# QVGOLI A ENVIRONMENTA L SERVICE S 

## Januar y 28 , 201 4 Vi a FedE x 

# hi JA N3 0 201 4 [ |

. ' • r-.f-^.-.-,.. ' • • • 

## Attn : Complianc e Tracker , AE-17 J Ai rEnforcemen t an d Complianc e Assuranc e Branc h Unite d State s Environmenta l Protectio n Agenc y Regio n 5 7 7 W
. Jackso n Blvd. , AE-17 J Chicago , I L 6060 4 R E : Veoli a E S Technica l Solutions , L.L.C
. 163121AA P 4 0 CF R Par t 6 3 - Subpar t EE E Nationa l Emissio n Standard s fo rHazardou s Ai rPollutant s fro m Hazardou s Wast e Combustor s Comprehensiv e Performanc e Tes t Report s an d Notificatio n o f Complianc e (NOC ) Complianc e Tracker , Pursuan t t o th e requirement s o f 4 0 CF R 63.1200 , subpar t EEE , Veoli a E S Technica l Solutions , L.L.C , hereb y submit s th e Performanc e Tes t Report s fo rIncinerator s 2 , 3 an d 4 an d th e Notificatio n o f Complianc e (NOC)
. Th e NO C document s complianc e wit h th e emissio n standard s an d continuou s monitorin g syste m requirements , an d identifyin g operatin g parameter s define d i n 4 0 CF R 63.120 9 an d 63.1219
. Veoli a 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 t Report s detai l complianc e wit h thes e standards
. I certif y unde rpenalt y o f la w tha t thi s documen t an d al l attachment s wer e prepare d unde rm y directio n o rsupervisio n i n accordanc e wit h a syste m designe d t o assur e tha t qualifie d personne l properl y gathe ran d evaluat e th e informatio n submitted
. Base d o n m y inquir y o f th e perso n o rperson s wh o manag e th e system , o rthos 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 t o f m y
# 7 Mobil e Avenue , Sauget , I L 6220 1 (618)271-2804 www.veoliaes.co m

# Q VGOLI A ENVIRONMENTA L SERVICE S 

## Complianc e Tracke r Januar y 28 , 201 4 Pag e 2 knowledg e an d belief , true , accurate , an d complete
. I a m awar e tha t ther e ar e significan t penaltie s fo rsubmittin g fals e information , includin g th e possibilit y o f fin e an d imprisonmen t fo rknowin g violations
. Upo n revie w o f thi s submittal , shoul d th e Agenc y hav e a nee d fo radditiona l informatio n o rquestions , pleas e contac t Denni s Warcho l a t (618 ) 271-280 4 o rvi a e-mai l a t dennis.warchol@veolia.co m o rm e a t (618 ) 271-280 4 o rvi a e-mai l a t doug.harris@veolia.com
. Sincerely , Veoli a E S Technica l Solutions , L.L.C
. Dou g Harri s Genera l Manage r Att
. cc : Mr
. Georg e Czerniak , Director , Ai ran d Radiatio n Divisio n USEP A Fil e

# 7 Mobil e Avenue , Sauget , I L 6220 1 (618 ) 271-280

4 www.veoliaes.co m

# El¥ I Notificatio n of Complianc e 

# 1^1^11^ ^

wit h th e ~ Fina l Replacemen t Standard s

o f th e Nationa l Emissio n Standard s fo r Hazardou s Ai r Pollutant s fo r

Hazardou s Wast e Combustor s (40 CF R 63 , Subpar t EEE ) Veoli a E S Technica l Solutions , L.L.C .

Sauget , Illinoi s

Veoli a E S Technica l Solutions , L.L.C .

7 Mobil e Avenu e Sauget , Illinoi s 6220 1

Januar y 28 , 201 3

UR S Corporatio n 940 0 Ambergie n Boulevar d Austin
. T

X 7872 9 P.O
. Bo x 20108 8 Austin , T

X 78720-108 8 Tel : 512.454.479 7 Fax : 512.454.880 7 www.urscorp.co m

## Tabl e o f Content s Pag e

1. 0 Certificatio

n Statemen

t1 2. 0 Introductio

n 2 2. 1 Tes t

Objective s 2 2. 2 CP T Schedul e 4 

## 3. 0 Uni tDescriptio

n 5 4. 0 Result

s o f th e Comprehensiv

e Performanc

e Tes t1 0 4. 1 Tes t

Protoco l Summar y 1 1 4. 2 Summar y o f

Result s 1 4 

## 5. 0 Operatin

g Paramete

r Limit s 1 8 6. 0 Base

s fo r Establishmen

to f OPL s 31

i i

## Lis t o f Table s Pag e

2- 1 HW C MAC T Standard s 3 4- 1 Dat aUse dto Establis h OPL s 1 3 4- 2 Uni t

2 Complianc e Summar y 1 5 4- 3 Uni t

3 Complianc e Summar y 1 6 4

- 4 Uni t

4 Complianc e Summar y 1 7 5

- 1 HW C MAC T Operatin g Paramete r Limit s fo r

the Fina l Replacemen t Standard s fo r Unit s 2 an d3 1 9 5- 2 HW C MAC T Operatin g Paramete r Limit s fo r

th e Fina l Replacemen t Standard s fo r Uni t 4 2 0 5- 3 Uni t

2 Developmen t

HW C MAC T Operatin g Limit s 2 1 5- 4 Uni t

3 Developmen t

HW C MAC T Operatin g Limit s 2 4 5- 5 Uni t

4 Developmen t

HW C MAC T Operatin g Limit s 2 7



## Lis t of Figure s Pag e 3- 1 Uni t

2 Proces s Flo w Diagra m7 3- 2 Uni t

3 Proces s Ho w Diagra m8 3- 3 Uni t

4 Proces s Flo w Diagra m9

ii i

## 1. 0 Certificatio n Statemen t

I certif y unde r penalt y o f

the la w tha

t thi s documen t

an dal l attachment s were prepare d unde r m y directio n or

supervisio n i n accordanc e wit h asyste mdesigne dt o assur e tha t qualifie d personne l properl y gathe r an devaluate the informatio n submitted . Base do n m y inquir y o f th e perso n o r

person s wh o manag e the system , o r thos e person s directl y responsibl e fo r gatherin g th

e information , th e informatio n submitte dis , t o th e bes t o f m y knowledg e an dbelief , true , accurate , an dcomplete . I a maware tha t ther e ar e significan t

penaltie s fo r

submittin g fals e information , includin g th

e possibilit y o f

fin e an dimprisonmen t

fo r knowin g violations . Signature: 

## Dou

g Harris u 

## Genera l Manage r Veoli a E S Technica

l Solutions

, L.L.C . Sauget , Illinoi s

1

## 2. 0 Introductio n Veoli aE S Technica l Solutions , L.L.C . (Veolia ) operate s thre e incinerator s a t it s Sauget , Illinoi s facility . Tw o o f th e incinerator s ar

e fixe dheart

h unit s (Unit s 2 an d3) , an dthe thir d incinerato r

i s arotary kil n uni t

(Uni t 4) . Al l o f

the incinerator s trea

t certai n waste s tha

t ar e classifie da

s hazardou s under

stat e and/o r federa l regulations , an dar e subjec t to the Nationa l Emissio n Standard s fo r Hazardou s Ai r

Pollutant s (NESHAPs ) fo r Hazardou s Wast e Combustor s (Titl e 4 0 o f the Cod e o f

Federa l Regulations , Part 6 3 [4 0 CF RPart

63] , Subpart EEE) , (i.e. , the HW C MACT) . A subsequent

Comprehensiv e Performanc e Tes t (CPT ) o f

the thre e incinerator s a t Veolia' s Sauge t

facilit y wa s complete do n Octobe r 30 , 2013 . Th e CP T demonstrate dapplicabl e emissio n standard s an destablishe dOPL s a s require db y the HW C MAC T fo r dioxins/furans , THC , CO , particulat e matter (PM) , hydrochlori c aci dan dchlorin e gas (HC1/C1 2 

### ) , mercury , SVM , an dLVM . Complianc e wit h th e DR E standard(99.99 % DRE ) i s demonstrate dusin g dat afro m previou s RCR A tria l burns . Th e subsequent CP T began wit h the performanc e o f RATA s o f

the C O an d0 2

### continuou s monitorin g system s (CEMS) . Th e RAT A o f th e C O an d0 2

### CEM S o f Uni t 4 wa s performe do n September 4 , 2013 . Th e RAT A o f the C O an d0 2

### CEM S o f Uni t 3 wa s performe do n September 5 , 2013 , an dthe RAT A o f the C O an d0 2

### CEM S o f Uni t 2 wa s performe do n September 6 , 2013 . Th e result s o f th e CP T ar

e presente di n an accompanyin g report , Comprehensive Performance Test Report for Fixed Hearth - Unit

2 Fixed Hearth - Unit 3 Rotary Kiln Incinerator - Unit 4 (CP T Report) . I n accordanc e wit h 4 0 CF R§63.1207(j)(l)(i ) an d§63.1207(j)(3) , the Notificatio n o f Complianc e (NOC ) an dCP T Repor t ar e bein g file d withi n 9 0 day s o f

completio n o f

th e CPT . 2. 1 Tes t Objective s Th e subsequent

CP T fo r th e Fina l Replacemen t

Standard s o f

th e HW C MAC T fo r

th e thre e incinerator s a

t Veoli aSauge t

wa s designe dan dconducte dt o demonstrate complianc e wit h the standard s an dassociate dOPL s o f th e HW C MAC T fo r

existin g incinerator s a

t §63.1219 . Th e CPT :

• Demonstrate dtha t th e incinerator s mee t

the applicabl e HW C MAC T emissio n limit s whil e treatin g hazardou s waste ; an d

• Re-establishe doperatin g parameter limit s (OPLs ) o n ke y operatin g variable s tha t wil l ensur

e tha t th e incinerato r

operate s withi n the HW C MAC T emissio n limit s whil e treatin g hazardou s waste .

2

### Th e tes t progra minclude dfeedin g liqui dan dsoli dwast e material s t o the incinerators , samplin g an danalyzin g the feedstreams , spikin g wast e feedstream s wit h metal s an dchlorine , monitorin g certai n proces s parameters , conductin g emission s testing , an dsamplin g o f wast e stream s an dspikin g materials . Applicabl e emission s standard s fo r th e incinerator s a

t Veoh aSauge

t unde r th e HW C MAC T regulation s ar e summarize di n Tabl e 2-1 . Tabl e 2-1 . HW C MAC T Standard s HA P or HA P Surrogat

e Fina l Replacemen t Standard s Destructio n an dRemova l Efficienc y 99.99 % Dioxins/Furan s 0.2 0 n g TEQ/dsc m- Unit s 2 an d3 1 

### 0.4 0 n g TEQ/dsc m- Uni t 4 1 2 

### Particulat e Matte r 0.01 3 gr/dscf, a t 7 % 0 2 

### Mercur y 13 0 (xg/dscm , a t 7 % O z 

### S V M (Semivolatil e metals , Cd , Pb ) 23 0 [xg/dscm , a t 7 % 0 2 

### L V M (Lo w volatilit y Metals , As , Be , Cr ) 9 2 u,g/dscm , a t 7 % 0 2 

### HC1/C1 2 

### 3 2 ppmv , dry , a t 7 % 0 2 

### , as chlorid e equivalents . C O 10 0 ppmv , dry , a t 7 % 0 2 

### Hydrocarbon s 1 0 ppmv , dry , a t 7 % 0 2

1 

### Toxicit y Equivalent s - relatin g th e relativ e concentration s an dtoxicit y o f th e dioxi n andfuran congener s an disomers t

o th e toxicity o f

2,3,7, 8 tetrachlorodibenzodioxin . 2

### The initia l particulat

e matte r contro l devic e i s abaghouse , an dth e OP L fo r th e maximuminle t

temperatur

e t o th e baghouse o f

Uni t 4 i s 399° F(i.e. , les s tha

n 400°F) . Durin g th

e CPT , th e averag e o f th e test ru n average s (during th

e samplin g fo r

Dioxins/Furans ) was 399°F . 

### Th e objective s fo r

th e subsequent

CP T fo r th e Fina l Replacemen t

Standard s o f

th e HW C MAC T fo r

eac h o f the thre e incinerator s wer e to :

• Demonstrat e complianc e wit h stac k ga s emission s les s than o r equa l to th e followin g limits , correctedt o 7 % O2 :

—Carbo n Monoxide : 10 0 ppmv , dry ;

—Tota l Hydrocarbons : 1 0 ppmv , dry ;

—Dioxins/Furans : 0.2 0 n g TEQ/dsc mfo r Unit s 2 an d3 , an d0.4 0 n g TEQ/dsc mfo r Uni t 4 ;

—Particulat e Matte r

(PM) : 0.01 3 grains/dscf ;

—Mercury : 13 0 |d,g/dscm ;

—Semivolatil e Metal s (SVM ) (C dan dP b combined) : 23 0 |i g /dscm ;

—Lo w Volatilit y Metal s (LVM ) (As , B e an dC r combined) : 9 2 \ig /dscm ; an d

—Hydroge n Chloride/Chlorin e (HCI /CI2) : 3 2 ppm v as C T equivalent , dry .
• Complianc e wit h th e DR E standard (99.99 % DRE ) i s demonstrate d usin g dat afro m previou s RCR A tria l burns . 3

### • Establis h limit s fo r operatin g parameters .
• Conduc t

aContinuou s Monitorin g Syste m(CMS ) performanc e evaluatio n test .
• Conduc t

aRelativ e Accurac y Tes t Audi t (RATA ) fo r

th e C O an dO 2 Continuou s Emission s Monitorin g System s (CEMS . 2. 2 CP T Schedul e Th e subsequent

CP T o f the thre e incinerator s a t th e Sauge t

facilit y began wit h the performanc e o f

RA T A s o f

th e C O an dO 2 continuou s monitorin g system s (CEMS) . Th e RAT A o f th e C O an d0 2

### CEM S o f Uni t 4 wa s performe do n September 4 , 2013 . Th e RAT A o f th e C O an d0 2

### CEM S o f

Uni t 3 wa s performe do n September 5 , 2013 , an dth e RAT A o f th e C O an d0 2 

### CEM S o f

Uni t 2 wa s performe do n Septembe r 6 , 2013 . Th e subsequent

CP T o f Uni t 2 wa s begu n Octobe r

8 , 2013 . Ru n 1 o f

the tes t wa s complete do n thi s day . Ru n 2 wa s performe do n Octobe r 9 , 2013 , bu t

onl y result s associate dwit h th e standardfo r

particulat e matter

ar e reporte d(i.e. , the firs t par t o f th e run) . Th e secon drun , identifie das Ru n 3 , wa s performe do n Octobe r 10 , 2013 . Th e thir dru n o f th e secon dpar

t o f th e test , fo r HC1/C1 2 

### , metals , an ddioxins/furans , (i.e. , Ru n 5 ) wa s performe do n Octobe r 30 , 2013 . Th e subsequent

CP T o f Uni t 3 wa s begu n Octobe r

15 , 2013 . Th e firs t

par t o f Ru n 1 , fo r PM , wa s complete do n thi s day . Testin g fo r HCI /CI2 , metals , an ddioxins/furans , ha dt o b e repeated . Ru n 2 wa s performe do n Octobe r 16 , 2013 , an dRu n 3 wa s performe d o n Octobe r

17 , 2013 . Th e thir dsuccessfu l ru n o f th e secon dpar

t o f th e tes t o f Uni t 3 fo r HCI /CI2 , metals , an ddioxins/furan s (i.e. , Ru n 4 ) wa s performe do n Octobe r 18 , 2013 . Th e subsequent

CP T o f Uni t 4 wa s begu n Octobe r

23 , 201 3 wit h the completio n o f Ru n 1 . Ru n 2 wa s performe do n Octobe r 24 , 2013 . Result s fo r

HCI /CI2 , metals , an ddioxins/furan s ar e reporte dfo r

Ru n 2 . P M result s fo r

Ru n 2 ar e no t reported . Ru n 3 wa s performe do n Octobe r 25 , 2013 . Th e thir d(accepted ) ru n fo r P M (i.e. , Ru n 4 ) wa s performe da t th e conclusio n o f

Ru n 3 fo r P M .

4

## 3. 0 Uni t Description s Veoli aoperate s tw o Fixe dHeart h Dua l Chambere dIncinerator s (Unit s 2 an d3 ) an don e rotary kil n incinerato r

(Uni t 4 ) a t the Sauget , I L facility . Th e tw o fixe dheart h unit s ar

e rate da t 1 6 millio n Btu/h r

each . Uni t

3 i s amirro r

imag e o f

Uni t 2 . Bot h o f

thes e unit s hav e thei r

ow n waste handlin g systems . Unit s 2 an d3 feature atwo-stag e combustio n process . Ignitio n o f waste materia l take s plac e i n the primar y (lower ) combustio n chamber (PCC) . A secondar

y (upper) combustio n chamber (SCC ) serve s a

s a n "afterburner " fo r

proces s gases . Liqui dwastes , organi c an daqueous , an dsoli dwaste s ar

e fe dt o th

e PCC . Air-atomizin g injector s ar e use dfo r

injectio n o f

high-Bt u liquids , low-Bt u liquid s an dspecialty fee dliquids . Solids , usuall y package di n plasti c o r fiberboar d containers , ar

e introduce dint o th e incinerato r throug h aPL C controlle dairlock-ra msyste mlocate d a t th e lowe r

fron t o f the PCC . Th e ai r pollutio n contro l system s o f Unit s 2 an d3 consis t

o f aspray drye r

absorbe r an d fabri c filte r

baghous e modules . Th e ai r pollutio n contro l syste mneutralize s acidi c compound s an d remove s particulat e matte r fro mthe exhaus t

gas . Tw o subsystems , the spray drye r absorbe r an dthe fabri c filter , carr y out

the chemica l neutralizatio n an dparticulat e remova l functions , respectively . A n induce ddraf

t fa n an dstac k

provid e the mechanical energ y require dto transpor t the flu e gas throug h the interconnectin g ductwork , to it s eventua l discharg e poin t to atmosphere . Th e onl y differenc e betwee n Unit s 2 and3 i s tha t Uni t 2 i s equippe dwit h fou r (4 ) baghous e modules , whil e Uni t 3 i s equippe dwit h thre e (3 ) baghous e modules ! However , eac h incinerato r i s operate d identicall y wit h onl y thre e baghous e module s i n servic e durin g operation . A complet e descriptio n o f Unit s 2 an d3 i s provide di n the CP T Plan . A proces s flo w diagra mfo r

Uni t 2 i s presente d i n Figur e 3-1 , an daproces s flo w diagra mfo r Uni t 3 i s presente d i n Figur e 3-2 . Uni t 4 i s rate da

t 5 0 millio n Btu/h r

an di s equippe dwit h it s ow n tank far msystem , dru m storage , bul k

solid s storag e an dfee dsystems . Uni t 4 include s arotar

y kil n as the PCC , an daSCC . Liquid s ar

e fe dt o either

th e kil n PC C o r

the SCC . Bul k

soli dwaste s ar

e fe dto th e kil n throug h the ra mfeeder . Containerize dwaste s ar e fe dt o the kil n throug h the ra mfeede r o r th e auxiliar y ra m feeder . Th e Uqui dwast

e injector s use di n the combustio n chamber s ar e air-atomizin g injectors , an d ar e use dfo r

injectio n o f

pumpabl e sludges , aqueou s waste s an dorgani c liqui dwaste s t o the kil n an dfo r injectio n o f

organi c liqui dwast

e t o the SCC .

5

### Th e ai r pollutio n contro l syste mconsist s o f atemperin g chamber , tw o spra y drye r absorbers , an dfabri c filte r baghous e module s wit h carbo n injection . Th e ai r pollutio n contro l syste mneutralize s acidi c compound s an dremove s particulat e fro mthe exhaus t gas . Tw o subsystems , th e spra

y drye r absorber an dthe fabri c filter , carry ou t the chemica l neutralizatio n an d particulat e remova l functions , respectively . A n induce ddraf t fa n an dstac k

provid e the mechanica l energ y require dto transpor t the flu e gas throug h the interconnectin g ductwork , t o it s eventua l discharg e poin t

to atmosphere . A complet e descriptio n o f Uni t 4 i s provide di n the Comprehensiv e Performanc e Tes t Plan . A proces s flo w diagra mfo r Uni t 4 i s presente d i n Figur e 3-3 .

6

### Figur e 3-1 . Uni t 2 Proces s FlowDiagra m

TAN KFAR M DIREC T INJEC T Mil ! I I I I I ,..T . TJ L TY COMBUSTIO N AI R BLOWER

tooooooH

TAN KFAR M ^ LO

W 

### e m DIREC T INJEC T LOT S / AI R 

### Mrrrr

- T T• T T T -SECCWOAR Y A I R EMERGENC Y

STAC K

INCINERATOR L0V£ R CHAMBE R

HOD/ 0 CONTAINER ^ GA S CYLINDERS . SPECIALT Y

FEEDE R INCINERATO R UPPE R CHAMBE R

PRIMAR Y FUE L WE T AS H DUMPSTE R i i UM E PREPARATIO N SYSTE M

SPRA Y DR Y A8SORBE R

DR Y SCRUBBE R SOLID S { DS S ) EN D DUM P MAI N STACK STAC K OA S ANAlY2fl ? S •
BAGHOUS E I.D . FA N

DR Y SCRUBBE R |S0LID S ( OS S ) EN D DUMP

cccax» ~ >oooo*> - FUELS/LIQUI D WAST E FLOW COMBUSTIO N AI R FLO W STAC KOA S FLO W AS H FLO

W SOU P WAST E FLO W LIM E SLURR Y FLO W



### 7

### Figure 3-2 . Uni t 3 Proces s Flo wDiagra m

TAN KFARM . DIREC T INJEC T HIG H

8T U LIQUID S m i l i i i i i T T T

### f V

SOLID S COMBUSTIO N AI R SLOWE R

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TANK. FAR M OIREC T INJEC T L O W B T U LIQUID S -UHDEWII K



### f m. •• f frrr
- T . T , T TT T . -SECONDAR Y
INCINERATO R LOWE R CHAMBE R EMERGENC Y STAC K LIM E

PREPARATIO N SYSTE M

INCINERATO R UPPE R CHAMBE R

BURNE R

W E TAS H DUMPSTE R 

### /

SPRA Y O R Y ABSORBE R

SPECIALT Y FEEDE R FUM E HOO D EMISSIO N CONTRO L SYSTE M PRIMAR Y FUE L O R YSCRUBBE R SCUD S ( DS S ) E N D DUM P

GLOV E BO X EMISSIO N CONTROL ! SYSTE M 

### JJMAI N STACK -

SIACK OA S ANALYSER S -

BAGHOUS E t.D . FA N

DR YSCRU8BE R SOLID S ( OS S ) EN D DUM P



### axxro- >OO0O* ~ 

### -\\\» - FUELSAIQUI D WAST E FLO W COMBUSTIO N AI R FLO W STAC KGA S FLOW AS KFLO

W SOLI D WAST E FLOW UM E SLURR Y FLO W



### 8

### Figur e 3-3 . Uni t 4 Proces s FlowDiagra m

TAN KFAR M DIREC T INJEC T HIG H

BTU " LIQUID S

SOLID S MAI N AUX . BULK . (ooocxx> i

« •

TAN KFAR M
_ LO W

BT U DIREC T INJEC T „ LIQUID S SURG E VEN T

KIL N DRY" SCRUBBE R S0LID 5 ( DS S ) | EN D DUM P EUER6ENC Y STAC K

SECONDAR Y COMBUSTIO N CHAMBE R TEMPERIN G

CHAMBE R

AS H ROLL-OF F |BWER |

;OMBUSTJOf | AI R BLOWER S SPRA Y DR Y ABSORBE R 

# I LIM E PREPARATIO N SYSTE M 

### ^— — SPRA Y DR Y ABSORBE R WE T AS H DR Y AS H OUMPSTfj ? DU,V?STE R DR Y SCRUBBE R SOLO S ( DS S ) EN D DUM P

\ PRIMAR Y V / FUE L f



### 9 DR Y SCRUBBE R [SOUD S ( DS S ) BH D DUM P

BAGHOUS E

CARBO N INJECTIO N SYSTE M MAI N STACK STAt KCA S

DR Y SCRUBBE R SOLID S : ( DS S ) EN D DUM P


### _ v . Fuas /uQW D WASTE : FLO W —.—to . COMBUSTIO N A W RO W

p ~ STAC KGA S RO W CXXCCO - AS H FLO W KJOOO* - SOU D WAST E FLO W .LIM E SLURR Y FLO W

## 4. 0 Result s o f th e Comprehensiv e Performanc e Tes t

I n Augus t

an dSeptember

o f 2008 , Veoli aconducte dtest s o f Unit s 2 , 3 , an d4 require db y th e informatio n collectio n request s fro mU.S . EP A Regio n 5 date dJun e 5 , 200 8 an dSeptember 12 , 2008 . Thos e test s began o n Augus t 11 , 200 8 fo r

Uni t 2 , Augus t

5 , 200 8 fo r

Uni t 3 , an d Augus t 21 , 200 8 fo r

Uni t 4 followin g tes t

plan s approve db y U.S . EP A Regio n 5 . Initia l Comprehensiv e Performanc e Test s (CPTs ) o f Unit s 2 , 3 , an d4 commence do n Decembe r 8 , 200 9 fo r Uni t 2 ; o n Decembe r

1 , 200 9 fo r

Uni t 3 ; an do n Decembe r

16 , 200 9 fo r

Uni t 4 , an dwere performe di n accordanc e wit h Comprehensiv e Performanc e Tes t Plan s approve db y U.S . EP A Regio n 5 . Th e HW C MACT , a t 4 0 CF R§ 63.1207(d) , state s "The date of commencement

of the initial comprehensive performance test is the basis for

establishing the deadline to commence the initial confirmatory performance test and the next comprehensive performance test. You may conduct performance testing at any time prior

to the required

date. The deadline for commencing subsequent confirmatory and

comprehensive performance testing is based on the date of commencement

of the previous comprehensive performance test." EP A Regio n 5 consider s tha

t th e star t o f the subsequent

CPT s b e base do n th e initiatio n o f the metal s test s performe di n 2008 , requirin g tha t the subsequent

CP T b e starte db y September 5 , 2013 , an dtha

t asite-specifi c tes t

pla n b e submitte dbefor e thi s date . Veoli aoriginall y submitte dt o EP A it s notificatio n o f

inten t an dsite-specifi c tes t

plan s (i.e. , comprehensiv e performanc e tes t plans ) fo r al l thre e unit s an daQualit y Assuranc e Projec t Pla n (QAPjP ) fo r

th e subsequent

CP T o n September

5 , 2012 . Revision s t o the CP T Plan s an dQAPj P wer e mad e base do n negotiation s wit h E P A Regio n 5 . Th e CP T Pla n an dQAPj P date dSeptember 25 , 201 3 wer e approve db y EP A Regio n 5 , an dthe subsequent CP T fo r Unit s 2 , 3 , an d4 wa s conducte di n accordanc e wit h thes e plans . E P A Regio n 5 consider s tha t testin g o f

al l thre e o f

th e incinerator s comprise s the CP T fo r Veolia' s facilit y i n Sauget . Veoli aSauge t starte dth e CP T o f

th e thre e incinerator s a t the Sauget facilit y o n Septembe r

4 , 201 3 wit h the performanc e o f th e RAT A o f

the C O an d0 2

### CEM S o f Uni t 4 . Testin g fo r

th e applicabl e parameter s o f th e HW C MAC T includin g dioxins/furans , tota l hydrocarbon s (THC) , carbo n monoxid e (CO) , particulat e matter (PM) , hydroge n chloride/chlorin e ga s (HCI /CI2) , mercury , SVM , an dLV M wa s complete do n Octobe r 30 , 2012 . Th e HW C MACT , a

t §63.1207(d)(3) , state s tha t "yo u mus t

complet e th e performanc e testin g withi n 6 0 day s afte r

th e dat e o f commencement... " Th e subsequent CP T o f th e thre e incinerator s a

t Veolia' s Sauge t

facilit y bega n b y the dat e require db y EP A Regio n 5 , an dwa s complete dwithi n 6 0 days .

1 0

### 4. 1 Tes t Protoco l Summar y

A definitio n o f

the applicabl e emissio n limit s an dthe resultin g operatin g parameter limit s (OPLs ) ar

e give n i n Sectio n 4. 0 o f th e CP T plan s fo r

eac h incinerator . Th e subsequent CP T o f eac h o f th e incinerator s include don e tes t condition , an dth e tes t

conditio n include done mod e o f operation . On e se

t o f OPL s wa s develope dfo r eac h incinerator . I n th e firs t

par t o f th e tes t fo r eac h incinerator , Veoli ademonstrate dcomplianc e wit h th e particulat e matter

standardo f

the HW C MAC T whil e the plan t wa s operate dt o establis h the maximu mas h feedrat e an dmaximu mcombustio n gas flowrat e OPL s a s require db y the HW C MAC T fo r

th e particulat e matter

standard . Complianc e wit h the standardfo r carbo n monoxid e wa s als o demonstrate ddurin g thi s portio n o f th e test . I n th e secon dpar

t o f the tes t fo r eac h incinerator , Veoli ademonstrate dcompliance , an d develope dOPLs , wit h the HC1/C1 2 

### , dioxins/furans , THC , CO , LVM , SVM , an dmercury standard s o f

the HW C MAC T whil e the plan t wa s operate dto establis h maximu mtota l hazardou s waste feedrate , maximu mpumpabl e hazardou s waste feedrate , minimu mprimar y combustio n chambe r

(PCC ) temperature , minimu msecondar y combustio n chambe r

(SCC ) temperature , maximu mLVM , SVM , an dH g feedrates , maximu mchlorin e feedrate , maximu m combustio n gas flowrate , an dmaximu minle t temperature t o the baghouse . As h wa s fe dt o the incinerator s a

t norma l (o r

higher ) level s durin g thi s portio n o f th e test . Complianc e wit h th e standardfo r

carbo n monoxid e wa s demonstrate ddurin g al l testing . Sample s o f

th e waste s fe ddurin g th e test s wer e sample dever y 1 5 minute s an d composite dfo r

analysis . Wast e fee dsample s wer e collecte di n coordinatio n wit h th e PM , HCI /CI2 , metals , an ddioxins/furan s stac k testing . Composit e liqui dwaste fee dsample s associate dwit h eac h o f th e fou r samplin g train s wer e analyze dfo r ash , total chlorine , hea

t content , moisture , density , an dviscosity . Th e composit e liqui dwast e fee dsample s collecte ddurin g the Metho d2 9 stac k

samplin g fro mthe secon dpar t o f the tes t were als o analyze dfo r

metal s (arsenic , beryllium , chromium , cadmium , lead , an dmercury) . Al l o f th e composit e soli dwast e fee d samples , containerize dan dbulk , fro mthe firs t an dsecon dpart s o f

th e tes t were analyze dfo r

total chlorine , ash , moisture , andhea t content . Th e composit e containerize dwast e fee dsample s fo r

Unit s 2 , 3 , an d4 , an dbul k

soli dwaste fee dsample s fro mUni t 4 , collecteddurin g the Metho d2 9 stac k samplin g fro mthe secon dpar t o f the tes t were als o analyze dfo r

metal s (arsenic , beryllium , chromium , cadmium , lead , an dmercury) . Chlorin e an dthe metal s lead , chromiu man dmercur y wer e spike dint o eac h o f th e thre e incinerator s during , an dthroughout , the secon dpar t o f eac h tes t

run . Pe r 4 0 CF R§63.1206(b)(7)(i)(A ) complianc e wit h the DR E standardi s require dt o b e 1 1

### demonstrate donl y on e tim e an dVeoli ademonstrate dDR E fo r eac h o f th e thre e incinerator s i n RCR A tria l burns . Th e RCR A tria l bur n fo r Uni t 2 wa s conducte di n January 1993 , an dthe RCR A tria l bur n fo r

Uni t 3 wa s conducte di n Novembe r 1996 . Th e RCR A tria l bur n fo r Uni t 4 wa s conducte di n Decembe r 1995 . Veoli adi dno t

re-demonstrate DR E i n the subsequen t CP T fo r th e Fina l Replacemen t

Standard s o f

th e HW C MAC T becaus e DRE , an dth e associate dOPLs , wer e demonstrate ddurin g the RCR A tria l burns , an doperatio n o f the incinerator s ha s no t significantl y change dsinc e thos e tests . Th e operatin g limit s demonstrate dwit h the standardfo r D R E i n th e RCR A Tria l Burn s o f Unit s 2 , 3 , an d4 wer e considere di n th e developmen t o f OPL s fo r the incinerators . Th e OPL s associate dwit h eac h o f the applicabl e emissio n standard s demonstrate d durin g the subsequen t

CP T (i.e. , PM , HCI /CI 2 gas , metals , an ddioxins/furans ) wer e develope d usin g proces s dat ataken durin g the collectio n o f th e applicabl e samplin g trai n (i.e. , EP A Metho d5 fo r

particulat e matter , Modifie dEP A Metho d26 A fo r HC1/C1 2 

### , EP A Metho d2 9 fo r metals , an dSW-84 6 Metho d0023 A fo r dioxins/furans) . Operatin g parameter dat awer e use das show n i n Tabl e 4- 1 t o develo p HW C MAC T OPLs .

1 2

### Tabl e 4-1 . Dat a Use d t o Establis h OPL s
Demonstrate

d OPL s Emissio n Standar d OPL s Develope d Durin g th e CP T Demonstrate

d OPL s Emissio n Standar d Uni

t2 Uni

t3 Uni

t4 Maximu mPumpabl e Wast e Feedrat e DR E 199 3 199 6 199 5 Maximu mPumpabl e Wast e Feedrat e TH C V Pumpabl Feedrat Dioxins/Furan s •/ • / Maximu mTotal Wast

e Feedrat e DR E 199 3 199 6 199 5 Maximu mTotal Wast

e Feedrat e TH C •/ Maximu mTotal Wast

e Feedrat e Dioxins/Furan s •/ •/ VMaximu mStack

Ga s Flowrat e SV M •/
Maximu mStack

Ga s Flowrat e L V M •/ Maximu mStack

Ga s Flowrat e P M • / •/ V Maximu mStack

Ga s Flowrat e 

### Hcyci 2 Maximu mStack

Ga s Flowrat e DR E 199 3 199 6 199 5 Maximu mStack

Ga s Flowrat e TH C Maximu mStack

Ga s Flowrat e Dioxins/Furan s •/ •/ 

### • Minimu mCombustio n Chambe r Temperatur

e i n th e PC C DR E 199 3 199 6 199 5 Minimu mCombustio n Chambe r Temperatur

e i n th e PC C TH C •/ • / Minimu mCombustio n Chambe r Temperatur

e i n th e PC C Dioxins/Furan s •/ S • / Minimu mCombustio n Chambe r Temperatur

e i n th e SC C DR E 199 3 199 6 199 5 Minimu mCombustio n Chambe r Temperatur

e i n th e SC C TH C / Minimu mCombustio n Chambe r Temperatur

e i n th e SC C Dioxins/Furan s • / V Maximu mTotal Feedrat

e o f LV M (As , Be , Cr ) L V M • / •/ Maximu mPumpabl e Feedrat e o f LV M (As , Be , Cr ) L V M •/ Maximu mFeedrat

e o f SV M (Pb , Cd ) SV M V V Maximu mFeedrat

e o f Mercur y (Hg ) H g •/ Maximu mFeedrat

e o f As h P M •/ • / Maximu mFeedrat

e o f Total Chlorine/Chlorid e HC1/C1 2 s •/ Maximu mFeedrat

e o f Total Chlorine/Chlorid e L V M •/ Maximu mFeedrat

e o f Total Chlorine/Chlorid e SV M V Maximu mBaghous e Inlet Temperatur

e TH C V • / Maximu mBaghous e Inlet Temperatur

e Dioxins/Furan s •/ •/ Maximu mBaghous e Inlet Temperatur

e L V M V Maximu mBaghous e Inlet Temperatur

e SV M •/ •/ Minimu mCarbo n Feedrat e Dioxins/Furan s N A N A V Minimu mCarbo n Feedrat e H g N A N A < / Minimu mSorben

t Feedrat e HC1/C1 2 •/ / •/ Minimu mCarrier

Flui dFlowrat

e HC1/C1 2 • / •/ 199 3 - Operating dat

afro mth e Januar y 199 3 RCR A Tria l Burn fo r Uni t 2 . 199 6 - Operatin g dat

afro mth e Novembe

r 199 6 RCR A Tria l Bur n fo r Uni t 3 . 199 5 - Operating dat

afro mth e Decembe

r 1995 RCR A Tria l Burn fo r Uni t 4 .



### 1 3

### 4. 2 Summar y o f Result s

Veoli asuccessfull y demonstrate dcomplianc e wit h al l o f the applicabl e regulatory requirement s o f

th e HW C MAC T fo r

Uni t 2 , Uni t 3 , an d Uni t

4 usin g th e result s fro mthe singl e tes t conditio n o f

eac h unit . Tabl e 4- 2 summarize s the result s o f th e emission s testin g o f Uni t 2 . Tabl e 4- 3 summarize s th e result s o f the emission s testin g o f Uni t 3 , an dTabl e 4- 4 summarize s the result s o f

th e emission s testin g o f Uni t 4 . Th e tes t

fo r eac h uni t

consiste do f

thre e reporte d run s fo r eac h paramete r

o f interest . Al l reporte dresult s o f th e CP T ar

e reporte di n the CP T Report . Th e ter m"tes t

condition " refer s t o the su mo f al l th e testin g activitie s designe dto demonstrate the operatio n o f th e waste incinerato r

unde r particula r

operatin g parameter s (e.g. , developmen t

o f operatin g parameter

limits ) unde r

th e HW C MACT . Th e ter m"tes t run " refer s t o th e replicat e testin g periods . A complet e definitio n o f th e tes t protoco l an dmethodolog y i s define di n the CP T Pla n an d QAPjP .

1 4

### Tabl e 4-2 . Uni t 2 Complianc e Summar y Uni t2 Paramete

r HW C MAC T Limi t Run l 10-8-1 3 Ru

n 2 10-9-1 3 Ru

n 3 10-10-1 3 Run 5 10-30-1 3 Averag

e Particulat e Matter - EP A Metho d5 0.01 3 gr/dsc f correctedt

o 7 % 0 2 <0.00087 <0.0006 8 <0.0005 8 <0.0007 1 HC1/C1 2- Modifie dEP A Metho d26 A 3 2 ppm v dry , a s CP , correcte dt

o 7 % 0 2 <2

9 <1 3 <1 8 <2 0 Metal s - EP A Metho d29 L V M 9 2 |xg/dscmcorrectedt o 7 % 0 2 <2. 8 <2. 4 <2. 5 <2. 6 SV M 23 0 (xg/dsc mcorrectedt

o 7 % 0 2 <1. 1 <0.7 8 <1. 0 <0.9 5 Mercur y 13 0 (ig/dsc mcorrectedt o 7 % 0 2 <9 0 <12 0 <9

5 <10

0 Dioxins/Furan s - SW-84 6 Metho d0023 A 0.20 ng/dsc mcorrecte dt o 7 % 0 2 0.0054 3 0.0062 4 0.015 7 0.0091 2 Total Hydrocarbon s (THC) 1 - EP A Metho d25 A 1 0 ppmv , dr y correctedt

o 7 % 0 2 1.6 0.1 8 0.49 0.7 5 Carbo n Monoxid e (CO) 1 10 0 ppmv , dr

y correcte dt

o 7 % 0 2 0.00 0.00 0.1 5 0.05 TH C an dC O result s collecte ddurin g th e stac k samplin g fo r

dioxins/furans .



### 1 5

### Tabl e 4-3 . Uni t 3 Complianc e Summar y Uni t 3 Paramete r HW C MAC T Limi t Run t 10-15-1 3 Ru n 2 10-16-1 3 Ru n 3 10-17-1 3 Ru n 4 10-18-1 3 Averag e Particulat e Matter - EP A Metho d5 0.01 3 gr/dsc f correctedt

o 7 % 0 2 0.00194 0.0020 2 0.0020 4 0.00200 HC1/C1 2- Modifie dEP A Metho d26 A 3 2 ppm v dry , a s CP , correctedt

o 7 % 0 2 <4. 5 <4. 4 <1. 8 <3. 6 Metal s - EP A Metho d29 L V M 9 2 ^ig/dsc mcorrectedt

o 7 % 0 2 <8. 6 <8. 9 <1 1 <9. 4 S V M 23 0 |xg/dscmcorrectedt o 7 % 0 2 <2 0 <1 4 <1 2 <1 5 Mercur y 13 0 u.g/dsc mcorrectedt

o 7 % 0 2 <5 9 <3 9 <4 6 <4 8 Dioxins/Furan s - SW-84 6 Metho d0023 A 0.20 ng/dsc mcorrecte dt o 7 % 0 2 0.0010 3 0.0011 5 0.0013 4 0.0011 8 Total Hydrocarbon s (THC) 1 - EP A Metho d25 A 1 0 ppmv , dr y correcte dt

o 7 % 0 2 0.4 4 0.2 6 0.5 7 0.4 3 Carbo n Monoxid e (CO) 1 10 0 ppmv , dr

y correcte dt

o 7 % 0 2 0.00 0.00 0.00 0.00

1 TH C an

dC O result s collecte ddurin g th e stac k samplin g fo r

dioxins/furans .



### 1 6

### Tabl e 4-4 . Uni t 4 Complianc e Summar y Uni t4 Paramete

r HW C MAC T Limi t Run t 10-23-1 3 Run 2 10-24-1 3 Ru

n 3 10-25-1 3 Run 4 10-25-1 3 Averag

e Particulat e Matter - EP A Metho d5 0.01 3 gr/dsc f correctedt

o 7 % 0 2 0.0026 9 0.0018 3 <0.001 9 <0.002 1 HC1/C1 2- Modifie dEP A Metho d26 A 3 2 ppm v dry , a s CP , correctedt

o 7 % 0 2 <1 1 <8. 0 <2 3 <1 4 Metal s - EP A Metho d2 9 L V M 9 2 [xg/dsc mcorrecte dt

o 7 % 0 2 <1 2 <9. 8 <7. 5 <9. 7 SV M 23 0 [xg/dsc mcorrecte dt

o 7 % 0 2 <8. 6 <4. 5 <1 0 <7. 8 Mercur y 13 0 ng/dsc mcorrectedt o 7 % 0 2 <7. 1 <8. 1 <1 5 <1 0 Dioxins/Furan s - SW-84 6 Metho d0023 A 0.40 ng/dsc mcorrecte dt o 7 % O z 0.13 8 0.13 2 0.13 9 0.13 7 Total Hydrocarbon s (THC) 1 - EP A Metho d2 5 A 1 0 ppmv , dr y correctedt

o 7 % 0 2 0.5 1 0.60 0.8 5 0.6 5 Carbo n Monoxid e (CO) 1 10 0 ppmv , dr

y correctedt

o 7 % 0 2 0.0 7 0.0 6 0.0 8 0.0 7

1 TH C an

dC O result s collecte ddurin g th e stac k samplin g fo r

dioxins/furans .



### 1 7

## 5. 0 Operatin g Paramete r Limit s

Tabl e 5- 1 an d5- 2 presen t th e operatin g parameter limit s (OPLs ) establishe dfo r the thre e incinerator s (i.e. , Uni t

2 , Uni t 3 , an dUni t

4 ) a t the Veoli afacilit y i n Sauget , Illinoi s i n complianc e wit h the Fina l Replacemen t Standard s o f

the HW C MACT . Uni t 2 an dUni t

3 ar e bot h Fixe dHeart h Dua l Chambere dIncinerators . Th e tw o fixe dheart h unit s ar

e identica l excep t tha t Uni t 2 i s equippe dwit h fou r (4 ) baghous e modules , whil e Uni t 3 i s equippe dwit h thre e (3 ) baghous e modules . However , eac h incinerato r i s operate didenticall y wit h onl y thre e baghous e module s i n servic e durin g operation . Uni t 3 i s amirro r

imag e o f Uni t 2 . Becaus e Uni t

2 an dUni t 3 ar e identica l an dar

e operate dth e sam

e way , on e set

o f OPL s fo r

Uni t 2 an dUni t

3 ar e establishe dfo r

both units . Th e OPL s fo r Unit s 2 an d3 ar

e establishe dselecting the mor e conservative , o r

stringent , valu e develope dfo r Uni t 2 o r Uni t 3 . Tabl e 5- 1 present s th e OPL s establishe dfo r

Uni t 2 an dUni t

3 . Tabl e 5- 2 present s the OPL s establishe dfo r Uni t 4 . OPL s t o compl y wit h th e Fina l Replacemen t Standard s wer e develope dbase do n dat a collecte ddurin g th e Octobe r 201 3 CPT , an ddat afo r DR E fro mRCR A Tria l Burn s conducte d i n 199 3 fo r

Uni t 2 , 199 6 fo r

Uni t 3 , an d199 5 fo r

Uni t 4 . Als o note tha

t OPL s were developed , as appropriate , durin g the EP A Metho d5 testin g fo r PM , Modifie dEP A Metho d26 A fo r HC1/C1 2 

### , EP A Metho d2 9 fo r metals , an dSW-84 6 Metho d0023 A fo r dioxins/furan s o f

the 201 3 CP T fo r eac h o f Uni t 2 , Unit , 3 an dUni t

4 . I n thos e case s wher e a n OP L i s applicabl e t o mor e tha n on e standard , the OP L wa s establishe dselectin g the more , o r most , stringen t

valu e (i.e. , th e lower , o r lowest , valu e where th e OP L i s amaximum , an dahigher , o r highest , valu e wher e th e OP L i s aminimum ) fro mthes e tests . Table s 5- 1 an d5- 2 presen t th e sourc e o f

th e OPL . Table s 5- 3 an d5- 4 presen t the base s fo r

developmen t

o f the OPL s show n i n Table s 5- 1 an d5-2 . Th e dat ause dt o develo p the OPL s ar e presente di n Tabl e 5- 3 fo r Uni t 2 , Tabl e 5- 3 fo r Uni t 3 , an dTabl e 5- 4 fo r

Uni t 4 fo r eac h o f th e Fina l Replacemen t

Standard s o f

the HW C MACT . Th e CP T Plan , tha t include dtes t

plan s fo r

Uni t 2 , Uni t 3 , an dUni t

4 , presente dan approac h t o extrapolat e the feedrate s o f SVM , tota l an dpumpabl e LVM , an dmercur y base do n th e SRE s (Syste mRemova l Efficiencies ) o f lead , chromium , an dmercur y measure ddurin g th e CPT . Th e OPL s fo r

the feedrate s o f

SVM , tota l an dpumpabl e LVM , o r mercur y presente di n thi s NO C d o no t

includ e extrapolatio n o f the feedrate s o f

SVM , tota l an dpumpabl e LVM , an d mercur y demonstrated , an dmeasured , durin g the CPT . A s presente di n the CP T Plan , Veoli a wil l hav e furthe r

discussion s wit h EP A Regio n 5 befor e extrapolatio n i s requested . Sinc e extrapolatio n o f

metal s feedrate s i s no t

bein g requeste db y thi s NOC , SRE s fo r lead , chromium , an dmercur y ar

e no t i n the CP T Report .

1 8

### Tabl e 5-1 . HW C MAC T Operatin g Paramete r Limit s fo r th e Fina l Replacemen t Standard s fo r Unit s 2 an d 3 Operatin g Paramete

r Permittin g Unit s OP L Establishe d From Operatin g Limi t Maximu mFeedrat

e o f Total Mercur

y 12-HR A 201 3 CP T Uni t 2 Metal s Test 0.002 1 lb/hr Maximu mTotal Feedrat e o f SV M (Pb , Cd ) 12-HR A 201 3 CP T Uni t 2 Metal s Test 6 2 lb/h r Maximu mTotal Feedrat e o f LV M (As , Be , Cr ) 12-HR A 201 3 CP T Uni t 3 Metal s Test 4 6 lb/h r Maximu mPumpable Feedrat e o f LV M (As , Be , Cr ) 12-HR A 201 3 CP T Uni t 3 Metal s Test 4 6 lb/hr Maximu mFeedrat

e o f Total Chlorine/Chlorid e 12-HR A 201 3 CP T Uni t 3 Metal s Test 20 4 lb/h r Maximu mFeedrat

e o f As h 12-HR A 201 3 CP T Uni t 2 P M Test 50 3 lb/h r Minimu mCombustio n Chambe r Temperatur

e i n th e PC C HR A 201 3 CP T Uni t 3 Dioxins/Furan s Test 1,709° F Minimu mCombustio n Chambe r Temperatur

e i n th e SC C HR A 201 3 CP T Uni t 3 Dioxins/Furan s Test 1,885° F Maximu mFlu e Gas Flowrat e HR A 201 3 CP T Uni t 3 P M Test 15,31 0 acf m Maximu mTotal Hazardou s Wast e Feedrat e HR A 1993 RCR A Tria l Burn Uni t 2 4,01 7 lb/hr Maximu mPumpable Hazardou s Wast e Feedrat e HR A 199 3 RCR A Tria l Burn Uni t 2 3,10

7 lb/hr
Maximu mBaghous e Inlet Temperature 1 HR A 201 3 CP T Uni t 2 an d3 Dioxins/Furan s an

d Metal s Test

s 420° F
Minimu mSorben

t Feedrat e HR A 201 3 CP T Uni t 2 HC1/C1 2Test 2.2 4 lb/l b C1 2 Minimu mCarrier

Flui dFlowrat

e HR A 201 3 CP T Uni t 2 HC1/C1 2Test 1.9 0 gal/lb C1 2 Emissio n Limi t

fo r Carbo n Monoxid e HR A 10 0 ppm v correcte d t o 7 % Q 2 HR A - Hourl y Rollin g Averag e 12-HR A - 12 -Hou r Rollin g Averag e

1 Measure da

s th e SD A (Spra

y Dryer/Absorber

) Outle t Temperature .



### 1 9

### Tabl e 5-2 . HW C MAC T Operatin g Paramete r Limit s fo r th e Fina l Replacemen t Standard s fo r Uni t 4 Operatin g Paramete

r Permittin g Unit s OP L Establishe d From Operatin g Limit Maximu mFeedrat

e o f Total Mercur

y 12-HR A 201 3 CP T Metal s Test 0.04 0 lb/h r Maximu mTotal Feedrat e o f SV M (Pb , Cd ) 12-HR A 201 3 CP T Metal s Test 621b/h r Maximu mTotal Feedrat e o f LV M (As , Be , Cr ) 12-HR A 201 3 CP T Metal s Test 4 6 lb/h r Maximu mPumpabl e Feedrat e o f LV M (As , Be , Cr) 12-HR A 201 3 CP T Metal s Test 461b/h r Maximu mFeedrat

e o f Total Chlorine/Chlorid e 12-HR A 201 3 CP T HC1/C1 2Tes

t 20 3 lb/hr Maximu mFeedrat

e o f As h 12-HR A 201 3 CP T P M Test 4,77 7 lb/hr Minimu mCombustio n Chambe r Temperatur

e i n th e PC C HR A 201 3 CP T Dioxins/Furan s Test 1,561° F Minimu mCombustio n Chambe r Temperatur

e i n th e SC C HR A 201 3 CP T Dioxins/Furan s Test 1,881° F Maximu mFlu e Gas Flowrat e HR A 201 3 CP T HCl/Cl z Test 37,39 3 acf m Maximu mTotal Hazardou s Wast e Feedrat e t o th e PC C HR A 201 3 CP T Dioxins/Furan s Test 10,63 2 lb/hr Maximu mPumpabl e Hazardou s Wast e Feedrat e t o th e PC C HR A 1995 RCR A Tria l Burn 3,31 2 lb/hr Maximu mTotal (Pumpable ) Hazardou s Wast e Feedrat e t o th e SC C HR A 201 3 CP T Dioxins/Furan s Test 1,20 3 lb/hr
Maximu mBaghous e Inle t Temperature 1 HR A 201 3 CP T Dioxins/Furan s an

dMetal s Test s 399° F

Minimu mCarbo n Injectio n Feedrat e HR A 201 3 CP T Dioxins/Furan s an

dMetal s Test s 6. 2 lb/hr Minimu mSorben

t Feedrat e HR A 201 3 CP T HC1/C1 2Test 2.1 3 lb/l b C1 2 Minimu mCarrier

Flui dFlowrat

e HR A 201 3 CP T HC1/C1 2Test 3.1 0 gal/lb C1 2 Emissio n Limi t

fo r Carbo n Monoxid e HR A 10 0 ppm v correcte dt

o 7 % 0 2 HR A - Hourl y Rollin g Averag e 12 -HR A - 12 -Hou r Rollin g Averag e

1 Measure da

s th e SD A (Spra

y Dryer/Absorber

) Outle t Temperature .



### 2 0

### Tabl e 5-3 . Uni t 2 Developmen t o f HW C MAC T Operatin g Limit s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

3 RCR A Tria l Burn 201

3 CP T Destructio

n an d Remova

l Efficienc

y 99.99 % >99.99970

% 1 Minimu mCombustio n Chambe r Temperatur

e i n th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R6 3 J209(i)(l)(ii) ] 1,658° F Minimu mCombustio n Chambe r Temperatur

e i n th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209G)(l)(ii) ] 1,848° F Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(j)(2)(ii) ] 15,605 acf m Maximu mTotal Hazardou s Wast e Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209Cj)(3)(ii) ] 4,01 7 lb/hr Maximu mPumpabl e Hazardou s Wast e Fee d HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(j)(3)(ii) ] 3,10 7 lb/hr Dioxins/Furan

s 2 0.2 0 ng/dsc m TEQ s correcte d t o 7 % 0 2 0.0091 2 Minimu mCombustio n Chambe r Temperatur

e i n th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(k)(2)(ii) ] 1,703° F Minimu mCombustio n Chambe r Temperatur

e i n th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [4 0 CFR63.1209(k)(2)(ii) ] 1,881° F Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(3)(i) ] 15,697 acf m Maximu mTotal Hazardou s Wast e Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(4)(ii) ] 4,43 0 lb/hr Maximu mPumpabl e Hazardou s Wast e Fee d HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(4)(ii) ] 3,51 8 lb/hr Maximu mBaghous e Inlet Temperature 3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(l)(i) ] 420° F



### 2 1

### Tabl e 5-3 . Uni t 2 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

3 RCR A Tria l Burn 201

3 CP T Mercur y 2 13 0 ug/dsc m correcte d t o 7 % O 2 <10 0 Maximu mFeedrat

e o f Total Mercur

y 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(0(1) ] 0.0021 2 lb/hr Particulat

e Matte r 2 0.01 3 grains/dsc

f correcte d t o 7 % 0 2 <0.0007 1 Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(m)(2)(i) ] 15,41 2 acf m Maximu mFeedrat

e o f As h 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(m)(3) ] 503. 0 lb/hr Semivolatil

e Metal s - SV M (Pb , Cd

) 2 23 0 ug/dsc m correcte d t o 7 % 0 2 <0.9 5 Lo w Volatil e Metal s - LV M (As , Be, Cr) 2 9 2 ug/dsc m correcte d t o 7 % 0 2 <2. 6 Maximu mTotal Feedrat

e o f SV M (Pb , Cd ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(A) ] 61. 9 lb/hr Maximu mTota l Feedrat

e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(B) ] 46. 3 lb/h r Maximu mPumpabl e Feedrat e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(C) ] 46. 3 lb/hr Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(n)(5)(i) ] 15,697 acf m Maximu mFeedrat

e o f Total Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(n)(4) ] 206. 1 lb/hr Maximu mBaghous e Inlet Temperatur

e 3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(n)(l) ] 420° F



### 2 2

### Tabl e 5-3 . Uni t 2 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

3 RCR A Tria l Burn 201

3 CP T Hydrochloric Aci d an

d Chlorin

e Ga s (HC1/C1 2 ) 2 3 2 ppm v combine

d a s CI " equivalents

, correcte d t o 7 % 0 2 <0.2 0 Maximu mFeedrat

e o f Total Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(l) ] 206. 1 lb/hr Maximu mFlu e Ga s Flo w HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(o)(2)(i) ] 15,55 7 acf m Minimu mSorben

t Feedrat e HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(4)(i) ] 2.2 4 Lb/l b C1 2 Minimu mCarrier

Flui dFlowrat

e HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(4)(ii) ] 1.9 0 Gal/l b C1 2 Tota l Hydrocarbon

s (THC ) 4 1 0 ppm v correcte

d t o 7 % 0 2 0.7 5 ppm v Carbo n Monoxid

e (CO ) 4 10 0 ppm v correcte

d t o 7 % 0 2 0.05 ppm v

1 Lowes t valu e measured , fo r

carbo n tetrachloride an

dmonochlorobenzene . Al l DRE s determinedt o be >99.99% . DR E measure dfo r th e semivolatil e POH C trichlorobenzene , an dth e volatil e POHC s carbo n tetrachloride an dmonochlorobenzene . Trichlorobenzen e an dmonochlorobenzene ar

e i n Clas s 1 o f

th e Therma l Stabilit y Index ; carbon tetrachloride i s i n Clas s 4 . 2Averag e value . 3 Measure da

s th e SD A (Spra

y Dryer/Absorber) Outlet Temperature . 4Averag e valu e secon

dhal f o f test .



### 2 3

### Tabl e 5-4 . Uni t 3 Developmen t o f HW C MAC T Operatin g Limit s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

6 RCR A Tria l Burn 201

3 CP T Destructio

n an d Remova

l Efficienc

y 99.99 % >99.99983

% 1 Minimu mCombustio n Chambe r Temperatur

e i n th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209())(l)(ii) ] 1,627° F Minimu mCombustio n Chambe r Temperatur

e i n th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(i)(l)(ii) ] 1,845° F Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(j)(2)(ii) ] 16,06 1 acf m Maximu mTotal Hazardou s Wast e Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63T209(j)(3)(ii) ] 5,09 8 lb/hr Maximu mPumpabl e Hazardou s Wast e Fee d HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(j)(3)(ii) ] 4,04 5 lb/hr Dioxins/Furan

s 2 0.2 0 ng/dsc m TEQ s correcte d t o 7 % 0 2 0.0011 8 Minimu mCombustio n Chambe r Temperatur

e i n th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(k)(2)(ii) ] 1,709° F Minimu mCombustio n Chambe r Temperatur

e i n th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(k)(2)(ii) ] 1,885° F Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(3)(i) ] 15,41 7 acf m Maximu mTotal Hazardou s Wast e Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(4)(ii) ] 4,41 0 Ib/h r Maximu mPumpabl e Hazardou s Wast e Fee d HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(4)(ii) ] 3,52 7 lb/hr Maximu mBaghous e Inlet Temperatur

e 3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(l)(i) ] 420° F



### 2 4

### Tabl e 5-4 . Uni t 3 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin

g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin

g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

6 RCR A Tria l Burn 201 3 CP T Mercury 2 13 0 ug/dsc m correcte

d t o 7 % 0 2 <4 8 Maximu mFeedrat

e o f Tota l Mercury 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.12090X1) ] 0.00220 lb/hr Particulat

e Matter 2 0.01 3 grains/dsc

f correcte d t o 7 % 0 2 0.0020 0 Maximu mFlu e Ga s Flowrate HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(m)(2)(i) ] 15,31 0 acf m Maximu mFeedrat

e o f As h 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(m)(3) ] 525. 8 lb/h r Semivolatil

e Metal s - SV M (Pb , Cd) 2 23 0 ug/dsc m correcte

d t o 7 % 0 2 <1 5 Lo w Volatil e Metal s - LV M (As

, Be , Cr) 2 9 2 ug/dsc m correcte

d t o 7 % 0 2 <9. 4 Maximu mTota l Feedrat

e o f SV M (Pb , Cd ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(A) ] 62. 3 lb/h r Maximu mTota l Feedrat

e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(B) ] 46. 1 lb/hr Maximu mPumpabl e Feedrat e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(n)(2)(i)(C) ] 46. 0 lb/h r Maximu mHu e Ga s Flowrate HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(n)(5)(i) ] 15,41 7 acf m Maximu mFeedrat

e o f Tota l Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CER63.1209(n)(4) ] 204. 2 lb/h r Maximu mBaghous e Inle t Temperature 3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(n)(l) ] 420° F



### 2 5

### Tabl e 5-4 . Uni t 3 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW C

MAC T Limi t 199

6 RCR A Tria l Burn 201

3 CP T Hydrochlori

c Aci d an d Chlorin e Ga s (HCI/C1 2 ) 2 3 2 ppm v combine

d a s CI " equivalents

, correcte d t o 7 % 0 2 <3. 6 Maximu mFeedrat

e o f Tota l Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(l) ] 204. 7 lb/h r Maximu mFlu e Gas Flo w HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(o)(2)(i) ] 15,37 8 acf m Minimu mSorben t

Feedrat e HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(4)(i) ] 2.09 Lb/l b C1 2 Minimu mCarrie r

Flui dFlowrat e HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(4)(ii) ] 1.8 4 Gal/l b C1 2 Tota l Hydrocarbon

s (THC) 3 1 0 ppm v correcte d t o 7 % 0 2 0.4 3 ppm v Carbo n Monoxid

e (CO) 3 10 0 ppm v correcte d t o 7 % 0 2 0.00 ppm v

1 Lowes t valu e measured , fo r

1,2,3-trichlorobenzene . Al l DRE s determinedt o be >99.99% . DR E measure d fo r th e semivolatil e POH C 1,2,3

- trichlorobenzene , an

dth e volatil e POHC s carbon tetrachloride an dtetrachloroethene . 1,2,3-Trichlorobenzene i s no t liste di n th

e Therma l Stabilit y Index , althoug

h 1,2, 4 -trichlorobenzen e an

d1,3,5-trichlorobenzen

e ar e liste di n Clas s 1 . Tetrachloroethen e i s i n Clas s 2 o f

th e Therma l Stabilit y Index ; carbo n tetrachloride i s i n Clas s 4 . 2Averag e value . 3 Measure da

s th e SD A (Spra

y Dryer/Absorber) Outlet Temperature . 4Averag e valu e secon

dhal f o f test .



### 2 6

### Tabl e 5-5 . Uni t 4 Developmen t o f HW C MAC T Operatin g Limit s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t 199

5 RCR A Tria l Bur n 201

3 CP T Destructio

n an d Remova

l Efficienc

y 99.99 % >99.99981%' Minimu mCombustio n Chambe r Temperatur

e i n th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(j)(l)(ii) ] 1,415° F Mmimu mCombustio n Chambe r Temperatur

e i n th e Secondar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(j)(l)(ii) ] 1 ,798 ° F Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(j)(2)(I) ] 44,90 0 acf m Maximu mTota l Hazardou s Wast e Feedrat e t o th e Primar y Combustio n Chambe

r HR A Averag e o f th e Test Ru n Maximu mHRA s [40CFR63.1209(j)(3)(ii) ] 18,66 7 lb/h r Maximu mPumpabl e Hazardou s Wast e Feedrat e t o th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(j)(3)(ii) ] 3,31 2 lb/h r Maximu mTota l (Pumpable) Hazardou s Wast e Fee d t o th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.12O90(3)(ii) ] 1,78 8 lb/h r



### 2 7

### Tabl e 5-5 . Uni t 4 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t 199

5 RCR A Tria l Bur n 201

3 CP T Dioxins/Furans 2 0.4 0 ng/dsc m TEQ s correcte d t o 7 % 0 2 0.13 7 Minimu mCombustio n Chambe r Temperatur

e i n th e Kil n HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(k)(2)(ii) ] 1,561° F Minimu mCombustio n Chambe r Temperatur

e i n th e SC C HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(k)(2)(ii) ] 1,881° F Maximu mFlu e Gas Flowrate HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(3)(i) ] 37,86 9 acf m Maximu mTota l Hazardou s Wast e Feedrat e t o th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(4)(ii) ] 10,63 2 lb/hr Maximu mPumpable Hazardou s Wast e Feedrat e t o th e Primar y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(4)(ii) ] 3,46 8 lb/h r Maximu mTota l (Pumpable) Hazardou s Wast e Fee d t o th e Secondar

y Combustio n Chambe

r HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(4)(ii) ] 1,20 3 lb/h r Maximu mBaghous e Inle t Temperature3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(k)(l)(i) ] 399° F Minimu mCarbo n Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(k)(6)(i) ] 6. 2 lb/h r Mercury 2 13 0 ug/dsc m correcte

d t o 7 % 0 2 <1 0 Maximu mFeedrat

e o f Tota l Mercury 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R63.1209(1X1) ] 0.040 1 lb/h r Minimu mCarbo n Feedrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(1)(3) ] 6. 2 lb/h r



### 2 8

### Tabl e 5-5 . Uni t 4 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t 199

5 RCR A Tria l Bur n 201

3 CP T Particulat

e Matter 2 0.01 3 grains/dsc

f correcte d t o 7 % 0 2 <0.002 1 Maximu mFlu e Gas Flowrate HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(m)(2)(i) ] 37,800 acf m Maximu mFeedrat

e o f As h 12-HR A Averag e o f th e Test Ru n Average s [40CFR63.1209(m)(3) ] 4,77 7 lb/h r Semivolatil

e Metal s - SV M (Pb , Cd ) 2 23 0 ug/dsc m correcte

d t o 7 % 0 2 <7. 8 Lo w Volatil e Metal s - LV M (As

, Be , Cr) 2 9 2 ug/dsc m correcte

d t o 7 % 0 2 <9. 7 Maximu mTota l Feedrat

e o f SV M (Pb , Cd ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R 63.1209(n)(2)(i)(A) ] 62. 0 lb/h r
Maximu mTota l Feedrat

e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R 63.1209(n)(2)(i

)(B) ] 46. 2 lb/hr
Maximu mPumpable Feedrat e o f LV M (As , Be , Cr ) 12-HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R 63.1209(n)(2)(i)(C) ] 45. 9 lb/h r
Maximu mFlu e Gas Flowrat e HR A Averag e o f th e Tes t Ru n Maximu mHRA s [4 0 CF R63.1209(n)(5)(i) ] 37,86 9 acf m Maximu mFeedrat

e o f Tota l Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(n)(4) ] 205. 0 lb/h r Maximu mBaghous e Inle t Temperature3 HR A Averag e o f th e Tes t Ru n Maximu mHRA s [40CFR63.1209(n)(l) ] 399° F



### 2 9

### Tabl e 5-5 . Uni t 4 Developmen t o f HW C MAC T Operatin g Limit s (continued ) Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t Measure d Value s Operatin g Paramete

r Averagin g Perio d Regulator

y Basi s HW

C MAC T Limi t 199

5 RCR A Tria l Bur n 201

3 CP T Hydrochlori

c Aci d an d Chlorin e Ga s (HCI /C1 2) 2 3 2 ppm v combine

d a s CI " equivalents

, correcte d t o 7 % 0 2 <1 4 Maximu mFeedrat

e o f Total Chlorine/Chlorid e 12-HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(l) ] 203. 2 lb/h r Maximu mFlu e Gas Flo w HR A Averag e o f th e Test Ru n Maximu mHRA s [40CFR63.1209(o)(2)(i) ] 37,39 3 acf m Minimu mSorben t

Feedrat e HR A Averag e o f th e Tes t Ru n Average s [40CFR63.1209(o)(4)(i) ] 2.1 3 Lb/l b C1 2
Minimu mCarrie r

Flui dFlowrat e HR A Averag e o f th e Tes t Ru n Average s [4 0 CF R 63.1209(o)(4)(ii) ] 3.1 0 Gal/l b C1 2 Tota l Hydrocarbon

s (THC) 4 1 0 ppm v correcte

d t o 7 % 0 2 0.6 5 ppm v Carbo n Monoxid

e (CO ) 4 10 0 ppm v correcte

d t o 7 % 0 2 0.0 7 ppm v

1 Lowes t valu e measured , fo r

hexachloroethane . Lowes t DR E measure

d fo r monochlorobenzen

e wa s >99.99983% . Al l DRE s determinedt o b e >99.99% . DR E measure

d fo r th e semivolatil e POHC s naphthalen e an dhexachloroethane , an

dth e volatil e POH C monochlorobenzene . Naphthalene an d monochlorobenzene ar

e liste di n Clas s 1 o f

th e Therma l Stabilit y Index . Hexachloroethane i s liste di n Clas s 5 o f th e Therma l Stabilit y Inde x Index .
2Averag e value . 3 Measure da

s th e SD A (Spra

y Dryer/Absorber) Outlet Temperature .
4Averag e valu e secon

dhal f o f test .



### 3 0

## 6. 0 Base s fo r Establishmen t o f OPL s Th e HW C MAC T ha s standard s fo r eigh t emissio n limit s an dfo r destructio n an dremova l efficienc y (DRE) . I n associatio n wit h eac h o f thes e standards , the HW C MAC T require s tha t feedrat e limit s and/o r

operatin g paramete r

limit s (OPLs ) b e establishe dfo r th e combustio n system s and/o r

fo r ai r pollutio n contro l equipment . Th e operatio n o f th e uni t withi n th e feedrat e limit s an dOPL s wil l ensure tha t th e standard s o f

th e HW C MAC T ar

e bein g continuousl y achieved . Liste dbelo w are the HW C MAC T limit s andth e feedrat e an dOPL s require dfo r eac h standard . Fo r

eac h feedrat e limi t

o r OPL , a n explanatio n i s provide dfo r the establishmen t

o f the feedrat e limi t

o r OPL . A s state d i n 4 0 CF R63.12090) , i f an operatin g parameter i s applicabl e to multipl e standard s the n th e mos t stringen t

limi t applies .



## • DR E - 4

0 CF R63.1209(j) Complianc e wit h the standar dfo r destructio n an dremova l efficienc y (DRE ) wa s demonstrate dusin g dat afro mRCR A Tria l Burn s conducte di n 199 3 fo r Uni t 2 , 199 6 fo r Uni t 3 , an d199 5 fo r

Uni t 4 . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar

e establishe dusin g dat afro mthes e tria l burns . Unit s 2 an d 3 Minimum Combustion Chamber Temperature in the PCC - 4 0 CF R63.1209(j)(l ) Minimu mcombustio n chambe r temperature i n th e PC C wa s develope ddurin g th e 199 3 RCR A Tria l Bur n fo r

Uni t 2 , 199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dth e 201 3 CP T o f Uni t 3 . Th e OP L fo r

minimu mcombustio n chambe r temperature i n th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 3 . Minimum Combustion Chamber Temperature in the SCC - 4 0 CF R63.1209(j)(l ) Minimu mcombustio n chambe r temperature i n th e SC C wa s develope ddurin g th e 199 3 RCR A Tria l Bur n fo r

Uni t 2 , th e 199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dth e 201 3 CP T o f

Uni t 3 . Th e OP L fo r

minimu mcombustio n chambe r temperatur e i n th e SC C wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 3 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(j)(2 ) Flu e ga s flowrate, as stac k ga s flowrate, i s monitore dcontinuousl y b y a n Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g the 199 3 RCR A Tria l Bur n fo r Uni t 2 an dth e 199 6 RCR A Tria l Bur n fo r Uni t 3 . Durin g th e 201 3 CP T fo r

Unit s 2 an d3 , the OP L fo r maximu mflu e ga s flowrate wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflue ga s flowrate wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g the P M testin g o f th e 201 3 CP T o f

Uni t 3 . Maximum Total

Hazardous Waste Feedrate to the PCC - 4 0 CF R63.1209(j)(3 ) Unit s 2 an d3 fee dbot h pumpabl e an dnonpumpabl e hazardou s waste s to th e PCC . Th e OP L fo r maximu mtota l hazardou s wast e feedrat e t o the PC C i s base do n th e combine dmeasure d nonpumpabl e an dpumpabl e waste feedrate s to th e PC C durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 , 199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dth e 201 3 CP T o f Uni t 3 .


### 3 1Th e OP L fo r maximu mhazardou s wast e feedrat e t

o th e PC C wa s establishe dfro mth e mos t stringen t valu e o f thes e tests , durin g the 199 3 RCR A Tria l Bur n o f Uni t 2 . Maximum Pumpable Hazardous Waste Feedrate to the PCC - 4 0 CF R63.1209(j)(3 ) Unit s 2 an d3 fee dbot h pumpabl e an dnonpumpabl e hazardou s waste s t o the PCC . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e t o the PC C i s base do n th e pumpabl e waste feedrat e t o the PC C durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 , 199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dth e 201 3 CP T o f Uni t 3 . Th e OP L fo r

maximu mpumpabl e hazardou s wast e feedrat e t o th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g the 199 3 RCR A Tria l Bu mo f Uni t 2 . 

### Uni t4 Minimum Combustion Chamber Temperature in the PCC (Kiln) - 4 0 CF R63.1209(j)(l ) Minimu mcombustio n chambe r temperatur e i n th e PC C wa s develope ddurin g th e 199 5 RCR A Tria l Bu man dth e 201 3 CP T o f Uni t 4 . Th e OP L fo r

minimu mcombustio n chambe r temperatur e i n the PC C wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e dioxins/furan s testin g o f

th e 201 3 CP T o f

Uni t 4 . Minimum Combustion Chamber Temperature in the SCC - 4 0 CF R63.1209fj)(l ) Minimu mcombustio n chambe r temperatur e i n th e SC C wa s develope ddurin g th e 199 5 RCR A Tria l Bu man dth e 201 3 CP T o f Uni t 4 . Th e OP L fo r

minimu mcombustio n chambe r temperatur e i n the SC C wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e dioxins/furan s testin g o f

th e 201 3 CP T o f

Uni t 4 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(j)(2 ) Flu e ga s flowrate , a s stac k ga s flowrate , i s monitore dcontinuousl y b y an Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 5 RCR A Tria l Bum . Durin g th e 201 3 CP T fo r Uni t 4 , th e OP L fo r

maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflue ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e HCl/C L testin g o f th e 201 3 CP T o f

Uni t 4 . Maximum Total

Hazardous Waste Feedrate to the PCC (Kiln) - 4 0 CF R63.1209(j)(3 ) Uni t 4 feed s bot h pumpabl e an dnonpumpabl e hazardou s waste s t o th e PC C (Kiln) . Th e OP L fo r maximu mtota l hazardou s wast e feedrat e t o the PC C i s base do n th e combine dmeasure d nonpumpabl e an dpumpabl e wast e feedrate s to th e PC C durin g th e 199 5 RCR A Tria l Bu man dth e 201 3 CP T o f

Uni t 4 . Th e OP L fo r

maximu mtota l hazardou s waste feedrat e t o th e PC C wa s establishe ddurin g the dioxins/furan s testin g o f the 201 3 CP T o f

Uni t 4 . Maximum Pumpable Hazardous Waste Feedrate to the PCC (Kiln) - 4 0 CF R63.1209(j)(3 ) Uni t 4 feed s bot h pumpabl e an dnonpumpabl e hazardou s waste s t o the PCC . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e t o the PC C i s base do n th e nonpumpabl e an d pumpabl e waste feedrat e to th e PC C durin g the durin g the 199 5 RCR A Tria l Bu man dth e 201 3 CP T o f Uni t 4 . Th e OP L fo r

maximu mpumpabl e hazardou s waste feedrat e to th e PC C wa s establishe ddurin g the 199 5 RCR A Tria l Bu mo f Uni t 4 . Maximum Total

(Pumpable) Hazardous Waste Feedrate t o th e SC C - 4 0 CF R63.1209(j)(3 ) Uni t 4 feed s pumpabl e hazardou s waste s t o the SCC . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e t o the SC C i s base do n th e pumpabl e waste feedrat e t o th e SC C durin g the 199 5 RCR A Tria l Bu man dth e 201 3 CP T o f Uni t 4 . Th e OP L fo r

maximu mpumpabl e hazardou s waste feedrat e t o the SC C wa s establishe ddurin g the dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 4 .



### 3 2

## • Dioxin s an d Furan s - 4 0 CF R63.1209(k

) Complianc e wit h th e standar dfo r dioxin s an dfuran s wa s demonstrate ddurin g the 201 3 CPT . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar e establishe dfro mth e 201 3 CPT . Unit s 2 an d 3 Gas Temperature at

the Inlet to a Dry Particulate Matter Control Device —

4 0 CF R63.1209(k)(l ) Th e dr y particulat e matte r contro l device s o n Unit s 2 an d3 are baghouses . Th e temperature to th e inle t o f th e baghous e i s measure das th e SD A (Spra y Dryer/Absorber ) Outle t Temperature , an d wa s develope ddurin g th e 201 3 CP T fo r Unit s 2 an d3 i n associatio n wit h th e standard s fo r Dioxins/Furan s an dMetals . Th e OP L fo r maximu mbaghous e inle t temperatur e wa s establishe d durin g th e dioxins/furan s an dmetal s testin g o f th e 201 3 CP T o f

Unit s 2 an d3 . Minimum Combustion Chamber Temperature in the PCC - 4 0 CF R63.1209(k)(2 ) Minimu mcombustio n chambe r temperature i n th e PC C wa s develope ddurin g th e 201 3 CP T fo r Uni t 2 an dthe 201 3 CP T o f Uni t 3 i n associatio n wit h the standar dfo r Dioxin s an dFurans . Th e OP L fo r minimu mcombustio n chambe r temperature i n the PC C wa s establishe dfro mth e mos t stringen t valu e o f thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 3 . Minimum Combustion Chamber Temperature in the SCC - 4 0 CF R63.1209(k)(2 ) Minimu mcombustio n chambe r temperature i n th e SC C wa s develope ddurin g th e 201 3 CP T fo r Uni t 2 an dth e 201 3 CP T o f Uni t 3 i n associatio n wit h th e standar dfo r Dioxin s an dFurans . Th e OP L fo r minimu mcombustio n chambe r temperature i n th e SC C wa s establishe dfro mth e mos t stringen t valu e o f thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 3 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(k)(3 ) Flu e gas flowrate, a s stac k ga s flowrate, i s monitore dcontinuousl y b y a n Annubar . Th e OP L fo r

maximu mflu e ga s flowrate i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 an dthe 199 6 RCR A Tria l Bur n fo r Uni t 3 . Durin g th e 201 3 CP T fo r

Unit s 2 an d3 , th e OP L fo r maximu mflue ga s flowrate wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrate wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g the P M testin g o f th e 201 3 CP T o f

Uni t 3 . Maximum Total

Hazardous Waste Feedrate to the PCC - 4 0 CF R63.1209(k)(4 ) Unit s 2 an d3 fee dbot h pumpabl e an dnonpumpabl e hazardou s waste s t o th e PCC . Th e OP L fo r maximu mtota l hazardou s wast e feedrat e to th e PC C i s base do n th e combine dmeasure d nonpumpabl e an dpumpabl e waste feedrate s t o th e PC C durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2,199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dthe 201 3 CP T o f Uni t 3 . Th e OP L fo r

maximu mhazardou s waste feedrat e to th e PC C wa s develope di n associatio n wit h th e standar dfo r

Dioxin s an dFuran s durin g th e 201 3 CP T fo r Uni t 2 an dth e 201 3 CP T o f Uni t 3 . Th e OP L fo r

maximu mhazardou s waste feedrat e to th e PC C wa s establishe dfro mth e mos t stringen t valu e o f thes e tests , durin g th e 199 3 RCR A Tria l Bur n o f Uni t 2 . Maximum Pumpable Hazardous Waste Feedrate to the PCC - 4 0 CF R63.1209(k)(4 ) Unit s 2 an d3 fee dbot h pumpabl e an dnonpumpabl e hazardou s waste s t o th e PCC . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e to th e PC C i s base do n th e pumpabl e wast e feedrat e to th e PC C durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 , 199 6 RCR A Tria l Bur n fo r Uni t 3 , th e 201 3 CP T fo r

Uni t 2 , an dth e 201 3 CP T o f Uni t 3 . Th e OP L fo r

maximu mpumpabl e wast e feedrat e t o th e PC C wa s develope di n associatio n wit h the standar dfo r Dioxin s an dFuran s durin g th e 201 3 CP T fo r

Uni t 2 an dth e 201 3 CP T o f Uni t 3 . Th e OP L fo r

maximu mpumpabl e hazardou s wast e feedrat e t o th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e 199 3 RCR A Tria l Bur n o f Uni t 2 .


### 3 3Particulate Matter Operating Limit

- 4 0 CF R63.1209(k)(5 ) No t applicable . Thi s OP L i s onl y applicabl e i f th e incinerato r

i s equippe dwit h a

n activate dcarbo n injectio n system . Carbo n i s no t injecte dint o Unit s 2 an d3 . Activated Carbon Injection Parameter Limits - 4 0 CF R63.1209(k)(6 ) No t applicable . Ther e i s n o carbo n injectio n syste mo n Unit s 2 an d3 . Carbon Bed

Parameter

Limits - 4 0 CF R63.1209(k)(7 ) No t applicable . Ther e i s no t acarbo n be do n th e incinerator s a t Sauget . Catalytic Oxidizer

Parameter

Limits - 4 0 CF R63.1209(k)(8 ) No t applicable . Ther e i s no t acatalyti c oxidize r

o n th e incinerator s a

t Sauget . 

### Uni t4 Gas Temperature at

the Inlet to a Dry Particulate Matter Control Device - 4 0 CF R63.1209(k)(l ) Th e dr y particulat e matte r contro l devic e o n Uni t 4 i s abaghouse . Th e temperatur e t o th e inle t o f th e baghous e i s measure da s th e SD A (Spra y Dryer/Absorber ) Outle t Temperature , an dwa s develope ddurin g th e 201 3 CP T fo r Uni t 4 i n associatio n wit h th e standard s fo r Dioxins/Furan s an dMetals . Th e OP L fo r maximu mbaghous e inle t temperature wa s establishe ddurin g th e dioxins/furan s an dmetal s testin g o f the 201 3 CP T o f

Uni t 4 . Minimum Combustion Chamber Temperature in the PCC (Kiln) - 4 0 CF R63.1209(k)(2 ) Minimu mcombustio n chambe r temperatur e i n th e PC C - th e kil n - wa s develope ddurin g th e 201 3 CP T fo r

Uni t 4 i n associatio n wit h th e standar dfo r Dioxin s an dFurans , an di n th e 199 5 RCR A Tria l Bur n o f

Uni t 4 fo r DRE . Th e OP L fo r

minimu mcombustio n chambe r temperature i n th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e dioxins/furan s testin g o f

th e 201 3 CP T o f

Uni t 4 . Minimum Combustion Chamber Temperature in the SCC - 4 0 CF R63.1209(k)(2 ) Minimu mcombustio n chambe r temperature i n th e SC C wa s develope ddurin g the 201 3 CP T fo r Uni t 4 i n associatio n wit h th e standar dfo r Dioxin s an dFurans , an di n th e 199 5 RCR A Tria l Bur n o f Uni t 4 fo r DRE . Th e OP L fo r

minimu mcombustio n chambe r temperatur e i n th e SC C wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 4 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(k)(3 ) Flu e ga s flowrate , a s stac k ga s flowrate , i s monitore dcontinuousl y b y an Annubar . Th e OP L fo r maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope ddurin g th e 199 5 RCR A Tria l Bur n fo r Uni t 4 . Durin g th e 201 3 CP T fo r Uni t 4 , th e OP L fo r

maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mthe mos t stringen t

valu e o f

thes e tests , durin g th e HC1/C1 2testin g o f th e 201 3 CP T o f

Uni t 4 . Maximum Total

Hazardous Waste Feedrate to the PCC (Kiln) - 4 0 CF R63.1209(k)(4 ) Uni t 4 feed s bot h pumpabl e an dnonpumpabl e hazardou s waste s t o th e PCC . Th e OP L fo r maximu mtota l hazardou s wast e feedrat e t o the PC C i s base do n th e combine dmeasure d nonpumpabl e an dpumpabl e wast e feedrate s to th e PCC . Th e OP L fo r maximu mhazardou s waste feedrat e to th e PC C wa s develope di n associatio n wit h th e standar dfo r Dioxin s an dFuran s durin g th e 201 3 CP T fo r

Uni t 4 , an di n th e 199 5 RCR A Tria l Bur n o f Uni t 4 fo r DRE . Th e OP L fo r maximu mhazardou s wast e feedrat e to th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 4 . Maximum Pumpable Hazardous Waste Feedrate to the PCC (Kiln) - 4 0 CF R63.1209(k)(4 ) Uni t 4 feed s bot h pumpabl e an dnonpumpabl e hazardou s waste s t o th e PC C - the kiln . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e to th e PC C i s base do n th e pumpabl e waste 

### 3 4feedrat e to th e PC C durin g th e 199 5 RCR A Tria l Bur n fo r Uni t 2 an dth e 201 3 CP T fo r Uni t 4 . Th e OP L fo r

maximu mpumpabl e wast e feedrat e to th e PC C wa s develope di n associatio n wit h th e standar dfo r

Dioxin s an dFuran s durin g th e 201 3 CP T fo r Uni t 4 an dth e 199 5 RCR A Tria l Bur n o f Uni t 4 fo r DRE . Th e OP L fo r

maximu mpumpabl e hazardou s waste feedrat e t o th e PC C wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e 199 5 RCR A Tria l Bur n o f Uni t 4 . Maximum Total

(Pumpable) Hazardous Waste Feedrate t o th e SC C - 4 0 CF R63.1209(j)(3 ) Uni t 4 feed s pumpabl e hazardou s waste s to th e SCC . Th e OP L fo r maximu mpumpabl e hazardou s waste feedrat e to th e SC C i s base do n th e pumpabl e waste feedrat e t o th e SC C durin g th e 199 5 RCR A Tria l Bur n an dth e 201 3 CP T o f Uni t 4 . Th e OP L fo r

maximu mpumpabl e hazardou s waste feedrat e to th e SC C wa s establishe ddurin g th e dioxins/furan s testin g o f th e 201 3 CP T o f

Uni t 4 . Particulate Matter

Operating Limit

- 4 0 CF R63.1209(k)(5 ) Th e particulat e matter

contro l devic e o n Uni t 4 i s abaghouse , an dthere are n o OPL s fo r baghouse s require db y th e HW C MACT . Activated Carbon Injection - 4 0 CF R63.1209(k)(6 ) Carbo n i s injecte dint o th e baghous e o n Uni t 4 . Th e minimu mcarbo n feedrat e wa s develope di n associatio n wit h th e standar dfo r Dioxin s an dFuran s an dth e standar dfo r Mercur y durin g th e 201 3 CP T fo r Uni t 4 . Th e OP L fo r

minimu mcarbo n feedrat e wa s establishe ddurin g th e dioxins/furan s an dmetal s testin g o f

th e 201 3 CP T o f

Uni t 4 . Carbon Bed

Parameter

Limits - 4 0 CF R63.1209(k)(7 ) No t applicable . Ther e i s no t acarbo n be do n th e incinerator s a t Sauget . Catalytic Oxidizer

Parameter

Limits - 4 0 CF R63.1209(k)(8 ) No t applicable . Ther e i s no t acatalyti c oxidize r

o n the incinerator s a

t Sauget .


## • Tota l Hydrocarbon

s - 4 0 CF R63.1209(a)(7

) Complianc e wit h the tota l hydrocarbon s standardwa s demonstrate ddurin g the 201 3 CPT . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar e th e sam

e a s fo r D R E an ddioxins/furans .



## • Mercur

y - 4 0 CF R63.1209(1

) Complianc e wit h th e standardfo r mercur y wa s demonstrate ddurin g th e 201 3 CPT . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar e establishe dfro mthe 201 3 CPT . Unit s 2 an d 3 Maximum Feedrate of Total Mercury - 4 0 CF R63.1209(1)(1 ) Th e maximu mfeedrat e o f mercur y wa s develope ddurin g th e 201 3 CP T o f Unit s 2 an d3 . Th e tota l feedrat e o f

Mercur y include s th e spikin g rate s an dth e contributio n o f mercur y wit h th e waste stream s - bot h pumpabl e an dnonpumpable , an dwa s establishe ddurin g th e metal s testin g o f the 201 3 CP T o f

Uni t 2 . Th e feedrat e fo r

mercur y ha s no t

bee n extrapolated . Wet Scrubber

- 4 0 CF R63.1209(1)(2 ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget .



### 3 5

### Minimum Pressure Drop Across a High Energy Scrubber - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(0)(3)(i ) No t applicable . Ther e i s no t ahig h energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum Pressure Drop for Low Energy Scrubber

- 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(o)(3)0i ) No t applicable . Ther e i s no t alo w energ y scrubbe r

o n th e incinerator s a

t Sauget . Minimum Liquid

Feed Pressure for

Low Energy Scrubber

- 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(o)(3)(iii ) No t applicable . Ther e i s no t ahig h energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum Liquid

to Gas Ratio - 4 0 CF R63.12090X2 ) an d4 0 CF R63.1209(o)(3)(v ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget . Activated Carbon Injection - 4 0 CF R63.1209(1)(3 ) No t applicable . Ther e i s n o carbo n injectio n syste mo n Unit s 2 an d3 . Activated Carbon Bed

- 4 0 CF R63.12090X4 ) No t applicable . Ther e i s no t acarbo n be do n th e incinerator s a t Sauget . Catalytic Oxidizer

Parameter

Limits - 4 0 CF R63.1209(k)(8 ) No t applicable . Ther e i s no t acatalyti c oxidize r

o n th e incinerator s a

t Sauget . 

### Uni t4 Maximum Feedrate of

Total Mercury - 4 0 CF R63.12090X1 ) Th e maximu mfeedrat e o f mercur y wa s develope ddurin g th e 201 3 CP T o f Uni t 4 . Th e tota l feedrat e o f

Mercur y include s th e spikin g rate s an dth e contributio n o f mercur y wit h th e wast e stream s - bot h pumpabl e an dnonpumpable , an dwa s establishe ddurin g th e metal s testin g o f the 201 3 CP T o f

Uni t 4 . Th e feedrat e fo r

mercur y ha s no t

bee n extrapolated . Wet Scrubber

- 4 0 CF R63.1209(1X2 ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget . Minimum Pressure Drop Across a High Energy Scrubber - 4 0 CF R63.12090X2 ) an d4 0 CF R 63.1209(0)(3)(i ) No t applicable . Ther e i s no t ahig h energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum Pressure Drop for Low Energy Scrubber

- 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(o)(3)(ii ) No t applicable . Ther e i s no t alo w energ y scrubbe r

o n th e incinerator s a

t Sauget . Minimum Liquid

Feed Pressure for

Low Energy Scrubber

- 4 0 CF R63.12090X2 ) an d4 0 CF R 63.1209(o)(3)(iii ) No t applicable . Ther e i s no t alo w energ y scrubbe r

o n th e incinerator s a

t Sauget . Minimum Liquid

to Gas Ratio - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R63.1209(o)(3)(v ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget . Activated Carbon Injection - 4 0 CF R63.1209(1)(3 ) Carbo n i s injecte dint o th e baghous e o n Uni t 4 . Th e OP L fo r

minimu mcarbo n feedrat e wa s develope di n associatio n wit h th e standar dfo r Dioxin s an dFuran s an dth e standar dfo r Mercur y


### 3 6durin g th e 201 3 CP T fo r

Uni t 4 . Th e OP L fo r

minimu mcarbo n feedrat e wa s establishe ddurin g th e dioxins/furan s an dmetal s testin g o f th e 201 3 CP T o f

Uni t 4 . Activated Carbon Bed

- 4 0 CF R63.1209(1)(4 ) No t applicable . Ther e i s no t acarbo n be do n th e incinerator s a t Sauget . Catalytic Oxidizer

Parameter

Limits - 4 0 CF R63.1209(k)(8 ) No t applicable . Ther e i s no t acatalyti c oxidize r

o n th e incinerator s a

t Sauget .



### • Particulat

e Matte r - 4 0 CF R63.1209(m

) Complianc e wit h th e standardfo r particulat e matter

wa s demonstrate ddurin g th e 201 3 CPT . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar e establishe dfro mth e 201 3 CPT . Control Device Operating Parameter Limits - 4 0 CF R63.1209(m)(l ) Th e HW C MAC T prescribe s OPL s fo r hig h energ y scrubber s an dwe t scrubber s use dto contro l particulat e matte r

(an dmetals) . Ther e i s n o hig h energ y scrubbe r o r we t scrubber s o n th e incinerator s a

t Sauge t use dfo r

contro l o f

particulat e matter . Th e contro l device s o n th e incinerator s a

t Sauge t that are designe dan doperate dto contro l particulat e matter (an dmetals ) are baghouses , an dth e HW C MAC T ha s n o OPL s fo r baghouses . Minimum Pressure Drop Across a High Energy Scrubber - 4 0 CF R63.1209(m)(l)(i)(A ) No t applicable . Ther e ar

e n o hig h energ y scrubber s o n th e incinerator s a t Sauget . Minimum Liquid

to Gas Ratio o r

Minimum Scrubber

Flowrate and

Maximum Flue Gas Flowrate for

a High Energy Scrubber - 4 0 CF R63.1209(m)(l)(i)(C ) No t applicable . Ther e ar

e n o hig h energ y scrubber s o n th e incinerator s a t Sauget . Minimum Blowdown Rate an dMinimum Scrubber Tank Volume or

Level- O R- Maximum Conductivity of Scrubber Water-AO CF R63.1209(m)(l)(B)(i ) No t applicable . Ther e ar

e n o we t scrubber s o n th e incinerator s a t Sauget . Minimum TankLevel-AQ CF R63.1209(m)(l)(B)(ii )

No t applicable . Ther e ar

e n o we t scrubber s o n th e incinerator s a t Sauge t 

### Unit s 2 an d 3 Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(m)(2 ) Flu e ga s flowrate , as stac k ga s flowrate , i s monitore dcontinuousl y b y a n Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h the standar dfo r DR E wa s develope d durin g the 199 3 RCR A Tria l Bur n fo r Uni t 2 an dth e 199 6 RCR A Tria l Bur n fo r Uni t 3 . Durin g th e 201 3 CP T fo r

Unit s 2 an d3 , th e OP L fo r maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g the P M testin g o f the 201 3 CP T o f

Uni t 3 . Maximum Ash Feedrate - 4 0 CF R63.1209(m)(3 ) Th e maximu mfeedrat e o f as h wa s develope ddurin g th e 201 3 CP T o f Unit s 2 an d3 , an dwa s establishe ddurin g th e P M testin g o f th e 201 3 CP T o f

Uni t 2 .



### 3 7

### Uni t4 Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(m)(2 ) Flu e ga s flowrate , a s stac k ga s flowrate , i s monitore dcontinuousl y b y a n Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 5 RCR A Tria l Bur n fo r Uni t 4 . Durin g th e 201 3 CP T fo r Uni t 4 , th e OP L fo r maximu mflu e ga s flowrat e wa s develope di n associatio n wit h the standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e HC1/C1 2testin g o f th e 201 3 CP T o f Uni t 4 . Maximum Ash Feedrate - 4 0 CF R63.1209(m)(3 ) Th e maximu mfeedrat e o f as h wa s develope ddurin g th e 201 3 CP T o f Uni t 4 , an dwa s establishe d durin g th e P M testin g o f th e 201 3 CP T o f

Uni t 4 .



### • Semivolatil

e Metal s an d Lo w Volatilit

y Metal s - 4 0 CR F 63.1209(n

) Complianc e wit h th e standardfo r semivolatil e metal s (SVM ) an dlo w volatilit y metal s (LVM ) wa s demonstrate ddurin g the 201 3 CPT . Applicabl e feedrate s an d OPL s associate dwit h thi s standardar e establishe dfro mth e 201 3 CPT . Unit s 2 an d 3 Maximum Inlet

Temperature to Dry Particulate Matter Air Pollution Control

Device - 4 0 CF R 63.1209(n)(l ) Th e dr y particulat e matte r contro l device s o n Unit s 2 an d3 ar e baghouses . Th e temperature t o th e inle t o f th e baghous e i s measure das th e SD A (Spra y Dryer/Absorber ) Outle t Temperature , an d wa s develope ddurin g th e 201 3 CP T fo r Unit s 2 an d3 i n associatio n wit h th e standard s fo r Dioxins/Furan s an dMetals . Th e OP L fo r maximu mbaghous e inle t temperatur e wa s establishe d durin g th e dioxins/furan s an dmetal s testin g o f th e 201 3 CP T o f

Unit s 2 an d3 . Maximum Feedrate of

Semivolatile and

Low Volatile Metals - 4 0 CF R63.1209(n)(2 ) Th e feedrate s o f

th e semivolatil e metal s (SVMs ) lea d(Pb ) an dcadmiu m(Cd) , an dth e lo w volatilit y metal s (LVMs ) arseni c (As) , berylliu m(Be) , an dchromiu m(Cr ) wer e demonstrate d durin g th e 201 3 CP T o f Unit s 2 an d3 . Th e tota l feedrate s o f th e SVM s an dLVM s includ e th e spikin g rate s an dth e contributio n o f thes e metal s wit h th e wast e stream s - bot h pumpabl e an d nonpumpable . Th e OP L fo r

maximu mfeedrat e o f

Semivolatil e Metal s (SVM ) wa s establishe ddurin g th e metal s testin g o f

th e 201 3 CP T o f

Unit s 2 an d3 . Th e OP L fo r

maximu mtota l feedrat e o f Lo w Volatilit y Metal s (LVM ) wa s establishe ddurin g th e metal s testin g o f

th e 201 3 CP T o f

Unit s 2 an d3 . Th e OP L fo r

maximu mfeedrat e o f

pumpabl e Lo w Volatilit y Metal s (LVM ) wa s establishe d durin g th e metal s testin g o f th e 201 3 CP T o f

Unit s 2 an d3 . Feedrate s fo r

SVM , tota l LVM , o r

pumpabl e LV M hav e no t bee n extrapolated .



### 3 8Control Device Operating Parameter Limits - 4 0 CF R63.1209(n)(3 ) Thes e OPL s ar

e identica l t o th e OPL s fo r the Particulat e Matte r standard . 4 0 CF R63.1209( D )(3 ) reference s 4 0 CF R63.1209(m)(l) . Th e OPL s establishe dfo r th e SV M an dLV M standard s an d the Particulat e Matte r

standar dare th e same , an dare establishe dfro mresult s o f th e 201 3 CPT . Minimum Pressure Drop Across a High Energy Scrubber

No t applicable . Ther e ar

e n o hig h energ y scrubber s o n th e incinerator s a t Sauget . Minimum Liquid

to Gas Ratio o r

Minimum Scrubber

Flowrate and

Maximum Flue Gas Flowrate for

a High Energy Scrubber No t applicable . Ther e are n o hig h energ y scrubber s o n th e incinerator s a t Sauget . Minimum Blowdown Rate an dMinimum Scrubber Tank Volume or

Level— O R- Maximum Conductivity of Scrubber

Water No t applicable . Ther e ar

e n o we t scrubber s o n th e incinerator s a t Sauget . Minimum Tank

Level - 4 0 CF R63.1209(n)(3 ) an d 4 0 CF R63.1209(m)(l)(B)(ii ) No t applicable . Ther e ar

e n o we t scrubber s o n th e incinerator s a t Sauget . Maximum Total

Chlorine and

Chloride Feedrate - 4 0 CF R63.1209(n)(4 ) Th e HW C MAC T prescribe s th e establishmen t o f th e feedrat e o f

tota l chlorin e an dchlorid e i n associatio n wit h bot h th e SV M an dLV M an d th e HC1/C1 2standards . Th e emissio n limit s fo r SVM , LV M (i.e. , metals), , an dHC1/C1 2wer e demonstrate di n th e 201 3 CPT . Th e feedrat e o f tota l chlorin e an dchlorid e include s th e spikin g rat e an dthe contributio n o f chlorin e wit h th e wast e stream s - bot h pumpabl e an dnonpumpable . Th e OP L fo r th e maximu mfeedrat e o f tota l chlorin e an dchlorid e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e metal s testin g o f the 201 3 CP T o f

Uni t 3 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(n)(5 ) Flu e ga s flowrate , as stac k ga s flowrate , i s monitore dcontinuousl y b y a n Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar d fo r DR E wa s develope d durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 an dth e 199 6 RCR A Tria l Bur n fo r Uni t 3 . Durin g th e 201 3 CP T fo r

Unit s 2 an d3 , th e OP L fo r maximu mflu e ga s flowrat e wa s develope d i n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an d Dioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e P M testin g o f th e 201 3 CP T o f

Uni t 3 . 

### Uni t4 Maximum Inlet

Temperature to Dry Particulate Matter Air Pollution Control

Device —

4 0 CF R 63.1209(n)(l ) Th e dry particulat e matte r contro l devic e o n Uni t 4 i s abaghouse . Th e temperatur e t o th e inle t o f th e baghous e i s measure da s the SD A (Spra y Dryer/Absorber ) Outle t Temperature , an dwa s develope ddurin g th e 201 3 CP T fo r Uni t 4 i n associatio n wit h th e standard s fo r Dioxins/Furan s an dMetals . Th e OP L fo r maximu mbaghous e inle t temperatur e wa s establishe ddurin g th e dioxins/furan s an dmetal s testin g o f th e 201 3 CP T o f

Uni t 4 . Maximum Feedrate of Semivolatile and

Low Volatile Metals - 4 0 CF R63.1209(n)(2 ) Th e feedrate s o f

the semivolatil e metal s (SVMs ) lea d(Pb ) an dcadmiu m(Cd) , an dth e lo w volatilit y metal s (LVMs ) arseni c (As) , berylliu m(Be) , an dchromiu m(Cr ) wer e demonstrate d durin g th e 201 3 CP T o f Uni t 4 . Th e tota l feedrate s o f th e SVM s an dLVM s includ e th e spikin g rate s an dth e contributio n o f thes e metal s wit h th e waste stream s - bot h pumpabl e an d nonpumpable . Th e OP L fo r

maximu mfeedrat e o f Semivolatil e Metal s (SVM ) wa s establishe d durin g th e metal s testin g o f

th e 201 3 CP T o f

Uni t 4 . 

### 3 9Th e OP L fo r maximu mtota l feedrat e o f Lo w Volatilit y Metal s (LVM ) wa s establishe ddurin g th e metal s testin g o f

th e 201 3 CP T o f

Uni t 4 . Th e OP L fo r

maximu mfeedrat e o f

pumpabl e Lo w Volatilit y Metal s (LVM ) wa s establishe d durin g the metal s testin g o f th e 201 3 CP T o f

Uni t 4 . Feedrate s fo r

SVM , tota l LVM , o r

pumpabl e LV M hav e no t bee n extrapolated . Control Device Operating Parameter Limits - 4 0 CF R63.1209(n)(3 ) Thes e OPL s are identica l t o th e OPL s fo r th e Particulat e Matte r

standard . 4 0 CF R63.1209(n)(3 ) reference s 4 0 CF R63.1209(m)(l) . Th e OPL s establishe dfo r th e SV M an dLV M standard s an dthe Particulat e Matte r

standar dar

e th e same , an dar

e establishe dfro mresult s o f th e 201 1 CPT . Minimum Pressure Drop Across a High Energy Scrubber

No t applicable . Ther e ar

e n o hig h energ y scrubber s o n the incinerator s a t Sauget . Minimum Liquid

to Gas Ratio o r

Minimum Scrubber

Flowrate and

Maximum Flue Gas Flowrate for

a High Energy Scrubber No t applicable . Ther e ar

e n o hig h energ y scrubber s o n the incinerator s a t Sauget . Minimum Blowdown Rate an dMinimum Scrubber Tank Volume or

Level- O R- Maximum Conductivity of Scrubber

Water No t applicable . Ther e are n o we t scrubber s o n th e incinerator s a t Sauget . Minimum Tank

Level - 4 0 CF R63.1209(n)(3 ) an d4 0 CF R63.1209(m)(l)(B)(ii ) No t applicable . Ther e ar

e n o we t scrubber s o n th e incinerator s a t Sauget . Maximum Total

Chlorine and

Chloride Feedrate - 4 0 CF R63.1209(n)(4 ) Th e HW C MAC T prescribe s th e establishmen t o f th e feedrat e o f

tota l chlorin e an dchlorid e i n associatio n wit h bot h th e SV M an dLV M an dthe HC1/C1 2standards . Th e emissio n limit s fo r SVM , LV M (i.e. , metals), , an dHC1/C1 2wer e demonstrate di n th e 201 3 CPT . Th e feedrat e o f tota l chlorin e an dchlorid e include s th e spikin g rat e an dth e contributio n o f chlorin e wit h th e wast e stream s - bot h pumpabl e an dnonpumpable . Th e OP L fo r th e maximu mfeedrat e o f tota l chlorin e an dchlorid e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e HC1/C1 2 testin g o f

th e 201 3 CP T o f

Uni t 4 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(n)(5 ) Flu e ga s flowrate , a s stac k ga s flowrate , i s monitore dcontinuousl y b y an Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 5 RCR A Tria l Bur n fo r Uni t 4 . Durin g th e 201 3 CP T fo r Uni t 4 , th e OP L fo r maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e HC1/C1 2testin g o f th e 201 3 CP T o f Uni t 4 .



### • Hydrochlori

c Aci d an

d Chlorin

e Ga s - 4 0 CF R63.1209(o

) Complianc e wit h the standardfo r hydrochlori c aci dan dchlorin e gas (HCI /CI2 ) wa s demonstrate ddurin g the 201 3 CPT . Applicabl e feedrate s an dOPL s associate dwit h thi s standardar

e establishe dfro mth e 201 3 CPT .

4 0

### Unit s 2 an d 3 Maximum Total

Chlorine and

Chloride Feedrate - 4 0 CF R63.1209(o)(l ) Th e HW C MAC T prescribe s th e establishmen t o f th e feedrat e o f

tota l chlorin e an dchlorid e i n associatio n wit h bot h th e SV M an dLV M an dthe HC1/C1 2standards . Th e emissio n limit s fo r SVM , LV M (i.e. , metals), , an dHC1/C1 2wer e demonstrate di n th e 201 3 CPT . Th e feedrat e o f tota l chlorin e an dchlorid e include s th e spikin g rat e an dth e contributio n o f chlorin e wit h th e waste stream s - bot h pumpabl e an dnonpumpable . Th e OP L fo r th e maximu mfeedrat e o f tota l chlorin e an dchlorid e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e metal s testin g o f th e 201 3 CP T o f

Uni t 3 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(o)(2 ) Flu e ga s flowrate , a s stac k ga s flowrate , i s monitore dcontinuousl y b y an Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 3 RCR A Tria l Bur n fo r Uni t 2 an dth e 199 6 RCR A Tria l Bur n fo r Uni t 3 . Durin g th e 201 3 CP T fo r

Unit s 2 an d3 , th e OP L fo r maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f thes e tests , durin g th e P M testin g o f th e 201 3 CP T o f

Uni t 3 . Dry Scrubber

- 4 0 CF R63.1209(o)(4 ) Th e contro l device s o n th e incinerator s a t Sauge t tha t are designe dan doperate dto contro l HC 1 an dCl 2are Spra y Dryer/Absorbers , considere das Dr y Scrubbers . Th e HW C MAC T prescribe s the establishmen t

o f OPL s fo r

dr y scrubber s i n associatio n wit h th e HC1/C1 2standard . Minimum Sorbent

Feedrate - 4 0 CF R63.1209(o)(4)(i ) Th e HW C MAC T prescribe s th e establishmen t o f an OP L fo r

sorben t feedrat e t

o adr y scrubber . Th e OP L fo r

the minimu mfeedrat e o f sorben t to th e Spra y Dryer/Absorbe r (SDA ) i s measure das th e feedrat e o f

lim e t o the SDA , an dwa s develope ddurin g th e 201 3 CP T fo r Unit s 2 an d3 i n associatio n wit h th e standar dfo r HC1/C1 2 . Th e OP L fo r

minimu msorben t

feedrat e t o th e SD A wa s establishe ddurin g th e HC1/C1 2testin g o f th e 201 3 CP T o f

Uni t 2 . Minimum Carrier

Fluid Flowrate or

Nozzle Pressure Drop - 4 0 CF R63.1209(o)(4)(ii ) Th e HW C MAC T prescribe s th e establishmen t o f a n OP L fo r

carrie r flui dflowrat e t o adr y scrubber . Th e OP L fo r

the minimu mcarrie r

flui dflowrat e t o th e Spra y Dryer/Absorbe r (SDA ) wa s develope ddurin g th e 201 3 CP T fo r Unit s 2 an d3 i n associatio n wit h th e standar dfo r HC1/C1 2 . Th e OP L fo r

minimu msorben t

feedrat e to th e SD A wa s establishe ddurin g th e HC1/C1 2testin g o f th e 201 3 CP T o f

Uni t 2 . Wet Scrubber

- 4 0 CF R63.1209(o)(3 ) Th e HW C MAC T prescribe s tha t operatin g paramete r

limit s fo r

we t scrubber s b e establishe d unde r th e hydrochlori c aci dan dchlorin e ga s standar dfoun di n 4 0 CF R63.1206(o)(3) . No t applicable . Ther e i s no t awe t scrubbe r

o n the incinerator s a

t Sauget . Minimum Pressure Drop Across a High Energy Scrubber - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(0)(3)(i ) No t applicable . Ther e i s no t ahig h energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum Liquid

Feed Pressure for

Low Energy Scrubber - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(o)(3)(iii ) No t applicable . Ther e i s no t alo w energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum pH

- 4 0 CF R63.1209(o)(3)(iv ) No t applicable . Ther e i s no t awe t scrubbe r

o n the incinerator s a

t Sauget .



### 4 1Minimum Liquid to Gas Ratio - 4 0 CF R63.1209(o)(3)(v ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget . 

### Uni t4 Maximum Total

Chlorine and

Chloride Feedrate - 4 0 CF R63.1209(o)(l ) Th e HW C MAC T prescribe s th e establishmen t o f th e feedrat e o f

tota l chlorin e an dchlorid e i n associatio n wit h bot h th e SV M an dLV M an dth e HC1/C1 2standards . Th e emissio n limit s fo r SVM , LV M (i.e. , metals), , an dHC1/C1 2wer e demonstrate di n th e 201 3 CPT . Th e feedrat e o f tota l chlorin e an dchlorid e include s the spikin g rat e an dth e contributio n o f chlorin e wit h th e wast e stream s - bot h pumpabl e an dnonpumpable . Th e OP L fo r th e maximu mfeedrat e o f tota l chlorin e an dchlorid e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e HC1/C1 2 testin g o f

th e 201 3 CP T o f

Uni t 4 . Maximum Flue Gas Flowrate or Production Rate - 4 0 CF R63.1209(o)(2 ) Flu e ga s flowrate , as stac k ga s flowrate , i s monitore dcontinuousl y b y an Annubar . Th e OP L fo r

maximu mflu e ga s flowrat e i n associatio n wit h th e standar dfo r DR E wa s develope d durin g th e 199 5 RCR A Tria l Bur n fo r Uni t 4 . Durin g th e 201 3 CP T fo r Uni t 4 , the OP L fo r maximu mflu e ga s flowrat e wa s develope di n associatio n wit h th e standard s fo r PM , HC1/C1 2 , SVM , LVM , Mercury , an dDioxins/Furans . Th e OP L fo r maximu mflu e ga s flowrat e wa s establishe dfro mth e mos t stringen t

valu e o f

thes e tests , durin g th e HC1/C1 2testin g o f th e 201 3 CP T o f Uni t 4 . Dry Scrubber

- 4 0 CF R63.1209(o)(4 ) Th e contro l device s o n th e incinerator s a t Sauge t tha t are designe dan doperate dt o contro l HC 1 an dCl 2ar

e Spra y Dryer/Absorbers , considere da s Dr y Scrubbers . Th e HW C MAC T prescribe s th e establishmen t

o f OPL s fo r

dr y scrubber s i n associatio n wit h th e HC1/C1 2standard . Minimum Sorbent

Feedrate - 4 0 CF R63.1209(o)(4)(i ) Th e HW C MAC T prescribe s the establishmen t o f an OP L fo r

sorben t feedrat e t o adr y scrubber . Th e OP L fo r

th e minimu mfeedrat e o f sorben t t o the Spra y Dryer/Absorbe r (SDA ) i s measure da s th e feedrat e o f

lim e to th e SDA , an dwa s develope ddurin g th e 201 3 CP T fo r Uni t 4 i n associatio n wit h th e standar dfo r

HC1/C1 2 . Th e OP L fo r minimu msorben t

feedrat e to th e SD A wa s establishe d durin g th e HC1/C1 2testin g o f th e 201 3 CP T o f

Uni t 4 . Minimum Carrier

Fluid Flowrate or

Nozzle Pressure Drop - 4 0 CF R63.1209(o)(4)(ii ) Th e HW C MAC T prescribe s th e establishmen t o f an OP L fo r

carrie r flui dflowrat e to adr y scrubber . Th e OP L fo r th e minimu mcarrie r

flui dflowrat e t o th e Spra y Dryer/Absorbe r (SDA ) wa s develope ddurin g th e 201 3 CP T fo r Uni t 4 i n associatio n wit h th e standar dfo r HC1/C1 2 . Th e OP L fo r minimu msorben t

feedrat e to th e SD A wa s establishe ddurin g th e HC1/C1 2testin g o f th e 201 3 CP T o f

Uni t 4 . Wet Scrubber

- 4 0 CF R63.1209(o)(3 ) Th e HW C MAC T prescribe s tha t operatin g paramete r

limit s fo r

we t scrubber s b e establishe d unde r th e hydrochlori c aci dan dchlorin e ga s standar dfoun di n 4 0 CF R63.1206(o)(3) . No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget . Minimum Pressure Drop Across a High Energy Scrubber - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(0)(3)(i ) No t applicable . Ther e i s no t ahig h energ y scrubbe r o n th e incinerator s a

t Sauget . Minimum Liquid

Feed Pressure for

Low Energy Scrubber - 4 0 CF R63.1209(1)(2 ) an d4 0 CF R 63.1209(o)(3)(iii ) No t applicable . Ther e i s no t alo w energ y scrubbe r o n th e incinerator s a

t Sauget .



### 4 2Minimum pH - 4 0 CF R63.1209(o)(3)(iv ) No t applicable . Ther e i s no t awe t scrubbe r

o n the incinerator s a

t Sauget . Minimum Liquid

to Gas Ratio - 4 0 CF R63.1209(o)(3)(v ) No t applicable . Ther e i s no t awe t scrubbe r

o n th e incinerator s a

t Sauget .


## • Carbon Monoxid

e - 4 0 CF R63.1203(a)(l)(i

) Complianc e wit h the standardfo r carbo n monoxid e wa s demonstrate da t al l time s durin g th e 201 3 CPT . 

## • Maximu

m Combustio

n Chambe

r Pressur

e - 4 0 CF R63.1206(c)(5

) an d 4 0 CF R 63.1209(p

) Unit s 2 an d 3 Combustio n syste mleak s ar e prevente dthroug h maintainin g atotall y seale dcombustio n chamber , couple dwit h th e us e o f an induce ddraf

t fa n tha t maintain s avacuu mo f 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 are bein g fe dt o the unit . 

### Uni t4 Th e kil n i s equippe dwit h adoubl e sea l syste mtha t i s comprise do f

overlapping , adjustable , stainles s stee l sprin g plate s o n both th e fee dan ddischarg e end s o f the kiln . Th e sealin g edge s o f eac h plate ar

e fitte d wit h asintered-meta l wea r sho e simila r

t o abrake sho e wit h the inne r seal restin g o n th e kil n shell . Th e powdere dmeta l formulatio n fo r the seal shoe s includ e graphit e granules , whic h mak e the shoe s self

lubricating . Th e voi dbetwee n the seal s an dth e outer shel l o f th e kil n i s pressurize dt o furthe r preven t fugitiv e emissions . I n additio n to the kil n seal system , Uni t 4 als o utilize s a

n induce ddraf

t fa n tha t maintain s avacuu mo f

- 0. 5 t o - 1. 0 inche s water

colum n whil e waste i s bein g fire dint o th e system .



## • Hazardou

s Wast e Residenc

e Tim e - 4 0 CF R63.1206(b)(ll

) Unit s 2 an d 3 Th e hazardou s wast

e ga s residenc e tim e fo r Uni t 2 i s calculate da s follow s usin g th e OP L fo r

the stac k ga s flowrat e i n th e curren t

NOC :

• Primar y Combustio n Chambe r Volum e - 63 5 ft 3 ; • Secondar y Combustio n Chambe r Volum e - 63 5 ft 3 ; • Tota l Volume-1,27 0 ft 3 ; • Maximu mFlu e Ga s Howrat e - 15,14 7 acf m(25 2 frVsec) ; an d
• Tota l Combustio n Zon e Residenc e Tim e = (1,27 0 ft 3 ) / 25 2 ftVsec ) = 5. 0 sec . Sinc e Uni t

2 i s afixe dhearth unit , residenc e tim e i s base do n th e trave l lengt h o f th e as h ra mtha

t function s to clea r

the primar y combustio n chambe r o f soli dwast e residue . A trave l length o f 11 0 inche s fo r

th e as h ra mha s bee n establishe das the criteri afo r determinin g whe n soli dwast e i s n o longe r i n th e combustio n zone . I n th e cas e o f a n as h ra mfailure , a

n elapse dtim e o f

on e hou r

ha s bee n establishe da s th e criteri afo r determinin g whe n soli dwast e i s n o longe r i n th e combustio n zone .



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### Uni t4 Th e hazardou s waste ga s residenc e tim e fo r th e Uni t 4 Rotar y Kil n Incinerato r i s calculate das follows :

" Rotar y Kil n Volum e - 1,34 6 ft 3 ;

• Secondar y Combustio n Chambe r Volum e - 3,08 4 ft 3 ;

• Tota l Volum e - 4,43 0 ft 3 ;

• Maximu mFlu e Ga s Flowrat e - 37,43 2 acfm(62 4 ft 3 /sec) ; an d

• Tota l Combustio n Zon e Residenc e Tim e = (4,43 0 ft 3 ) / (62 4 ftVse c = 7. 1 sec . Solid s residenc e tim e i n th e Uni t 4 kil n i s dependen t

upo n th e kil n rotatio n rate , solid s be ddepth , an da numbe r o f othe r parameter s set

b y design . Th e maximu msolid s hazardou s waste residenc e tim e fo r th e Uni t 4 incinerato r

(i.e. , i n the rotar y kiln ) i s 3 0 minute s base do n calculation s usin g an equatio n fro m Chemica l Engineerin g Handbook , Perry' s 5 * Edition . Base do n the equation : 0 = [(O.19L)/(NDS) ] Where : 0 i s th e residenc e tim e i n minutes , Li s th e kil n lengt h i n feet , N i s the rotationa l spee di n revolution s pe r minute , S i s th e kil n slop e i n fee t pe r feet , an d D i s th e interna l diamete r i n feet . Insertin g the know n value s fo r L (35) , N (2) , S (0.0174) , an dD (6.5 ) resul t i n asolid s residenc e tim e fo r th e rotar y kil n o f

3 0 minutes .



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