# 0 VEOLI A

ENVIRONMENTA L SERVICE S

TECHNICALSOLUTION S 1 

### Ub l I 

## 4 200 8 N ORT H A MERICA * A! R ENFORCEMENTBRANC H 

### Octobe r 10 , 200 8 . l_, ' ^PA J RCGIOK J 5 

### Vi a FedE

x Attn : Complianc

e Tracker

, AE-17J Ai rEnforcemen

tan d Complianc

e Assuranc

e Branc h Unite d State s Environmenta

l Protectio

n Agenc y Regio n 5 7 7 W . Jackson Blvd. , AE-17J Chicago , I

L 6060 4 RE : Veolia E S Technica l Solutions , L.L.C . 163121AA

P 4 0 CF RPar

t6 3 - Subpar

tEE E Nationa l Emissio

n Standard

s fo r Hazardou

s Ai rPollutant

s fro m Hazardou

s Wast e Combustor

s Notificatio

n o f Complianc

e (NOC ) Complianc

e Tracker, Pursuan tt o Appendi

x B , Item

s 9 , 1 1 an d 1 2 o f th e Reques

tt o Provid e Informatio

n Pursuan

tt o th e Clea n Ai rAc tfro m USEPA , Regio

n 5 , date d Februar y 22, 2008 , revise

d Jun e 5, 200 8 an d revise d o n Septembe

r 16 , 2008, Veolia E S Technica

l Solutions , L.L.C , hereb y submit s th e Notificatio

n o f Complianc

e (NOC) , th

e Performanc

e TestReport

s fo rIncinerator

s 2 , 3 an d 4 an d th e Significan

tModificatio

n t o th e Par t7 1 Permit . Th e NO G 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

r limit s fo rmercury

, SV M an d LV M define d i n 4 0 CF R63.120

9 an d 63.1219. Veolia i

s no w complyin

g wit h al l operatin g requirement

s specifie

d i n thi s NOC . Th

e Performanc

e Tes tReport s detai l complianc

e wit h these standard

s an d th e Significan

tModificatio

n reques t tha tth e revise d OPL' s b

e incorporate

d int o Veolia' s Par

t7 1 permit . I certif y unde r penalt y o f la w tha tthi s documen

tan d al l attachment

s wer e prepare d unde r m y directio n o rsupervisio

n i n accordanc

e wit h a syste m designe d t o assur e tha tqualifie d personne

l properl y gathe r an d evaluat

e th e

Veoli a E S Technica l Solutions , LL.C
. # 7 Mobil e Ave , Sauget , I L 6220 1 tel : 61 8 27 1 280 4 - fax : 61 8 27 1 212 8

### informatio n submitted. Base d o

n m y inquir y o f th e perso n o r person s wh o manag e th e system , o

r thos e person s directl y responsibl

e fo r gatherin

g th e information

, th e informatio

n submitted

, i s t o th e bes to f m y knowledg

e an d belief , true , accurate , an

d complete. I a

m awar e tha tther e ar e significan

tpenaltie

s fo r submittin

g fals e information

, includin g th e possibilit

y o f fin e an d imprisonmen

tfo r knowin g violations . Upo n revie w o f thi s submittal

, shoul d th e Agenc y hav e a nee d fo r additiona

l informatio

n o r questions , please contac tDenni s Warcho

l a t(618 ) 271-280

4 o r vi a e-mai l a tdwarchol@onvxes.co m o r mysel f a t(618 ) 27 1 -280 4 o r vi a e-mai l a t dharri s @ onvxes.com. . Sincerely , Veolia.E S Technica

l Solutions , L.L.C . Genera l Manage

r Att . cc : Geneviev

e Damico , USEP A (Significan tModificatio

n Only ) USEP A Fil

e

### Veoli a E S Technica l Solutions , L L C . Significan t Modificatio n t o Par t 7 1 Permi t titl e V Permi t # : V-IL-1716300103-08-0 1 

### Pursuan tt o 4 0 CF B 71.7(e)(3) , Veolia E S Technica l Solutions , L.L.C . i

s submittin

g a significan

tmodificatio

n t o ou r Par t7 1 Permi tnumbe r V-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 r th e modification

. Th e requeste

d modification

s ar e a s followed :

• Section 1 (B

) Date s o f Constructio

n fo r Incinerator

s 2 , 3 an d 4

• Section 2. 1 (C)(2

) Operatin

g Paramete

r Limit s fo r Unit s 2 , 3 an d 4

• Section 2.

2 Materia

l Processing , Handlin

g o f Leve l 2 Container

s

• Section 2.4 Storag

e Tanks , Monitorin

g an d Testin g fo r Tank s Maintaine

d a tAtmospheri

c

• 55 0 Gasoline Storage, Insignifican tActivit y

• Dru m Sampling, Insignifican tActivit y

### Sectio n 1 (B ) Source Emissio

n Point s Veoli a reques

ttha tth e date s o f constructio

n fo r Incinerator

s 2 , 3 an d 4 b e modifie d a s followed : Incinerato

r # 2 # 3 # 4 Thes e revised date

s ar e take n directl y fro m th e constructio

n permit s issued b y IEP A (constructio

n permit s attached) , Dat e o f Constructio

n 9/198 6 (correc ti n permit ) 8/198 8 (permi tstate s 9/1986 ) 8/198 8 (permi tstate s 6/1988 )

### Illinoi s fe^Q^maijfel ProiBfitiei n Agenc y - WM

Chufeftii l Rbad , %ringrield

, I L 6270 6 2T7/782-2T1 3 PERMITTEE

, COHSTRUCTION : PERMI T Trad e Wast e Incineratio n Attention ; Jame

s L . Gar y 7 Mobil e Avenu

e Sauget, Illinoi s 62201-106 9 Applicatio n Applicant 1 

### ' No. : 8312005 3 s Designation : Subject : Tw

o TWI-2UU

U Incinerator s Septembe r 2 . I.D , Mo,.,: 163121AA P Dat e (Received : Jun

e 9 , 198 6 Dat e Locati o n Issued : ¥ 7 198

6 Mobil e Avenue

, Sauge t 

# Q Permiti s hereb y grante d t o the above-designate d Permitte

e t o CONSTRUC

T emission source(s ) and/or ai r pollutio n contro l equipmen tconsistin g of

tw o TWI-200 0 Serie s 2 Hazardou

s Wast e Incinerator s on

e wit h a Jo y Spra y Dr y Adsorbe r an d fabri c filter , an

d tli e secon

d uni twit

h a Ventur

i Scrubber , Cycloni c Wate

r Ga s Separator , Induce

d Draf tFan , an

d Exhaus

tExpansio

n Tan k a s describe d i n th

e above-referenced application . Thi s Permi ti s subjec tt

o standar d condition s attache

d heret o an d th e followin g specia l condition(s) : 1 . Th e incinerato r whe

n constructe d shal l includ e a Wast e Fee d Interloc k Syste m t o insure thatwast

e i s no tfe d t o th e incinerato r unles s al l critica l operatin g parameter s ar e wit h acceptabl e limits . A s par to f thi s syste m stac k monitor

s shal l b

e installe d o

n eac h incinerato r fo r Oxygen , Carbo n Monoxide

, an d Hydrocarbons . Fo r th e incinerato r wit

h th e SD A th e followin g tw

o additiona l emission monitor s ar e required : Broke

n Ba g Detecto r an

d hydroge

n chlorid e monitor . 2 . Particulat e matte r emission

s fro m th e incinerato r shal l no texcee d 0.0 8 grain s pe

r dr y standar

d cubi c foo to f

ga s discharged t

o th e atmosphere

, pursuan tt o 3 5 111 . Adm

. Cod e 121.181(b) . 3 . Carbo

n monoxid

e emission

s fro m th e incinerato r shal l no texcee d 50 0 part s pe r million , correcte d t o 5 0 percen

texces s air , pursuan

tt o 3 5 111 . Adm

. Cod e 216,141 . 4 . Hydroge

n chlorid e emission

s fro m incinerator s 2 an

d 3 shal l no

texcee d 4 lbs/h r o r th

e contro l devices shal 1 demonstrat e a minimu

m HC L remova

l efficienc y o

f

fECEIVE D SE P 8 198 8

### niinpi s Enyireiitoenta l Protectio n Agenc y •* 220 0 Ohxit-cMi;! ifeafl, Sp^ift^eia , IL 6270 J Pap : ' # 5 . Th e ne w incinerator s shal l b e constructe d an

d operated_wit

h a wast

e cutof f „ interloc k syste

m whic h wil l preven

tintroductio n of

wast e int o th

e incinerato r whe

n an y o f the followin g event s hav e occurred .

: 

### a . T.D , fatf

i faftiife: , li . Atomizin

g ai r pressure belo

w 1 0 psig . c . Incinerato r chambe r pressure 2

" w.c . abov

e atmosphori

c fo r mor

e tha n 5 seconds . d , Emergenc

y stuck opens . e « Failur e t

o sustai n operatin g parameter s speci f iet i i n spefeia

T conditio n 3 .

.. , ... . -f


### f t Burne

r failur e i n th

e primar

y o r secondar

y chamber

. g . Whe

n primar

y chambe

r temperatur

e fall s belo

w 150Q°F o r secondar y chambe r exceed

s 2275°F . h . Carbo

n monoxid

e concentratio n exceed s 50B pp i o

r excee d 5 0 pp m fo r mor e tha n three minutes i Fo r Th e Incfnerato r Wit

h A Ventur

i Sffrujjbe

r it Quenc

h wate r flo w beio

w 10 0 gpm . Veritur i scrubbe

r wate r belo w 3 7 gpm , pressur

e dro p acros s Ventur

i scrubber les s tha

n 21 " w.c. , scrubber p H les s tha

n 6 an d flu e ga

s temperatur

e enterin g the scrubbe r greate r tha

n 180°F . Fp r Th e loc i tveffato

r W i t h A Spra

y Drye r A^gorbei

? k . Loss o f

siurr y f16

W t o SDA , 1 * Hig h hydroge

n c h 1 o r id e concerttration i n th e stack: , m . Hig h opacit

y a s indicate d b

y th e broke n ba g detector , h . Hig h inle ttemperatur

e t o th e fabri c fitter . 6 . Th e incinerator s an

d associate d ai r pollutio n contro l equipmen tshal l b

e constructe d suc

h tha tth e value s o f

th e parameter

s bein g monitore

d ar e displaye d fo r operatin g personnel . 7 . Operation of

th e incinerato r utilizin g auxiliar y fue l wil l b e limite d a

s t o composition an

d incinerato r operatin g condition s whic h wil l mee

tal l applicabl e regulations . Suc h a requestshoul

d b e incorporate d i n th e tria l bur

n plan .lilted ^ 

### Protectio n Agenc y * 220 0 Churchil l Road , Springfield , 

### i t6270 6 Pag e % 8 : 

### . Trad

e Wast e Incineratio n shal l submi tas-buil tplans an

d specification s t

o

- the Agenc

y a s par tof

thei r operatin g permi tapplication , 9. Prio r t

o operatio n th

e ne w units , 2 an

d 3 , shal l b

e teste d pursuan

tt o a n Agenc y approve

d tria l bur

n plan * Trad

e Wast e Incineratio n shal l submi ta detaile d tria l bur

n plan fo r Agenc

y approva

l prio r t

o startup - Th

e tria l bur n plan shal l provide fo r demonstratio n of th e incinerators ' destructio n an d remova

l efficiency * an

d particulat e matter , carbo n monoxide

, organi c material , an

d hydroge

n chlorid e emission

s throughou

tthe rang

e of wast e characteristic s an

d incinerato r operating parameter s fo r whic

h a n operatin g permi

twil l b e sought

. Suc h tria l bur

n pla n shoul d als o indicat e perio d of

operatio n o f

incinerator s during shakedow n an d testing . Standar

d conditio n 9 whic

h allow s 3 0 day s fo r shakedow

n an d testing , i s hereb

y supercede

d b y thi s condition . A n operatin g permitwil l only b e issue d fo r thes e incinerator s afte r a 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 operating permitma

y limi tth

e incinerato r operatin g parameter s an d th e compositio

n o f th e incinerator' s wast e feed . 10, A s parto f

th e tria l bur

n plan , Trad

e Wast e Incineratio n shal l propos e procedure

s fo r maintainin g operatin g records . Suc h procedure

s shal l includ e appropriat

e notificatio n t

o th e Agenc y an d actio n t

o b e take n b operatin g personne

l i n the even

to f equipmen

tmalfunctio n o

r breakdown

. 11 . Emission

s o f particulat e matte

r (TSP) , sulfu r oxides (S02) , nitrogen oxide s (NOx) , organic material (OM ) an d carbo n monoxid

e (CQ ) shal l no

t excee d th e amount

s specifie d i n th

e Tabl e below . Emissio n Sourc e TS P S O 2 NO

X Existin g Incinerato r 1 5 . 0 7. 7 4. 0 Me w Incinerator s 3 0 .0 1,5.

4 8. 0 Annua l Emission

s (Tons/Year

) Q M C O Storag e Operation

s 0 . 1 1.8 6,9 '6.6

, 13, 2 Thes e limit s ar

e base d o n storag e a

s indicate d i n th

e the potentia l emission s o f the incinerator s a

### permi tapplication .

Bhara t Mtfthur , P.E . Manager , Permi t

Sectio n Divisio n o f

Ai r Pollutio n Contro l BM:JDC:jmm/1857F/25-2 7 cc : Regio n 1

### Illinoi s Enviro$j3p$!fc| i PfbteGtion Agenc y 220 0 GfturehH

i i&m & BpXi^UU, T

L 6270 G CONSTRUCTIO

N PERMI T PERMITTE

E Trad e Wast e Incineration , A Divisio n o f Chemica l Wast e Managemen

t Attention : Jame

s L . G.ar y 7 Mobile Avenu

e Sauget , Illinoi s 62201-106 $ Applicatio n No. : 8710002 4 I.D . No. : 163121AA P Applicant' s Designation : INCI RDat

e Received : Ma

y 24 t

### 198

8 Subject : TW

I 200 Q Serie s 2 , Incinerato r Dat e Issued : Augus

t19 , 198

8 Location:" T Mobile Avenue , Sauget , Illinoi s

Permiti s hereb

y grante d t o the above-designate d Permitte

e t o CONSTRUC

T emission source{s ) and/o r ai r pollutio n contro l equipmen tconsistin g o f Incinerato r #

3 Mode l TW I 200 0 wit h associate d Dr

y Scrubbe

r a s describe d i n th

e above-referenced application . Thi s Penni ti s subjectt

o standar

d condition s attached heret

o an d th e followin g specia l condition(s) : 1 . Particulat e matte r emissions fo r th

e incinerato r shal l no texcee d 0.0 8 grain s pe

r dr y standar

d cubi c foo to f

th e ga s discharged t

o th e atmosphere

, pursuan

tt o 3 5 111 . Adm

. Cod e 121.181(b) . 2 . Carbo

n monoxid

e emission

s fro m the incinerato r shal l no texcee d 50 0 part s pe rmillio n correcte d to J

### 5 0 percen

texces s air , pursuan

tto 3 5 111 . Adm

. Cod e 216.141 . 3 . Th e incinerato r shal l b e equippe

d wit h sensor

s t o monito

r th e fol1owing parameters : a . Uppe

r an d lowe r combustio

n chambe

r exi tga

s temperature . b . Uppe

r an d lowe r combustio

n chambe

r pressure . c . Spra

y dryer adsorbe

r inle ttemperature. d . Spra

y drye r adsorbe

r outle ttemperature . e . Lim

e siurr y hea

d tan k liqui d level . f . Wate

r pressur

e t o slurr y hea

d tan k makeup

. g . Baghous

e tub e shee tpressur

e drop . h . Combustio

n stac k ga s flo w rate . i . Stac

k ga s oxyge n concentration .

mmw\ km 

## 2 3 %.• •• - \

J . 

### i 

### : Illinoi s E$^irdnmen;fca l Protection Agenc

y ' 22Q

0 <Gh.u.rehUl-

: Rdad , Springfield

, I L §270 6

• 4 3- 

### 1 , m > n . 6 .
r . Si t . 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 . Stac k gas . opacity . Liqui d and/o r sludge wast e flo w rat e int o the ffteiiierator . Soli d wast

e charged . Primar y fue l pressure . Combustio

n ai r pressure . Primar y Burne r & Pilo tflame . Secondar y Burner

s & Pilot s flames . Emergenc

y stac k latch . Th e incinerato r shal l b e designe

d an d constructed t

o operat

e wit h a n automati c wast e fee d cutof

f interloc k syste

m whic h wil l preven

tth e introductio n of

wast e int o th

e incinerato r whe

n operatin g outsid e th e permitted rang

e of parameters . a . Startup rang

e o f parameter

s ar e establishe d base

d upo n desitj n specification s an

d performanc

e test s conducte

d o n Incinerato r Unit2 an d ca n b e change d afte r successfu l stac k tes tdemonstratio

n o n Uni t 3, - (1 ) Primar

y chambe

r belo w 1600°F . (2 ) Secondar

y chambe

r belo w 1800°F . (3 ) Primar

y or secondar

y chambe

r abov e atmospheri

c pressure . (4 ) Spra y drye r adsorbe

r inle tgreate r tha

n 22Q0°F . (5 ) Spra y dryer adsorbe

r outle tgreate r tha

n 4Q0° F o r belo

w 370PF . (6 ) Lo w liqui d leve l i n lim e slurr y hea

d tank , (7 ) Lo w makeu p wate r pressur

e int o slurr y hea

ttank . (8 ) Baghous

e tub e shee tpressur

e dro p greate r tha

n 1 0 inche s Wate r co l um n * (9 ) Combustio

n stac k ga s flo w les s tha

n 5,00 0 acf m o r greate r tha

n 15,00 0 acfm. (10 ) Oxyge n concentratio n les s tha n 6% b y volume

. (11 ) Carbo

n monoxid

e concentratio n greate r tha n 50 Q ppm . (12 ) Carbo n monoxid

e concentratio n greate r tha n 5 0 pp m fo r 3 minutes . (13 1 Total hydrocarbo

n concentratio n greate r tha n 10 0 pp m correcte d t o 7% oxygen

, (14 ) HC I concentratio n greate r tha n 10 0 pp m fo r 1 hour , (15 ) Opacit

y greate r tha

n 10% , (16 ) Primar y fue l pressur

e belo w 3 0 psig . (17 ) Combustio

n ai r pressur

e belo w 1 0 inche s W.C. (18 ) Primar y burne r failure . (19 ) Secondar

y burne r failure . (20 ) Emergenc

y stac k open .

### Illinoi s Epvironh^ S Protectio n Agenc y • 220 0 ^Harchi U R>>sd , Springfield

, li s 62^06 .

b . Operating parameter s wil l b e establishe d base

d upo n evaluatio n o

f actua l operatio n an

d measure

d emission

s durin g a tria l burn . 5 . Th e incinerato r an

d associate d ai r pollutio n contro l equipmen tshal l b e constructe d suc

h tha tth

e values o f

the parameter

s monitore

d and/o r indicato r o f

acceptabl e statu s are displaye d fo r operatin g personne

l wit h audibl e an

d visua l alarms . 6 . Th e Permittee shal l submi ta s buil tplan

s o f th e incinerato r an

d ai r pollutio n contro l equipmen ta s par to f

th e operatin g permi

tapplication . | * Th e Remitte e shal l no tinitiat e th

e start-u p o

f the incinerato r withou t writte n approva

l fro m th e Agency

. Thi s specia l conditio n supercede s standar d conditio n 6(b) . I . Stac k emission tests shal l b e conducte

d o n thi s Uni t3 Incinerato r t o establis h emissio

n rate s an

d complianc

e wit h th e applicabl e regulations . Th e require d stac

k test s ar

e t o b e conducte

d b y a n independen

ttester . a . Emissio

n test s ar

e require d fo r th

e followin g pollutants : (1 ) Particulat e matter , (2 ) Hydroge

n chloride . (3) Nitroge

n oxides . (4 ) Carbo

n Monoxide

. (5 ) Principa l organi c hazardou s components

. & Th e Permittee shal l submi tastac k tes t pla n a tleas t6

0 day s i n advanc e fo r Agenc

y approval . Th

e pla n shal l contai n detaile d plan s an d procedures . c u Written notic e o f th e schedule

d date s fo r complianc

e stac k testin g shal l b e give n a tleas t3

0 day s i n advanc

e t o th e Agency

. Fina l notic e shal l b

e give n verball y no

tles s tha

n 7 day s before emissio

n testin g begins . Th

e require d notic e shal l b e given t

o th e following : Illinoi s Environmenta l Protectio n Agenc

y Attn : Permi

tSectio n Manage

r Divisio n o f

Ai rPollutio n Contro l P.O . Bo x 1927 6 Springfield , Illinoi s 62794-927 6 217/782-2113 Illinoi s Environmenta l Protectio n Agency Attn : Sourc e Emissio n Tes t Specialis t Divisio n o f

Ai r Pollutio n Contro l Th e Intercontinenta l Cente r 170 1 Firs t

Avenue Maywood , Illinoi s 6015 3

### rilifi^i s EtlVironmenta l Protectio n Agenc

y 22Q0

. €^ui?clitl

j 

### ftoady Spfinifieid , IL 6270 6



### Illinoi s Environmenta l Protectio n Agenc

y Divisio n o f

Ai r Pollutio n Contro l - Regiona

l Offic e 200 9 Mal l Stree t Collinsville , Illinoi s 6223 4 618/345-070

0 I * Prio r t

o startup , the Permitte e shal l submi

tinstrumentation an

d monitoring specifications - A proposa l fo r th e detail s of

recor d keeping ; an d repor tformat

s use d t o sho w complianc

e wit h th e limitation s of

th e operatin g parameter

s require d t o b

e monitore

d i n special conditio n 3 of thi s constructio n permi tshal l b

e submitte

d t o th e Agenc y fo r approval . ••a: . Th e instrumentatio n an

d dat a loggin g equipmen

tshal l provide fo r storag e qf 100 % o f the incinerato r parameter s an d stac k monitore

d results i n a compute r readable format . Copie s shal l b

e mad e availabl e t

o th e Agenc y i n a suitabl e compute r readabl

e format. b . Th e dat a loggin g equipmen

tshal l als o provide fo r recordin g wast e > analysi s paramete

r fo r a s burne d v/ast e streams. " Th e dat a loggin g equipmen

tshal l provide rea l tim e access t o th

e incinerato r operatin g parameter s throug h a telecommunicatio

n compute

r port . d . Th e proposa

l shal l se tfort h the hardwar e an d softwar

e specification s fo r th e informatio n syste

m alon g wit h availabl e option

s i n report format s an d dat a exchang

e media. e . Th e permitte

e shal l instal l a compute r linku p syste

m wit h IEP A Springfield , IEP

A Collinsvill e an

d som e locatio n wit

h publi c access . Suc h a syste

m an d locatio n wil l requir e Agenc y approval . 10 . Prio r t

o startup , the Permitte e shal l submi

tdetail s o f

a n operato r trainin g progra

m fo r Agenc

y approval . 11 . Prio r t

o startup , the Permitte e shal l submi

tfo r Agenc

y approval , specification s fo r on-sit e securit y includin g video cameras , monitoring cabine tlocks an

d seal s an

d detail s o f

security fencing . 12 . Emission

s o f particulat e matte

r (TSP) , sulfu r oxide s (S0;>) , nitrogen oxide s (M0

X

### ) , organi c material (OM) , 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 . P'agf i 4

Emissio n Sourc

e TS

P Annual Emission s (Tons/Year ) SQ 2 NO

x O M C C O Incinerato r

Uni t 1 Incinerato r

Uni t 2 Incinerato r

Uni t 3 incinerato r

Uni t 4 * Wast e Storag e 15,0 15. 0 15. 0 16.9 2 7. 7 7.7 7. 7 50,7 6 4. 0 4. 0 4. 0 61. 6 0. 9

0. 9 0. 9 3. 1 6. 6 6. 6 6. 6 13.6 8\ 

### Illinoi s Environmenta l Protection Agency • 2j2pfl 4®ftthil l Kxwd , Springfield

, I L 6270 6 Pag e 5 *Thes e limit s ar

e establishe d base

d o n 720 5 hour s o f operatio n pe

r yea r an d averag e emission rate s given i n th e application . Thes e limit s wil l B

e revise d afte r th

e stack tes tresult s ar e reviewed , 13 . Prio r t

o startup , the 1 

### permittee shal l provid e detail s of th e Quality Assurance/Qualit

y Control program

s fo r th e monitorin g system

s specifie d i n -Specia l Conditio n 3 abov

e fo r Agtenc

y approval . Pleas e not

e tha tthe start-u p an d tria l bur

n pla n a s submitte

d wit h the applicatio n i s no

tacceptable . Plan deficiencie s wil l b e identifie d a ta 1ater time .

Divisio n o f

Ai r Pollutio n Contro l TAS:JDC:ds:5035H/32-3 S cc : Regio

n 3

### DEBtEG^FOBt Y PROTECTIO N AGENC Y DIVISIO N O F AI RPOLLUTIO N CONTRO L ,iJul y 1 , 198 5 Fo rassistance i n preparing 1 a penni tapp^6|!^li4 contactth e Permi tSection , Illinoi s Environmenta l Protectio n Agepc y Divisio n o f

Ai rPollutio n Contro l Permi tSection 220 0 Churchil l Road Springfield , Illinoi s 6270 6 (217 ) 782-2113 o ra regiona l offic e o f th e Fiel d Operation s Section . Th e regiona l office s an d thei r area s o f responsibilit

y ar e show

n o n th e map . Th e addrease s an d telephon

e number

s o f the regional office s ar

e as follows : Illinoi s EP A Region 1 Intercontinenta

l Cente r 170 1 S , 1stAvenu e Maywood , Illinoi s 6015 3 (312 ) 345-978

0 Illinoi s EP A Region 2 5416 North University Peoria , Illinoi s 6161 4 (309 ) 691-220

0 Illinoi s EP A Region 3 200 9 Mal l Street Collinsville , Illinoi s 6223 4 (618 ) "345-070

0

### Illinoi s Environmental Protectio n AgeiYcj y < 220. 0 Churchil l Road , Springfield , I L 62W6 

### 217/782-2113 CONSTRWlG N p£$$T 

### Trad e Wast e Incineratio n A Divisio n o f

Chemica

l Wast e MSnajgeffien

t Attn : Game

s L * Gar y 7 Mobi l Avenu e Sauget , Illinoi s 6220

1 Applicatio n No. : 8801000 1 Mo ^ 163121AA P Applicant' s Designation : INCI N # 4 Dafc

g Received : Marc

h 2 % 198 8 Subject ; Transportabl e Rotar y Kil n IncifteraTto r Dat e Issued : Augus

t3 , 198 8 Location: T Mobil

e Avenue

, Sauget , I L Permiti s hereb

y grante

d to th e above-designate d Permittee t o CONSTRUC

T emission source(s ) and/o r ai r pollutio n contro l equipmen tconsistin g of

a Transportabl e Rotar

y Kil n Incinerato r Uni t# 4 equippe d wit h a dr y scrubbe

r an d I a baghouse

, a s describe d i n th

e above-reference d application . Thi s Permi ti s I subjec tto standar d condition s attache d heret o an d the followin g specia l i eondition(s) : 1 . Particulat e matter emissions fron i th e incinerato r shal l no texcee d 0.$ | grain s pe

r dr y standar

d cubi c foo to f

th e ga

s discharge

d t o th e atmosphere

, pursuan

tt o 3 5 111 . Adm

. Cod e 121.181(b) . 2 . Carbo

n monoxid

e emission

s fro m th e incinerato r shal l no texcee d 50 0 parts pe r millio n correcte d t o 5 0 percentexces s air , pursuan tt o 3 5 111 . Adm

. Cod e 216.141 . I K Th e incinerato r shal l b e equippe

d with sensor s t

o continuously monito r th e I followin g parameters :

a . Kil n an

d secondar

y combustio

n chamber exi tga

s temperature. b . Kil n an

d secondar

y combustio

n chamber pressure . c . Spra

y drye r adsorbe r inle ttemperature . i. Spra

y drye r adsorber outle ttemperature . Lim e slurr y fee dtan k

liqui dleve l low . Wate r pressur e t o slurr y fee dtan k makeup . Baghous e tub e shee t

pressur e drop . Combustio n stac k

ga s flo w rate . Stac k ga s oxyge n concentration . Stac k ga s carbo n monoxide concentration . Stac k ga s tota l hydrocarbo n concentration . Stac k ga s HC L concentration , m. • -tac k

ga s infrare dabsorption . n.. . iqui dand/o r

sludge ' waste Ho w rat e int o th e incinerator , l i dwast e charged .

### mis, EnvirQivnie n ta l Rpoteetio

n Agenc y - M&Q Chtirchil l Road , Sprhigfteid

, th

i Primar

y fue l pressure . I . Combustio n air - pressure . I . Primar

y Burne r & Pilo tflame , f s . Secondar y Burner

s & Pilot s flame . J t . Emergenc y stack latch . I Th

e incinerato r shal l b e designe

d an d constructe d t

o operat

e wjt h a n #automati

c wast e fee d cutof

f interloc k syste m whic h wil l preven

tthe J introductio n of wast e int o th

e incinerato r whe

n operatin g outsid e th e f permitted rang e of parameters . j a . Startup rang e o f parameter

s ar e establishe d base

d upo n design I specification s an d performanc

e test s conducte

d o n Incinerato r Unit2 I an

d ca n b e change d afte r successfu l stack tes tdemonstratio n oi l rUni t4 .

(1 } Kil n chambe

r belo w 160Q°F . (2 ) Secondar

y chambe

r belo w 18DQ°F . (3 ) Kil n o r secondar

y chambe

r above atmospheri

c pressure . (4 ) Spra y dryer adsorbe

r inle tgreate r tha

n 220 0 F . (5 ) Spra y dryer adsorbe

r outle tgreate r tha n 400° F o r belo

w 37Q°F , (6 ) Lo w liqui d leve l i n lim e slurr y fee d tank. (7 ) Lo w makeu p wate r pressur

e int o slurr y fee

d tank . ) (8

) Baghous

e tub e shee tpressur

e dro p greate r tha

n 1 0 inches wate

r column. (9 ) Oxyge

n concentratio n les s tha n 6% b y volume ^ (10 ) Carbo n monoxid

e concentratio n greate r tha n 50 0 ppm . (11) Carbo

n monoxid

e concentratio n greate r tha n 5 0 pp m fo r 3 minutes . (12 ) Total hydrocarbo

n concentratio n greate r tha n 10 0 pp m correcte d to 1% oxyge

n fo r on

e hou r running average. (13 ) HC I concentratio n greate r tha n 1Q O pp m fo r 1 hou

r runnin g average . (14 ) Opacit

y greate r tha

n 1Q& . (15 ) Primar y fue l pressur

e belo w 3 0 psig . (16 ) Combustio

n ai r pressur

e below 1

0 inches W.C

. (17 ) Kil n burne

r failure . (18 ) Secondar

y burne r failure . (19 ) Emergenc

y stac k open . (20 ) Combustio

n stac k ga s flo w parameter s wil l b e establishe d a ta late r stage . b . Operating parameter s shal l b

e establishe d base

d upo n evaluatio n o

f actua l operatio n an

d measure

d emission s during atria l burn * 5 . Th e incinerato r

an d associate dai r

pol l utio n contro l equipmen t shal l be constructe dsuc h tha t th e value s o f

th e parameter s monitore dand/o r indicato r

o f acceptabl e statu s ar e displaye dfo r operatin g personne l wit h audibl e an d visua l alarms .

### Pag e 3

6 . Th e Permittee sha,

n submi ta s bui H plan s fo r th e incinerato r an

d ai r pollutio n contro l equipmen ta s par to f

th e operatin g permi

tapplication . 1\ Th #Perfliitte e shal l ho tiriitiat e thf e start-u p o f

th e irtcirterftb r withou t writte n approva

l fro m # e Agg^iiy

. This 1 

### specia l cbhdittb h supersede s standar d conditio n 6|bl . 8 , Stac k emission test s shal l b e conducted- o

n thi s Iflfihe^riito r to establis h emissio n rate s an

d complianc

e wit h th e applicabl e regulations . Th e require d stac

k test s ar

e t o b e conducte

d b y a n independen

ttester . $ . Emissio

n tests ar

e require d fo r th e followin g pollutants : (1 ) Particulate'matter . (2) Hydroge

n chloride . (3) Nitroge

n oxides . (4 ) Carbo n monoxide

. (5 ) Destructio n o f

principa l organi c hazardou s components

, b . Th e Permittee shal l submi ta start-u p pla n an d tria l bur

n plans an

d procedures . Suc

h a tria l bur

n plan shal l require th e Agency' s approva l 3 0 day s prio r t

o an y start-u p an

d testing . ;e . Written notic e of the scheduled date

s fo r complianc

e stac k testin g shal l b e given a tleas t3

0 day s i n advanc

e t o th e Agency

. Fina l notic e shal l b

e given verball y notles s tha n 7 day s before emission testin g begins . Th

e require d notic e shal l b e give n t o th e following : Illinoi s Environmenta l Protectio n Agenc

y Attn : Permi

tSectio n Manage

r Divisio n o f

Ai r Pollutio n Control P.O . Bo x 1927 6 Springfield , I

L 62794-927

6 217/782-2113 \ Illinoi s Environmenta l Protectio n Agenc

y \ Attn : Sourc e Emission Tes tSpecialis t \ Divisio n o f Ai r Pollutio n Contro l • Intercontinenta l Center

170 1 Firs tAvenu

e Maywood , I L 6015 3 312/345-978

0 Illinoi s Environmenta l Protectio n Agency Divisio n o f

Ai r Pollutio n Control-Regiona l Offic e | 200

Q Mal l Stree t 1 Collinsville , I L 6223 4 I 618/345-070 Q

### Illinoi s Environmenta l frof«Slfet tJ%iftof ' 22W

Q)uitm}\ 

## loa4%»0gpai , I L 

### Wf&& 

### Pltge : 4 9 . Prio r t

o startup , the Permittee shal l submi tinstrumentation an

d monitorin g specifications . A proposa l fo r th e detail s of

recor d keepin g an d repor tformat

s use d t o sho w complianc

e wit h th e limitation s o f

th e operatin g parameter

s require d to b

e monitore

d i n specia l conditio n 3 o f thi s constructio n permi tshal l b

e submitte

d t o th e Agenc y fo r approval . I U Th e instrumentatio n an

d dat a loggin g equipmen

tshal l provid e fo r storage o f

1Q0 % o f th e incinerato r parameter s an d stac k monitore

d result s i n a compute r readabl e format. Copie s shal l b

e mad e availabl e t

o the Agenc

y i n a suitabl e compute r readabl

e format . Th e dat a loggin g equipmen

tshal l als o provide fo r recording wast e analysi s paramete

r fo r a s burne d wast e streams . Hie dat a loggin g equipmen

tshal l provide real tim e acces s t

o the incinerato r operatin g parameter s throug h a telecommunicatio

n compute

r port * d. " Th e proposa

l shal l se tfort h th

e hardwar

e an d softwar

e specification s fo r the informatio n syste m along wit

h availabl e option

s i n report format s an d dat a exchang

e media. e . Th e permittee shal l instal l a compute r linkup syste

m wit h IEP A Springfield * IEP

A Collinsvill e an

d som e locatio n wit

h publi c access . Suc h a syste

m an d locatio n wil l requir e Agenc y approval . 10. Prio r t

o startup , th

e Permittee shal l submi tdetail s o f

a n operato r trainin g progra

m fo r Agenc

y approval . j l . Prio r t

o startup , th

e Permittee shal l submi tfo r Agenc

y approval , specification s fo r on-sit e securit y includin g vide o cameras, monitoring cabine tlock s an

d seal s an

d detail s of

security fencing . 12 . Emission

s o f particulat e matte

r (TSP) , sulfu r oxide s (SQg) , nitroge n oxides {MO^l

, organi c materia l (OM), an d carbo n monoxid

e {CO ) shal l no

t excee d th e amount

s specifie d i n the Table below .

Thes e limit s ar e establishe dbase d o n 720 5 hour s o f

operatio n pe r

yea r an d averag e emissio n rate s give n i n th e application . Thes e limit s wil l b e revise dafte r

th e stac k

tes t result s ar e reviewed , 13 . Prio r

t o startup , th e permitte e shal l provid e detail s o f th e Qualit y Assurance/Qualit y Contro l program s fo r th e monitorin g system s specifie di n Specia l Conditio n 3 abov e fo r Agenc y approval . Emission Sourc e Annua l Emission

s (Tons/Year

) TS P S0 2 NO x O M C O Incinerato r Uni t4 16.9 2 50.7 6 61. 6 3. 1 13.6

8

### Pag

e 5 Th e Agenc y wil l r.eviet

f whe n amende d whe n the y ar e received . ; §|art-M p pla n afl d tfta l bam p l ain

s

Terry \A . Stoe

* Manager7~Per

m Divisio n of

AiV-PelTutiG n Control TAS:JDC:jmm/4932H/51-5 5 Wi Regio

n ISTAT £O FILUN01 S EMVIRONMEKTA L PROTECTIO N AGENC Y BIV1SV3 N O FAI RPOLLUTIO N CONTRO L

220 0 CHURCHIL L ROA D SPRINGFIELD , ILLINOI S 62 ,70 6

STANDAR D CONDITION S FO RCONSTRUCTION/DEVELOPMEN T PERMIT S ISSUE D B Y TH E ILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y

Th e Illinoi s Environmenta l Protection . Ac t(Illinoi s Revise d Statutes , Chapte r 111-1/2 , Sectio n 1Q39 ) authorizes the Environmenta l Protection . Agency t o impos e condition s o n permit

s whic h i tissues . The followin g condition s ar e applicahl e unles s suspersede d b y specia l conditio n (a) . 1. Unles s thi s permithas bee n extended o r i thas "bee n voide d b

y a newly issue d permit , thi s permlttwul expire-on e yea r fro m th e dat

e o f issuance , unles s a continuou s progra m o f constructio n o r developmen to n thi s projec

thas starte d by suc

h time ; % Th e constructio n o r developmen tcovered by thi s permi tshal l b e don e i n complianc

e wit h applicabl e provision s o f th e Illinoi s Environmenta l Protectio n Ac tan d Regulation s adopted b y th e Illinoi s Pollutio n Contro l Board . 8 * Ther e shal l b

e n o deviations fro m the approve d plan s an d specification s unles s a writte n requestfo r modification , alon g with plans an d specification s a s required , shal l hav e bee n submitte d t

o th e Agency an d a supplementa l writte n permitissued . The pfirrnittij e shal l allow - an y dul y authorize d agen to f Ihe Agency upo n th e presentatio n o f Credentials. ; at ? reasonabl e times : a . t o ente r the permittee' s propert y wher e actua l or potential effluent , emissio n o r nois e source s ar e locate d o r wher e an y activity i s t

o b e conducted pursuan tt o thi s permit , b . t o hav e acces

s t o an d t o cop y an y record s require d t o b e kep tunde r th e term s an d conditions o

f thi s permit, c t o inspect, includin g durin g any hours o f operation o

f equipmentconstructe d o r operate d unde r thi s permit

, suc h equipmen

tan d any equipmen

trequire d t

o b e kept , used , operated , calibrate d an d maintaine d unde r thi s d . t o obtain , an d remov

e -sample

s o f an y discharg e o r emission s o f pollntantS i an d to ente r and utiliz e an y photographic , recording , testing , monitorin g or other equipmentfo r th e purpos e o f preserving , testing , monitoring , o r recordin g an y activity , discharge , 'o r emissio n authorize d b y thi s permit. Th e issuance o

f thi s permit : a . shal l no tb

e considere

d a s i n an y manne r affectin g th e titl e o f th e premise

s upo n which th e permitte d facilitie s ar

e t o b e located , b . doe s 'no t

releas e th e permitte e from , an y liabilit y fd r damage : t o perso n O

r propert y cause db y o f resultin g fro m th e construction , maintenance , o r operatio n o f

th e propose dfacilities , e . doe s no t

releas e th e permitte e fro mcomplianc e wit h othe r applicabl e statute s an d regulation s o f th e Unite d States , o f

th e Stat e o f

Illinois , o r

wit h applicabl e loca l laws , ordinance s an d regulations , d , doe s no t

tak e int o consideratio n o r attes t to th e structura l stabilit y o f an y unit s o r

part s o f

the project , an d AP C Ui K-f«uv. . IU/HS 1 090-QQ SE2fM$EiJ«^ ^ 

## decisio n ow Am B^tLtjTto K

## g©w¥rq L j«i y i , ism Fo rassistanc e i n preparin g a permi tapplicatio n contac tth e Permi tSection , Illinoi s Environmenta l Protectio n Agenc y Divisio n o f

Ai rPollutio n Contro l Permi tSectio n 2Z00 Churchil l Roa d Springfield , Illinoi s 6270 6 (217 ) 7S2-211 3 ora regiona l offic e of th e Eiel d Operation s Section . Th e regiona l office s ati d thei r area s of responsibilit

y ar e show n o n th e map . The addresse s an d telephon e numbers of th e regional office s ar e as follows : Illinoi s EP A Regio n 1 Intercontinenta l Cente r 170 1 S, . 1s tAvenu e

xMaywpod , Illinoi s 6015 3 (312) " 345-978

0 Illinoi s EP A Region . 2 541 5 Nort h Universit y Peoria , Illinoi s 61614 (309 ) 691-220

0 Illinoi s EP A Regio n 3 2009 Mai l Stree t Collinsville , Illinoi s 6223 1 (618 ) 345-070

0 

### i 

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### Illinois ; ^^OIlJEftlKfia l PrdtectioR ; AgQfjMy « 220 0 CUurcfclf

l Road , ^rringfield

, I L 62?0l 217/782-2113 JOIN T Gd «S f RUCTI08 ; 

### AN D QPEKATlU t PtfRMl

T 

### Trad e Wast e Incineration . A Divisio n o f

Chemica

l Wast e Management

, Inc . Attn : Jame

s L . Gar y 7 Mobile Avenu

e Sauget , Illinoi s 62201-106 9 Applicatio n No. : 8803010 1 Afipl I leant 1 

### s Designation : TAN KFARM 3 Subject : Tanf

c Far m Numbe

r 3 Pat e Issued : Jun

e 27 , 198

8 location : 7 Mobile Avenue , Sauget., It

, I,D , Ho. : 163121AA P Dat e Received : Marc

h 29 , 198

8 Operatin g Permi tExpiratio n Date : Jun

e 30 , 199

0

Permi ti s hereb

y grante

d to th e above-designate

d Permittee t

o CONSTRUC

T an d OPERAT E emissio

n source(s ) and/o r ai r pollutio n contro l equipmen tconsistin g o f ten 12,00

0 gal . an

d sixtee n 30,00

0 gal . wast

e blendin g an

d storage tank

s wit h carbo n adsorptio n an

d associate d truc

k an d rai l ca r unloading station s wit h vapo r balanc e a s describe d i n the above-reference d application . Thi s Permi ti s subjectto standar d condition s attache

d heret o an d the follov/in g specia l condition(s) : Operatio n of the emission source(s ) included i n thi s permi tshal l no

t begi n unti l al l associate d ai r pollutio n contro l equipmen tha s bee n constructe d an

d i s operationa

l 2 . Withi

n 60 day

s fro m th e issuanc

e o f thi s permi

ta carbo

n adsorbe

r breakthroug

h monitorin g progra

m shal l b

e submitte

d fo r Agenc

y approval . Operatio n o f thi s tan

k far m shal l no

tbegi n unti l th

e Agenc y ha s approve

d th e breakthroug

h monitor program

. 3 . Emission

s o f organi c material shal l no texcee d 2. 5 tons/year . Thi s limi t i s base d o n informatio n provided i n th e application .

Terr y y\ . Swe

i tze£/P . E . Manager , Permi t

Sectio n Divisio n o f

Ai r Pollutio n Contro l TAS:JDC:jmm/4939H/5 4 cc : Regio n 3STAT E O FILLINOI S ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O FAI RPOLLUTIO N CONTRO L 22Q o C HURCHIL L ROA O SPRINGFIELD , ILLINOI S 6270 6



### STANDAR D CONDITION S FO RCONSTRUCTION/DEVELOPMEN T PERMIT S ISSUE D B Y TH E ILLINOI S ENVHIONMENTA L PROTECTIO N AGENC Y

Th e Illinoi s Environmenta l Protectio n Ac t(Illinoi s Revise d Statutes , Chapte r 111-1/2, Sectio n 1039 ) authorizes th e Environmenta l Protectio n Agenc y t o impose conditions o n permit s whic h i tissues . Th e followin g condition s are applicabl e unles s suspersede d by specia

l condition fa). 1 . Unles s thi s permi thas been extende d o r i tha

s bee n voide d b y a newl

y issued permit , thi s permi twil l expir e on e yea tfro m th e dat

e of issuance , unles s a continuous progra m o f constructio n o r developmen to n thi s projec

tha s starte d b

y such time . 2 . Th e constructio n o r developmen tcovere d by thi s permi tshal l b e don e i n compliance wit h applicabl e provisions o f th e Illinoi s Environmenta l Protectio n Ac tand Regulation s adopte d b y th e Illinoi s Pollutio n Contro l Board . 3 . Ther e shal l b e n

o deviation s from th e approve d plan s an

d specification s unles s a writte n requestfo r modification , alon g with plan s an d specification s a s required , shal l hav

e bee n submitted t

o th e Agenc y an d a supplementa l writte n permi tissued . j f " \ Th e permittee shal l allo w an y dul y authorize d agetitO f th e £c0n&f

upo n th e p «ege |^fe^j | # f cr:edentiate

> a 

### & reasonable times : a . to ente r th e permittee' s propert y wher e actua l or potentia

l effluent , emissio n o r noise source s ar e locate d o r wher e an y activit y i s t

o b e conducted pursuan tt o thi s permit

, b . t o hav e access t

o an d t o cop y any record

s require d t

o b e kep tunder th e terms an d conditions o f thi s permit , c. t o Inspect , includin g durin g an

y hour s o

f operatio n of

equipmen

tconstructed o

r operate

d under thi s permit

, such equipmentan d any equipmen trequire d t

o b e kept , used, operated , calibrate d an d maintaine d under thi s permit, d . to , obtai n an d remov

e Sfttaple

s o f an y discharge or eipissjon g o f pollutantS i and e . t o ente r an d utiliz e any photographic , recording , testing , monitorin g O rothe r equipmentfo r the purpos e of preserving , testing , monitoring , o r recordin g an y activity , discharge , or emissio n authorized b y thi s permit. 5. Th e issuance ; o f

thi s permit : a , shal l notb

e considered a

s i n an y manne

r affectin g th e titl e of the : premise

s upon \vhic h th e permitted facilitie s are t o b e located , b . doe s no t

releas e th e permitte e fro man y liabilit y fo r damag e t o perso n orpropert y cause db y o r resulting

- fro m th e construction , maintenance , o r operatio n o f

th e propose dfacilities ,

- N

### e . doe s no t

releas e th e permitte e fro mcomplianc e Wit h othe r applicabl e statute s an d regiUatioh s o f th e Unite d f States , o f

th e Stat e o f

Illinois , o r

wit h applicabl e loca l laws , ordinance s an d regulations , d . doe s no t

tak e int o consideratio n o r attes t t o th e structura l stabilit y o f an y unit s o r

part s o f th e project , an d I L ST32-022

6 AP G IB S XRev . 10/85 1 (39*00 5STAT E OB -imNOlS ^ ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O FAf

RPOLLUTIO N CONTRO

L

. , - ZZOO^CHLfBCKlLLiROAD, „ SPRINGFIELD* , ILLINOI S 0270 6

STANDAR D CONDITION S

. EO R. OPERATIN G PERMIT S

Th e Illkoi s M^^^^P^&l^'^$^ ; ^B (Maxtiis Revise d SMtutee i Chapter Sectio n i£)3| ) gtaiit s th e Envirnntoegta l ^t^ctift n %eiitj y a^^ei^-'tcdm f ttaj g coho^tiph

s q n p whfefi ; i tissues . ffih'i ^^cp&^.c^nolffljn s ate applicabl e unles s siape;rsejie a by special perBut ; eonditlonfa X 1 . Th e issuance o f

thi s permi tdoe

s no treleas e th e permittee fro m complianc e wit h stat

e an d federa

l regulation s which ar e par to

f the Illinoi s Stat e Implementatio n Plan , a s Wel l a s wit h other applicabl e statute s an d regulation s o f th e Unite d State s o r th e State o f Illinoi s or with applicabl e loca l laws , ordinance s an d regulations. ! 2 * The tAgejac y ha s Issue d thi s permi tbase d upo n the informatio n submitted b y th e permittee i n the permit , application - An y misinformation , fals e statemento r mispresentatio n i n th e applicatio n shal l be grounds fo r revocatio n unde r 3

6 ID . Adm . Cod

e 261.207 . The permitte e shal l notauthorize , cause , directo tallo w an y modification , a s define d i n 3

5 111 . Adm * 

### (Sj§S

£ 201.102 , o

f equipment, operations or practices which ar e reflecte d i n th e permi tapplicatio n a s submitted , unles s a ne

w applicatio n o

r reques tfo rrevisio n ofth e existin g permi tis file d wit h th e Agency an d unles s a ne w permi tor revisio n of th e existin g permit(s ) i s iBsue d fo r such modification . Thi s permi tonly cover s emissio n source

s and contro l equipmen twhil e physicall y presen ta tth e inaleatfe

i plian tlocation(s) . Unles s th e permi tspecificall y provide s fo r equipmen

trelocation , thi s permiti s voi d fora

n ite m o f equipmen

to n th e da

y i ti s removed fro m the permitte d locatioaCs ) o r i f al l equipmen

tis removed

, notwithstandin g th e expiratio n dat e specifie d o

n the permit . 4 , Th e permitte e shal l allow an y dul y authorize d §gen tof th e Agency ; upo

n the presentation O

f credentials , a

t reasonabl e times : a . t o ente r th

e permittee' s propert y wher e actual o r potential effluent , emission o rnoise source

s ar e locate d o r wher e an y activit y is t

o b e conducted pursuan tt o thi s permit , b . t o have acces

s t o an d t o cop y an y records require d t o be kep tTinde

r th e term s an d condition

s of thi s permit

, q . t o inspect , includin g durin g an y hour s o f operatio n o

f equipmentconstructed o roperate

d under thi s permit

, such equipmen

tan d an y equipmen

trequire d t

o b e kept

, used , operated, calibrate d an d maintaine d unde

r thi s p erm i t, . .

. d . t o obtai n an d remov

e sample

s o f any disehairg

e o r emissio n of

pollutants , and e . t o ente r

an d utiliz e an y photographic , recording , testing , monitorin g o r othe r equipmen t

fo r th e purpos e o f preserving ; testing , monitorin g o r recordin g an y activity , discharg e o r emissio n authorize db y thi s permit . 5 . Tli e issuanc e o f

thi s permit : ja , shal l no t

b e considere da s i n an y manne r affectin g th e titl e o f th e premise s upo n whic h th e permitte d ; . facilitie s ar e located . b . doe s no t

releas e th e permitte e fro man y liabilit y fo r damag e to perso n or

propert y cause d b y o r resultin g fro m th e construction , maintenance , o r operatio n o f

th e facilities ,CMtfio/iuucMTji ? jMMrrrt / L ,.»-,,-.> , *M * AB«ic« r 1 c authorize dt o r*qiifr « tht afafprnwtton und« r EWIMKHE8W

L PR0TESTIO

H AGENC Y tHtno U Hevlta dStatute , 1979, Chante r I U UZ Sactlo n loi

o , DIVISIO N O F AI RPOLLUTIO

N C0KrR0L5 l « cl ?* ur f

* f *• « Informatio n ItfwI^Mlur at o d o t q 220 0 CttBfCMf

n SrtSW V « ¥

!«* * civi l rxmalt v u p t a$IO,O0aO 0 Bfl da n odditi s <:«)THcrtpr nmnini

S » w c cM ' P«i*It V u p t o tLOOO-O O fareac h d. y th e fatt&r aS ^tt m SPRINGFIELD

, ttllNOIS 6270 6 « fto « u p t D $t,Dgo.G & ^ dImprisonmen t u p t aana vote. ,Tti fon n ha s b»* n approve db y th e Fotf mManaownan t C*ttt» &

J ^ f rOfrOJWER * 2a . NAME ? O FC0 !?PqRAT e DIVISIO N O

RPLAff T (I f OIFfEREH

T FRO H W«ER )r . ft. 'tWWfeBiMSSR i Eb , STREE T AOORES

S O F'EHIS ^ SQIIRCE : 1:c ; STREET

. ADDRESS O

FOWNER * CIT Y J0 p EHlSSlfi N SOURCE* " TELEPHON E NUMBER

: Id: . fiT p ^ COWfTY : zf. LOCATED WITHI N CIT Y LIMITS ; " • YE S ON O le w STATf. : " " 'If s ?I P CppE ? • Z§> TDHKSHIP: : 2{I . *I P CODE :

P£RMt T INFORMATIO

N AN O REFERENC

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''APPLICATIO N NUMBE

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H NUMBE R I S TH E DAT A AH O INFORMATIO

N PREVtQOSL

Y SUBMITTE

D TRUE , OQRftECT, CURREN

T AN D COMPLETE

? OURIH

G TH I MAXIMU M E H OPERATIO N INCREASE D S REPQRTIN

I ISSrON S Fff i HAVE

REMAINE D TH E SAM E 1 PERIO

D J M THIS DECREASE D PERCENTAG

E B Y WHIC H EMISSIONS ' HAV

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CREASE D Of t DECREASE

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## * E I YE S Q fi d .....i l

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S ADOPTE D APRIL 14 , 197,2 , AN

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N I S TRUE , CORRECT, COMPLETE , AN D CURRENT . TH

E SIGNATUR

E MUS T B E THA T O FTH E PERSO N AUTHORIZE

D T O EXECUT

E A H OPERATIN

G PERMI T APPLICATION ; AUtHbRIZE D SIGNATUR

E . .

A COP Y O FTHIS FOR

M MUS T B E SUBMITTE

D FO REAC H PERMI T APPLICATION LISTE

D ABOVE . THIS DOCUMEN

T I S NO T A PERMI

T APPLICATION AN

D I S SOLEL

Y FO RSTATISTICA

L AN O INFORMATIONA

L PURPOSES . IFTH E INFORMATIO

N CONTAINE

D I N A LISTE

D PERMI T APPLICATION I S N

O LONGE RCORRECT

, MATERIA

L CORRECTIN

G TH E APPLICATIO

N SHOUL D B E SEN

T T O TH E PERMI T SECTIO N O FTI C DIVISIO N O

FAI RPOLLUTIO

N CONTROL

. I FTH E CQRRFCTtn

w I S DU E T O A MODIFICATIO

N {INCREASE I

N EMISSIONS ) O

RNE W FrtlTPMOr r

«•>< • ..;w .v, . CONSTRUCTIO

N PPnmrtnai T.V.« "DIRECTOR Y ENVIRONMENTA L PROTECTIO N AGENC Y DIVISIO N O F A m POLLUTIO N CONTRO L

U O OAVltl S 

### g*dyl,lliS 5 1 1 

### 1 Fo rassistanc e i n preparin g a permi tapplicatio n contac tth e Permi tSection , Hlmois : Environmenta l Protectio n Agenc y Divisio n o f

Ai rPollutio n Contro l Permi tSectio n 22Q 0 Churchil l Road Springfield , IUinof

e 6270 6 (217 ) 782-211 3 o ra regiona l offic e o f th e Fiel d Operation s Section , Th e regiona l office s an d thei r area s o f responsibilit

y ar e show

n o n th e map . The addresse s an d telephone number s of th e regiona

l office s are a

a follows ; niinoi s EP A Regio n 1 Intercontinenta l Gente r 170 1 S . 1s

tAvenu e Maywood , Illinoi s 6016 3 (312 ) 345-978

0 niinoi s EP A Regio n 2 541 5 Nort h Universit y Peoria , Illinoi s 61614 (309 ) 691-220

0 Illinoi s EP A Regio n 3 200 9 Mal l Street Collinsville , Illinoi s 6223 4 (618 ) 345-070

Q

### Section 2. 1 (C)(2 ) Modificatio

n o f operatin g parameter

s limit s (OPL's) Table . Pursuan tt o th e Reques

tt o Provid e Informatio

n Pursuan

tt o th e Clean Ai

r Ac t date d June 5 , 200

8 an d subsequentl

y revise d o n Septembe

r 12 , 2008 , attache

d i s a revise

d Operatin

g Parameter

s Limit s (OPL's) tabl

e tha treflec tth e mercury

, SV M and LVM OPL' s define d i n 4 0 CF R63.1209 . Th e OPL' s wer

e modifie

d base d o n th e result s o f th e performanc

e testin g tha t wer e approve

d b y th e USEPA , Regio

n 5 o n Augus t8, 200 8 an d conducte

d i n Augus tan d September

, 2008 . Thes e tes

tpla n result s hav e bee n submitte

d a s par to f th e Requestfro

m USEP A describe

d above. Veoli a ha

s extrapolate

d meta l feedrat e limit s fo r mercury

, SV M and LVM . Thes e feedrate s wer e extrapolate

d usin g th e protoco

l provide d b y USEP A (attached

) an d include

d i n th e Performanc

e Tes tPlan . The calculatio n sheet s ar e include

d wit h thi s request

. However

, based o

n th e extremel

y hig h Syste m Remova

l Efficiencies (SRE's ) achieve d durin g thi s testing , Veolia ha

s lowere d th e extrapolate

d meta l feedrate

s fo r SV M and LV

M a tUni t4 t o accoun

tfo r historica

l meta l feedrat e dat a a s define d i n 4 0 CF R1209(n)(2)(ii)(B)(2) . Veolia ha s also lowere d th e extrapolate

d meta l feedrate

s fo r SV M an

d LV M a tUni t2 t o matc h thos e values a

tUni t3 an d agai n takin g int o accoun thistorica

l meta l feedrat e dat a as define

d i n 4 0 CF R120

9 (n)(2)(ii)(B)(2) . Attache d dat a sheet s detail'th

e extrapolate

d OPL' s compare

d t o th e requeste

d OPL's . I n orde r for extrapolatio

n t o b e utilized, Veolia conducte d these performanc

e tes t usin g meta l feedrate

s a s define d i n 4 0 CF R120

7 (f)(1)(x)(B), tha

twer e greate r tha n "th e historica

l rang e o f norma l metals , feedrates " fe

d t o th e unit s ove r th e las tyear , included i

s a tabl e tha tdefines averag

e feedrate

s fo r metal s ove r th e pas tyear compare

d t o th e actua l rate s tha twer e spike d an d fe d t o th e incinerator

s durin g th e performanc

e test . A s i s detailed, th

e metal s fed t o th e incinerator

s durin g th e performanc

e tes twer e significantl

y highe r tha n th e historica l rang e o f norma l meta l feed s ove

r tha tyea r an d i n som e case s wer

e highe r tha 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 used th

e extrapolate

d metho d define d i n th e Performanc

e Tes tPla

n as require d b y 4 0 CF R120

7 (f)(1)(x ) (A ) and give

n t o Veolia b

y USEP A Regio

n 5 a s a n approve

d metho d bu talso too k int o accoun thistorica

l meta l feedrate

s fo r eac h uni ti n settin g thes e extrapolate

d value s as require

d b y th e 4 0 CF R120

9 (n)(2)(ii)(B)(2) . Veoli a i s requestin

g approva

l o f thes e extrapolate

d feedrate

s no t oni y becaus e i

tfollowe d th e requirement

s o f th e Regulation

s bu ti tha s bee n th e Agency' s practic

e o f permittin

g extrapolatio

n wit h othe r Regio n 5 incinerators . Veoli a reques

ttha textrapolatio

n b e approve

d based o

n th e merit s o f th e methodolog

y utilized, th

e meta l federate

s a twhic h th e performanc

e test s wer e

### conduce d an d theftes t result s an d becaus e the ; re q

ha s bee n complie d wit h a s define d i n th e MAC T regulat.on , 4 0 CF R 63.1200 .

### yeolia.'Environmenta l Service s - Page : 1 3 o f 17 6 ' P c r m i t N o . :

; 

### V -1 L -171 6 3 0 01 0 3 - 0 8 - 0 1



### . 2 . . ..Permittee , must'operat e Unit s 2 , 3 , an d 4 unde r thes e operating.parameter s limit s (OPI/s ) to ' demonstrate. . -fcpmpliance.-wit hEEE . .Operatin g Parameter s Uni t # 2 . Uni t # 3 Uni t # 4 • R.WFC

O • • Minimu mprimar ycombustion

- •'chamber ; temperature . - (63, ijo9 ( j ) ay,-m (2)') : •' . 1,712 ° F li 7.34-°F ' Lr/> . 71 2 . •

• / 1 ,509° F . 1/5.0. 7 ; : Minimu m

hourl y rollin g averag e Minimu msecondar y.; • . . .. : cbmbu.s'tion'chamber " V ' ; • , : "temperatur e • ' .. - • (63.120 9 (j)'<l ) , (k ) (2 ) KV:,. ; T OCf) c p i n n ^" ° v Minimu m hourl y rollin g averag e Minimu msecondar y.; • . . .. : cbmbu.s'tion'chamber " V ' ; • , : "temperatur e • ' .. - • (63.120 9 (j)'<l ) , (k ) (2 ) KV:,. ; li?84 5 - 1,84 5 3 - f U O -J .J . 1, 8 86 . Minimu m

hourl y rollin g averag e Maximum-flu e gas - f lowrate'•'.. ' b r '-productio n :.rat e • • ••• • - . 5( 6 3 ,120 . 9 ( j ) (2)

Y A (k) (.3 ) , • : <m > (2) > (n ) (5 ) , *o);(2) ) , .'.' ' 13,2CG . acf / m i n 15,14 7 13,11 1 acf/. .

m i n ' . . . - • 15,14 7 . : .43,- 4 00- '

acf/min . 38,08 6 hourl y

rollin g average s Maximu mhazardou s wast e . - pumb 1 abl e feedrat e rat e fo r .eac h combustio n chamber. . ' (63.120 9 (j ) (3) , . (k ) (4 ) } 3,003
- lbs/h r 3,12 3 4y160
-

lbs/h r ' . • 3 ,12 3 3 '?"^3,25 6

lbs/h r fo r -PC C '.an d trW l , 00 6 lbs/h r fo r sec - hourl y

-rollin g average s

• Maximum , hazardou s '.wast e '-: ' •total ' feedrate ; rats,' , for- '

. .each, : c6mpus.tio'h . chambe r '.,'' ,

: ^6A : i 2-09 X i ) o j -

/ ( : k.);(4)') . A-r

1 4 0
- • - lbs/h r 4,30 1 5,.344
-

lbs/h r 4,30 1 17,907 ^

•lbs/h r fo r I?CC - and ' 1 -7^ : ,1,00 6 Ibs/hr.for . .se c . '

- • hourl y

rollin g ..averag e basi s Operatio n o f wast e .firin g - ' syste mt

o r eac h .location ' ' • 'wher e -wast e i s fed-t o the ' .incinerato r (6. 3 ..120.9•'( j ) (4 ) ) '• ' Minimu m wast e . atomizatio n pressur e f o r lo w BT U wast e - 15 p s i Minimum ' •

wast e atomizatio n •

- pressur e f o r lo w BT U wast e - 1 5 P s i Minimum ' •

'wast e atomizatio n pressur e f o r lo w BT U wast e - 1 5 p s i Instanta n

' eou s

Maximu mtemperatur e o f th e gas. , a t th e inltet . (63 . i209.(k ) (! ) ) V (nHl ) ) . 420° F 420° F 4 3 4 hourl y rollin g averag e Minimu mcarbo n injectio n ' . ' r u t e (6 3 . !20 9 (k ) ]((, ) (i ) ) N/ A N/ A -6- ' lbs/hr . 6 . 2 hourl y

foilin g -averag e Minimum.'carrier..

- flui d (ga s o r liquid) , flowrat e o r •••'.'.' . pressur e .dro p . - ' (63 . 120 9 (k ) (6 ) (ii ) )..'. . y-,-.''.- N/ A N/ A, ' .minimu m ' hig h . pressure' : 4 psi g Maximu mlo 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 performanc e tes t (6 3 . 1.20 9 (k

) (6 ) (iii ) ) N/ A N/ A NORI T America s inc . DARCO ®FG L Tota l feedrat e of
- mercur y 0.017 4 0.017 4 0 . 25 7 1.2-hou r

### .Vebii a Environmenta l Serv-ice s . ' • Page : 1 4 o f 17 6

•Wrmi tNo . :.-V-IL-1716300i03-08-0 1 Oper a fci"»g~ Parameter s . Uni t # 2 Uni t #

3 Uni t #

4 RHFC

O {63.1209A) ; C D (i ) ) .... _ • ; rollin g averag e Maximum,;ash- . federat e • t 6 ^i26 $jm -H3i y

;'•' ' •.•

. - 

### . 67 3 •' . 9.13. 4 lbs/hf . ~ . . 

### • 67 3 7,CG 9

lbs/h r 

### 8,77 7 12-hou r •

rollin g averag e ' •Total j 'feeidrate ^ o f setai^ p Jai 'tiie ; fhfetal s ^(^^l^ainfXzi-i i i ) j'.' : '/ . ; '',; . '

• 

### '. ' 459 . \ 45. 9 v 

### 50. 0 12-hp.u r rollin g average ' limit s Total.-.feedrate-.o f lo w • . .volatile''rtie'tal s - :

: X63vi26 9 (n') : (2) ' (i i ) ).'.. ' . . 

### 39 9 ••. V 

### -39 9 50 0 . 12-hour • rollin g averag e limit s ;.Fefedra.t e •.limit s : -.fo r lo w '; ' 'y^oiatil ^ 'metal s .i n pumpabl e ' f eedstream s V

„•••' " .(63.120 9 (n ) (2 ) (vii. ) ) 

### 36 8 36 8 42 7 12^-hou r rollin g average ' limit s FeedraLte-'To f tota l chlorin e •'and . chlorid e .in ' al l • ' 'fe'edsl.ream s ' ('63 . 120 9 (n ) (4 ) > •(fli(ll ) ::
- -. • - 2-tKr . lbs/h r .



### ' . 229 . ';. 2-43
- lbs/h r ' 

### 22 9 •irhi-

lbs/h r 

### 25 2 " • 12-hou r rollin g average . Minimum , so'rbent'.' . feedrat e 'f63 . ) 209. : (o)'(4' ) (i ) ) 

### 1. 7 6 lb./l b : ri? . : 

### 1. 7 6 lb/l b ei*> r ' - 

### 1.0 1 lb/l b

r-1 2 • Minimum-carrier , flui d • .bojciate l o c nozzle , pressure . ;.:drppV :f9x";---tVve--Spray..
- dr y'• ' •;• : 'adsoricr : ; ' ( 6.3 . 120 9 . . . (o ) (4):(ii)•)'.:•; ' :•'•': : - . 

### 1.7 0 Ga1 / 1 

### C1 2 • i 

### 1.7 0 Gal /

l bG1 2 1.6 1 Gal /

l bC1 2

" The'..bTarid:•• ( i

. e. ',. manufacturer')' ' an d typ e o f ' • sdrberit'-us'edXdurin g the
cpmpieh'ensiy e performanc e .'tes t ; (63'.120' 9 •'(oH .4). : (iii ) (A)' ) Mississipp i Lim e Compan y Hydrate d Lim e Cod e MR20 0 Mississipp i •

Lim e Compan y Hydrate d Lim e Cod e MR20 0 Mississipp i

Lim e Company . Hydrate d Lim e Cod e MR200 . Maximu mcombustio n chambe r pressur e (63.12 0 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

f o r unit s 2 an d 3 an d instanta n eou s Co r uni t 4 ;-; 3 J ' - '.-Coiuplxanc e wit h standards' : 140 ' C . F ;R.

- • § 6 3 .120"6. (b ) (.1 ) ]

. ^V"'/.' ' .'thp'- emissio n standard s and-operatin g requirement s se t '-;. : .\.. . ; . f o rf;h ' derive d fron v .Subpar t EEK appl y.a t al l time s .'.•': ' i : ' 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 r ha s bee n cu t of f fo r a perio d o f tim e no tUSEP A Approve d Extrapolatio n Metho d Tota l Tota l LVMEmis . SVMEmis . H g Emis . Stackflow Oxyge n LV M Fee d Rat e (ER) SV M Fee d Rat e (ER ) H g Fee d Rat e (ER ) Tes t Dat

a Ru n (dscfm ) ( % dry ) (lb/hr

) (lb/hr

) (lb/hr

) (lb/hr

) (lb/hr

) (lb/hr

) Uni t 2 (8/08

) 1 549 6 11.7

2 0.005 2 0.00079 1 2 557

2 11.5

4 0.004 4 0.00082

2 3 535

7 11.

3 •- • . • " - • 0.004 6 0.000799 Uni t 2 (9/08

) 1 469 8 11.21 4 7 ; 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 4

7 0.00010 1 6 3 0.00036

4 Uni t 3 (8/08

) i 566 5 11.9

9 5

1 0.00038

8 65 0.00079 9 0.004

5 0.00074

8 2 5719, 10.9 6 5 1 . 0.00030 8 6

6 0.0010

3 0.005

6 0.000938 3 589

0 11.9

8 5

2 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 0030 6 0.0015 3 2 1725

5 12.1 3 5 5 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

8USEP A Approve d Extrapolatio n Metho d [1 ] [2

] [3

] [4

] 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 ) Stackflo w o f Standar d OP L Limi t (Total ) Limi t (Pump. ) (9/08 ) (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) (lb/hr

) 1 9.9.9997 3 671 8 0.00173 4 65 2 2 99.9999 1 707 5 0.00182 6 195 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

I U [2

] [3

] [4

] Propose d Uni t 2 (SVM ) Remova l Max . E R a t 75 % SV M Feedrate Extrapolatio n Em . Std. : 23 0 ug/dsc m Efficienc y (RE ) Stackflo w o f Standar d OP L Limi t (9/08 ) (% ) (dscfm.7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) 1 99.9993 6 671 8 0.00433 4 67 5 2 99.9997 8 707 5 0.00456 4 202 9 3 99.9994 2 761 4 0.00491 2 85 0 Av g 99.9995 2 713 6 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 Feedrat e Extrapolatio n Em . Std. : 13 0 ug/dscm Efficienc y (RE ) Stackflo w o f Standar d OP L Limi t (8/08 ) (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) 1 84.7 9 829 1 0.00302 4 0.019 9 2 81.3 2 824 6 0.00300 7 0.016 1 3 82.6 3 773 2 0.00281 9 0.016 2 Av g 82.9 1 809 0 0.00295 0 0.017 4 

### I 0.01 7 Extrapolate dmetal s feedrate s calculate dusing USEP A approvedmethod .USEP A Approve d Extrapolatio n Metho d [1 ] [2

] [3

] [4

] Propose d Propose d Uni t 3 (LVM ) Remova l Max . E R a t 75 % LV M Feedrate Extrapolatio n Extrapolatio n Em . Std. : 9 2 ug/dscm Efficienc y (RE ) Stackflo w of Standar d OP L Limi t Limi t (Pump. ) (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) (lb/hr

) 1 99.99924 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

] [3

] [4

] Propose d Uni t 3 (SVM ) Remova l Max . E R a t 75 % SV M Feedrate Extrapolatio n Em . Std. : 23 0 ug/dscm Efficienc y (RE ) Stackflo w of Standar d OP L Limi t (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) 1 99.9987 7 880 2 0.00567 9 46 2 2 99.99844 797 5 0.00514 5 33 0 3 99.9989 9 914 2 0.00589 8 58 5 Av g 99.9987 3 8640 0.00557 4 45 9 45 9

[1 ] [2

] [3

] [4

] Propose d Unit3(Hg ) Remova l Max . ERat75 % H g Feedrat e Extrapolatio n Em . Std. : 13 0 ug/dsc m Efficienc y (RE ) Stackflo w o f Standar d OP L Limi t (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/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 8640 0.00315 1 0.019 2 0.01 7 | Extrapolate dmetal s feedrate s calculate dusing USEP A approvedmethod .USEP A Approve d Extrapolatio n Metho d [1 ] [2

] [3

] [4

] Propose d Propose d Uni t 4 (LVM ) Remova l Max . E R a t 75 % LV M Feedrat e Extrapolatio n Extrapolatio n Em . Std. : 9 2 ug/dscm Efficienc y (RE ) Stackflo w o f Standar d OP L Limi t Limi t (Pump. ) (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) (lb/hr

) 1 99.9996 1 2771 1 0.00715 1 183 8 2 99.9992 3 2723 4 0.00702 8 91 0 3 99.9989 3 2568 3 0.00662 8 622 Av g 99.9992 6 2687 6 0.00693 6 112 3 50 0 42 7 [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/dscm Efficienc y (RE ) Stackflo w o f Standar d OP L Limi t (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) 1 99.9986 2 2771 1 0.01787 8 129 1 2 99.9980 0 2723 4 0.01757 1 87 9 3 99.9982

4 2568 3 0.01657 0 94 3 Av g 99.9982 9 2687 6 0.017340 103 8 50 0 [1 ] [2

] [3

] [4

] Propose d Unit4(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 ) Stackflo w of Standar d OP L Limi t (% ) (dscfm,7%02 ) (lb/hr ) (lb/hr

) (lb/hr

) 1 95.0 0 2771 1 0.01010 5 0.202 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 Extrapolate dmetal s feedrate s calculate dusing USEP A approvedmethod .1 Yea r Metal s Dat a 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 Uni t 4 SV M Uni t 2 Uni t 3 Unlt 4 H g 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

) : 1 2 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

8 1 2 H r Ma x Valu e 0.00539 6 0.0041 6 0.0537 3 1 2 H r Av g Valu e 1.8 8 1.1

8 .3.0

3 1 2 H r Av g Valu e . 1.7 5 •: ' 1.9

8 3.81 1 2 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 5.5

5 StdDe v 5.7 1 ."•'," . 6.8

0 6.0

9 StdDe v '•'•; ' 0.000710 9 0.000568

3 0.00894

3 Av g + 1 StdDe v 7.8 8 4.8

7 8.5

8 Av g + 1 StdDev 7.4 6 8.7

8 9.9

0 Av g +1 StdDev 0.00100 8 0.00081 2 0.01617 5 Avg + 2 StdDev 13.8 8 8.5

6 14.13 Av g + 2 StdDev 13.1 7 15.5

8 15.9

9 Av g + 2 StdDev 0.00171 9 0.001379 9 0.02511 8 200 8 Tes t Fee d Rate s 4 7 5

1 ' '5

5 200

8 Tes t Fee d Rate s 6 3 6

5 65 200 8 Tes t Fee d Rate s 0.004 7 0.005 1 0.03 1Utilizatio n o f Metho d2 3 fo r

Dioxin/Fura n Emission s Th e HW C MAC T standar dat . 4 0 CF R§63.1208(b)(l)(i)(A ) specifie s th e us e o f EP A SW-84 6 Metho d0023 A t o determin e complianc e wit h th e emissio n standar dfo r dioxin s ari dfurans . Alternatively , th e standar dprovide s i n 4 0 CF R§63.1208(b)(l)(i)(B ) tha t Metho d2 3 (4 0 CFR , Par t 60 , Appendi x A ) ca n b e used , afte r approva l b y the Administrator . Lubrizo l request s approva l t o us e Metho d2 3 t o determin e complianc e wit h th e emissio n standar dfo r dioxin s an d furan s whe n i t

conduct s th e WHR I CPT . Furthe r explanatio n an djustificatio n fo r thi s alternativ e monitorin g reques t

i s foun di n Sectio n 6.1. 3. 3 Mercur y Feedrat e Limit.Determinatio n Lubrizo l requeste dawaive r fro mconductin g th e performanc e tes t t o documen t

complianc e wit h th e mercur y emissio n standar dpe r 4 0 CFR63.1207(m ) an d63.7(h) . Thi s reques t wa s include d i n th e 200 2 CP T Pla n an dapprove db y U S EP A o n Augus t 29 , 2003 . Lubrizo l wil l utiliz e th e maximu mtheoretica l emission , coricentratiq n (MTEC ) approac h t o documen t on-goin g complianc e wit h the mercur y emissio n standar dpe r 4 0 CF R63.1207(m)(4). . Thi s approac h i s base do n al l the mercur y fe dt o th e eombusto r bein g emitte dthroug h th e stac k (Le. , d o no t

tak e an y credi t

fo r mercur y remova l i n th e ARCS) . Th e mercur y concentratio n i n al l feedstream s wil l b e determine dpe r

the feedstrea manalysi s pla n (FAP ) require db y 4 0 CF R63.1209(c) ! Th e mercur y feedrat e o f

eac h feedstrea mwil l b e determine dpe r th e discussio n i n Sectio n 3 .1 . Base d o n historica l analytica l an dwast e feedrat e data , the maximu mmercur y feedrat e limi t wil l b e 0.001 4 lb/hr . Thi s OP L wil l b e monitore do n aI2-HR A basi s an dwil l b e interlocke dt o the AWFC O system . Pe r 4 0 CF R63.l207(m)(5) . th e ful l detectio n limi t wil l b e assume dfo r feedstream s wher e mercur y i s no t detected. . I n addition , aminimu mflu e ga s flo w rat e (acfm ) OP L ha s bee n determined . Base do n flu e ga s parameter s collecte di n conjunctio n wit h th e 200 3 CPT , the mercur y emissio n limi t o f 13. 0 ug/dsc ma

t 7 percen t

oxyge n an dth e maximu mmercur y feedrat e o f 0.001 4 lb/hr ; th e minimu m flue ga s flo w rate o f

773 8 acfmwa s calculated . Th e flu e ga s flo w rat e i s continuousl y monitore d an dth e minimu mOP L wil l b e interlocke dt o the AWFC O system . Th e minimu mflu e ga s flow, rat e OP L wil l b e monitore do n a12-HR A basis . Thes e tw o OPL s i n conjunctio n assur e complianc e wit h the mercur y emissio n limi t pe r 4 0 CF R63.1207(m)(4) . 3. 4 Metal s Feedrat e Extrapolatio n Procedure s I n orde r t o establis h a n approac h fo r controllin g meta l hazardou s ai r pollutants , U S EP A groupe d th e metal s i n categorie s b y thei r relativ e volatility . Th e categorie s includ e lo w volatilit y metal s (LVM) , semi-volatil e metal s (SVM ) an dvolatil e metals . Th e LV M categor y include s arsenic ,

1 8beryllium , an dchromium . Th e SV M categor y consist s o f cadmiu man dlead . Mercur y i s the onl y volatil e meta l regulate db y th e MAC T standard . Fo r th e purpos e o f

the CPT , on e meta l fro meac h ofth e LV M an dSV M categorie s wil l b e spike d t o the incinerator . Th e mercur y feedrat e limi t i s establishe dan dmonitore dbase do n the maximu mtheoretica l emissio n concentration , a s discusse di n Sectio n 3.3 . Th e emissio n limit s fo r the LV M an dSV M categorie s fo r existin g incinerator s are :

• LV M (tota l o f

As , Be , an dCr ) 9 2 ug/dscm , correcte dt o 7 % 0 2 • SV M (tota l o f

C dan dPb ) 23 0 fig/ds'em , correcte dt o 7 % 0 2 Lubrizo l intend s t o spik e metal s durin g the CP T t o assur e tha t meta l feedrate s demonstrate d durin g th e CP T wil l allo w fo r adequat e flexibilit y base do n historica l meta l feedrat e data . However , du e t o variation s i n wast e feedstreams , analytica l uncertainties , an dothe r factors , Lubrizo l wil l continu e t o utiliz e th e metal s feedrat e extrapolatio n procedur e pe r 4 0 CF R 63.1209(n)(2)(ii ) base do n the prio r approva 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 r

U S EPA' s Boile r

an dIndustria l Furnac e (BIF ) Regulation s (U S EPA , OSWER , EPA530-R-92-011 , PB92-15 4 947 , Marc h 1992 ) provide s a detaile ddiscussio n o f th e theoretica l rational e fo r upwar dextrapolatio n o f allowabl e metal s feedrate s base do n th e relationshi p o f metal s feedrate s an demission s rate s demonstrate ddurin g testin g o f

aunit . Th e relationshi p o f metal s feedrate s an dresultin g emissio n rate s i s comple x an d dependen t

o n anumbe r

o f factor s includin g operatin g conditions , th e ai r pollutio n contro l system , an dthe meta l feedrat e itself . Thi s guidanc e ha s propose dtha t thre e zone s o f

relationshi p betwee n feedrat e an demissio 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 i n th e combustio n gas , 2 ) entrainment , whic h describe s the condition s durin g whic h rnetal s ar e primaril y entraine do n th e as h particle s i n th e system , an d3 ) complex , whic h include s the effect s fro mbot h soli dan dliqui dfee dstream s beyon dth e poin t a t whic h metal s concentration s i n th e liqui dstrea malon e ar e i n exces s o f the ga s saturatio n point . Th e guidanc e propose s that withi n eac h o f thes e zones , th e relationshi p o f feedrat e an demissio n rate i s linear . Therefore , extrapolatio n o f

metal s feedrate s withi n azon e i s performe dsimply , b y assumin g alinea r relationship . Additionally , contribution s o f metal s fro msoli dan dliqui dstream s are additive .

1 9Lubrizo l utilize dth e remova l efficienc y (RE ) demonstrate d durin g the 200 2 CP T fo r LV M an d S V M an d75 % o f

th e HW C MAC T emissio n standar d fo r th e respectiv e meta l categorie s t o determin e .th e permitte dLV M an dSV M feedrate . Th e step s fo r utilizin g extrapolatio n t o calculat e th e LV M an dSV M feedrat e limit s ar e detaile dbelow . 1 . Determin e th e demonstrate d LV M an dSV M R E base d o n dat ademonstrate d durin g th e CPT . LVMRE, % = (LV M feedrate , lb/h r - LV M emissio n rate (ER) , lb/hr ) x 10 0 L V M feedrat e lb/h r

„ _„ . (SVMfeedrate,lb/hr-SV M emissionrate(ER),lb/hr) x 10 0 S V M feedrate , lb/h r 2 . Utiliz e the flu e ga s flowrat e measure d b y th e stac k tes t cre w (i n dscfrn ) an dcorrec t t o 7 % oxyge n usin g th e followin g calculation : dscfrn (measured) *(14 -s - (21 - dry %O z )) = dscfrn, 7%0 2 3 . Calculat e the maximu mmas s emissio n rat e (ER ) o f LV M an dSV M at

7 5 percen t

o f th e H W C MAC T emissio n standar d base d o n the ga s flowrat e demonstrate d durin g th e CPT : Max LVM ER, lb/hr

= 69pg/dscm, 7% 0 2 *dscfrn, 7% 0 2 *0.0283 dscm/dscf *60min/hr

*1 lb/453.6g*lg/10 6 /xg Max SVM ER, lb/hr

= 173 /ig/dscm, 7%0 2 *dscfrn, 7% 0 2 *0.0283 dscm/dscf * 60••min/h

r * 1 lb/453. 6 g * 1 g/10 6 fig A. Calculat e the permitte dLV M an dSV M feedrat e OP L base d o h th e mas s emissio n rate s determine di n ste p 3 an dth e LV M an dSV M RE' s demonstrate d durin g th e CPT . L V M feedrat e OPL , lb/h r = Ma x LV M ER , lb/h r ((100-LVMRE,% ) -100 ) S V M feedrat e OPL , lb/h r = Ma x SV M ER , lb/h r ((100-SVMRE , % ) -100 )

2 0Th e LV M calculatio n applie s t o pumpabl e LV M an dtota l LVM , base do n th e respectiv e

feedrate s o f

pumpabl e an dtota l LV M demonstrate dduring , the CPT . Th e U S EP A approve dthi s extrapolatio n procedur e fo r th e LV M an dSV M feedrat e OP L i n alette r date dAugus t

29 , 2003 . 3. 5 Waive r o f

Monitorin g i n Certai n Feedstream s Lubrizo l doe s no t

inten dt o perfor mfeedstrea mmonitorin g fo r natura l ga s an dproces s ai r durin g th e up-comin g CPT , a s requeste di n th e 200 2 CP T pla n an dapprove db 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 r

request . I n 4 0 CF R63.1207(f)(l)(xi ) an d63.1209(c)(5 ) the HW C MAC T Standar drequire s documentatio n o f

th e expecte dlevel s o f th e regulate dconstituent s i n natura l gas , proces s ai r an d feedstream s fro mvapo r recover y systems . Th e WHR I utilize s fue l oi l a s th e auxiliar y fuel . Natura l ga s i s onl y utilize ddurin g start-u p a s apilo t (se e Sectio n 4,8) . Therefore , th e natura l ga s discussio n i s no t

applicable . Th e regulate dconstituent s i n fue l oi l ar e determine dpe r th e Feedstrea mAnalysi s Pla n an dth e feedrat e i s continuousl y monitored : Th e contributio n o f thi s feedstrea mi s include di n calculatio n o f th e tota l regulate dconstituen t feedrat e t o th e WHR I b y th e PLC . Ther e ar e n o feedstream s fro mvapo r recover y system s associate dwit h th e WHRI . Th e combustio n ai r

(proces s air ) fo r

th e uni t

i s draw n fro mambien t ai r nea r th e unit . Sinc e th e WHR I syste mi s operate da t les s tha n ambien t

pressure , the fugitiv e emission s o f regulate d constituent s fro mthe uni t wil l b e negligible . Additionally , fugitiv e emission s fro mothe r processin g equipmen t (tanks , pumps , etc. ) ar e controlle dpe r RCR A Subpar t

BB . Therefore , th e feedrat e o f

regulate dconstituent s i n the proces s ai r introduce dt o the WHR I syste mwil l b e considere dnegligibl e a s compare dt o th e regulate dconstituent s containe di n th e wast e an dfue l feedstreams . 3. 6 Operatio n o f

Wast e Firin g System I n 4 0 CF R63.1209(j)(4 ) th e HW C MAC T Standar drequire s tha t a n operato r

mus t specify operatin g parameter s an dlimit s t o ensur e tha t goo doperatio n o f

eac h hazardou s Waste firin g syste mi s maintaine dt o ensur e complianc e wit h the PR E standards . Th e require dOPL s pe r 4 0 C F R63.1209(j)(l ) -(3 ) are :

• Minimu mcombustio n chambe r temperature s

• Maximu mflu e ga s flowrat e

• Maximu mwast e feedrat e

2 1

### 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 th e Materia l Processin g Area s tha t excee d th e containe rsiz e limit s fo rLeve l 1 controls . Th e processin g o f Leve l 2 container s a t Veoli a i s identica l t o tha t o f 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 CF 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 y Monitorin g an d Testin g sectio n t o reflec t onl y thos 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 w atmospheri 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 GF 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 w atmospheri c pressure . Th e las t sentenc e o f 2.4(D)(1 ) simpl y need 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 wit h 4 0 CF R 71.5(c)(11 ) an d 3 5 IA C 201.210 . Thi s activit y 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 y HA P i n exces s o f 10001 b pe ryear . Likewise , i t doe s no t emi t mor e tha n 1. 0 l 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 l b / hou r o f an y HA 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 th e dru m crushin g operation : Accordin g t o previou s TR I report s submitte d b y th e facility , th e majo rregulate d constituent s processe d b y th e facility , tha 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 y conservativ 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 th e VO M contai n in , an d release d fro m th e 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 c pressur e = 14. 7 ps i Densit y o f ai ra t 20° C = 0.074 8 lb/ft 3 

### Molecula rweigh t o f ai r= 28.9 7 Ib/lb-mol e Dimension s o f a 55-gallo n dru m = 2 4 inc h diamete rx3 3 inc h hig h = 2 f t diamete rx2.7 5 f t hig h Volum e o f a 55-gallo n dru m = |~ | * (radius) 2 

### * heigh t

= 3.14 . *(1) 2 

### * 2.7 5 = 8.63 5 ft 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 l b 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 l b methano l vapo ri s containe d i n a n empt y 5 5 gallo n drum . I f a n empt y dru 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 wit h 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 y drum s o f non-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 sampie d ar e les s tha n 5 5 gallon s i n size . Approximatel y hal f o f th e drum s receive d contai n solids , whic h emi t littl e o rn o vapors . I f 0.0045 7 l b o f methano l i s emitte d wit h ever y dru m sampled , assum e tha t hal f o f tha t i s attribute d t o HA P material ; 0.00228 5 l b HA P pe rdrum . Veoli a currentl y sample s approximatel y 3 0 drum s pe rhour , roughl y 3 hour s pe rday , 6 day s pe rweek ; 93 6 hour s / year . 3 0 druni s /

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

hou r* 93 6 hour s /

yea r= 12 8 l b VO M / yea r 3 0 drum s /

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

### 0.068 6 l 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 y relate d t o th e numbe ro f samples ; thi s i s t o sa y tha t whe n th e wor k loa d i s increased , th e hour s spen t samplin g increase s accordingly . Th e numbe ro f drum s sample d pe rhou rwil l no t fluctuate , o n th e average , dramatically . Eve n i f Veoli a sa w a 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 w th e limit s require d t o b e a n insignifican t activity . 4 3 drum s /

hou r* 0.0045 7 l b methano l / dru m = 0.19 7 l b VO M / hou r 0.19 7 l 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 l b HA P / dru m = 0.098 2 l b HA P / hou r 0.098 2 l b HA P /

hou r* 93 6 hour s /

yea r= 9 2 l b HA P /

yea r 4 0 GF R 71.5(c)(11 ) limit s insignifican t activitie s t o 2 TP Y regulate d ai r pollutant . Eve n i f samplin g th e unlikel y 4 3 drum s / hour , ther e ar e no t enoug h hour s i n a yea rfo rVeoli a t o excee d th e emissio n limit s give n a t 4 0 CFR71.5(c)(11)
. 400 0 l b VO M /

yea r* 1 h r/

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

yea r* 1 h r/

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

year : 8,73 6

### 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)( 1 i ) 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 y HA 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 ro f 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 y HA 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

thai 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 th e USEP A website . Th e versio n mos t recentl y use d wa s TANK S 4.0.9d . Th e maximu m annua l gasolin e emission s calculate d b y TANK 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 o approac h th e 2 TP Y regulate d ai rpollutan t limit , Veoli 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 o TANK S calculations ; A t thi s throughput , 3,74 0 l b (1.8 7 T ) o f gasolin e emission s woul d b e release d annually . Th e constituent s o f gasolin e var y significantly , 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 th e annua l throughpu t o f 4 millio n gallons , i f on e quarte ro f th e tota l gasolin e emissionsar e attribute d t o toluene , thi s woul d resul t i n emission s o f 93 5 l b toluen e annually , whic h doe s ho t excee d th e 1,00 0 l b HA P limit . Wit h respec t t o th e 1. 0 lb / hou rlimi t o n an y non-HA P pollutant , assum e tha t Veoli a unexplainabl y triple s th e 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 (16 8 hours) , thi s woul d stil l no t excee d th e 1. 0 lb/hou rlimit .

### Regardin g the : 0. 1 lb/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 l b fo rth e 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 y excee d 0. 1 l b Toluen e pe rhour . Thes e extremel y exaggerate 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 y o 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 y qualif y i 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 16:4 6 Ru n Lengt h (minutes ) - 13 0 PP M PP M PP M PP M PP M Wast e Typ e Btu/l b %ChIorin 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 5 150 0 PC C Lo w Bt u 285 0 0.00 2 0.6 6 0.0 3 0.00 3 0.0 6 0.0002 5 0.00 6 (Chromiu mSpike ) 0 0 26. 6 0 0 0 0 17700 0 PC C S p Fd r 80 0 0.0 1 12. 5 0.00 5 0.00 1 0.0 1 0.0002 5 0.3 3 Containerize dSolid s 18 0 0.0 8 63. 4 313.9 2 196. 2 92.2 1 0.2 5 1177. 2 (Lea dSpike ) 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 Chromi c Aci d: StartWg t En dWg t Tota l Wg t Averag e (Batc h CH08H00216 ) L b L

b L

b Lb/H r 1124. 8 56 8 556. 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 24 5 47 4 2. 6 Ib/chg 6. 4 Ib/chg 62.1 % Pb 89.8 % CI 2Uni t # 2 Revise d Run# 1 Date : 09/08/0 8 Tes t Time : 14:3 6 t o 16:4 6 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 (lb/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 2.8 9 7. 1 8. 9 0.0 0 0.00 0 0.08 8 0.00 0 0.8 2 PC C Lo w Bt u 101 8 2.9 0 0. 0 6. 7 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 (Chromiu mSpike ) 25 7 0.0 0 0. 0 68. 4 0.0 0 0.00 0 0.00 0 0.00 0 45.4 9 PC C S p Fd r 24 4 0.2 0 0. 0 30. 5 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 Containerize dSolid s 47 4 0.0 9 0. 4 300. 2 0.1 5 0.09 3 0.04 4 0.00 0 0.5 6 (Lea dSpike ) 100 0.0 0 0. 0 63. 6 61.8 5 0.00 0 0.00 0 0.00 0 0.0 0 (Chlorin e Spike ) 24 5 0.0 1 220. 2 1. 2 0.0 0 0:00 0 0.00 0 0.00 0 0.0 0 Total s 288 6 6. 1 22 8 48 0 62. 0 0.09 1 0.1 3 0.0 0 46. 9Uni t # 2 Revise d Ru n # 2 Date : 09/09/0 8 Tes t Time : 12:2 0 t o 14:3 0 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 PC C Hig h Bt u 493 0 1. 5 1.6 7 0.7 2 0.1 1 16 0 0.0002 5 140 0 PC C Lo w Bt u 176 0 0.00 2 0.0 3 0.0 3 0.00 4 0.0 4 0.0002 5 0.002 5 (Chromiu mSpike ) 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 0.0002 5 0.1 2 Containerize dSolid s 32 0 0.1 6 60. 8 234.9 6 156.6 4 88.1 1 0.2 5 949.6 3 (Lea dSpike ) 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 Chromi c Aci d: Star t Wg t En dWg t Tota l Wg t Averag e (Batc h CH08H00216 ) L b L

b L

b Lb/H r 1076. 6 522. 9 553. 7 25 6 Solids : Numbero 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 5 201 5 39. 2 93 0 10 2 25 1 57 7 2. 6 Ib/chg 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 t o 14:3 0 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 0.00 0 0.08 8 0.00 0 0.7 7 PC C Lo w Bt u 110 3 1.9 4 0; 0 0. 3 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 (Chromiu mSpike ) 25 6 0.0 0 0. 0 68. 0 0.0 0 0.00 0 0.00 0 0.00 0 45.2 3 PC C S p Fd r 24 4 0.1 9 0. 0 22. 8 0,0 0 0.00 0 0.00 0 0.00 0 0.0 0 Containerize dSolid s 57 7 0.1 8 0. 9 350. 8 0.1 4 0.09 0 0.05 1 0.00 0 . 0.5 5 (Lea dSpike ) 10 2 0.0 0 0. 0 65. 2 63.3 4 0.00 0 0.00 0 0.00 0 0.0 0 (Chlorin e Spike ) 25 1 0.0 1 225. 5 1. 3 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 Total s 308 2 5. 0 23 5 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 : 09:4 4 t o 11:5 3 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 24 0 0.0002 5 63 0 PC C Lo w Bt u 148 0 0.002 5 0.0 1 0.0 3 0.00 5 0.0 4 0.0002 5 0.002 5 (Chromiu mSpike ) 0 0 26. 6 0 0 0 0 17700 0 PC C S p Fd r 24 0 0.0 1 6.4 1 0.00 5 0.00 2 0.00 5 0.0002 5 0.3 7 Containerize dSolid s 25 0 0. 1 61. 5 234.2 4 165.9 2 87.8 4 0.2 5 97 6 (Lea dSpike ) 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 Chromi c Aci d: Star t Wg t En dWg 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 Solids : Numbero f 1 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 4 207 1 39. 1 96 3 10 2 25 0 61 2 2. 6 ib/ch g 6. 4 Ib/chg 62.1 % P b 89.8 % CI 2Uni t # 2 Revise d • Ru n # 3 Date : 09/10/0 8 Tes t Time : 09:4 4 t o 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 Typ 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 2.6 2 8. 8 5. 5 0.0 0 0.00 0 0.13 2 0.00 0 0.3 5 PC C Lo w Bt u 105 5 1.5 6 0. 0 0. 1 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 (Chromiu mSpike ) 26 1 0.0 0 0. 0 69. 5 0.0 0 0.00 0 0.00 0 0.00 0 46.2 3 PC C S p Fd r 23 4 0.0 6 0. 0 15. 0 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 Containerize dSolid s 61 2 0.1 5 0. 6 376. 2 0.1 4 0.10 1 0.05 4 0.00 0 0.6 0 (Lea dSpike ) 10 2 0.0 0 0. 0 64. 9 63.0 8 0.00 0 0.00 0 0.00 0 0.0 0 (Chlorin e Spike ) 25 0 0.0 1 224. 5 1. 3 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 I 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 Ru n Lengt h (minutes

) — 13 0 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 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 0.5 1 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 PC C S 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) 25 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 : Start Wg t En d Wg t Tota l Wg t Averag e (Batc h CH08E00643) L b L b L b Lb/H r 1225. 6 67 6 549. 6 25 4 Solids : Numbe ro 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 rHou 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/ch g 0.03 1 Ib/ch g 5. 8 Ib/ch g I 62.1 % P b 98 7 pp m H g 89.8 % CI 2Uni t # 2 Revise d Ru n # 1 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 Feedrate 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 0.0000 1 0.0 0 0.00 0 0.00 6 0.00 0 0.0 0 PC C Lo wBt u 108 7 0.1 6 5. 5 1. 2 0.0000 1 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 (Lea d 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 0 209 1 0.003 9 64. 6 0.4 1 0.0 2 0.0 0 48. 8Uni t # 2 Revise d Ru n # 2 Date : 08/12/0

8 Tes t Time : 11:0

5 to 13:1 6 Ru n Lengt h (minutes ) - - 13 1 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 289 0 3. 4 7 0.042 5 1. 3 0. 1 1 1 0.01 5 4. 7 PC C Lo wBt 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 0.0 1 0.0 5 0.002 5 0.2 2 Containerize d Solid s 1690 1 0.3 3 6.0 1 4.87 1 960. 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 66 7 0 0 0 0 0 Total s Chromi c Aci d : Start Wg t En d Wg t Tota l Wg t Averag e (Batc h CH08E00643 ) L b L b L b Lb/H r 812. 9 252. 8 560. 1 25 7 Solids : Numbe ro 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 rHou 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 22 8 49 5 2. 6 Ib/ch g 0.03 1 Ib/ch g 5. 8 Ib/ch g 62.1 % P b 66 7 pp m H g 89.8 % CI 2 IUni t # 2 Revise d Ru n # 2 Date : 08/12/0

8 Tes t Time : 11:0

5 to 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 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 49 9 1.44 17. 0 34. 9 0.0000 2 0.0 0 0.00 0 0.00 5 0.00 0 0.0 0 PC C Lo wBt 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 0.0024 1 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 63.6 0 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 0.0008 1 0.0 0 0.00 0 0.00 0 0.00 0 0.0 0 Total s 280 5 2. 5 22 9 21 8 0.003 3 64. 1 0.3 7 0.0 1 0.0 0 49. 3Uni t # 2 Revise d Ru n # 3 Date : 08/13/08 Tes t Time : 10:3

9 t o 12:4

7 Ru n Lengt h (minutes ) - 12 8 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 164 0 3. 2 6.5 4 0.0 4 1. 1 0. 1 1 7 0.01 5 4. 1 PC C Lo wBt 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 25 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 Aci d : Start Wg t En d Wg t Tota l Wg t Averag e (Batc h CH08E00643 ) L b L b L b Lb/H r 725. 4 188. 2 537. 2 25 2 Solids : Numbe ro 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 rHou 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 22 3 48 9 2. 6 Ib/ch g 0.03 1 Ib/ch g 5. 8 Ib/ch g j 62.1 % P b 54 8 pp m H g 89.8 % CI 2Uni t # 2 Revise d Ru n # 3 Date : 08/13/08 Tes t Time : 10:39 t o 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 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 0.8 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 Lo wBt 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 0.4 1 0.35 2 0.00 4 0.00 0 .2.5 2 (Lea d 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 Total s 280 6 3. 6 22 2 21 7 0.003 1 62. 5 0.3 5 0.0 1 0.0 0 48. 3Uni 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 y Fee 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 . o f 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 run ave.'s) Tota l LV M Fee d (Lb/hr ) 4 7 4 7 4 7 4 7 (Ave . o f tes t run ave.'s ) SV M Fee d (Lb/hr ) 6 2 6 4 6 3 6 3 (Ave . o f tes t run ave.'s ) Chlorin e Fee d (Lb/hr ) 22 8 23 5 23 4 23 2 (Ave . o f tes t run ave.'s )Recalculate dMeta l Concentration s i n Soli dWaste s

200 8 Metal s Emissio n Testin g ft' A Uni t 2 -'''*'--

xReporte 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 Moistur e 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 4.8 6
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 Moistur e 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 9/10/200 8 3 87.8 4 0.2 5 97 6 234.2 4 165.9 2 N ANotificatio 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 o f

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

EE E — Nationa l Emissio n Standard s fo r Hazardou s Ai r

Pollutant s fo r

Hazardou s Wast e Combustors . Thi s NO C i s bein g mad e in accordanc e wit h §63.9(h) . SECTIO N I GENERA L INFORMATIO N A . I f yo u hav e bee n issue daTitl e V permit , d o no t complet e thi s form . Submi t you r NO C i n accordanc e wit

h you r Titl e V permit . [§63.9(h)(3) ] B . I f yo u hav e no t

bee n issue daTitl e V permit , complet e th e remainin g portion s o f thi s sectio n an dals o complet e Section s Il-IX . [§63.9(h)(2)(i) ] C . Prin t o r typ e the followin g informatio n fo r eac h facilit y fo r

whic h yo u ar e makin g notificatio n o f complianc e status : Operatin g Permi t Numbe r(OPTIONAL ) Facilit y I .P . Numbe r(OPTIONAL ) 

## V-IL-1716300103-08-0 1 1LD09864242 4 Responsibl e Official' s Name/Titl e 

## Dou g Harri s Stree t Addres s 

## # 7 Mobil e Av e Cit y Stat e ZI P Cod e 

## Sauge t IL 

### 62201-106 9 Facilit y Nam e (i f differen t fro m Responsibl e Official' s Name ) 

## Veoli a E S Technica l Solutions , L.L.C
. Facilit y Stree t Addres s (I f differen t tha n Responsibl e Official' s Stree t Address ) Facilit y Loca l Contac t Nam e Titl e Phon e (OPTIONAL ) 

## Dou g Harri s Genera l Manage r 618-271-280 4 Cit y Stat e ZI P Cod e 

## Sauge t I L 62201-106 9

• . Indicat e the relevan t standar d or

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 rthi s notificatio n (relevan t standar d o rothe rrequirement ) Complianc e Dat e (mm/dd/yy ) 

## 4 0 CF R 63.1200 Jun e 30 , 200 4

1SECTIO N I I CERTIFICATIO N (Note: you may edit the text in this section as deemed appropriate) Base dupo n informatio n an dbelie f forme dafte r

areasonabl e inquiry , I , a s aresponsibl e officia l o f the above-mentione dfacility , certif y th e informatio n containe di n thi s repor t i s accurat e an dtru e t o the bes t o f m y knowledge . Th e above-mentione dfacilit y ha s complie dwit h th e relevan t

standar d o r an dothe r

applicabl e requirement s reference di n th e relevan t standard . [§63.9(h)(2)(i)(G) ] Nam e o f Responsibl e Officia l (Prin t o rType ) Titl e Dat e (mm/dd/yy ) 

## Dou g Harri s Genera l Manage r 10/10/200 8 Signatur e of Responsibl e Officia l

SECTIO N II I Describ e the method s yo u use dt o determin e compliance , [§63.9(h)(2)(i)(A) ] RCR A Tria l Bur n Dat afro mEP A approve dtestin g a s require dbyth e RCR A Part B permi t

an dtestin g conducte dprio r

t o the complianc e dat e usin g al l approve dEP A method s wa s use dto demonstrat e complianc e wit

h al l applicabl e emissio n standard s define din 4 0 CF R63.1203 . I n addition , Performanc e Testin g approve db y USEPA , Regio n 5 o n Augus t 8 , 200 8 an dconducte din Augus t an dSeptembe r

o f 2008 . Se e th e attache dOperatin g Parameter s Table s an dHW C MAC T Emissio n Standard s tabl e fo r Unit s 2/ 3 an d Uni t 4 , that defin e th e operatin g parameter s establishe ddurin g testin g tha t ensure s complianc e wit h th e performanc e standards . SECTIO N I V Describ e th e results o

f an y performanc e tests , opacit y d r visibl e emissio n observations , continuou s monitorin g syste m(CMS ) performanc e evaluations , and/o r other monitorin g procedure s or

method s that

wer e conducted . [§63.9(h)(2)(i)(B) ] Se e attache dtes t

results tha

t wer e use dt o develo p th e limit s define din th e Operatin g Paramete r Table s reference di n Sectio n II I o f thi s report . Thes e result s als o includ e monitorin g method s an dprocedures . Als o attache dar e the Facility' s Continuou s Emission s Monitorin g Syste mQuality Assuranc e Pla n an dContinuou s Monitorin g Syste mQualit y Contro l Program . SECTIO N V Describ e tti e method s yo u wil l us e to determin e continuou s compliance , includin g adescriptio n o f monitorin g an dreportin g requirement s an dtes t methods . [§63.9(h)(2)(i)(Q ] Continuou s complianc e i s base do n th e operatin g paramete r limit s establishe dfro mcomplianc e testing , define di n th e attache dOperatin g Parameter s Tabl e reference din Sectio n 11 1 o f thi s report . Thes e incinerato r

operatin g parameter s ar e monitore dcontinuousl y t o verif y complianc e b y aproces s monitorin g an dcontro l system . Th e detail s of thes e system s ar e define din detai l in Sectio n 2.0 , Incinerato r

Proces s descriptio n reference di n Sectio n VII I of thi s reportan dattached .

2SECTIO N V I Describ e the typ e an dquantit y o f hazardou s ai r

pollutant s (HAP ) emitte db y th e sourc e (or surrogat e pollutant s i

f specifie di

n th e relevan t

standard) , reporte din unit s an daveragin g time s an din accordanc e wit

h th e tes t

method s specifie din th e relevan t standard . [§63.9(h)(2)(i)(D) ] Se e attache dtes t

result s f ro mcomplianc e testin g tha t wa s con d the HAP' s an dother

pollutant s define di n Subpart EEE . . _

^ . .•„•;,.... : SECTIO N VI I I f the relevan t

standar dapplie s t o bot h majo r an dare asources , presen t a n analysi s demonstratin g whethe r th e affecte dsourc e i s amajo r sourc e (usin g th e emission s dat a generate dfo r

thi s notification . [§63.9(h)(2)(i)(E) ] Thi s facilit y i s amajo r

sourc e du e to it s applicability to th e NESHA P regulations , specificall y Subpart EE E an dSubpar t

DD . Regardles s o

f th e facility' s emissio n concentrations , this.:facility-i s amajo r sourc e b y definition ; . :
SECTIO N VII I Describ e th e ai r

pollutio n contro l equipmen t (o r method ) fo r

eac h emissio n point , includin g eac h Contro l devic e (o

r method ) fo r

eac h hazardou s ai r

pollutan t

an dthe contro l efficienc y (percent ) fo r eac h contro l devic e (o

r method) . [§63.9(h)(2)(i)(F) ] Se e attache dSectio n 2.0 , Incinerato r Proces s Descriptio n fro m200 8 Performanc e Tes t Plan s fo r Incinerator s 2 , 3 an d4 tha t describe s th e ai r

pollutio n contro l equipmen t fo r eac h emissio n point . Also , se e attache dth e complianc e testin g dat adefine din Sectio n I V o f thi s repor

t tha t detail s th e contro l efficienc y fo r

eac h contro l device . , . SECTIO N IX A . Di dyo u submi t

a n applicatio n fo r

constructio n o r

reconstructio n unde r

§63.5(d ) tha

t containe d preliminar y d

r estimate ddata ? [§63.9(h)(5) ] Ye s i.; . Not'- . . No t applicabl e : . (di dnot

submi t a n applicatio n fo r

constructio n or reconstruction) . 8 . I f yo u answere dyes , provid e actua l emissio n dat aor othe r correcte dinformatio n below .

EN D O F FORM . A Responsible Official

must sign this form -? Se e Sectio n II .

3i 

## HW C MAC T Emissio n Standard s

Paramete r Unit s Standar d Metho do f Complianc e Dioxin/Fura n (D/F )
Mercur y (Hg ) *
Semivolatil e Metal s (SVM ) Cadmium , Lea d* L o w Volatil e Metal s (LVM ) Arsenic , Beryllium , Chromiu m* Carbo n Monoxid e (CO ) Hydroge n Chloride/Chlorin e (HC1/C12 ) Particulat e ng/dsc mTE Q ug/dsc m ug/dsc m ug/dsc m
ppm v
ppm v mg/dsc m 

### 0.20

13 0
24 0
9 7 

### 10 0
7 7 

### 3 4 Operatin g Paramete r Limit s Operatin g Paramete r Limit s Operatin g Paramete r Limit s Operatin g Paramete r Limit s Continuou s Emission s Monito r Operatin g Paramete r Limit s Operatin g Paramete r Limit sUNIT S 2/ 3 OPERATIN G PARAMETER S

Operatin g Paramete

r Maximu mTota l Pumpabl e Wast e (Hourl y Rollin g Total ) Maximu mTota l Hazardou s Wast e (Hourl y Rollin g Total ) Maximu mStack

Ga s Flo w Rat e (Hourl y Rollin g Average ) Minimu mPrimar

y Combustio n Chambe r Temperatur

e (Hourl y Rollin g Average ) Minimu mSecondar

y Combustio n Chambe r Temperatur

e (Hourl y Rollin g Average ) Maximu mBaghous e Inle t Temperatur

e (Hourl y Rollin g Average ) ^ax . Pump . Lo w Volatil e Metal s Feedrat e (1 2 Hou r

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

Rollin g Total ) Maximu mSem

i Volatil e Metal s Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mMercury Feedrat e (1 2 Hou r Rollin g Total ) Maximu mChlorin e Feedrat e (1 2 Hou r Rollin g Total ) Maximu mAs h Feedrat

e (1 2 Hou r Rollin g Total ) Minimu mSorben

t Feedrat e (Hourl y Rollin g Average ) Minimu mCarrier

Flui dFlowrate (Hourl y Rollin g Average ) Unit s Lb/h r Lb/h r Acfm Deg F Deg F Deg F

Lb/h r Lb/h r Lb/h r Lb/h r Lb/b r Lb/h r Lb/l b CI 2 Gal/l b CI , Limit s

312 3 430 1 15,14 7

171 2

184 5

420

4 6 4 7 63 0.004 7 22 9 67 3 1.7 6 1.7 0 Tes t

Dat e 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 Performanc e

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

DRE , D/ F

D/F , SVM , L V M L V M L V M SV M H g SVM , LV M HC1/C1 2 Part . HC1/C1 2 HCyC1 2UNI T 4 OPERATIN G PARAMETER S

Performanc

e Operatin g Paramete

r Unit s Limits TestDat e Standard s Maximu m Tota l Pumpable Lb/h r Wast e (Hourl y Rollin g Total ) Maximu m Total 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 Combustion De g F Chambe r Temperatur

e (Hourly Rollin g Average ) Minimu m Secondar

y Combustion De g F Chambe r Temperatur

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 Metals Lb/h r Feedrat e (1 2 Hou r Rollin g Total ) Max ; Total Lo w Volatil e Metal s Lb/h r Feedrat e (1 2 Hou r Rollin g Total ) Maximu m Semi Volatil e Metal s Lb/h r Feedrat e (1 2 Hou r Rollin g Total ) Maximu m Mercury Fee d rat e Lb/h r (1 2 Hou r Rollin g Total ) Maximu m Chlorin e Feed rat e Lb/h r (1 2 Hou r Rollin g Total ) Maximu m As h Fee d Rat e (1 2 Lb/h r Hou r Rollin g Total ) Carbo n Injectio

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 38,086

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 , L V M DRE , D/ F

DRE , D/ F

D/F , SVM , L V M L V M L V M SV M H g SVM , LVM , HC1/C12 Part . D/F , H g

Minimu m Sorben

tFeedrat

e Lb/l b Cl 21.0 1 (Hourl y Rollin g Average) Minimu m Carrie r Flui d Flowrat e Gal/l b Cl 21.6 1 (Hourl y Rollin g Average) Dec , 199 5 Dec , 199

5 HC1/C12

HC1/C1 2

# UNIT 2 EMISSIO N RESULT S

# ENS R Tabl e 3- 3 R M 2 9 Samplin g Parameter s an d Emissio n Result s - Wee k o f Augus t 11 , 200 8 (Ru n No . j t j 2 3 •Dat e T lt-Aug-0 8 f 12-Aug-3 3 \ 13-Aag-a a \ Start Tim e Unit s T 14:4 0 T 11:0 5 T 10:3 9 Sto p Tim e r 16:5 0 r131 6 f 12:4 7 AVG S ! Samplin

g Parameter

s — X 29 5 5 | Barometri c Pressur e in . H g r?9.6i ) f 2 9 5 0 29.6 1 \ Volum e Metere d de f r8 3 65 0 f 86.04 4 r85.61 1 81.99 6 | Sampl e Volum e dsc f i 76.75 0 i 80.23 3 i 78.03 6 78.34 0 : Moistur e I O i a t Stac k % v/ v % dr y | 39. 9

T 11.7 2 j 40. 1

r11.5 4 ; 41. 4

f 11.3 0 40. 5

11.5 2 Av g Stac k

Temp . ° F f 36 9 r37 0 r35 8 ' 36 5 ! Stac k Flowrat e dscfr n !5^49 5 ! 5 ,57 2 \5 ,35 7 5,47 5 i isokinetic s % f 9 3 9 6 9 7 9 5 Mercun r(Hg ) — Quantit y Collecte d p g 1 83. 5 i 8 9 4 \87. 9 87 . 6 Stac k Con e @ 7 % 0 2 ug /m 3 1 58 . 0 ! 58. 2 j 57. 4 57. 9 i Stac k Emissio n Rat e Ib/h r i 7.9 1 E-0 4 i 8.22E-0 4 7 99L-0 4 ' 8.04E-0 4

g /se c I 9.96E-0 5 I 1.04E-0 4 i 1.0 1 E-0 4 ' 1 01L-0 4 Tota l Chromiu

m (Cr ) — LV M Quantit y Collecte d M 9 i 78.7 5 ! 75.6 6 ; 73.1 5 75.8 5 Stac k Cone
. @ 7

% 0 2 pg

/m 3 I 54.6 6 i 49.2 8 i 47.7 6 50.5 7 Sf.ir k Emissio n Rat e lb/h r 7 46E-0 4 ! 6 951. . 0 4 i 6.64E-0 4 7.02E-0 4

g/se c | 9.40E-0 5 I 8.76E-0 5 i 8.37E-0 5 8.84E-0 5 Cadmiu m (Cd ) — SV M Quantit y Collecte d M' 9 I 1.9 9 : 2.0 6 1.86 v

# _ Stac k Cone
. @ 7 % Q 2 ug/m 3 1.3 8 1.3 4 1.2 1 1.3 1 i Stac k Emissio n Rat e lb/h r i 1.88E-0 5 i 1.89E-0 5 " ' 1.081.-0 5 " 1.82 b 0 5

g/se c i 2.37E-0 6 i " 2.38E-0 6 " ; 2 12F . 0 6 " 2.29 L 0 6 Lea d (Pb)- i Quantit y Collecte d SV M p g i 329. 5 36 9 2 36 9 5 r " 35 6 0 8 Stac k Cone
. @ 7 % 0 2 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 3.39E-0 3 \ 3 36 L 0 3 ' 3.29E-0 3 g/se c 3 93E-0 4 • 4 .27L -04" ' '423L-0 4 r4 j : 4E-fJ 4 Arseni c (As ) — I Quantit y Collecte d p g i 17.0 0 10.0 8 5 .6 7 r1 0 9 2 Stac k Cone
. @ 7

% 0 2 ug/m 3 i 118 0 6.5 7 3 .7 0 7 .3 6 Stac k Emissio n Rat e ib/h r i 1 61F . 0 4 i 9 261

- 05 ; 5 15E0 5 ' l 0 2 L 0 4 j j g/sec i 2.03E-0 5 i 1.1/E-0 5 6.49E -0 6 ' 1.28E-6 5 [Berylliu m (Be ) — Quantit y Collecte d p g j 0.2 0 • 02 0 \ 0.2 0 ' 0.2 0 (Stac k Cone
. @ 7

% 0 2 ug/m 8 1 0.1 4 : 0.1 3 j 0 .1 3 0.1 3 j Stac k Emissio n Rat e ib/h r j 1 89 b 0 8 ; 1.84E-0 6 ; 1.82E-0 6 r 1.85E-0 6 I i g /se c ? 39l f 0 7 2.32F-0 7 : 2 29r : 0 7 ' 2.33E-0 7 LV M Total = ug/m 3 i 56 . 0 51. 6 53. 8 ;SVMTota ( = ug/m 3 j 230. 1 I 241. 8 ' • 242 . 5 238.

1

C:\DOCUME-1\klarich.TWI\LOCALS-1\Temp\notesD3055 0 Weoli a Repor tUni t2 final.doc 3-4 Octobe r 200 8

# ENS R

Tabl e 3-4 Summar y o f HW C MAC T Metal 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 11.8 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

y Standar d = 9 7 ug/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 Pb 22 9 24 0 24 1 C d 1.3 8 1.3 4 1.2 1 Total SV M 23 0 24 2 24 2 23 8

SV M Regulator

y Standar d = 24 0 ug/m 3 Mercur y Emission s -ug/m 3 @ 7 % 0 2 Ru n 1 Ru n 2 Ru n 3 Averag e 58. 0 58. 2 57. 4 57. 9 Mercur y Regulator

y Standar d = 13 0 ug/m 3

C:\DOCUME~1\klarich.T

W l\LOCALS- 1 \Temp\notesD3055 0 Weoli a Repor tUni t2 final.do

c 3- 5 Octobe r 200 8

# ENS R Tabl e 3- 5 R M 2 9 Samplin g Parameter s an dEmissio n Result s - Wee k o f Septembe r

8 , 200 8

Ru n No . 1 2 3 Dat e r 08-Sep-0 8 r 09-Sep-0 8 r lO-Sep-0 8 Star t Time Unit s r 14:3 6 r

12.2 0 * 09:4 4 Sto p Tim e r 16:4 6 r

14:3 0 r

11:5 3 AVG S Samplin g Parameter

s — Barometri c Pressur e in . H g r 29.6 0 r

29.7 5 r

29.7 2 " 29.7 1 Volum e Metere d de f " 77.38 2 r

79.26 9 r

78.90 5 ' 77.05 9 Sampl e Volum e dsc f 75.29 6 78.40 7 78.65 4 ' 77.45 2 Moisture % v/ v 41. 4 41. 2 41. 8 41. 5 0 2a t Stac k % dr y r 11.2 1 r

10.9 1 r

11.3 5 11.1 6 Avg . Stac k

Temp . ° F r 38 5 " 38 1 r 38 4 r

38 3 Stac k Flowrat e dscfrn 4,69 8 5,09 9 5,24 8 5,01 5 Isokinetic s % 10 7 10 3 10 0 10

4 Tota l Chromiu m (Cr ) — LV M Quantit y Collected pg 12.1 6 2.7 9 9.1 8 r 8.0 4 Stac k Cone . @ 7 % 0 2 ug/m 3 8.1 6 1.7 4 5.9 8 5.2 9 | Stac k Emissio n Rate Ib/h r 1.00E-0 4 2.40E-0 5 8.10E-0 5 r 6.85E-0 5 i jj/se c 1.26E-0 5 3.02E-0 6 1.02E-0 5 " 8.63E-0 6 Cadmiu m (Cd ) - - SV M Quantit y Collected P

9 2.7 3 2.7 4 2.2 0 r 2.5 5 Stac k Cone . @ 7 % 0 2 ug/m 3 1.8 3 1.7 1 1.4 3 1.66 Stac k Emissio n Rate Ib/h r 2.25E-0 5 2.35E-0 5 1.94E-0 5 r 2.18E-0 5 j/se c 2.83E-0 6 2.96E-0 6 2.44E-0 6 " 2.75E-0 6 LeadfPb}- - SV M Quantit y Collected p

g 45. 6 13. 9 39. 0 r 32.8 4 Stac k Cone . @ 7 % 0 2 ug/m 3 30. 6 8. 7 25. 4 21. 6 Stac k Emissio n Rat

e Ib/h

r 3.76E-0 4 1.20E-04 3.45E-0 4 r 2.80E-0 4 g/se c 4.74E-0 5 1.5 1 E-0 5 4.34E-0 5 r 3.53E-0 5 Arseni c (As ) — Quantit y Collecte d pg 2.8 0 2.1 0 2.1 0 r 2.3 3 Stac k Cone . @ 7 % 0 2 ug/m 3 1.8 8 1.3 1 1.3 7 r 1.5 2 Stac k Emissio n Rate Ib/h r 2.3 1 E-0 5 1.8 1 E-0 5 1.85E-0 5 r 1.99E-0 5 g/se c 2.9 1 E-0 6 . 2.28E-0 6 2.34E-0 6 r 2.5 1 E-0 6 Beryllium

. (Be ) — Quantit y Collected pg 0.2 0 0.2 0 0.2 0 r 0.2 0 Stac k Cone . @ 7 % 0 2 pg/m 3 0.1 3 0.1 2 0.1 3 0.1 3 Stac k Emissio n Rate Ib/h r 1.65E-0 6 1.72E-0 6 1.77E-0 6 " 1.7 1 E-0 6 g/se c 2.08E-0 7 2.17E-0 7 2.22E-0 7 r 2.16E-0 7 j LV M Total = ...Ha / m 3 10. 2 3. 2 7. 5 6. 9 iSV M Tota

l = pg/m 3 32. 4 10. 4 26. 9 23. 2 f
C:\DOCUME-1\klarich.TWI\LOCALS-1\Temp\notesD3055 0 Weoli a Repor tUni t2 final.do

c 3- 6 Octobe r 200 8

# ENS R Tabl e 3- 6 Summar y o f HW C MAC T Metal s - Septembe r 8 , 200 8

Lo wVolatil e Metal s Emission s - ug/m 3 @ 7 % G 2 Metal s Ru n 

### 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 Total LV M 10. 2 3. 2 7. 5 6. 9

LV M Regulator

y Standard= 9 2 ug/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 30. 6 8. 7 25. 4 C d 1.8 3 1.7 1 1.4 3 Total SV M 32. 4 10. 4 26. 9 23. 2

SV M Regulator

y Standard= 23 0 ug/rn 3

C:\DOCUME-1\klarich.TWI\LOCALS-1\Temp\notesD3055 0 Weoli a Repor tUni t2 final.do

c 3- 7 Octobe r 200 8

# 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 Tim e Sto p Tim e Unit s 1 05-Aug-0 3 " 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 SamplingParameter

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

Temp . Stac k Flowrat e Isokinetic s in . H g de f dsc f % v/ v % dry ° F dscfr n % r29.2 3

r88.53 9 78.48 8 42. 3 11.9 9

r37 2 5,66 5 9 2 r29.6 5

" 87.45 2 84.25 8 43. 6 10.9 6

r37 7 5,71 9 9 8 r29.6 5 T85.94 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 Mercur y (Hg ) — Quantity Collecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e p g

ug/m 3 lb/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 j " 90. 4

57. 9 ' 8.36E-0 4 " 1.05E-0 4 Tota l Chromiu m (Cr ) - Quantity Collecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e LV M

M 9 ug/m 3 Ib/h r g/se c 37.5 0

26.2 2 3.58E-0 4 4.5 1 E-0 5 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

r 2.78E-0 4 ' 3.50E-0 5 Cadmiu m (Cd ) — Quantity Collecte d Stac k Cone
. @ 7% 0 2 Stac k Emissio n Rat e SV M

P S ug/m 3 Ib/h r g/se c 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 Lea d (Pb ) — Quantity Collecte 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 83. 5

58. 4 7.97E-0 4 1.00E-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 r89.1 8

r56. 9

r8.24E-0 4

r1.04E-0 4 Arseni c (As ) — Quantity Coliecte d

- Stac k Cone . @ 7 % 0 2 Stac k Emissio n Rat e p g

pg/m 3 Ib/h r g/se c 3.1 5

2.2 0 3.0 1 E-0 5 3.79E-0 6 3.7 5

2.1 9 3.37E-0 5 4.24E-0 6 1.9 4

1.2 7 1.80E-0 5 2.27E-0 6 r2.9 5

1.8 9

r 2.73E-0 5

r3.43E-0 6 Bervlliu m (Be ) — Quantity Collecte d Stac k Cone
. @ 7 % 0 2 Stac k Emissio n Rat e M

O ug/n f Ib/h r g/se c 0.2 0

0.1 4 1.9 1 E-0 6 2.41.E-0 7 0.2 0

0.1 2 1.80E-0 6 2.26E-0 7 0.2 0

0.1 3 1.86E-0 6 2.34E-0 7 r0.2 0

0.1 3

r 1.85E-0 6 " 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\klarich.TWI\LOCALS~1\Temp\notesD3055 0 Weoli a Repor tUni t3 draft.do

c 3- 2 Octobe r 200 8

# ENS R

Tabl e 3 -2 Summar y o f HW C MAC T Metal s 

### L o w Volatil e Metal s Emission s - [jg/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 y Standar d = 9 2 ug/m 3 

### Semi-Volatil e Meta l Emission s - jjg/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 0.5 3 0.4 1 Tota l SV M 58. 6 67. 1 46. 2 57. 3

SV M Regulator y Standar d = 23 0 pg/rrf * Mercur y Emission s -jjg/ 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 y Regulator y Standar d = 13 0 ug/m 3

C:\DOCUME-1\klarich.TWI\LOCAUS-1\Temp\notesD3055 0 Weoli a Repor tUni t3 draft.do

c 

### 3- 3 Octobe r 200 8

# UNIT 4 EMISSIO N RESULT S

# ENS R

Tabl e 3- 2 R M 2 9 Samplin g Parameter s an dEmissio n Rate s Run No . Dat e Star t Tim e Sto p Tim e Unit s 1

r 21-Aug-0 8

r 13:25

r 15:3 7 2

r 22-Aug-0 8

r 10:5 0

r 13:0 1 3

r 23-Aug-0 8

r 08:5 5 " 10:5 9 AVG S Samplin g Parameter

s - Barometri c Pressur e Volum e Metere d Sampl e Volume Moistur e 0 2a 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 dscfr n % r 29.5 4

r 90.93 8 89.02 3 39. 0

r 12.27

r 39 0 17,28 0 10 1 r

29.6 9

r 89.78 4 88.43 3 39.5 . r 12.1 3 " 38 8 17,25 5 10 0 r 29.6 4

r 91.42 0 89.26 4 40. 3

r 11.6 3

r 39 4 17,18 9 10 2 " 29.6 2 " 90.71 4 88.907 39. 6 12.0 1 " 39 1 17,24 1 10 1 Mercur y (Hg l — Quantit y Collecte d Stac k Cone . @ 7 % 0 2 Stac k Emissio n Rat

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

37. 9 1.53E-0 3 1.93E-0 4 38. 7 24. 4 9.99E-04 1.26E-0 4 42. 3 25. 0 1.08E-0 3 1.3 6 E-0 4 " 46. 9 29 . 1

r 1.20E-0 3

r 1.5 1 E-04 Tota l Chromiu

m (Cr) — Quantit y Collecte d Stac k Cone . @ 7 % 0 2 Stac k Emissio n Rat

e LV M p g ug/m 3 Ib/h r g/se c 3.1 2

1.9 8 8.0 1 E-0 5 1.0 1 E-0 5 8.2 8

3.9 6 1.62E-0 4 2.04E-0 5 6.4 0

3.7 8 1.63E-0 4 2.05E-0 5 r

5.27 3.2 4

r 1.35E-0 4

r 1.70E-05 Cadmiu m (Cd) — Quantit y Collecte d Stac k Cone . @ 7 % 0 2 Stac k Emissio n Rat

e SV M p g ug/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 " 1.1 2

0.6 9

r 2.87E-0 5 k 3.6 1 E-0 6 LeadtVb)- Quantit y Collecte 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 34. 3

21. 8 8.8 1 E-0 4 1.1 1 E-0 4 49. 1 30. 9 1.27E-0 3 1.60E-0 4 44. 5

26. 3 1.13E-0 3 1.4 3 E-0 4 " 42.6 3 26. 4

r 1.09E-0 3

r 1.38E-0 4 Arseni c (As) — Quantit 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 4.8 2

3.0 7 1.2 4 E-0 4 1.56E-0 5 9.8 2

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

9.5 9 4.13E-04 5.2 1 E-0 5 r

10.2 9 6.2 8

r 2.63E-0 4 " 3.32E-0 5 Berylliu m fBe ) - Quantit 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 0.20

0.1 3 5.13E-0 6 6.47E-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 B.42E-0 7 ' 0.2 0

0.1 2

r 5.13E-0 6 ' 6.46E-0 7 LV M Tota l = ...H9 / m 3 5. 2 10. 3 13. 5 9. 6 SV M Tota l = pg/m 3 22. 3 31. 7 27. 1 27 . 0 C:\DOCUME~1\klarich.TWI\LOCALS-1\Temp\notesD305S 0 3- 3 Octobe r 200 8 \-7902083.do

c

# ENS R Tabl e 3- 3 Summar y o f

HW C MAC T Metal s

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 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 Total LV M 5. 2 10. 3 13. 5 9. 6 LV M Regulator

y Standard= 9 2 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 Pb 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

y Standard= 23 0 ug/m 3 Mercur y Emission s -ug/m s @ 7 % 0 2 Ru n 1 Ru n 2 Ru n 3 Averag e 37. 9 24. 4 25. 0 29 . 1 Mercury Regulator

y Standar d = 13 0 ug/m 3

C:\DOCUME-1\klarich.TWI\LOCALS-1\Temp\notesD3055 0 W902083.do

c 3- 4 Octobe r 200 8

# SYSTE M REMOVA L EFFICIENC Y (SRE ) FO R UNITS 2 , 3 AN D 4200

8 Metal s Testin g Remova l Efficiencie s 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 Efficienc y (RE) 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 99.9997 9 3 99.9995 8 3 99.9989 3 Av g 99.9998 1 Av g 99.9994 0 Av g 99.9992 6

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 Efficienc y (RE) Em . Std. : 23 0 ug/dsc m 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 Av g 99.9987 3 Av g 99.9982 9 Unit2(Hg ) Remova l L

_Unit3(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 Efficienc y (RE) Em . Std. : 13 0 ug /dsc m Ru n Efficienc y (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 T Performanc 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 aoperate s 2 Fixe dHeart h Dua l Chambere dIncinerator s (Units 2 an d3 ) an done rotar y kil n incinerato

r (Uni t 4) a t the Sauget , I

L facility . Th e two fixe dheart h unit s ar

e rateda t 1 6 million Btu/h

r each . Incineration Uni t No . 3 i s amirro

r imag e o f Uni t No . 2 . Bot

h o f thes e unit s hav e thei

r ow n wast e handlin g system s a s describe di

n th e section s tha

t follow . Th e onl

y differenc e bein g Uni

t No . 2 i s equippe dwit

h four (4 ) baghous e modules , whil e Uni

t No . 3 i s equippe dwit

h thre e (3 ) baghous e modules . However , eac h incinerator i s operate didentically wit

h onl y three baghous e module s in servic e during 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 Fee d Syste m an d Blendin g Operation s Th e fixe dheart

h incinerator

i s designe dt

o receiv e containers , aqueou s liquidwastes , organi c liqui dwastes , specialt y liqui dfeeds , gase s an ddirect injec t liquid s fe dthroug

h th e aqueou s o

r organi c liqui dfee dsystems . Thes e unit s can receiv e an y combination o

f waste s - liquid , semi-solid , soli do r gase s - wit

h ahea t valu e o f u p t o 1 6 millio n Btu/hr . Uni t 2 i s supporte db

y storage/blen dtank s locate din Tan k Far m#1 . Rate s o

f fee dar e controlle da

t eac h incinerator . Segregate dliquidwaste s ar e store dunti

l utilize din th

e wast e blending facilities . A t

tha t time , liquid s ar e delivere dt

o the blending tank s wher e th e daily liqui dfee dt

o th e incinerato

r i s formulated , tested , an drelease dt

o th e incinerator . Blendin g o f store dliqui dwaste s t

o achiev e optimu

mheating 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 use dt o segregate different

wast e strea mtype s fo r

blendin g o

f liqui dfee dt

o th e incinerator . Severa l criteri a ar e importan

t in designin g ablendfro mavailabl e waste s tha t hav e been segregate dprincipally b y physica l an dchemical properties . Thes e includ e compatibility , prope

r rang e o f heatin g value , an dpermi

t restriction s regarding elementa

l compositio n (base don emissio n limitations) . Th e materia l i s transferre dthrough abovegroun dpipeline s fro mth e tan k far mt o th e incinerator . Pipeline s use dt o transfer liqui dorgani c wast

e an daqueou s waste ar

e equippe dwit

h strainers . I n complianc e wit

h th e Benzen e NESHAP , al l tank s ar e vente dt

o individua

l carbo n adsorptio n canister s fo r remova l of organic s before vapor

i s discharge dto the atmosphere . Eac h carbo n adsorbe r canister i s essentially equivalen

t t o a5 5 gallo n containe

r o r greater , i f necessary . Al l tank s ar

e equippe dwit

h conservatio n vents , in addition t o th e carbo n canister

adsorber . Al l tank s ar

e grounded , an dflam e arrestor s ar e installe dbetween th

e carbo n adsorber s an dthe tanks . 2.2.1. 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui dwast

e injector s use di

n th e combustio n chamber s are air-atomizing injectors . Thes e ar e use dfor injectio n of

high Btu , low Bt

u liquid s an dspecialt

y fee dliquids . Dua

l flui dinjectio n nozzle s wil l b e use dfo r atomizatio n ofth e waste . Eac h ofth e injector s i s rate da t 0-30 0 gph . Th e liqui dwast

e fee dnozzle s ar

e serve db y paralle l redundan

t pump s an drecirculatio n system s wit h back pressur e control .

Q:\mw97\Projects\10002022\Veoli a Performanc

e Tes tPla n U 2 Revise d 073008.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc e Tes t Pla n Pag e 2 o f 1 2 2.2.1. 2 Package dan dBul k Soli d Container s of

waste s are sample dan danalyze dafter receipt i n accordanc e wit

h th e facility' s Waste Analysi s Plan . Thes e waste s ca

n the n be delivere ddirectl

y t o Uni t 2 o r repacke dinto.small combustible container s a t th e facility . Fiberboar

do r plasti c container s (full

y o r partiall y ful l of waste) , u p t o 40-gallo n size , ma

y b e charge ddirectl

y t o th e primar y chamber . Thes e will b e receive da t the dock adjoinin g eac h fixe dheart h incinerator , an dcharge dt o th e incinerator

withi n 2 4 hour s o r returne dt

o permitte dstorage . Solids , usually package di n plasti c o

r fiberboardcontainers , ar e introduce dint

o th e incinerato

r throug h aPL C controlle dairlock-ra

msyste mlocate da

t th e lowe r fron t o f th e primar y chambe r o f th e incinerator . The airloc

k i s compose dof arefractory-line ddoor , adoo r int o the airlock

enclosure , an dtw

o pneumatic rams . The action of the feeder

i s a s follows :

• Wit h the incinerator

doo r closed , th

e airloc k doo r i s opened . • The firs t

pneumati c ra

m(loa dram ) pushe s weighe dcharge s o f waste int o th e airloc k chamber . • Th e airlock

door i s closed . • A switch i s activate deithe r automaticall

y o r manually , whic h open s the doo r t o th e incinerato

r an d actuate s th

e ra m(charg e ram

) tha t pushe s the wast

e int o the incinerator . The ra

mthe n retracts and th e incinerator

door closes . 2.2.1. 3 Specialt y Liqui dFeed s an dGase s Specialt y Fee dSystem s associate dwit h Incinerato

r No . 2 ar e a s follow s

• Specialt

y Feede r
• Compresse dGa s Cylinde r Fee dSyste m
• Direct

Injec t Liqui dFee dSyste 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 )(Hi){B) an d (C ) Incinerato r No . 2 feature s atwo-stag e combustio n process . Ignitio n o f waste materia

l take s plac e i

n th e primar y (lower ) combustio n chambe

r (PCC) . A secondar

y (upper ) combustio n chambe

r (SCC ) serve s a s a

n "after-burner " fo r

proces s gases . Ignitio

n ofth e waste take s plac e a t temperature s i

n exces s o

f 170 0 degree s F . Th e secondar y combustio n chambe

r maintain s aminimu

mtemperatur

e o f approximatel

y 180 0 degree s F . Th e fixe dheart

h incinerator

i s fabricate do

f carbo n steel . Th e primar y chamber

ha s a n externa l diamete r o f 9 fee t an di s 17. 5 fee t

long . Th e interio

r wall s o f th e chambe

r ar e line dwit

h approximatel

y 1 0 inche s o

f bric k refractor y an dinsulatio n backing , makin g th e interna l operating diamete

r approximatel

y 7'2" . Th e cross sectiona l are aofth e chambe

r i s thu s 40. 3 squar

e feet . Tabl e 2- 2 provide s asummar y ofth e incinerato

r desig n specifications . Liqui dandsoli dwast

e feed s ente

r th e lowe r chambe r o n th e front-fac e o

f th e chamber . The primar y burne r an dthe specialt

y fee dinjector

ar e locate dnea

r th e front-fac e ofth e chamber an dar e mounte dtangentially . Q:\mw97\Projecls\10002D22Weoli a Performanc

e Tes tPla n U 2 Revise d 07300B.do

cf

\ Revision : 1 Date : Jul y 200 8 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc e Tes t Pla n Section : 2. 0 Pag e 3 o f 1 2 The primar

y burne r i s aNort h America

n burne r rateda t 12. 0 millio n Btu/hr . andi s use din th e lowe r chambe r t o maintain permittedtemperatures . I t will bur n onl y natura l ga s o r No . 2 fue l oil . Th e burne r systemi s supplie dwit

h combustio n ai

r a t astati c pressure o

f 30 " wate r colum n (WC) . Th e pilo

t for th e primar y burne r wil l bu mnatura l gas . Th e fue l syste mfo r

th e lowe r chambe r (an dsecondar

y combustio n chamber

) i s controlle db

y aFactor

y Mutua l approve dburne

r managemen

t syste mcomplet

e wit h interlock s an dsafet

y valves . 2.3. 2 Secondar y Combustio n Chambe r Th e secondar

y combustio n chamber

(SCC) i s ahorizontal , cylindrica l chambe r tha t ha s a n externa l diamete r o f 9 fee t an di s 17. 5 fee t

long . Th e interio

r wall s o f th e chamber

ar e line dwit

h approximatel

y 1 0 inche s o

f bric k refractor y an dinsulatio n backing , makin g the interna l operatin g diamete

r approximatel

y 7'2" . Th e cross sectiona l are aof the chambe

r i s thu s 40. 3 squar

e feet . Followin g ignition o

f the wast e materia l unde r controlle do

r starved-air

condition s i

n th e lowe r chamber , off

gase s trave l throug

h arefractory-line dflu e ga s passag e int o the uppe

r chamber , which act s a s a n afterburner . Turbulenc e i s achieve db y the tangentia

l introduction of

air an dadditiona

l fue l i n th e uppe r chamber . Th e SC C i s equippe dwit h one burne

r mountedtangentiall

y o n the sid e ofth e chamber . Th e burne r i s aNort h America n burne r rate da t 6. 0 million Btu/h

r an di s fuele dwit

h natura l ga s o r fue l oil . A s wit h the primar

y chambe r burner , th e SC C burne

r i s supplie dwit

h atomizin g ai

r an di s equippe dwit

h a burne r managemen

t system . Thi s syste mcontrol s the ignition an dinitiate s an automati c shutof f whe n ther e i s alos s o f flame , combustio n ai

r supply , fue l pressure , atomizin g air pressure , o

r pilo t burner . Leaving the uppe

r chamber , th

e ho t ga s strea mtravel s through 2 8 fee t o f refractory-line dstack

section s befor

e reaching the star

t o f the ga s scrubbin g system . Th e combine dvolume o f th e uppe r an dlowe r chambers , th

e flu e ga s passag e an dthe ho t crossove r

sectio n i s approximately 1,56 7 cubi c feet . Th e tota

l retention tim

e o f combustio n gase s within th e syste mi s approximatel y 5 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) ] The thermocoupl e tha

t monitors temperatur

e in th e primar y combustio n chambe

r i s locate do

n to p ofth e chambe r abou t fiv e fee t fro mthe transition . Th e thermocoupl e tha t monitors temperatur

e i n the SC C i s locate d o n to p o f th e chamber

abov e the transition . 2.3. 4 Hazardou s Wast e Residenc e Tim e [4 0 CF R § 63.1207(f)(1)(ix) ] Th e Hazardou s waste ga s residenc e tim e fo r th e Fixe dHeart

h Incinerato

r i s calculate da s follows :

• Primar

y Combustio n Chambe r

Volume - 63 5 ft 3

• Secondar

y Combustio n Chamber

Volume - 63 5 ft3

. Tota l Volum e -127 0 ft 3

• MaximumFlu e Ga s Flowrat e -17,38 2 acf

m(29 0 ff/sec )

• Total Combustio n Zon e Residenc e Time = (127 0 ft3 )/(29 0 ff/sec ) = 4. 4 sec 

## ( Q:\mw97\Projects\10002022\Veoli a Performanc

e Tes tPla n U 2 Revise d 073008.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc e Tes t Pla n Pag e 4 o f 1 2 2.3. 5 Combustio n Syste m Lea k Combustio n syste mleak s ar e prevente dthrough maintainin g atotall y seale dcombustion chamber , couple d wit h th e us e o f a n induce ddraf

t fa n tha t maintain s avacuumof

normall y - 4 t o - 6 inche s o

f wate r colum n i n bot h combustio n chamber s whil e waste s ar

e bein g fe dt

o th e unit . 2.3. 6 Emergenc y Safet y Ven t The incinerator

i s equippe dwit

h a n emergenc y safet

y ven t (ESV ) locate da

t th e to p o f th e secondar

y combustio n chamber . Thi s ES V i s arefractory-line demergenc y therma l relief ven t (TRV) whic

h i s heldi n th e close dpositio n b

y apneumati c cylinder . Th e contro l valv e i n the lin e supplying air

t o the cylinde

r an dth e cylinde r ven t valv e whic h open s the TR V ar e locate di

n the control roo

mfo r eac h unit . Valv e lock s (wit h key s attached ) ar e utilize dt

o dete r indiscriminat

e operatio n of

thes e valves . Opening o f th e TR V allow s ho

t combustio n ga s t

o ven t fro mth e combustio n syste mduring emergenc y shutdown events . Th e purpos e ofth e TR V i s t o protect th e downstrea

mAPC S fro mexcessiv e temperatur e situations . A limi

t switc h on th e TR V shut s of f al l wast e feed s t o th e syste ma s i

t sense s tha

t the 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 [4 0 CF R §63.1207(f)(1)(viii) ] Equipmen

t malfunction s ar

e identifie db

y the contro l system , observatio n o f proces s control variables , o r b y regula r fiel dinspections . I n th e even t o f mino r equipmen

t malfunction s (e.g . waste fee do r scrubbe r leaks) , th

e control roo

moperato

r wil l be notified . Th e contro l roo moperator

will the n clos e th

e wast e fee dvalve s an ddisabl e th e wast e fee d pumps . I n the even

t o f major equipmen

t malfunction s (e.g . fire) , the emergenc y sto p butto n locate din th

e control roo

m wil l b e pushed . I

f thi s butto n i s pushed , al l equipment wil l switch t

o its 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 r pollutio n contro l systemconsist s o f aspray drye

r absorbe r andfabri c filte

r baghous e modules . Th e ai r pollution contro l syste mneutralize s acidi c compound s an dremove s particulat e fro mth e exhaus t gas . Tw o subsystems , the spra

y drye r absorbe r an dth e fabri c filter , carr

y ou t the chemica

l neutralizatio n an dparticulat e remova l functions , respectively . A thir dsubsystem , the lim

e system , i s use dt

o prepar e an dprovid

e lim e slurr y t o th e spra y drye r absorber for us e in the chemical neutralizatio n process . The induce ddraf t fa n an dstack provid e th e mechanical energy require dt o transpor

t th e flu e ga s throug

h th e interconnecting ductwork , t o it s eventua l discharg e poin

t t o atmosphere . 2.5.1. 1 Lim e Syste m Th e lim e syste mprepare s lim

e slurr y fo r us e i n th e chemical neutralizatio n proces s i n sufficient

supply an d concentratio n t

o maintai n continuou s flu e ga s treatment in th e spra

y drye r absorber . Th e syste mha s been designe dfo r

batc h mixin g t

o provide thi s service . Veoli autilize s hydrate dlim e a s its neutralizin g agen t in f th e ai r pollutio n contro l systems . Th e key neutralizatio n paramete r ofth e hydrate dlim

e i s the "Ca O Equivalent" . Figure 4- 1 i s th e specificatio n shee t

fo r th e hydrate dlim

e tha t Veoli auses . Veoli aha s use d thi s specifi c produc t

fo r ove r 2 0 year s an dplan s to continu e wit h it s use . Although , i

f Veoli adoe s chang e Q:\mw97\Projects\10002022\Veoli a Performanc

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r typ e o f lim e i n th e future , i

t woul dhav e a"Ca O Equivalent " specificatio n equa l to o r greate r tha n th e 72.6 % show n o n Figure 4-1 . Hydrate dlim

e i s store di n astorag e bi n abov e the lim

e preparation area . The storag e bi n i s size dt

o hold enough hydrate dlim

e t o maintai n several day s o

f systemoperation a

t th e maximu

mcombustio n rat

e o f th e incinerator . Lim

e i s discharge dthroug

h the conical storag e bi

n bottom . Th e flo w o

f th e materia l fro mth e bi n i s aide db y avibrating "live bottom, " o r bi n activator . A variabl e spee dscre w feeder i s use dt o mete r the hydratedlim

e i n th e proportion s require dfo r batch mixin

g lim e slurry . Th e lim

e i s mixedwit

h wate r in atan k beneat h the lim e storag e bin . The scre w feede r spee dan dth

e rat e tha t wate r i s adde dt

o the lim e slurr y tan k ar e variabl e s o tha

t the desire dlim

e solid s concentratio n ca

n b e achieve di

n th e tank . Th e variabl e fee d adjustment s allo w water

andlim e t o b e adde dt

o th e lim e slurr y tan k a t arat e tha t wil l allo w abatch mod

e o f mixing . A n agitator

i s provide din th e slurr

y tan k t o mi x th e wate r an dlim e an dt o maintai n the suspensio n o

f lim e solids . Th e mixe dlim

e slurr y i s pumpeda

t acontinuou s rat

e o f flow throug

h arecirculatio n loop t

o th e atomize r a t arat e o f u p to 1 0 gpm . 2.5.1. 2 Spra y Dr y Absorbe r Uni t 2 i s equippe dwit

h aSpra y Drye r Absorber

(SDA ) locate dimmediatel y downstrea

mo f th e secondar

y combustio n chamber . Th e SD A uni t i s fabricate do f

3/ 8 inch carbo n steel . Th e functio n o f th e SD A i s to :

• Furthe

r coo l the combustio n gase s fro m1600-2000oF t o 300-500oF , • Neutraliz e an dremov e HC I an dothe

r acid s fro mth

e combustio n gases , • Remov e aportio n o

f th e particulat

e (fl y ash ) fro mthes e gases . Slurr y flo w t o th e spra y drye r absorbe r (SDA ) i s metere db

y aflo w control valv e t

o obtain th

e prope r fee d concentratio n t

o the spra

y drye r absorber atomizer . Automati c (o

r manual) adjustmen

t t o the flo w i s mad

e a s afunctio n o

f the outpu t fro mahydrochlori c aci d(HCI ) analyzer

in th e ga s duct

downstrea

mo f the fabri c filter . Th e amoun

t of slurr y metere di s proportiona l t o the amoun

t o f HC I monitored . Th e slurr y passe s through astationar y swirl-typ e liqui ddistributo r int o the atomize

r wheel wher

e induce d centrifuga

l forc e fro mth e rapidl

y spinnin g whee l discharge s th e slurr y throug h th e wheel.nozzle s a

t hig h velocity . Th e desig n o

f the atomize

r wheel , its rat

e o f spin , andth

e discharg e velocit

y o f th e slurry , creat

e a clou do f finel y divide ddroplet s aroundth e peripher y ofth e atomize

r wheel . Coolin g wate

r i s als o passe d throug h th e atomize

r t o provide additiona

l ga s coolin g t

o the system . Th e wate

r flo w i s no

t metered , bu

t i s controlle db

y afeedbac k

signa l fro mth e atomize

r powe r transmitter . Thi s provide s verificatio n tha t wate r flo w t o th e atomize r increase s o

r decrease s in proportion t o th e spra y drye r absorbe r outle t temperature . Flu e ga s enter s fro mth e botto mo f th e spra y drye r absorbe r throug h avertical , centrall

y locate ddisperser . Th e disperser

direct s th e flu e ga s through th e zon e fille db y th e atomize dslurr

y clou dwher

e the flu e ga s an d slurr y mi x an dmos t

of th e absorptio n occurs . Th e gase s the n flo w downwar

dthroug h th e absorber

chambe r an dexi t throug h abotto msid e duct . A s th e gase s contac t

an dpas s throug

h th e clou do f atomize dlim

e slurry , the wate r i n the slurr

y evaporates , coolin g the gases . Simultaneously , th e lim e in the slurr

y react s wit

h th e hydroge n chloride in th e gase s t

o produc e calciu msalts . Some o f th e resulting dr

y material , consistin g o

f calciumsalts , fl y as h an dexces s lime , fall s t o th e conical botto

mo f th e unit . Th e dr

y materia l fro meac h uni

t i s discharge dt

o aconveyo r

syste mwhic h transport s i t t o adum p traile r o r equivalen

t typ e system .

Q:\mw97\Projects\10D02022\VeDli a Performanc

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performance Tes t Pla n Pag e 6 o f 1 2 2.5.1. 3 Fabri c Filte r Ga s exhauste d fro mthe spra y drye r absorbe r i s distributed b

y manifol dduct s t

o fou r fabri c filte

r modules . Th

e uni t i s operate dwit

h onl y thre e module s on-line wit h th e fourt h module off-lin e i

n astandby mode . Withi n eac h filte r module , the ga s i s passe d throug h Teflon-coate dfiberglas s clot h bags . The ga s passe s fro mth e outsid e t o th e inside o

f the filter bags . Particulat

e entraine di

n th e ga s strea

mi s mechanicall

y deposite do

n th e outsid e o f th e filte r bag s a s the ga s passe s throug h th e cloth . Eac h module ha s aclean air plenu mandhousing sectio n t

o contain approximatel

y 9 6 bags . Eac h ba

g i s approximatel

y 6 " i n diameter

b y 20 ' long . Th e baghouse s ar e fabricate dfro m3/16 " mil dstee l plate , o

f welded construction , ga s tigh

t an dstiffene dt

o withstandth

e maximu moperating negativ e pressure . Eac h compartmen

t ha s atub e sheet

tha t support s th

e bag s andprovide s for

to p bag/cag e removal . Acces s t o th e clea n ai r plenu mi s vi aasid e acces s doo r i n th e clea n ai r plenum . Th e fabri c filte

r cleanin g mechanis mutilize s jet s of ai r t o clea n th e filte r bags . Periodically , the cleanin g sequenc e will b e initiated . Th e sequenc e i s starte da t th e en do f a4 hou r timedcycle , whe

n th e differentia

l pressur e acros s the filter

reache s apredetermine dsetpoin t o f approximatel

y 7.0 " w.c , o

r whe n th e operato r initiate s acycle . Th e controlle r the n sequence s t

o each row o

f filte r bag s i n eac h module , releasin g aburs t o f ai r opposit e t o th e directio n o

f ga s flow . Th e quickl

y release dburst

o f ai r dislodge s dust

cak e on th e exterio r o f eac h ba g a s i t travel s fro mthe to

p t o th e botto mofth e bags . Release dfro mth e bag , th e dus t cak e fall s b y gravit y int o the hopper

a t the botto mofth e module . Fromther e i t i s discharge dt

o aconveyo

r systemwhic

h transport s i

t t o adum p trailer , o

r equivalen

t type system . Treate db

y th e spra y drye r absorber an dfiltere db

y th e fabri c filters, th

e cleane dflu e ga s exit s the fabri c filter module s t

o an outle

t manifol dfo r

exhaust . 2.5.1. 4 Induce dDraf t Fa n an dStac k Th e induce d draf

t fa n an d stac k

ar e locate ddownstrea

mo f th e fabri c filter . Combustion gase s ar e draw n throug h the syste mby a7 5 h

p induce ddraf

t (ID ) fan , rateda

t 15,00 0 acf

ma t 400 ° F saturated , an d22 " wate r colum n pressure . Th e induce ddraf t fa n provide s th

e mechanis mfo r

transporting th

e incinerato

r flu e ga s throug h th e spra y drye r absorber , fabri c filter , andal l interconnecting ducts . The I D fa n include s a

n inle t volum e contro l damper

to b e use dt

o contro l th

e velocit y o f th e ga s withi

n th e ductin g an dtreatmen

t devices . Treate dgase s ar

e exhauste dfro mthe induce ddraf t fa n t o th e atmospher

e throug h a90-ft . hig

h stack . Th e stack diamete r fo r Unit 2 i s 3 9 inche s I.D . Th e stack i s equippe dwit

h instrumen

t sampling ports anda samplin g platfor

mfo r emission s testing . Figur e 5- 1 provide s detail s o

n th e desig n andsampl e por t location s an dconfiguration s fo r

th e stack . 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 ) systemconsist s o f sampl e probes , sampl e deliver y and conditioning apparatus , an dga s analyzers . Sample s ar e extracte d fro mth

e sampling ports o n th

e stack . A CE M performanc e tes t

an dqualit

y assuranc e progra

mha s bee

n implementedi

n accordanc e wit

h th e Appendi x t o Subpar t

EE E o f Part 63

— Qualit

y Assuranc e Procedure s fo r Continuou s Emission s Monitor s Use dfo r

Hazardou s Wast e Combustors . Response s fro meac h CEM S will b e fe dt o th e Contro l Syste m(CS ) wher e the C O hourl

y rolling averag e i s calculate dan dinterlocke dt o the waste fee d cutof

f valve s a s par

t o f the Automati c Wast

e Fee d Cutof

f System
Q:\mw97\Projects\1[)D02022\Veoli a Performanc

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n Sectio n 2.8 , below . Th e followin g provide s abrie f descriptio n ofth e CEM S instrument s includin g th

e operating rang e an dmeasuremen t principal . 2.6. 1 CE M Syste m Descriptio n Th e Continuou s Emission s Monitoring System s (CEMS ) currentl y bein g utilize da

t Incinerato

r 2 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota

l hydrocarbon s an doxygen . Thes e monitors , excep t opacity , are extractiv e device s mountedi n samplin g port s o

n th e stack . Th e tabl e belo w summarize s th e analyzer specifications . Th e opacit

y monito r continuousl

y measure s the stack

ga s opacit

y an dreport s the measurement s t o a n indicator an darecorder . An opacit y tha t exceed s aprese

t limi t trigger s a

n alar man dinterlock . Carbo n monoxide an dhydroge n chloride ar

e monitoredwit

h extractiv e non-dispers e infrare danalyzers . Tota l hydrocarbo n i s monitore dwit h a n extractiv e flam e ion detecto r analyzer . Oxyge n i s monitoredwit h a zirconiu moxide cell . Stac k ga s flo w rat

e i s continuousl

y monitore dusin g a

n anuba r tha t send s a4-2 0 m

A signa l t o th e PL C which convert s the signal t

o 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 Monoxide Ecoche mMC 3 0-20 0 ppm v 0-3000 ppm

v Infrared Total hydrocarbon s Thermoelectro n 0-100 ppm v FID/lnfrare d Hydroge n chloride Ecoche mMC 3 0-1,000 ppm v Infrared Opacit y Teledyn e 0-100 % Whit e ligh t Stac k ga s flo w PSE/Rosemoun t 0-20,000 acf m Pressure dro

p 2. 7 Proces s Monitorin g an d Contro l Th e facilit

y i s equippe dwit

h astate-of-the-ar

t monitoring an dcontro l system , whic h facilitate s complianc e wit h permi t conditions , an dotherwise , collect s proces s control information , facilitate s efficient operation an ddetect s an dprevent s damag e t

o th e facility . Th e syste mconsist s o f thre e major

components :

• A human-machin e interfac e (HMI ) system , • Programmabl e logi c controller' s (PLC's) , an d

• A high spee detherne t cabl e connect s al l contro l syste mcomponent s Th e desire dcontro l function s ar e implemente dthroug

h th e HM I system . Al l digita

l contro l an demergenc y interlock s ar e accomplishe db y th e PLC . Th e contro l syste mi s capabl e o f monitoring the "operationa l envelope " o

f the incinerator

an di s capabl e o

f performin g anumbe

r o f activitie s including : Q:\mw97\Projects\100D2022\Veoli a Performanc

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• Contro l roo

mindicatio n o

f processo r

sensor s locate dwithi

n th e incinerator

system(such a s pressur e indicatio n o

f afiel dinstalle dpressur

e transmitter) ;
• Proces s controlle

r fo r singl e instrumen

t loop s o r an individua

l sub-system , suc h a s atemperatur e control loo

p involving asenso r

reading fro mone temperatur e transmitte

r affectin g th

e functio n o

f on e temperatur

e control valve ; an d

• Alar mfo r a n exceedanc e o

f adesignate dsetpoint , suc h a s ahig h pressur e o r lo w temperature . Th e proces s contro l compute r wil l continuousl

y contro l an dmonito

r th e operatio n ofth e incinerator . Whe n outof-rang e condition s exist , i t will notif y the operato

r o f thos e conditions . Th e proces s control compute r i s programme dt

o shut-down equipmen

t (i.e. , brin g th e syste mint

o asaf e mode) whe

n designate dparameter s ar e exceeded , whic h i s aprotective mechanis magains t potentia l equipmen

t damage , operation outside o f permi t limits , o r condition s tha

t migh t leadt o areleas e t

o th e environment . Continuou s monitorin

g ofth e incinerato

r an dscrubbe

r syste mi s an importan

t aspec t o f th e syste mdesign . A digita l readou t o f al l monitorin

g instrumentation i s displaye don th e main control screen . A n audibl e an dvisua l alar malert s th

e incinerator

operato r t o significan

t deviation s fro mnorma

l operating conditions . Thi s system allow s an immediat

e respons e t

o advers e condition s b

y the operator . Automati c wast e fee dcut-of

f an d incineratio n shutdown mechanism s ar e als o interlocke dwit

h th e monitoring systema

t o r prio r t o reachin g permi t limi t levels . Monitoring method s andcalibratio n frequencie s ar e liste di n Tabl e 2-3 . Th e Incinerato

r ha s a n independen

t proces s control compute r tha t interface s t

o th e Quantu mprogrammable controllers . Th e proces s compute r i s capabl e o

f controlling the incinerato r in cas e o f afailur e in aHM I server . Thi s compute

r run s aRSVIE W HM

I control softwar

e tha t provide s operator

interfac e t

o al l instrumentation and 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 incinerator

ha s an Automati c Waste Fee dCut-Of f (AWFCO ) Syste mtha

t wil l shu t wast e feed s of

f i n th e even t certain operating parameter s deviat e fro mallowabl e set

points . Th e PL C continuousl y monitors operatin g parameters , making adjustment s t o th e proces s a s neede dfo r

prope r control . Alar

mlogi c i s incorporate dint

o th e PL C syste mt

o automaticall

y initiat e a n AWFCO . Tabl e 2- 3 summarize s th e curren t AWFC O se

t points . AWFC O limits hav e been establishe dbase do n several factor s tha

t ar e summarize d below .

• Regulatory/permit

limits - establishe dt

o compl y wit h existin g permits . An exampl e o f thi s typ e o

f limi t i s th e lo w temperatur

e limit , belo w which wast

e canno t b e fe dunti

l the prope

r limi t i s re-established . I n addition , th e HW C MAC T regulation s requir e tha t the AWFC O systemb e interlocke dwit h the spa n of eac h proces s instrumen

t tha t i s par t ofth e Continuou s Monitoring System(CMS) . A listin g o f thes e CM S instrument s an dthei r interlocke dspa

n setpoint s i s maintaine da s par t o f Veolia' s Operatin g Record . • Proces s safet

y limits - establishe dt

o assure proces s equipmen t i s protectedan dunsaf

e operatin g condition s d o no

t occur . A n exampl e o

f thi s i s inadequat

e exces s air

i n th e combustio n chambe

r tha t ca n leadt o fue l rich conditions . • Utilit y o r Powe r failur e - establishe dt

o facilitat e acontrolle dshutdow n o f th e proces s during los s o

f proces s air, steam , wate

r o r electricity . An exampl e o f thi s i s th e los s o f instrumen

t air tha t i s necessar y fo r certain type s o

f proces s instrument s t

o functio n properly . Waste s wil l no t b e re introducedint

o th e incinerator s unti

l prope r operatio n o

f ke y instrument s i s re-established . Q:\mw97\Projeds\10002022Weoli a Performanc

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o the AWFC O system , operator s can manuall y shutdown wast

e feed s or

th e entir e proces s shoul d thi s b e needed . 2.8. 1 AWFC O Syste m Testin g Veoli atest s the AWFC O system s bi-weekly , a s weekly testin g wouldundul y interfer e wit h operation s b

y ceasin g an drestartin g waste feeds , potentiall y increasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s during th

e downtime , an dincreasin g operating costs . Testin g ofth e AWFC O systemi s atime-consumin g an dmanpowe r intensiv e process . Th e curren t testin g progra

mha s been i

n plac e unde

r th e RCR A permi

t fo r ove r 2 0 year s an dha s prove

n t o b e adequat

e i n detecting problems . Thi s rationale i s include di n the facility' s AWFC O Plan . I n some case s thi s testin g occur s mor e frequently depending o n ho w ofte n actua

l AWFCO s occur

a t th e unit . Pe r

th e require dfrequency , incinerator personne l check

th e functionalit

y o f AWFC O logi c tha

t i s par t o f the incinerator' s PL C syste mt o mak e sur e tha t shoul dproces s condition s deviat

e fro mallowabl e limits , th e compute

r logi c wil l initiat e waste fee dshutdown s a s required . Thi s i s accomplishe db

y manually simulating proces s condition s tha t ar e outside allowabl e limits andobserving an ddocumentin g whe

n th e contro l o

r block valv e softwar

e logi c o n the waste fee dline begin s t o initiat e valv e closure . Shoul dactual AWFCO s occu r during agiven testin g period , thes e ar e documente db

y operating personne l t

o satisf y regulator

y requirement s fo r

syste mtesting . Result s o f thi s testin g ar

e documentedo

n a separat e AWFC O Testin g Lo g an dmaintaine da 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 Onc e equipmen

t i s installe dan doperational , Veoli autilize s a n extensiv e preventativ e maintenanc e (PM ) progra mt o keep equipmen

t operationa

l an dpreven

t breakdown s an dfailures . Base dupo n th e type o f equipmen t an dhistorica

l operation s an dmaintenanc e experience , schedule s fo r variou s inspectio n an dPM activitie s ar

e followed . Thi s include s aspect s suc h a s documenting detaile dmaintenanc e historie s o n equipment , routin

e inspectio n an dlubrication program s fo r high wea r equipmen

t an dnon-destructiv e testing o f piping an dvessel s usin g technique s lik e ultrasoun dt

o asses s integrity . Th e frequenc y o f thes e activitie s varie s dependin g upon the equipment , P M activit y an dthe incinerator' s shutdow n schedule . Fo r example , frequent

(i.e. , weekly ) instrumen

t an dcertai n mechanica

l equipmen

t check s ar

e mad e fo r critica l proces s items . Lubrication , vibratio n analysi s an dothe r mechanica

l integrit y check s are.don e a

t longe r frequencie s lik

e monthl y o r quarterly . An dfinally , suc h item s a s inspectin g refractor y bric k fo r wear , ar e typically performe dwhe n th e entir e incinerator

i s shu t dow n fo r maintenance . 2.9. 2 Tes t Progra m Preparatio n Activitie s Prior t o testing , instrumentatio n associate dwit h key parameter s o

f th e tes t will b e checked , calibrated , o r replaced , a s appropriate , t o ensur e prope r operatio n ofth e instrumentatio n durin g testin g (i.e. , wast e fee d flowmeter s an dscales , CEM's , pressur e transmitters , thermocouples , stac k flowmeters , etc.) .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc e Tes t Pla n Pag e 1 0 o f 1 2 Tabl e 2- 2 Technica l Informatio n Summar y o n Incinerato r No . 2 Manufacture

r Trade Waste Incineration | Mode l No . TWI-2000 , Serie s 2 Typ e Fixe dHearth , Dua l Chambe r Dat e o f Manufacture 198 7 Dimension s Primary . Chambe r Secondary Chambe 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 Primary Chambe r Burne r Secondar y Chambe r Burne 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 Natural Ga s Natural Ga s Prime r Move r Induce dDraf t Fa n 15,00 0 acf

m@ 400° F saturated , 2 2 in . water colurn n

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e Tes tPla n U 2 Revise d 07300B.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc e Tes t Pla n Pag e 1 1 o f 1 2 Tabl e 2- 3 Curren t

AWFC O Parameter s an d Limit s fo r Incinerato r

No . 2 Syste m Devic e Unit s Cutof f Limit s Calibratio n

Frequenc y Tota l Pumpabl e Wast e Fee d rat e 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 y Hig h BT U Liqui d feedrat e Mas s flo w mete r lb/h r >2,01 2 Annuall y Lo w BT U Liqui d feedrat e Mas s flo w mete r Ib/h r > 1,99 3 Annuall y Specialt y feede r Scal e Ib/h r >72 4 Quarterl y Tota l LV M Feedrat e Mas s Flowmeters/Scale s Ib/h r > 1,26 4 (1 2 HRA ) Annually/quarterl y j Pumpabl e LV M Feedrat e Mas s flo w meter/Scale s lb/h r > 1,26 4 (1 2 HRA ) Annually/quarterl y j SV M Feedrat e Mas s Flowmeters/Scale s Ib/h r >3,477(1 2 HRA ) Annually/quarterl y Mercur y Feedrat e Mas s Flowmeters/Scale s Ib/h r > 0.007 3 (12HRA ) Annually/quarterl y 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 j Primary Combustio n Chambe rTemperatur e Typ e KThermocoupl e ° F <1,59 0 (one-minut e average ) <1,71 2 (HRA 1 ) £2,40 0 (instantaneous ) Annuall y I Secondar y Combustio n Chambe rTemperatur e Typ e KThermocoupl e ° F <1,79 4 (one-minut e average ) <1,84 5 (HRA 1 ) >2,40 0 (instantaneous ) Annuall y Primary Combustio n Chambe rpressur e Pressur e transmitte r in . w.c . >-0. 1 ( 5 secon d delay ) Quarterl y Secondar y Combustio n Chambe rpressur e Pressur e transmitte r in . w.c . > -0. 1 (5 secon d delay ) Quarterl y Chlorin e Fee d t o Slurry Flo w Rati o Flowmete r rati o > 33. 5 Annuall y Spra y Drye rAdsorbe rOutle t Temperatur e Typ e KThermocoupl e ° F >50 0 (on e minut e average ) >42 0 (HRA ) Annuall y Combustio n Ga s Flo w Rat e Pito t Tub 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 y Stac k carbo n monoxid e Infrare d ppm v >100 (HRA ) S50 0 (on e minut e average ) Quarterl y 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 Ligh t % >1 0 (on e minut e average ) Quarterl y Stac k hydroge n chloride 2 Infrare d ppm v >10 0 (HRA ) >50 0 (on e minut e average ) Quarterl y Fabri c filte rpressur e dro p Delt a P transmitte r in . w.c . £ 2 o r> 1 0 ( 1 min . 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 i s a RCR A permi t limi t only . Q:\mw97\Projects\1000202ZWeoli a Performanc

e Tes tPla n U 2 Revise d 073008.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 2 HW C MAC T Performanc 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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tPla n U 2 Revise d 073008.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 T Performanc e Tes t Pla n Pag e 1 of 1 2 

## 2. 0 Engineerin g Descriptio n

2. 1 Proces s Overvie w Veoli aoperate s 2 Fixe dHeart h Dua l Chambere dIncinerators (Units 2 an d3 ) an don e rotar y kiln incinerator (Uni t 4 ) a t the Sauget , I

L facility . Th e tw

o fixe dheart

h units ar

e rateda t 1 6 million Btu/h

r each . Incineration Uni t No . 3 i s amirro

r imag e o f Uni t No . 2 . Bot

h o f thes e units hav e thei

r ow n wast e handling system s a s describe di

n th e section s tha

t follow . Th e onl

y differenc e being Uni

t No . 2 i s equippe dwit

h four (4 ) baghous e modules , while Uni

t No . 3 i s equippe dwit

h three (3 ) baghous e modules . However , eac h incinerator i s operate didentically wit

h onl y three baghous e module s i n servic e during 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 3 Liqui d Wast e Fee d Syste m an d Blendin g Operation s Th e fixe dheart

h incinerato

r i s designe dt

o receiv e containers , aqueou s liquidwastes , organi c liqui dwastes , specialt y liqui dfeed s an ddirect

injec t liquid s fe dthrough the aqueou s o r organi c liquidfee dsystems . Thes e unit s can receiv e an

y combination of

waste s - liquid , semi-soli do r soli d- - wit

h ahea t valu e o f u p t o 1 6 million Btu/hr . Uni t 3 i s supporte db

y storage/blen dtank s locate din Tan k Far m#1 . Rate s o

f fee dar e controlle da

t eac h incinerator . Segregate dliquidwaste s ar e store dunti

l utilize din th

e wast e blending facilities . A t

tha t time , liquid s ar e delivere dt

o the blendin g tank s wher e the dail y liqui dfee dt

o the incinerato

r i s formulated , tested , an drelease dt

o th e incinerator . Blendin g o f store dliqui dwaste s t

o achiev e optimu

mheating 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 use dt o segregate differen

t wast e strea mtype s for

blendin g o

f liqui dfee dt

o th e incinerator . Several criteri a ar e importan

t i n designin g ablen dfro mavailabl e waste s tha t hav e been segregate d principall y b y physica l an dchemical properties . Thes e include compatibility , prope r rang e o f heating value , an dpermi t restriction s regardin g elementa

l compositio n (base do

n emissio n limitations) . Th e materia l i s transferre dthrough abovegroun dpipeline s fro mth e tan k far mt o th e incinerator . Pipeline s use dt o transfer liquidorgani c wast

e an daqueou s wast

e ar e equippe dwit

h strainers . I n complianc e wit

h the Benzen e NESHAP , al l tank s ar e vente dt

o individua

l carbo n adsorptio n canister s for remova l of organic s befor

e vapo r i s discharge dt

o th e atmosphere . Eac h carbo n adsorbe r canister i s essentiall y equivalen

t t o a5 5 gallo n containe

r o r greater , i f necessary . Al l tank s ar

e equippe dwit

h conservatio n vents , i n addition t o th e carbo n caniste

r adsorber . Al l tank s ar

e grounded , andflame arrestor s are installe dbetween th

e carbon adsorber s andth e tanks . 2.2.1. 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui dwaste injector s use di n th e combustio n chamber s ar e air-atomizing injectors . Thes e ar e use dfo r injectio n o f

high Btu , low Bt

u liquid s an dspecialt

y fee dliquids . Dua

l flui dinjectio n nozzle s will b e use dfo r atomizatio n of

the waste . Eac h o

f th e injector s i s rateda

t 0-30 0 gph . Th e liqui dwast

e fee dnozzle s ar

e serve db y paralle l redundan

t pump s an drecirculatio n system s wit h back pressur e control .

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e Tes tPla n U 3 07300 8 Revision.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 T Performanc e Tes t Pla n Pag e 2 of 1 2 2.2.1. 2 Package d an d Bul k Soli d Container s o f

waste s ar

e sample dandanalyze dafter receip t in accordanc e wit

h th e facility' s Wast

e Analysi s Plan . Thes e waste s ca

n the n b e delivere ddirectl

y t o Uni t 3 o r repacke dint

o smal l combustibl e container s a t the facility . Fiberboardo r plasti c container s (full

y o r partially ful l of

waste) , u

p t o 40-gallo n size , ma

y b e charge ddirectly t

o th e primar y chamber . Thes e wil

l be receive da

t the doc k adjoinin g eac h fixe dheart h incinerator , an dcharge dt o th e incinerato

r withi n 2 4 hour s or

returnedt

o permittedstorage . Solids , usuall y package di n plasti c o r fiberboar dcontainers , ar

e introduce dint

o th e incinerato

r throug h aPL C controlle dairlock-ra

msyste mlocate da

t th e lowe r fron t of the primar

y chambe r o f th e incinerator . Th e airlock i s compose dof arefractory-line ddoor , adoo r int o th e airloc k enclosure , an dtw

o pneumati c rams . Th e actio n o f th e feede r i s a s follows :

• Wit h th e incinerato

r doo r closed , th

e airlock doo r i s opened . • Th e firs t

pneumati c ra

m(loa dram ) pushe s weighe dcharge s of wast e int o th e airlock chamber . • Th e airloc k

doo r i s closed . • A switc h i s activate deithe r automaticall

y o r manually , whic h open s th e door t o the incinerato

r an d actuate s th

e ra m(charg e ram

) tha t pushe s th

e waste int

o th e incinerator . Th e ra

mthe n retracts an d th e incinerator

doo r closes . 2.2.1. 3 Specialt y Liqui d Feed s an d Gase s Specialt y Fee dSystem s associate dwit h Incinerato

r No . 3 ar e a s follow s

• Hoode dSpecialt

y Containe

r Feeder
• Glov e Bo x Emissio n Contro l System s
• Direc t

Inject Liqui dFee dSyste 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 r No . 3 feature s atwo-stag e combustio n process . Ignitio n o f waste materia

l take s plac e i

n th e primar y (lower ) combustio n chambe

r (PCC) . A secondar

y (upper ) combustio n chambe

r (SCC ) serve s a s a

n "after-burner " fo r

proces s gases . Ignitio

n o f th 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 y combustion chambe

r maintain s aminimu

mtemperatur

e o f approximatel

y 180 0 degree s F . Th e fixe dheart

h incinerator

i s fabricate do

f carbo n steel . Th e primar y chambe r ha s a n externa l diamete r o f 9 fee t an di s 17. 5 fee t

long . The interio

r wall s o f th e chambe

r ar e line dwit

h approximatel

y 1 0 inche s o

f bric k refractor y an dinsulatio n backing , making th e interna l operatin g diamete

r approximatel

y 7'2" . The cross sectiona l are aofth e chambe

r i s thu s 40. 3 squar

e feet . Tabl e 2- 2 provide s asummar y ofth e incinerato

r desig n specifications . Liqui dan dsoli dwast

e feed s ente

r the lowe r chambe r on th e front-fac e o

f th e chamber . Th e primar y burne r an dth e specialt y fee dinjecto

r ar e locate dnea

r the front-fac e ofth e chambe r an dar e mounte dtangentially .
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y burne r i s aNort h America

n burne r rateda t 12. 0 million Btu/hr . an di s use din th e lowe r chambe r t o maintai n permitte dtemperatures . I t wil l bur n onl y natura l ga s o r No . 2 fue l oil . Th e burne r systemi s supplie dwit

h combustio n ai

r a t astati c pressure o

f 30 " wate r colum n (WC) . Th e pilo

t fo r th e primar y burne r wil l bur n natura l gas . Th e fue l syste mfo r

th e lowe r chambe r (an dsecondar

y combustio n chamber

) i s controlle db

y aFactor

y Mutua l approve dburne

r managemen

t syste mcomplet

e wit h interlock s an dsafet

y valves . 2.3. 2 Secondar y Combustio n Chambe r Th e secondar

y combustio n chamber

(SCC ) i s ahorizontal , cylindrical chamber tha t ha s an externa

l diamete r o f 9 fee t an di s 17. 5 fee t

long . Th e interior

wall s o f th e chamber

ar e line dwit

h approximately 1 0 inche s o f brick refractor y andinsulatio n backing , makin g th e interna l operatin g diamete

r approximately 7'2" . Th e cross-sectiona l are ao f th e chamber

i s thu s 40. 3 square feet . Following ignitio n ofth e wast e materia l unde r controlle do

r starved-ai

r condition s i

n th e lowe r chamber , off

gase s travel through arefractory-line dflu e ga s passag e int o the uppe

r chamber , whic h act s a s a n afterburner . Turbulenc e i s achieve db y th e tangentia

l introduction of

ai r an dadditiona

l fue l in the uppe

r chamber . Th e SC C i s equippe dwit h on e burne r mountedtangentiall

y o n th e sid e o f th e chamber . Th e burne

r i s aNort h America n burne r rate da t 6. 0 million Btu/h

r an di s fuele dwit

h natura l ga s o r fue l oil . A s wit h th e primar y chambe r burner , the SC C burne

r i s supplie dwit

h atomizin g air

an di s equippe dwit

h a burne r managemen

t system . Thi s syste mcontrol s th e ignition an dinitiate s an automati c shutof f whe n ther e i s alos s of flame , combustio n ai

r supply , fue l pressure , atomizin g ai r pressure , o

r pilot burner . Leavin g th

e uppe r chamber , th

e ho t ga s strea mtravel s through 2 8 fee t o f refractory-line dstack

section s befor

e reaching the star

t of th e ga s scrubbin g system . Th e combine dvolum e o f th e uppe r an dlowe

r chambers , th

e flu e ga s passag e an dth

e ho t crossover

sectio n i s approximately 1,56 7 cubi c feet . Th e tota

l retention tim

e o f combustio n gase s within th e systemi s approximately 5 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 monitors temperatur

e in the primar

y combustio n chambe

r i s locate do

n to p ofth e chambe r abou t fiv e fee t fro mth e transition . Th e thermocoupl e tha t monitor s temperatur

e in the SC C i s locate d o n to p of th e chambe

r abov e th e transition . 2.3. 4 Hazardou s Wast e Residenc e Tim e [4 0 CF R §63.1207(f)( 1 )(ix) ] Th e Hazardou s waste ga s residenc e tim e fo r th e Fixe dHeart

h Incinerato

r i s calculate da s follows :

• Primar

y Combustio n Chamber

Volume-63 5 ft 3

• Secondar

y Combustio n Chambe

r Volum e - 63 5 ft 3

• Tota l Volume-127 0 ft 3

• MaximumFlu e Ga s Flowrat e -17,38 2 acf

m(29 0 ff/sec )

• Total Combustio n Zon e Residenc e Time = (127 0 ft 3 )/(29 0 fP /sec ) = 4. 4 se c

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e Tes tPla n U 3 07300 8 Revision.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 T Performanc e Tes t Pla n Pag e 4 o f 1 2 2.3. 5 Combustio n Syste m Lea k Combustio n syste mleak s ar e prevente dthrough maintaining atotall y seale dcombustion chamber , coupled wit h the us e o

f a n induce ddraf

t fan tha t maintain s avacuumo

f normall y - 4 t o - 6 inche s of

wate r colum n in bot h combustio n chamber s whil e waste s ar e being fe dt

o the unit . 2.3. 6 Emergenc y Safet y Ven t Th e incinerator

i s equippe dwit

h a n emergenc y safet

y ven t (ESV ) locate da

t th e to p o f th e secondar

y combustio n chamber . Thi s ES V i s arefractory-line demergenc y therma l relie f ven t (TRV ) whic h i s heldi

n th e close dpositio n b

y apneumatic cylinder . Th e contro l valv e i n th e lin e supplying air

t o th e cylinde r andth e cylinde r ven t valv e which open s th

e TR V ar e locate di

n th e contro l roo

mfo r eac h unit . Valv e lock s (wit h key s attached) ar

e utilize dt

o dete r indiscriminat

e operatio n of

thes e valves . Opening o f the TR V allow s ho

t combustio n ga s t

o ven t fro mth e combustio n syste mduring emergenc y shutdow n events . Th e purpos e o f th e TR V i s t o protect th e downstrea

mAPC S fro mexcessiv e temperatur e situations . A limi

t switch on th

e TR V shut s of f ai l waste feed s t

o the syste ma s i

t 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 [4 0 CF R §63.1207(f)(1)(viii) ] Equipmen

t malfunction s ar

e identifie db

y the contro l system , observatio n o f proces s contro l variables , o r b y regula r fiel dinspections . I n th e even t o f mino r equipmen

t malfunction s (e.g . waste fee do r scrubber leaks) , th

e contro l roo

moperato

r will be notifie db

y radio . The contro l roomoperator will the n disabl e the wast

e fee dpump s an dclos e th e wast e fee dvalves . I n th e even t o f major equipmen

t malfunction s (e.g . fire) , the emergenc y sto p butto n locate di n th

e control roo

m wil l b e pushed . I

f thi s butto n i s pushed , al l equipmen t will switch 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 r pollution contro l systemconsist s o f aspra y drye r absorber an dfabri c filte

r baghouse . The ai

r pollutio n contro l syste mneutralize s acidi c compound s andremove s particulat e fro mth e exhaus t

gas . Tw o subsystems , the spra

y drye r absorber an dth e fabri c filter , carr y ou t the chemica

l neutralizatio n andparticulat e remova l functions , respectively . A thir dsubsystem , the lim

e system , i s use dt

o prepar e an dprovid

e lim e slurr y t o th e spra y drye r absorbe r fo r us e in th e chemical neutralizatio n process . Th e induce ddraf t fa n andstac

k provid e the mechanica

l energy require dt

o transpor

t the flu e ga s throug

h the interconnecting ductwork, t o its eventua l discharg e poin

t t o atmosphere . 2.5.1. 1 Lim e Syste m Th e lim e syste mprepare s lim

e slurr y fo r us e in the chemica

l neutralizatio n proces s i

n sufficien t

suppl y an d concentratio n t

o maintai n continuou s flu e ga s treatmen t in the spra

y drye r absorber . Th e syste mha s bee n designe dfo r

batc h mixin

g t o provid e thi s service . Veoli autilize s hydrate dlim e a s its neutralizing agen

t in f th e air pollution contro l systems . Th e key neutralizatio n paramete r of th e hydratedlim

e i s the "Ca O Equivalent" . Figur e 4-1 i s th e specificatio n shee t fo r the hydrate dlim

e tha t Veoli auses . Veoli aha s use dthi s specifi c Q:\mw97\Projects\10002022Weoli a Performanc

e Tes tPla n U 3 07300 8 Revision.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 T Performanc e Tes t Pla n Pag e 5 o f 1 2 product fo r ove r 20 year s andplan s t

o continu e wit

h it s use . Although , i

f Veoli adoe s chang e supplier s o r type o f lim e in the future , i

t woul dhav e a"Ca O Equivalent ' specificatio n equa l t o o r greate r tha n th e 72.6 % show

n o n Figur e 4-1 . Hydrate dlim

e i s store din astorag e bin abov e the lim e preparatio n area . The storag e bin i s size dt o hol d enoug h hydrate dlim

e t o maintai n several day s o

f syste moperatio n a

t th e maximu mcombustio n rat

e o f th e incinerator . Lim

e i s discharge dthroug

h the conical storag e bi

n bottom . Th e flo w o

f the materia

l fro mth e bi n i s aide db y avibrating "live bottom, " o r bi n activator . A variabl e spee dscre w feeder i s use dt o mete r th e hydrate dlim

e i n th e proportion s require dfo r batch mixing lim

e slurry . Th e lim

e i s mixe dwit

h wate r in atan k beneat h th e lim e storag e bin . Th e scre w feede r spee dan dth e rat

e tha t wate r i s adde dt

o the lim e slurr y tan k ar e variabl e s o tha

t th e desire dlim

e solid s concentratio n can b e achieve di n the tank . Th e variabl e fee d adjustment s allo w wate

r andlim e to b e adde dt

o the lim e slurr y tan k a t arat e tha t will allo w abatch mod

e o f mixing . A n agitator

i s provide din the slurr

y tan k t o mi x th e wate

r an dlim e andt o maintain th

e suspensio n o

f lim e solids . Th e mixe dlim

e slurr y i s pumpe da

t acontinuou s rat

e o f flo w throug

h arecirculatio n loo

p t o th e atomize r a t arat e of u p t o 1 0 gpm . 2.5.1. 2 Spra y Dry Absorbe r Uni t 3 i s equippe dwit

h aSpra y Drye r Absorber

(SDA ) locate dimmediatel y downstrea

mofth e secondar

y combustio n chamber . Th e SD A uni t i s fabricate dof

3/ 8 inch carbo n steel . Th e functio n o f th e SD A i s to :

• Furthe

r coo l th e combustio n gase s fro m1600-2000oF t o 300-500oF , • Neutraliz e an dremove HC I an dothe r acid s fro mth

e combustio n gases , • Remov e aportio

n o f th e particulat

e (fl y ash ) fro mthes e gases . Slurr y flo w t o th e spra

y drye r absorber (SDA ) i s metere db

y aflo w contro l valv e t

o obtain the prope

r fee d concentratio n t

o th e spra y drye r absorber atomizer . Automati c (o

r manual) adjustmen

t to the flo w i s mad

e a s afunctio n of

th e outpu t fro mahydrochlori c aci d(HCI ) analyzer

in th e ga s duct

downstrea

mo f the fabri c filter . Th e amoun

t of slurr y meteredi s proportiona

l t o the amoun

t of HCI monitored . Th e slurr y passe s throug

h astationar

y swirl-typ e liqui ddistributo r int o th e atomize r whee l wher

e induce d centrifuga

l forc e fro mth e rapidl

y spinnin g whee l discharge s the slurr y throug h th e whee l nozzle s a

t hig h velocity . Th e desig n ofth e atomize r wheel , its rat

e o f spin , an dthe discharg e velocit y of th e slurry , creat

e a clou do f finel y divide ddroplet s aroun dthe peripher y o f th e atomize

r wheel . Coolin g wate

r i s als o passe d throug h th e atomizer

t o provid e additiona

l ga s coolin g t

o the system . Th e wate

r flo w i s not

metered , bu

t i s controlle db

y afeedbac k

signa l fro mthe atomize

r powe r transmitter . Thi s provide s verificatio n tha t wate r flo w t o the atomize

r increase s d

r decrease s i

n proportion t

o th e spra y drye r absorbe r outle t temperature . Flu e ga s enter s fro mthe botto mo f th e spra y drye r absorbe r through avertical , centrally locate ddisperser . Th e disperser

direct s the flu e ga s through the zon e fille db y th e atomize dslurr

y clou dwhere the flu e ga s an d slurr y mi x an dmos t

o f th e absorptio n occurs . Th e gase s then flo w downwar dthroug h th e absorber

chambe r an dexi t through abottomsid e duct . A s th e gase s contac t

an dpas s throug

h th e clou dof

atomize dlim

e slurry , th e wate r i n the slurr

y evaporates , coolin g th

e gases . Simultaneously , th e lim e i n the slurr

y react s wit

h th e hydroge n chloride in th

e gase s t o produc e calciu msalts . Som e of th e resulting dr

y material , consistin g o

f calciumsalts , fl y as h an dexces s lime , fall s t o th e conica

l bottomofth e unit . Th

e dr y materia l fro meac h uni

t i s discharge dt

o aconveyo r

systemwhic h transport s i t t o adum p traile r o r equivalen

t typ e system .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC T Performanc e Tes t Pla n Pag e 6 o f 1 2 2.5.1. 3 Fabri c Filte r Ga s exhauste dfro mth

e spra y drye r absorber i s distributedb

y manifoldduct s t

o three fabri c filte

r modules . Within eac h filte

r module , th

e ga s i s passe dthroug

h Teflon-coate dfiberglas s clot h bags . The ga s passe s fro m th e outsid e t

o th e inside ofth e filte

r bags . Particulate , entrainedi n th e ga s stream , i s mechanicall y deposite d on th e outside o

f th e filte r bag s a s the ga s passe s throug h th e cloth . Eac h modul e ha s aclea

n ai r plenu man dhousin g sectio n t

o contain approximatel

y 9 6 bags . Eac h ba

g i s approximately 6 " i

n diamete r b y 20 ' long . Th e baghouse s ar e fabricate dfro m3/16 " mil dsteel plate , o

f welded construction , ga s tigh

t andstiffene dt

o withstan dth

e maximu moperating negativ e pressure . Eac h compartmen

t ha s atub e sheet

tha t support s th

e bag s andprovide s fo r

to p bag/cag e removal . Acces s t o th e clea n air plenu mi s vi aaside acces s door in th e clea n ai r plenum . Th e fabri c filte

r cleanin g mechanis mutilize s jet s o f ai r t o clea n th e filte r bags . Periodically , th

e cleanin g sequenc e will b e initiated . Th e sequenc e i s eithe r starte d a t th e endo f atime dcycle , o

r whe n th e differentia

l pressure acros s the filte

r reache s apredetermine dsetpoin t o f approximatel

y 7.0 " w.c , o

r whe n th e operato r initiate s acycle . Th e controlle r the n sequence s t

o eac h ro w o f filte r bag s in eac h module , releasing aburst o f ai r opposit e t o the directio n o

f ga s flow . Th e quickl

y release dburst

o f air dislodge s dust

cak e o n th e exterio r o f eac h bag a s i

t travel s fro mth

e to p t o the botto

mo f the bags . Release dfro mthe bag , th e dust cak e fall s b y gravit y int o th e hoppe

r a t th e botto mo f the module . Fromther

e i t i s discharge dt

o aconveyo

r syste mwhic h transport s i

t t o adum p trailer , o

r equivalen

t typ e system . Treate db y the spra y drye r absorbe r an dfiltere db

y th e fabri c filter , th

e cleane dflu e ga s exit s th e Fabri c filte

r module s t o a n outle t manifol dfor

exhaust . 2.5.1. 4 Induce d Draf t Fa n an d Stac k Th e induce ddraf

t fa n an dstack

ar e locate ddownstrea

mofth e fabri c filter . Combustio n gase s ar e draw n through th

e syste mb

y a7 5 h p induce ddraf

t (ID ) fan , rateda

t 15,000 acf

ma t 400 ° F saturated , and22 " wate r colum n pressure . Th e induce ddraf t fa n provide s th

e mechanis mfo r

transporting th

e incinerato

r flu e ga s through th

e spra y drye r absorber , Fabri c filter , an dal l interconnecting ducts . Th e I D fa n include s a

n inle t volum e control dampe

r t o be use dt

o contro l the velocit

y ofth e ga s withi

n the ducting an dtreatmen t devices . Treate dgasse s exhauste dfro mthe induce ddraf t fa n t o th e atmospher

e through a90-ft . hig

h stack . Th e stac k diamete r i s 3 9 inche s I.D . Th e stac k i s equippe dwit

h instrumen

t samplin g ports an dasampling platfor m for emission s testing . Figur e 5- 1 provide s detail s on th e desig n andsampl e por

t location s an

dconfigurations . 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 ) systemconsist s o f sampl e probes , sampl e deliver y and conditioning apparatus , an dga s analyzers . Sample s ar e extractedfro mth

e transitio n ductin

g locate dbetwee

n th e scrubber

andstack . A CE M performanc e tes t an dqualit

y assuranc e progra

mha s bee

n implementedi

n accordanc e wit

h the Appendi x t o Subpar t EE E o f Par t 63—Qualit

y Assuranc e Procedure s fo r Continuou s Emission s Monitor s Use d fo r Hazardou s Wast e Combustors . Response s fro meac h CEM S will b e fe dt o th e Contro l Syste

m(CS ) wher

e th e C O hourl

y rollin g averag e i s calculate dan dinterlocke dt o the waste fee dcutof

f valve s a s par

t o f the Automati c Wast

e Fee dCutof

f System (AWFCO ) discusse din Sectio n 2.8 , below . Th e followin g provide s abrie f descriptio n o

f th e CEM S instrument s including th

e operatin g rang e an dmeasuremen t principal .

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t Incinerato

r 3 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota

l hydrocarbon s an doxygen . Thes e monitors , excep t opacity , ar e extractiv e device s mountedi n samplin g ports on the stack . Th e tabl e belo w summarize s th e analyzer specifications . Th e opacit

y monito r continuousl

y measure s the stac k

ga s opacit

y an dreport s the measurement s t o an indicato r an darecorder . A

n opacit y tha t exceed s aprese

t limi t trigger s a n alar man dinterlock . Carbo n monoxide an dhydroge n chloride ar

e monitore dwit

h extractiv e non-dispers e infrare danalyzers . Tota l hydrocarbo n i s monitore dwit h a n extractiv e flam e ion detecto r analyzer . Oxygen i s monitoredwit h a zirconiu moxide cell . Stac k ga s flo w rat

e i s continuousl

y monitoredusin g an anuba r tha t send s a4-2 0 m

A signa l t o the PL C whic

h convert s th e signal 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 Oxyge n COS A 0-25 % Electrochemica l Carbo n Monoxide Ecoche mMC 3 0-200 ppm v 0-3000 ppm

v Infrared Total hydrocarbon s Thermoelectro n 0-100 ppm v FID/lnfrare d Hydrogen chloride Ecoche mMC 3 0-1,000 ppm v Infrare d Opacit y Teledyn e 0-100 % Whit e ligh t Stac k ga s flo w PSE/Rosemoun t 0-20,000 acf m Pressur e dro

p

2. 7 Proces s Monitorin g an d Contro l Th e facilit y i s equippe dwit

h astate-of-the-ar

t monitoring an dcontro l system , which facilitate s complianc e wit h permi t conditions , an dotherwise , collect s proces s contro l information , facilitate s efficient operatio n an ddetect s an dprevent s damag e t

o th e facility . Th e syste mconsist s o f thre e major

components :

• A human-machin e interfac e (HMI ) system , • Programmabl e logi c controller' s (PLC's) , an d 2.7.1. 1 A hig h spee d ethernet cabl e connect s al l contro l syste m component s Th e desire dcontro l function s ar e implemente dthrough the HM I system . Al l digita

l contro l an demergenc y interlock s ar

e accomplishe db

y th e PLC . Th e contro l syste mi s capabl e of monitoring the "operationa l envelope " ofth e incinerator an di s capabl e o

f performing anumbe

r o f activitie s including :

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC T Performanc e Tes t Pla n Pag e 8 o f 1 2

• Contro l roo

mindication o

f processo r

sensor s locate dwithi

n th e incinerato

r system(suc h a s pressur e indicatio n o

f afiel dinstalle dpressur

e transmitter) ;
• Proces s controlle

r fo r singl e instrumen

t loop s o r a n individua

l sub-system , suc h a s apressur e control loo p involvin g asensor

reading fro mon

e pressur e transmitte

r affectin g th

e functio n o

f one pressur

e control valve ; and

• Alar mfo r a n exceedanc e o

f adesignate dsetpoint , suc h a s ahig h pressur e o r lo w temperature . Th e proces s contro l compute r will continuously control an dmonito r th e operation o

f th e incinerator . Whe

n out-of-rang e condition s exist , i t wil l notif y th e operato r o f thos e conditions . Th e proces s control compute r i s programmedt

o shut-dow

n equipmen

t (i.e. , brin g th e systemint

o asaf e mode ) whe n designate dparameters ar e exceeded , whic h i s aprotective mechanis magains t potentia l equipmen

t damage , operatio n outsid e o f permi t limits , or condition s tha

t migh t leadt o areleas e t

o th e environment . Continuou s monitoring ofth e incinerato r an dscrubbe

r syste mi s a

n importan

t aspec t ofth e syste mdesign . A digita l readou t o f al l monitorin

g instrumentation i s displaye don the main control screen . A n audibl e an dvisua l alar malert s the incinerato

r operato r t o significan

t deviation s fro mnorma

l operating conditions . Thi s syste m allow s a n immediat

e respons e t

o advers e condition s b

y th e operator . Automati c wast e fee dcut-of

f an d incineratio n shutdown mechanism s ar e als o interlockedwit

h the monitorin

g systema

t o r prio r t o reaching permi t limi t levels . Monitoring method s an dcalibratio n frequencie s ar e listedi n Tabl e 2-3 . Th e Incinerato

r ha s an independen

t proces s control compute r tha t interface s t

o th e Quantu mProgammabl e controllers . Th e proces s compute r i s capabl e o

f controlling the incinerator i n cas e o f afailur e i n acomputer . Thi s compute

r run s aRSVIE W HM

I contro l softwar

e tha t provide s operato

r interfac e t

o al l instrumentation and 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

r ha s an Automati c Waste Fee dCut-Of f (AWFCO ) Syste mtha

t wil l shu t wast e feed s of

f i n th e even t certain operatin g parameters deviat e fro mallowabl e se t

points . Th e PL C continuousl y monitors operating parameters , makin g adjustment s t

o th e proces s a s neede dfo r

prope r control . Alar

mlogi c i s incorporate dint

o th e PL C systemt

o automaticall

y initiat e a n AWFCO . Tabl e 2- 3 summarize s the curren t AWFC O se

t points . AWFC O limit

s hav e been establishe dbase do n severa l factor s tha

t ar e summarize d below .

• Regulatory/permit

limits - establishe dt

o compl y wit h existin g permits . A n example o f thi s typ e o

f limi t i s th e lo w temperatur

e limit , belo w which wast

e can no t b e fe dunti

l th e prope r limi t i s re-established . I n addition , th e HWC MAC T regulation s requir e tha t th e AWFC O systemb e interlockedwit h th e spa n o f eac h proces s instrumen

t tha t i s par t ofth e Continuou s Monitoring System(CMS) . A listing o f thes e CM S instrument s andthei r interlocke dspa

n setpoint s i s maintaineda s par t o f Veolia' s Operating Record . • Proces s safet

y limits - establishe dt

o assure proces s equipmen t i s protectedan dunsaf

e operating condition s do no

t occur . A n exampl e o

f thi s i s inadequat

e exces s ai

r in th e combustio n chambe

r tha t ca n lea dt o fue l ric h conditions . • Utilit y o r Powe r failur e - establishe dt

o facilitat e acontrolle dshutdow

n o f th e proces s during los s o

f proces s air , steam

y wate r o r electricity . A n exampl e of thi s i s th e los s o f instrumen

t ai r tha t i s necessar y fo r certain type s proces s instrument s t o functio n properly . Waste s will no t b e re-introduced int o the incinerator s unti

l prope r operation o

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o th e AWFC O system , operator s ca n manuall y shutdow n waste feed s o r the entir e proces s shoul d thi s b e needed . 2.8. 1 AWFC O Syste m Testin g Veoli atest s th e AWFC O system s bi-weekly , a s weekly testin g woul dundul y interfer e wit h operation s b

y ceasin g an drestartin g wast e feeds , potentiall

y increasin g emissions , incurring excessiv e downtime , burnin g additiona l natura l ga s during th

e downtime , an dincreasin g operatin g costs . Testin g o f the AWFC O syste

mi s atime-consumin g an dmanpowe r intensiv e process . Th e curren t testin g progra

mha s been i

n plac e unde

r th e RCR A permi

t fo r ove r 2 0 year s an dha s proven t o be adequat

e i n detectin g problems . Thi s rational e i s include di n th e facility' s AWFC O Plan . I n some case s thi s testin g occur s mor e frequently dependin g on ho w ofte n actua

l AWFCO s occur

a t th e unit . Pe r

the require dfrequency , incinerator personnel chec k

the functionalit

y of AWFC O logi c tha

t i s par t of th e incinerator' s PL C syste mt o mak e sur e tha t shoul dproces s condition s deviate fro mallowabl e limits , the compute r logi c will initiat

e wast e fee dshutdown s a s required . Thi s i s accomplishe db

y manuall y simulatin g proces s condition s tha t ar e outside allowabl e limits an dobserving an ddocumentin g when th e control o

r bloc k valv e softwar

e logi c o n the wast

e fee dlin e begin s t o initiat e valv e closure . Shoul dactua

l AWFCO s occur

during agiven testin g period , thes e ar e documente db

y operating personne l t

o satisf y regulator

y requirement s fo r

syste mtesting . Result s o f thi s testin g ar

e documente do

n a separate AWFC O Testin g Lo g an dmaintaine da s par t o f the 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 Onc e equipmen

t i s installe dan doperational , Veoli autilize s a n extensiv e preventativ e maintenanc e (PM ) progra mt o kee p equipmen

t operationa

l an dpreven

t breakdown s an dfailures . Base dupo n the typ e o

f equipmen t an dhistorica

l operation s an dmaintenanc e experience , schedule s fo r variou s inspectio n an dP M activitie s ar

e followed . Thi s include s aspect s suc h a s documentin g detaile dmaintenanc e historie s on equipment , routine inspectio n an dlubricatio n program s for hig h wea r equipmen

t an dnon-destructiv e testin g of piping an dvessel s usin g technique s lik e ultrasoun dt

o asses s integrity . Th e frequenc y o f thes e activitie s varie s dependin g upon th e equipment , P M activit

y an dth e incinerator' s shutdown schedule . Fo r example , frequent

(i.e. , weekly ) instrumen

t andcertain mechanical equipmen t check s ar

e mad e for critica l proces s items . Lubrication , vibration analysi s an dothe r mechanical integrit

y check s ar

e done a t longe r frequencie s lik

e monthl y o r quarterly . An dfinally , suc h item s a s inspectin g refractor y bric k fo r wear , ar e typically performe dwhe n th e entir e incinerator

i s shu t dow n fo r maintenance . 2.9. 2 Tes t Progra m Preparatio n Activitie s Prio r t o testing , instrumentation associate dwit h ke y parameter s o

f the tes t will b e checked , calibrated , o r replaced , a s appropriate , t o ensur e prope r operatio n ofth e instrumentatio n during testin g (i.e. , wast e fee d flowmeter s an dscales , CEM's , pressure transmitters , thermocouples , stac k flowmeters , etc.) .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC T Performanc e Tes t Pla n Pag e 1 0 o f 1 2 Tabl e 2- 2 Technica l Informatio n Summar y o n Incinerato r No . 3 j Manufacture

r Trade Waste Incineratio n I Model No . TWI-2000 , Serie s 2

Typ e Fixe dHearth , Dua l Chambe r Dat e o f Manufactur

e 198 8 Dimension s Primary Chambe r Secondary Chambe r External Lengt

h 17.5 ' 17.5 ' j Externa l Diameter 9 ' 9 ' j Interna

l Diamete r 7'2 " 7'2 " j Cross-sectiona l are a 40. 3 squar e fee t 40. 3 squar e fee t J Burner s Primar y Chambe r

Burne r Secondary Chambe r Burne 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/hr Fue l Natural Ga s Natura l Ga s | Prime r

Move r Induce dDraf t Fa n 15,00 0 acf

m@ 400° F saturated , 2 2 in . wate r colum n

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Tabl e 2- 3 Curren t

AWFC O Parameter s an dLimit s fo r Incinerato r

No . 3 Syste m Devic e Unit s Cutof f Limit s Calibratio n

Frequenc y Tota l Pumpabl e Wast e Fee drat e Mas s Flowmeters/Scale s Lb/h r > 3,12 3 (HRA ) Annually Tota l Waste Feedrate Mas s Flowmeters/Scale s Lb/h r >4,30 1 Annually/quarterl y Hig h BT U Liqui dfeedrat e Mas s flo w mete r Ib/h

r >2,01 2 Annually Lo w BT U Liqui dfeedrate Mas s flo w mete r Ib/h

r > 1,99 3 Annuall y Specialt y feede r Scal e Ib/h r >724 Quarterl y Tota l LV M Feedrate Mas s Flowmeters/Scale s Ib/h r > 1,26

4 (1 2 HRA ) Annually/quarterl y Pumpabl e LV M Feedrate Mas s Flowmeters/Scale s Ib/h r > 1,26

4 (1 2 HRA ) Annually/quarterl y SV M Feedrate Mas s Flowmeters/Scale s Ib/h r >3,477(12HRA ) Annually/quarterl y Mercur y Feedrate Mas s Flowmeters/Scale s Ib/h r > 0.007 3 (12HRA ) Annually/quarterl y Chlorin e Feedrate Mas s Flowmeters/Scale s Ib/h r >23 7 (1 2 HRA ) Annually/quarterl y As h Feedrate Mas s Flowmeters/Scale s Ib/h r > 67 3 (1 2 HRA ) Annually/quarterl y Primar y Combustio n Chamber Temperatur

e Typ e K

Thermocoupl e ° F <1,590 (one-minut e average ) <1,71 2 (HRA 1 ) >2,40 0 (instantaneous ) Annually Secondary Combustio n Chambe r Temperature Typ e K Thermocoupl e ° F <1,79 4 (one-minut

e average ) < 1,84 5 (HRA 1 ) >2,40 0 (instantaneous ) Annuall y Primar y Combustio n Chamber pressure Pressur e transmitte r in . w.c . >-0. 1 (

5 secon ddelay ) Quarterl y Secondar y Combustio n Chamber pressure Pressur e transmitte r in . w.c . > -0. 1 (

5 secon ddelay ) Quarterl y Chlorin e Fee dt

o Slurry Flo w Rati o Flowmete r rati o >33. 5 Annually Spra y Drye r Adsorbe r Outle t Temperatur

e Typ e K

Thermocoupl e ° F >50 0 (on e minut e average ) >42 0 (HRA ) Annuall y Combustio n Ga s Flo w Rat e Pitot Tub e acf

m >17,19 8

>15,53 4 (HRA ) Annuall y Stac k Ga s Exces s Oxyge n ZirconiumOxid e fue l cel l % < 3 (one-minut e avg. ) Quarterl y Stack carbo n monoxide Infrare d ppm v >10

0 (HRA ) >50 0 (on e minut e average ) Quarterl y Stac k Hydrocarbo n FI D ppm

v 2 :1 0 (on

e minut e average ) Quarterl y Stack ga s opacit

y Whit e Ligh t % >1 0 (on e minut e average ) Quarterl y Stack hydrogen chloride 2 Infrared ppm v >10

0 (HRA ) >50 0 (on e minut e average ) Quarterl y Fabri c filte

r pressure dro

p DeltaP transmitte r in . w.c . < 2 o

r > 1 0 ( 1 min . average ) Quarterl y HR A mean s "hourl

y rollin g average " a s calculate dby averagin g the previou s 6 0 one-minut e averag e values . 2Thi s i s aRCR A permi

t limi t only .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 3 HW C MAC T Performanc e Tes t Pla n Pag e 1 2 o f 1 2 Figur e 2- 1 Hydrate d Lim e Specification s

Ced e KP.20 0

9 7 , 2 »

7 2 . a t c •?

a . ©

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Q:\mw97\Projects\10002022\VeDli a Performanc

e Tes tPla n U 3 07300 8 Revision.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc 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 aoperate s 2 Fixe dHeart h Dua l Chambere dIncinerators (Units 2 an d3 ) andon e rotar y kil n incinerato

r (Uni t 4 ) a t th e Sauget , I

L facility . Th e two fixe dheart h unit s ar e rateda t 1 6 millio n Btu/h r each . Incineration Uni t No . 3 i s amirro

r imag e o f Uni t No . 2 . Bot

h o f thes e unit

s hav e thei

r ow n wast e handling system s a s describe di

n th e section s tha

t follow . Th e onl

y differenc e being Uni

t No . 2 i s equippe dwit

h four (4 ) baghous e modules , whil e Uni

t No . 3 i s equippe dwit

h three (3 ) baghous e modules . However , eac h incinerator i s operate didentically wit

h onl y thre e baghous e module s i n servic e during operation . Uni t 4 i s rateda

t 5 0 millio n Btu/h r an di s equippe dwit

h its own tan

k far msystem , dru

mstorage , bul

k solid s storag e an dfee dsystems . 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 Wast e Fee d Syste m an d Blendin g Operation s Th e Uni t 4 Rotar y Kil n can incinerat

e an y o f th e wast e tha t Veoli ai s authorize dan dpermitte dt o receive . Al l physical form s o

f waste s wil

l b e handle dan dfe db

y th e system' s waste fee ddevices . Liquid s wil l b e fe dt o eithe r th e kil n o r the Secondar

y Combustio n Chambe

r (SCC) . Bul

k soli dwaste s wil

l be fe dt o th e kil n throug h eithe r the ra mfeeder . Containerize dwaste s will b e fe dt o the kil n throug h th e ra mfeeder o r th e auxiliar y ra m feeder . Thi s uni

t ca n receiv e an

y combination o

f waste s - liquid , semi-solid , o r soli d- wit

h ahea t valu e of u p t o 5 0 million Btu/hr . Uni t 4 i s supporte db

y storag e tank s locate din Tan k Far m#3 . Thes e tank s ar

e use dt o stor e th e liqui dorgani c waste , aqueou s wastes , an dpumpable sludge s t o be fe dt 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 can b e use da s fee dtank s t o the incinerator . Several criteri aar e importan

t in designin g a blen dfro mreceive dwastes . Thes e includ e compatibility , prope

r rang e o f heating value , an dpermi t restriction s regardin g elementa l compositio n (base don emissio n limitations) . Pump s t o transfer thes e waste s t o the syste mar

e installe din the tan

k farm . Th e materia

l i s transferre dthroug

h abovegroundpipeline s fro m th e tan k far mt o the incinerator . Pipeline s use dt o transfer liquidorgani c wast

e an daqueou s wast

e ar e equippe dwit

h strainers . I n complianc e wit

h th e Benzen e NESHAP , al l tank s are vente dt o individua

l carbo n adsorptio n canister s fo r remova l o f organic s before vapor

i s discharge dt

o th e atmosphere . Eac h carbo n adsorbe r caniste r i s essentiall y equivalen

t t o a5 5 gallo n containe

r o r greater , i f necessary . Al l tank s ar

e equippe dwit

h conservatio n vents , in additio n t o th e carbo n canister

adsorber . Al l tank s ar

e grounded , an dflame arrestor s ar e installe dbetween th e carbo n adsorber s an dthe tanks . 2.2.1. 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui dwaste injector s use di n the combustio n chamber s ar e air-atomizing injectors . Thes e ar e use dfo r injectio n o

f pumpabl e sludges , aqueou s waste s an dorgani c liquidwaste s t o th e kil n andfo r injectio n o

f organi c liqui dwast

e t o th e SCC . Dua

l flui dinjectio n nozzle s wil l b e use dfo r

atomization o

f th e waste . Eac h o

f th e injector s i s rateda

t 0-300 gph . Th e liqui dwast e fee dnozzle s ar

e serve db

y parallel redundan

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

Q:\mw97\Projects\10002022\Veoli a Performanc

e Tes tPla n U 4 07300 8 Rewsion.do

cRevision : 1 Date : Jul y 200 8 Section ; 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 2 o f 1 5 2.2.1. 2 Package dan d Bul k Soli d Container s of

waste s ar

e sample dan danalyze dafter receipt in accordanc e wit

h th e facility' s Waste Analysi s Plan . Thes e waste s ca n the n b e delivere ddirectl

y t o Uni t 4 or repacke dint

o smal l combustibl e container s a t the facility . Repackage dcontainer s ar e delivere dto , an dstaged , i n the Containe

r Storag e Uni

t No . 6 adjacen

t t o th e Uni t 4 incinerator . Whe

n schedule dfor

feedin g t o th e system , the container s o f wast e are transferre db

y forklift s t o th e fee dconveyor s servin g Uni t 4 . Bul k solid s an dnon-pumpabl e waste s ar e delivere dan ddischarge dint o wast e fee dbin s i

n th e Bul k Solid s Storag e Buildin g afte r

bein g received , sampled , an danalyzed . A clamshel l operating fro ma n overhea

dcrane i s use dt o transfer thes e waste s fro mth

e bin s t o th e fee dhopper s dischargin g t o th e system' s ra

mfeeder . Th e weigh hoppe

r i s equippe dwit

h weig h cell s s o eac h charg e o

f waste ca n be weighe dbefor

e i t i s discharge dint

o the ra mfeeder . Fugitiv e emission s ar e controlle db

y abaghouse , cyclone , an dcarbo n adsorptio n syste mconnecte dt o thi s system . Th e ra mfeede r i s a25-inc h wid

e b y 4 2 inc h hig h (insid e dimensions ) rectangula r tub e operate db

y a hydraulicall

y driven ram . Th e ra

mtub e i s equippe dwit

h avertical , hydraulically operate dcharg e doo r nea r th e kil n end . Thi s door

i s opene dbefor

e th e ra mbegin s advancin g t

o pus h acharg e int

o th e kiln . Afte r

th e ra m ha s full y retracted , alimi

t switc h triggers th

e door t o clos e s o a s t

o protect th e ra mfeeder fro mthe kiln' s radian t heat . Th e ra

mi s capabl e o

f operating fro m0-3 0 cycles/hour . Th e to p fac e o f the ra mfeede r ha s a2 ' x 2 ' opening which receive s wast e charge s fro mth

e hopper . The ra

m feeder isolatio n gate , the charg e door , andth e ra moperat e in sequence . A

t the beginning o

f acycle , th

e ra m i s fully retracted . O n a"start " comman dfro mthe operato

r o r th e programmable controller , the ra mfeeder isolation gat

e open s t o receiv e acharg e o

f wast e fro mth e hopper . Th e gat

e then closes , th

e charg e doo

r opens , an dthe ra

mbegin s it s advance . Onc e th e ra mreache s it

s ful l extension , i

t begin s t o retract . Whe

n th e ra mi s fully retracted , the charg e doo r i s close dan dth

e cycl e ca

n b e repeated . Thi s system' s sequence d operation combine dwit

h th e negativ e pressur

e i n th e kil n preven t fugitiv e emission s fro mescapin g th e kil n ra mfeeder system . Th e ra mfeede r als o receive s container s o f waste s delivere db

y a n auxiliar y fee dsystem . Th e auxiliar y fee d conveyor i s capabl e of

handling charg e weight s o f 1 t o 10 0 pounds . Th e systemi s capabl e of handling charg e size s u p t o 2 4 inche s i

n diamete r an d2 4 inche s tall . Th e auxiliar y fee dconveyor

i s capabl e o

f making 6 0 charge s a n hou r or on e complet

e cycl e ever

y minute . 2.2.1. 3 Specialt y Liqui d Feed s Th e Specialt

y Fee dSyste massociate dwit h Incinerato

r No . 4 i s aDirect

Injec t Liqui dFee dSystem . 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 [40 CF R §63.1207(f)(1)(iii)(B ) an d (C ) Incinerato r No . 4 feature s atwo-stag e combustion process . Ignitio n o f wast e materia l take s plac e in th

e kiln , o r primar y combustio n chambe

r (PCC) . A secondar

y combustio n chambe

r (SCC ) serve s a s a

n "after-burner " fo r proces s gase s an di s als o permittedt o incinerat

e hig h Bt u liquidwaste . Ignitio

n o f th e wast e take s plac e a

t temperature s in exces s of 160 0 degree s F . Th e secondar y combustio n chambe

r maintain s aminimu

m temperatur

e of approximately 187 5 degree s F . Th e rotar y kil n i s fabricate do

f carbo n steel . I

t ha s approximat

e dimension s o

f 8'8 " O.D . X 35 ' long . I

t i s supporte don aone-degre e slop e b y tw o stee l tire s o

r riding rings . Eac h ridin

g ring ride s o

n tw o pair s o

f steel Q:\mw97\ProJects\10002022\Veoli a Performanc

e Tes tPla n U 4 07300 8 Revision.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 3 of 1 5 trunnion s an dhav e an approximat e outsid e diamete r o f 9 feet 5 inches . Th e thicknes s andfac e widt h o f th e trunnion s ar

e approximatel

y 6 inche s and9 inches , respectively . Tabl e 2- 2 provide s asummar

y ofth e incinerator

desig n specifications . Th e kiln i s line dwit

h approximatel

y 7 Vz inche s o

f dens e abrasion-resistant

high-alumin afirebrick

refractory . Wit h thi s refractor

y system , th

e kiln ha s a

n inside diamete

r o f approximately 7 feet

an dalengt

h o f approximately 3 5 feet , a

n integra l cross-sectio n are ao

f approximately 3 8 squar

e feet anda n interna l volum e o f approximately 1,346 cubi c feet . Al l kil n feed s will ente

r throug h th e uppe r kil n fac e plat

e whic h i s locate do

n th e fee dendo

f th e kiln . The plat

e contain s aprimar

y burner , three liqui dfee dnozzle s (fo r pumpabl e sludge , aqueou s waste , andhig h Bt u liqui d waste) , ara

mfeede r andasurg e vent . Th e primar

y burne r i s equivalen

t t o aNort h America

n 'Fue l Directed ' burne

r o f 2 5 MMBtu/hr . an dbum s No . 2 fue l oil o r natura l gas . Th e burne

r systemi s supplie dwit

h approximately 4,00 0 acf mcombustio n ai

r a t astati c pressure o

f 20 " wate r colum n (WC) . Th e pilo

t fo r th e primar y burne r will bur n natura l gas . Th e fue l syste mfo r

th e kil n (an dsecondar

y combustio n chamber

) i s controlle db

y aFactor

y Mutua l approve d burne r managemen

t systemcomplet

e wit h interlocks an dsafet

y valves . 2.3. 2 Secondar y Combustio n Chambe r (SCC ) Th e SC C i s avertical , cylindrica l chambe r having approximat

e dimension s o

f 10'-6 " O.D . x 71 ' high . I

t i s fabricate dof

carbo n stee l an dline dwit h a n inne r cours e (ho

t face ) of approximatel

y si x inche s o

f high alumin a refractor y an da n oute

r cours e of

approximatel

y two inche s o

f insulatin g refractory . Wit h thi s installe d refractory , th

e SC C ha s a

n inside diamete

r o f approximatel

y nine feet . Th e effectiv e lengt h (ga s retention length ) of the chambe

r i s approximatel

y 48 ' - 6" . Consequently , the SC C ha s across-sectio n are ao f 6 4 squar e fee t anda n effectiv e volume o

f approximatel

y 3,08 4 cubi c feet . A

t maximu mcombustion ga s flows , the combustio n ga s residenc e tim e i s greate

r tha n tw o seconds . Combustio n gase s fro mthe kil n ente r th e botto mo f th e SC C through arefractory-line dside duct an dexi t fro m the to p o f the SC C through arefractory-line dduct t o the temperin g chamber . Th e floor o f th e chambe r i s slope dt o facilitat e th e remova

l o f as h andsolid s throug

h asla g tap . Th e SC C i s equippe dwit h on e burne r mounte do n th e sidewal l of

the chambe

r nea r th e bottom . Th e burne

r i s aTran e Therma

l Model , o

r equivalent , wit

h adesig n hea

t releas e of

approximatel

y 3 0 millio

n Btu/hr . Thi s burne r i s supplie dwit

h No . 2 fue l oi l o

r natura l ga s an dcombustio n air . A s wit h the kil n burner , th

e SC C burne

r i s supplie dwit

h atomizin g air

andi s equippe dwit

h aburne r managemen

t system . Thi s systemcontrol s th e ignition andinitiate s an automati c shutof f whe n ther e i s alos s o f flame , combustio n ai

r supply , fue l pressure , atomizing ai r pressure , pilo

t burne r o r I D fan . Th e SC C burne

r i s ahigh-intensity , vorte

x type uni t wit h aspi n van e assembly , locate dwithi n the windbox t

o impar t an intens e rotar

y motio n t o the combustion air . Thi s rotar y motion an dthe burne

r desig n provid

e complet e mixing o

f air andfuel , an drecirculatio n o f th e gase s within the combustion chambe r promote s rapi d combustio n an dhigh hea t intensity .

Q:\rnw97\Projects\10002022\Veoli a Performanc

e Tes tPla n U 4 07300 8 Revision.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 4 of 1 5 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 pyromete

r tha t monitors temperatur

e i n th e rotar y kil n i s locate dtop-cente

r i n th e transitio n sectio n between the rotar

y kil n andth e SC C abou

t two fee t downstrea

mfro mth

e exi t o f th e kiln . The thermocoupl e tha t monitor s temperatur

e i n th e SC C i s locate do

n th e wes t

side of th e chambe r nea r the SC C exi

t duct . 2.3. 4 Hazardou s Wast e 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 r the Uni t 4 Rotar y Kil n Incinerato

r i s calculate da s follows :

• Rotar y Kiln Volum

e - 1 34 6 ft 3

• Secondar

y Combustio n Chambe

r Volume - 308 4 ft 3

• Tota l Volume - 443 0 ft 3

• MaximumFlu e Ga s Flowrat e - 43,00 0 acf

m(71 7 ft 3 /sec )

• Total Combustio n Zon e Residenc e Time = (443 0 ft 3 )/(71 7 ftVsec ) = 6. 2 sec 2.3. 5 Combustio n Syste m Lea k Th e kiln itself

i s equippe dwit

h adouble sea l syste mtha t i s comprise do

f overlapping , adjustable , stainles s stee l sprin g plate s o n bot h th e fee danddischarg e end s o f th e kiln . Th e sealin g edge s o f eac h plat e ar e fitted wit h asintered-meta

l wea r sho e simila

r t o abrak e sho e wit

h th e inne r sea l restin g o n th

e kil n shell . Th e powdere dmeta

l formulatio n fo r

th e sea l shoe s include graphit e granules , whic h mak

e th e shoe s self

lubricating . Th e voi dbetwee n th e seal s an dth

e oute r shel l ofth e kil

n i s pressurize dt

o furthe r preven t fugitiv e emissions . I

n addition t

o th e kil n sea l system , Uni

t 4 als o utilize s an induce ddraf t fan tha t maintain s avacuum o f - 0. 5 t o - 1.0 inche s wate

r colum n while waste i s bein g fire dint o the system . 2.3. 6 Emergenc y Safet y Ven t Uni t 4 i s equippe dwit

h tw o emergenc y vents , one locate da t th e kil n inle t whic h act s a s an emergenc y pressur e relief , the secon di s locate da

t the top of

th e SC C a s atherma

l relief vent . Th e emergenc y ven

t a t th e kiln inle t wouldonl

y b e require dfo r

a n occurrenc e tha

t overwhelm s th

e abilit y o f the I D fa n t o contro l th

e pressure o

f th e kiln . Th e vent

an dchut e openin g i s designe dsuc h tha t wast e fro mth e bul k solid s chut

e woul dno

t imped e th e escapin g ga s flow . A deflector separate s th

e fee dflo w fro mth

e ven t opening . Th e entrainmen t of solid s throug

h the surg e ven

t i s minimal . A s a

n extraprecaution , th

e exhaus t opening o f th e ven t i s angle dt

o provid e ahorizonta

l exit , thereb y minimizing solid s entrainmen t int o the air . Th e vent i s kept close dby weightedlouvers . Thes e louver s wil l open onl y i f the pressur

e in the kil

n suddenly rises beyon dth

e compensatin g capacit

y of the I D fan . A limi

t switch o n th e louver s will automaticall y shutof f all wast e feed s t o th e kil n andSC C whe

n th e ven t i s opened . Th e incinerator

i s als o equippe dwit

h a n emergenc y safety ven

t (ESV ) locate da

t th e to p o f th e secondar

y combustio n chamber . Thi s ES V i s arefractory-line demergenc y therma l relief ven t (TRV ) which i s hel di

n th e close dpositio n b

y apneumati c cylinder . Th e contro l valv e in th e line supplyin g ai

r t o th e cylinde r andth e cylinde r ven t valv e whic

h open s th

e TR V ar e locate din the control roo mfo r eac h unit . Valv e lock s (wit h key s attached ) ar e utilize dt

o dete r indiscriminat

e operatio n o

f thes e valves . Openin g ofth e TR V allow s ho t combustio n ga s t

o ven t fro mthe combustio n syste mduring emergenc y shutdown events . Th e purpos e ofth e TR V i s t o protect the downstrea

mAPC S fro mexcessiv e temperatur e situations . A limi

t switch on the TR V shut s of f al l wast e feed s t o the systema s i

t sense s tha

t the ca p i s opening . Q:\rnw97\Projects\1D002022\VeDli a Performanc

e Tes tPla n U 4 07300 8 Revision.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc 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 db

y the contro l system , observatio n of proces s control variables , o r b y regula r fiel dinspections . I n the even

t of amino

r equipmen

t malfunctio n (e.g . wast

e fee do r scrubber leaks) , th

e control roo

moperato

r will b e notified . Th e contro l roomoperato r wil l the n clos e th

e wast e fee dvalve s an ddisabl e th e wast e fee d pumps . I n th e even t of majo r equipmen

t malfunctio n (e.g . fire) , th e emergenc y sto

p butto n locate di

n th e control roo

m will b e pushed . I

f thi s butto n i s pushe dall equipmen t will switch t

o its 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 r pollutio n contro l syste mconsist s o f atemperin g chamber , two spra y drye r absorbers , an dfabri c filte r baghous e modules . Th e ai r pollution control syste mneutralize s acidi c compound s an dremove s particulat e fro mth e exhaus t

gas . Tw o subsystems , th e spra y drye r absorbe r an dth e fabri c filter , carr

y ou t th e chemica

l neutralizatio n an dparticulat e removal functions , respectively . A thir dsubsystem , th

e lim e system , i s use dt

o prepar e an dprovide lim

e slurr y t o the spra y drye r absorbe r fo r us e i n th e chemical neutralization process . Th e induce ddraf

t fa n an dstac k

provide th

e mechanica

l energ y requiredt

o transpor

t th e flu e ga s throug

h th e interconnecting ductwork , t o it s eventua

l discharg e poin

t to atmosphere . 2.5.1. 1 Temperin g Chambe r Th e temperin g chambe

r i s avertical , cylindrica

l uni t designe dt

o coo l th e combustio n gase s usin g aserie s o f interna l dual-flui d(wate

r an dair ) spra y nozzles . Th e combustio n gase s ente r the to p o f th e chamber , flo w downwar dthrough the spra

y patter n an dexi t fro mth e botto mofth e chamber . Th e spra y patter n i s designe d t o eliminat e direc t contac t o f wate r wit h refractory , an dth

e chambe r i s designe dt

o maintai n adr y botto munde r al l operatin g conditions . Tha t is , the injectio n rat

e o f spra y wate r i s controlle ds o tha

t i t i s completel

y vaporize d an dcarrie dou

t o f the chambe

r i n th e combustio n gases . Th e tempering chamber i s approximatel

y 49 ' hig h wit h 11 ' I.D . an di s fabricate do f % inch nomina

l plat e thicknes s carbo n stee l (AST M A36 ) an dlinedwit h refractory . Th e spra

y nozzle s an dextension s ar e fabricate do

f 30 4 S S material . Th e temperin g chamber

i s size ds o tha

t acombustio n ga s retention tim e o f greate r tha n on e secon dwil

l be maintaine da

t al l ga s flows . Becaus e some molte n particulat

e material s in the combustion gase s ar e coole di

n thi s proces s uni

t t o belo w thei

r fusio n point, some solid s ar e generate d an dcollecte di n th e chamber . Therefore , th e chambe

r ha s acon e botto

man daslid e gat

e t o facilitate the remova

l of solids . Thes e solid s ar

e discharge dont

o aconveyo r

system , whic h transport s the mt o ahopper . 2.5.1. 2 Lim e Syste m Th e lim e syste mprepare s lim

e slurr y fo r us e in the chemica

l neutralizatio n proces s i n sufficient supply an d concentratio n t

o maintain continuou s flu e ga s treatmen t in th e spra y drye r absorber . Th

e systemha s bee

n designe dfo r

batch mixing t

o provide thi s service . Veoli autilize s hydratedlim e a s its neutralizing agen

t in f th e air pollution contro l systems . Th e ke y neutralizatio n paramete r o f th e hydrate dlim

e i s th e "Ca O Equivalent" . Figur e 4- 1 i s th e specificatio n shee t fo r the hydrate dlim

e tha t Veoli auses . Veoli aha s use dthi s specifi c produc t fo r over 2 0 year s an dplan s t

o continu e wit

h it s use . Although , i

f Veoli adoe s chang e supplier s o r type Q:\mw97\Projects\10002022Weoli a Performanc

e Tes tPla n U 4 07300 8 Revision.do

cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 6 o f 1 5

o f lim e in the future , i

t woul dhav e a"Ca O Equivalent " specificatio n equa l t o o r greate r tha n th e 72.6 % show

n o n Figur e 4-1 . Hydrate dlim

e i s store di n astorag e bi n abov e th

e lim e preparatio n area . Th e storag e bin i s size dt o hol d enough hydrate dlim

e t o maintain several day s o f syste moperation a

t th e maximu mcombustio n rat

e o f th e incinerator . Lime i s discharge dthroug h th e conica l storag e bi

n bottom . The flo w o

f th e materia l fro mth e bi n i s aide db y avibrating "live bottom, " o r bi n activator . A variabl e spee dscre w feede r i s use dt o mete r th e hydrate dlim

e i n th e proportion s require dfor batc h mixin g lim e slurry . Th e lim

e i s mixedwit

h wate r i n atan k beneat h the lim e storag e bin . Th e scre w feeder spee dan dth

e rat e tha t wate r i s adde dt

o th e lim e slurr y tan k ar e variabl e s o tha

t th e desire dlim

e solid s concentratio n ca n b e achieve di

n th e tank . Th e variabl e fee d adjustment s allo w wate

r andlim e t o b e adde dt

o th e lim e slurr y tan k a t arat e tha t wil l allo w abatch mod

e o f mixing . A n agitato

r i s provide di

n th e slurr y tan k t o mi x the wate

r andlim e andt o maintai n th e suspensio n o

f lim e solids . Th e mixedlim

e slurr y i s pumpeda

t acontinuou s rat

e o f flo w throug

h arecirculatio n loo

p t o th e SD A nozzle s a

t arat e o f u p t o 1 0 gp mt o eac h nozzle . 2.5.1. 3 Spra y Dr

y Absorbe r Uni t 4 i s equippe dwit

h tw o Spra

y Drye r Absorber s (SDA ) locate dimmediatel y downstrea

mo f th e Temperin

g Chamber . Eac h SD A uni t i s fabricate do

f 3/ 8 inch carbo n steel . Th e functio n ofth e SDA s i s to :

• Furthe

r coo l th e combustio n gase s fro m600-800° F t o 300-500°F , • Neutraliz e an dremov e HC I an dothe

r acid s fro mth

e combustio n gases , • Remov e aportio

n o f th e particulat

e (fl y ash) fro mthes e gases . Slurr y flo w t o eac h spra

y drye r absorber (SDA ) i s metere db

y aflo w control valv e t

o obtain th

e prope r fee d concentratio n t

o the spra

y drye r absorber . Manua

l adjustmen

t t o th e flo w i s mad

e a s afunctio n o

f th e SD A outle t temperatur

e an da s afunctio n o

f th e outpu t fro mahydrochlori c aci d(HCI ) analyzer

i n th e ga s duc t downstrea

mo f the fabri c filter . Sinc e the Tempering Chamber accomplishe s initia

l coolin g o

f the gases , n

o additiona l wate r i s use di n th e SDA s fo r

ga s temperatur

e control . Th e combine dunit s ar

e size dt o remov e mor

e tha n 82 0 Ib/hr. of

chlorine fro mth

e combustio n gases . Eac h SD A i s approximatel

y 72 ' high by 107 " i

n diameter . Eac h uni

t include s aheadsection , an da60 ° conica l hopper . Eac h SD A chambe r ha s on e acces s doo

r i n the uppe

r section . Eac h hoppe

r ha s on e acces s door, a flange dclean-ou

t port, an dadrain connection . Th e SD A headsectio n consist s o f aflange dinle

t connection an daho t ga s inle t plenum . Th e dual-flui datomizing nozzle s includ e stainles s steel housing s andstellited inserts . Th e nozzle s are assemble dt o permi t fiel dremova

l fro mth e piping . Th e tw

o lim e slurr y pipin g header s hav e automati c isolatio n valves . Combustio n gase s ente

r th e to p o f eac h o f thes e units , flo w downwar dthroug h acentra

l duc t an dar e disperse dsymmetrically fro mthi s duc t int o th e absorbe r chambe r a t avelocit y an ddirectio n tha

t assure s optima l contac t wit h th e clou dof

atomize dlim

e slurr y droplet s introducedint

o th e chambe r b y dual-flui d(lim

e slurr y an dair ) nozzles . Th e gase s the n flo w downwar dthrough eac h absorbe

r chambe r an dexi t throug h a botto mside duct . A s th e gase s contac t an dpas s throug

h the clou do

f atomize dlim

e slurry , th

e wate r i n th e slurr y evaporates , coolin g th e gases . Simultaneously , the lim e i n the slurr

y react s wit

h th e hydroge

n chlorid e in the gase s t

o produc e calciu msalts . Some o f th e resulting dr

y material , consistin g o

f calciumsalts , fly as h an dexces s lime , fall s t

o th e conical botto

mof eac h unit . Th e dr

y materia l fro meac h uni

t i s discharge dt

o a conveyo r syste mwhich transport s i t t o adum p traile r o r equivalen

t typ e system .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 7 of 1 5 2.5.1. 4 Fabri c Filte r Ga s exhauste dfro mth

e spra y drye r absorber s i s distributedt o two fabri c filte

r module s connecte din parallel . Eac h modul e i s divide dint o thre e compartment s connecte din parallel , whic h contain multiple fabri c filte r bag s through whic h th

e combustio n gase s pas s t o remove particulates . Withi n eac h compartment , th

e ga s i s passe dthrough Teflon-coate dfiberglas s clot h bags . Th e ga s passe s fro mth e outside t

o th e inside ofth e filte

r bags . Particulate entraine din th e ga s strea

mi s mechanically deposite do n th e outside ofth e filte

r bag s a s th

e ga s passe s throug

h th e cloth . Eac h compartmen

t ha s aclea

n ai r plenu man dhousing sectio n t

o contain approximatel

y 30 8 bags . Eac h ba

g i s approximately 5 " in diamete r b y 5 ' long . Th e baghouse s ar e fabricate dfro m3/16 " mildstee l plate , o f welde d construction , ga s tigh

t an dstiffene dt

o withstandth

e maximu

moperating negativ e pressure . Eac h compartmen

t ha s atub e sheet

tha t support s th

e bag s an dprovide s fo r

to p bag/cag e removal . Acces s t o th e clea n ai r plenumi s vi aaboltedacces s door . Eac h traile r mounteduni

t contain s th

e compresse dair

headers , ga s inle t an doutle t manifolds , an dth

e conveyor . Th e fabri c filte

r cleanin g mechanis mutilize s jet s o f ai r t o clea n th e filte r bags . Periodically , the cleanin g sequenc e wil l b e initiated . Th e sequenc e i s starte d whe n th e differentia

l pressur e acros s th

e filte r reache s a predetermine dsetpoin

t of approximately 8.0 " w.c . o r whe n the operato

r initiate s acycle . Th e controlle r the n sequence s t

o eac h row of

filte r bag s i n eac h module , releasin g aburst o f ai r opposit e t o th e directio n o

f ga s flow . Th e quickly release dburs t of ai r dislodge s dus t

cake on the exterio

r o f eac h ba g a s i t travel s fro mth

e to p t o th e botto

mofth e bags . Release dfro mth e bag , th e dus t cake fall s b

y gravit y int o the hoppe

r a t the botto m of th e module . Fro mther

e i t i s discharge dt

o aconveyor

syste mwhich transport s i t t o adum p trailer , o

r equivalen t typ e system . Treate dby th e spra

y drye r absorber s an dfiltere db

y th e fabri c filters , th

e cleane dflu e ga s exit s th e fabri c filte

r compartment s t

o a n outle t manifol dfo r

exhaust . 2.5.1. 5 Carbo n Injectio n Th e carbo n injectio n syste mwill ai r injec t activate dcarbo n int

o th e plenu mimmediatel

y upstrea mofth e baghouse s an dallo w fo

r amor e efficient

mean s o f controlling Dioxin/Fura

n an dmercur

y emissions . Thi s syste mwil l b e controlle dby a n existin g PL C which wil

l contro l th

e inpu t o f activate dcarbo n t

o the baghous e inle t plenum . 2 t

o 20 pound s pe

r hou r o f powderedactivate dcarbo n wil l b e ai r injecte dint

o thi s plenu

man d allo w fo r direc t contac t wit h the stac k

gase s exiting th

e SDA's . Th e amoun

t o f carbo n i s dose di n adust-fre e manne r int o alow pressur

e ai r strea mvi apneumati c eduction . Th e eductor

use s ablowe

r fo r the motive air . High an dlow ai r pressur e switche s ensur

e tha t the blowe

r i s operatin g correctl

y an dtha t th e carbo n deliver

y systemi s clea

r fro mobstruction . The minimu mhig h pressur e settin g i s 4 psi g an dth

e maximu

mlo w pressure setting i s 1 inch wate r column . Th e carbon/air

strea mwil l the n trave l throug

h piping t o th e injectio n nozzl e int

o th e ductwork . Th e carbo n wil l contact the ga s strea

mexitin g the SDA' s an dallo w fo r

the adsorptio n o

f an y dioxin/furan s an dmercur y tha t migh t b e presen

t in thi s stream . Adsorptio n will continu e a s th e stac k gase s procee dthroug

h th e baghouses . Th e clea n stac k ga s will exi

t th e final stac k

vi athe induce ddraf

t fa n an dthe capture dsolid s will b e discharge dfro mth e baghouse s vi ath

e scre w conveyin g syste mint o a n enclose ddum

p traile r fo r disposal a

t aSubtitle C landfill . 2.5.1. 6 Induce d Draf t Fa n an d Stac k Th e induce ddraf

t fa n an dstac k

ar e locate ddownstrea

mo f the fabri c filter . Combustio n gase s ar e draw n throug h the syste mb

y a40 0 h p induce ddraf

t (ID ) fan , rated a

t 53,00 0 acf

ma t 400° F saturated , an d25 " wate r colum n pressure . Th e induce ddraf t fa n provide s th

e mechanis mfo r

transporting th

e incinerator

flu e ga s Q:\rnw97\Projects\10002022\Veoli a Performanc

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y drye r absorber , fabri c filter , an dall interconnecting ducts . The I D fa n include s a

n inle t volume contro l dampe

r t o be use dt

o control th

e velocit y o f th e ga s within th

e ductin g andtreatmen

t devices . Treate dgase s ar

e exhauste dfro mth

e induce ddraf

t fa n t o th e atmospher

e throug h a100-ft . hig

h stack . Th e stac k diamete r fo r Uni t 4 i s 4 8 inche s I.D . Th e stack i s equippe dwit

h instrumen

t sampling port

s an da samplin g platfor

mfo r emission s testing . Figur e 5- 1 provide s detail s o

n the desig n andsample por t location s an dconfiguration s fo r

the stack . 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 ) systemconsist s o f sampl e probes , sampl e deliver y an d conditionin g apparatus , andga s analyzers . Sample s ar e extracte dfro mthe transition ductin g locate dbetwee

n the I D fa n an dthe stack . A CE M performanc e tes t andqualit

y assuranc e progra

mha s been implementedi n accordanc e wit

h th e Appendi x t o Subpar t EE E o f Par t 63—Quality Assuranc e Procedure s fo r Continuou s Emission s Monitor s Use dfo r Hazardou s Wast e Combustors . Response s fro meac h CEM S will b e fe dt o the Contro l Syste m(CS ) wher e th e C O hourl

y rollin g averag e i s calculate dan dinterlocke dt o th e wast e fee dcutof

f valve s a s par

t o f th e Automati c Wast

e Fee dCutof

f System (AWFCO ) discusse di

n Sectio n 2.8 , below . Th e following provide s abrie f descriptio n ofth e CEM S instrument s includin g th e operating rang e an dmeasuremen t principal . 2.6. 1 CE M Syste mDescriptio n Th e Continuou s Emission s Monitoring System s (CEMS ) currentl y bein g utilize da

t Incinerato

r 4 analyze s for opacity , carbo n monoxide , hydroge n chloride , tota

l hydrocarbon s an doxygen . Thes e monitors , except opacity , ar e extractiv e device s mountedi n th e ductwor k between the I

D fa n an dth

e stack . Th

e tabl e belo w summarize s th e analyzer specifications . Th e opacit

y monito r continuousl

y measure s th

e stack ga s opacit

y an dreport s the measurement s t o a n indicato r an darecorder . A n opacit y tha t exceed s aprese

t limi t trigger s a

n alar mandinterlock . Carbo n monoxide an dhydroge n chloride ar

e monitoredwit

h extractiv e non-dispers e infrare danalyzers . Tota l hydrocarbo n i s monitore dwit h a n extractiv e flame ion detector analyzer . Oxyge n i s monitore dwit h a zirconiu moxid e cell . Stac k ga s flo w rat

e i s continuousl

y monitoredusin g a

n anuba r tha t send s a4-2 0 m

A signa l t o the PL C which convert s th e signal t

o acfm . Tabl e 2- 1 Veoli aE S Technica l Solution s - Continuou s Emission s Monitor s Paramete r Curren t Mfg . Rang e Principl e Oxyge n COS A 0-25 % Electrochemica l Carbo n Monoxide Echoche mM C 3 0-200 ppm v 0-3000 ppm

v Infrared Total hydrocarbon s Thermoelectro n 0-100 ppm v FID/lnfrare d Hydroge n chloride Echoche mM C 3 0-1000 ppm v Infrared Opacit y Teledyn e 0-100 % Whit e ligh t Stac k ga s flo w PSE/Rosemoun t 0-55,000 acf m Pressure dro

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2. 7 Proces s Monitorin g an d Contro l Th e facilit

y i s equippe dwit

h astate-of-the-ar

t monitorin

g an dcontro l system , whic h facilitate s complianc e wit h permi t conditions , an dotherwise , collect s proces s control information , facilitate s efficient operation anddetect s an dprevent s damag e t

o the facility . Th e systemconsist s o f thre e major

components :

• A human-machin e interfac e (HMI ) system , • Programmabl e logi c controller' s (PLC's) , an d

• A hig h spee detheme t cabl e connect s all control syste mcomponent s Th e desire dcontro l function s ar e implementedthroug

h the HM I system . Al l digita

l contro l an demergenc y interlock s ar

e accomplishe db

y the PLC . Th e contro l syste mi s capabl e o f monitorin g th e "operationa

l envelope " o

f the incinerator

an di s capabl e o

f performing anumbe

r o f activitie s including :

• Contro l roomindication of processo r

sensor s locate dwithin th e incinerator

system(such a s pressur e indicatio n of

afiel dinstalle dpressure transmitter) ;
• Proces s controlle

r fo r singl e instrumen

t loop s o r a n individua

l sub-system , suc h a s atemperatur e contro l loop involving asenso r reading fro mone temperatur e transmitte

r affectin g th

e functio n o

f on e temperatur

e control valve ; an d

• Alar mfo r an exceedanc e o

f adesignate dsetpoint , suc h a s ahig h pressure o

r lo w temperature . Th e proces s contro l compute r will continuousl

y contro l an dmonito

r the operatio n o

f th e incinerator . Whe

n outof-rang e condition s exist , i t will notif y th e operato r o f thos e conditions . Th e proces s contro l compute r i s programme dt

o shut-down equipmen

t (i.e. , brin g th e syste mint

o asaf e mode) whe n designate dparameters ar e exceeded , whic h i s aprotectiv e mechanis magains t potentia l equipmen

t damage , operation outsid e o f permi t limits , or condition s tha

t migh t leadt o areleas e t

o th e environment . Continuou s monitoring ofth e incinerator an dscrubbe

r syste mi s a

n importan

t aspec t ofth e systemdesign . A digita l readou t of al l monitorin

g instrumentation i s displaye do n the main contro l screen . A n audibl e an dvisua l alar malert s th

e incinerato

r operator t o significan

t deviation s fro mnorma

l operatin g conditions . Thi s syste m allow s a n immediat

e respons e t

o advers e condition s b

y the operator . Automati c wast e fee dcut-of

f and incineratio n shutdow n mechanism s ar e als o interlocke dwit

h th e monitorin

g syste ma

t o r prio r t o reaching permi t limi t levels . Monitoring method s andcalibratio n frequencie s ar e liste di n Tabl e 2-3 . Th e Incinerato

r ha s a n independen

t proces s control compute r tha t interface s t

o the Allen-Bradle y programmable controllers . Th e proces s compute r i s capabl e of

controlling th

e incinerator

in cas e o f afailur e i n aHM I server . Thi s compute

r run s aRSVIE W HM

I contro l software tha

t provide s operator

interfac e t

o al l instrumentation an dcontrols . 2. 8 Automati c Wast e Fee d Cut-of f Syste m [4 0 CF R §63.1207(f)( 1 )(iii)(F) ] The incinerator

ha s a n Automati c Waste Fee dCut-Of f (AWFCO ) Syste mtha

t will shu t wast e feed s of f i n th e even t certai n operatin g parameter s deviat e fro mallowabl e set

points . Th e PL C continuously monitors operating parameters , making adjustment s t o th e proces s a s neede dfo r prope r control . Alar

mlogi c i s incorporate dint

o th e PL C syste mt

o automaticall

y initiat e an AWFCO . Tabl e 2- 3 summarize s th e curren t
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points . AWFC O limit

s hav e been establishe dbase do n severa l factor s tha

t ar e summarize d below .

• Regulatory/permi

t limits - establishe dt

o compl y wit h existing permits . A n exampl e o f thi s typ e o

f limi t i s th e lo w temperatur

e limit , below whic h waste canno t b e fe dunti

l the prope

r limi t i s re-established . I n addition , th

e HWC MAC T regulation s requir e tha t the AWFC O systemb e interlocke dwit h th e span o f eac h proces s instrumen

t tha t i s par t ofth e Continuou s Monitorin g Syste m(CMS) . A listin g o f thes e CM S instruments andthei r interlocke dspan setpoint s i s maintaineda s par t o f Veolia' s Operating Record . • Proces s safet

y limit s - establishe dt

o assure proces s equipmen t i s protectedan dunsaf

e operating condition s d

o no t occur . A n exampl e of

thi s i s inadequat

e exces s ai

r i n th e combustion chambe

r tha t ca n leadt

o fue l ric h conditions . • Utilit y o r Powe r failur e - establishe dt

o facilitate acontrolle dshutdow n o f the proces s during los s o f proces s air, steam , wate

r or electricity . An exampl e o f thi s i s th e los s o f instrumen

t ai r tha t i s necessar y fo r certain type s o

f proces s instrument s t

o functio n properly . Waste s will no t b e re introduce dint

o th e incinerator s unti

l prope r operatio n o

f ke y instruments i s re-established . I n additio n to th

e AWFC O system , operator s ca n manually shutdown wast e feed s o r th e entir e proces s shoul d thi s b e needed . 2.8. 1 AWFC O Syste m Testin g Veoli atest s the AWFC O system s bi-weekly , a s weekly testing woul dundul y interfer e wit h operation s b

y ceasin g an drestarting wast e feeds , potentiall

y increasin g emissions , incurring excessiv e downtime , burnin g additiona l natura l ga s during th

e downtime , an dincreasin g operating costs . Testin g ofth e AWFC O syste mi s atime-consumin g andmanpowe r intensiv e process . Th e curren t testing progra

mha s been i

n plac e unde

r the RCR A permi

t fo r ove r 2 0 year s an dha s prove

n t o b e adequat

e i n detecting problems . Thi s rational e i s include din the facility' s AWFC O Plan . I n som e case s thi s testing occur s mor e frequentl

y dependin g o

n how often actua

l AWFCO s occu

r a t th e unit . Pe r

th e require dfrequency , incinerato r personnel chec k

the functionalit

y o f AWFC O logic tha

t i s par t o f th e incinerator' s PL C systemt o mak e sur e tha t shoul dproces s condition s deviat

e fro mallowable limits , th e compute

r logi c will initiat

e wast e fee dshutdown s a s required . Thi s i s accomplishe dby manuall y simulating proces s condition s tha t ar e outsid e allowabl e limits an dobserving an ddocumentin g whe

n th e control o

r block valv e software logi c o

n the wast

e fee dlin e begin s to initiat

e valv e closure . Shoul dactua

l AWFCO s occur

durin g agiven testin g period , thes e ar e documente db

y operating personne l t

o satisf y regulator

y requirement s fo r

syste mtesting . Result s o f thi s testing ar

e documente do

n a separate AWFC O Testing Lo g an dmaintaine da s par t o f th e unit' s Operating 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 Onc e equipmen

t i s installedan doperational , Veoli autilize s a n extensiv e preventative maintenanc e (PM ) progra mt o keep equipmen

t operationa

l an dpreven

t breakdown s an dfailures . Base dupon the typ e o f equipmen t an dhistorica

l operation s an dmaintenanc e experience , schedule s fo r variou s inspectio n andP M activitie s ar

e followed . Thi s include s aspect s suc h a s documenting detaile dmaintenanc e historie s o n equipment , routin

e inspection an dlubricatio n program s fo r high wea r equipmen

t an dnon-destructiv e testing o f

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o asses s integrity . Th e frequenc y o f thes e activitie s varie s dependin g upo n th e equipment , P M activit

y an dth e incinerator' s shutdown schedule . Fo r example , frequent

(i.e. , weekly ) instrumen

t an dcertai n mechanical equipmen t check s ar

e mad e fo r critica l proces s items . Lubrication , vibratio n analysi s an dothe r mechanical integrit

y check s are don

e a t longe r frequencie s lik

e monthl y o r quarterly . An dfinally , suc h item s a s inspectin g refractor y bric k for wear , ar e typically performe dwhe n the entir e incinerato r

i s shu t down fo r maintenance . 2.9. 2 Tes t Progra m Preparatio n Activitie s Prio r t o testing , instrumentatio n associate dwit h ke y parameter s o

f th e tes t wil l b e checked , calibrated , o r replaced , a s appropriate , t o ensure prope

r operatio n o

f th e instrumentatio n during testin g (i.e. , wast e fee d flowmeter s an dscales , CEM's , pressure transmitters , thermocouple s an dpyrometers , stac k flowmeters , etc.) .

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cRevision : 1 Date : Jul y 200 8 Section : 2. 0 Veoli a E S Technica l Solution s Uni t 4 HW C MAC T Performanc e Tes t Pla n Pag e 1 2 o f 1 5 Tabl e 2- 2 Technica l Informatio n Summar y o n Incinerato r No . 4 Manufacture

r Trad e Waste Incineratio n Mode l No . TWI-2000 , Serie s 2 Typ e Rotar y Kil n Dat e of Manufacture 198 9 Dimension s Primary Chambe r Secondary Chambe r Externa l Lengt

h 35 ' 48'6 " External Diamete r 8'8 " 10'6 " Interna l Diamete r 7 ' 9 ' Cross-sectiona l are a 3 8 squar e fee t 6 4 squar e fee t Burner s Primary Chambe r Burner Secondary Chambe r Burne 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/hr Fue l Natura l Ga s Natural Ga s Prime r Move r Induce dDraf t Fa n 4,00 0 acf

m@ 400° F saturated , 2 0 in . wate r colum n

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AWFC O Parameter s an d Limit s fo r Incinerato r

No . 4 Syste m Devic e Unit

s Cutof

f Limit s Calibratio n

Frequenc y Primar y Combustio n Chambe rTemperature Pyromete r ° F <1,24 0 (one-minut e average ) <1,507 (HRA 1 ) £2,40 0 (instantaneous ) Annuall y Secondar y Combustio n Chambe r Temperatur e Typ e KThermocoupl e ° F 21,82 5 (one-minute average ) •=1,88 6 (HRA 1 ) 52,40 0 (instantaneous ) Annuall y Primar y Combustio n Chambe rpressur e Pressur e transmitte r in . w.c . £ atmospheri c (instantaneous ) Quarterl y Secondar y Combustio n Chambe rpressur e Pressur e transmitte r in . w.c . 5 atmospheri c (instantaneous ) Quarterl y Spra y Drye rAdsorbe rInlet Temperatur e Typ e KThermocoupl e ° F £ 1,200 (on e minute average ) Annuall y Spray Drye rAdsorbe rOutle t Temperature Typ e KThermocoupl e ° F > 50 0 (on e minute average ) >43 5 (HRA ) Annuall y Tota l Pumpabl e Wast e Feedrat e Mas s flo w meter/scale s Ib/h r >426 2 (HRA ) Annuall y Tota l Wast e Feedrat e Mas s flo w meter/scale s Ib/h r >14,802 (HRA ) Annually / Quarterl y LV M Feedrat e Mas s flo w meter/scale s Ib/h r >120 (1 2 HRA ) Annually / Quarterl y SV M Feedrat e Mas s flo w meter/scale s Ib/h r >11 7 (1 2 HRA ) Annually / Quarterl y Mercur y Feedrat e Mas s flow meter/scale s lb/h r >0.067(12HRA ) Annually / Quarterl y Chlorin e Feedrat e Mas s flow meter/scale s lb/h r >27 4 (1 2 HRA ) Annually / Quarterl y As h Feedrat e Mas s flo w meter/scale s lb/h r >8,777(12HRA ) Annually / Quarterl y Carbo n Feedrat e Mas s flow mete r Ib/h r > 6 (HRA ) Quarterl y Carbo n Injectio n Syste m Maximu m Lo w Pressur e Pressur e Switc h in . w.c . > 1 Quarterl y Carbo n Injectio n Syste m Minimu m Hig h Pressur e Pressur e Switc h psi g < 4 Quarterl y Chlorin e Fee d to Slurr

y Flo w Rati o Flo w Mete r Rati o >44. 4 Annuall y Combustio n Ga s Flo w Rat e Anuba r acf m > 43,90 0 (HRA) Annuall y Stac k Ga s Exces s Oxyge n Zirconiu m Oxid e fue l cel l % £ 3 (on e minute average ) Quarterl y Stac k carbo n monoxid e Infrare d ppmv >100(HRA ) >50 0 (on e minute average ) Quarterl y Stac k Hydrocarbo n FI D ppmv >1 0 (on e minute average ) Quarterl y Stac k ga s opacit

y Whit e Ligh t % £1 0 (on e minut e average ) Quarterl y Q:Vnw97\Projec[s\10002022Weoli a Performanc

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y Stac k hydroge n chloride 2 Infrare d ppmv >100(HRA) 250 0 (on e minute average ) Quarterl y Liqui d feedrat e Mas s flow mete r Ib/h r > 1,700 Annuall y Sludg e feedrat e Mas s flow mete r Ib/h r > 1,10 0 Annuall y Drumme d an d Bul k

Solid s Feedrat e Scal e lb/h r > 15,00 0 Quarterl y Fabri c filte rpressur e dro p Delt a P transmitte r in . w.c . < 2 o r> 1 0 (on e minute 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 i s a RCR A permi t limi t only .

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## CONTINUOU S MONITORIN G SYSTE M QUALIT Y CONTRO L PROGRA M

Prepare dfor : Veoli aE S Technical Solutions , LL C

Sauget, Illinoi s

Prepare dby : Frankli n Engineerin g Group , Inc . Franklin , Tennesse

e

Octobe r 200 8TABL E O F CONTENT S

1.0 INTRODUCTIO N AN D BACKGROUN D 1

1. 1 SUMMAR Y O FFACILIT 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 1 3 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



## (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 i1. 0 INTRODUCTIO N AN D BACKGROUN D

Veoli aE S Technica l Solutions , LL C (Veolia ) own s an doperate s tw o fixe dheart h incinerator s (Unit s 2 an d3 ) an darotar y kil n incinerato r (Uni t 4 ) at it s facilit y locate di n Sauget , Illinois . Th e incinerator s ar e subjec t t o th e Nationa l Emission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r Hazardou s Wast e Combustor s (HWC) , Par t 63 , Subpar t EE E ( § 63.120 0 t o § 63.1221) . Th e NESHA P specifie s emission s standard s whic h reflec t

emission s performanc e o f Maximu mAchievabl e Contro l Technologie s (MACT) , an di s commonl y referre dt 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 dimplemen t a Continuou s Monitorin g Syste m(CMS ) Qualit y Contro l (QC ) Program . Th e purpos e o f th e Q C Progra mi s t o outlin e procedure s use dt o verif y tha t th e CM S ar e properl y installed , calibrated , an dcollectin g accurat e dat ao n a n ongoin g basis . Th e CM S performanc e evaluatio n tes t pla n wa s submitte da s par t o f th e Comprehensiv e Performanc e Tes t

Plan . Th e Q C Progra mdemonstrate s Veolia' s complianc e wit h th e requirement s se t fort h i n § 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 mi s require dt o contai n description s o f initia l an dsubsequen t CM S calibration , calibratio n drift , preventiv e maintenance , dat arecording , calculation s an dreporting ; an d acorrectiv e actio n pla n fo r malfunctionin g CMS . Tabl e 1- 1 present s the regulator y reference s relate dt o th e Q C program , followe db y the sectio n o f thi s pla n tha t

addresse s eac h specifi c requirement . Som e reference s ar e mad e t o othe r HW C MAC T require dfacilit y operatin g plans . Thi s Q C Progra mi s intende dt o fulfil l th e requirement s o f § 63.8(d)(2) , an dinclude s informatio n relate dt o th e procedure s fo r eac h ofth e followin g operations :

• Initia l an dsubsequen t calibratio n ofth e CM S

• Determinatio n an dadjustmen t o f th e calibratio n drif t

ofth e CM S

• Preventiv e maintenanc e ofth e CMS , includin g spar e part s inventor y

• Dat arecording , calculations , an dreportin g

• Progra mo f

correctiv e actio n fo r

malfunctionin g CMS .Tabl e 1- 1 Regulator y Checklis tfo 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 dmaintenanc 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 dmalfunctio n pla n fo r CM S SSM P Pla n § 63.8(c)(3 ) Verificatio n o f operationa l statu s C M S PE T Pla n § 63.8(c)(7)(h ) Out-of-contro l CM S dat awil l no t b e use di n average s an dcalculations . Sectio n 4. 0 § 63.8(c)(7)(h ) Correctiv e action s fo r a n out-of-contro l CM S Sectio n 4. 0 an d SSM P Pla 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 dimplemen t Q C portio n o f

CM S Q A progra m Sectio n 1. 0 § 63.8(d)(2 ) Q A progra minclude s th e developmen t an dsubmitta l o f th e performanc e evaluatio n tes t pla n Sectio n 2.1. 1 § 63.8(d)(2)(i ) Develo p writte n procedure s fo r initia l an dsubsequen t calibration s Section s 2.1.1 , 2.1. 2 § 63.8(d)(2)(h ) Develo p writte n procedure s fo r determinatio n an d adjustmen t

o f calibratio n drift s Sectio n 2. 2 § 63.8(d)(2)(iii ) Develo p writte n procedure s fo r preventiv e maintenanc e an dspar e part s inventor y Sectio n 2. 3 § 63.8(d)(2)(iv ) Dat arecording , calculations , an dreportin g Section s 3.1 , 3. 2 § 63.8(d)(2)(vi ) Correctiv e action s fo r malfunctionin g CM S Sectio n 4. 0 § 63.8(e)(3 ) Performanc e evaluatio n o f CM S C M S PE T Pla n § 63.8(g ) Reductio n o f monitorin g dat a Sectio n 3. 2 § 63.10(b)(1 ) Maintainin g file s Sectio n 3. 1 § 63.10(b)(2)(ix ) Maintai n record s o f measurement s fro mperformanc e evaluation s Sectio n 3. 1 § 63.10 (b )(2)(vi ) Maintai n record s o f eac h perio ddurin g whic h aCM S i s malfunctioning , o r

inoperativ e an dou t

o f contro l Sectio n 4. 0 an d

SSM P Pla 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 dopacit y an dvisibl e emissio n observation s Sectio n 3. 1 § 63.10 (b )(2)(x ) Maintai n record s o f CM S calibratio n check s Sectio n 2.1. 2

2Tabl e 1- 1 (continued ) Regulator y Checklis tfo 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 dmaintenanc e performe do n th e CM S Sectio n 3. 1 § 63.10(c)(1 ) Recordkeepin g requirement s fo r CM S measurement s (includin g unavoidabl e breakdown s an dout-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 dimplemen t CM S Q A progra mprocedure s Sectio n 1. 0 § 63.10(c)(5 ) Maintai n record s o f dat e an dtim e fo r

CM S inoperabilit y (excep t

fo r zer o an dhigh-leve l checks ) Sectio n 3. 1 § 63.10(c)(6 ) Maintai n record s o f dat e an dtim e fo r

CM 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 t includ e period s o f

Startup , Shutdown , Malfunctio n (SSM ) Sectio n 3. 1 §63.10(e)(3)(i ) Submitta l o f semiannua l exces s emission s an dCM S performanc e repor t Sectio n 3. 1 § 63.10(e)(3)(v ) Conten t an dsubmitta l dat ao f exces s emission s an d C M S performanc e repor t Sectio n 3. 2 §63.10(e)(3)(vi ) Conten t o f summar y repor t

require db 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 fo r submittin g onl y th e summar y repor t Sectio n 3. 2 §63.10(e)(3)(viii ) Conditio n fo r submittin g bot h th e summar y repor t an d exces s emission s an dCM S performanc e repor t Sectio n 3. 2 §63.1209(b)(2)(i ) Calibratio n o f thermocouple s an dpyrometer s Sectio n 2. 1 § 63.1209(b)(3 ) Frequenc y o f CM S sampling , evaluation , computing , an drecordin g o f

regulate dparamete r Sectio n 3. 1 § 63.1209(b)(5 ) Calculatio n o f rollin g average s Sectio n 3. 1 § 63.1209(f)(1 ) § 63.1211(c ) require s tha t CM S ar e installed , calibrated , an doperationa l b y th e complianc e dat e C M S PE T Pla n
Notes : PE T Performanc e Evaluatio n Tes t SSM P Startup , Shutdown , Malfunctio n Pla n SD P Standar

dDivisio n Practice sTh e dat acollecte dfro mCM S mstrumentatio n i s use dt o demonstrat e th e unit' s

complianc e wit h th e performanc e requirement s promulgate di n th e Interi mHW C Maximu mAchievabl e Contro l Technolog y (MACT ) standard . Th e Q A Progra moutline s procedure s use dt o verif y tha t th e CM S ar e properl y calibrate dan dcollectin 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 fo r eac h incinerato r

system) , genera l reference s t o aCM S syste mo r incinerato r

syste mi n thi s documen t wil l impl y al l thre e systems . Informatio n tha t i s onl y applicabl e t o on e o r tw o o f th e thre e system s wil l b e clearl y identified . Thi s documen t

i s organize da s follows : S ectio n 1. 0 Introductio n an dB ackgroun d Sectio n 2. 0 CM S Calibratio n an dPreventiv e Maintenanc e Sectio n 3. 0 CM S Recordkeepin g an dReportin g Sectio n 4. 0 CM S Correctiv e Action s Thi s pla n als o assimilate s informatio n an dprocedure s foun di n othe r documents . A s require db y § 63.6(e)(3)(vi) , othe r document s containin g procedure s o r informatio n referre dt o i n thi s pla n wil l b e mad e availabl e fo r inspectio n whe n requeste db y th e Administrator . Th e remainde r

o f thi s sectio n provide s a n overvie w o f th e incineratio n syste mfollowe 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 dpreventiv e maintenanc e requirements . Sectio n 3. 0 addresse s requirement s relate dt o facilit y documentatio n an dreporting . Sectio n 4. 0 define s an d discusse s nonstandar doperation s o f th e CM S an dapplicabl e correctiv e actions . 1. 1 Summar y o f

Facilit y Informatio n Brie f summarie s whic h describ e th e fixe dheart h incinerator s an dth e rotar y kil n incinerato r

ar e presente di n thi s section . 1.1.1 Fixed

Hearth Incinerators Eac h ofth e fixe dheart h incinerator s include s th e followin g components :

• Fee dequipmen t• Primar y an dsecondar y combustio n chamber s

• Lim e injectio n syste m

• Spra y drye r

absorbe r

(SDA ) » Fabri c filte r

baghous e

• Solid s an das h remova l system s

• Induce ddraf t

(LD ) fa n an dstac k

• mstrumentation , controls , an ddat aacquisitio n system s Variou s soli dan dliqui dwaste s an dgaseou s feedstream s ar e thermall y treate d i n th e fixe dheart h incinerators . Soli dwast e i s fe dt o th e primar y (lower ) combustio n chambe r vi aafee dconveyo r syste man dpneumati c ram . Liqui dwast e fro mtank s an dtanke r truck s ar e fe dt o th e primar y combustio n chambe r throug h tw o atomize dliqui dinjectors . Liqui dwast e fro mcontainer s ar e fe dt o th e primar y combustio n chambe r throug h a specialt y fee dinjector . A gaseou s feedstrea mi s fe dt o th e Uni t 2 primar y combustio n chambe r directl y fro mga s cylinders . Of f gase s from ahoode dfeed . emissio n contro l syste man dfrom awast e handlin g glov e bo x ar e fe ddirectl y t o th e Uni t 3 secondar y combustio n chamber . Combustio n chambe r temperature s ar e maintaine dusin g natura l ga s fire dt o adedicate dburne r i n bot h th e primar y an dsecondar y chambers . Combustio n ga s exit s th e secondar y combustio n chambe r an denter s th e SDA , whic h provide s aci dga s remova l an dcoolin g o f th e combustio n gas . Combustio n ga s exit s th e S D A an di s distribute dt o th e fabri c filte r baghouses , whic h provid e particulat e matte r removal . Th e induce ddraf t fan , locate ddownstrea mo f th e baghouses , move s th e combustio n ga s throug h th e syste man dexhaust s th e ga s throug h th e mai n stack . Hot , we t

ga s i s extracte ddownstrea mo f th e baghous e throug h acontinuou s emission s monitorin g system . Thi s syste mfeature s amulti-componen t infrare dga s analyze r tha t detect s hydroge n chloride , carbo n monoxide , an dwate r vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations . 1.1.2 Rotary Kiln Incinerator Th e rotar y kil n incinerato r include s th e followin g components :

• Wast e fee dsyste m

• Primar y an dsecondar y combustio n chamber s

• Temperin g chambe r

• Lim e injectio n syste m

• Spra y drye r

absorbe r• Carbo n injectio n syste m

• Fabri c filte r

baghous e

• Solid s an das h remova l system s

• L D fa n an dstac k

• Instrumentation , controls , an ddat aacquisitio n system s Variou s soli dan dliqui dwaste s ar e thermall y treate d i n th e rotar y kil n incinerator . Soli d waste s ar e fe dt o ara mfeede r vi aaclamshell , adru mfee dconveyor , an da n auxiliar y fee dconveyor . A hydrauli c ra mpushe s th e soli dwast e int o th e kiln . Liqui dwast e fro m tank s an dtanke r

truck s i s fe dt o th e primar y an dsecondar y combustio n chamber s throug h atomize dliqui dinjectors . Combustio n chambe r temperature s ar e maintaine dusin g natura l ga s fire dt o adedicate dburne r i n bot h th e primar y an dsecondar y chambers . Combustio n ga s exit s th e secondar y combustio n chambe r an denter s th e temperin g chamber , whic h provide s coolin g ofth e combustio n gases . Th e combustio n ga s exit s th e temperin g chambe r

an di s distribute dbetwee n tw o identica l SDAs , whic h provid e aci d ga s remova l an dadditiona l ga s cooling . A carbo n injectio n syste mi s utilize dfo r controllin g dioxin/fura n an dmercur y emissions . Th e activate dcarbo n i s ai r injecte dint o th e combustio n ga s immediatel y downstrea mo f th e convergenc e o f

combustio n gase s fromth e SDAs . Fro mth e SDAs , combustio n ga s i s distribute dt o fabri c filte r baghouses , whic h provid e particulat e matte r removal . Th e I D fan , locate ddownstrea mo f th e baghouses , move s th e combustio n ga s throug h th e syste man dexhaust s th e ga s throug h th e mai n stack . Hot , we t

ga s i s extracte ddownstrea mo f th e I D fa n throug h acontinuou s emission s monitorin g system . Thi s syste mfeature s amulti-componen t infrare dga s analyze r tha t detect s hydroge n chloride , carbo n monoxide , an dwate r vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations . 1. 2 CM S Instrumentatio n Thi s sectio n describe s th e CM S instrument s use dmonito r regulate dproces s parameter s fo r demonstratin g on-goin g complianc e wit h th e Interi mHW C MAC T emissio n standards . A summar y o f specification s fo r

CM S instrumentatio n i s provide di n Tabl e 1-2 . Th e Interi mHW C MAC T standar drequire s al l CMS' s b e installe di n location s tha t provid e representativ e measurement s o f emission s o r

proces s parameters . Al l CM S

6f Tabl e 1- 2 C M S Instrumen tSpecification 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 dFeedrat e Mas s Flowmete r FT-21 5 Micr o Motio n D 40S-S S 0-3,600 lb/h r Fee dLin e Hig h BT U Liqui dDirec t

Injectio n Feedrat e Scal e WT-215D I Weigh-Troni x WI-.13 0 0-60,000 lb Fee dLin e Lo w BT U Liqui dFeedrat e Mas s Flowmete r FT-21 6 Micr o Motio n D 40S-S S 0-3,600 lb/hr Fee dLin e Lo w BT U Liqui dDirec t

Injectio n Feedrat e Scal e WT-215D I Weigh-Troni x WI-.13 0 0-60,000 lb Fee dLin e Specialt y Fee dWeight Weig h Scal e WT-20 4 Toledo 8140 EX P 0-4,000 l b #20

4 Specialt

y Feede r Drumme dSolid s Fee dWeight Weig h Scal e WT-21 0 Toledo A14 0 0-40 0 l b Soli dCharg e

Conveyo r Cylinde r Ga s Feedrat

e d

P Cel l FT-21 7 Yokogaw a YA11 F 0-1 0 in . w.c . (0-6 0 lb/min ) Cylinde r Gas Fee dSyste

m PC C Temperatur

e Type K

Thermocoupl e TT-200A/ B Modico n B883-20 0 0-2500 ° F Primar y Chambe r SC C Temperatur

e Type K

Thermocouple TT-219A/ B Modico n B883-20 0 0-2500 ° F Secondar y Chambe r PC C Pressur

e Pressur e Transmitte

r PT-20 0 Rosemon t 1151DP -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 Inlet

Temperatur

e Type K Thermocouple TT-27 0 Modico n 833-200 0-250 0 ° F SD A Outle t Combustio n Ga s Flo w Rat e dPCel l FT-28 3 Rosemoun t 1151D R 0-20,000 acf m Stack Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-28 9 COS A ZFN-11YA1-2Z 1 0-25 % CEM S Buildin g Stac k Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare d Photomete

r AT-288 E EcoChe m MC 3 0-20 0 / 0-300 0 ppm v CEM S Buildin g Stack Hydroge n Chlorid e Concentratio n Multicomponent Infrare d Photomete

r AT-288 E EcoChe m MC 3 0-1000 ppm v CEM S

Buildin g Stac k Ga s Moisture Concentratio n Multicomponent Infrare d Photomete

r AT-288 E EcoChe m MC 3 0-60 % CEM S Buildin g Lim e Slurr

y Flo w Rat

e Mag . Flowmete r FT-28 8 Fischer & Porte r 10D147 5 0-1 0 GP M SD A Penthous e Lim e Slurry Densit

y Densit

y Transduce r AT-968 Solartro n Mobre y 784 6 0-10 0 Lb/Ft 3 SD A Penthous e

7Tabl e l-2(continued ) CM S Instrumen tSpecification 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 dFeedrat e Mas s Flowmete r FT-31 5 Micr o Motio n DS-04 0 0-3,60 0 lb/h r Fee dLin e Hig h BT U Liqui dDirec t

Injectio n Feedrat e Scal e WT-315D I Weigh-Troni x WI-13 0 0-60,000 l b Fee dLin e Lo w BT U Liqui dFeedrat e Mas s Flowmete r FT-31 6 Micr o Motio n DS-04 0 0-3,60 0 lb/h r Fee dLin e Lo w BT U Liqui dDirec t

Injectio n Feedrat e Scal e WT-315D I Weigh-Troni x WI-13 0 0-60,000 lb Fee dLin e Specialt y Fee dWeight Weig h Scal e WT-30 4 Toledo AI4 0 EX P 0-2,000 lb #30 4 Hoode d Feede r Drumme dSolid s Fee dWeight Weig h Scal e WT-31 0 Toled o A14 0 0-40 0 lb Soli dCharg e

Conveyo r PC C Temperatur

e Type K

Thermocoupl e TT-300A/ B Modico n 883-200 0-250 0 ° F Primar

y Chambe r SC C Temperatur

e Typ e K

Thermocouple TT-319A7 B Modico n 883-200 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 dLin e TR V Positio n Positio n Switc h ZS-32 4 Square- D 900 7 CG2B 2 open/clos e Emergenc y Stac k Baghous e Inlet

Temperatur

e Type K

Thermocoupl e TT-37 0 Modico n 833-200 0-250 0 ° F SD A Outlet Combustio n Ga s Flo w Rat e dPCel l FT-38 3 Rosemoun t 115 1 D R 0-20,000 acf m Stack Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-38 9 COS A ZFN-11YA1-2Z 1 0-25 % CEM S Buildin g Stac k Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare d Photomete

r AT-388 E EcoChe m MC 3 0-200/0-300 0 ppm v CEM S

Buildin g Stack Hydroge n Chlorid e Concentratio n Multicomponent Infrare d Photomete

r AT-388 E EcoChe m MC 3 0-100 0 ppm v CEM S

Buildin g Stac k Ga s Moisture Concentratio n Multicomponent Infrare d Photomete

r AT-388 E EcoChe m MC 3 0-60 % CEM S Buildin g Lim e Slurr

y Flo w Rat

e Mag . Flowmete r FT-38 8 Fischer & Porte r 10D147 5 0-1 0 GP M SD A Penthous e Lim e Slurry 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

8Tabl e 1 (continued ) C M S Instrumen tSpecification s Applicatio

n Instrumen t Ta

g Numbe r Manufacture

r Mode

l Operatin

g Rang e Locatio

n UnitNo . 4 Wast e Feedrat e t o X-1 0 Nozzl e Mas s Flowmete r FT-12 9 Micr o Motio n DS10.0 S 128 0-7,000 lb/h r Fee dLin 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 0-6,000 lb/h r Fee dLin 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 0-8,000 lb/hr Fee dLin 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 0-7,000 lb/h r Fee dLin e Cla mShel l Fee dWeight (shredded solids ) Loa dCel l WT-00 1 Toled o 8140 0-2,000 l b Ra mFee d Hoppe r Dru mConveyo r

Solid s Weight Loa dCel l WT-014 A Toled o 8140 0-1,000 lb Dru m Conveyo r Auxiliar y Conveyo r

Solid s Weight Loa dCel l WT-14 B Toled o 8140 0-20 0 lb Auxiliar y

Conveyo r PC C Temperatur

e Pyromete r TT-305A/ B Irco n Modline 4 44-99-F

1-0- 1 0-3,000 ° F Kil n Outlet SC C Temperatur

e Type R

Thermocoupl e TT-317A/ B Chesse l 351 0 0-3,000 ° 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 . Kil n Hoo d Surg e Ven t

Positio n Positio n Switc h ZSC-02 6 Square- D 9007CG2B 2 open/clos e Kil n 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 .

System Carbo n Injectio n Carrier

Ga s Suppl y Pressur

e Pressur e Switc h PSL-438 A Dwyer 333 0 Tri p Points : ± 5 in . w.c . Carbo n

Injectio n Lin e Carbo n Feede

r Discharg e Pressur

e Pressur

e Switc h PSH-438 B Dwyer 321 5 Tri p Points : < 3 psi g > 1 3 psi g Carbo n

Injectio n Lin e

9Tabl e 1 (continued ) C M S Instrumen tSpecification 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 Outlet

Temperatur

e (Baghous e Inlet

Temperature) Typ e K

Thermocouple TT-417A/ B Modico n B883-20 0 0-2,50 0 ° F SD A X-1 8

Outle t SD A X-1 9 Outlet

Temperatur

e (Baghous e Inlet

Temperature

) Type K Thermocouple TT-418A/ B Modico n B883-20 0 0-2,500 ° F SD A X-1 9 Outle t Combustio n Ga s Flowrate PitotTube/dPCel l FT-559A/ B Automatio n Servic e 1151DRF228 3 0-55,000 acf m Stack Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-560A/ B COS A ZFN-11YA1-2Z 1 0-20 % CEM S Buildin g Stack Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare d Photomete

r AT-556 E EcoChe m MC 3 0-20 0 / 0-300 0 ppm v CEM S Buildin g Stac k Hydroge n Chlorid e Concentratio n Multicomponent Infrare d Photomete

r AT-556 E EcoChe m MC 3 0-1000 ppm v CEM S

Buildin g Stack Ga s Moisture Concentratio n Multicomponent Infrare d Photomete

r AT-556 E EcoChe m MC 3 0-60 % CEM S Buildin g

Lim e Slurry Flo w Rat

e Mag . Flowmete r FT-61 5 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 DIT-60 9 Solartro n Mobre y 784 6 0-10 0 Lb/Ft 3 Lim e Sil o

1 0operatin g paramete r measuremen t

device s a

t th e Veoli afacilit y ar e installe di n complianc e wit h thi s requirement . A descriptio n o f th e type s o f

CM S instrumentatio n follows : Mass/Feedrat e Monitors : Liqui dwast e feedrate s fro mtank s ar e measure db y corioli s mas s flowmeters . Direc t

injec t liqui dfeedrate s fro mtanke r truc k ar e calculate dusin g th e continuousl y monitore dweigh t

o f th e tanker . Al l soli dwast e charge s ar e weighe dusin g ascale/loa dcel l prio r t o bein g fee dt o th e incinerator . Thes e measurement s ar e use dt o calculat e pumpabl e waste , tota l waste , an dconstituen t feedrates . Fo r Uni t 4 , th e outpu t

o f acalibrate dfeede r

i s utilize dt o calculat e th e feedrat e o f powdere d activate dcarbon , whic h i s injecte dint o th e plenu mupstrea mofth e baghouses . Pressure/Differentia l Pressur e Monitors : Primar y combustio n chambe r pressur e i s measure d b y diaphrag mactuate dpressur e transmitters . Th e positio n o f th e dampe r

immediatel y upstrea m o f th e I D fa n i s varie dt o contro l stac k ga s flowrat e an dt o maintai n kil n combustio n chambe r negativ e pressur e (draft) . Th e primar y combustio n chambe r pressur e i s interlocke dwit h wast e feeds . Fo r Uni t 2 , pressur e dro p i n th e cylinde r ga s feedstrea mi s measure dan dconverte dt o afeedrate . Th e feedrat e i s use dt o calculat e thi s feedstream' s contributio n t o th e chlorine , lo w volatil e metals , an dsemivolatil e metal s feedrate s t o th e incinerator . Fo r Uni t 4 , pressur e switche s ar e utilize dt o ensur e tha t th e carbo n feede r

discharg e pressure , an d th e carbo n injectio n ai r blowe r discharg e pressur e ar e withi n th e desig n limits . Th e pressur e dro p acros s apito t tub e i n th e stac k

i s continuousl y monitore dan duse dt o calculat e th e stac k

ga s flowrate . Temperatur e Monitors : Fo r Unit s 2 an d3 , redundan t thermocouple s ar e use dt o measur e th e temperatur e i n bot h combustio n chambers . A thermocoupl e i s als o locate da t th e exi t t o th e SD A an di s th e primar y elemen t fo r th e SD A exi t

temperatur e contro l loop . Uni t 4 i s equippe dwit h redundan t pyrometer s i n th e primar y chambe r an dredundan t thermocouple s i n th e secondar y chamber . Eac h SD A outle t i s equippe dwit h redundan t thermocouple s use dfo r temperatur e contro l an dmonitorin g o f th e baghous e inle t

temperature .

1 1Emergenc y Safet y Ven tPositio n Monitors : Th e positio n o f th e emergenc y safet y ven t (ESV ) i s indicate da s ope n o r close db y apositio n transmitter . N o wast e o r fue l ca n b e fe di f

th e ES V positio n 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 r i s locate ddownstrea mo f th e I D fa n an d monitor s th e relativ e particulat e matte r loadin g o f

th e combustio n ga s exitin g th e baghouses . Alarm s an dinterlock s base do n thi s relativ e measuremen t ar e indication s o f

apotentia l ba g lea k o r failure . Procedure s fo r setu p an dadjustment s t o th e ba g lea k detectio n syste mar e no t covere d b y thi s Q C program . Th e Operatio n an dMaintenanc 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 danalyze s stac k ga s fo r

th e concentration s o f carbo n monoxid e (CO) , Hydroge n Chlorid e (HCI) , an d moistur e usin g amulticomponen t infrare dphotometer . Th e oxyge n concentratio n i s analyze d simultaneousl y usin g azirconiu moxid e analyzer . Thes e dat aar e use dt o calculat e th e stac k ga s C O concentratio n o n adr y basis , correcte dt o 7 % O2 . Th e CEM S Q A Pla n provide s additiona l detail s o n th e CEMS .

1 22. 0 CM S CALIBRATIO N AN D PREVENTIV E MAINTENANC E

Thi s sectio n discusse s th e calibratio n an dpreventiv e maintenanc e requirement s t o mee t the requirement s o f

§ 63. 8 (d) . 2. 1 CM S Calibratio n T o ensur e ongoin g complianc e wit h th e Interi mHW C MAC T standard , i t i s essentia l tha t

th e dat acollecte dfro mth e CM S b e measure dan drecorde di n a n accurat e manner . Initia l calibrations , subsequen t calibration , an dCEM S calibration s ar e describe di n thi s section . 2.1.1 Initial

CMS Calibration A s par t o f Veolia' s Qualit y Contro l Program , th e CM S instrument s wer e initiall y calibrate dprio r t o th e Interi mHW C MAC T complianc e date . Calibratio n prio r t o th e complianc e dat e i s require ds o tha t

al l collecte ddat aar e reliabl e an daccurate . Al l initia l calibratio n dat aar e par t o f th e operatin g record . Initia l calibration s o f new/replacemen t

instrument s wil l b e performe dpe r th e manufacture' s writte n procedures . I n lie u o f a n initia l calibratio n fo r new/replacemen t instrument s o r

instrumen t

components , th e facilit y ma y us e amanufacturer' s certification . 2.1.2 Subsequent

CMS Calibration Subsequen t

calibration s o n CM S instrumentatio n wil l b e performe da s neede dan di n accordanc e wit h th e manufacture' s writte n procedures . Calibration s wil l b e performe da s correctiv e measure s fo r

hig h calibratio n drift . Calibration s ma y b e require dwhe n restorin g CM S instrument s afte r

maintenanc e o r

repairs . Al l calibratio n adjustment s wil l b e documente db y record s ofth e calibratio n drif t determine dbefor e an dafte r th e instrumen t

wa s serviced . Som e instrument s suc h a s differentia l pressur e cell s mus t b e remove dfro mservic e an dbenc h calibrated . T o minimiz e downtim e thes e instrument s ma y b e replace dwit h acalibrate dspare . Th e Uni t

4 primar y combustio n chambe r pyrometer s wil l b e replace dat leas t annuall y wit h a factor y calibrate dpyrometer . Electroni c check s an dreplacement s o f thermocouple s wil l b e performe dpe r

th e facility' s Thermocoupl e Calibration , Operation , an dReplacemen t Procedure . A calibratio n recor dfor mi s availabl e fo r eac h CM S instrumen t an dwil l b e use dt o documen t calibratio n audits , calibrations , an dreplacements . Th e mos t recentl y complete dcalibratio n recor ddocument s tha t th e instrumen t

i n servic e meet s th e qualit y contro l criteri ase t fort h b y thi s program . Thes e calibratio n record s contai n "calibratio n notes " whic h provid e th e instrumen t technicia n wit h procedure s specifi c t o agive n instrument . Th e calibratio n recor dform s fo r CM S instrument s ar e incorporate di n thi s Q C Progra mb y reference .

1 32.1.3 CEMS Calibration Audits and Calibration CEM S QA/Q C procedure s ar e provide db y th e Continuous Emission Monitoring System Quality Assurance Plan. Thes e procedure s ar e maintaine da t th e facilit y an ddescrib e th e requirement s fo r CEM S drif t

checks , audits , calibrations , preventiv e maintenance , an drecordkeeping . 

### 2. 2 CM S Calibration Audit s C M S calibratio n audit s ar e performe dt o determin e th e calibratio n drif t (CD ) o f

CM S instruments . Calibratio n Drif t (CD ) i s th e bia s betwee n th e CM S instrumen t readin g an da calibratio n reference . Tabl e 2- 1 present s th e requirement s fo r CM S calibratio n audits . Eac h C M S instrumen t

wil l b e subjecte dacalibratio n audi t a t th e frequenc y indicate di n Tabl e 2-1 . Th e calibratio n audi t wil l b e performe da t th e low-leve l (zero ) an dhigh-leve l check s indicated . Th e calibratio n chec k wil l confir mtha t

al l proces s variabl e indication s (e.g. , loca l reading , contro l roo mdisplay ) a t th e high-leve l valu e agre e wit h th e calibratio n referenc e withi n Vi o f th e require dtolerance . Calibratio n adjustments/correctiv e action s mus t b e take n i f

thi s calibratio n drif t i s greate r

tha n X A o f th e require dtolerance . I f th e calibratio n drif t exceed s th e require d tolerance , th e instrumen t i s considere dout-of-control . Sectio n 4. 0 describe s th e correctiv e action s fo r

out-of-control , inoperative , an dmalfLinctionin g CMS . I f th e accurac y o f

aCM S instrumen t

i s i n question , th e C D i s determine dan ddocumente dprio r t o performin g maintenance , repairs , o r adjustments . Th e troubleshooting/calibration s o f CM S instrument s wil l b e performe di n amanne r consisten t

wit h th e manufacturer' s writte n procedure s an drecommendations . Th e C D determine dafte r calibrations/correctiv e action s hav e bee n take n wil l documen t

th e effect s o f

th e adjustment s an ddemonstrat e tha t th e instrumen t

i s performin g properly . Calibratio n record s wil l documen t CD , whic h i s a n indicato r o f th e stabilit y o f

th e CM S calibratio n ove r

time . Th e amoun t

o f drif t an dstabilit y i s dependan t o n th e typ e o f

instrumen t an dth e calibratio n frequency . Veoli ama y increas e o r decreas e th e frequenc y o f particula r calibratio n audit s t o th e exten t warrante db y a n assessmen t o f a n instrument' s stability . Veoli a wil l maintai n regularl y schedule dcalibratio n audi t interval s fo r

eac h CM S instrument . Calibration s wil l b e performe dt o preven t excessiv e C D an dt o maintai n th e vahdit y o f th e dat a collecte dfro mth e monitorin g system .

1 4

### T L .2- 1 C M S Calibratio n Audi tRequirement 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 t No . 2 Hig h BT U Liqui dFeedrat 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 dDirec t

Injectio n Feedrat e Scal e WT-215D I Quarterly 01 b 25,000 lb 10 % Lo w BT U Liqui dFeedrat 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 dDirec t

Injectio n Feedrat e Scal e WT-215D I Quarterly 01 b 25,00 0 l b 10 % Specialt y Fee dWeight Weig h Scal e WT-20 4 Quarterly 01 b -50 0 l b 10 % Drumme dSolid s Fee dWeight Weig h Scal e WT-21 0 Quarterly 01 b -5 0 l b 10% Cylinde r Ga s Feedrat

e dPCel l FT-21 7 Annuall y 0 in . w.c . 1 0 in . w.c . 10% Primary Combustio n Chambe r Temperatur

e Typ e K Thermocoupl e TT-200A/ B Refe r t o th e Thermocoupl e Calibration , Operation , an dReplacemen

t Procedur e Secondar y Combustio n Chambe

r Temperatur

e Type K Thermocouple TT-219A/ B Refe r t o th e Thermocouple Calibration , Operation , an dReplacemen

t Procedur 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-224 Annuall y AWFC O interloc k energize dwhen ope

n Pas s Baghous e Inlet

Temperatur

e Type K Thermocouple TT-27 0 Se e Calibratio n RecordFor m Combustio n Ga s Flo w Rat e d

P Cel l FT-28 3 Annuall y 0-0.05 in . w.c . 0.45-0.5 0 in . w.c . 10 % Lim e Slurry Flo w Rat

e Mag . Flowmete r FT-28 8 Annuall y Ogp m 1-1 0 gp m 10% Lim e Slurry Densit

y Densit

y Transduce

r AT-96 8 Replace , a s required , with factor

y service dtransduce

r Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-28 9 Per CEM S Q A Plan Stack Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare d Photomete

r AT-288 E Per CEM S Q A Plan Stac k Hydroge n Chlorid e Concentratio n Multicomponent Infrare d Photomete

r AT-288 E Per CEM S Q A Plan Stac k Ga s Moisture Concentratio n Multicomponent Infrare d Photomete

r AT-288 E Per CEM S Q A Plan

1 5Tabl e 2- \ ontinued ) CM S Calibratio n Audi tRequirement 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 dFeedrat e Mas s Flowmete r FT-31 5 Annuall y 0- 5 lb/mi n 15-2 5 lb/mi n 10 % Hig h BT U Liqui dDirec t

Injectio n Feedrat e Scal e WT-315D I Annuall y 01 b 25,000 lb 10 % Lo w BT U Liqui dFeedrat 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 dDirec t

Injectio n Feedrat e Scal e WT-315D I Annuall y 01 b 25,000 lb 10 % Specialt y Fee dWeight Weig h Scal e WT-30 4 Quarterly 01 b -20 0 l b 10 % Drumme dSolid s Fee dWeight Weig h Scal e WT-31 0 Quarterly 01 b -5 0 l b 10% Primar y Combustio n Chambe

r Temperatur

e Type K Thermocoupl e TT-300A/ B Refe r t o th e Thermocouple Calibration , Operation , an dReplacemen

t Procedur

e Secondar y Combustio n Chambe

r Temperatur

e Type K Thermocoupl e TT-319A/ B Refe r t o th e Thermocouple Calibration , Operation , an dReplacemen

t Procedur

e Primar y Combustio n Chambe

r Pressur e Pressur e Transmitte

r PT-30 0 Quarterly -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-32 4 Annuall y AWFC O interloc k energizedwhe

n ope n Pas s Baghous e Inlet

Temperatur

e Type K

Thermocoupl e TT-37 0 Refer t o th e Thermocoupl e Calibration , Operation , an dReplacemen

t Procedur

e Combustio n Ga s Flo w Rat e dPCel l FT-38 3 Annuall y 0-0.05 in . w.c . 0.45-0.5 0 in . w.c . 10% Lim e Slurry Flo w Rat

e Mag . Flowmete r FT-38 8 Annuall y Ogp 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 dtransduce

r Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-38 9 Pe r CEM S Q A Plan Stac k Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare d Photomete

r AT-388 E Per CEM S Q A Pla n Stac k Hydroge n Chlorid e Concentratio n Multicomponent Infrare d Photomete

r AT-388 E Per CEM S Q A Pla n Stack Ga s Moisture Concentratio n Multicomponent Infrare d Photomete

r AT-388 E Per CEM S Q A Pla n

1 6Tabl e V. bntinued ) C M S Calibratio n Audi tRequirementi 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 t No . 4 Wast e Feedrat e t o X-1 0 Nozzl e Mas s Flowmete r FT-12 9 Annuall y 0- 5 lb/mi 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 lb 10 % Wast e Feedrat e to 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 mShel l Fee dWeight (shredded solids ) Loa dCel l WT-00 1 Quarterly 01 b -20 0 l b 10 % Dru mConveyo r

Solid s Weight Loa dCel l WT-014 A Quarterl y 01 b -10 0 l b 10 % Auxiliar y Conveyo r

Solid s Weight Loa dCel l WT-14 B Quarterly 01 b -5 0 lb 10% Primar y Combustio n Chambe

r Temperatur

e Pyromete r TT-305A/ B Replac e a t leas t annually with factor

y calibrate dPyromete

r Secondar y Combustio n Chambe

r Temperatur

e Type R Thermocoupl e TT-317A7 B Refe r t o th e Thermocouple Calibration , Operation , an dReplacemen

t Procedur e Primar y Combustio n Chambe

r Pressur e Pressur e Transmitte

r PT-30 0 Quarterly -9. 0 t o -8. 0 in . w.c . 0 t

o 1. 0 in . w.c , 10 % Surge Ven t

Positio n Positio n Switc h ZS-02 6 Annuall y AWFC O interloc k energize dwhen ope

n Pas s ES V Positio n Positio n Switc h ZS-32 4 Annuall y AWFC O interloc k energize dwhen ope

n Pas s Carbo n Feedrat

e Feede r WT-43 8 Quarterly 0 lb/mi n 6-3 0 lb/mi n 10% Carbo n Injectio n Carrier

Ga s Lo w Pressur e Pressur e Switc h PSL-438 A Annuall y Energiz e Switc h Pas s Carbo n Injectio n Carrier

Ga s Hig h Pressur

e Pressur e Switc h PSH-438 B Annuall y Energiz e Switc h Pas s

1 7

### Tabl e 2- . ontinued

) CM S Calibratio

n AuditRequirement

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 t No . 4 (continued ) SD A X-1 8 Outlet

Temperatur

e (Baghous e Inlet

Temperature) Type K

Thermocouple TT-417A/ B Refer t o th e Thermocouple Calibration , Operation , an dReplacemen

t Procedur

e SD A X-1 9 Outlet

Temperatur

e (Baghous e Inlet

Temperature) Typ e K

Thermocoupl e TT-418A/ B Refer t o th e Thermocoupl e Calibration , Operation , an dReplacemen

t Procedur

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 Slurry Flo w Rat

e Mag . Flowmete r FT-61 5 Annuall y 0 gp m 1-1 0 gp m 10% Lim e Slurry Densit

y Densit

y Transduce

r D±T-60 9 Replace , a s required , wit

h factor y service dtransduce

r Stack Ga s Oxyge n Concentratio n Zirconiu mOxid e Analyze r AT-560A/ B Per CEM S Q A Plan Stack Ga s Carbo n Monoxid e Concentratio n Multicomponent Infrare dPhotomete

r AT-556 E Per CEM S Q A Plan Stack Hydroge n Chlorid e Concentratio n Multicomponent Infrare dPhotomete

r AT-556 E Per CEM S Q A Plan Stack Ga s Moisture Concentratio n Multicomponent Infrare dPhotomete

r AT-556 E Per CEM S Q A Plan

1 82. 3 Preventiv e Maintenanc e

Veoli atake s dail y proactiv e measure s t o assur e tha t potentia l problem s wit h th e CM S ar e quickl y identifie dan davoided , i f possible . Dail y maintenanc e check s include :

• Verificatio n tha t

proces s variable s ar e reasonabl e

• Compariso n o f

reading s fro mredundan t instrument s -
• Cleanin g an dvisua l chec k o f monitorin g equipmen t

• Communicatio n betwee n operator s an dinstrumen t technician s Thes e check s ar e documente do n adail y logshee t fo r eac 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 fo r

routin e repair s o f

th e affecte dCM S equipmen t ar e mad e readil y availabl e onsite . A spar e part s inventor y fo r eac h componen t

o f th e CM S i s include di n th e record s maintaine db 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 di n the facility' s Operatio n an dMaintenanc e Pla n an dth e CEM S Q A Plan .

1 93. 0 CM S RECORDKEEPIN G AN D REPORTIN G

Thi s sectio n discusse s recordkeepin g an dreportin g requirement s fo r CM S instrumentatio n a s specifie db y §63.1211 . 3. 1 Recordkeepm g Veoli awil l follo w the recordkeepin g requirement s a s specifie di n § 63.10(b) , includin g th e semiannua l exces s emission s an dCM S performanc e report . Veoli awil l maintai n thes e record s o f

CM S dat afo r

aminimu mo f

5 year s followin g th e dat e o f eac h occurrence , measurement , maintenance , correctiv e action , report , o r record . A t

a minimum , th e mos t

recen t 2 year s o f

dat awil l b e retaine donsite . Belo w i s abrie f summar y o f

thes e requirements . Veoli awil l maintai n record s o n th e following :

• Th e occurrenc e an dduratio n o f eac h startup , shutdown , o r malfunctio n o f operation . • Th e occurrenc e an dduratio n o f eac h malfunctio n o f th e ai r pollutio n contro l an dmonitorin g equipment . Maintenanc e performe do n th e ai r pollutio n contro l an dmonitorin g equipmen t

• Action s take n durin g period s o f startup , shutdown , an dmalfunctio n (includin g correctiv e action s t o restor e th e proces s o r ai r pollutio n contro l syste mt o norma l operation ) whe n suc h action s ar e differen t th e procedure s outline di 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 di n whic h aCM S i s malfunctionin g o r inoperativ e (includin g out of-contro l periods )

• Al l require dmeasurement s neede dt 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 dopacit y an dvisibl e emissio n observation s

• Al l CM S calibratio n check s

• Al l adjustment s an dmaintenanc e performe do n CM S

• Al l require dCM S measurement s (includin g dat arecorde ddurin g unavoidabl e C M S breakdown s an dout-of-contro l periods )

• Th e dat e an dtim e identifyin g eac h perio ddurin g whic h th e CM S wa s inoperativ e excep t

fo r zer o (lo w level ) an dhig h leve l check s

20• Th e dat e an dtim e identifyin g eac h perio ddurin g whic h th e CM S wa s out-of

contro l a s define db y § 63.8(c)(7 )

• Th e specifi c identificatio n (dat e an dtim e o f commencemen t

an dcompletion ) o f eac h perio do f

exces s emission s an dparamete r monitorin g exceedances , a s define di n th e relevan t standard , tha t

occur s durin g period s othe r tha n startup , shutdowns , an dmalfunctions . • Th e natur e an dcaus e o f an y malfunctio n

• Th e correctiv e actio n take n o r preventiv e measure s adopte d

• Th e natur e o f

th e repair s o r

adjustment s t o th e CM S tha t wa 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 t ar e par t

o f qualit y contro l progra mdevelope dan d implemente dfo r

CM S unde r

§ 63.8(d) . A l l CM S instrumentatio n wil l b e operate do n acontinuou s basis . Th e detecto r respons e wil l b e evaluate da

t leas t ever y 1 5 seconds , an dthes e value s wil l b e use dt o calculat e regulate dparameters . Fo r parameter s interlocke dwit h th e AWFC O syste mo n a n hourl y rollin g averag e basis , ra w dat awil l b e average dan drecorde da t leas t onc e pe r

minute . On e minut e average s wil l b e use dt o calculat e th e hourl y rollin g averages . Th e pumpabl e waste , tota l waste , an dconstituen t feedrat e operatin g paramete r limit s ar e base s o n rollin g total s i n lie u o f

rollin g averages . A n integra l par t

o f th e CM S i s th e dat aacquisitio n an ddat ahistoria n systems , whic h record s al l operatin g dat agenerate db y th e CM S instruments . Th e dat ahistoria n an d associate darchiv e file s ar e par t o f th e operatin g record . CM S instrumen t calibrations , maintenanc e activities , an dcorrectiv e action s ar e recorde dan dkep t i n th e operatin g record . Al l dat acollecte ddurin g CM S PET s ar e recorde dan dkep t i n th e operatin g record . 3. 2 Reportin g Veoli awil l follo w th e reportin g requirement s a s specifie di n § 63.10 . I n addition , Veoli a wil l develo p an dinclud e i n th e operatin g recor daDocumentatio n o f Complianc e (DOC ) pe r § 63.1211(c) . Th e DO C mus t includ e asigne dan ddate dcertificatio n tha t th e CEM S an dCM S ar e installed , calibrated , an dcontinuousl y operatin g i n complianc e wit h th e requirement s o f

Subpar t EEE .

2 1Ra w dat afro mth e CM S wil l b e collected , reduce da s describe di n § 63.8(g) , an d

include di n th e CM S PE T report . Thi s dat awil l b e analyze dt o determin e complianc e wit h th e HW C MAC T an dth e result s wil l b e submitte da s par t o f th e notificatio n o f complianc e require db y § 63.1207(j) . Th e conten t

an ddeadlin e requirement s fo r th e exces s emission s an dmonitorin g syste m performanc e report s ar e specifie di n § 63.10(e)(3)(v) . Th e requirement s fo r th e summar y repor t ar e give n i n § 63.10(e)(3)(vi) . A s note di n § 63.10(e)(3)(vii) , Veoli ai s require dt o onl y submi t th e summar y repor t

i f th e tota l duratio n o f

exces s emission s o r

proces s o r

contro l syste mparamete r exceedance s fo r th e reportin g perio di s les s tha n on e percen t o f th e tota l operatin g tim e fo r th e reportin g period , an dCM S downtim e fo r th e reportin g perio di s les s tha n fiv e percen t o f th e tota l operatin g tim e fo r

th e reportin g period . Conversely , additiona l reportin g i s require db y § 63.10(e)(3)(viii ) i f

th e tota l duratio n o f exceedances , o r

th e tota l CM S downtim e durin g th e reportin g period , i s greate r tha n th e allowabl e percentag e o f th e reportin g period . Tabl e 3- 1 provide s alis t o f Veolia' s reportin g requirements .

2 2Tabl e 3- 1 Reportin g Requirement s

Regulator y Citatio n Descriptio n Frequenc y § 63.1211(c ) Recor dDocumentatio 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 t ha s bee n issued , owne r operato r mus t submi t result 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 ) Afte r Titl e V permi t

ha s bee n issued , owne r operato r mus t submi t result s o f

require dperformanc 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 di n writte n extensio n o f complianc e § 63.10(d)(5)(i ) Periodi c startup , shutdown , an dmalfunctio n report s

(durin g reportin g period ) Submitte d simultaneou s wit h exces s emissio n repor t § 63.10(d)(5)(H ) Startup , shutdown , an dmalfunctio n report s whe n

action s ar e take n tha t ar e inconsisten t

wit h SSMP . 2 workin g day s fro m commencemen t

o f action , followe dwit h a lette r explainin 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 performanc e repor t Semiannuall y - b y the 30t h da y followin g th e en do f eac h calenda r hal f performanc e tes t

2 34. 0 CM S CORRECTIV E ACTION S

I f aCM S i s foun dt o b e out-of-control , inoperative , o r malfunctioning ; correctiv e action s mus t b e take n t o retur n th e CM S t o norma l operation . Definition s use di n determinin g th e typ e o f

correctiv e actio n require dar 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 r high-leve l calibratio n drif t exceed s tw o time s th e applicabl e C D specificatio n i n th e applicabl e performanc e specificatio n o r

procedure ; o r

• Th e CM S fail s aperformanc e tes t audit , relativ e accurac y audit , relativ e accurac y tes t

audit , o r

linearit y tes t

audit . Th e onl y applicabl e performanc e specificatio n t o th e CM S i s Performanc e Specificatio n (PS ) 4 B o f

4 0 CF RPar t

63 , Appendi x B . P S 4 B applie s t o th e 0 2an dC O CEMS . Th e requirement s o f

P S 4 B an dadditiona l requirement s Veoli aimpose s o n th e CEM S ar e detaile di n th e CEM S Q A Plan . I n th e absenc e o f promulgate dperformanc e specificatio n applicabl e t o non-CEM S CM S instruments , Veoli aha s self-impose dahigh-leve l C D specification , a s describe di n Sectio n 2.0 . Whe n aCM S i s out-of-control , Veoli awil l tak e th e necessar y correctiv e actio n an dshal l repea t al l necessar y test s whic h indicat e tha t th e syste mi s out-of-control . Correctiv e action s an dretestin g wil l continu e unti l th e CM S i s returne dt o norma l operation . Th e beginnin g o f

th e out-of-contro l perio di s th e hou r tha t th e calibratio n drif t

indicate s tha t th e CM S ha s exceede dit s performanc e specifications . Th e en do f th e out-of-contro l perio di s th e hou r

followin g th e completio n o f correctiv e actio n an dsuccessfu l demonstratio n tha t

th e CM S i s withi n it s allowabl e limits . Durin g th e perio dth e CM S i s out-of-control , recorde ddat ashal l no t b e use di n dat aaverage s an dcalculations , o r t o mee t an y dat aavailabilit y requiremen t establishe dunde r

thi s part . Veoli awil l submi t

al l informatio n concernin g out-of-contro l periods , includin g star t an d en ddate s an dhours , an ddescription s o f correctiv e action s taken , i n th e exces s emission s an dcontinuou s monitorin g syste mperformanc e repor t require db y § 63.10(e)(3) . Malfunction: Fo r

us e i n thi s plan , malfunctio n i s define da s an y sudden , infrequent , an d no t reasonabl y preventabl e failur e o f ai r pollutio n contro l o r monitorin g equipment .

2 4Malfunctio n als o include s th e failur e o f aproces s o r

an y proces s equipmen t t o operat e i n anorma l o r

usua l manner . Failure s tha t ar e cause di n par t

b y poo r

maintenanc e o r careles s operatio n ar e no t malfunctions . Th e Program of

Corrective Actions for Malfunctions i s Attachmen t 4 ofth e SSM P Plan . Thi s progra maddresse s ho w th e incinerato r wil l b e operate dan dmaintaine ddurin g malfunctions . I n thi s program , potentia l malfunction s ar e liste dfo r eac h portio n o f

th e incinerato r

system . Th e malfunction s ar e event s tha t ar e recognize db y th e operator , o r indicate db y a n alarm , an dthreate n t o caus e a n exceedance . I n th e respons e t o th e malfunctio n and/o r

alarms , th e operato r

wil l appl y discretio n an dattemp t t o maintai n th e incinerato r

syste mwithi n regulator y limits . I n th e progra mo f correctiv e actions , potentia l cause s o f

eac h malfunctio n ar e listed . Th e operato r wil l utiliz e proces s knowledge , jo b experience , and , i f needed , assistanc e fro mothe r personne l t o identif y th e caus e o f

th e malfunction . Fo r eac h potentia l cause , action s t o correc t th e failur e ar e listed . Th e correctiv e action s prescribe dma y requir e th e collaboratio n o f multi

discipline dpersonne l wh o ar e qualifie dt o retur n th e incinerato r syste mt o prope r

workin g condition s (i.e. , maintenanc e personnel , instrumen t technicians , engineering )

2 5

## CONTINUOU S EMISSION S MONITORIN G SYSTE M QUALIT Y ASSURANC E PLA N

Preparedfor : Veoli aE S Technica

l Solutions , LL C Sauget , Illinoi s

Prepare dby : Frankli n Engineerin g Group , Inc . Franklin , Tennesse e

Octobe r 200 8TABL E O FCONTENT S

1. 0 INTRODUCTIO N AN D BACKGROUN D 1

1. 1 DESCRIPTIO N O FCEM S 1 1. 2 OVERVIE W O FREGULATOR 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 FTH 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



# c iINDE X O F TABLE S f TABL E 1 - 1 REGULATOR Y REQUIREMENT S FO RTH E CEM S Q C PROGRA M AN D TH E CEMSQAPLA 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



# C i i1.0 INTRODUCTIO N

Veoli aE S Technica l Solutions , LL C (Veolia ) own s an doperate s tw o fixedheart h incinerator s (Unit s 2 an d3 ) an datransportabl e rotar y kil n incinerato r (Uni t 4 ) a t it s facilit y locate di n Sauget , Illinois . Thes e incinerator s ar e subjec t t o th e Nationa l Emission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r Hazardou s Wast e Combustor s (HWCs) , Par t 63 , Subpar t

EE E (§§63.120 0 t o 63.1221) . Th e NESHA P fo r HWC s specifie s emission s standard s whic h reflec t emission s performanc e o f maximu m achievabl e contro l technologie s (MACT) , an di s commonl y referre dt o a s th e HW C MACT . Fo r eac h incinerator , Veoli autilize s acontinuou s emission s monitorin g syste m(CEMS ) fo r demonstratin g on-goin g complianc e wit h th e carbo n monoxid e (CO ) emissio n standard . Thes e CEM S ar e subjec t t o th e requirement s o f the Appendi x t o 4 0 CF RPar t 63 , Subpar t

EEE— Qualit y Assurance Procedures for Continuous Emissions Monitors Used for Hazardous Waste Combustors. Thi s pla n ha s bee n develope dpe r th 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 t

th e CEM S generates , collects , an dreport s vali ddat atha t i s precise , accurate , complete , an do f aqualit y tha t

meet s th e requiremen t o f th e HW C MAC T Standar dan dth e applicabl e performanc e specification . 1. 1 Descriptio n o f CEM S Eac h incinerato r

i s equippe dwit h a n EcoChe mAnalytic s MC 3 CEMS , whic h consist s o f th e followin g majo r

components :

• Heate dstac k

sampl e prob e

• Heate dtrace dumbilica l

• Heate dsampl e pum p

• EcoChe mMC 3 multicomponen t infrare d(IR ) ga s analyze r

• Zirconiu moxide-base doxyge n analyze r

• Syste mcontrolle r an ddat aacquisitio n syste m Hot , we t

stac k ga s i s draw n throug h th e heate dstac k sampl e prob e an dhea t trace d umbilica l usin g aheate dsampl e pump . Th e samplin g locatio n i s downstrea mo f th e induce ddraf t

(ID ) fan . Th e umbilica l supplie s instrumen t ai r t o th e filter

prob e t o allo w fo r automate dperiodi c blowback . I t als 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 dat approximatel y 185° C throug h the

1samplin g equipmen t an danalyze r

sampl e cel l t o preven t th e remova l o f

pollutant s fro m th e sampl e throug h contac t wit h condense dmoisture . Th e sampl e cel l consist s o f multipl e mirror s tha t wer e adjuste dan daligne da t th e factor y t o se t th e pat h lengt h appropriat e fo r th e specifi c application . Th e MC 3 multicomponen t I Rphotomete r

use s aGa s Filte r

Correlatio n analytica l techniqu e t o continuousl y monito r th e stac k

ga s concentration s o f HC I an dCO . Th e Singl e Bea mDua l Wavelengt h analytica l techniqu e i s use dt o continuousl y monito r stac k ga s wate r

vapo r (H 2 0 ) concentrations . A technica l descriptio n an dspecificatio n fo r th e CEM S i s presente di n Sectio n 2. 0 o f th e M C 3 Operations Guide, Section 2.1. 1 document s th e lowes t rang e fo r

eac h componen t an da n accurac y o f

±2 % o f

full-scal e value . Th e lowe r threshol di s 1 % o f

th e lowes t range . Thes e technica l specification s documen t tha t th e CEM S i s capabl e o f meetin g the requirement s o f

th e Appendi x t o Par t 63 , Subpar t

EE E an dPerformanc e Specificatio n 4 B o f 4 0 CF RPar t

60 , Appendi x B . Th e syste mcontrolle r control s th e samplin g syste mtemperatures , purge/blowback , calibratio n checks , dat ahandling , messaging , an dalarms . Th e CEM S controlle r i s integrate dwit h th e incinerato r dat aacquisitio n system , automati c wast e fee dcutof f (AWFCO ) system , an dth e mai n contro l system . A l l thre e incinerator s ar e equippe dwit h COS A mode l ZFN-11YA1-2Z 1 0 2analyzers . Thes e analyzer s ar e zirconiu moxid e cell s an dar e locate ddownstrea mofth e L D fan . 1. 2 Overvie w o f

Regulator y Requirement s Cross-reference s an dsummarie s o f th e applicabl e regulator y requirement s ar e presente d i n Tabl e 1-1 . Thi s tabl e indicate s th e sections , tables , an dfigure s o f thi s documen t

tha t addres s eac h particula r requirement .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 tEE E o f

Par t6 3 Descriptio n CEM S Q A Pla n Sectio n Sectio n 3.1.a. 1 Check s fo r componen t

failures , leaks , an dothe r abnorma l condition s 3. 0 3. 1 Sectio n 3.1.a. 2 Calibratio n o f CEM S 2. 2 Sectio n 3.1.a. 3 Calibratio n Drif t determinatio n an dadjustmen t o f CEM S 2.1,2. 2 Appendi x A Sectio n 3 . l.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 o f CEM S (includin g spar e part s inventory ) 3. 0 Appendi x A Sectio n 3.1.a. 6 Dat arecording , calculations , an dreportin g 4. 1 5. 0 Sectio n 3.1.a. 7 Check s o f recor dkeepin g 5. 0 Sectio n 3.1.a. 8 Accurac y audi t procedures , includin g samplin g an danalysi s method s 2.3,2. 5 Appendi x A Sectio n 3.1.a. 9 Progra mo f correctiv e actio n fo r malfunctionin g CEM S 3. 4 Sectio n 3.1.a . 1 0 Operato r trainin g an dcertificatio 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 list s an ddat asheet s Appendi x A Sectio n 3.2. 4 Preventiv e maintenanc e procedure s 3. 0 

# (
3Tabl 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 tEE E o f

Par t6 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 dlocatio n o f al l record s an dreport s 5. 0
Sectio n 3.2. 6 Provision s fo r revie w o f

th e CEM S data ; revision s o r

update 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 ) Calibratio n Drif t 2. 1 Appendi x A Sectio n 4. 3 Dail y Syste mAudi t 3. 1 Sectio n 4. 4 Dat arecordin g an dreportin g 5. 0 Sectio n 5. 1 Relativ e Accurac y Tes t Audi t (RATA ) 2. 5 Sectio n 5. 2 Absolut e Calibratio n Audi t (ACA ) 2. 3 Sectio n 5. 3 Interferenc e Respons e Tes t (IRT ) 2. 4 Sectio n 5. 4 Excessiv e audi t inaccuracie s Tabl e 2- 1 2. 3 2. 5

f
42. 0 CEM S CALIBRATION S AN D PERFORMANC E

Th e CEM S mus t

b e operated , calibrated , an dmaintaine dt o ensur e conformanc e wit h th e Appendi x t o Par t

63 , Subpar t

EE E an dth e EP A Performanc e Specificatio n 4 B (P S 4B) . Calibratio n drif t

check s an dperformanc e demonstration s ar e performe dperiodicall y o n th e CEM S base do n th e followin g schedule :

• Dail y calibratio n check s fo r determinatio n o f

Calibratio n Drif t

(CD ) an dZer o Drif t (ZD) . • Quarterl y Absolut e Calibratio n Audi t (ACA ) fo r

determinin g calibratio n erro r (CE)for0 2 , CO , an dHCI . • Annua l Relativ e Accurac y Tes t Audi t (RATA ) fo r

determinin g th e CEM S relativ e accurac y (RA ) fo r

C O emissions . Th e procedures , Q C criteria , correctiv e actions , an drecordkeepin g associate dwit h thes e drif t check s an daudit s ar e describe di n thi s section . A summar y o f th e Q C criteri aan d correctiv e action s i s presente di n Tabl e 2-1 . Blan k dat asheet s ar e provide di n Appendi x A . 2. 1 Dail y Drif tCheck s Dail y drif t

check s ar e automaticall y initiate db y th e CEM S controller . Durin g th e automate dcalibratio n sequence , calibratio n gase s ar e injecte dfro mpressurize dcylinder s throug h th e samplin g system . Th e sequenc e start s wit h th e T Ranalyze r zer o ga s tha t

i s fre e o f an y ofth e constituent s analyze db y th e I Ranalyzer . Thi s zer o ga s ma y als o serv e a s th e spa n ga s fo r

th e integrate dO 2 analyzer . Th e zer o ga s flow s throug h th e syste m wit h enoug h tim e allowe dfo r th e analyze r

t o full y respon dt o th e gas . The n th e analyze r respons e t o th e zer o ga s i s recorde dfo r on e minut e an daveraged . Th e nex t calibratio n ga s i n th e calibratio n sequenc e i s th e firs t I Ranalyze r

spa n gas . Thi s spa n ga s i s a calibratio n standar dtha t ha s on e o r

mor e constituen t

concentration s a

t th e analyze r

spa n valu e (thi s ga s ma y als o b e use da s th e zer o ga s fo r th e 0 2analyzer) . Th e firs t spa n ga s flow s throug h th e syste mt o allo w th e analyze r enoug h tim e t o full y respon dt o th e gas . The n th e analyze r

respons e t o th e first

spa n ga s i s recorde dfo r on e minut e an daveraged . Thi s i s the n repeate dfo r th e secon dspa n ga s an dthe n possibl y athir dspa 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 calibratio n sequenc e ha s bee n designe dt o no t excee dth e 2 0 minut e maximu mallowabl e CEM S downtim e whil e burnin g hazardou s waste .

5Tabl e 2- 1 Overvie w o 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 Dail y ± 2 % o f spa n Zer o Adjustmen t

o 2 (25% ) Z D an dC D Dail y ±0.5 % 0 2 Zero/Spa n Adjustmen t

o 2 (25% ) C D Dail y ±1.0 % 0 2 Shu t of f waste , service/calibrate , conduc t A C A o 2 (25% ) Cumulativ e Spa n

Adjustmen t Pe r

Adjustmen t ±1.5 % 0 2 Shu t of f waste , service/calibrate , conduc t AC A o 2 (25% ) C E Quarterly 1 0.5 % 0 2 Shu t of f waste , service/calibrate , conduc t RAT A o 2 (25% )

R A Annuall y 1.0 % 0 2 Shu t of f waste , service/calibrate , repea t RAT A

C O (200 ppm ) Z D an dC D Dail y ± 3 % o f spa n Zero/Spa n Adjustmen t

C O (200 ppm ) C D Dail y ± 5 % o f spa n fo r 6 ou t o f 7 da y Shu t

of f waste , service/calibrate , conduc t AC A C O (200 ppm ) C D Dail y ± 6 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A C O (200 ppm ) Cumulativ e Spa n

Adjustmen t Pe r

Adjustmen t ± 9 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A C O (200 ppm ) C E Quarterl y 1 5 % Shu t of f waste , service/calibrate , conduc t RAT A C O (200 ppm )

R A 2 Annuall y 5 ppmd v @ 7 % 0 2 (Se e Sectio n 2.5 ) Shu t of f waste , service/calibrate , conduc t RAT A Th e ACA s fo r

determinin g th e 0 2an dC O C E ar e conducte dquarterly , excep t i n aquarte r

whe n aRAT A i s conducte dinstead . Th e R A accurac y fo r C O i s base do n th e unit s o f th e C O emissio n standar d(ppmd v @ 7 % 0 2 ) . C O dat acollecte dfro mth e analyze r durin g th e RAT A wil l includ e lo w an do r hig h rang e value s pe r th e norma l operatin g requirements . 6Tabl e 2- 1 (continued ) Overvie w o 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 (300 0 ppm ) Z D an dC D Dail y ±3 % o f spa n Zero/Spa n Adjustmen t
C O (300 0 ppm ) C D Dail y ±5 % o f spa n fo r 

### 6 ou t o f 

### 7 da y Shu t

of f waste , service/calibrate , conduc t AC A C O (300 0 ppm ) C D Dail y ±6 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A C O (300 0 ppm ) Cumulativ e Spa n

Adjustmen t Pe r Adjustmen t ±9 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A C O (300 0 ppm )

C E Quarterly 3 

### 5 % Shu t

of f waste , service/calibrate , conduc t RAT A

HC I (100 0 ppm ) Z D an dC D Dail y ±3 % o f spa n Zero/Spa n Adjustmen t
HC I (100 0 ppm ) C D Dail y ±5 % o f spa n fo r 

### 6 ou t o f 

### 7 da y Shu t

of f waste , service/calibrate , conduc t AC A HC I (100 0 ppm ) C D Dail y ±6 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A HC I (100 0 ppm ) Cumulativ e Spa n

Adjustmen t Pe r Adjustmen t ±9 % o f spa n Shu t

of f waste , service/calibrate , conduc t AC A HC I (100 0 ppm )

C E Quarterly 4 

### 5 % Shu t

of f waste , service/calibrate , conduc t AC A Th e ACA s fo r

determinin g th e 0 2an dC O C E ar e conducte dquarterly , excep t i n aquarte r

whe n aRAT A i s conducte dinstead . A RAT A fo r

HC I ma y b e performe dannuall y i n lie u o f performin g a n AC A i n tha t quarter .



### 7Th e drif t fo r eac h stac k

ga s constituen t

i s determine da s th e differenc e betwee n th e know n constituen t

concentratio n i n th e calibratio n ga s an dth e analyze r reading . Z D i s th e drif t determine dusin g zer o gas . C D i s th e drif t determine dusin g spa n gases . Z D an d C D ar e determine ddail y fo r 0 2 , CO , an dHCI . Z D fo r H 2 0 i s als o detennine ddaily . Th e Z D an dC D ar e recorde db y th e CEM S datalogge r a s apercen t

o f full-scal e deviatio n (Dev%) . Give n tha t th e "spa n value " i s equa l t o th e "full-scale " value , Dev % i s calculate da s follows : 

### Dev% = \Drift%\

^. n , referenceconcetration - analyzer responce , 

### Dnft% = — - 100 span value Fo r C O an d0 2 , i f

Dev % fo r

C D exceed s th e limit s specifie di n th e applicabl e Performanc e Specification s i n 4 0 CF RPar t 60 , Appendi x B , th e analyze r mus t b e calibrated . I f

th e Dev % fo r

C D i s greate r

tha n th e prese t

toleranc e (Tol% ) th e instrumen t technicia n wil l notif y th e incinerato r operato r

an dwast e feed s wil l b e shu t of f unti l conectiv e measure s hav e bee n taken . Th e C D tolerance s fo r bot h O 2 an dC O hav e bee n se t a t th e tw o time s th e performanc e specificatio n limits . A calibratio n failur e alar m indicate s tha t

th e analyze r

i s out-of-contro l an dmus t b e service dan drecalibrated . A n A C A mus t

b e conducte dt o documen t tha t th e analyze r

i s withi n th e performanc e specification s prio r

t o resumin g hazardou s wast e burning . Fo r CO , i f th e Dev % fo r

C D i s greate r

tha n 5 % fo r

6 ou t o f 7 days , the n th e analyze r i s out-of-contro l an dmus t b e service dan drecalibrated . A n AC A mus t b e conducte dt o documen t

tha t th e analyze r

i s withi n th e performanc e specification s prio r t o resumin g hazardou s wast e burning . Simila r requirement s fo r

drif t limit s appl y t o HCI , excep t tha t n o performanc e specification s hav e bee n promulgate dfo r CEM S monitorin g thes e parameters . I n lie u o f limit s specifie db y a n EP A Performanc e Specification , Veoli aha s develope dself

impose dperformanc e specificatio n limit s fo r HCI . Thes e limit s ar e specifie di n Tabl e 2

- 1 . 2.2 Calibratio n Calibratio n o f

th e analyze r

wil l b e conducte dperiodicall y t o ensur e tha t th e result s o f drif t checks , ACAs , o r RATA s mee t

th e applicabl e performanc e specifications . 8Calibratio n fo r eac h I Rchanne l (H 2 0 , CO , an dHCI ) ma y b e performe ddail y durin g th e automate dcalibratio n sequenc e use dt o determin e calibratio n drift . Fo r eac h calibratio n ga s use ddurin g th e automate dsequence , th e automati c calibratio n wil l rese t th e analyze r respons e t o correspon dwit h th e know n referenc e concentrations . An y automate d calibratio n adjustmen t wil l b e mad e immediatel y afte r th e analyze r

respons e t o th e calibratio n ga s i s recorde delectronically . Th e drif t determine dimmediatel y prio r t o a calibratio n adjustmen t i s equa l t o th e magnitud e o f th e adjustment . Th e oxyge n analyze r use s atwo-poin t

calibratio n curve . Th e firs t calibratio n poin t

reset s th e measure d concentratio n o f

ai r t o 20.94% . Th e secon dcalibratio n poin t reset s th e measure d concentratio n o f

alo w concentratio n calibratio n ga s t o it s know n concentration . Thi s calibratio n i s performe dmanually . T o documen t th e calibratio n adjustment , th e actua l measuremen t

at eac h cahbratio n poin t prio r t o adjustmen t

wil l b e recorded . Followin g servic e t o the MC 3 analyze r tha t coul daffec t

it s calibration , eac h I Rchannel , an dth e 0 2analyze r

wil l b e calibrated . Th e CEM S Drif t an dCalibratio n Dat aShee t i n th e Appendi x t o thi s documen t wil l b e use dt o trac k th e cumulativ e spa n adjustment s (i.e. , chang e i n th e cahbratio n factor) . Sectio n 5. 5 ofth e MC 3 CEM S Operations Guide an dSectio n 4. 4 o f

th e MC 3 CEM S System Guide shoul db e referre dt o a s neede dfo r additiona l detai l regardin g calibratio n o f th e CEMS . I f th e cumulativ e calibratio n adjustmen t fo r C D i s thre e time s th e performanc e specificatio n limit s a t an y time , hazardou s wast e burnin g wil l b e cutoff . Th e analyze r wil l b e serviced , recalibrated , an da n AC A wil l documen t tha t hazardou s wast e burnin g ca n recommence . A calibratio n facto r tha t ha s bee n verifie dthroug h a n AC A wil l becom e th e ne w referenc e poin t fo r assessin g th e cumulativ e adjustment s mad e t o correc t fo r calibratio n drift . Th e incinerato r

ca n remai n o n hazardou s wast e durin g CEM S drif t checks , calibrations , purges , an dcorrectiv e action s fo r CEM S failure s provide dtha t th e CEM S downtim e doe s no t excee d2 0 minutes . Durin g thes e times , th e instantaneou s value s use dt o determin e one-minut e average s o f dry , oxyge n correcte dconcentration s o f C O ar e discarded . Thi s allowanc e i s provide db y Sectio n 6. 2 an d6.5. 1 o f th e Appendi x t o Subpar t EEE . Th e applicabl e regulator y requirement s d o no t limi t th e frequenc y tha t

thi s allowanc e ca n b e utilized . Typically , thi s allowanc e wil l onl y b e utilize donc e pe r da y fo r

th e dail y drif t checks . Sinc e th e oxyge n analyze r canno t b e calibrate ddurin g th e automati c calibratio n o f th e I Rchannels , calibratio n o f th e oxyge n analyze r wil l requir e additiona l downtime .I f ather e i s aCEM S failure , th e incinerato r ma y remai n o n hazardou s wast e provide dthat th e CEM S ca n b e restore dwithi n 2 0 minutes . Followin g downtime , th e CEM S mus t b 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 t th e hourl y rollin g averag e (HRA ) fo r C O i s representativ e o f curren t operatin g conditions , CEM S dat avalidit y mus t b e a t leas t 75 % (i.e. , 6 0 vali don e minut e average s pe r 8 0 minute s o f

norma l operations) . 2. 3 Absolut e Calibratio n Audi t A n AC A i s conducte dquarterl y fo r O2 , C O (hig h an dlo w range) , an dHCI . Fo r O 2 an d C O , a n AC A i s no t

conducte di n th e quarte r tha t th e require dannua l RAT A i s performed . Th e AC A i s conducte daccordin g t o th e calibratio n erro r (CE ) tes t

procedur e describe di n th e Performanc e Specification s 4B . Durin g th e ACA , th e analyze r i s challenge dove r eac h rang e wit h EP A Protoco l 1 cylinde r gases . Th e EP A Protoco l 1 cylinde r gase s ar e NIS T traceabl e calibratio n standards . Fo r agive n parameter , th e analyze r respons e i s recorde dat

thre e measuremen t

points . Thi s i s the n repeate dtwic e t o giv e thre e set s o f data . Th e C E at

eac h measuremen t

poin t i s determine da s follows :
CE = FS •100%

wher e di s th e mea n differenc e betwee n th e CEM S respons e an dth e know n referenc e concentratio n an dF S i s th e spa n value . Fo r C O an dHCI , th e C E determine da t eac h measuremen t

poin t canno t excee d5% . Fo r O2 , C E canno t

excee d2% . I f

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 t resum e unti l correctiv e measure s hav e bee n take n an daRAT A demonstrate s tha t th 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 r correct s fo r

interference s usin g additiv e an dmultiplicativ e interferenc e tables . Thes e table s wer e generate dpe r th e manufacturer' s procedur e at th e initia l setu p o f

th e CEM S system . A n Interferenc e Respons e Tes t (IRT ) i s liste di n the Appendi x t o Subpar t EEE , however , th e Performanc e Specificatio n 4 B doe s no t includ e requirement s o r

acceptanc e criteri afo r a n interferenc e respons e test . Veoli awil l perfor m
1 0Interferenc e Respons e Test s a t suc h tim e a s U S EP A specifie s th e tes t procedure s an d acceptabl e criteri afo r a n Interferenc e Respons e Test . 2. 5 Relativ e Accurac y Tes tAudi t Th e Relativ e Accurac y Tes t Audi t (RATA ) i s require dannuall y fo r 0 2an dC O CEMS . Th e Relativ e Accurac y (RA ) tes t procedure s require db y Sectio n 7. 2 o f P S 4 B reference s incorrec t

section s o f

P S 3 (fo r

0 2 ) an dP S 4 A (fo r CO) . Th e applicabl e section s o f 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 . • O 2 referenc e methods : Sectio n 8. 2 o f P S 3

• C O referenc e methods : Sectio n 8. 2 o f P S 4A . • 0 2R A calculations : Sectio n 12. 0 o f P S 3

• COR A calculations : Sectio n 12. 0 o f P S 2

• 0 2R A criterion : Sectio n 13. 2 o f P S 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 dbelow : U S EP A Metho d3/3 A (Stac k Ga s Compositio n an dMolecula r Weight ) Th e samplin g an danalytica l procedure s outline di n thi s metho dwil l b e use dt o determin e th e 0 2compositio n o f th e stac k

ga s durin g th e RATA . Usin g thi s method , aga s sampl e i s extracte dfro mth e stac k at aconstan t

rat e fo r

determinatio n o f

O2 , CO 2 an dmolecula r weight . Th e integrate dgasba g collectio n optio n wil l b e employed . Th e gasbag s wil l b e analyze dusin g a n Orsa t analyzer . A s a n alternative , th e Metho d3 A (instrumenta l analyzer ) metho dmayb e use dfo r analysi s o f

th e sample . U S EP A Metho d4 (Stac k Ga s Moistur e Content ) I f necessary , th e samplin g an danalytica l procedure s outline di n thi s metho dwil l b e use d t o determin e th e moistur e conten t o f th e stac k

ga s durin g th e RATA . Usin g thi s method , aga s sampl e i s extracte dfro mth e stack . Th e ga s passe s throug h aserie s o f impinger s tha t contai n reagents . Th e impinger s ar e connecte di n serie s an dar e containe di n a n ic e bat h i n orde r

t o assur e condensatio n o f th e moistur e i n th e ga s stream . An y moistur e tha t i s no t condense di n th e impinger s i s capture di n th e silic agel , ensurin g tha t al l moistur e ca n b e weighe dan dentere dint o moistur e calculations . U S EP A Metho d1 0 (Carbo n Monoxid e CEMS )
1 1A continuou s emission s monito r wil l b e use dt o continuousl y sampl e exhaus t ga s fo r carbo n monoxid e analysi s a s describe di n EP A Metho d10 . Usin g thi s method , a continuou s ga s sampl e i s extracte dfro mth e exhaus t gas , an di s analyze dfo r carbo n monoxid e (CO ) usin g aLuft-typ e Non-Dispersiv e Infrare dAnalyze r (NDLR) , o r

anothe r equivalen t

analyzer . Thi s samplin g an danalysi s wil l occu r continuousl y throughou t th e duratio n o f

eac h ru n ofth e RATA . Durin g ates t

ru n o f th e RATA , U S EP A referenc e method s ar e utilize dt o obtai n stac k ga s data . Thes e dat aar e use dt o calculat e th e stac k ga s dr y O 2 concentratio n an dth e stac k ga s C O concentratio n correcte dt o seve n percen t oxyge 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) . Th e averag e stac k ga s O 2 (% , dry ) an dC O (ppmdv , @ 7 % 0 2 ) concentrations—a s calculate dfro mth e installe dCEM S ove r th e duratio n o f

th e run—ar e compare dt o th e valu e obtaine dusin g th e referenc e methods . Th e RAT A consist s o f aminimu mo f

9 tes t runs . I f mor e tes t

run s ar e conducted , a t leas t 9 dat aset s wil l b e use dt o determin e RA , an dn o mor e tha n thre e set s o f dat awil l b e rejected . Th e O 2 an dC O R A calculation s an d acceptanc e criteri aar e presente dbelow . RA oxygen <1.0%O 2 ,dry

+ \CC\ RM •100% <10%...forRM> 50ppmdv @ 7% 0 2
+ \CC\ < 5ppmdv@7%0 2 ...for RM

<50ppmdv @ 7% 0 2 where , d = -^(RMj-CEMSi)

n j n = numbe r

o f tes t run s RMt = th e concentratio n determine db y th e referenc e metho dfo r the i t htes t

ru n CEMSi = th e concentratio n determine db y th e CEM S fo r th e i t htes t

ru n CC = th e 2. 5 percen t erro r confidenc e coefficien t (se e Sectio n 12. 4 o f

P S 2 )

I f aRAT 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 t resum e unti l correctiv e measure s hav e bee n take n an daRAT A demonstrate s tha t th e CEM S i s operatin g withi n th e performanc e

1 2specifications . I f C O emissio n level s ar e significantl y low , i t ma y b e difficul t

t o produc e meaningfu l result s usin g th e R A tes t procedure . Unde r

thes e circumstances , Veoli awil l reques t approva l t o utiliz e th e Alternativ e R A Procedur e prescribe db y Sectio n 7. 3 o f P S 4B . .



### 1 33. 0 CEM S MAINTENANC E

Veoli aha s develope dapreventativ e maintenanc e progra mfo r th e CEMS . Thi s progra m include s frequen t

inspection s o f

th e CEM S i n orde r t o identif y potentia l componen t failures , leaks , an ddat aqualit y issues . Th e CEM S preventativ e maintenanc e progra m als o include s schedule dreplacemen t o f critica l component s an dmaintenanc e o f spar e part s inventory . Al l schedule dan dunschedule dmaintenanc e o f th e CEM S wil l b e documente di n aCEM S logboo k maintaine dfo r

eac h incinerator . Sectio n 8. 0 o f th e MC 3 CEM S Operations Guide provide s detail s fo r daily , weekly , monthly , quarterly , an d annua l inspectio n an dmaintenanc e activities . Procedure s an drecordkeepin g fo r the specifi c inspectio n an dmaintenanc e activitie s ar e describe dbelow . 3. 1 Dail y Syste m Audi t Th e Dail y Syste mAudi t includes :

• Revie w o f

th e dail y drif t

chec k dat a

• Inspectio n ofth e recordin g syste m

• Chec k

fo r controlle r

alarm s an derror/warnin g message s

• Chec k

expecte dcalibratio n value s

• Chec k

o f curren t dat astatu s

• Chec k

o f calibratio n ga s cylinde r pressure s

• Chec k

calibratio n ga s pressur e regulato r setting s

• Inspectio n o f

the instrumen t

ai r pressur e

• Inspectio n o f

th e stac k

ga s samplin g syste m Th e Dail y Syste mAudi t Checklis t

wil l b e use dt o documen t th e findings fro mth e dail y syste maudit . A CEM S Drif t an dCahbratio n Dat aShee t wil l b e complete ddurin g th e dail y syste maudi t

i n orde r

t o trac k

an devaluat e drif t

an dadjustment 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 di n sufficien t quantitie s on-sit e t o perfor mroutin e maintenanc e activities . I t i s anticipate dtha t

thes e spar e part s an dtypica l maintenanc e supplie s wil l b e adequat e t o servic e th e CEMS . Som e service s an dreplacemen t o f component s mus t

b e performe db y a n EcoChe mAnalytic s Servic e Enginee r t o avoi d violatio n ofth e syste mcertification .



### 1 4Th e followin g consumabl e part s hav e bee n targete d fo r periodi c inspectio n an d replacemen t

fo r maintainin g th e CEMS :

» Ai r conditione r

filter s fo r

CEM S shelte r

• Instrumen t

ai r coalescin g filter s

• Sampl e pum p Teflo n diaphrag m

• Sampl e pum p Teflo n flappe r valv e

• Sampl e prob e interna l filte r

• Sampl e prob e gasket s

• Probe-ti p filte r Th e followin g spar e part s ar e no t par t o f routin e maintenanc e an dwoul db e replac e b y a n EcoChe mServic e Engineer :

• Cel l fron t

cove r gaske t

• Cel l inle t

filte r

• Cel l window s wit h o-rin g gasket s

• Cel l mirror s Th e CEM S Calibratio n Ga s an dSpar e Part s Lo g i s provide di n Appendi x A an dwil l b e use da s neede dt o kee p trac k o f inventory . 3. 3 Calibratio n Ga s Suppl y an d Certificatio n A summar y ofth e calibratio n gase s neede dt o perfor mth e dail y drif t checks , calibrations , an dACA s i s presente d i n Tabl e 3-1 . Th e numbe r o f ga s cylinder s maintaine don-sit e depend s o n th e specifi c mixtur e o f gase s i n eac h cylinde r an dth e lea dtim e require dfo r placin g orders . A n inventor y o f calibratio n gase s wil l b e conducte di n conjunctio n wit h th e spar e part s inventor y t o ensur e tha t th e appropriat e gase s ar e availabl e fo r use . Certificatio n fro mth e supplie r o f cahbratio n ga s qualit y wil l b e kep t wit h th e mos t

recen t spar e part s inventor y documentation . Eac h calibratio n sequenc e deplete s approximatel y 4 0 psi , an dacylinde r wit h les s tha n 15 0 ps i shoul db e replaced . Th e dail y syste maudi t include s inspectio n o f th e calibratio n ga s cylinde r

pressure s an dwil l b e use dtrac k usag e an dt o predic t

whe n t o reorder .

1 5Tabl e 3- 1 Summar y o f

Concentratio n Requirement s fo r Calibratio n Gase s
Constituen t Q C Paramete r Concentratio n

Requiremen t Accurac y H 2 0 Z D 0 % pe r ga s supplie r o 2 Z D 0 % pe r ga s supplie r o 2 C D 25 % pe r ga s supplie r o 2 A C A 0-2 % E P A Protoco l 1/NIS T Traceabl e o 2 A C A 8-10 % E P A Protoco l 1/NIS T Traceabl e o 2

A C A 14-16 % E P A Protoco l 1/NIS T Traceabl e C O (lo w range ) Z D 0 pp m pe r ga s supplie r (lo w range ) C D 20 0 pp m pe r ga s supplie r C O (lo w range ) A C A 0-4 0 pp m E P A Protoco l 1/NIS T Traceabl e C O (lo w range )

A C A 60-8 0 pp m E P A Protoco l 1/NIS T Traceabl e C O (lo w range )

A C A 140-16 0 pp m E P A Protoco l 1/NIS T Traceabl e C O (hig h range ) Z D 0 pp m pe r ga s supplie r (hig h range ) C D 300 0 pp m pe r ga s supplie r C O (hig h range ) A C A 0-60 0 pp m E P A Protoco l 1/NIS T Traceabl e C O (hig h range )

A C A 900-120 0 pp m E P A Protoco l 1/NIS T Traceabl e C O (hig h range )

A C A 2100-240 0 pp m E P A Protoco l 1/NIS T Traceabl e H C I Z D 0 pp m pe r ga s supplie r I C D 100 0 pp m pe r ga s supplie r H C I A C A 0-20 0 pp m E P A Protoco l 1/NIS T Traceabl e H C I

A C A 300-40 0 pp m E P A Protoco l 1/NIS T Traceabl e H C I

A C A 700-80 0 pp m E P A Protoco l 1/NIS T Traceabl e

1 63 . 4 Correctiv e Actio n fo r Malfunctionin g CEM S

I t i s Veolia' s polic y t o minimiz e the occurrenc e o f malfunction s b y takin g aproactiv e approac h t o facilit y maintenance . Proactiv e measure s includ e th e preventiv e maintenanc e describe di n thi s section , an dth e calibratio n an dperformanc e testin g describe di n Sectio n 2.0 . Frequen t inspection s an davailabilit y o f spar e part s allo w fo r th e timel y completio n o f a s neede dservic e t o th e CEM S prio r t o amajo r

malfunction . Operatin g an dmaintainin g th e incinerato r durin g amalfunctio n wil l b e conformanc e wit h th e Startup, Shutdown, and Malfunction Plan (SSMP) . Attachmen t 4 t o th e SSM P i s th e Program of

Corrective Action for Malfunctions. Sectio n 9. 2 o f th e Program of Corrective Action for Malfunctions addresse s correctiv e action s fo r malfunctionin g CEMS . Sectio n 9. 0 throug h 9. 2 ofth e MC 3 CEM S Operations Guide ma y b e referre dt o a s neede dfo r

troubleshootin g an dcorrectiv 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 dwit h th e automati c wast e fee dcutof f (AWFCO ) syste mt o assur e on-goin g complianc e wit h C O emissio n standards . Th e AWFC O syste mi s designe dt o immediatel y an dautomaticall y shu t o f al l wast e t o th e incinerato r i n th e even t

o f a n exceedanc e o f

a n emissio n o r

operatin g limit . Th e CEM S i s integrate dwit h AWFC O syste mthroug h interlocks . Thes e interlock s ar e condition s whic h trigge r arela y causin g th e AWFC O syste mt o activate . Thi s 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 afo r 0 2( % vol) , H 2 0 ( % vol) , an dC O (ppmv ) consist s o f instantaneou s value s whic h hav e no t bee n smoothe do r

averaged , evaluate donc e ever y 1 5 seconds . Thes e value s ar e use dt o calculat e C O emission s i n th e unit s o f emissio n standards . Calculation s equivalen t t o th e followin g procedure s ar e performe dt o compar e th e stac k

ga s emission s t o th e C O emissio n standard . Firs t 15-secon ddat ai n th e unit s o f th e emissio n standard s ar e calculated :

f \ CO, ppmv CO @7%0 7

, ppmdv = r ° 2 100%-^H 2 O,%) 14% 21%- C L V 100%-(H 2 O,%) Th e calculate d15-secon ddat aar e the n use dt o calculat e one-minut e average s (OMAs) . Th e curren t

minut e OM A i s average dwit h th e previou s 5 9 OMA s t o generat e a n hourl y rollin g averag e (HRA) . Al l roundin g i s avoide dfo r th e number s use dt o calculat e HRAs . Th e HR A o f

C O emission s ar e rounde dt o tw o significan t figures. I f th e HR A C O emissio n concentratio n exceed s th e C O emissio n standar do f 10 0 ppmd v @ 7 % 0 2 , a n AWFC O wil l occur . 4. 2 Drif tLimit s A s describe di n Sectio n 2.1 , wast e feed s wil l b e manuall y shu t of f i n cas e adrif t

limi t i s exceeded . Fo r

C O an d0 2 , drif t limit s ar e equa l t o 2 time s th e performanc e specifications . Comparabl e drif t limit s hav e bee n establishe dfo r excessiv e H 2 0 drift .

1 85.0 . RECORDKEEPIN G AN D QUALIT Y ASSURANC E REVIEW S

Documentatio n generate d fro mCEM S QA/Q C procedure s an dmonitorin g wil l b e kep t on-sit e fo r

aperio do f

fiv e years . Th e dat aan ddocumentatio n tha t i s generate d an d reviewe di s kep t

i n variou s location s a t th e Veoli afacility . Tabl e 6- 1 belo w list s the storag e locatio n an dforma t o f thi s documentation . Maintenanc e an dInstrumen t Technician s hav e th e primar y responsibilit y fo r creatin g an d organizin g CEM S dat asheets , dail y syste maudi t checklists , maintenanc e logbook , an d spar e par t

inventor y records . Th e Environmenta l Engineer/Specialis t o r designe e wil l chec k thes e record s quarterl y t o verif y completio n an dorganization . Thi s revie w wil l als o conside r

th e followin g requirements : 1 . Wheneve r

excessiv e audi t

inaccuracie s occu r

fo r tw o consecutiv e quarters , the curren t writte n procedure s wil l b e revise do r th e CEM S modifie do r replace dt o correc t th 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 t o n recor dan dmad e availabl e fo r inspection . 2 . I f th e Z D and/o r

C D exceed(s ) tw o time s th e limit s i n th e Performanc e Specifications , o r

i f th e cumulativ e adjustmen t t o th e Z D and/o r

C 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 di n 4 0 CF R63.8(c)(7)) , an dth e even t wil l b e reporte d i n th e facility' s semi-annua l "Exces s Emission s an dCM S Performanc e Report" . Furthe r detai l o n thi s repor t ca n b e foun di n th e facilit y CM S Qualit y Assuranc e Program . O n a n annua l basi s th e Environmenta l Engineer/Specialis t o r designe e wil l revie w al l CEM S dat agenerate d fo r th e previou s 1 2 month s an dprepar e abrie f interna l report/mem o summarizin g findings . Base do n thi s review , th e Environmenta l Engineer/Specialis t

o r designe e wil l solici t recommendation s fo r revision s t o th e CEM S Qualit y Assuranc e Plan . Th e CEM S Qualit y Assuranc e Pla n wil l b e revise da s neede d t o maintai n QA/Q C o f

th e CEMS . Al l version s o f thi s pla n fo r

th e las t fiv e year s remai n i n th e operatin g record .

1 9Tabl e 5- 1 CEM S Record s an d Report s Record/Repor t Storag e Locatio n Media/Format 1 CEM S Q A Pla n

- Curren t

Versio n

- Previou s Versio n Incinerato r Manager' s Offic e Operatin g Record s Archive s H D and/o r P R D CEM S Reading s an d HR A

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Dat aHistoria n Operatin g Record s Archive s H D and/o r R D R D Drif t an d Calibratio n Data :

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Operatin g Record s Archive s P and/o r R D Absolut e Calibratio n Audi t

- Previou s yea r

thoug h yea r

t o dat e

- Remainin g archive s Operatin g Recor dArchive s P and/o r R D Relativ e Accurac y Tes t Audi t

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Operatin g Recor dArchive s P and/o r R D Dail y Syste mAudi t

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Operatin g Recor dArchive s P and/o r R D Preventiv e Maintenanc e Logboo k

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Operatin g Record s Archive s P and/o r R D Spar e Part s Inventor y

- Previou s yea r

throug h yea r

t o dat e

- Remainin g archive s Operatin g Record s Archive s P and/o r R D

Annua l Revie w o f

CEM S Dat a Operatin g Record s Archive s P and/o r H D and/o r R D

1 Medi aFormat : H D - Compute r o r networ k

har ddriv e R D - Removabl e driv e (floppy , CD , backu p tape ) P - Pape r

documentatio n


### 2 06. 0 OPERATO RTRAININ G AN D CERTIFICATIO N

Trainin g i s provide dt o Veoli aemployee s o n th e basi s o f thei r jo b title . Individual s specificall y involve di n th e operatio n o f th e incinerato r

an dassociate dCEM S ar e th e Instrumen t

Technicians , Incinerato r Operators , an dEnvironmenta l Engineer/Specialist . Th e Veoli aoperato r

trainin g an dcertificatio n progra mmeet s th e requirement s outline di n 4 0 CF R63.1206(c)(6) . Documentatio n o f employe e trainin g an dcertificatio n i s kep t wit h th e Trainin g Director , an di s availabl e fo r revie w upo n request .

2 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 FTH 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 2 0 (6 0 % ) Zero 

# | O z(25% ) Zero Calibratio n C O (20 0 ppm ) Zero Calibratio n C O (300 0 ppm ) Zero Calibratio n HC I (100 0 ppm ) Zero Calibratio n
Drif t % = Referen ° e - AnalyZer . 100% -

Spa n Valu e (Nam e & Title ) Adjustment

% = Drif t % (i f zero/spa n wa s rese t during drif

t check ) Cumulativ e Adjustmen

t % = (Previou s Cumulativ e Adjustmen t % ) + (Curren

t Adjustmen

t % ) ~ /o ; i \

### ABSOLUT E CALIBRATIO N AUDI T (ACA ) DAT A SHEE T

Paramete r


# •o 2 

### C H CO-lo w rang e E H CO-hig h rang e
• HC I NIS T Traceabl e Calibratio n Standard s Paramete r


# •o 2 

### C H CO-lo w rang e E H CO-hig h rang e
• HC I Ga s Concentratio n Paramete r


# •o 2 

### C H CO-lo w rang e E H CO-hig h rang e
• HC I L o w (Zero ) 

### ± Paramete r


# •o 2 

### C H CO-lo w rang e E H CO-hig h rang e
• HC I M i d 

### ± Paramete r


# •o 2 

### C H CO-lo w rang e E H CO-hig h rang e
• HC I Hig h 

### ±
R U N NUMBE R Concentratio n Differenc e R U 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 u

### , . „ Mea n Differenc e Cahbratio n Erro r

= * 10 0 Spa n Valu e

(Name ) (Title ) (Signature ) (Date)RELATIV E ACCURAC Y TES T AUDI T RAT A DAT A SHEE T Referenc e Metho d CEM S Differenc e Referenc e Metho d CEM S Differenc e Run H 2 0 , % (i f applicable ) 0 2 , % we

t (i f applicable ) 0 2 ,%dr y 0 2 , % dr y 0 2 , % dr

y C O ppm

v (i f applicable ) C O ppmd v C O ppmd

v @7%0 2 C O ppmd v @7%0 2 C O 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 dDeviatio n Confidenc e Coefficien t COR A (Name) (Title ) (Signature) (Date)CEM S DAIL Y SYSTE M AUDI T Initial s

Verify tha

t th e mos t recen t drif t checks an

dcalibratio n adjustment

s ar e withi n limits . Complet e Drif t an dCalibratio n Dat aSheet . Correctiv e Actions : Verify prope

r operatio n o f

CEM S dat

arecordin g andprintin g Correctiv e Actions : Chec k fo r controller

alarms an

derror/warnin g message s Correctiv e Actions : Chec k expectedcalibratio n value s Correctiv e Actions : Chec k curren t emission s dat

astatu s Correctiv e Actions : Verify calibratio n ga

s cylinder pressure s (>15 0 psi ) Correctiv e Actions : Verify pressur

e regulator

setting s (approximately 25-3 5 psi ) Correctiv e Actions : Verify prope

r instrumen

t ai r pressur e t o CEM S umbilica l Correctiv e Actions : Perfor mvisua l inspectio n o f th e stac k ga s sarriplin g syste

m Correctiv e Actions :

(Name) (Title ) (Signature ) (Date )CEM 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 A C A Gases : cylinder s cylinder s cylinder s cylinder s Composition :

Composition : Composition : Composition :

PARTS : A i r conditione r

filter s fo r

CEM S shelte r Instrumen t

ai r coalescin g filter s ____ _ Sampl e pum p Teflo n diaphrag m Sampl e pum p Teflo n flappe r valv e Sampl e prob e interna l filte r Sampl e prob e gasket s Probe-ti p filter Cel l fron t

cove r gaske t Cel l inle t

filter Cel l window s wit h o-rin g gasket s Cel l mirror s Tubin g Fitting s Solenoi dValue s Thermocouple s Electroni c part s

Othe r spar e part s

Inventor y take n by : Date :