0730D 8 Revision.do c


### VE S 00084 8Revision : 1 Date: Jul y 200 8 Section : 2.0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 5 o f 1 5
2. 4 Procedure s fo r Rapidl y Stoppin g Hazardou s Wast e Fee d Durin g Equipmen t Malfunctio n [4

0 CF R §63.1207(f)(1)(viii) ] Equipmen t malfunction s ar e identifie d b

yth e contro l system , observatio n of proces s contro l variables , o rb y regula rfiel d inspections
. I n th e even t of a mino requipmen t malfunctio n (e.g
. wast e fee d o rscrubbe rleaks) , th e contro l roo m operato r wil l b e notified
. Th e contro l roo m operato rwil l the n clos e th e wast e fee d valve s an d disabl e th e wast e fee d pumps . I n th e even t of majo requipmen t malfunctio n (e.g
. fire) , th e emergenc ysto p butto n locate d i n th e contro l roo m wil l b e pushed
. I f thi s butto n i s pushe d al l equipmen t wil l switc h to its fail-saf e position
. 2. 5 Ai r Pollutio n Contro l Equipmen t [40 CF R §63.1207(f)(1)(ili)(G) ] 2.5. 1 Ai r Pollutio n Contro l System s Description s Th e ai rpollutio n contro l syste m consist s o f a temperin g chamber , tw o spra ydrye rabsorbers , an d fabri cfilte r baghous e modules
. Th e ai rpollutio n contro l syste m neutralize s acidi ccompound s an d remove s particulate fro m th e exhaust gas . Two subsystems , th e spraydrye rabsorbe ran d th e fabri cfilter , carr you t th e chemica l neutralizatio n an d particulate remova l functions , respectively
. Athir d subsystem , th e lim e system , i s use d t o prepare an d provid e lim e slurr yt o th e spra

ydrye rabsorbe rfo rus e i n th e chemica l neutralizatio n process . Th e induce d draf

t fa n an d stac k

provid e th e mechanica l energ yrequire d t o transpor t th e flu e ga s throug h th e interconnectin g ductwork , t o it s eventua l discharg e poin t t o atmosphere
. 2.5.1. 1 Temperin g Chamber Th e temperin g chambe ri s a vertical , cylindrica l uni t designe d t o coo l th e combustio n gase s usin g a serie s o f interna l dual-flui d (wate ran d air ) spraynozzles
. Th e combustio n gase s ente rth e to p ofth e chamber , flo w downwar d throug h th e spra

ypattern an d exi t fro m th e botto m ofth e chamber
. Th e spra ypattern i s designe d to eliminat e direc

t contac t o f wate rwit h refractory , an d th e chambe ri s designe d to maintai n a dr ybotto m unde r al l operatin g conditions
. Tha t is , th e injectio n rate of spraywate ri s controlle d s o tha t i t i s completel yvaporize d an d earne d ou t o

f th e chambe ri n th e combustio n gases . Th e temperin g chambe ri s approximatel y49 ' hig h wit h 11 ' I.D
. an d i s fabricate d of % inc h nomina l plat e thicknes s carbo n stee l (AST M A36 ) an d line d wit h refractory
. Th e spraynozzle s an d extension s are fabricate d of 30 4 S S material
. Th e temperin g chambe ri s size d s o tha t a combustio n ga s retentio n tim e o f greate rtha n on e secon d wil l b e maintaine d a

t al l ga s flows
. Becaus e som e molte n particulat e material s i n th e combustio n gase s are coole d i n thi s proces s uni t to belowthei rfusio n point , som e solid s ar e generate d an d collecte d i n th e chamber
. Therefore , th e chambe rhas a con e botto m an d a .slid e gat e t o facilitat e th e remova l o f solids
. Thes e solid s ar e discharge d ont

o a conveyo rsystem , whic h transport s the m t o a hopper
. 2.5.1. 2 Lime Syste m Th e lim e syste m prepare s lim e slurr yfo rus e i n th e chemica l neutralizatio n proces s i n sufficien t suppl yan d concentratio n to maintai n continuou s flu e ga s treatmen t i n th e spra ydrye rabsorber
. Th e syste m ha s bee n designe d fo rbatc h mixin g t o provid e thi s service
. Veoli a utilize s hydrate d lim e a s its neutralizin g agen t in f th e ai rpollutio n contro l systems
. Th e keyneutralizatio n paramete rofth e hydrate d lim e i s th e "Ca O Equivalent'
. Figure 4- 1 i s th e specificatio n shee t fo rth e hydrate d lim e tha t Veoli a uses . Veoli a ha s use d thi s specifi c produc t fo rove r2 0 years an d plan s to continu e wit h its use ! Although , i f Veoli a doe s chang e supplier s o rtyp e Q:\mw97VProjects\10002022VVeoli a Performanc e Tes t Pla n U 4 07300 8 Revision.do c 

### VE S 00084 9Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC TPerformanc e Tes t Pla n Pag e 6 o f 1 5
o f lim e i n th e future , i t woul d have a "Ca O Equivalent " specificatio n equa l to o rgreate rtha n th e 72.6 % show n o n Figure 4-1
. Hydrate d iim e i s store d i n a storag e bi n abov e th e lim e preparatio n area . Th e storag e bi n i s size d to hol d enoug h hydrate d iim e t

o maintai n severa l days o f syste m operatio n a

t th e maximu m combustio n rat e ofth e incinerator
. Lim e i s discharge d throug h th e conica l storag e bi n bottom
. Th e flow o f th e materia l fro m th e bi n i s aide d b ya vibratin g "live bottom, " o rbi n activator
. Avariabl e spee d screwfeede ri s use d to mete rth e hydrate d lim e i n th e proportion s require d fo rbatc h mixin g lim e slurry
. Th e lim e i s mixe d wit h wate ri n a tan k beneat h th e lim e storag e bin
. Th e scre wfeede rspee d an d th e rat e tha t wate ri s adde d to th e lim e slurr ytan k ar e variabl e s o tha

t th e desire d lim e solid s concentratio n ca n b e achieve d i n th e tank
. Th e variabl e fee d adjustments allo wwate ran d lim e t o b e adde d t o th e lim e slurr ytan k a t a rat e tha t wil l allowa batc h mode o f mixing
. A n agitato ri s provide d i n th e slurr ytan k t o mixth e wate ran d lim e an d t o maintai n th e suspensio n o f lim e solids
. Th e mixe d lim e slurr yi s pumped a

t a continuou s rat

e o f flo wthroug h a recirculatio n loo p t o th e SD Anozzle s a

t a rate o f u p to 1 0 gp m t o eac h nozzle
. 2.5.1. 3 Spra yDr

yAbsorbe r Uni t 4 i s equippe d wit h tw o SprayDrye rAbsorber

s (SDA) locate d immediatel ydownstrea m o f th e Temperin g Chamber
. Eac h SDAuni t i s fabricate d o f 3/ 8 inc h carbo n steel
. Th e functio n of th e SDA s i s to :

• Furthe rcoo l th e combustio n gase s fro m 600-800° F to 300-500°F , • Neutraliz e an d remove HC I an d othe racid s fro m th e combustio n gases , • Remove a portio n of th e particulat e (fl yash ) fro m thes e gases . Slurr yflowt o eac h spraydrye rabsorbe r(SDA) i s metere d b ya flowcontro l valve t

o obtai n th e prope rfee d concentratio n to th e spra

ydrye rabsorber
. Manua l adjustmen t t o th e flow i s mad e a s a functio n o f th e SD A outlet temperatur

e an d a s a functio n o

f th e output fro m a hydrochlori caci d (HCI ) analyze ri n th e ga s duc t downstrea m o

f th e fabri cfilter
. Sinc e th e Temperin g Chambe raccomplishe s initia l coolin g o f th e gases , n o additiona l wate ri s use d i n th e SDA s fo rga s temperatur e control
. Th e combine d units ar

e size d to remove mor

e tha n 82 0 Ib/hr
. of chlorin e fro m th e combustio n gases . Eac h SD Ai s approximatel y72 ' hig h b y107 " i n diameter
. Eac h uni t include s a head section , an d a 60 ° conica l hopper
. Eac h SD Achambe rha s on e acces s doo ri n th e uppe rsection
. Eac h hoppe rha s on e acces s door , a flange d clean-ou t port , an d a drai n connection
. Th e SD Ahea d sectio n consist s o f a flange d inlet connectio n an d a ho t gas inlet plenum
. Th e dual-flui d atomizin g nozzle s includ e stainles s stee l housing s an d stellite d inserts
. Th e nozzle s ar e assemble d t o permi t fiel d remova l fro m th e piping
. Th e tw o lim e slurr

ypipin g headers have automati cisolatio n valves
. Combustio n gase s ente rth e top o f eac h of thes e units , flowdownwar d throug h a centra l duc

t an d ar e disperse d symmetricall yfrom'thi s duc t int o th e absorbe rchambe ra t a velocit yan d directio n tha

t assure s optima l contac

t wit h th e clou d of atomize d lim e slurr ydroplets introduce d into th e chambe rb ydual-flui d (lim e slurr yan d air ) nozzles
. Th e gase s the n flowdownwar d throug h eac h absorbe rchambe ran d exi t throug h a botto m sid e duct
. A s th e gase s contac t an d pas s throug h th e clou d o f atomize d lim e slurry , th e wate ri n th e slurr yevaporates , coolin g th e gases . Simultaneously , th e lim e i n th e slurr yreacts wit h th e hydroge n chlorid e i n th e gase s to produce calciu m salts
. Som e o f th e resultin g dr

ymaterial , consistin g o

f calciu m salts , fl yas h an d exces s lime , fall s to th e conica l botto m of eac h unit
. Th e dr ymateria l fro m eac h uni t i s discharge d t o a conveyo rsyste m whic h transports i t t o a dum p traile ro requivalen t typ e system
.

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### VE S 00085 0Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veoli a ES Technical Solution

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2.5.1. 4 Fabri cFilte r Ga s exhauste d fro m th e spra ydrye rabsorber

s i s distribute d t

o tw o fabri cfilte rmodules connecte d i n parallel
. Eac h modul e i s divide d int o thre e compartment

s connecte d i n parallel , whic h contai n multipl e fabri cfilterbag s throug h whic h th e combustio n gase s pas s t o remov e particulates
. Withi n eac h compartment , th e ga s i s passe d throug h Teflon-coate d fiberglas s clot h bags
. Th e gas passe s fro m th e outsid e t o th e insid e ofth e filte r bags
. Particulat e entrained i n th e gas strea m i s mechanicall ydeposite d o n th e outsid e ofth e filte rbag s as th e ga s passe s throug h th e cloth
. Eac h compartment ha

s a clea n ai rplenu m an d housin g sectio n t o contai n approximately308 bags
. Eac h bag i s approximatel y5 " i n diamete rb y5 ' long
. Th e baghouse s ar e fabricate d fro m 3/16 " mil d stee l plate , o f welded construction , ga s tigh t an d stiffene d to withstan d th e maximu m operatin g negativ e pressure . Eac h compartmen t ha s a tube sheet tha t support s th e bag s an d provide s forto p bag/cag e removal
. Acces s t o th e clea n ai rplenu m i s vi a a bolte d acces s door
. Eac h traile rmounted uni t contain s th e compresse d ai rheaders , ga s inlet an d outle

t manifolds , an d th e conveyor . Th e fabri cfilte rcleanin g mechanis m utilize s jets o f ai rt o clea n th e filte rbags
. Periodically , th e cleanin g sequenc e wil l b e initiated
. Th e sequence i s starte d whe n th e differentia l pressur e acros s th e filte rreache s a predetermine d setpoin t of approximatel y8.0 " w.c . o rwhe n th e operato rinitiate s a cycle
. Th e controlle rthe n sequence s t

o eac h ro wo f filte rbag s i n eac h module , releasin g a burs t o f ai ropposite t

o th e directio n o

f ga s flow. Th e quickl yrelease d burs t o f ai rdislodge s dus

t cak e o n th e exterio ro

f eac h ba g a s it travel s fro m th e to p t o th e botto m ofth e bags
. Release d fro m th e bag , th e dus t cak e fall s b ygravit yint o th e hoppe ra

t th e botto m o f th e module
. Fro m ther

e it i s discharge d to a conveyo rsyste m whic h transport s i t to a dum p trailer , o r equivalen t typ e system
. Treate d b yth e spra ydrye rabsorber

s an d filtere d b

yth e fabri cfilters , th e cleane d flu e ga s exits th e fabri cfilte r compartment

s to a n outle

t manifol d fo rexhaust
. 2.5.1. 5 Carbo n Injectio n Th e carbo n injectio n syste m wil l ai rinjec t activate d carbo n int

o th e plenu m immediatelyupstrea m o f th e baghouse s an d allowfora mor e efficien t mean s o

f controllin g Dioxin/Fura n an d mercur yemissions
. Thi s syste m wil l b e controlle d b y a n existin g PL C whic h wil l contro l th e input of activate d carbo n to th e baghous e inle t plenum
. 2 to 2 0 pound s pe rhou ro f powdered activate d carbo n wil l b e ai rinjecte d int o thi s plenu m an d allowfo rdirec

t contac t with th e stac k

gase s exitin g th e SDA's
. Th e amount of carbo n i s dose d i n a dust-fre e manne rint o a lo wpressur e ai rstrea m vi a pneumati ceduction
. Th e educto ruse s a blowe rfo rth e motiv e air
. Hig h an d lo

wai rpressur

e switche s ensur

e tha t th e blowe ri s operatin g correctl yan d tha t th e carbo n deliver

ysyste m i s clea rfro m obstruction
. Th e minimu m hig h pressur e settin g i s 4 psi g an d th e maximu m lowpressur e settin g i s 1 inc h wate rcolumn
. Th e carbon/ai rstrea m wil l the n trave l throug h pipin g to th e injectio n nozzl e into th e ductwork
. Th e carbo n wil l contac t th e ga s strea m exitin g th e SDA' s an d allow.fo rth e adsorptio n o f an ydioxin/furan s an d mercur ytha t might b e presen t i n thi s stream
. Adsorptio n wil l continu e as th e stac k gase s procee d throug h th e baghouses
. Th e clea n stac k ga s wil l exi t th e fina l stac k vi a th e induce d draf

t fa n an d th e capture d solid s wil l b e discharge d fro m th e baghouse s vi a th e screwconveyin g syste m into a n enclose d dum p traile rfo rdisposa l a t a Subtitl e C
. landfill
. 2.5.1. 6 Induce d Draf t Fa n an d Stac k Th e induce d draf

t fa n an d stac k

are locate d downstrea m o f th e fabri cfilter
. Combustio n gase s ar e drawn throug h th e syste m b

ya 40 0 h p induce d draf

t (ID ) fan , rated ' a

t 53,00 0 acf m a

t 400 ° F saturated , an d 25 " wate r colum n pressure . Th e induce d draf t fa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s Q;Vnw97\Projects\10DD2022Weoll a Performanc e Tes t Pla n U 4 07300 B Revision.do c


### VE S 00085 1Revision : 1 Date : Jul y200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC TPerformanc e Tes t Pla n Pag e 8 o f 1 5 throug h th e spra

ydrye rabsorber , fabri cfilter , an d al l interconnectin g ducts
. Th e I D fa n include s a n inle t volum e contro l dampe rto b e use d t o contro l th e velocit yofth e ga s withi n th e ductin g an d treatmen t devices
. Treate d gase s ar

e exhauste d fro m th e induce d draf t fa n t o th e atmospher

e throug h a 100-ft
. hig h stack
. Th e stac k diamete rfo rUni t 4 i s 4 8 inche s I.D
. Th e stac k i s equippe d wit h instrumen t samplin g port s an d a samplin g platform fo remission s testing
. Figur e 5- 1 provide s detail s o n th e desig n an d sampl e por t location s an d configuration s fo rth e stack
. 2. 6 Stac k

Emission s Monitorin g [40 CF R §63.1207(f)(1)(iii)(H) ] Th e continuou s emission s monitorin g (CEM ) syste m consist s o f sampl e probes , sampl e deliver yan d conditionin g apparatus , an d ga s analyzers
. Sample s ar e extracte d fro m th e transitio n ductin g locate d betwee n th e I D fa n an d th e stack
. ACE M performance test an d qualit yassuranc e progra m has bee n implemente d i n accordanc e wit h th e Appendi x t o Subpart EE E of Par t 63—-Qualit

y Assuranc e Procedure s fo r Continuou s Emission s Monitors Use d fo r Hazardou s Wast e Combustors . Response s fro m eac h CEM S wil l b e fe d t o th e Contro l Syste m (CS ) wher e the.C O hourlyrollin g averag e i s calculate d an d interlocke d t o th e wast e fee d cutof f valve s a s par

t ofth e Automati cWaste Fee d Cutof f Syste m (AWFCO ) discusse d i n Sectio n 2.8 , below
. Th e followin g provide s a brief descriptio n ofth e CEM S instruments includin g th e operatin g rang e an d measuremen t principal
. 2.6. 1 CE M Syste m Descriptio n Th e Continuou s Emission s Monitorin g System s (CEMS ) currentl ybein g utilize d a t Incinerato r4 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , except opacity , ar e extractive device s mounte d i n th e ductwork betwee n th e I D fa n an d th e stack
. Th e tabl e below summarize s th e analyze rspecifications
. Th e opacit

ymonito rcontinuousl ymeasure s th e stac k ga s opacit

yan d report

s th e measurement

s to a n indicato ran d a recorder
. A n opacit ytha t exceed s a preset limi t trigger s a n alarm an d interlock
. Carbo n monoxid e an d hydroge n chlorid e ar e monitore d wit h extractiv e non-dispers e infrare d analyzers
. Tota l hydrocarbo n i s monitore d wit h a n extractive flam e io n detecto ranalyzer
. Oxyge n i s monitored wit h a zirconiu m oxid e cell
. Stac k ga s flowrate i s continuousl ymonitore d usin g a n anuba rtha t send s a 4-2 0 m Asigna l t o th e PL C whic h converts th e signa l to acfm
.

Tabl e 2-1 Veoli a E S Technica l Solution s - Continuou s Emission s Monitors Paramete r Curren t Mfg . Rang e Principl e Oxyge n COS A 0-25 % Electrochemica l Carbo n Monoxid e Echoche m M C 3 0-20 0 ppmv 0-300 0 ppmv Infrared Tota l hydrocarbon s Thermoelectro n 0-10 0 ppmv FID/lnfrare d Hydroge n chlorid e Echoche m M C 3 0-100 0 ppmv Infrared Opacit y Teledyn e 0-100 % Whit e ligh t Stac k ga s flo w PSE/Rosemoun t 0-55,00 0 acf m Pressure dro p Q:\mvv97\ProjeclsY100D2022\veoli a Performance Tes t Pla n U 4 073008 Revision.do c 

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### 2. 7 Process Monitorin g and Contro l Th e facilityi s equippe d wit h a state-of-the-ar t monitorin g an d contro l system , whic h facilitate s compliance wit h permi t conditions , an d otherwise , collect s proces s contro l information , facilitate s efficien t operatio n an d detects an d prevent s damag e t

o th e facility
. Th e syste m consist s o f thre e majo rcomponents :

• Ahuman-machin e interface (HMI ) system , • Programmabl e logi ccontroller' s (PLC's) , an d
• Ahig h spee d etherne t cabl e connects al l contro l syste m components Th e desire d contro l function s ar e implemente d throug h th e HM I system
. Al l digita l contro l an d emergenc y interlocks ar

e accomplishe d b

yth e PLC
. Th e contro l syste m i s capabl e o f monitorin g th e "operationa l envelope " o f th e incinerato ran d i s capabl e o f performin g a numbe ro

f activitie s including :

• Contro l roo m indicatio n o f processo rsensors locate d withi n th e incinerato rsyste m (suc h a s pressure indicatio n of a fiel d installe d pressure transmitter) ;
• Proces s controlle rfo rsingl e instrumen t loop s o ra n individua l sub-system , suc h a s a temperatur e contro l loo p involvin g a senso rreadin g fro m on e temperatur e transmitte raffectin g th e functio n o f on e temperatur

e contro l valve ; an d
• Alar m fo ra n exceedanc e of a designate d setpoint , suc h a s a hig h pressure o rlowtemperature
. Th e proces s contro l compute rwil l continuousl ycontro l an d monito rth e operatio n of th e incinerator
. Whe n out of-rang e condition s exist , it wil l notif yth e operato ro

f thos e conditions
. Th e proces s contro l compute ri s programme d t

o shut-dow n equipmen t (i.e. , brin g th e syste m into a saf e mode) whe n designate d parameter s ar e exceeded , whic h i s a protective mechanis m agains t potentia l equipmen t damage , operatio n outsid e of
. permi t limits , o rcondition s tha t migh t lea d to a releas e t o th e environment
. Continuou s monitorin g ofth e incinerato ran d scrubbe rsyste m i s a n importan t aspect ofth e syste m design
. A digita l readou t of al l monitorin g instrumentatio n i s displaye d o n th e mai n contro l screen . A n audibl e an d visua l alar m alert s th e incinerato roperato rto significan t deviation s fro m norma l operatin g conditions
. Thi s syste m allows a n immediate respons e t o advers e condition s b

yth e operator
. Automati cwast e fee d cut-of f an d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m a t o rprio rt o reachin g permi t limi t levels
. Monitorin g method s an d calibratio n frequencie s ar e liste d i n Tabl e 2-3
. Th e Incinerato rha s a n independen t proces s contro l compute rtha t interface s to th e Allen-Bradle y programmabl e controllers
. Th e proces s compute ri s capabl e of controllin g th e incinerato ri n cas e of a failur e i n a HM I server , thi s compute rrun s a RSVIE W HM I contro l softwar e tha t provide s operato rinterface t o al l instrumentatio n an d controls
. 

### 2. 8 Automati c Wast

e Fee d Cut-of f Syste m [4

0 CF R §63.1207(f)( 1 )(iii)(F) ] Th e incinerato rha s a n Automati cWast e Fee d Cut-Of f (AWFCO ) Syste m tha

t wil l shu t waste feed s of

f i n th e even t certai n operatin g parameter s deviat e fro m allowabl e se t points
. Th e PL C continuousl ymonitor s operatin g parameters , makin g adjustments t o th e proces s a s neede d fo rprope rcontrol
. Alar m logi ci s incorporate d into th e PL C syste m t o automaticall yinitiat e a n AWFCO
. Tabl e 2- 3 summarize s th e curren t

Q:Vnw97\ProjectsMD002022\Veoll a Performanc e Tes t Pla n U 4 O7300 8 Revision.do c 

### VE S 00085 3Revision : 1 Date : Jul y200 8 Section ; 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC TPerformanc e Tes t Pla n Pag e 1 0 o f 1 5 AWFC O se t points
. AWFC O limit s have bee n establishe d base d o n severa l factor s tha t ar e summarize d below
.
• Regulatory/permi t limit s - establishe d t

o compl ywit h existin g permits
. A n exampl e o f thi s typ e o

f limi t i s th e lowtemperatur

e limit , belo

wwhic h wast e canno

t b e fe d unti l th e prope rlimi t i s re-established
. I n addition , th e HWC MAC Tregulation s requir e tha t th e AWFC O syste m b e interlocke d wit h th e spa n o f eac h proces s instrument tha t i s par t ofth e Continuou s Monitorin g Syste m (CMS)
. Alistin g o f thes e CM S instrument

s an d thei rinterlocke d spa n setpoints i s maintaine d a s par t o f Veolia' s Operatin g Record
. • Proces s safet

ylimit s - establishe d t

o assure , proces s equipmen t i s protecte d an d unsafe operatin g condition s d o no

t occur . A n exampl e of thi s i s inadequate exces s ai ri n th e combustio n chambe rtha t ca n lea d t o fue l rich conditions
. • Utilit yo rPowe rfailur

e - establishe d to facilitat e a controlle d shutdow n o f th e proces s durin g los s of proces s air , steam , wate ro relectricity
. A n exampl e o f thi s i s th e los s o

f instrumen t ai rtha

t i s necessar yfo rcertai n type s o

f proces s instruments to functio n properly
. Waste s wil l no t b e re introduce d int

o th e incinerator

s unti l prope roperatio n o

f ke yinstrument

s i s re-established
. I n additio n to th e AWFC O system , operator s ca n manuall yshutdow n wast e feed s o rth e entir e proces s shoul d thi s b e needed
. 2.8. 1 AWFC O Syste m Testin g Veoli a test s th e AWFC O system s bi-weekly , a s weekl ytestin g woul d undul yinterfer e wit h operation s b

y ceasin g an d restartin g waste feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l gas durin g th e downtime , an d increasin g operatin g costs
. Testin g ofth e AWFC O syste m i s a time-consumin g an d manpowe rintensive process . Th e curren t testin g progra m ha s bee n i n plac e unde rth e RCR Apermi t fo rove r2 0 year s an d has prove n t

o b e adequat e i n detectin g problems
. Thi s rational e i s include d i n th e facility' s AWFC O Plan
. I n som e case s thi s testin g occur s mor e frequentl ydependin g o n how ofte n actua l AWFCO s occu ra t th e unit
. Pe rth e require d frequency , incinerato rpersonne l chec k th e functionalit

yo f AWFC O logi ctha

t i s par t o f th e incinerator' s PL C syste m to mak e sur e tha t shoul d proces s condition s deviat e fro m allowabl e limits , th e compute rlogi cwil l initiat e waste fee d shutdown s a s required
. Thi s i s accomplishe d b

ymanuallysimulatin g proces s condition s tha t are outsid e allowabl e limits an d observin g an d documentin g whe n th e contro l o rbloc k valve softwar

e logi co n th e wast

e fee d lin e begin s t o initiate valv e closure
. Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e ar e documente d b

yoperatin g personne l to satisf

yregulator

yrequirements fo rsyste m testing
. Result s o f thi s testin g are documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par t o f th e unit' s Operatin g Record
. 

### 2. 9 Ai r Pollutio n Contro l Equipmen t Maintenanc

e Practice

s [4 0 CF R §63.1207(f)(1){iii)(G)] 2.9. 1 Progra m Overvie w Once equipmen t i s installe d an d operational , Veoli a utilize s a n extensive preventativ e maintenance (PM ) progra m t o kee p equipment operationa l an d preven t breakdown s an d failures
. Base d upo n th e typ e o f equipmen t an d historica l operation s an d maintenance experience , schedule s fo rvariou s inspectio n an d P M activitie s are followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenance historie s o n equipment , routin e inspectio n an d lubricatio n program s fo rhig h wea requipmen t an d non-destructive testin g o f

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### VE S 00085 4Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technical Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Plan Pag e 1 1 o f 1 5 pipin g an d vessel s usin g technique s like ultrasoun d to asses s integrity
. Th e frequenc yo f thes e activitie s varie s dependin g upo n th e equipment , P M activit yan d th e incinerator' s shutdow n schedule
. Fo rexample , frequen t (i.e. , weekly ) instrumen t an d certai n mechanica l equipmen t check s ar e mad e fo rcritica l proces s items
. Lubrication , vibratio n analysi s an d othe rmechanica l integrit ycheck s are don e a

t longe r frequencie s lik

e monthl yo rquarterly
. An d finally , suc h item s a s inspectin g refractor ybric k fo rwear , ar

e typicall yperforme d whe n th e entir e incinerato ri s shu t down fo rmaintenance
. 2.9.2 Tes t Progra m Preparatio n Activitie s Prio rto testing , instrumentatio n associate d wit h ke yparameter

s o f th e test wil l b e checked , calibrated , o r replaced , a s appropriate , t o ensure prope roperatio n of th e instrumentatio n durin g testin g (i.e. , waste fee d flowmeter s an d scales , CEM's , pressure transmitters , thermocouple s an d pyrometers , stac k flowmeters , etc.)
.

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### VE S 00085 5Revision : 1 Date: Jul y 200 8 Section ; 2.

0 Veolia ES Technical Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 2 o f 1 5
Tabl e 2-2 Technica l Informatio n Summary o n Incinerato r No . 4 Manufacture r Trad e Wast e Incineratio n Mode l No
. TWI-2000 , Serie s 2 Typ e Rotar yKil n Dat e o f Manufacture 198 9 Dimension s Primar yChambe r Secondar yChambe r Externa l Lengt h 35 ' 48'6 " Externa l Diamete r 8'8 " 10'6 " Interna l Diamete r T 9 ' Cross-sectiona l are a 3 8 squar e fee t 6 4 squar e fee t Burner s Primar yChambe rBurne r Secondar yChambe rBurne r Manufacture r Nort h America n Tran e Therma l Siz e 12. 0 Millio n Btu/h r 3 0 Millio n Btu/h r Fue l Natura l Ga s Natura l Ga s Prime rMove r Induce d Draf t Fa n 4,00 0 acf m @ 400 D F saturated , 2 0 in
. wate rcolum n

Q:\rnw97\Projecls\

1 rj002O22Weoli a Performanc e Tes l Pla n U 4 07300 B Revisiondo c 

### VE S 00085 6Revision : 1 Date: Jul y 200 8 Section : 2.

0 Veolia E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 3 o f 1 5
Tabl e 2- 3 Curren t AWFC O Parameter s an d Limit s fo r Incinerato r No . 4 i Syste m Devic e Units Cutof f Limits Calibratio n

Frequenc y Primar y Combustio

n Chambe

r Temperatur

e Pyromete

r ° F <1,24 0 (one-minut

e average

) <1,50 7 (HRA

1) £2,400 (instantaneous

) Annuall

y Secondar y Combustio

n Chamber Temperatur

e Typ e KThermocoupl

e ° F £1,82 5 (one-minut e average

) <1,88 6 (HRA

1) £2,400 (instantaneous

) Annuall

y ' Primar y Combustio

n Chambe

r pressur e Pressur

e transmitte

r in . w.c. £ atmospheri c (instantaneous

) Quarterl

y j [Secondar

y Combustio

n Chambe

r pressur e Pressur

e transmitte

r in . w.c . > atmospheri c (instantaneous

) Quarterl

y | [Spra y Drye r Adsorber Inle

t Temperatur

e Typ

e KThermocoupl

e ° F > 1,20

0 (on e minut e average

) Annuall

y | Spra y Drye r Adsorbe

r Outle t Temperatur

e Typ e KThermocoupl

e ° F £ 50

0 (on e minut e average

) >43 5 (HRA ) Annuall

y Total Pumpabl

e Wast e Feedrat e Mas

s flo wmeter/scale

s lb/h r >426 2 (HRA ) Annuall

y Tota l Wast e Feedrat

e Mas s flowmeter/scale

s Ib/hr >14,80 2 (HRA ) Annually

/ Quarterl y |LV M Feedrat

e Mas s flowmeter/scale

s Ib/hr >12 0 (1 2 HRA

) Annually

/ Quarterl y SV M Feedrat

e Mas s flowmeter/scale

s Ib/hr >117(12HRA ) Annually

/ Quarterl y | Mercur y Feedrat

e Mas s flo wmeter/scale

s Ib/h r >0.067(12HRA ) Annually

/ Quarterl y | Chlorin e Feedrat e Mas s flowmeter/scale

s ib /h r >274(12HRA ) Annually

/ Quarterl y j Ash Feedrat

e Mas s flowmeter/scale

s lb/h r >B,777(12HRA ) Annually

/ Quarterl y j Carbo n Feedrat

e Mas s flo wmete r Ib/hr > 6 (HRA ) Quarterl

y j Carbon Injectio

n Syste m Maximu m Lo

w Pressur e Pressur e Switc h in . w.c . > 1 Quarterl y Carbon Injectio

n Syste m Minimum High Pressur e Pressur e Switc h psig < 4 Quarterl y Chlorin e Fee d t o Slurr y Flo wRati o Flo

wMete r Rati

o >44.

4 Annuall y J Combustio

n Ga s Flo wRat e Anuba r acf

m £43,90 0 (HRA ) Annuall

y Stack Ga s Exces s Oxyge n Zirconiu m Oxid e fue l cel l % £ 3 (on e minut e average

) Quarterl

y Stac k carbo n monoxid

e Infrare d ppm

v £100 (HRA ) £500 (on e minut e average

) Quarterl

y Stac k Hydrocarbo

n FI D ppm v £1 0 (on

e minut e average

) Quarterl

y j Stac k ga s opacit y Whit e Ligh t % £1 0 (on e minut e average

) Quarterl

y I

Q:\rrMi971ProJectsU00n2022\veoll a Performance Tes t Pla n U 4 073008 Revisfon.do c 

### VE S 00085 7Revision : 1 Date : Jul y 200 8 Section : 2.

0 Veolia E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 4 o f 1 5
j Syste m Devic e Unit

s Cutof

f Limit s Calibratio n

Frequenc y Stac k hydroge n chloride 2 Infrare d ppm

v >10

0 (HRA ) >50 0 (on e minut e average

) Quarterl

y Liqui d feedrat e Mas s flo wmete r lb/h r > 1,70 0 Annuall

y Sludg e feedrat e Mas s flowmete

r Ib/h

r > 1,10

0 Annuall

y Drumme d and Bulk

Solids Feedrat

e Scal e Ib/h

r > 15,00

0 Quarterl

y | Fabric filte

r pressur e dro p Delt a P transmitte

r in . w.c . <

2 or > 1 0 (on e minut e average

) Quarterl

y
1 HR A mean s "hourl y rollin g average " a

s calculate

d b y averagin

g th e previou s 6 0 one-minut

e averag e values. 2 Thi s is a RCRA permi

t limi t only .

Q;\nTO87\ProjectsM0002n22tt/eoli a Performance Tes t Pla n U 4 07300 8 Revision.do c 

### VE S 00085 8Revision : 1 Date : Jul y 200 8 Section : 2.

0 Veolia E S Technica l Solution s Uni t 4 HW C MAC TPerformanc

e Tes t Pla n Pag e 1 5 o f 1 5 Figur e 2- 1 Hydrate d Lim e Specification s

MTSSffSSlPP I HOTKE Y PLAS T

Hydrate d Lijr. e User s &\?Vi£

ja'ii d KJtie-a r raeraisal s CtKie x 2i>«iiiXi**tJ.<;J:i clienrAo.ttl . Analysi s t o 97 , 2 »



# . . ..... . .72. 8 L a ?3. 6

73. 3 C

O 74 . 3 CaCO s..... . 0 . B S t o i.7 5 0.0 8 tf l O - I O S 3 5S<fuiv«Xea t . . 

# . ... . . . . O.OI B t o 0 . OS.- l a^o a : . . . . 0.-3 8 t o o.as . a^o a : . . . . - 0.2 0 t o 0.3 0 o.or t o 0.3. 0 a. 4 0 H i O.C S Zru o E^ C ... . 

# . . . . . . . 0.3 0 - I. U 0.9 3 L O 0 .01 2 •0-001 5 t o 0.002 5 c.3.1 PfcvsSevjt l Atalvsl-i s Kictu s 10 0 ICO . SS . i > mes h 92. o t>ilu-Ai fcjf

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Q:\mw97\Projecte\10002022\VBoll a Performanc e Tes t Pla n U4 073008 Revision.do c 

### VE S 00085 9

## CONTINUOU S MONITORIN G SYSTE M QUALIT Y CONTRO L PROGRA M



## Prepare dfor : Veoli aE S Technica

l Solutions , LL C Sauget , Illinoi s

Preparedby : Frankli n Engineering Group , Inc . Franklin , Tennesse

e

October200

8TABL E O F CONTENT S
1.0 INTRODUCTIO N AN D BACKGROUN D 1 1. 1 SUMMAR Y O F FACILIT Y INFORMATIO N 4 1.1.1 Fixed

Hearth Incinerators 4 1.1.2 Rotary Kiln Incinerator. 5 1. 2 CM S INSTRUMENTATIO N 6 2. 0 CM S CALIBRATIO N AN D PREVENTIV E MAINTENANC E 1 3 2. 1 CM S CALIBRATIO N , 13 2.1.1 Initial

CMS Calibration 13 2.1.2 Subsequent

CMS Calibration. 13 2.1.3 CEMS Calibration Audits and Calibration ,14 2. 2 CM S CALIBRATIO N AUDIT S 1 4 2. 3 PREVENTIV E MAINTENANC E 1 9 3. 0 CM S RECORDKEEPIN G AN D REPORTIN G 2 0

3. 1 RECORDKEEPIN G 2 0 3. 2 REPORTIN G - 2 1 4. 0 CM S CORRECTIV E ACTION S 2 4

(
.


### VE S 00086 1

### INDE X O F TABLE S
TABL E 1 - 1 REGULATOR Y CHECKLIS T FO RTH E CM S Q A PROGRA M 2 TABL E 1 - 2 CM S INSTRUMEN T SPECIFICATION S 7 TABL E 2- 1 CM S CALIBRATIO N AUDI T REQUIREMENT S 1 5 TABL E 3- 1 REPORTIN G REQUIREMENT S 2 3



### ii i VE S 00086 2

### 1. 0 INTRODUCTIO N AN D BACKGROUN D Veoli aE S Technica

l Solutions

, LL C (Veolia

) own s an d operate

s tw o fixed heart

h incinerator

s (Unit s 2 an d 3 ) an d arotar y kil n incinerato

r(Uni t4 ) a tit s facilit y locate d i n Sauget , Illinois . Th

e incinerator

s ar e subjec tt o th e Nationa

l Emission

s Standard

s fo r Hazardou

s Ai rPollutant

s (NESHAP) forHazardou s Wast e Combustor

s (HWC) , Par

t63 , Subpar tEE E ( § 63.120

0 t o § 63.1221). Th

e NESHA Pspecifie

s emission

s standard

s whic h reflec temission

s performanc

e o f Maximu

m Achievabl

e Contro l Technologie

s (MACT) , an

d is commonl

y referre d t o a s th e HW C MACT . Hazardou

s wast e combustor

s ar e require d [pe r§ 63.8(d)(2)

] t o establis h an d implemen

ta Continuou

s Monitorin

g Syste m (CMS ) Qualit

y Contro l (QC ) Program

. Th e purpos e o f th e Q C Progra

m i s t o outlin e procedure

s use d t o verif y tha tth e CM S ar

e properl y installed, calibrated

, an d collectin

g accurat

e dat ao n a n ongoin

g basis. Th

e CM S performanc

e evaluatio

n tes tpla n wa s submitte

d a s par tof th e Comprehensiv

e Performanc

e Tes tPlan. Th e Q C Progra

m demonstrate

s Veolia' s complianc

e wit h th e requirement

s se tfort h in § 63.8(d)(2) , a

s wel l a s th e additiona

l qualit y assuranc

e (QA ) requirements

. Th e Q C Progra m i s require

d t o contai n description

s of initia l an d subsequen

tCM S calibration

, calibratio

n drift , preventiv

e maintenance

, dat arecording

, calculation

s an d reporting ; an

d acorrectiv

e actio n pla n formalfunctionin

g CMS . Tabl

e 1- 1 present

s th e regulator

y reference s relate d t o th e Q C program

, followe d b y th e sectio n o f thi s pla n tha taddresse

s eac h specifi c requirement

. Som e reference

s ar e mad e t o othe rHW C MAC T require d facilit y operatin g plans . This Q C Progra

m i s intende d t o fulfil l th

e requirement

s of . § 63.8(d)(2) , an

d include s informatio

n relate d t o th e procedure

s foreac h ofth e followin

g operations :

• Initia l an d subsequen

tcalibratio

n o f th e CM S
• Determinatio

n an d adjustmen

to f th e calibratio

n drif tofthe CM S
• Preventiv

e maintenanc

e ofth e CMS , includin

g spar e part s inventor

y
• Dat arecording

, calculations

, an d reportin

g
• Progra

m o f correctiv e actio n fo rmalfunctionin

g CMS .

1Tabl e 1-1 Regulator y Checklis t fo r th e CM S Q A Progra m Regulator y Citatio n Descriptio n Pla n Sectio n 

### § 63.8(c)(1) ® Operatio n an d maintenanc

e o f eac h CM S Sectio n 1.2,2. 3 O& M Pla

n CEM S Pla

n § 63.8(c)(l)(iii) Startup , shutdown

, an d malfunctio

n pla n forCM S SSMPPla n § 63.8(c)(3

) Verification o f

operationa

l statu s CM S PE T Pla n § 63.8(c)(7)(ii

) Out-of-contro

l CM S dat

awil l no tbe use d i n average

s an d calculations. Sectio n 4. 0 § 63.8(c)(7)(H

) Correctiv

e action s fora n out-of-contro

l CM S Sectio n 4. 0 an d SSMPPla

n § 63.8(c)(8

) Out-of-contro

l CM S infonnatio

n t o b e submitte

d Sectio

n 4. 0 § 63.8(d)(2

) Develo

p an d implemen

tQ C portio

n o f CM S Q A progra m Sectio n 1. 0 § 63.8(d)(2

) Q A progra

m include

s th e developmen

tan d submitta

l o f th e performanc

e evaluatio

n tes tpla n Sectio n 2.1.1 § 63.8(d)(2) ® Develo p writte n procedure

s forinitia

l an d subsequen

t calibration

s Section s 2.1.1 , 2.1. 2 § 63.8(d)(2)(h

) Develo

p writte n procedure

s fordeterminatio

n an d adjustmen

to f calibratio

n drift s Sectio n 2. 2 § 63.8(d)(2)(iii

) Develo

p writte n procedure

s fo rpreventiv

e maintenanc

e an d spar e part s inventor

y Sectio n 2. 3 § 63.8(d)(2)(iv

) Dat arecording

, calculations, an

d reportin

g Section s 3.1 , 3. 2 § 63.8(d)(2)(vi

) Correctiv

e action s fo rmalfunctionin

g CM S Sectio n 4. 0 § 63.8(e)(3

) Performanc

e evaluatio

n o f CM S CM S PE T Pla n § 63.8(g ) Reductio

n o f monitorin

g dat a Sectio n 3. 2 § 63.10(b)(1) Mamtainin g files Sectio n 3.1 § 63.10(b)(2)(ix

) Maintai

n record s o f measurement

s fro m performanc

e evaluation

s Sectio n 3.1 § 63.10(b)(2)(vi

) Maintai

n record s o f eac h perio d durin g whic h aCM S i

s malflmctioning, o

rinoperativ

e an d ou tof contro l Sectio

n 4. 0 an d SSMPPla

n § 63.10(b)(2)(vii

) Maintai

n record s o f measurement

s t o demonstrat

e complianc

e Sectio n 3. 1 § 63.10(b)(2)(viii

) Maintai

n record s o f result s o f CM S performanc

e evaluation

s an d opacit y an d visible emissio

n observation

s Sectio n 3. 1 § 63.10(b)(2)(x

) Maintai

n record s o f CM S cahbratio

n check s Sectio

n 2.1. 2

2 

### VE S 000864Tabl e 1-1 (continued ) Regulator y Checklis t fo r th e CM S Q A Progra m Regulator y Citatio n Descriptio n Pla n Sectio n 

### § 63.10(b)(2)(xi

) Maintai

n record s o f al l adjustment

s an d maintenanc

e performe d o n th e CM S Sectio n 3.1 § 63.10(c)(1) Recordkeepin g requirement

s forCM S measurement s (includin g unavoidabl

e breakdown

s an d out-of-contro

l situations

) Sectio n 3.1 §63.10(c)(13 ) Maintai n record s o f tota l proces s operatin

g tim e durin g th e reportin

g perio d Sectio n 3.1 §63.10(c)(14 ) Develo p an d implemen

tCM S Q A progra

m procedure

s Sectio

n 1. 0 § 63.10(c)(5

) Maintai

n record s o f dat e an d tim e fo rCM S inoperabilit

y (excep tfo rzer o an d high-leve

l checks ) Sectio

n 3.1 § 63.10(c)(6

) Maintai

n record s o f dat e an d tim e forCM S out-of

contro l period s Sectio n 3.1 § 63.10(c)(8

) Maintai

n record s o f identificatio

n o f eac h tim e perio d o f exceedance

s - doe s no tinclud e period s o f Startup , Shutdown

, Malfunctio

n (SSM ) Sectio n 3.1 § 63.10(e)(3)(i

) Submitta

l of semiannua

l exces s emission

s an d CM S performanc

e repor t Sectio n 3. 1 § 63.10(e)(3)(v

) Conten

tan d submitta

l dat ao f exces s emission

s an d CM S performanc

e repor t Sectio n 3. 2 §63.10(e)(3)(vi ) Conten to f summar y repor trequire d b y (e)(3)(vii

) an d (e)(3)(viii

) t o thi s sectio n Sectio n 3. 2 § 63.10(e)(3)(vii

) Conditio

n forsubmittin

g onl y th e summar

y repor t Sectio

n 3. 2 §63.10(e)(3)(viii ) Conditio n fo rsubmittin

g bot h th e summar

y repor tan d exces s emission

s an d CM S performanc

e repor t Sectio

n 3. 2 § 63.1209(b)(2)(f

) Calibratio

n o f thermocouple

s an d pyrometer

s Sectio

n 2.1 § 63.1209(b)(3

) Frequenc

y o f CM S sampling

, evaluation

, computing

, an d recordin

g o f regulate d paramete

r Sectio n 3. 1 § 63.1209(b)(5

) Calculatio

n o f rolling average

s Sectio n 3. 1 § 63.1209(f)(1 ) § 63.1211(c ) require s tha tCM S ar e installed, calibrated

, an d operationa

l b y th e complianc

e dat e CM S PE T Pla

n |
Notes : PE T Perfonnanc

e Evaluatio

n Tes t SSM PStartup

, Shutdown

, Malfunctio

n Pla n SD PStandar

d Divisio n Practice

s



### VE S 00086 5

### Th e dat acollecte

d from CM S mstrumentatio n is use d t o demonstrat

e th e unit' s comphanc

e wit h th e perfonnanc

e requirement

s promulgate

d in th e Interi m HW C Maximu m Achievabl

e Contro l Technolog

y (MACT ) standard

. Th e Q A Progra

m outline

s procedure

s use d t o verif y tha tth e CM S ar

e properl y calibrate

d an d collectin

g accurat

e dat ao n a n ongoin g basis. Du e t o th e similarit

y o f th e thre e CM S system

s (on e foreac h incinerato

rsystem), genera

l reference

s t o aCM S syste

m o rincinerato

rsyste m i n thi s documen

twil l impl

y al l thre e systems . Informatio

n tha ti s onl y applicabl

e t o on e o rtw o o f th e thre e system s wil l b e clearl y identified . This documen

tis organize

d a s follows : Sectio n 1. 0 Introductio

n an d Backgroun

d Sectio n 2. 0 CM S Calibratio

n an d Preventiv

e Maintenanc

e Sectio n 3. 0 CM S Recordkeepin g an d Reportin

g Sectio n 4. 0 CM S Correctiv

e Action s Thi s pla n als o assimilate

s informatio

n an d procedure

s foun d i n othe rdocuments

. A s require d b y § 63.6(e)(3)(vi) , othe rdocument

s containin

g procedure

s o rinformatio

n refened t

o i n thi s pla n wil l b e mad e availabl

e fo rinspectio

n whe n requeste

d b y th e Administrator

. Th e remainde

ro f thi s sectio n provide

s a n overvie w o f th e incineratio

n syste m followe

d b y adiscussio

n o n th e CM S instrumentation . Sectio n 2. 0 discusse

s CM S initia

l an d continuin

g calibratio

n an d preventiv

e maintenanc

e requirements

. Sectio n 3. 0 addresse

s requirement

s relate d t o facilit y documentatio

n an d reporting

. Sectio n 4. 0 define s an d discusse s nonstandar

d operation

s o f th e CM S an

d apphcabl

e correctiv

e actions. 1. 1 Summar y o f Facilit y Informatio n 

### Brief summarie

s whic h describ

e th e fixed heart

h incinerator

s an d th e rotar y kiln incinerato

rar e presente

d i n thi s section . 1.1.1 Fixed

Hearth Incinerators 

### Eac h ofth e fixed heart

h incinerator

s include s th e following components :

• Feed equipmen

t

A 

### VE S 00086 6

### • Primar y an d secondar

y combustio

n chamber

s
• Lime injectio

n syste m
• Spra y drye rabsorbe r(SDA )
• Fabri c filterbaghous

e
• Solid s an d as h remova

l system s
• Induce

d draf t(ID ) fa n an d stac k
• Instrumentation

, controls, an

d dat aacquisitio

n system s Variou s soli d an d liquid waste

s an d gaseou s feedstream

s ar e thermall

y treate d i n th e fixed heart

h incinerators

. Solid wast

e i s fe d t o th e primar y (lower ) combustio

n chambe r vi aafee d conveyo

rsyste m an d pneumati

c ram. Liquid wast

e fro m tank s an d tanke r truck s ar e fe d t o th e primar y combustio

n chambe

rthroug h tw o atomize

d liqui d injectors

. Liqui d wast

e from container

s ar e fe d t o th e primar y combustio

n chambe

rthroug h a specialt y fee d injector

. A gaseou

s feedstrea

m is fe d t o th e Uni t2 primar

y combustio

n chambe rdirectl y from ga

s cylinders. Of

f gase s from ahoode

d feed . emissio

n contro l syste m an d from awast

e handhn

g glov e bo x ar e fe d directl y t o th e Uni t3 secondar

y combustio

n chamber

. Combustio

n chambe

rtemperature

s ar e maintaine

d usin g natura l ga s fired t o adedicate

d burne ri n bot h th e primar y an d secondar

y chambers

. Combustio

n ga s exit s th e secondar

y combustio

n chambe

ran d enter s th e SDA, . whic

h provide s aci d ga s remova l an d coolin g ofth e combustio

n gas . Combustio

n ga s exit s th e SD A an d is distribute

d t o th e fabri c filterbaghouses

, whic h provid e particulat

e matte r removal. Th

e induce d draf tfan, locate

d downstrea

m of th e baghouses

, move s th e combustio

n ga s throug h th e syste m an d exhaust

s th e ga s throug h th e mai n stack . Hot , we tga s i s extracte

d downstrea

m pf th e baghous

e throug h acontinuou

s emission

s momtorin

g system . Thi s syste m feature

s amulti-componen

tinfrare d ga s analyze rtha t detect s hydroge

n chloride

, carbo n monoxide

, an d wate rvapo rconcentrations

. A n integrate d zirconiu

m oxide-base

d analyze

rdetect s oxyge n concentrations

. 1.1.2 Rotary Kiln Incinerator 

### Th e rotar y Mln.incinerato

rinclude s th e followin

g components :

• Wast e fee d syste m
• Primar

y an d secondar

y combustio

n chamber

s
• Temperin

g chambe

r
• Lime injectio

n syste m
• Spra y drye rabsorbe r

### • Carbo n injectio n syste m
• Fabric filterbaghous e
• Solid s an d as h remova

l system s
• I D fa n an d stac k
• Instrumentation

, controls, an

d dat aacquisitio

n system s Variou s solid an

d liquid waste

s ar e thermall

y treate d i n th e rotar y kil n incinerator

. Solid waste s ar e fe d t o a ra m feede rvi a a clamshell, a dru m fee d conveyor

, an d a n auxiliar

y fee d conveyor

. A hydrauli

c ra m pushe s th e soh d wast e int o th e kiln . Liqui d wast

e from tank s an d tanke rtruck s i s fe d t o th e primar y an d secondar

y combustio

n chamber

s throug h atomize d liqui d injectors. Combustio n chambe

rtemperature

s ar e maintaine

d usin g natura l ga s fired t o adedicate

d burne ri n bot h th e primar y an d secondar

y chambers

. Combustio

n ga s exit s th e secondar

y combustio

n chambe

ran d enter s th e temperin

g chamber , whic h provide

s coolin g o f th e combustio

n gases . Th e combustio

n ga s exit s th e temperin g chambe

ran d is distribute

d betwee n tw o identica

l SDAs , whic

h provid e aci d ga s remova

l an d additiona

l ga s cooling . A carbo

n injectio

n syste m i s utilize

d fo r controllin

g dioxin/fura

n an d mercur

y emissions. Th

e activate

d carbo n i s airinjecte

d int o th e combustio

n ga s immediatel

y downstrea

m o f th e convergenc

e o f combustio

n gase s from th e SDAs . Fro

m th e SDAs , combustio

n ga s i s distribute

d t o fabri c filterbaghouses

, whic h provid

e particulat

e matte rremoval. Th

e I D fan , locate

d downstrea

m of th e baghouses

, move s th e combustio

n ga s throug h th e syste m an d exhaust

s th e ga s throug h th e mai n stack . Hot , we tga s i s extracte

d downstrea

m o f th e I D fa n throug h a continuou

s emission

s monitorin

g system . Thi s syste m feature

s a multi-componen

tinfrare d ga s analyze

rtha t detect s hydroge

n chloride

, carbo n monoxide

, an d wate rvapo rconcentrations

. A n integrate d zirconiu

m oxide-base

d analyze

rdetect s oxyge n concentrations

. 1. 2 CM S Instrumentatio n Thi s sectio n describe

s th e CM S mstrument

s use d monito rregulate

d proces s parameter

s fo rdemonstratin

g on-goin

g complianc

e wit h th e Interi m HW C MAC T emissio n standards

. A summar

y of specification

s forCM S instrumentatio n is provide

d i n Tabl

e 1-2 . Th e Interi m HW C MAC T standar d require

s al l CMS' s b

e installe

d i n location

s tha t provid e representativ

e measurement

s o f emission

s o rproces s parameters

. Al l CM S

6 

### VE S 00086 8Tabl e 1- 2 CM S Instrumen t Specification s Applicatio

n Instrumen t Ta

g Numbe r Manufacture

r Mode

l Operatin

g Rang e Locatio

n Uni tNo . 2 Hig h BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-21

5 Micr

o Motio n D 40S-S

S 0-3,60

0 lb/h r Fee

d Lin e Hig h BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-215D I Weigh-Troni

x WI-.13

0 0-60,00

0 l b Fee

d Lin e Lo w BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-216 Micr o Motio n D 40S-S

S 0-3,60

0 lb/h r Fee

d Lin e Lo w BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-215D I Weigh-Troni

x WI-.13

0 0-60,00

0 l b Fee

d Lin e Specialt y Fee d Weigh t Weig

h Scal e WT-20

4 Toled

o 814

0 EX P 0-4,00

0 l b #20

4 Specialt y Feede r Drumme d Solid s Fee d Weigh t Weig

h Scal e WT-21

0 Toled

o A14

0 0-40

0 l b Soli

d Charg e Conveyo r Cylinde rGa s Feedrat e d

PCel l FT-21

7 Yokogaw

a YA11 F 0-1 0 in, w.c . (0-6 0 lb/min ) Cylinde

rGa s Fee d Syste m PC C Temperatur

e Type K

Thermocoupl

e TT-200A/

B Modico

n B883-20

0 0-250

0 ° F Primar

y Chambe r SC C Temperatur

e Type K

Thermocoupl

e TT-219A/

B Modico

n B883-20

0 0-250

0 °F Secondar

y Chambe r PC C Pressur

e Pressur e Transmitte

r PT-20

0 Rosemon

t 1151D

P -7.

5 t o 2. 5 in. w.c . Primar

y Chambe r ES V Positio

n Positio n Switc h ZS-22

4 Square-

D 900

7 CG2B 2 open/clos

e Emergenc

y Stac k Baghous e Me tTemperatur

e Type K Thermocoupl

e TT-27

0 Modico

n 833-20

0 0-250

0 ° F SD

A Outle t Combustio

n Ga s Flo w Rat e dPCell FT-28 3 Rosemoun

t 1151D

R 0-20,00

0 acf m Stac

k Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxid e Analyze r AT-28

9 COSA ZFN-11YA1-2Z 1 ' 0-25 % CEMS

Buildin g Stac k Ga s Carbo n Monoxid

e Concentratio

n Multicomponen t Infrare d Photomete r 0-20 0 / 0-300 0 ppm v CEM

S Buildin g Stac k Hydroge

n Chlorid e Concentratio

n Multicomponen t Infrare d Photomete r AT-288

E EcoChe

m MC

3 0-100

0 ppm v CEM

S Buildin g Stac k Ga s Moistur e Concentratio

n 0-60 % Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-28

8 Fische

r& Porte r 10D147

5 0-1 0 GP

M SD

A Penthous

e Lim e Slurr y Densit y Densit

y Transduce r AT-96

8 Solartro

n Mobre y 784

6 0-10 0 Lb/Ft 3 SD A Penthous

e

### Tabl e l-2(continued ) CM S Instrumen t Specification s Applicatio

n Instrumen t Ta

g Numbe r Manufacture

r Mode

l Operatin

g Rang e Locatio

n UnitNo . 3 Hig h BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-31

5 Micr

o Motio n DS-04

0 0-3,60

0 lb/h r Fee

d Lin e Hig h BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-31 5 D I Weigh-Troni

x WI-13

0 0-60,00

0 l b Fee

d Lin e Lo w BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-316 Micr o Motio n DS-04

0 0-3,60

0 lb/h r Fee

d Lin e Lo w BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-31 5 D I Weigh-Troni

x WT-13

0 0-60,00

0 l b Fee

d Lin e Specialt y Fee d Weigh t Weig

h Scal e WT-30

4 Toled

o AI40EXP 0-2,00 0 l b #30

4 Hoode d Feede r Drumme d Solid s Fee d Weigh t Weig

h Scal e WT-31

0 Toled

o A14

0 0-40

0 l b Soli

d Charg e Conveyo r PC C Temperatur

e Type K

Thermocoupl

e TT-300A/

B Modico

n 883-20

0 0-250

0 ° F Primar

y Chambe r SC C Temperatur

e Type K

Thermocoupl

e TT-319A/

B Modico

n 883-20

0 0-250

0 °F Secondar

y Chambe r PC C Pressur

e Pressur e Transmitte

r PT-30

0 Rosemoun

t 115

1 d P -7.

5 t o 2. 5 in . w.c . Fee

d Lin e TRV Positio

n Positio n Switc h ZS-32

4 Square-

D 900

7 CG2B 2 open/clos

e Emergenc

y Stac k Baghous e Inle tTemperatur

e Type K Thermocoupl

e TT-37

0 Modico

n 833-20

0 0-250

0 ° F SD

A Outle t Combustio

n Ga s Flo w Rat e d

PCel l FT-38

3 Rosemoun

t 115

1 D R 0-20,00

0 acf m Stac

k Stac k Ga s Oxyge n Concentratio

n Znconiu

m Oxid e Analyze r AT-38

9 COSA ZFN-11YA1-2Z 1 0-25 % CEM

S Buildin g Stac k Ga s Carbo n Monoxid

e Concentratio

n Multicomponen t 0-200/0-300 0 ppm v CEMS

Buildin g Stac k Hydroge

n Chlorid e Concentratio

n Infrare d Photomete r AT-388

E EcoChe

m MC

3 0-100

0 ppm v CEMS

Buildin g Stac k Ga s Moistur e Concentratio

n 0-60 % Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-38

8 Fische

r& Porte r 10D147

5 0-1 0 GP M SD

A Penthous

e Lim e Slurr y Densit y Densit

y Transduce

r AT-96

9 Solartro

n Mobre y 784

6 0-10 0 Lb/Ft 3 SD A Penthous

e

8 

### VE S 00087 0Tabl e ! (continued ) CM S Instrumen t Specification s Applicatio

n Instrumen t Ta

g Numbe r Manufacture

r Mode

l Operatin

g Rang e Locatio

n Uni tNo . 4 Wast e Feedrat e t o X-10 Nozzl

e Mas s Flowmete

r FT-12

9 Micr

o Motio n DS10.0

S 12 8 0-7,00

0 lb/h r Fee

d Lin e Wast e Feedrat e t o X-l l Nozzl

e Mas

s Flowmete

r FT-13

8 Micr

o Motio n D100S-H

Y 0-6,00

0 lb/h r Fee

d Lin e Wast e Feedrat e t o X-1 2 Nozzl e Mas s Flowmete

r FT-14

5 Micr

o Motio n DL100S-S

S 0-8,00

0 Ib/h r Fee

d Lin e Wast e Feedrat e t o X-2 2 Nozzl e Mas s Flowmete

r FT-21

2 Micr

o Motio n D1D0OS-S

S 0-7,00

0 lb/h r Fee

d Lin e Cla m Shel l Fee d Weigh t (shredde d solids ) Loa

d Cel l WT-00

1 Toled

o 814

0 0-2,00

0 l b Ra

m Fee d Hoppe r Dru m Conveyo

rSolid s Weigh t Loa d Cel l WT-014

A Toled

o 814

0 0-1,00

0 l b Dru

m Conveyo r Auxiliar y Conveyo

rSolid s Weigh t Loa d Cel l WT-14

B Toled

o 814

0 0-20

0 l b Auxiliar

y Conveyo r PC C Temperatur

e Pyromete r TT-305A/

B Irco

n Modline

4 44-99-F1-0- 1 0-3,00

0 °F Kiln Outle

t SC C Temperatur

e Type

R Thermocoupl

e TT-317A/

B Chesse

l 351

0 0-3,00

0 °F SC C Outle

t PC C Pressur

e Pressur e Transmitte

r PT-30

0 Rosemoun

t 1151DR2

F -9.

0 t o 1. 0 in. w.c . Kiln Hoo

d Surg e Ven tPositio n Positio

n Switc h ZSC-02

6 Square-

D 9007CG2B

2 open/clos

e Kiln Fac

e TR V Positio n Positio n Switc h ZSC-31

6 Square-

D 900

7 CG2B 2 open/clos

e Emergenc

y Stac k Carbo n Feedrat e Feede r C-1

7 K-Tro

n K2T3

5 0-10

0 Carbo

n Inject . Syste m Carbo n Injectio n Carrie rGa s Suppl y Pressur e Pressur e Switc h PSL-438

A Dwye

r 333

0 Tri

p Points: ±5 jn . w.c . Carbo

n Injectio n Lin e Carbo n Feede rDischarg

e Pressur e Pressur e Switc h PSH-438

B Dwye

r 321

5 Tri

p Points: < 3 psi g > 1 3 psi g Carbo

n Injectio n Lin e



### VE S 00087 1Tabl e 1 (continued ) CM S Instrumen t Specification s Applicatio

n Instrumen t Ta

g Numbe r Manufacture

r Mode

l Operatin

g Rang e Locatio

n Uni tNo . 4 (continued

) SD A X-1 8 Outle

tTemperatur

e (Baghous e Inle tTemperature

) Type K Thermocoupl

e TT-417A/

B Modico

n B883-20

0 0-2,50

0 °F SD

A X-18 Outle t SD A X-1 9 Outle

tTemperatur

e (Baghous e Inle tTemperature

) Type K Thermocoupl

e TT-418A/

B Modico

n B883-20

0 0-2,50

0 ° F SD

A X-1 9 Outle t Combustio

n Ga s Flowrat e PitotTube/dPCel l FT-559A/

B Automatio

n Servic e 1151DRF228

3 0-55,00

0 acf m Stac

k Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxid e Analyze r AT-560A/

B COSA ZFN-11YA1-2Z 1 0-20 % CEMS

Buildin g Stac k Ga s Carbo n Monoxid

e Concentratio

n Multicomponen t Infrare d Photomete

r AT-556

E EcoChe

m MC

3 0-20

0 / 0-300 0 ppm v CEMS Buildin g Stac k Hydroge

n Chlorid e Concentratio

n Multicomponen t Infrare d Photomete

r AT-556

E EcoChe

m MC

3 0-100

0 ppm v CEMS

Buildin g Stac k Ga s Moistur e Concentratio

n Multicomponen

t Infrare d Photomete

r AT-556

E EcoChe

m MC

3 0-60

% CEMS

Buildin g

Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-615 Fische r& Porte r 10D147

5 0-8 0 GP

M SD A Nozzle

s Lim e Slurr y Densit y Densit

y Transduce

r DLT-60

9 SolartronMobre

y 784

6 0 -10 0 Lb/Ft 3 Lim

e Sil o

1 0 

### VE S 00087 2

### operatin g paramete

rmeasuremen

tdevice s a tth e Veoliafacilit

y ar e installe d i n complianc

e wit h thi s requirement

! A descriptio

n of th e type s o f CM S instrumentatio

n follows : Mass/Feedrat

e Monitors : Liquid wast e feedrate

s fro m tank s ar e measure

d b y corioli s mas s flowmeters. Direc

tinjec tliquid feedrate

s from tanke

rtruc k ar e calculate

d usin g th e continuousl

y monitore d weigh to f th e tanker . Al l soli d wast e charge s ar e weighe d usin g ascale/loa

d cel l prio r t o bein g fee d t o th e incinerator

. Thes e measurement

s ar e use d t o calculat

e pumpabl

e waste , tota l waste , an d constituen

tfeedrates

. ForUni t4, th e outpu to f acalibrate

d feede ri s utilize d t o calculat

e th e feedrat e o f powdere d activate d carbon , whic h is injecte

d int o th e plenu m upstrea

m ofth e baghouses

. Pressure/Differentia l Pressur e Monitors : Primar y combustio

n chambe

rpressur e is measure

d b y diaphrag

m actuate

d pressur e transmitters

. Th e positio n o f th e dampe rimmediatel

y upstrea m o f th e I D fa n is varie

d t o contro l stac k ga s flowrat e an d t o maintai

n Mi n combustio

n chambe

r negativ e pressur e (draft) . Th

e primar y combustio

n chambe

rpressur e is interlocke

d wit h wast e feeds. ForUnit2 , pressur

e dro p i n th e cylinde rga s feedstrea

m i s measure

d an d converte

d t o afeedrate

. Th e feedrat

e is use d t o calculat

e thi s feedstream' s contributio n t o th e chlorine

, lo w volatil e metals , an d semivolatil

e metal s feedrate

s t o th e incinerator

. ForUni t4 , pressur e switche

s ar e utilize d t o ensur e tha tth e carbo n feede rdischarg

e pressure

, an d th e carbo n injectio n ai rblowe rdischarg

e pressur e ar e withi n th e desig n limits. Th e pressur e dro p acros s apito ttub e i n th e stac k is continuousl

y monitore

d an d use d t o calculat

e th e stac k ga s flowrate

. Temperatur e Monitors : Fo rUnit s 2 an d 3 , redundan

tthermocouple

s ar e use d t o measur e th e temperatur

e i n bot h combustio

n chambers

. A thermocoupl

e i s als o locate d a tth e exi tt o th e SD A an d i s th e primar y elemen tfo rth e SD A exi

ttemperatur

e contro l loop . Uni t4 i s equippe

d wit h redundan

tpyrometer

s i n th e primar y chambe

ran d redundan

t thermocouple

s in th e secondar

y chamber

. Eac h SD A outle

ti s equippe

d wit h redundan

t thermocouple

s use d fortemperatur

e contro l an d monitorin

g ofth e baghous

e inle ttemperature

.

1 1 

### VE S 00087 3

### Emergenc y Safety Ven t Positio n Monitors : Th e positio n ofth e emergenc

y safet y ven t(ESV) is indicate

d a s ope n o rclose d b y apositio

n transmitter

. No wast

e o rfue l ca n b e fe d i f th e ES V position i

s "open" . Th

e Emergenc

y Safet y Ven t(ESV ) Pla

n provide

s detail s o n th e ES V systems . Ba g Lea k

Detectio n System : A triboelectri c senso ri s locate d downstrea

m o f th e I D fa n an d monitor s th e relativ e particulat

e matte rloadin g of th e combustio

n ga s exitin g th e baghouses

. Alarms an

d interlock

s base d on thi s relativ e measuremen

tar e indication

s of apotentia

l ba g lea k o rfailure . Procedure

s fo rsetu p an d adjustment

s t o th e ba g lea k detectio

n syste m ar e no tcovere d b y thi s Q C program

. Th e Operatio

n an d Maintenanc

e Pla n provide

s detail s o n th e ba g lea k detectio n system . Continuou s Emission s Monitorin g System : Th e CEM S continuousl y sample

s an d analyze

s 

### stac k ga s forth e concentration

s o f carbo n monoxid

e (CO) , Hydroge

n Chlorid

e (HCI) , an

d moistur e usin g a multicomponen

tinfrare d photometer

. Th e oxyge n concentratio

n is analyze

d simultaneousl

y usin g azirconiu

m oxid e analyzer

. Thes e dat a ar e use d t o calculat

e th e stac k ga s C O concentratio

n o n a dr y basis, correcte

d t o 7 % O2
. Th e CEM S Q A Pla

n provide

s additiona

l detail s on th e CEMS .

1 2 

### VE S 00087 4

### 2. 0 CM S CALIBRATIO N AN D PREVENTIV E MAINTENANC E This sectio

n discusse

s th e calibratio

n an d preventiv

e maintenanc

e requirement

s t o mee tth e requirement

s o f § 63.8(d). 2. 1 CM S Calibratio n T o ensur e ongoin g comphanc

e wit h th e Interi m HW C MAC T standard , iti s essentia

l tha tth e dat acollecte

d fro m th e CM S b

e measure

d an d recorde

d i n a n accurat

e manner

. Initia l calibrations, subsequen

tcalibration

, an d CEM S calibration

s ar e describe

d i n thi s section . 2.1.1 Initial

CMS Calibration 

### A s par to f Veolia' s Qualit

y Contro l Program

, th e CM S instrument

s wer e initiall y calibrate

d prio r t o th e Interi m HW C MAC T comphanc e date . Cahbratio

n prio rt o th e complianc

e dat e i s require d s o tha tall collecte

d dat a ar e reliabl e an d accurate

. Al l initia

l cahbratio

n dat a ar e par tof th e operatin

g record . Initia l calibration

s o f new/replacemen

tinstrument

s wil l b e performe

d pe r th e manufacture' s writte

n procedures

. I n lie u o f a n initia l cahbratio

n fornew/replacemen

t instrument

s o rinstrumen

tcomponents

, th e facilit y ma y us e amanufacturer' s certification. 2.1.2 Subsequent

CMS Calibration 

### Subsequen

tcalibration

s o n CM S instrumentatio

n wil l b e performe

d a s neede d an d i n accordanc

e wit h th e manufacture' s writte n procedures

. Calibration

s wil l b e performe

d a s correctiv

e measure s forhig

h calibratio

n drift . Calibration

s ma y b e require

d whe n restorin

g CM S instrument

s afte rmaintenanc

e o rrepairs. Al l calibratio n adjustment

s wil l b e documente

d by record s ofth e cahbratio

n drif tdetermine

d befor e an d afte rth e instrumen

twa s serviced

. Som e instrument

s suc h a s differentia

l pressur e cell s mus tb e remove d from servic

e an d benc h calibrated

. T o rniriimiz

e downtim

e thes e instrument

s ma y b e replace d wit h a calibrate

d spare . Th e Uni t4 primar

y combustio

n chambe

rpyrometer

s wil l b e replace d a tleas tannuall y wit h a factor y calibrate

d pyrometer

. Electroni

c check s an d replacement

s o f thermocouple

s will b e performe d pe rth e facility' s Thermocoupl e Calibration

, Operation

, an d Replacemen

tProcedure

. A cahbratio

n recor d for m is availabl

e foreac h CM S instrumen

tan d wil l b e use d t o documen

t calibratio

n audits , calibrations, an

d replacements

. Th e mos trecentl y complete

d calibratio

n recor d document

s tha tth e instrumen

ti n servic

e meet s th e qualit y contro l criteri ase tfort h b y thi s program . Thes e cahbratio

n record s contai n "calibratio

n notes " whic

h provid e th e instrumen

t technicia n wit h procedure

s specific t

o agive n instrument

. Th e calibratio

n recor d form s fo rCM S instrument

s ar e incorporate

d i n thi s Q C Progra

m by reference

.

1 3 

### VE S 00087 52.1.3 CEMS Calibration Audits and Calibration CEM S QA/Q C procedure s ar e provide

d b y th e Continuous Emission Monitoring System Quality 

### Assurance Plan. Thes e procedure

s ar e maintaine

d a tth e facilit y an d describ e th e requirement

s forCEM S drif

tchecks, audits

, calibrations

, preventiv

e maintenance

, an d recordkeeping

. 2. 2 CM S Calibratio n Audit s CM S calibratio

n audit s ar e performe

d t o determin

e th e calibratio

n drif t(CD ) o f

CM S instruments

. Cahbratio

n Drif t(CD) is th

e bia s betwee n th e CM S instrumen

treadin g an d a cahbratio

n reference

. Tabl e 2- 1 present

s th e requirement

s fo rCM S calibratio

n audits . Eac h CM S instrumen

twil l be subjecte

d a cahbratio

n audi ta tth e frequenc

y indicate

d i n Tabl

e 2-1 . Th e calibratio

n audi twil l b e performe

d a tth e low-leve

l (zero ) an d high-leve

l check s indicated

. Th e calibratio

n chec k will confir

m tha tal l proces

s variabl e indication

s (e.g., loca

l reading , contro l roo m display

) a tth e high-leve

l valu e agre e wit h th e calibratio

n referenc

e wilhin Vi o

f th e require d tolerance

. Calibratio

n adjustments/correctiv

e action s mus tb e take n i f thi s cahbratio

n drif ti s greate rtha n Vi o f th e require d tolerance

. I f th e calibratio

n drif texceed s th e require

d tolerance , th e instrumen

ti s considere

d out-of-control. Sectio n 4. 0 describe

s th e correctiv

e action s forout-of-control, inoperative , an d malfunctionin

g CMS . If th e accurac

y o f a CM S instrumen

tis i n question

, th e C D i s determine

d an d documente

d prio r t o performin

g maintenance

, repairs , o radjustments

. Th e troubleshooting/calibration s o f CM S instrument

s wil l b e performe

d i n a manne

rconsisten

twit h th e manufacturer' s writte n procedure

s an d recommendations

. Th e C D determine

d afte rcalibrations/correctiv

e action s hav e bee n take n wil l documen

tth e effect s o f th e adjustment

s an d demonstrat

e tha tth e instrumen

ti s performin

g properly . Cahbratio

n record s wil l documen

tCD , whic

h i s a n indicato

ro f th e stabilit y o f th e CM S cahbratio n ove rtime . Th e amoun to f drif tan d stabilit y i s dependan

to n th e typ e o f instrumen

t an d th e cahbratio

n frequency

. Veoli a ma

y increas e o rdecreas

e th e frequenc

y o f particula r calibratio n audit s t o th e exten twarrante

d b y a n assessmen

to f a n mstrument's stability

. Veolia wil l maintai

n regularl

y schedule

d cahbratio

n audi tinterval

s foreac

h CM S instrument

. Cahbration

s wil l b e performe

d t o preven texcessiv

e C D an d t o maintai

n th e validit y of th e dat a collecte d fro m th e monitorin

g system .

1 4 

### VE S 00087 6CM S Calibratio n Audi t Requirement s Applicatio

n Instrumen t Ta

g Numbe r Frequenc

y o f Calibratio

n Audi t Lo w Leve l Chec k Poin t Hig

h Leve l Chec k Poin t Toleranc

e Uni tNo. 2 Hig h BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-21

5 Annuall

y 0-

5 lb/mi n 15-2

5 lb/mi n 10

% ' Hig h BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-215D I Quarterl

y 01

b 25,00

0 l b 10

% Lo w BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-21

6 Annuall

y 0-

5 lb/mi n 15-2

5 lb/mi n 10

% Lo w BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-215D I Quarterl

y 01

b 25,0001 b 10

% Specialt y Fee d "Weigh t Weig

h Scal e WT-20

4 Quarterl

y 01

b -50

0 l b 10

% Drumme d Solid s Fee d Weigh t Weig

h Scal e WT-21

0 Quarterl

y 01

b -5

0 l b 10

% Cylinde rGa s Feedrat e dPCel

l FT-21

7 Annuall

y 0 in

. w.c . 1

0 in . w.c . 10

% Primar y Combustio

n Chambe

r Temperatur

e TypeK

Thermocoupl

e TT-200A/

B Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Secondar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-219A/

B Refe

rt o th e Thermocoupl

e Cahbration

, Operation

, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe r Pressur e Pressur e Transmitte

r PT-20

0 Quarterl

y -7.

5 t o -6. 5 1.

5 t o 2. 5 i n w.c . 10

% ES V Positio

n Positio n Switc h ZS-22

4 Annuall

y AWFCO interloc k eneTgize d whe

n ope n Pas

s Baghous e Inle tTemperatur

e TypeK Thermocoupl

e TT-27

0 Se e Calibratio

n Recor d For m Combustio

n Ga s Flo w Rat e dPCel

l FT-28

3 Annuall

y 0-0.0

5 in . w.c . 0.45-0.5

0 in. w.c . 10

% Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-28

8 Annuall

y Ogp

m 1-1

0 gp m 10

% Lim e Slurr y Densit y Densit

y Transduce r AT-96

8 Replace , a s required , wit h factor y service d transduce

r Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxid e Analyze r AT-28

9 Pe rCEM S Q A Pla n Stac k Ga s Carbo n Monoxid

e Concentratio

n Stac k Hydroge

n Chlorid e Concentratio

n Stac k Ga s Moistur e Concentratio

n Multicomponen

t Infrare d Photomete

r AT-288

E Pe rCEM S Q A Pla n

1 5


### VE S 00087 7Tabl e 2- \ ,ontinued ) CM S Cabbratio n Audi t Requirement s Applicatio

n Instrumen t Ta

g Numbe r Frequenc

y o f Calibratio

n Audi t Lo w Leve l Chec k Poin t Hig

h Leve l Chec k Poin t Toleranc

e Uni tNo . 3 Hig h BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-315 Annuall y 0-

5 lb/mi n 15-2

5 lb/mi n 10

% Hig h BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-315D I Annuall

y 01

b 25,00

0 l b 10

% Lo w BT U Liqui

d Feedrat e Mas

s Flowmete

r FT-31 6 Annuall y 0-

5 lb/h r 15-2

5 lb/mi n 10

% Lo w BT U Liqui

d Direc tInjectio n Feedrat e Scal e WT-315D I Annuall

y 01

b 25,00

0 l b 10

% Specialt y Fee d Weigh t Weig

h Scal e WT-30

4 Quarterl

y 01

b -20

0 I b 10

% Drumme d Solid s Fee d Weigh t Weig

h Scal e WT-31

0 Quarterl

y 01

b -50 l

b 10

% Primar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-300A/

B Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Secondar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-319A/

B Refer

, t o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe

r Pressur e Pressur e Transmitte

r PT-30

0 Quarterl

y -7.

5 t o -6. 5 1.

5 t o 2. 5 in w.c , 10

% ES V Positio

n Positio n Switc h ZS-32

4 Annuall

y AWFC O interloc k energize

d whe n ope n Pas

s Baghous e Inle tTemperatur

e Type K Thermocoupl

e TT-37

0 Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Combustio

n Ga s Flo w Rat e dPCel l FT-38 3 Annuall

y 0-0.0

5 in. w.c . 0.45-0.5

0 in . w.c . 10

% Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-38

8 Annuall

y 0 gp

m 1-1

0 gp m 10

% Lim e Slurr y Densit y Densit

y Transduce r AT-96

9 Replace , a s required , wit h factor y service d transduce

r Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxid e Analyze r AT-38

9 Pe rCEMS Q

A Pla n Stac k Ga s Carbo n Monoxid

e Concentratio

n Multicomponen t Infrare d Photomete

r AT-388

E Pe rCEMS QA Pla

n Stac k Hydroge

n Chlorid e Concentratio

n Multicomponen t Infrare d Photomete

r AT-388

E Pe rCEMS QA Pla

n Stac k Ga s Moistur e Concentratio

n Multicomponen

t Infrare d Photomete

r AT-388

E Pe rCEMS QA Pla

n

1 6 | 

### VE S 00087 8Tabl e 2'bntinued ) CM S Calibratio n Audi t Requirement s Applicatio

n Instrumen t Ta

g Numbe r Frequenc

y o f Drif t Check/Accurac

y Audi t Lo

w Leve l Chec k Poin t Hig

h Leve l Chec k Poin t Toleranc

e Uni tNo
. 4 Wast e Feedrat e t o X-10 Nozzl

e Mas s Flowmete

r FT-12

9 Annuall

y 0-

5 lb/rni n 15-2

5 lb/mi n 10

% Wast e Feedrat e t o X- l 1 Nozzl

e Mas s Flowmete

r FT-13

8 Annuall

y 01

b 21,00

0 l b 10

% Wast e Feedrat e t o X-1 2 Nozzl e Mas s Flowmete

r FT-14

5 Annuall

y 0-

5 lb/mi n 15-2

5 lb/mi n 10

% Wast e Feedrat e t o X-2 2 Nozzl e Mas

s Flowmete

r FT-21

2 Annuall

y 01

b 21,00

0 l b 10

% Cla m Shel l Fee d Weigh t (shredde d solids ) Loa

d Cel l WT-00

1 Quarterl

y 01

b -20

0 l b 10

% Dru m Conveyo

rSolid s Weigh t Loa d Cel l WT-014

A Quarterl

y oi b -1001 b 10 % Auxiliar y Conveyo

rSolid s Weigh t Loa d Cel l WT-14

B Quarterl

y 01

b -50 l

b 10

% Primar y Combustio

n Chambe

r Temperatur

e Pyromete r TT-305A/

B Replac e a tleas tannuall y wit h factor y calibrate

d Pyromete

r Secondar y Combustio

n Chambe

r Temperatur

e Type R Thermocoupl

e TT-317A/

B Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe

r Pressur e Pressur e Transmitte

r PT-30

0 Quarterl

y -9.

0 t o -8. 0 in . w.c . 0 t o 1. 0 in . w.c , 10

% Surg e Ven tPositio n Positio

n Switc h ZS-02

6 Annuall

y AWFC O interloc k energize

d whe n ope n Pas

s ES V Positio

n Positio n Switc h ZS-32

4 Annuall

y AWFC O interloc k energize

d whe n ope n Pas

s Carbo n Feedrat e Feede r WT-43 8 Quarterl

y 0 lb/mi

n 6-3

0 lb/mi n 10

% 1 Carbo n Injectio n Carrie rGa s Lo w I Pressur e Pressur e Switc h PSL-438

A Annuall

y Energiz e Switc h Pas s 1 Carbo n Injectio n Carrie rGa s 1 Hig h Pressur e Pressur e Switc h PSH-438

B Annuall

y Energiz e Switc h Pas s

1 7 

### VE S 00087 9

### Tabl e 2- . ,antinued ) CM S Calibratio n Audi tRequirement s Applicatio n Instrumen t Ta g Numbe r Frequencyo f Drif t Check/Accurac y Audi t Lo wLeve l Chec k

Poin t Hig

h Leve l Chec k Poin t Toleranc e Uni t No
. 4 (continued ) SD A X-18 Outle

tTemperatur

e (Baghous e Inle tTemperature

) TypeK Thermocoupl

e TT-417A/

B Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e SD A X-19 Outle

tTemperatur

e (Baghous e Inle tTemperature

) TypeK Thermocoupl

e TT-418A/

B Refe

rt o th e Thermocoupl

e Calibration

, Operation

, an d Replacemen

tProcedur

e Combustio

n Ga s Flowrat e PitotTube/dPCel l FT-559A/

B Annuall

y 0 in. w.c

. 1.7

4 i n w.c . 10

% Lim e Slurr y Flo w Rat e Mag

. Flowmete

r FT-61

5 Annuall

y 0 gp

m 1-1

0 gp m 10

% Lim e Slurr y Densit y Densit

y Transduce

r DIT-60

9 Replace , a s required , wit h factor y service d transduce

r Stac k Ga s Oxyge n Concentratio

n Zirconiu m Oxid e Analyze r AT-560A/ B Pe rCEM S Q A Pla n Stac k Ga s Carbo n Monoxid

e Concentratio

n Multicomponeh t Infrare d Photomete

r AT-556

E Pe rCEM S Q A Pla n Stac k Hydroge

n Chlorid e Concentratio

n Multicomponeh t Infrare d Photomete

r AT-556

E Pe rCEM S Q A Pla n Stac k Ga s Moistur e Concentratio

n Multicomponeh t Infrare d Photomete

r AT-556

E Pe rCEM S Q A Pla n

1 8 

### VE S 00088 0

### 2. 3 Preventiv

e Maintenanc

e Veoli atake

s dail y proactiv

e measure

s t o assur e tha tpotentia l problem

s wit h th e CM S ar

e quickl y identifie d an d avoided

, i f possible . Daily mamtenanc

e check s include :

• Verification tha

tproces s variable

s ar e reasonabl

e
• Compariso

n o f reading s fro m redundan

tinstrument

s •
• Cleanin

g an d visua l chec k of monitorin

g equipmen

t
• Communicatio

n betwee n operator

s an d instrumen

ttechnician

s Thes e check s ar e documente

d o n adail y logshee

tforeac

h incinerator

. Th e preventiv

e maintenanc

e o n th e CM S als

o include s th e cahbratio

n audit s previousl

y described

. Al l necessar

y part s forroutin

e repair s o f th e affecte d CM S equipmen

tar e mad e readil y availabl

e onsite . A spar e part s inventor

y fo reac h componen

to f th e CM S is include

d i n th e record s maintaine

d b y th e Maintenanc

e Department

. Additiona

l detail s regardin

g preventiv

e maintenanc

e applicabl

e t o th e CM S ar

e provide d i n th e facility' s Operatio

n an d Maintenanc

e Pla n an d th e CEM S Q A Plan.

1 9

### 3. 0 CM S RECORDKEEPIN G AN D REPORTIN G Thi s sectio

n discusse

s recordkeepin

g an d reportin

g requirement

s fo rCM S instrumentatio

n a s specifie d b y § 63.1211 . 3. 1 Recordkeeping Veoli awil l follo w th

e recordkeepin

g requirement

s a s specified i n § 63.10(b), includin g th e semiannua

l exces s emission

s an d CM S performanc

e report . Veoli awil l maintai

n thes e record s o f CM S dat

afo raminimu

m o f 5 year s following th

e dat e o f eac h occurrence

, measurement

, maintenance

, correctiv

e action, report

, o rrecord . A ta minimum, th

e mos trecen t2 year s o f dat awil l b e retaine d onsite . Belo w i s abrie f summar y o f thes e requirements

. Veoli awil l maintai

n record s on th e following :

• Th e occurrenc

e an d duratio

n o f eac h startup

, shutdown

, o rmalfunctio

n o f operation

. • The occurrenc

e an d duratio n o f eac h malfunctio

n o f th e ai rpollutio

n contro l an d monitorin

g equipment

. Maintenanc

e performe

d o n th e ai rpollutio

n contro l an d monitorin

g equipmen

t
• Actions take

n durin g period s o f startup , shutdown

, an d malfunctio

n (includin

g correctiv e action s t o restor e th e proces s orai rpollution contro

l syste m t o norma l operation

) whe n suc h action s ar e differen

tth e procedure

s outline d i n th e SSM P
• Al l informatio

n necessar

y t o demonstrat

e conformanc

e wit h th e SSM P
• Eac h perio d i n whic

h aCM S i s malfunctionin g o rinoperativ

e (includin

g outof-contro

l periods )
• Al l require

d measurement

s neede d t o demonstrat

e complianc

e wit h arelevan

t standard . • Al l result

s o f performanc

e tests , CM S performanc

e evaluations

, an d opacit y an d visible emissio

n observation

s
• Al l CM S calibratio

n check s
• Al l adjustment

s an d maintenanc

e performe

d on CM S
• Al l require

d CM S measurement

s (includin

g dat arecorde

d durin g unavoidabl

e CM S breakdown

s an d out-of-contro

l periods )
• The dat

e an d tim e identifying eac

h perio d durin g whic h th e CM S wa

s inoperativ

e excep tfo rzer o (lo w level ) an d high level check

s
2 0

### • Th e dat e an d tim e identifyin

g eac h perio d durin g whic h th e CM S wa

s out-ofcontro l a s define d b y § 63.8(c)(7

)
• Th e specifi c identificatio

n (dat e an d tim e o f commencemen

tan d completion

) o f eac h perio d o f exces s emission

s an d paramete

rmonitorin

g exceedances

, a s define d i n th e relevan tstandard

, tha toccur s durin g period s othe rtha n startup , shutdowns

, an d malfunctions. • Th e natur e an d caus e o f an y malfunctio

n
• Th e correctiv

e actio n take n o rpreventiv

e measure

s adopte d
• Th e natur e o f th e repair s o radjustment

s t o th e CM S tha

twa s inoperativ

e o r out-of-contro

l
• Th e tota l proces s operatin

g tim e durin g th e reportin

g perio d
• Al l procedure

s tha tar e par to f qualit y contro

l progra m develope

d an d implemente

d fo rCM S unde

r§ 63.8(d) . Al l CM S instrumentatio n wil l b e operate d o n acontinuou

s basis. Th

e detecto rrespons

e wil l b e evaluate

d a tleas tever y 1 5 seconds

, an d thes e value s wil l b e use d t o calculat

e regulate d parameters

. Forparameter

s interlocke

d wit h fh e AWFC O syste

m o n a n hourl y rolling averag

e basis, ra

w dat awill be average

d an d recorde

d a tleas tonc e pe rminute . On e minut e average

s will b e use d t o calculat

e th e hourl y rolling averages

. Th e pumpabl

e waste , tota l waste , an d constituen

tfeedrat e operatin

g paramete

rlimit s ar e base s o n rolling total s i n lie u o f rolling averages

. A n integra

l par to f th e CM S i s th

e dat aacquisitio

n an d dat ahistoria n systems

, whic h record s al l operatin

g dat agenerate

d b y th e CM S instruments

. Th e dat ahistoria

n an d associate d archiv e file s ar e par to f th e operatin

g record. CM S instrumen tcalibrations, maintenanc

e activities, an

d correctiv

e action s ar e recorde

d an d kep ti n th e operatin

g record. Al l dat

acollecte d durin g CM S PET s ar

e recorde

d an d kep ti n th e operatin

g record. 3. 2 Reportin g Veoli awil l follow fh

e reportin

g requirement

s a s specifie d i n § 63.10

. I n addition

, Veoha wil l develo

p an d includ e i n th e operatin

g recor d aDocumentatio

n o f Complianc

e (DOC ) pe r§ 63.1211(c) . Th

e DO C mus

tinclud e asigne d an d date d certificatio

n tha tth e CEM S an d CM S ar

e installed

, calibrated

, an d continuousl

y operatin

g i n complianc

e wit h th e requirement

s o f Subpar tEEE .

2 1

### Ra w dat afrom th

e CM S wil l b

e collected, reduce

d a s describe

d i n § 63.8(g) , an

d include d i n th e CM S PE T report

. Thi s dat

awil l be analyze

d t o determin

e complianc

e wit h th e HW C MAC T an

d th e result s wil l b e submitte

d a s par tof th e notificatio

n o f complianc

e require d b y § 63.1207(j) . The conten

tan d deadlin e requirement

s forth e exces s emission

s an d momtorin

g syste m performanc

e report s ar e specifie d i n § 63.10(e)(3)(v) . Th e requirement

s forth e summar

y repor tar e give n i n § 63.10(e)(3)(vi) . A s note d i n § 63.10(e)(3)(vii) , Veoh ais require d t o only submi

tth e summar

y repor ti f th e tota l duratio n o f exces s emission

s o rproces s o rcontro l syste m paramete

rexceedance

s fo r th e reportin

g perio d is les s tha n on e percen to f th e tota l operatin

g tim e forth e reportin

g period , an

d CM S downtim

e fo rth e reportin

g period i s les

s tha n five percen

to f th e tota l operatin g tim e forth e reportin

g period . Conversely, additiona l reportin g is require

d b y § 63.10(e)(3)(viii

) i f th e tota l duratio n o f exceedances

, o rth e tota l CM S downtim

e durin g th e reportin

g period , i

s greate rtha n th e allowabl

e percentag

e o f th e reportin

g period. Table 3-1 provide

s a lis to f Veoha' s reportin

g requirements

.

2 2

### Tabl e 3- 1 Reporting Requirement s Regulator

y Citatio n Descriptio n Frequenc y § 63.1211(c

) Recor

d Documentatio

n o f Complianc

e i n th e operatin

g recor d Onc e § 63.10(d)(2

) Befor

e Titl e V permi

tha s bee n issued, owne

roperato r mus tsubmi tresult s o f performanc

e test . B y th e 60t h da y followin g ever y performanc

e tes t § 63.10(d)(2

) AfterTitle V permi tha s bee n issued, owne

roperato r mus tsubmi tresult s o f require d performanc

e tests . B y th

e 60t h da y followin g require d performanc

e tes t § 63.10(d)(4

) Progres

s report s A s specifie d in writte

n extensio n o f complianc

e § 63.10(d)(5)(i

) Periodi

c startup , shutdown

, an d malfunctio

n report s (durin g reportin

g period ) Submitte d simultaneou

s wit h exces s emissio n repor t § 63.10(d)(5)(ii

) Startup

, shutdown

, an d malfunctio

n report s whe n action s ar e take n tha tar e inconsisten

twit h SSMP . 2 workin g day s from commencemen

to f action , followe d wit h a lette rexplainin

g exten t withi n 7 workin

g days . § 63.10(e)(3)(i

) Submitta

l o f semiannua

l exces s emission

s an d CM S perfonnanc

e repor t Semiannuall y - b y th e 30t h da y followin

g th e en d o f eac h calenda

r half performanc

e tes t|

2 3 

### VE S 00088 5

### 4. 0 CM S CORRECTIV E ACTION S L f a CM S i s foun d t o b e out-of-control, inoperative , o rmalfunctioning ; correctiv e action s mus tb e take n t o retur n th e CM S t o norma l operation

. Definition

s use d i n determinin

g th e typ e o f correctiv

e actio n require d ar e give n below . Out-of-control: A CM S i s out-of-contro

l if :

• Th e zer o (lo w level) , mid-level , o

rhigh-leve

l calibratio

n drif texceed s tw o time s th e applicabl

e C D specificatio

n i n th e apphcabl

e performanc

e specificatio

n o rprocedure ; o r
• Th e CM S fails a performanc e tes taudit , relativ e accurac

y audit , relativ e accurac y tes taudit , o rlinearit y tes taudit . Th e onl y applicabl

e performanc

e specificatio

n t o th e CM S is Performanc

e Specificatio

n (PS) 4 B o f 4 0 CF RPar

t63 , Appendi

x B . P S 4 B applie s t o th e 0 2

### an d C O CEMS . Th

e requirement

s o f PS 4 B an d additiona

l requirement

s Veoha impose

s o n th e CEM S ar

e detaile d i n th e CEM S Q A Plan. I

n th e absenc e o f promulgate

d performanc

e specificatio

n applicabl e t o non-CEM S CM S instruments , Veolia ha

s self-impose

d a high-leve

l C D specification, a

s describe

d i n Sectio

n 2.0 . Whe n a CM S is out-of-control, Veoli awil l tak e th e necessar

y correctiv

e actio n an d shal l repea tall necessar

y test s whic h indicat e tha tth e syste m is out-of-control. Correctiv e action s an d retestin

g wil l continu

e until th

e CM S i s returne

d t o norma l operation

. Th e beginnin g o f th e out-of-contro

l perio d i s th e hou rtha tth e calibratio

n drif tindicate s tha t th e CM S ha

s exceede

d it s performanc

e specifications. The en d o f th e out-of-contro

l perio d i s th e hou rfollowing th

e completio

n o f correctiv

e actio n an d successfu

l demonstratio

n tha tth e CM S is withi

n it s allowabl

e limits . Durin

g th e perio d th e CM S i s out-of-control, recorde

d dat a shal l no tb e use d i n dat aaverage

s an d calculations, o

rt o mee tan y dat aavailabilit

y requiremen

testablishe

d unde rthi s part . Veohawil l submi

tal l informatio

n concernin

g out-of-contro

l periods, includin

g star tan d en d date s an d hours, an

d description

s o f correctiv e action s taken , i n th e exces s emission

s an d continuou

s monitorin

g syste m performanc

e repor trequire d b y § 63.10(e)(3). Malfunction: Fo rus

e i n thi s plan , malfunctio

n i s define d a s an y sudden , infrequent

, an d no treasonabl

y preventabl

e failur e o f ai rpollutio

n contro l o rmonitorin

g equipment

.

2 4 

### VE S 00088 6

### Malfunctio n als o include s th e failur e o f aproces s o ran y proces s equipmen

tt o operat e i n anorma l o rusua l manner . Failure

s tha tar e cause d i n par tb y poo rmaintenanc

e o r careles s operatio n ar e no tmalfunctions. Th e Program of

Corrective Actions forMalfunctions i s Attachmen

t4 of th e SSM PPlan. 

### Thi s progra m addresse

s ho w th e incinerato

rwil l b e operate d an d maintaine

d durin g malfunctions. I

n thi s program

, potentia l malfunction

s ar e hste d foreac h portio n o f th e incinerato

rsystem . Th e malfunction

s ar e event s tha tar e recognize

d b y th e operator

, o r indicate d b y a n alarm , an d threate n t o caus e a n exceedance

. I n th e respons

e t o th e malfunctio

n and/o ralarms , th e operato rwil l appl

y discretio

n an d attemp tt o maintai n th e incinerato

rsyste m withi n regulator

y limits . I

n th e progra m of correctiv

e actions

, potentia l cause s o f eac h malfunctio

n ar e listed. Th

e operato

rwil l utiliz

e proces s knowledge

, jo b experience

, and , i f needed , assistanc

e from othe

rpersonne

l t o identif y th e caus e o f th e malfunction

. Foreac

h potentia

l cause , action s t o correc tth e failur e ar e hsted . Th e correctiv

e action s prescribe

d ma y requir e fh e collaboratio

n o f multidiscipline

d personne

l wh o ar e quahfie

d t o retur n th e incinerato

rsyste m t o prope rworkin g condition s (i.e. , maintenanc

e personnel

, instrumen

ttechnicians

, engineering

)

25

## CONTINUOU S EMISSION S MONITORIN G SYSTE M QUALIT Y ASSURANC E PLA N



## Prepare dfor : Veoli aE S Technica

l Solutions , LL C Sauget , Illinoi s

Prepare d by : Franklin Engineerin

g Group , Inc

. Franklin, Tennesse

e

Octobe r200 8TABL E O F CONTENT S
1. 0 INTRODUCTIO N AN D BACKGROUN D 1 1. 1 DESCRIPTIO N O F CEM S 1 1. 2 OVERVIE W O F REGULATOR Y REQUIREMENT S 2 2. 0 CEM S CALIBRATION S AN D PERFORMANC E 5 2. 1 DAIL Y DRIF T CHECK S 5 2. 2 CALIBRATIO N 8 2. 3 ABSOLUT E CALIBRATIO N AUDI T 1 0 2. 4 INTERFERENC E RESPONS E TES T 1 0 2. 5 RELATIV E ACCURAC Y TES T AUDI T 1 1 3. 0 CEM S MAINTENANC E 1 4 3. 1 DAIL Y SYSTE M AUDI T 1 4 3. 2 SPAR E PART S INVENTOR Y 1 4 3. 3 CALIBRATIO N GA S SUPPL Y AN D CERTIFICATIO N 1 5 3. 4 CORRECTIV E ACTIO N FO RMALFUNCTIONIN G CEM S 1 7 4.0 . INTEGRATIO N O F TH E CEM S WIT H TH E AWFC O SYSTE M 1 8 4. 1 EMISSIO N STANDARD S 1 8 4. 2 DRIF T LIMIT S 1 8 5.0 . RECORDKEEPIN G AN D QUALIT Y ASSURANC E REVIEW S 1 9 6. 0 OPERATO RTRAININ G AN D CERTIFICATIO N 2 1



### VE S 00088 9

### INDE X O F TABLE S
TABL E 1 - 1 REGULATOR Y REQUIREMENT S FO RTH E CEM S Q C PROGRA M AN D TH E

CEM S Q A PLA N 3 TABL E 2- 1 OVERVIE W O F CEM S PERFORMANC E REQUIREMENT S 6 TABL E 3- 1 SUMMAR Y O F CONCENTRATIO N REQUIREMENT S FO RCALIBRATIO N GASE S 1 6


### LIS T O F APPENDICE S
APPENDI X A CEM S DAT A SHEET S AN D CHECKLIST S



### i i VE S 00089 0

### 1. 0 INTRODUCTIO N Veoli aE S Technica

l Solutions

, LL C (Veoha

) own s an d operate

s tw o fixed heart

h incinerator

s (Unit s 2 an d 3 ) an d a transportabl

e rotar y kil n incinerato

r(Uni t4 ) a tit s facilit y locate d i n Sauget

, Illinois . Thes

e incinerator

s ar e subjec tt o th e Nationa

l Emission

s Standard

s forHazardou

s Ai rPollutant

s (NESHAP) forHazardou s Wast e Combustor

s (HWCs) , Par

t63 , Subpar tEE E {§§63.120 0 t

o 63.1221). Th

e NESHA Pfo

r HWC s specifie

s emission

s standard

s whic h reflec temission

s performanc

e o f maximu m achievabl

e contro l technologie

s (MACT) , an

d is commonl

y referre d t o a s th e HW C MACT . Fo reac h incinerator

, Veoli a utilize

s a continuou

s emission

s monitorin

g syste m (CEMS ) fo rdemonstratin

g on-goin

g comphanc

e wit h th e carbo n monoxid

e (CO ) emissio

n standard . Thes e CEM S ar

e subjec tt o th e requirement

s ofth e Appendi

x t o 4 0 CF RPar

t 63, Subpar

tEEE— Qualit

y Assurance Procedures forContinuous Emissions Monitors 

### Used for Hazardous Waste Combustors. Thi s pla n ha s bee n develope

d pe rth e CEM S qualit y assuranc

e (QA)/qualit

y contro l (QC) requirements

. Implementatio

n o f thi s pla n wil l ensur

e tha tth e CEM S generates

, collects, an

d report s vah d dat a tha ti s precise , accurate , complete

, an d of a quaht y tha tmeet s th e requiremen

to f th e HW C MAC T Standar d an d th e apphcabl

e performanc

e specification. 1. 1 Description o

f CEM S Eac h incinerato

ri s equippe

d wit h a n EcoChe

m Analytic

s MC 3 CEMS , whic

h consist s of th e followin

g majo rcomponents :

• Heate

d stac k sampl e prob e
• Heate

d trace d umbilica

l

• Heate

d sampl e pum p
• EcoChe

m MC 3 multicomponen tinfrare d (FR ) ga s analyze r
• Zirconiu

m oxide-base

d oxyge n analyze

r
• Syste m controlle

ran d dat a acquisitio

n syste m Hot, we tstac k ga s i s draw n throug h th e heate d stac k sampl e prob e an d hea ttrace d umbilica l usin g a heate

d sampl e pump. Th

e samplin

g locatio n i s downstrea

m of th e induce d draf t(K> ) fan. Th

e umbihca

l supphe s mstrumen

tai rt o th e filterprob

e t o allo w fo rautomate

d periodi

c blowback

. I tals o supplie s calibratio

n gase s throug h th e samplin

g system . Th e stac k ga s sampl e i s maintaine

d a tapproximatel

y 185° C throug

h th e

1

### samplin g equipmen

tan d analyze

rsampl e cel l t o preven tth e remova

l o f pollutant

s from th e sampl e throug h contac twit h condense

d moisture

. Th e sampl e cell consist

s o f multipl e mirror s tha twer e adjuste d an d aligne d a tth e factor y t o se tth e pat h lengt h appropriat

e fo rth e specifi c application

. Th e MC 3 multicomponen

t L Rphotomete

ruse s aGa s FilterCorrelatio

n analytica

l techniqu

e t o continuousl

y monito r th e stac k ga s concentration

s of HC I an d CO . Th

e Singl e Bea m Dua l Wavelengt

h analytica l techniqu

e is use d t o continuousl

y monito

rstac k ga s wate rvapo r(H2O ) concentrations

. A technica

l descriptio

n an d specificatio

n forth e CEM S i s presente

d i n Sectio

n 2. 0 o f th e MC 3 Operations Guide, Section 2.1. 1 document s th e lowes trang e foreac h componen

t an d a n accurac

y o f ±2 % o f full-scale value. Th

e lowe rthreshol

d i s 1 % of th e lowes t range . Thes e technica

l specification

s documen

ttha tth e CEM S i s capabl

e o f meetin g th e requirement

s o f th e Appendi

x t o Par t63 , Subpar

tEE E an d Perfonnanc

e Specificatio

n 4 B o f 4 0 CF RPar

t60 , Appendi

x B . Th e syste m controlle

rcontrol

s th e samplin

g syste m temperatures

, purge/blowback

, calibratio

n checks, dat

a handhng

, messaging

, an d alarms . Th e CEM S controlle

ri s integrate d wit h th e incinerato

rdat a acquisitio

n system , automati

c wast e fee d cutof f (AWFCO ) system

, an d th e mai n contro l system . Al l thre e incinerator

s ar e equippe

d wit h COS A mode

l ZFN-11YA1-2Z 1 O

2 analyzers

. Thes e analyzer

s ar e zirconiu

m oxid e cell s an d ar e locate d downstrea

m ofth e L

D fan. 1. 2 Overvie

w o f Regulator

y Requirement

s Cross-reference

s an d summarie

s o f th e applicabl

e regulator

y requirement

s ar e presente

d i n Tabl e 1-1 . This tabl

e indicate

s th e sections

, tables , an d figures of

thi s documen

ttha t addres s eac h particula

rrequirement

.

2 VE S 00089 2

# c Tabl e 1- 1 Regulator y Requirement s fo r th e CEM S Q C Progra m an d th e CEM S Q A Pla n Regulator y Reference : Appendi x t o Subpar t EE E o f Par t 6 3 Descriptio n CEM S Q A Pla n Sectio n 

### Sectio n 3.1.a. 1 Check s fo rcomponen

tfailures, leaks

, an d othe r abnorma l condition

s 3. 0 3.1 Sectio n 3.1.a. 2 Calibratio n of CEM S 2. 2 Sectio n 3.1.a. 3 Cahbratio n Drif tdeterminatio

n an d adjustmen

t o f CEM S 2.1,2.2 Appendi x A Sectio n 3.1.a. 4 Integratio n o f CEM S wit

h th e AWFC O syste

m 4.

0 Sectio n 3.1.a. 5 Preventiv e Maintenanc

e of CEM S (includin

g spar e part s inventory

) 3. 0 Appendi x A Sectio n 3 . l.a. 6 Dat arecording

, calculations, an

d reportin

g 4. 1

5. 0 Sectio n 3.1 . a . 7 Check s of recor d keepin g 5. 0 Sectio n 3.1.a. 8 Accurac y audi tprocedures

, includin g samplin

g an d analysi s method s 2.3,2.5 Appendi x A Sectio n 3.1.a. 9 Progra m o f correctiv

e actio n formalfunctionin

g CEM S 3. 4 Sectio n 3.1.a.l0 Operato rtrainin g an d certificatio

n 6. 0 Sectio n 3.1. b Reportin g o f excessiv e inaccuracie

s 5. 0 Sectio n 3.2. 1 Q A responsibilitie s 5. 0
Sectio n 3.2. 2 Schedule s for : (1 ) dail y check s (2 ) periodi

c audit s (3 ) preventiv

e maintenanc

e (1 ) 3.0,3. 1 (2 ) 2.0 , Tabl e 2- 1 (3 ) 3. 0 Sectio n 3.2. 3 Chec k hst s an d dat asheet s Appendi x A Sectio n 3.2. 4 „— , __=_= , 

### Preventiv e maintenanc

e procedure

s 3. 0 

# (

VE S 00089 3

### (

V Tabl e 1-1 (Continued )

Regulator y Requirement s fo r th e CEM S Q C Progra m an d th e CEM S Q A Pla n Regulator y Reference : Appendi x t o Subpar t EE E o f Par t 6 3 Descriptio n CEM S Q A Pla n Sectio n


### Sectio n 3.2. 5 Descriptio n o f th e media , format , an d locatio n o f al l record s an d report s 5. 0
Sectio n 3.2. 6 Provision s fo rrevie

w o f th e CEM S data; revision s o rupdate s o f th e Q A pla n base d o n revie w 5. 0
Sectio n 4. 1 Check, record, quantify : (1) Zer

o Drif t (2 ) Cahbratio

n Drif t 2. 1
Sectio n 4. 2 Recordin g Requirement

s for : (1) Zer

o Drif t (2 ) Cahbratio

n Drif t 2. 1 Appendi x A Sectio n 4. 3 Dail y Syste m Audi t 3. 1 Sectio n 4. 4 Dat arecordin

g an d reportin

g 5. 0 Sectio n 5.1 Relativ e Accurac

y Tes tAudit(RATA ) 2. 5 Sectio n 5. 2 Absolut e Calibratio

n Audit(ACA ) 2. 3 Sectio n 5. 3 Interferenc e Respons

e Tes t(IRT ) 2. 4
Sectio n 5. 4 Excessiv e audi tinaccuracie

s Tabl e 2-1 2. 3 2. 5



# (

VE S 00089 4

### 2. 0 CEM S CALIBRATION S AN D PERFORMANC E Th e CEM S mus

tb e operated

, calibrated

, an d maintaine

d t o ensur e conformanc

e wit h th e Appendi x t o Par t63, Subpar

tEE E an d th e EP A Performanc

e Specificatio

n 4 B (P S 4B) . Cahbratio

n drif tcheck s an d performanc

e demonstration

s ar e performe

d periodicall

y o n th e CEM S base

d o n th e followin

g schedule :

• Dail y calibratio

n check s fo rdeterminatio

n o f Calibratio

n Drif t(CD) an

d Zer o Drif t(ZD) . • Quarterl

y Absolut

e Calibratio

n Audit(ACA ) fo rdeterminin g cahbratio

n erro r (CE)for0 2 

### , CO , an

d HCI . • Annua

l Relativ e Accurac

y Tes tAudi t(RATA ) fordeterminin g th e CEM S relativ

e accurac y (RA ) fo rC O emissions

. Th e procedures

, Q C criteria

, correctiv

e actions , an d recordkeepin

g associate

d wit h thes e drif tcheck s an d audit s ar e describe

d i n thi s section . A summar

y o f th e Q C criteri

aan d correctiv e action s i s presente

d i n Tabl

e 2-1 . Blan

k dat asheet s ar e provide

d i n Appendi

x A . 2.1 Dail y Drif

tCheck s Dail y drif

tcheck s ar e automaticall

y initiate d by th e CEM S controller

. Durin g th e automate d calibratio

n sequence

, calibratio

n gase s ar e injecte d from pressurize

d cylinder

s throug h th e samplin

g system . Th e sequenc

e start s wit h th e L Ranalyze

rzer o ga s tha ti s free o f an y o f th e constituent

s analyze d b y th e I Ranalyzer

. This zer

o ga s ma y als o serv e a s th e spa n ga s forth e integrate

d O 2 analyzer

. Th e zer o ga s flow s throug h fh e syste m wit h enoug h tim e allowe d forth e analyze rt o full y respon

d t o th e gas . The n th e analyze r respons e t o th e zer o ga s is recorde

d foron e minut e an d averaged

. Th e nex tcahbratio

n ga s i n th e cahbratio

n sequenc

e is th e firstI Ranalyze

rspa n gas . This spa

n ga s i s a cahbratio n standar d tha tha s on e o rmor e constituen

tconcentration

s a tth e analyze rspa n valu e (thi s ga s ma y als o b e use d a s th e zer o ga s forth e O 2 analyzer) . Th

e firstspa

n ga s flow s throug h th e syste m t o allo w th e analyze

renoug h tim e t o fully respon

d t o th e gas . The n th e analyze rrespons e t o th e firs tspa n ga s is recorde

d fo ron e minut e an d averaged

. This i s the n repeate

d forfh e secon d spa n ga s an d the n possibl

y a thir d spa n ga s dependin g upo n th e compositio

n o f th e spa n gases . Th e tota l duratio n o f thi s cahbratio

n sequenc e ha s bee n designe

d t o no texcee d th e 2 0 minut e maximu

m allowabl

e CEM S downtim e whil e burnin g hazardou

s waste .



### VE S 00089 5/—* \

Tabl e 2- 1 Overvie wo f CEM S Performanc e Requirement s Analyze r Paramete r (Spa n Value ) Q C Paramete r Minimu m Frequenc y Q C Limi t Correctiv e Actio n 

### H 2 

### 0 (60% ) 

### Z D Daily ±2 % of spa n Zer

o Adjustmen

t

o 2 (25% ) 

### Z D an

d C D Daily ±0.5 % 0 2 

### Zero/Spa n Adjustmen

t

o 2 (25% ) 

### C D Daily ±1.0%O 2 

### Shu tof f waste , service/calibrate

, conduc tAC A o 2 (25% ) 

### Cumulativ e Spa n Adjustmen

t Pe

r Adjustmen

t ±1.5 % 0 2 

### Shu tof f waste , service/calibrate

, conduc tAC A o 2 (25% ) 

### C E Quarterly 1 

### 0.5 % 0 2 

### Shu

tof f waste , service/calibrate

, conduc t RAT A o 2 (25% )


### R A Annuall y 1.0

% 0 2 

### Shu

tof f waste , service/calibrate

, repea tRAT A

C O (20 0 ppm ) 

### Z D an d C D Daily ±3 % of spa n Zero/Spa

n Adjustmen

t

C O (20 0 ppm ) 

### C D Daily ±5 % o f spa n for6 ou tof 7 da y Shu

tof f waste , service/calibrate

, conduc tAC A
C O (20 0 ppm ) 

### C D Daily ±6 % o f spa n Shu

tof f waste , service/calibrate

, conduc tAC A C O (20 0 ppm ) 

### Cumulativ e Spa n Adjustmen

t Pe

r Adjustmen

t ±9 % of

spa n Shu

tof f waste , service/calibrate

, conduc tAC A C O (20 0 ppm ) 

### C E Quarterly 1 

### 5 % Shu

tof f waste , service/calibrate

, conduc t RAT A C O (20 0 ppm )



### R A 2 

### Annuall y 5 ppmd

v @ 7 % 0 2 

### (Se e Sectio n 2.5 ) Shu

tof f waste , service/calibrate

, conduc t RAT A Th e ACA s fordeterminin

g th e 0 2

### an d C O C E ar

e conducte

d quarterly

, excep ti n aquarte

rwhe n aRAT A i

s conducte

d instead . Th e R A accurac

y forC O i

s base d o n th e unit s o f th e C O emissio

n standar

d (ppmd v @ 7 % 0 2 

### ) . C O dat

a collecte

d fro m th e analyze rdurin g th e RAT A wil l includ

e lo w an d o rhig h rang e value s pe rth e norma l operatin

g requirements

. 6


### VE S 00089 6Tabl e 2- 1 (continued ) Overvie wo f CEM S Performanc e Requirement s Analyze r Paramete r (Spa n Value ) Q C Paramete r Minimu m Frequenc y Q C Limi t Correctiv e Actio n

C O (3000 ppm ) 

### Z D an d C D Daily ±3 % o f spa n Zero/Spa

n Adjustmen

t
C O (3000 ppm ) 

### C D Daily ±5 % of spa n fo r6 ou to f 7 da y Shu tof f waste , service/calibrate

, conduc tAC A C O (3000 ppm ) 

### C D Daily ±6 % o f spa n Shu

tof f waste , service/calibrate

, conduc tAC A C O (3000 ppm ) 

### Cumulativ e Spa n Adjustmen

t Pe

r Adjustmen

t ±9 % o

f spa n Shu

tof f waste , service/calibrate

, conduc tAC A C O (3000 ppm )
C E 

### Quarterly 3 

### 5

% Shu

tof f waste , service/calibrate

, conduc tRAT A

HC I (100 0 ppm ) 

### Z D an d C D Daily ±3 % o f spa n Zero/Spa

n Adjustmen

t
HC I (100 0 ppm ) 

### C D Daily ±5 % o f spa n fo r6 ou to f 7 da y Shu tof f waste , service/calibrate

, conduc tAC A HC I (100 0 ppm ) 

### C D Daily ±6 % o f spa n Shu

tof f waste , service/calibrate

, conduc tAC A HC I (100 0 ppm ) 

### Cumulativ e Spa n Adjustmen

t Pe

r Adjustmen

t ±9 % o

f spa n Shu

tof f waste , service/calibrate

, conduc tAC A HC I (100 0 ppm )


### C E Quarterly 4 

### 5

% Shu

tof f waste , service/calibrate

, conduc tAC A Th e ACA s fo

rdeterminin

g th e 0 2

### an d C O C E ar

e conducte

d quarterly

, excep ti n aquarte

rwhe n aRAT A i

s conducte

d instead . A RAT A fo

rHC I ma y b e performe

d annuall y i n lie u o f perforrnin

g a n AC A i n tha

tquarter .

7



### VE S 00089 7

### Th e drif tforeac h stac k ga s constituen

ti s determine

d a s th e differenc

e betwee n th e know n constituen

tconcentratio

n i n th e calibratio

n ga s an d th e analyze

rreading

. Z D i s th e drif tdetermine

d usin g zer o gas . C D i s th

e drif tdetermine

d usin g spa n gases . Z D an d C D ar e determine

d dail y forO2 , CO , an d HCI . Z D forH2

O i s als o determine

d daily . Th e Z D an d C D ar e recorde d by th e CEM S datalogge

ra s apercen

to f full-scale deviatio

n (Dev%). Give

n tha tth e "spa n value " i

s equa l t o th e "full-scale " value, Dev% i s calculate d a s follows : Dev%=-\Drift%\

n reference concetration - analyzerresponce ,„„ Drift% = ^ L— ——- --100 span value 

### Fo rC O an

d 0 2 

### , i f Dev% fo rC D exceed s th e limit s specifie

d i n th e apphcabl

e Performanc

e Specification

s i n 4 0 CF RPar

t60 , Appendi

x B , th e analyze

rmus tb e cahbrated

. If th e Dev % forC D is greate

rtha n th e prese ttoleranc e (Tol% ) th

e instrumen

t technicia n wil l notif

y th e incinerato

roperato

ran d wast e feed s wil l b e shu tof f unti l correctiv e measure

s hav e bee n taken . Th e C D tolerance

s forbot h O 2 an d C O hav

e bee n se ta tth e tw o time s th e performanc

e specificatio

n hmits . A calibratio n failur e alar m indicate s tha tth e analyze ri s out-of-contro

l an d mus tb e service d an d recalibrated. A n AC A mus

tb e conducte

d t o documen

ttha tth e analyze

ri s withi n th e performanc

e specification

s priort o resumin

g hazardou

s wast e burning. Fo rCO , i f

th e Dev % fo

rC D is greate

rtha n 5 % fo r6 ou

to f 7 days , the n th e analyze

ri s out-of-contro

l an d mus tb e service d an d recalibrated

. A n AC A mus

tbe conducte

d t o documen ttha tth e analyze

ri s within th

e performanc

e specification

s priort o resumin

g hazardou

s wast e burning

. Simila rrequirement

s fordrif

tlimit s appl y t o HCI , excep

ttha tn o performanc

e specification

s hav e bee n promulgate

d fo rCEM S monitorin

g thes e parameters

. I n he u o f limit s specifie

d by a n EP A Performanc

e Specification , Veoli a ha s develope

d selfimpose d performanc

e specificatio

n hmit s fo rHCI . Thes

e hmit s ar e specifie d i n Tabl

e 2 - 1 . 2. 2 Calibratio n Cahbratio

n o f th e analyze

rwil l be conducte

d periodicall

y t o ensur e tha tth e result s o f drif tchecks, ACAs , o

rRATA s mee

tth e applicabl

e performanc

e specifications . 8 

### VE S 00089 8

### Calibratio n fo reac h I Rchanne l (H2O , CO , an d HCI ) ma y b e performe

d dail y durin g th e automate d cahbratio

n sequenc

e use d t o determin

e cahbratio

n drift . Foreac h calibratio

n ga s use d durin g th e automate

d sequence

, th e automati

c calibratio

n wil l rese

tth e analyze r respons e t o correspon

d wit h th e know n referenc

e concentrations

. Any automate

d calibratio

n adjustmen

twil l b e mad e immediatel

y afte rth e analyze

rrespons

e t o th e calibratio n ga s is recorde

d electronically

. Th e drif tdetermine

d immediatel

y prio rt o a calibratio n adjustmen

ti s equa l t o th e magnitud

e o f th e adjustment

. Th e oxyge n analyze

r use s a two-poin

tcalibratio

n curve . Th e firs tcalibratio

n poin treset s th e measure

d concentratio

n o f ai rt o 20.94%

. Th e secon d calibratio

n poin treset s th e measure

d concentratio

n o f a lo w concentratio

n calibratio

n ga s t o it s know n concentration

. Thi s cahbratio

n i s performe

d manually

. T o documen

tfh e cahbratio

n adjustment

, th e actua l measuremen

ta teac h cahbratio

n poin tpriort o adjustmen

twil l b e recorded

. Following servic

e t o th e MC 3 analyze

rtha tcoul d affec tit s calibration

, eac h ER . channel , an d th e 0 2

### analyze

rwill b e calibrated

. Th e CEM S Drif

tan d Cahbratio

n Dat a Shee ti n th e Appendi

x t o thi s documen

twill b e use d t o trac k th e cumulativ

e spa n adjustment

s (i.e. , chang

e i n th e calibratio

n factor) . Sectio

n 5. 5 ofth e MC 3 CEM S Operations Guide an d Sectio n 4. 4 o f th e MC 3 CEM S System Guide shoul d be referre

d t o a s neede d fo r additiona l detai l regardin

g cahbratio

n o f th e CEMS . I f th e cumulativ

e calibratio

n adjustmen

tforC D is thre

e time s th e performanc

e specificatio

n limit s a tan y time , hazardou

s wast e burnin g wil l b e cutoff . Th e analyze

r wil l b e serviced, recalibrated , an d a n AC A wil l documen

ttha thazardou

s wast e burnin g ca n recommence

. A calibratio

n facto rtha tha s bee n verifie d throug h a n AC A wil l becom e th e ne w referenc

e poin tforassessin

g th e cumulativ

e adjustment

s mad e t o correc t fo rcahbratio

n drift . Th e incinerato

rca n remai n o n hazardou

s wast e durin g CEM S drif

tchecks , calibrations

, purges , an d correctiv

e action s forCEM S failure

s provide d tha tth e CEM S downtim

e doe s no texcee d 2 0 minutes

. Durin g thes e times, th

e instantaneou

s value s use d t o determin

e one-minut

e average

s of dry , oxyge n correcte

d concentration

s o f C O ar e discarded

. This allowanc e i s provide

d by Sectio

n 6. 2 an d 6.5.1 o f

th e Appendi

x t o Subpar tEEE . Th

e applicabl e regulator

y requirement

s d o no tlimi tth e frequenc

y tha tthi s allowanc

e ca n b e utilized . Typically , thi s allowanc

e wil l onl

y be utilize

d onc e pe rda y forth e dail y drif t checks . Sinc e th e oxyge n analyze

rcanno tb e calibrate

d durin g th e automati

c cahbratio

n o f th e I Rchannels

, calibratio

n o f th e oxyge n analyze

rwil l requir

e additiona

l downtime

.

### I f a ther e is aCEM S failure

, th e incinerato

rma y remai n o n hazardou

s wast e provide

d tha t th e CEM S ca

n be restore

d withi n 2 0 minutes. Following downtime

, th e CEM S mus

tb e withi n th e performanc

e specification

s describe

d i n thi s document

. Otherwise

, hazardou

s wast e burnin g wil l ceas

e unti l th e appropriat

e correctiv e measure

s ca n b e taken . T o ensur

e tha tth e hourl y rolling averag

e (HRA ) fo

r C O is representativ

e o f curren toperatin

g conditions, CEM S dat avahdit y mus tb e a tleas t 75 % (i.e. , 6 0 vali d on

e minut e average

s pe r8 0 minute s o f norma l operations). 2. 3 Absolut e Calibratio n Audi t 

### A n AC A is conducte

d quarterl

y fo rO2 , C O (hig

h an d lo w range), an

d HCI . ForO

2 an d CO , a n AC A i s no tconducte

d i n th e quarte rtha tth e require d annua l RAT A is performed

. Th e AC A i s conducte

d accordin

g t o th e cahbratio

n erro r(CE ) tes

tprocedur

e describe

d in th e Performanc

e Specification

s 4B . During fh

e ACA , th

e analyze

ri s challenge

d ove r eac h rang e wit h EP A Protoco

l 1 cylinde

rgases . Th e EP A Protoco

l 1 cylinde

rgase s ar e NIS T traceabl

e cahbratio

n standards

. Fo ra give

n parameter

, th e analyze

rrespons e i s recorde d a tthre e measuremen

tpoints. This i

s the n repeate d twic e t o giv e thre e set s o f data . Th e C E a teac h measuremen

tpoin ti s determine

d a s follows :
CE=~-100% FS 

### wher e d is th e mea n differenc

e betwee n th e CEM S respons

e an d th e know n referenc

e concentratio

n an d F S i s th

e spa n value . ForC O an

d HCI , th

e C E determine

d a teac h measuremen

tpoin tcanno texcee d 5% . For O2 , C E canno

texcee d 2% . If a n AC A fail s t

o pas s th e Q C criterio

n (i.e. , th

e audi t indicate s excessiv

e inaccuracy) , the

n hazardou

s wast e burnin g canno tresum e unti l correctiv e measure

s hav e bee n take n an d a RAT A demonstrate s tha tth e CEM S i

s operatin g withi n th e performanc

e specifications . 2. 4 Interferenc e Respons e Tes t 

### Th e MC 3 analyze

rcorrect

s forinterference

s usin g additiv

e an d multiphcativ

e interferenc

e tables. Thes

e table s wer e generate

d pe rth e manufacturer' s procedur e a tth e initia l setu p o f th e CEM S system

. A n Interferenc

e Respons

e Tes t(IRT ) i s liste d i n th e Appendi x t o Subpar tEEE , however

, th e Performanc

e Specificatio

n 4 B doe s no tinclud e requirement

s o racceptanc

e criteri afo ra n interferenc

e respons e test . Veoli awil l perfor

m
1 0 

### VE S 00090 0

### Interferenc e Respons

e Test s a tsuc h tim e a s U S EP A specifie

s th e tes tprocedure

s an d acceptabl e criteri afo ra n Interferenc

e Respons

e Test . 2. 5 Relativ

e Accurac

y TestAudi t Th e Relativ e Accurac

y Tes tAudi t(RATA ) i

s require d annuall

y for0 2

### an

d C O CEMS. . Th e Relativ e Accurac

y (RA ) tes

tprocedure

s require d by Sectio

n 7. 2 o f P S 4 B reference

s incorrec tsection s o f P S 3 (fo r0 2 

### ) an d P S 4 A (fo rCO) . Th

e apphcabl

e section s of th e performanc

e specification

s are :

• RAT A procedures : Section s 8.4. 3 throug h 8.4. 5 o f P S 2 . • 0 2

### referenc

e methods : Sectio

n 8. 2 of PS 3
• C O referenc

e methods : Sectio

n 8. 2 o f P S 4A . • 0 2

### R A calculations : Sectio n 12. 0 o f P S 3
• COR A calculations : Sectio n 12. 0 o f P S 2
• 0 2

### R A criterion : Sectio n 13. 2 of PS 3
• C O R A criteria : Sectio n 13. 2 o f P S 4 A A brie f summar y o f th e applicabl

e referenc

e method s ar e provide

d below . U S EP A Metho

d 3/3A (Stac

k Ga s Compositio

n an d Molecula

rWeight ) Th e samplin

g an d analytica

l procedure

s outline d in thi s metho d wil l b e use d t o determin

e th e 0 2

### compositio

n o f th e stac k ga s durin g th e RATA . Using thi

s method , aga s sampl e is extracte

d from th

e stac k a ta constan

trat e fo rdeterminatio

n o f 0 2 

### , C0 2

### an

d molecula

r weight . Th e integrate

d gasba g collectio

n optio n will b e employed

. Th e gasbag s wil l b e analyze d usin g a n Orsa tanalyzer

. A s a n alternative

, th e Metho d 3A (instrumenta

l analyzer ) metho d mayb e use

d fo ranalysi s of th e sample . U S EP A Metho

d 4 (Stac k Ga s Moistur

e Content

) I f necessary

, th e samplin

g an d analytica

l procedure

s outline d in thi s metho d wil l b e use d t o determin

e th e moistur

e conten tof th e stac k ga s durin g th e RATA . Usin

g thi s method , a ga s sampl e i s extracte

d from th

e stack . Th e ga s passe s throug h a serie s o f impinger

s tha tcontai n reagents

. Th e impinger

s ar e connecte

d i n serie

s an d ar e containe

d i n a n ic e bat h in orde rt o assur e condensatio

n o f th e moistur

e i n th e ga s stream . Any moistur

e tha t is no tcondense

d i n th e impinger

s is capture

d i n th e silic a gel, ensurin

g tha tal l moistur e ca n b e weighe d an d entere d int o moistur e calculations. U S EP A Metho

d 1 0 f Carbo n Monoxid

e CEMS ) 1 1

### A continuou s emission

s monito rwil l b e use d t o continuousl

y sampl e exhaus tga s fo r carbo n monoxid

e analysi

s a s describe

d i n EP A Metho

d 10 . Using thi

s method

, a continuou

s ga s sampl e i s extracte

d from th

e exhaus tgas , an d is analyze

d forcarbo

n monoxid e (CO ) usin

g aLuft-type Non-Dispersiv e mfrare d Analyze

r(NDTR) , o

ranothe r equivalen

tanalyzer

. Thi s samplin

g an d analysi s wil l occu

rcontinuousl

y throughou

tth e duratio n o f eac h ru n ofth e RATA . During a tes

tru n o f th e RATA , U S EP A referenc e method s ar e utilize d t o obtai n stac k ga s data . Thes e dat a ar e use d t o calculat

e th e stac k ga s dr y O 2 concentratio

n an d th e stac k ga s C O concentratio

n correcte

d t o seve n percen toxyge n i n unit

s o f part s pe r million , dr

y volum e (i.e. , i n th

e unit s ofth e emissio

n standard

, 10 0 ppmd v C O @ 7

% O2)
. The averag

e stac k ga s 0 2

### (% , dry ) an d C O (ppmdv

, @ 7 % 0 2 

### ) concentrations—a s calculate d from th

e installe d CEM S ove

rth e duratio n o f th e run—ar

e compare

d t o th e valu e obtaine d usin g th e referenc

e methods

. Th e RAT A consist

s o f a minimu

m o f 9 tes t runs. If mor e tes trun s ar e conducted

, a tleas t9 dat a set s wil l b e use d t o detennin

e RA , an d n o mor e tha n thre e set s o f dat awil l b e rejected

. Th e O 2 an d C O R A calculation

s an d acceptanc

e criteri aar e presente

d below .

RA,

### co d

+ CC RM •100% < 10% ...forRM > 50ppmdv @ 7% 0 2 \d\ + |CC | < 5ppmdv@7% 0 2...forRM < 50ppmdv @ 7% 0 2 

### where , d = — - V (RM. - CEMS,)


### n = numbe

ro f tes trun s RMi = th

e concentratio

n determine

d b y th e referenc

e metho d fo rth e i t h

### tes tru n CEMSi = th

e concentratio

n determine

d b y th e CEM S forth

e 1 t h 

### tes tru n CC = th

e 2. 5 percen terro rconfidenc

e coefficien

t(se e Sectio n 12. 4 o f P S 2 )

If aRAT A fails t

o pas s th e Q C criterio

n (i.e. , th

e audi tindicate s excessiv

e inaccuracy) , the n hazardou

s wast e burnin g canno tresum e unti l correctiv

e measure

s hav e bee n take n an d a RAT A demonstrate s tha tth e CEM S i s operatin

g withi n th e performanc

e 1 2 VE S 00090 2

### specifications . I f C O emissio

n level s ar e significantl

y low, itma

y b e difficultt

o produc e meaningfu

l result s usin g th e R A tes tprocedure

. Unde rthes e circumstances

, Veoli awill reques tapprova

l t o utiliz e th e Alternativ

e R A Procedur

e prescribe

d b y Sectio

n 7. 3 o f P S 4B . .

1 3 

### VE S 00090 3

### 3. 0 CEM S MAINTENANC E Veoli aha

s develope

d apreventativ

e maintenanc

e progra m forth e CEMS . This progra

m include s frequen

tinspection

s o f th e CEM S i n orde

rt o identif y potentia

l componen

t failures , leaks, an

d dat a qualit y issues. Th

e CEM S preventativ

e maintenanc

e progra m als o include

s schedule

d replacemen

to f critica l component

s an d maintenanc

e o f spar e part s inventory

. Al l schedule

d an d unschedule

d maintenanc

e o f th e CEM S wil l b

e documente

d i n aCEM S logboo

k maintaine

d foreac h incinerator

. Sectio n 8. 0 ofth e MC 3 CEM S Operations Guide provide s detail s fordaily, weekly, monthly , quarterly

, an d annua l inspectio

n an d maintenanc

e activities . Procedure s an d recordkeepin

g forth e specific inspectio

n an d maintenanc

e activitie

s ar e describe

d below . 3. 1 Dail y Syste

m Audi t Th e Dail y Syste

m Audi tincludes :

• Revie

w of th e dail y drif tchec k dat a
• Inspectio

n ofth e recordin

g syste m
• Chec k fo rcontrolle

ralarm s an d error/warnin

g message

s
• Chec k expecte d calibratio

n value s
• Chec k of curren tdat astatu s
• Chec k o f calibratio

n ga s cylinderpressure

s
• Chec k calibratio

n ga s pressur e regulato

rsetting s
• Inspectio

n o f th e instrumen

tai rpressur e
• Inspectio

n o f th e stac k ga s samplin

g syste m Th e Dail y Syste

m Audi tChecklis

twil l b e use d t o documen

tth e trading s fro m th e dail y syste m audit . A CEM S Drif

tan d Cahbratio

n Dat a Shee twil l b e complete

d durin g th e dail y syste m audi ti n orde rt o trac k an d evaluat e drif tan d adjustment

s mad e t o th e CEMS . 3. 2 Spar

e Part s Inventor

y CEM S spar

e part s ar e maintaine

d i n sufficien

tquantitie

s on-sit e t o perfor m routin

e maintenanc

e activities. I

ti s anticipate

d tha tthes e spar e part s an d typica l maintenanc

e supplie s wil l b e adequat

e t o servic e th e CEMS . Som

e service s an d replacemen

tof component

s mus tb e performe

d b y a n EcoChe

m Analytic

s Servic e Enginee

rt o avoi d violatio n ofth e syste

m certification.

1 4 

### VE S 000904

### Th e following consumabl e part s hav e bee n targete d fo rperiodi c inspectio

n an d replacemen

tformaintainin

g th e CEMS :

• Ai rconditione

rfilter s forCEM S shelte

r
• mstrumen

tai rcoalescin

g filters

• Sampl

e pum p Teflon diaphrag

m
• Sampl

e pum p Teflon flappervalv

e
• Sampl

e prob e interna l filter
• Sampl

e prob e gasket s
• Probe-ti

p filter Th e following spar

e part s ar e no tpar to f routin e maintenanc

e an d woul d be replac

e b y a n EcoChe m Servic e Engineer :

• Cel l fron

tcove rgaske t
• Cel l inle

tfilter
• Cel l window

s wit h o-rin g gasket s
• Cel l mirror

s Th e CEM S Calibratio

n Ga s an d Spar e Part s Lo g i s provide d i n Appendi

x A an d wil l b e use d a s neede d t o kee p trac k o f inventory

. 3. 3 Calibratio n Ga s Suppl y an d Certificatio n 

### A summar

y o f th e cahbratio

n gase s neede d t o perfor m th e dail y drif tchecks, calibrations

, an d ACA s i s presente

d i n Tabl

e 3-1 . Th

e numbe ro f ga s cylinder

s maintaine

d on-sit e depend s o n th e specific mixtur

e o f gase s i n eac h cylinde ran d th e lea d tim e require d for placin g orders . A n inventor

y o f cahbratio

n gase s wil l b e conducte

d i n conjunctio

n wit h th e spar e part s inventor

y t o ensur e tha tth e appropriat

e gase s ar e availabl

e fo ruse

. Certificatio

n fro m th e supplie ro f cahbratio

n ga s qualit y wil l b e kep twit h th e mos trecen t spar e part s inventor

y documentation

. Eac h calibratio

n sequenc

e deplete s approximatel

y 4 0 psi , an d a cylinde

rwit h les s tha n 15 0 psi shoul

d b e replaced ; Th

e dail y syste m audi tinclude s inspectio

n o f th e calibratio

n ga s cylinde rpressure

s an d wil l b e use d trac k usag e an d t o predic twhe n t o reorder

.

1 5 

### VE S 00090 5

### Tabl e 3- 1 Summar y o f Concentratio

n Requirement

s fo rCalibratio n Gase

s
Constituen

t Q C

Paramete

r Concentration Requiremen

t Accuracy H 2 

### 0 Z D 0 % pe

rga s supplie r o 2 

### Z D 0 % pe

rga s supplie r o 2 

### C D 25 % pe

rga s supplie r o 2 

### AC A 0-2 % EP A Protoco

l 1/NIST Traceabl

e o 2 

### AC A 8-10 % EP A Protoco

l 1/NIST Traceabl

e o 2



### AC A 14-16 % EP A Protoco

l 1/NIST Traceabl

e C O (lo w range ) Z D Opp m pe

rga s supplie r (lo w range ) C D 20 0 pp m pe

rga s supplie r C O (lo w range ) AC A 0-4 0 pp m EP A Protoco

l 1/NIST Traceabl

e C O (lo w range )
AC A 60-8 0 pp m EP A Protoco

l 1/NIST Traceabl

e C O (lo w range )

AC A 140-16 0 pp m EP A Protoco

l 1/NIST Traceabl

e C O (hig h range ) Z D Opp m pe

rga s supplie r (hig h range ) C D 300 0 pp m pe

rga s supplie r C O (hig h range ) AC A 0-60 0 pp m EP A Protoco

l 1/NIST Traceabl

e C O (hig h range )
AC A 900-120 0 pp m EP A Protoco

l 1/NIST Traceabl

e C O (hig h range )

AC A 2100-240 0 pp m EP A Protoco

l 1/NIST Traceabl

e HC I Z D Opp m pe

rga s supplie r I C D 100 0 pp m pe

rga s supplie r HC I AC A 0-20 0 pp m EP A Protoco

l 1/NIST Traceabl

e HC I
AC A 300-40 0 pp m EP A Protoco

l 1/NIST Traceabl

e HC I

AC A 700-80 0 pp m EP A Protoco

l 1/NIST Traceabl

e |

1 6 

### VE S 00090 6

### 3. 4 Corrective Actio n fo rMalfunctioning CEM S I tis Veolia' s polic

y t o minimiz

e th e occurrenc

e of malfunction

s by takin

g aproactiv

e approac h t o faciht y maintenance

. Proactiv

e measure

s includ e th e preventiv

e maintenanc

e describe

d i n thi s section , an d th e calibratio

n an d performanc

e testin g describe d i n Sectio

n 2.0 . Frequen

tinspection

s an d availabiht

y of spar e part s allo w for th e timel y completio

n o f a s neede d servic e t o th e CEM S prio

rt o amajo rmalfunction

. Operatin g an d maintainin

g th e incinerato

rdurin g amalfunctio

n wil l b e conformanc

e wit h th e Startup, Shutdown, and Malfunction Plan (SSMP) . Attachmen t4 t o th e SSMPi

s th e Program of

Corrective Action forMalfunctions. Sectio n 9. 2 o f th e Program of 

### Corrective Action forMalfunctions addresse s correctiv

e action s formalfunctionin

g CEMS . Sectio

n 9. 0 throug h 9. 2 ofth e MC 3 CEM S Operations Guide maybe referre d t o a s neede d fortroubleshootin

g an d correctiv

e maintenanc

e o f th e CEMS .

1 74.0 . INTEGRATIO N O F TH E CEM S WIT H TH E AWFC O SYSTE M 

### Th e CEM S i s integrate

d wit h th e automati

c wast e fee d cutof f (AWFCO ) syste

m t o assur e on-goin g comphanc

e wit h C O emissio

n standards

. Th e AWFC O syste

m is designe

d t o immediatel

y an d automaticall

y shu tof al l wast e t o th e incinerato

rin th e even tof a n exceedanc

e o f a n emissio

n o roperatin

g limit . Th e CEM S i

s integrate

d wit h AWFC O syste m throug

h interlocks. Thes

e interlock

s ar e condition

s whic h trigge rarela y causin g th e AWFC O syste

m t o activate

. This sectio

n describe

s th e AWFC O interlock

s associate

d wit h th e CEMS . 4. 1 Emissio n Standard s 

### Th e CEM S ra

w dat a for0 2

### (

% vol) , H 2 

### 0 (

% vol) , an

d C O (ppmv

) consist s o f instantaneou

s value s whic h hav e no tbee n smoothe

d o raveraged

, evaluate

d onc e ever y 1 5 seconds

. Thes e value s ar e use d t o calculat

e C O emission

s i n th e unit s of emissio n standards

. Calculation

s equivalen

tt o th e following procedure

s ar e performe

d t o compar

e th e stac k ga s emission

s t o th e C O emissio

n standard

. Firs t15-secon

d dat a i n th e unit s of th e emissio n standard

s ar e calculated : f \ CO@7%0 2

,ppmdv •• CO, ppmv



### WO%-(H 2 

### O,%) 14%

21%- o 2

,% 

### 100%-(H 2 

### O,%)
Th e calculate

d 15-secon

d dat a ar e the n use d t o calculat

e one-minut

e average

s (OMAs) . Th e curren tminut e OM A is average

d wit h th e previou

s 5 9 OMA s t

o generat e a n hourl y rolling averag

e (HRA) . Al l roundin

g i s avoide d fo rth e number

s use d t o calculat

e HRAs . Th e HR A of

C O emission

s ar e rounde d t o tw o significan

tfigures. I f th e HR A C O emissio

n concentratio

n exceed s th e C O emissio

n standar

d of 10 0 ppmd v @ 7 % 0 2 

### , a n AWFC O wil l occur

. 4. 2 Drif t Limit s 

### A s describe

d i n Sectio

n 2.1 , wast

e feed s will b e manuall

y shu tof f i n cas e adrif tlimiti s exceeded . Fo rC O an

d 0 2 

### , drif

tlimit s ar e equa l t o 2 time

s th e performanc

e specifications . Comparabl e drif tlimit s hav e bee n estabhshe

d fo rexcessiv

e H 2 

### 0 drift

.

1 8

### 5.0 . RECORDKEEPIN G AN D QUALIT Y ASSURANC E REVIEW S Documentatio

n generate

d from CEM S QA/Q C procedure s an d monitorin

g wil l b e kep t on-sit e fora perio

d o f five years

. Th e dat a an d documentatio

n tha ti s generate

d an d reviewe d i s kep ti n variou

s location

s a tth e Veoli a facility. Tabl e 6- 1 belo w list s th e storag e locatio n an d forma to f thi s documentation

. Maintenanc

e an d Instrumen

tTechnician

s hav e th e primar y responsibiht

y forcreatin

g an d organizin g CEM S dat

a sheets , dail y syste m audi tchecklists, maintenanc e logbook

, an d spar e par tinventor

y records

. Th e Environmenta

l Engineer/Specialis

to rdesigne e will chec k thes e record s quarterl

y t o verif y completio

n an d organization

. This revie

w will als o conside rth e followin

g requirements : 1 . Wheneve

rexcessiv

e audi tinaccuracie

s occu rfo rtw o consecutiv

e quarters

, th e curren twritte n procedure

s wil l b e revise d o rth e CEM S modifie

d o rreplace d t o correc tth e deficienc

y causin g th e excessiv

e inaccuracies

. Previou

s version s o f writte n procedure

s wil l b e kep to n recor d an d mad e availabl e fo rinspection

. 2. I f th e Z D and/o

rC D exceed(s

) tw o time s th e limit s i n th e Performanc

e Specifications , o

ri f th e cumulativ

e adjustmen

tt o th e Z D and/o

rC D exceed(s

) thre e time s th e limit s i n th e Performanc

e Specifications, th

e CEM S i

s considere

d "out-of-control " (a

s define d i n 4 0 CF R63.8(c)(7)) , an

d th e even twil l b e reporte d in th e facility' s semi-annua

l "Exces s Emission

s an d CM S Performanc

e Report" . Furthe rdetai l o n thi s repor tca n b e foun d i n th e facilit y CM S Quaht

y Assuranc

e Program . O n a n annua l basi s th e Environmenta

l Engineer/Specialis

to rdesigne

e wil l revie

w al l CEM S dat

a generate

d forth

e previou

s 1 2 month s an d prepar e a brie f interna l report/mem

o summarizin

g findings. Base

d o n thi s review

, th e Environmenta

l Engineer/Specialis

to rdesigne

e wil l solici

trecommendation

s fo rrevision

s t o th e CEM S Quaht y Assuranc

e Plan. Th

e CEM S Quaht

y Assuranc

e Pla n wil l b e revise d a s neede d t o maintai n QA/Q C o f

th e CEMS . Al l version

s of thi s pla n forth e las tfive year

s remai n in th e operatin

g record.

1 9

### Tabl e 5-1 CEM S Records an d Report s Record/Repor

t Storag e Locatio n Media/Format 1 

### CEM S Q A Pla

n

- Curren

tVersion

- Previou

s Version Incinerato rManager' s Office Operatin g Record s Archive

s H D and/o

rP R D CEM S Reading

s an d HR A

- Previou

s yea rthroug h yea rt o dat e

- Remainin

g archive s Dat aHistoria

n Operatin g Record s Archive

s H D and/o

rRD R D Drif tan d Calibratio

n Data :

- Previou

s yea rthroug h yea rt o dat e

- Remainin

g archive s Operatin g Record s Archive

s Pand/o

rRD Absolut e Cahbratio

n Audi t

- Previou

s yea rthoug h yea rt o dat e

- Remainin

g archive s Operatin g Recor d Archive

s Pand/o

rR D Relativ e Accurac

y Tes tAudi t

- Previou

s yea rthroug h yea rt o dat e

- Remainin

g archive s Operatin g Recor d Archive

s Pand/o

rRD Dail y Syste

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1 

### MediaFormat: H D - Compute ro rnetwor k har d driv e R D - Removabl

e driv e (floppy, CD , backu

p tape ) P- Pape rdocumentatio

n
2 0 

### VE S 00091 0

### 6. 0 OPERATO RTRAININ G AN D CERTIFICATIO N Trainin g is provide

d t o Veoli aemployee

s o n th e basi s of thei rjob title. Individual

s specifically involve

d in th e operatio

n o f th e incinerato

ran d associate

d CEM S ar

e th e Instrumen

tTechnicians, Incinerato rOperators

, an d Environmenta

l Engineer/Specialist

. Th e Veoli aoperato

rtrainin g an d certificatio

n progra m meet s th e requirement

s outline d i n 4 0 CF R63.1206(c)(6) . Documentatio n of employe

e trainin g an d certificatio

n is kep t wit h th e Trainin g Director

, an d is availabl

e fo rrevie w upo n request .

2 1 VE S 00091 1APPENDI X A CEM S DAT A SHEET S AN D CHECKLIST S



### NOTE : TH E FOLLOWIN G SHEET S AR E FO REXAMPL E PURPOSE S ONLY . VEOLI A MA Y UTILIZ E EQUIVALEN T DOCUMENTATIO N FO RAN Y O F TH E SHEET S INCLUDED .CEM S DRIF T AN D CALIBRATIO N DAT A SHEE T Paramete

r (Spa n Value ) Dat

e & Tim e Concentratio n Drif t% Adjustmen t% Cumulativ

e Adjustmen

t% Paramete

r (Spa n Value ) Dat

e & Tim e Referenc

e Analyze

r Drif

t% Adjustmen t% Cumulativ

e Adjustmen

t% H z O (6 0 % ) Zer o O j (25% ) Zer o Calibratio n C O (20 0 ppm ) Zer o Calibratio n C O (300 0 ppm ) Zer o Calibratio n HC I (100 0 ppm ) Zer o Calibratio n
Drift%^ Ref6renCe - AnalyZer .100 %

Spa n Valu e ( Nam e & Title ) Adjustmen

t% = Drif

t% (i f zero/spa n wa s rese tdurin g drif tcheck ) Cumulativ e Adjustmen

t% = (Previou

s Cumulativ

e Adjustmen

t% ) + (Curren

tAdjustmen

t% ) ~ (Signature )

### ABSOLUT E CALIBRATIO N AUDI T(ACA ) DAT A SHEE T

Paramete r

• o 2 

### Q CO-Io wrang e C D CO-hig h rang e
•HC I NIS T Traceabl e Calibratio n Standard s Paramete r

• o 2 

### Q CO-Io wrang e C D CO-hig h rang e
•HC I Ga s Concentratio n Paramete r

• o 2 

### Q CO-Io wrang e C D CO-hig h rang e
•HC I Low (Zero ) ± Paramete r

• o 2 

### Q CO-Io wrang e C D CO-hig h rang e
•HC I Mi d ± Paramete r

• o 2 

### Q CO-Io wrang e C D CO-hig h rang e
•HC I High ±
RU N NUMBE R Concentratio n Differenc e RU N NUMBE R Referenc e Analyze r Lo w Mi d Hig h 1 - Lo w 2 -Mi d 

# - 3 -Hig h 

# - ~ 

### 4 -Lo w — 

# - 5 -Mi d - - 

# - 6 -Hig h


# - - 7 -Lo w 

# - - 8 -Mi d ~ _ _ 

### 9 -Hig h 

# - MEA N DIFFERENC E = CALIBRATIO N ERRO R = MEA N DIFFERENC E = CALIBRATIO N ERRO R = % % %

_r 

### , , . _Mea n Differenc

e Cahbratio

n Error= * 10 0 Spa n Valu e
(Name ) (Title ) (Signature

) (Date )



### VE S 00091 4RELATIV E ACCURAC YTES TAUDI T RAT A DATASHEE T Referenc e Metho d CEM S Differenc e Referenc e Metho d CEM S Differenc e Ru n H 2 0 , % (i f applicable

) 0 2 , % we

t (i f applicable

) 0 2 ; % dr

y 0 2 s% dr

y 0 2 , % di

y CO ppm

v (i f applicable

) C O ppmd

v C O ppmd

v @7 %0 2 CO ppmd v @7 %0 2 CO ppmd

v @ 7 % 0 2 1 2 3 4 5 6 7 8 9 1 0 1 1 1 2 0 2 R A | Mea n Differenc

e Standar d Deviatio

n I Confidenc

e Coefficien

t COR A
(Name ) (Title ) (Signature

) (Date )

### CEM S DAIL Y SYSTE M AUDI T Initial s Verif y tha tth e mos trecen tdrif tcheck s an d calibratio

n adjustment

s ar e withi n limits . Complet e Drif tan d Calibratio

n Dat aSheet . Correctiv e Actions : Verif y prope roperatio

n o f CEM S dat a recordin

g an d printin g Correctiv e Actions : Chec k fo rcontrolle

ralarm s an d error/warnin

g message

s Correctiv e Actions : Chec k expecte d calibratio

n value s Correctiv e Actions : Chec k curren temission

s dat astatu s Correctiv e Actions : Verif y calibratio

n ga s cylinde rpressure

s (>15 0 psi ) Correctiv e Actions : Verif y pressur e regulato

rsetting s (approximatel

y 25-3 5 psi ) Correctiv e Actions : Verif y prope rinstrumen

tai rpressur e t o CEMS umbilica

l Correctiv e Actions : Perfor m visua l inspectio

n o f th e stac k ga s samplin g syste m Correctiv e Actions :

(Name ) (Title ) . (Signature

) (Date )



### VE S 00091 6CEM S CALIBRATIO N GA S AN D SPAR E PART S LO G
CALIBRATIO N GASES : 

### (Attac h al l certificatio

n forms ) Zer o gas : Spa n ga s 1 : Spa n ga s 2 : Spa n ga s 3 : AC A Gases : cylinder s cylinder s cylinder s cylinder s Composition : Composition : Composition : Composition :

PARTS : 

### Ai rconditione

rfilter s fo rCEM S shelte

r Instrumen

tai rcoalescin

g filter s Sampl e pum p Teflo n diaphrag

m Sampl e pum p Teflo n flappe

rvalv e Sampl e prob e interna l filte r____ _ Sampl e prob e gasket s Probe-ti p filter Cel l frontcove

rgaske t Cel l inle tfilter Cel l window

s wit h o-rin g gasket s Cel l mirror

s Tubin g Fitting s Solenoi d Value s Thermocouple

s Electroni c part s
Othe rspar e part s

Inventor y take n by : _ _Date :

VE S 00091 7