APPENDI X G STARTUP , SHUTDOWN , AN D MALFUNCTIO N PLA N

### STARTUP , SHUTDOW N AN D MALFUNCTIO N PLA N Prepare dfor : Veoli aE S Technica l Solutions , LL C

Sauget , Illinoi s

Prepare dby : Frankli n Engineerin g Group , Inc . Franklin , Tennesse e

October200

8TABL E O F CONTENT S

1. 0 INTRODUCTIO N 1 1. 1 REGULATOR Y REQUIREMENT S 2 1. 2 RECORDKEEPIN GAN D REPORTIN GPROCEDURE S 2 1.2.1 Records 4 1.2.2 Reports 4 2. 0 ENGINEERIN G DESCRIPTIO N 6 3. 0 STARTU PAN D SHUTDOW N PROCEDURE S 1 3 3. 1 STARTU P1 3 3. 2 NORMA LSHUTDOW N1 5 4. 0 MALFUNCTION S 1 6 4. 1 MEASURE S T O MINIMIZ ETH EFREQUENC Y O FMALFUNCTION S 1 6 4. 2 MEASURE S T O MINIMIZ ETH ESEVERIT Y O FMALFUNCTION S 1 8 4. 3 CORRECTIV EMEASURE S 1 9

iLIS T O F TABLE S TABL E1 - 1 OVERVIE WO FREGULATION S REGARDIN GSTARTUP , SHUTDOW NAN D

MALFUNCTIO N3 TABL E4- 1 SUMMAR Y O FPOTENTIA LMALFUNCTION S AN D CAUSE S 1 7 TABL E4- 2 REDUNDAN T EQUIPMEN T AN D SYSTEM S FO RMINIMIZIN GTH EFREQUENC Y

O RSEVERIT Y O FMALFUNCTION S 2 0

LIS T O F FIGURE S FIGUR E2- 1 FIXE D HEART H INCINERATOR , UNI T 2 , BLOC K FLO WDIAGRA M 7 FIGUR E2- 2 FFXE D HEART H INCINERATOR , UNI T 3 , BLOC K FLO WDIAGRA M 8 FIGUR E2- 3 ROTAR Y KIL NINCINERATOR , UNI T 4 , BLOC K FLO WDIAGRA M 1 1

LIS T O F ATTACHMENT S ATTACHMEN T 1 STARTU PRECORDKEEPIN GFOR M ATTACHMEN T 2 SHUTDOW NRECORDKEEPIN GFOR M ATTACHMEN T 3 MALFUNCTIO NRECORDKEEPIN GFOR M ATTACHMEN T 4 PROGRA M O FCORRECTIV EACTION S FO RMALFUNCTION S

i i1.

0 INTRODUCTIO N Veoli aE S Technica l Solutions , LL C (Veolia ) own s an doperate s tw o fixedheart hincinerator s (Unit s 2 an d3 ) an darotary kil nincinerato r (Uni t 4 ) a t it s facilit y locate di n Sauget , Illinois . Th e incinerator s ar

e subjec t

to th e Nationa l Emission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r

Hazardou s Wast e Combustor s (HWC) , 4 0 CFR , Part 63 , Subpar

t EE E( § 63.120 0 to § 63.1221) . Th e NESHA Pspecifie s emission s standard s whic hreflec t emission s performanc e o f Maximu mAchievabl e Contro l Technologie s (MACT) , an di s commonl y referre dto as th e H W C MACT . Th e HW C MAC T Standarddefine s th e contro l o f emission s durin g normal , day-to-da y operations . I n order to addres s th e contro l o f emission s durin g transien t periods , the developmen t

o f aStartup , Shutdown , an dMalfunctio n Pla n (SSMP ) i s required . Startup , shutdown , an dmalfunctio n (SSM ) ar e define di n § 63. 2 a

s follows :

• Startup - th e settin g i n operatio n o f an affecte dsourc e o r

portio n o f

an affecte dsourc e fo r an y purpos e

• Shutdown - th e cessatio n o f operatio n o f

a n affecte dsourc e o r

portio n o f

an affecte d sourc e fo r

an y purpos e

• Malfunction - an y sudden , infrequent , an dno t reasonabl y preventabl e failur e o f ai r pollutio n contro l an dmonitorin g equipment , proces s equipment , o r aproces s to operat

e i nanorma l or

usua l manner

whic hcauses , o r

ha s th e potentia l to cause , th e emissio n limitation s i n an applicabl e standardto b e exceeded . Failure s tha t ar e cause di n part

b y poo r maintenanc e o r

careles s operatio n ar

e no t malfunction s Durin g thes e transien t

period s o f

operations , asourc e mus t confor mwit hit s SSMP . Therefore , durin g period s o f

startup , shutdown , an dmalfunction s th e operatin g an dmaintainin g o f the incinerato r

wil l b e consisten t

wit hth e procedure s an dcorrectiv e action s tha t ar e prescribe di n thi s plan . Thi s wil l ensur e tha t emission s ar

e minimized , to th e extent practical . Th e purpos e o f

thi s startup , shutdown , an dmalfunctio n pla n i s to :

• Prescrib e procedure s fo r operatin g the incinerato r system s durin g period s o f startup , shutdown , an dmalfunctio n tha t ar e consisten t

wit hsafety an dgoo dai r pollutio n contro l practice s

• Describ e measure s fo r th e preventio n an dminimizatio n o f exces s emission s durin g period s o f

startup , shutdown , an dmalfunctio n

• Reduc e th e reportin g burde n associate dwit hperiod s o f startup , shutdown , an d malfunctio n

• Satisf

y th e requirement s o f

§ 63.1206(c ) an d§ 63.6(e)(3) , as show n i n Tabl e 1- 1

1Du e t o the similarit y o f th e thre e incinerato r

systems , general reference s to an incinerato r i n thi s documen t

wil l impl y al l thre e incinerato r systems . Infonnatio n tha t i s onl y applicabl e t o on e o r tw o o f the thre e unit s wil l b e clearl y identifie deither parentheticall y o r

delineate db y th e sectio n heading . A s require db y § § 63.6(e)(v ) an d63.6(e)(vi) , thi s pla n an dother document s containin g procedure s o r

informatio n referre dto i n thi s pla n wil l b e mad e availabl e fo r inspectio n whe n requeste db y th e Administrator . I f Veoli ai s require dto submi t copie s o f

thi s pla n o r

portion s o f thi s pla n (o r

relate ddocuments ) confidentia l busines s informatio n entitle dto protectio n from disclosur e wil l b e clearl y designated . Th e remainde r

o f thi s sectio n provide s an overvie w o f regulator y requirement s an daprogra mfo r complianc e wit hth e recordkeepin g an dreportin g requirements . Sectio n 2. 0 reference s an engineerin g descriptio n o f the incinerator , ai r

pollutio n contro l system , an dcontinuou s monitorin g system . Sectio n 3. 0 addresse s th e startu p an dshutdow n o f

the incinerato r

system . Sectio n 4. 0 addresse s potentia l malfunction s o f th e incinerato r

system . 1.1 Regulator

y Requirement

s On e o f the objective s fo r

thi s documen t

i s to establis haprogra mtha t wil l ensure complianc e wit hrelevan t

section s o f

the Interi mMAC T Standards . Tabl e 1- 1 include s th e regulator y requirement s an dth e locatio n o f eac hrequiremen t

addresse dherein . 1. 2 Recordkeepin g and Reportin g Procedures Thi s sectio n addresse s th e recordkeepin g an dreportin g requirement s relate dto period s o f SSM . Th e startup , shutdown , an dmalfunctio n report s discusse di n thi s pla n ensur e tha t Veoli ai s satisfyin g th e general duty to minimiz e emission s an ddocumen t tha t action s taken durin g thos e period s ar

e consisten t

wit hthi s plan . Thes e report s an drecord s provid e th e necessary documentatio n to shiel dtransient event s fromth e HW C MAC T emissio n standard s impose do n steady-state operations . A s lon g a

s action s take n durin g atransien t event sufficientl y maintai n th e incinerato r syste m withi n limits , ther

e i s n o justificatio n i n distinguishin g tha t event fromsteady-state operations . Fo r example , problem s ma y aris e tha t mee t th e definitio n o f

amalfunctio n ye t

do no t impac t th e abilit y to maintai n th e incinerato r syste mwithi n limits . I n thes e cases , maintainin g th e incinerato r

syste mwithi n limit s substantiate s tha t th e action s take n sufficientl y met th e objective s o f

thi s SSM Pan dminimize demission s to agreate r degre e than require db y regulations . 2Tabl e 1-1 Overview o

f Regulations Regardin g Startup , Shutdow n and Malfunctio n Regulatory Citatio n Descriptio n SSM P Section § 63.6(e)(3) ® Purpos e o f th e SSM P 1. 0 § 63.6(e)(3) ® Procedure s fo r operatin g an dmaintainin g th e sourc e durin g startup 3.1 , Tabl e 3- 1 § 63.6(e)(3)(i ) Procedure s fo r operatin g an dmaintainin g th e sourc e durin g shutdow n 3.2 , Tabl e 3- 1 § 63.6(e)(3) ® Procedure s fo r operatin g an dmaintainin g th e sourc e durin g malfunctio n Attachmen t 4 § 63.6(e)(3) ® Aprogra mo f correctiv e actio n fo r

malfunctionin g proces s Attachmen t 4 § 63.6(e)(3)(a ) Durin g SSM , operate an dmaintai n sourc e i n accordanc e wit hSSM P 1. 0 § 63.6(e)(3)(iii ) Record s an dreport s whe n action s confor mwit hSSM P 1.2. 1 § 63.6(e)(3)(iv ) Record s an dreport s whe n action s d o no t confor mwit hSSM Pan d resul t i n a n exceedanc e 1.2. 2 § 63.6(e)(3)(v ) Availabilit y o f curren t an dsupersede dSSMP s 1. 2 § 63.6(e)(3)(vi ) Us e an davailabilit y o f othe r plan s 1. 0 § 63.6(e)(3)(viii ) Revision s to th e SSM P 1.2. 2 § 63.10(b)(1 ) Maintainin g file s 1. 2 § 63.10(b)(2) ® Recor doccurrenc e an dduratio n o f eac hstartup an dshutdow n 1.2. 1 § 63.10(b)(2)(ii ) Recor doccurrenc e an dduratio n o f eac hmalfunctio n 1.2. 1 § 63.10(b)(2)(iv ) Record s o f action s inconsisten t

wit hSSM P 1.2. 1 § 63.10(b)(2)(v ) Record s demonstrating conformanc e wit hSSM P 1.2. 1 § 63.10(b)(2)(vi ) Recor dperiod s o f malfunctionin g CM S 1.2. 1 § 63.10(d)(5) ® Periodi c startup , shutdown , an dmalfunctio n report s 1.2. 2 § 63.10(d)(5)(ii ) Immediat e startup , shutdown , an dmalfunctio n report s 1.2. 2 § 63.1206(c)(2)(ii)(A ) Descriptio n o f potentia l cause s o f

malfunction s Tabl e 4-1 , Attachmen t

4 § 63.1206(c)(2)(ii)(A ) Action s to minimiz e th e frequenc y an dseverit y o f malfunction s 4.1,4. 2 Tabl e 4- 2 Attachmen t

4 § 63.1206(c)(2)(ii)(C ) Change s t o th e pla n 1.2. 2 § 63.1206(c)(2)(iii ) Projecte doxyge n correctio n facto r to us e durin g startup an d shutdow n 3. 0 § 63.1206(c)(2)(iv ) Recor dpla n i n th e operatin g recor d 1. 2 § 63.1206(c)(2)(v)(A)(l ) AWFC O requirement s durin g malfunction s 3. 0 § 63.1206(c)(2)(v)(A)(3)(i ) Investigatio n an devaluatio n o f excessiv e exceedance s durin g malfunction s 1.2. 2 § 63.1206(c)(2)(v)(A)(3)(i ) Revision s t o SSM Pdu e to excessiv e exceedance s durin g malfunction s 1.2. 2 § 63.1206(c)(2)(v)(A)(3)(ii ) Recor dresult s fro minvestigatio n an devaluatio n o f excessiv e exceedance s 1.2. 2 § 63.12006(c)(2)(v)A(3)(ii ) Addition s t o exces s emission s report [ § 63.10(e)(3) ] du e t o excessiv e exceedance s durin g malfunction s 1.2. 2 § 63.1206(c)(2)(v)(B)(l ) Wast e fee drestriction s an dothe r OPL s durin g startup an dshutdow n 3. 0 § 63.1206(c)(2)(v)(B)(2 ) Interloc k OPL s o f

(c)(2)(v)(B)(l ) wit hAWFC O syste m 3. 0 § 63.1206(c)(2)(v)(B)(3 ) AWFC O du e to exceedanc e o f startup/shutdow n OP L 3. 0

3Accordingly , th e recordkeepin g an dreportin g requirement s presente di n thi s sectio n ar e onl y applicabl e to period s o f SS M i n whic hther

e i s areasonabl e expectatio n tha t a n OP L o r emissio n standardca n no t b e met . Thi s include s al l startups , al l shutdowns , an dal l malfunction s tha

t resul t i n an exceedanc e o f

an operatin g limi t

o r emissio n standard . Malfunction s tha

t preven t the abilit y to document on-goin g complianc e ar e als o subjec t

to recordkeepin g an dreportin g requirements . Thi s plan , al l revision s t o thi s plan , an dal l record s an dreport s describe di n thi s sectio n wil l b e retaine di n th e operatin g recor dfo r a t leas t fiv e years . 1.2.1 Records SS M record s wil l includ e th e following :

• Dat e an dtim e o f

eac hSS M

• Th e duratio n o f

eac hSS M

• Documentatio n to demonstrate tha t action s taken durin g period s o f SS M ar

e consisten t

wit hthi s SSM P

• Descriptio n o f

an y action s take n durin g period s o f SS M tha

t ar e no t consisten t wit hprocedure s i n thi s SSM P

• Result s o f

investigation s an devaluation s o f excessiv e exceedance s occurrin g durin g malfunction s Attachment s 1 , 2 , an d3 ar e blan k recordkeepin g form s fo r startups , shutdowns , an d malfunctions , respectively . Th e informatio n recorde do n thes e form s wil l b e utilize dto documen t

conformanc e wit hth e SSM Pan dto compl y wit hth e reportin g requirements . Th e startup , shutdown , an dmalfunctio n reportin g requirement s ar e describe di n the nex t section . 1.2.2 Reports Revision s to thi s SSM Pma y b e mad e withou t prio r agenc y approva l to reflec t change s i n equipmen t

an dprocedure s an dto meet th e regulatory requirements . An y suc hrevision s mad e durin g asemiannua l reportin g perio dwil l b e submitte dwit hthe periodi c SS M report . Revision s to thi s plan—whic halter th e scop e o f

activitie s durin g astartup , shutdown , o r

malfunction—wil l no t take effec t

unti l awritte n notice , describin g th e revisions , i s submitte dto th e permittin g authority . Change s mad e t o thi s pla n tha t ma y significantl y increas e emission s ar e subjec t to approva l b y th e Administrator . A writte n reques t fo r approva l o f

the change s an dth e revise dSSM Pwil l b e submitte dto th e

4Administrato r withi n 5 day s afte r

makin g suc hachang e to thi s plan . Shoul dan SS M event occu r tha t i s no t addresse do r

inadequatel y addresse di n thi s SSMP , Veoli awil l mak e th e appropriat e revision s to thi s pla n withi n 4 5 day s afte r th e event . A ninvestigatio n an devaluatio n wil l b e performe do n eac hse t o f 1 0 exceedance s o f

a specifi c emissio n standardo r aspecifi c operatin g parameter limi t tha t occu r durin g malfunction s withi n a6 0 da y period . Withi n 4 5 day s o f th e 1 0 exceedance , th e investigatio n wil l determin e plausibl e cause s fo r eac hexcessiv e exceedance . Th e evaluatio n wil l conclud e ho w to minimiz e th e frequency , duration , an dseverit y o f eac h excessiv e exceedance . Th e excessiv e emission s repor t require dunde r

§ 63.10(e)(3 ) wil l includ e asummary o f

eac hinvestigatio n an devaluatio n require ddurin g th e semiannua l reportin g period . I

n addition , th e excessiv e emission s repor t wil l includ e an y change s to thi s pla n tha

t ma y resul t

fro mrequire dinvestigation s an devaluation s o f excessiv e exceedance s occurrin g durin g malfunctions . Periodi c SS M report s wil l b e submitte dto th e Administrato r semiannually , i f

astartup , shutdown , o r

malfunctio n occurre ddurin g tha t semiannua l reportin g period . Thi s repor t wil l take th e for mo f

aletter to th e Administrato r

an dinclud e th e followin g information :

• A statemen

t tha t action s take n durin g al l period s o f startup , shutdown , o r malfunctio n wer e consisten t wit hth e procedure s give n i n thi s SSM P

• Th e number , duration , an dabrie f descriptio n o f

eac hmalfunctio n

• Th e name , title , an dsignature o f th e owner/operato r

(o r other responsibl e official ) certifyin g th e accurac y o f th e repor

t A nimmediat e SS M report wil l b e submitte di f

an actio n performe ddurin g aperio do f SS M i s no t

consisten t

wit hthi s plan ; an da n OP Lo r

emissio n standardi s exceeded . Withi n tw o workin g day s afte r suc han action , th e Administrato r wil l b e advise dvi a telephon e o r

fax . Withi n 7 workin g day s afte r suc han action , aletter to the Administrato r

wil l b e delivere do r

postmarked . Th e letter wil l explai n th e event , reason s fo r no t followin g thi s plan , an ddescription s o f th e exces s emission s and/o r operatin g parameter

monitorin g exceedance s believe dto hav e occurred . Th e letter wil l als o includ e th e name , title , an dsignature o f th e owner/operato r

(o r other responsibl e official ) certifyin g th e accurac y o f th e report .

52.

0 ENGINEERIN G DESCRIPTIO N Brie f description s o f

th e fixedheart

hincinerator s an dth e rotary kil nincinerato r ar e presente di n thi s section . A detaile dengineerin g descriptio n o f th e Uni t

2 an d3 incinerator s i s provide db y Technical Description—Fixed

Hearth, Incinerators Units NOS. 2 & 3. A detaile dengineerin g descriptio n o f th e Uni t 4 incinerator s i s provide db y Technical Description, Transportable Rotary Kiln Incinerator Unit No. 4. Drawin g number s PFD-2000 , PFD-3000 , PFD-400 0 ar e th e proces s flo w diagram s fo r thes e incinerators . Thes e document s an ddrawing s ar e incorporate dhere b y reference . 2. 1 Fixe d Hearth Incinerator s Eac ho f th e fixedheart

hincinerator s include s th e followin g components :

• Fee dequipmen t

• Primar y an dsecondar y combustio n chamber s • Lim e injectio n syste m • Spra y drye r

absorber (SDA )

• Fabri c filte r

baghous e • Solid s an das hremova l system s • Induce ddraf

t (ID ) fa n an dstac k

• Instrumentation , controls , an ddat aacquisitio n system s Figur e 2- 1 present s abloc k flow diagra mo f

th e Uni t 2 incinerato r

system . Th e bloc k flo w diagra mfo r

Uni t 3 i s presente di n Figur e 2-2 . Avariet y o f

solid , liquid , an dgaseou s waste s ar e thermall y treate di n th e fixedheart h incinerators . Soli dwaste i s fe dt o th e primar y (lower ) combustio n chambe r vi aafee d conveyo r

syste man dpneumati c ram . Liqui dwaste fro mtank s an dtanker truck s ar

e fe d to th e primar y combustio n chamber throug htw o atomize dliqui dinjectors . Bot hUnit s 2 an d3 ar

e equippe dwit haspecialt y waste fee dsystems . Th e Uni t 2 primar y waste fro mliqui dcontainer s an dga s cylinder s ar e fe dto th e Uni t

2 primar y combustio n chambe r throug haspecialt y fee dport . Wast e fromliqui dcontainer s i s fe dfrom a hoode dfee dsyste mt

o th e Uni t

3 primar y combustio n chamber througl i aspecialt y fee d injector . Of f

gase s fromth e hoode dfee demissio n contro l syste mar e fe ddirectl y to

6Mil l I I I I I T TTT T COMBUSTIO N A I R BLOWE R

ik>ooooc H

TAN KFAR M L O W B T U DIREC TINJEC T LIQUID S T T TTT T

LIQUI D CONTAINER : G A S CYLINDERS . SPECIALT Y FEEDE R

PRIMAR Y FUE L W E TAS H DUMPSTE R EMERGENC Y STAC K LIM E PREPARATIO N SYSTE M

MAI N STACK -

STAC K GA S ANALYZER S SPRA Y D R Y ABSORBE R BAGHOUS E

D R YSCRUBBE R SOLID S ( DS S ) E N D DUM P D R YSCRUBBE R ISOLID S ( DS S ) E N D DUM P

occoco lOOO O FUELS/LIQUI D WAST E FLO W

COMBUSTIO N AI R FLO W STAC KGA S FLO W A S H FLO W SOLI D WAST E FLO W LIM E SLURR YFLO W

Figur e 2- 1 Fixe d Hearth Incinerator , Uni t2, Bloc kFlo w Diagra m

7TAN KFAR M

pooooo w

TAN KFAR M L O W B T U DIREC TINJEC T LIQUID S W E TAS H DUMPSTE R

SPECIALT YFEEDE R FUM E HOO D EMISSIO N CONTRO L SYSTE M PRIMAR Y FUE L LIM E PREPARATIO N SYSTE M 

# 1

SPRA Y D R Y ABSORBE R

D R YSCRUBBE R |SOLID S ( DS S ) E N D DUM P

GLOV E BO X EMISSIO N CONTROL ] SYSTE M

Figur e 2-

2 Fixe d Hearth Incinerator , Uni t3 , Bloc kFlo w Diagra m

8 STAC K GA S ANALYZER S

BAGHOUS E s L D . FA N BAGHOUS E 

# 1 L D . FA N

tOR Y SCRUBBE R SOLID S ( DS S ) E N D DUM P

• P* FUELS/LIQUI D WAST E FLO W COMBUSTIO N AI R FLO W + ~ STAC KGA S FLO W COCCOC* - AS H FLO W OOOC+ - SOLI D WAST E FLO W

LIM E SLURR YFLO Wth e Uni t 3 secondary combustio n chamber . Of f gase s fro mawast e handlin g glov e bo x ar e als o fe ddirectl y to th e Uni t 3 secondary combustio n chamber . Th e primar y combustio n chamber mai n burne r

an dth e secondary combustio n chamber mai n burne r

ar e use dto maintai n temperature s o n natura l gas . Combustio n gase s exi t th e primar y combustio n chamber an dente

r int o th e secondary combustio n chamber , whic h serve s as an afterburner . Combustio n gase s exi t th e secondary combustio n chamber an d enter th e SDA . Th e secondary combustio n chamber i s equippe dwit han emergenc y stack . Lim e slurr y an dwate r

ar e fe dto th e SD A atomizer . Th e atomize r ha s arapidl y spinnin g whee l tha

t atomize s th e lim e slurr y an dwate r int o aclou do f

fin e droplets . Combustio n gase s ar e directe dupwar dthroug hadisperse r i n th e SD A an dint o th e clou do f fin e drople t create db y th e atomizer . Thi s provide s aci dga s remova l an dcoolin g o f th e combustio n gas . Drie dspent chemical s an das hsettl e to th e botto mo f th e SD A an dar

e discharge dt o th e as hremova l system . Combustio n ga s exit s th e SD A an di s distribute dto th e fabri c filte r modules . Uni t

2 ha s fou r fabri c filte r

module s an dUni t

3 ha s thre e fabri c filte r modules . Combustio n ga s passe s throug hTeflon-coate dfiberglas s clot hbags . Particle s i n th e combustio n gase s ar e deposite do n the outsid e o f eac hba g i n th e filte r

module . Durin g th e ba g cleanin g cycle , aburs t o f ai r i n th e directio n opposit e to th e ga s flo w dislodge s particulat e matter fro m th e bag . Th e induce ddraf

t fa n i s locate ddownstreamo f th e fabri c filte r

baghouse . Th e induce d draf t fa n move s the combustio n ga s throug hth e syste man dexhaust s th e ga s throug hth e mai n stack . Hot , we t ga s i s extracte ddownstreamo f the baghous e througl i acontinuou s emission s monitorin g system . Thi s syste mfeature s amulti-componen t infrare dga s analyze r

tha t detect s hydroge n chloride , carbo n monoxide , an dwater vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations . 2. 2 Rotary Kil n Incinerato r Th e rotar y kil nincinerato r include s th e followin g components :

• Wast e fee dsyste m 9• Primar y an dsecondary combustio n chamber s • Temperin g chambe r • Lim e injectio n syste m • Spra y drye r

absorber • Carbo n injectio n syste m • Fabri c filter

baghous e • Solid s an das hremova l system s • Induce ddraf

t (ID ) fa n an dstac k

• Instrumentation , controls , an ddat aacquisitio n system s Figur e 2- 3 present s abloc k flo w diagra mo f

th e Uni t 4 incinerato r

system . Avariet y o f

soli dan dliqui dwaste s ar e thermall y treate di n th e rotary kil nincinerator . Soli dwaste s ar

e fe dt o ara mfeede r

vi aaclamshell , adru mfee dconveyo r an dan auxiliar y fee dconveyor . A hydrauli c ra mpushe s th e soli dwaste int o th e kiln . Liqui d waste fro mtank s an dtanke r truck s i s fe dt o th e primar y an dsecondary combustio n chamber s throug hatomize dliqui dinjectors . Th e primar y combustio n chambe r mai n burne r

an dth e secondary combustio n chamber mai n burne r

ar e use dto maintai n temperature s o n natura l gas . Combustio n gase s exi t th e primar y combustio n chambe r an dente

r int o th e secondary combustio n chamber , whic h serve s as an afterburner . A surg e ven t i s locate da

t th e front

o f the kil nan dthe secondary combustio n chambe r

i s equippe dwit hatherma l relie f vent . Combustio n gase s exi t th e secondary combustio n chamber an dente

r the temperin g chamber . Proces s wate r i s fe dto temperin g chambe r throug hai r

atomize dspray nozzles . Combustio n gas i s coole das i t passe s throug hth e spray o f water . Th e water

i s completel y vaporized , coolin g th e combustio n gas . Th e combustio n gas exit s th e temperin g chambe r

an di s distribute dbetwee n tw o identica l SDAs . Lim e slurr y i s fe dto eac hSD A throug hai r atomize dspray nozzles . Combustio n gase s ar e directe ddownwar dthroug haduc t i n th e SD A an dthe n disperse dsymmetricall y int o th e clou do f

atomize dlime . Thi s provide s aci dgas remova l an dcoolin g o f th e combustio n gas . Drie dspent chemical s an das hsettl e to th e botto mo f th e SD A an dar

e discharge dt o the as hremova l system .

1 0TAN KFAR M L O W B T U DIREC TINJEC T^ LIQUID S

PRIMAR Y FUE L

Figur e 2-

3 Rotary Kil n Incinerator , Uni t4 , Bloc k Flo w Diagra m

1 1 D R YSCRUBBE R SOLID S { DS S ) E N D DUM P

CARBO N INJECTIO N SYSTE M

D R YSCRUBBE R |SOLID S ( DS S ) E N D DUM P

FUELS/LIQUI D WAST E FLO W COMBUSTIO N AI R FLO W » ~ STAC KGA S FLO W CCCCCC* - AS H FLO W TOOO SOLI D WAST E FLO W \\\ » LIM E SLURR YFLO WAcarbo n injectio n syste mi s utilize dfo r controllin g dioxin/fura n an dmercur y emissions . Th e activate dcarbo n i s ai r injecte dint o th e combustio n ga s immediatel y downstreamo f th e convergenc e o f

combustio n gase s fro mth e SDAs . Combustio n gase s exi t the SDA s an dar

e distribute dto tw o fabri c filte r modules . Eac h modul e ha s thre e compartment s i n paralle l containin g multipl e fabri c bags . Combustio n ga s passe s throug hth e fabri c bags . Particle s i n th e combustio n gase s ar e deposite do n th e outsid e o f

eac hbag . Durin g th e ba g cleanin g cycle , aburs t o f ai r i n th e directio n opposit e to the ga s flo w dislodge s particulat e matte r fro mth e bag . Th e induce ddraf

t fa n i s locate ddownstrea mo f th e fabri c filte r

baghouse . Th e induce d draf t fa n move s th e combustio n ga s throug hth e syste man dexhaust s the ga s throug hth e mai n stack . Hot , we t gas i s extracte ddownstreamo f th e I D fa n throug hacontinuou s emission s monitorin g system . Thi s syste mfeature s amulti-componen t infrare dgas analyze r

tha t detect s hydroge n chloride , carbo n monoxide , an dwate r vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations .

1 23.

0 STARTU PAN D SHUTDOW N PROCEDURE S Th e purpos e o f

thi s sectio n i s to prescrib e procedure s fo r th e startu

p an dshutdow n o f

th e incinerato r

system . Thi s sectio n als o clarifie s whic haction s ar e withi n th e scop e o f

th e regulator y definitio n o f startup an dshutdown . T o satisf y the requirement s o f

§ 63.1206(c)(2)(v)(B) , waste fee drestrictio n an doperatin g limit s hav e bee n impose dto startup s an dshutdowns . Durin g astartup , th e feedin g o f hazardou s waste to th e incinerato r wil l no t b e initiate dunti l al l operatin g parameter s ar e withi n limits . Hazardou s wast e wil l no t b e fe ddurin g ashutdow n event . Consisten t

wit hth e requirement s o f § 63.1206(c)(2)(iii) , Veoli awil l utiliz e an oxyge n correctio n facto r

o f 1. 6 (i.e. , 12.3 % O2

) durin g period s o f

startu p an dshutdown . Thi s wil l eliminat e wid e variation s i n correcte dC O concentratio n tha t can occu r

durin g startup an dshutdow n du e to change s i n th e oxyge n concentration . Th e oxyge n correctio n facto r o f 1. 6 i s base do n the averag e oxyge n correctio n facto r observe ddurin g norma l operation s o f

th e incinerators . Thi s "default " oxyge n correctio n facto r ca n onl y b e utilize dwhe n th e waste residenc e tim e i n th e primar y combustio n chambe r ha s expire d an dwhe n the incinerato r i s i n startup o r

shutdown . Veoli aha s develope dstandar ddivisio n practice s (SDPs ) fo r th e operatio n o f

eac h incinerato r

syste man dancillar y equipmen t an dsystems . Th e SDP s containin g startup an dshutdow n procedure s fo r th e incinerator s are :

• SD P 220 1 Startup, Operation, and Shutdown of

No. 2/3 Incinerators

• SD P 241 7 Startup, Operation, and Shutdown of

No. 4 Incinerator 3. 1 Startup A l l startup s ar

e precede db y ashutdown . Dependin g o n th e purpos e o f th e precedin g shutdown , portion s o f th e ai r pollutio n contro l syste mma y b e i n servic e upo n commencin g astartup . Thi s wil l b e reflecte do n th e startup recor d(se e Attachment s 1) . Durin g astartup , waste wil l no t b e introduce dunti l al l operatin g parameter s ar e withi n limits . A startu

p even t i s conclude donc e waste i s introduce dan dal l operatin g parameter s ar

e withi n limits . Veolia' s startu

p procedure s ar

e representativ e o f

safety an dgoo dai r

pollutio n contro l practices . Th e procedure s ar e designe dto minimiz e th e potentia l fo r exces s emission s b y ensurin g tha

t al l equipmen t

i s full y operationa l (withi n permi t limits ) prio r

to the 1 3introductio n o f hazardou s waste to th e system . Adherenc e to thes e startu p procedu i wil l emplo y th e knowledg e an dskill s demonstrate dthroug hth e implementatio n o f 1 Operato r Trainin g an dCertificatio n Program .

1 43.

2 Norma l Shutdown Som e shutdown s wil l allo w th e primar y combustio n chamber to cool . Prio r

to thes e shutdowns , th e incinerato r wil l b e burnin g auxiliar y fue l onl y an dth e hazardou s waste residenc e tim e wil l hav e transpired . A shutdow n wil l b e initiate dwit hthe shutof f o f auxiliar y fue l to th e incinerato r o r b y shutof

f o f th e I D fan . Othe r

shutdown s wil l b e initiate dwit hth e cessatio n o f al l waste feed s b y th e operato r to stabiliz e syste moperatin g parameters . Portion s o r al l o f th e ai r pollutio n contro l syste mma y remai n i n operatin g mod e a t th e conclusio n o f

ashutdow n throug hth e subsequent startup . Veolia' s shutdow n procedure s ar e representativ e o f

safet y an dgoo dai r

pollutio n contro l practice . Th e procedure s ar e designe dto minimiz e th e potentia l fo r exces s emission s b y ensurin g tha

t al l waste feed s ar

e of f and/o r th e hazardou s waste residenc e tim e ha s transpire dprio r

to th e shutdow n o f

the incinerato r

system . Adherenc e to thes e shutdow n procedure s wil l emplo y th e knowledg e an dskill s demonstrate dthroug hth e implementatio n o f

th e Operato r

Trainin g an dCertificatio n Program . Procedure s fo r emergenc y shutdow n ar e describe di n th e nex t

sectio n regardin g malfunctions .

1 54.

0 MALFUNCTION S Th e purpos e o f

thi s sectio n o f

th e Startup , Shutdow n an dMalfunctio n Pla n i s to :

• Defin e potentia l malfunction s an dthei r cause s • Describ e measure s to minimiz e th e frequenc y an dseverit y o f malfunctions . • Prescrib e procedure s fo r operatin g an dmaintainin g th e incinerato r durin g malfunction s • Prescrib e action s t o correc t th e caus e o f

amalfunctio n Asummary o f

potentia l malfunction s an dthei r cause s i s give n i n Tabl e 4-1 . Thi s lis t o f potentia l malfunction s i s arrange daccordin g to uni t operations . Th e occurrenc e o f an y event liste di n Tabl e 4- 1 shoul db e responde dto as amalfunctio n an damalfunctio n recordkeepin g form , include das Attachmen t 3 , shoul db e initiated . Durin g th e respons e to thes e events , i t

wil l b e determine di f th e event

meet s th e regulatory definitio n o f a malfunction . 4. 1 Measures t

o Minimiz e th

e Frequency o

f Malfunction s Th e followin g measure s contribut e to preven t malfunctions :

• Incinerato r

syste mdesig n consisten t wit hsafety an dgoo dengineerin g practice s • Hazard s an doperabilit y studie s o f th e incinerator s • Appropriat e frequenc y o f preventativ e maintenanc e an dinspectio n • Goo doperatin g practice s • Wel l traine dan dqualifie dpersonne l Veolia' s performanc e history , thi s document , an dth e followin g regulatory document s serv e as evidenc e o f Veolia' s proactiv e measure s to minimiz e th e frequenc y o f malfunctions .

• Operation and

Maintenance Plan

• Operating Training and Certification Program

• Continuous Emissions Monitoring System Quality Assurance Plan (CEMS QA Plan)

• Continuous Monitoring System Quality Control Plan (CM S Q C Plan )

• Automatic Waste Feed Cutoff System Operability Test Procedures

1 6Tabl e 4- 1 Summar y o f Potentia

l Malfunction s and Cause s Potential Malfunction s fo rUnits 2,3 , an d 4 Potential Causes fo ra Malfunctio n GENERA L

- Los s o f

Electrica l Powe r

Suppl y

- Los s o f

Instrument/Plan t

Ai r Suppl y

- Los s o f

Plan t Nitroge n Suppl y

- Los s o f

Cit y Wate r

Suppl y

- Los s o f

Proces s Wate r

Pressure/Flo w (Uni t

4 )

- Malfunctio n o f

Safet y Interloc k

o r Automati c Wast e Fee d Cutof f Interloc k

- Excessiv e Ai r

In-leakag e i n Ai r

Pollutio n Contro l Syste m PRIMAR Y COMBUSTIO N CHAMBE R

- Los s o f

Natura l Ga s Pressure/Flo w t o PC C Mai nBurne r

- Los s o f

Combustio n Ai r

Pressure/Flo w to PC C

- PC C Mai nBurne r

Pilo t Failur e

- Los s o f

Wast e Flo w t o PC C Injecto r

- Los s o f

Wast e Feedrat e Contro l t o PC C Injecto r

- Los s o f

Atomizatio n Ai r

Pressur e t o aPC C Injecto r

- Los s o f

PC C Draft

Contro l (Uni t

4 )

- Los s o f

PC C Temperatur e Contro l

- Flam e Failur e

- Kil nRotatio n Malfunctio n (Uni t 4 )

- Bulk/Charg e Fee dDoo r Malfunctio n

- Physical/Mechanica l Interna l Equipmen t Failur e

- PC C Sea l Visua l Emission s Monitorin g an dRecordin g Syste m

- Rapi dStea mGeneratio n fro mAs hCollectio n Syste mWate r SECONDAR Y COMBUSTIO N CHAMBE R

- Los s o f

Natura l Ga s Pressure/Flo w t o SC C Mai nBurne r

- Los s o f

Combustio n Ai r

Pressure/Flo w t o SC C

- SC C Mai nBurne r

Ignitio n Failur e

- Los s o f

Wast e Flo w to SC C Injecto r

- Los s o f

Wast e Feedrat e Contro l t o SC C Injecto r

- Los s o f

Atomizatio n Ai r

Pressur e t o aSC C Injecto r

- Los s o f

SC C Temperatur e Contro l

- Flam e Failur e

- Emergenc y Safet y Ven t Openin g

- Physical/Mechanica l Interna l Equipmen t Failur e - Lo w Wate r Leve l i n Sla g Collectio n Syste m(Uni t 4 )

- Rapi dSteamGeneratio n fro mAs hCollectio n Syste mWate r TEMPERIN G CHAMBE R(UNI T 4 )

- Los s o f

Temperin g Chambe r

Exi t Ga s Temperatur e Contro l

- Los s o f

Atomizatio n Ai r

Pressur e t o Nozzl e LIM E SLURR Y SYSTE M

- Los s o f

Lim e Fee dt o Lim e Slurr y Fee dTan k

- Malfunctio n i n Lim e Slurr y Concentratio n UNIT S 2 AN D 3 SPRA Y DRYE RABSORBE R(SDA )

- Los s o f

Lim e Slurr y Flo w to SD A

- Los s o f

Lim e Slurr y Flo w Contro l

- Los s o f

Cit y Wate r

Flo w to SD A

- Los s o f

Coolin g Ai r

Flo w t o Atomize r

- Los s o f

SD A Exi t

Ga s Temperatur e Contro l

- Atomize r

Failur e UNIT S 4 SPRA Y DRYE RABSORBE R(SDA )

- Los s o f

Lim e Slurr y Flo w t o SD A

- Los s o f

Lim e Slurr y Flo w Control/Exi t Ga s Temperatur e Contro l

- Los s o f

Atomizatio n Ai r

Pressur e t o SD A Nozzl e CARBO N INJECTIO N SYSTE M (UNI T 4 )

- Los s o f

Carrie r Ga s Pressur e

- Loss/Restrictio n o f

Activate dCarbo n Flo w

- Los s o f

Plan t Ai r Pressure/Flo w t o Carbo n Bul k Sac k BAGHOUS E & INDUCE D DRAF T (TD ) FA N

- Torn/Leakin g Ba g

- Ba g Blinding/High-Hig hPressur e Dro p

- Los s o f

Stac k Ga s Flowrat e Contro l (Uni t 2 an d3 )

- Baghous e Isolatio n Dampe r Malfunctio n (Uni t

4 )

- I D Fa n Failur e CONTRO L SYSTEM/CONTINUOU S MONITORIN G SYSTE M

- Contro l System/Continuou s Monitorin g Syste mMalfunctio n

- Continuou s Emission s Monitorin g Syste mMalfunctio n Mechanical/electrica l failur e o f

rotatin g equipment . Plugging/physica l failur e o f lines/nozzle s Physical/electrica l failur e o f instrumentatio n Mechanical/electrica l failur e o f

actuate d valves/damper s Physical/electrica l failur e o f contro l syste m Mechanical/electrica l failur e o f

utilit y supplie s Electrical/actuatio n failur e o f safet y interlock s Physical/mechanica l interna l equipmen t

failur e

1 7Despit e thes e efforts , equipmen t failure s an dother

operatin g anomalie s ca n occur . Withi n th e scop e o f

regulatory requirements , th e operatin g recor dwil l contai n th e appropriat e documentatio n to establis htha t poo r maintenanc e o r

careles s operation s ar e no t contributin g factor s to th e caus e o f amalfunction . 4. 2 Measures t

o Mmimiz e th

e Severit

y o f Malfunction s Th e followin g measure s contribut e to minimiz e the severit y o f malfunctions :

• Alarm s an dinterlock s • AWFC O testin g • Failur e position s fo r critica l equipmen t

• Wel l traine dan dqualifie dpersonne l

• Desig n o f

th e incinerato r

syste m Typically , an event

tha t meet s th e definitio n o f amalfunctio n wil l trigge r an alarm . A n alar minform s the operato r o f th e situatio n an dma y provid e a n opportunity to avoi dan exceedance . I f

condition s becom e unsaf e o r excee doperatin g limits , interlock s ar e i n plac e fo r

an automate drespons e tha t i s specifi c to th e triggerin g condition . Refe r to Veolia' s Documentation of Compliance o r

Notification of

Compliance, whicheve r i s currentl y applicable , fo r detail s o n AWFC O conditions . Additiona l detail s o n alarm s an d interlock s ar

e maintaine do n pipin g an dinstrumentatio n diagram s (P&IDs ) Th e mos t

critica l ke y to minimizin g th e severity o f malfunction s i s the functionalit y o f AWFC O interlocks . Accordingly , Veoli aperform s testin g o f the AWFC O system , as describe di n the AWFCO Plan. Thi s testin g confirm s astat e o f readines s to respon dto a malfunctio n i n amanner tha t wil l minimiz e th e releas e o f hazardou s ai r

pollutants . Throug htrainin g an djo b experience , th e operato r wil l hav e th e proces s knowledg e tha t qualifie s hi mto us e discretio n i n respondin g to malfunctions . Du e t o the unusua l an d dynami c condition s tha t ar e present durin g amalfunction , operato r discretio n i s essentia l to minimizin g the severity o f malfunctions . A n operato r ca n evaluate proces s condition s an dalarm s an dchoos e th e bes t respons e to avoi dan exceedance , i f possible . I f

th e malfunctio n adversel y affect s th e functionalit y o f alarms , interlocks , o r

fai l saf e positions , th e operato r

mus t recogniz e the situatio n an drespon dappropriately . I n the event tha t th e malfunctio n affect s th e abilit y to automaticall y cutof f waste , th e operato r

wil l manuall y cutoff waste feed s as quickl y as possible .

1 8Th e desig n o f th e eac hincinerato r

syste mals o ensure s tha t th e severit y o f

malfunction s wil l b e minimized . Thi s include s alarm s an dinterlocks , th e fai l saf e positio n o f

actuate d valves , an dredundant

instrumentatio n an dproces s equipment . Also , th e desig n o f eac h incinerator' s instrumentatio n an dcontro l system s provide s th e operato r convenien t

acces s to proces s variabl e indication , includin g positio n indicatio n o f selecte dactuate dvalves . Thi s i s essential to providin g th e operato r th e informatio n require dto bes t evaluate syste mcondition s an dresponses . Tabl e 4- 2 list s potentia l malfunction s an dassociate d redundant

equipmen t

an dsystem s tha

t ar e availabl e to preven t

thes e malfunction s o r to minimiz e th e potentia l fo r asignifican t

releas e o f

hazardou s ai r

pollutants . 4. 3 Correctiv e Measures Th e Program of

Corrective Actions for Malfunctions i s Attachmen t 4 o f thi s document . Thi s progra maddresse s ho w th e incinerato r wil l b e operate dan dmaintaine ddurin g malfunctions . I n thi s program , potentia l malfunction s ar e liste dfo r

eac hportio n o f

th e incinerato r

system . Th e malfunction s ar e event s tha

t wil l b e recognize db y th e operator , o r indicate db y an alarm , an dthreate n to caus e an exceedance . I n th e respons e to th e malfunctio n and/o r

alarms , th e operato r

wil l appl y discretio n an dattemp t to maintai n th e incinerato r

syste mwithi n regulatory limits . I n th e progra mo f correctiv e actions , potentia l cause s o f

eac hmalfunctio n ar

e listed . Th e operato r wil l utiliz e proces s knowledge , jo b experience , and , i f needed , assistanc e fro mother personne l to identif

y th e caus e o f th e malfunction . Fo r eac hpotentia l cause , action s to correc t th e failur e ar

e listed . Th e correctiv e action s prescribe dma y requir e th e collaboratio n o f multi

discipline dpersonne l wh o ar e qualifie dto return th e incinerato r syste mto prope r

workin g condition s (i.e. , maintenanc e personnel , contro l syste mtechnicians , engineering) .

1 9Tabl e 4- 2 RedundantEquipmen tand System s fo r Minimizin g th

e Frequency o rSeverit y o f Malfunction s RedundantEquipment/Systems Potentia l Malfunction s Prevented/Minimize d Emergenc y generato r

(Uni t 4 ) Los s o f Electrica l Powe r

Suppl y Universa l Powe r

Suppl y (UPS ) syste mpower s computers , monitors , an dcontro l system s Los s o f Electrica l Powe r

Suppl y Tw o compressor s ar

e o n ho t standb y (Uni t

4 ) Thre e ai r compressor s runnin g an don e compresso r o n ho t standb y (Uni t

2 an d3) . Los s o f Instrument/Plan t

Ai r Suppl y Dua l Proces s Wate r

Pump s Los s o f Proces s Wate r

Pressure/Flo w Dedicate dPC C combustio n ai r fa n (Uni t

4 ) Los s o f

Combustio n Ai r

Pressure/Flo w to PC C Dedicate dSC C combustio n ai r fa n (Uni t

4 ) Spar e SC C combustio n ai r

fa n (Uni t

4 ) Los s o f Combustio n Ai r

Pressure/Flo w to SC C Multipl e Temperin g Chambe r Nozzle s Los s o f Temperin g Chambe r

Exi t Ga s Temperatur e Contro l Los s o f Atomizatio n Ai r

Pressure to Nozzl e Dua l Slurr y Fee dPump s (Uni t 4 ) Share dBack-u p Pum p (Uni t 2 an d3 ) Los s o f Slurr y Fee dto SD A Off-lin e Spare Lim e Slurr y Atomize r (Uni t 2 & 3 ) Atomize r

Failur e Dua l SDA s (Uni t

4 ) Los s o f Lim e Slurr y Flo w to SD A Los s o f Lim e Slurr y Flo w Control/Exi t Ga s Temperature Contro l Los s o f Atomizatio n Ai r

Pressur e to SD A Nozzl e Off-lin e Spare Baghous e Modul e (Uni t 2 ) Torn/Leakin g Ba g Tw o baghous e module s wit hthre e compartment s each . 5 compartment s provid e sufficien t particulat e remova l s o tha

t on e o f th e 6 compartment s ca n b e isolate das aspare . (Uni t 4 ) Torn/Leakin g Ba g

2 0

### ATTACHMEN T 1 STARTU PRECORDKEEPIN G FOR MVEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU PRECOR D

(Pag e 1 of3 ) Thi s report

pertain s t o astartup o f Uni t 2/3/ 4 (circl e one) . Startu p even t

initiate don : (Month/Day/Year , Hours : Minutes ) Startu p even t

conclude don : (Month/Day/Year , Hours : Minutes ) Th e tota l duratio n o f

thi s startup event

was : (Hour s : Minutes ) Attache dto thi s for mi s achecklis t that summarize s th e approve dstartup procedure s reference di n Veolia' s Startup, Shutdown, and Malfunction Plan (SSMP) . Th e operationa l step s tha t hav e bee n checke ddocumen t tha t th e detaile dstartup procedure s were followed . Wer e al l action s associate dwit hthi s startup event i n conformanc e wit hth e SSMP ? Ye s / N o (circl e one) . I f no , describ e th e inconsisten t action s below .

Wer e there an y exceedance s o f a n operatin g paramete r limit ? Ye s /

N o (circl e one) . I f

yes , pleas e list/describe . I f an y action s wer e no t

consisten t

wit hth e SSM Pan da n operatin g paramete r limi t wa s exceeded , a n immediat e SS M report

i s required .

Notes/Recommendations :

Th e followin g signatur e certifie s th e accurac y o f

thi s record : (Name ) (Title ) (Signature ) (Date )VEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU PRECOR D

(Pag e 2 o f

3 )

Uni t2 an d 3 Incinerato rStartup Checklis t Initial s Verif y that

pre-startu p ha s bee n complete d Chec k therma l relie f

ven t (TRV ) Star t combustio n ai r

fa n Star t PC C mai n burne r

an dtemperature ramp-u p Star t SC C mai n burne r

an dtemperature ramp-u p Chec k stac k ga s flo w an dSD A temperature s contro l setting s Star t I D fan . Monito r

SD A temperature whil e rampin g u p stac k ga s flowrat e Clos e TR V Star t lim e slurr y Establis hal l operatin g parameter s withi n limit s Operator' s Notes :

Note : Certai n ai r

pollutio n contro l an dancillar y equipmen t ma y b e operationa l prio r t o startup (Signatur e o f

Shif t Leade r o r Designee ) (Date )VEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU PRECOR D

(Pag e 3 o f

3 )

Uni t4 Incinerato rStartup Checklis t Initial s Verif y tha

t pre-startu p ha s bee n complete d Chec k therma l relie f

ven t (TRV ) Star t I D fa n an dset

kil ndraf

t (star t o f purg e cycle ) Star t SC C combustio n ai r

fa n Star t the kil ncombustio n ai r fa n (purg e cycl e complete ) Start SC C mai n burne r

an dtemperature ramp-u p Star t PC C mai n burne r

an dtemperature ramp-u p Star t kil nrotatio n befor e 50 0 ° F Start th e kil nsea l ai r Star t th e SC C conveyo r Se t u p the temperin g chambe r fo r operatio n Set u p lim e slurr y injectio n syste m Se t u p th e SDA s fo r

operatio n Se t u p the as hcollectio n syste m Set u p the baghouse s fo r

operatio n Slowl y ramp-u p th e temperin g chambe r exi t temperature Continu e PC C an dSC C temperature ramp-u p Star t th e kil nsea l conveyo r Establis hal l operatin g parameter s withi n limit s Operator' s Notes :

Note : Certai n ai r

pollutio n contro l an dancillar y equipmen t ma y b e operationa l prio r to startup . (Signatur e o f

Shif t Leade r o r Designee ) (Date )

### ATTACHMEN T 2 SHUTDOW N RECORDKEEPIN G FOR MVEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 1 o f

3 ) Thi s report

pertain s t o ashutdow n o f Uni t 2/3/ 4 (circl e one) . Shutdow n even t

initiate don : (Month/Day/Year , Hour s : Minutes ) Shutdow n even t

conclude don : (Month/Day/Year , Hour s : Minutes ) Th e tota l duratio n o f

thi s shutdow n even t

was : (Hour s : Minutes ) Attache dt o thi s for mi s achecklis t tha t summarize s th e approve dshutdow n procedure s reference di n th e Veolia Startup, Shutdown, and Malfunction Plan (SSMP) . Th e operationa l step s tha t hav e bee n checke ddocumen t tha t th e detaile dshutdow n procedure s wer e followed . Wer e al l action s associate dwit hthi s shutdow n even t i n conformanc e wit hth e SSMP ? Ye s / N o (circl e one) . I f no , describ e th e inconsisten t action s below .

Wer e there an y exceedance s o f a n operatin g paramete r limit ? Ye s /

N o (circl e one) . I f

yes , pleas e list/describe . I f an y action s wer e no t

consisten t

wit hth e SSM Pan da n operatin g paramete r limi t wa s exceeded, a n immediat e S S M report

i s required .

Notes/Recommendations :

Th e followin g signatur e certifie s th e accurac y o f thi s record : (Name ) (Signature ) (Title ) (Date )VEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 2 o f

3 )

Uni t2 an d 3 Incinerato rShutdow n Checklis t Initial s Verif y tha

t al l wast e feed s are of f

and/o r tha t th e hazardou s waste residenc e tim e ha s transpire d Monito r CEM S outpu t

to verif y stabl e condition s Ope n th e stac k

ca p Sto p th e I D fa n Shu t of f wate r an dlim e slurr y flo w t o th e atomize r Remov e atomize r

an dpositio n li d Operator' s Notes :

Note : Al l o r

certai n ai r

pollutio n contro l an dancillar y equipmen t ma y remai n operationa l throughou t shutdown . Onc e th e hazardou s waste residenc e tim e ha s transpired , operator' s discretio n ca n b e applied .

(Signatur e o f

Shift Leade r o r Designee ) (Date )VEOLI A ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 3 o f

3 )

Uni t4 Incinerato rShutdown Checklis t Initial s Verif y that

al l wast e feed s ar

e of f and/o r tha t th e hazardou s wast e residenc e tim e ha s transpire d Shu t of f th e kil nburne r

an dSC C burne r Shu t of f th e kil nan dSC C combustio n ai r fan s Reduc e th e temperin g chambe r outle t temperature to 50 0 ° F Shutdow n SD A (a

t appropriat e temperatures ) Shutdow n temperin g chambe r (a t appropriat e temperatures ) Afte r PC C an dSC C reac hth e appropriat e temperature , shu t of f th e I D fa n Operator' s Notes :

Note : A l l o r

certai n ai r

pollutio n contro l an dancillar y equipmen t ma y remai n operationa l throughou t shutdown . Onc e th e hazardou s wast e residenc e tim e ha s transpired , operator' s discretio n ca n b e applied . (Signatur e o f

Shif t Leade r o r Designee ) (Date )

### ATTACHMEN T 3 MALFUNCTIO N RECORDKEEPIN G FOR MVEOLI A ENVIRONMENTA L SERVICES , INC . MALFUNCTIO N RECOR D

(Pag e 1 o f

1 ) Thi s repor t

pertain s t o amalfunctio n o f Uni t 2/3/ 4 (circl e one) . Th e malfunctio n event occurre don : (Month/Day/Year , Hour s : Minutes ) Th e malfunctio n event conclude don : (Month/Day/Year , Hour s : Minutes ) Th e tota l duratio n o f

thi s malfunctio n event was : (Hour s : Minutes ) Th e Veolia Program of Corrective Actions for

Malfunctions mus t

b e adhere dt o fo r

th e operatin g an dmaintainin g o f th e incinerato r

syste man dfo r

correctin g the caus e o f the malfunction . Describ e the malfunction , th e automate dand/o r

operato r response , the potentia l caus e o f th e malfunction , an dthe correctiv e action s taken :

Wast e Feed s of f

Tim e — Incinerato r

"Clea r o f Waste " Tim e — Wer e al l action s associate dwit hthi s malfunctio n even t i n conformanc e wit hth e SSMP ? Ye s / N o (circl e one) . I f no , initiat e a n immediat e startup , shutdown , an dmalfunctio n report . List/describ e the exceedance s tha t occurre d(o r

believe dto hav e occurred ) du e to thi s malfunction :

Notes/Recommendations :

Th e followin g signatur e certifie s the accurac y o f thi s record : (Name ) (Title ) (Signature ) (Date )

### ATTACHMEN T 4 PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

### PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S TABL E O F CONTENT S 1. 0 GENERA L

1. 1 Operatin g an dMaintainin g th e Syste mdurin g Malfunction s 1. 2 Los s o f

Electrica l Powe r

Suppl y 1. 3 Los s o f

Instrument/Plan t

Ai r Suppl y 1.4 Los s o f

Plan t Nitroge n Suppl y 1. 5 Los s o f

Cit y Wate r

Suppl y 1. 6 Los s o f

Proces s Wate r

Pressure/Flo w (Uni t

4 ) 1.7 Malfunctio n o f Safet y Interloc k

o r Automati c Wast e Fee dCutof f Interloc k 1. 8 Excessiv e Ai r In-leakag e i n Ai r

Pollutio n Contro l Syste m 2. 0 PRIMAR Y COMBUSTIO NCHAMBE R

2. 1 Los s o f

Natura l Ga s Pressure/Flo w to PC C Mai nBurne r 2. 2 Los s o f

Combustio n Ai r

Pressure/Flo w to PC C 2. 3 PC C Mai nBurne r Pilo t Failur e 2. 4 Los s o f

Wast e Flo w t o PC C In j ecto r 2. 5 Los s o f

Wast e Feedrat e Contro l to PC C Injecto r 2. 6 Los s o f

Atomizatio n Ai r

Pressur e to aPC C Injecto r 2. 7 Los s o f

PC C Draft

Contro l (Uni t

4 ) 2. 8 Los s o f

PC C Temperatur e Contro l 2. 9 Flam e Failur e 2.1 0 Kil nRotatio n Malfunctio n (Uni t 4 ) 2.1 1 Bulk/Charg e Fee dDoo r Malfunctio n 2.12 Physical/Mechanica l Interna l Equipmen t Failur e 2.1 3 PC C Sea l Visua l Emission s Monitorin g an dRecordin g Syste m 2.1 4 Rapi dSteamGeneratio n fro mAs hCollectio n Syste mWate r 3. 0 SECONDAR Y COMBUSTIO NCHAMBE R

3. 1 Los s o f

Natura l Ga s Pressure/Flo w t o SC C Mai nBurne r 3. 2 Los s o f

Combustio n Ai r

Pressure/Flo w t o SC C 3. 3 SC C Mai nBurne r Ignitio n Failur e 3. 4 Los s o f

Wast e Flo w t o SC C Injecto r (Uni t 4 ) 3. 5 Los s o f

Wast e Feedrat e Contro l t o SC C Injecto r (Uni t 4 ) 3. 6 Los s o f

Atomizatio n Ai r

Pressur e t o aSC C Injecto r 3. 7 Los s o f

SC C Temperatur e Contro l 3. 8 Flam e Failur e 3. 9 Physical/Mechanica l Interna l Equipmen t Failur e 3.1 0 Lo w Wate r

Leve l i n Sla g Collectio n Syste m(Uni t 4 ) 3.1 1 Emergenc y S afet y Ven t Openin g 3.1 2 Rapi dSteamGeneratio n fro mAs hCollectio n Syste mWate r 4. 0 TEMPERIN GCHAMBE R(UNI T 4 )

4. 1 Los s o f

Temperin g Chambe r

Exi t Ga s Temperatur e Contro l 4. 2 Los s o f

Atomizatio n Ai r

Pressur e to Nozzl e 5. 0 LIM ESLURR Y SYSTE M

5.1 . Los s o f

Lim e Fee dto Lim e Slurr y Fee dTan k 5.2 . Malfunctio n i n Lim e Slurr y Concentratio n 6. 0 UNIT S 2 AN D 3 SPRA Y DRYE RABSORBE R(SDA )

6.1 . Los s o f

Lim e Slurr y Flo w t o SD A6.2 . Los s o f Lim e Slurr y Flo w Contro l 6.3 . Los s o f

Cit y Wate r

Flo w to SD A (Uni t

2 an d3 ) 6.4 . Los s o f

Coolin g Ai r

Flo w t o Atomize r 6.5 . Los s o f

SD A Exi t

Ga s Temperatur e Contro l 6.6 . Atomize r

Failur e 7. 0 UNI T 4 SPRA Y DRYE RABSORBE R(SDA ) 7.1 . Los s o f

Lim e Slurr y Flo w to SD A 7.2 . Los s o f

Lim e Slurr y Flo w Control/Exi t Ga s Temperatur e Contro l 7.3 . Los s o f

Atomizatio n Ai r

Pressur e to SD A Nozzl e 8. 0 CARBO NINJECTIO NSYSTE M (UNI T 4 ) 8.1 . Los s o f

Carrie r Ga s Pressur e 8.2 . Loss/Restrictio n o f Activate dCarbo n Flo w 8.3 . Los s o f

Plan t Ai r Pressure/Flo w t o Carbo n Bul k Sac k 9. 0 BAGHOUS E& INDUCE D DRAF T (ID ) FA N 9.1 . Torn/Leakin g B a g 9.2 . Ba g Blinding/High-Hig hPressur e Dro p 9.3 . Los s o f

Stac k Ga s Flowrat e Contro l (Uni t 2 an d3 ) 9.4 . Baghous e Isolatio n Dampe r Malfunctio n (Uni t

4 ) 9.5 . I D Fa n Failur e 10. 0 CONTRO LSYSTEM/CONTINUOU S MONITORIN GSYSTE M 10.1 . Contro l System/Continuou s Monitorin g Syste mMalfunctio n 10.2 . Continuou s Emission s Monitorin g Syste mMalfunctio nVEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

GENERA L 1.1 . Operatin g and Maintainin g th e Syste m durin g Malfunction s 1.1.1 . Du e to th e sudden , infrequent , an dunusua l condition s associate d wit hmalfunctions , continuall y evaluat e th e situation . Usin g discretion , respon di n amanne r consisten t

wit hsafety an dgoo dai r pollutio n contro l practices . 1.1.2 . Tak e the followin g action s to minimiz e th e releas e o f hazardou s ai r pollutant s 1.1.2.1 . Cutoff

al l waste feed s and/o r

confir mtha

t th e automati c waste fee dcutof

f syste mfunctione dproperly . 1.1.2.2 . Maintai n operatin g parameter s withi n limits , i f possible . 1.1.2.3 . I f

applicable , follo w th e procedure s provide db y the Emergency Safety Vent Plan. 1.1.3 . Kee p superviso r and/o r maintenanc e superviso r informed , as appropriate . 1.1.4 . Identif

y th e malfunctio n an dpotentia l cause . 1.1.5 . Implemen t

correctiv e action s involvin g th e troubleshootin g o f failure s an dth e servicin g and/o r replacin g o f

components , as needed . Refe r

to manufacture' s troubleshootin g an dservic e recommendations , as needed . 1.1.6 . Recor dth e appropriate informatio n usin g amalfunctio n recor d form . 1.2 . Los s of

Electrica l Powe

rSupply 1.2.1 . Verif y prope r

failur e positio n o f

actuate dvalves . 1.2.2 . Identif

y lin k i npowe r

suppl y paththa

t i s no t operational . 1.2.3 . Tak e th e necessar y action s to restore th e suppl y o f electrica l power . 1.3 . Los s o

f Instrument/PlantAi rSuppl y 1.3.1 . Verif y prope r

failur e positio n o f

actuate dvalves . 1.3.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e components : 1.3.2.1 . Identif

y the location/caus e o f th e restrictio n o f instrumen t

ai r flow . 1.3.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . Pag e 1 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 1.3.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 1.3.3.1 . Identif

y caus e o f

actuatio n failure . 1.3.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 1.3.3.3 . Service/replace actuato r and/o r valv e components , as needed . 1.3.4 . I n cas e o f

mechanical/electrica l failur e a t ai r suppl y source : 1.3.4.1 . Identif

y th e caus e o f

the failure . 1.3.4.2 . Tak e th e necessary action s to restore th e suppl y o f

instrument/plan t

air . 1.4 . Los s of

PlantNitrogen Suppl y 1.4.1 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e components : 1.4.1.1 . Identif

y th e location/caus e o f

th e restrictio n o f

nitroge n flow . 1.4.1.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 1.4.2 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 1.4.2.1 . Identif

y caus e o f

actuatio n failure . 1.4.2.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 1.4.2.3 . Service/replac e actuator and/o r valv e components , as needed . 1.4.3 . I n cas e o f

mechanical/electrica l failur e a t nitroge n suppl y source : 1.4.3.1 . Identif

y th e caus e o f

th e failure . 1.4.3.2 . Tak e th e necessary action s to restore th e suppl y o f

nitrogen . 1.5 . Los s of

Cit y Wate rSupply 1.5.1 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e components : 1.5.1.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 1.5.1.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 1.5.2 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 1.5.2.1 . Identif

y caus e o f

actuatio n failure . 1.5.2.2 . Service/replace electrica l and/o r pneumati c components , as needed . Pag e 2 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

1.5.2.3 . Service/replac e actuato r and/o r valv e components , as needed . 1.5.3 . I n cas e o f

mechanical/electrica l failur e a t cit y wate r

suppl y source : 1.5.3.1 . Identif

y th e caus e o f

th e failure . 1.5.3.2 . Tak e th e necessary action s to restore the suppl y o f cit y water . 1.6 . Los s o

f Process Wate rPressure/Flo w (Uni t4 ) 1.6.1 . Fo r

los s o f cit y wate r

suppl y to proces s wate r tank , see 1.5 . 1.6.2 . I n cas e o f

mechanical/electrica l failur e o f proces s wate r

pump : 1.6.2.1 . Diagnos e pump/driv e failure . 1.6.2.2 . Service/replac e th e pump/drive , a s needed . 1.6.2.3 . Restor e electrica l powe r suppl y to th e pump . 1.6.3 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e components : 1.6.3.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 1.6.3.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 1.6.4 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 1.6.4.1 . Identif

y caus e o f

actuatio n failure . 1.6.4.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 1.6.4.3 . Service/replace actuato r and/o r valv e components , as needed . 1.6.5 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 1.6.5.1 . Identif

y fault y contro l syste mcomponent . 1.6.5.2 . Service/replac e contro l syste mcomponents , a s needed . 1.7 . Malfunctio n o

f Safet y Interlock o rAutomati c Wast e Feed Cutof

f Interlock 1.7.1 . I f safet y interloc k

o r AWFC O interloc k

wa s erroneousl y triggered , procee dwit hcorrectiv e actions . 1.7.2 . I f safet y o r

AWFC O conditio n exist s bu t automate drespons e failed , cutof

f waste fee das quickl y as possible , the n procee dwit h correctiv e actions . 1.7.3 . I n cas e o f

physical/electrica l failur e o f instrumentation : 1.7.3.1 . Identif

y fault y instrumentatio n component . 1.7.3.2 . Service/replace fault y instrumentatio n components , as

needed . Pag e 3 o f 2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 1.7.4 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve/damper : 1.7.4.1 . Identif

y caus e o f

actuatio n failure . 1.7.4.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 1.7.4.3 . Service/replac e actuato r and/o r valv e components , as needed . 1.7.5 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 1.7.5.1 . Identif

y fault y contro l syste mcomponent . 1.7.5. 2 Service/replac e contro l syste mcomponents , as needed . 1.8 . Excessiv

e Ai rIn-leakag

e i n Ai rPollutio n Contro l Syste m 1.8. 1 I n cas e o f

hole s du e to corrosion : 1.8.1.1 . Identif

y locatio n o f

hole . 1.8.1.2 . Repai r

syste mas needed . 1.8. 2 I n cas e o f

ope n ports , manways , acces s ports , etc . 1.8.2.1 . Identif

y locatio n o f

ope n port , manway , etc . 1.8.2.2 . Replac e cove r o n ope n port , manway , etc .

Pag e 4 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

PRIMAR Y COMBUSTIO N CHAMBE R 2.1 . Los s of

Natura l Gas Pressure/Flo w t o PC C Mai n Burne r 2.1.1 . I n cas e o f

plugging/physica l failur e o f lin e or lin e component : 2.1.1.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 2.1.1.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 2.1.2 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 2.1.2.1 . Identif

y caus e o f

actuatio n failure . 2.1.2.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 2.1.2.3 . Service/replac e actuato r and/o r valv e components , a s needed . 2.1.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.1.3.1 . Identif

y fault y contro l syste mcomponent . 2.1.3.2 . Service/replac e contro l syste mcomponents , as needed . 2.1.4 . I n cas e o f

mechanical/electrica l failur e a t natura l ga s suppl y source : 2.1.4.1 . Identif

y th e caus e o f

th e failure . 2.1.4.2 . Tak e th e necessary action s to restore th e suppl y o f

natura l gas . 2.2. Los s of

Combustio n Ai rPressure/Flo w t o PC C 2.2.1 . I n cas e o f

mechanical/electrica l failur e o f combustio n ai r

blower : 2.2.1.1 . Diagnos e blower/driv e failure . 2.2.1.2 . Service/replac e th e blower/drive , as needed . 2.2.1.3 . Restor e electrica l powe r suppl y to th e blower . 2.2.2 . I n cas e o f

physica l failur e o f

combustio n ai r

duct : 2.2.2.1 . Identif

y th e locatio n o f

duc t failure . 2.2.2.2 . Service/replac e fault y duct , as needed . 2.2.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 2.2.3.1 . Identif

y caus e o f

actuatio n failure . 2.2.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 2.2.3.3 . Service/replac e actuato r and/o r valv e components , as needed . Pag e 5 of2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 2.2.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.2.4.1 . Identif

y fault y contro l syste mcomponent . 2.2.4.2 . Service/replac e contro l syste mcomponents , as needed . 2.3 . PC C Mai n Burne rPilo tFailur e 2.3.1 . Fo r

los s o f natura l ga s pressure/flow , see 2.1 . 2.3.2 . Fo r

los s o f combustio n ai r

pressure/flow , see 2.2 . 2.3.3 . I n cas e o f

physical/electrica l failur e o f igniter : 2.3.3.1 . Identif

y caus e o f

ignite r failure . 2.3.3.2 . Service/replac e ignite r and/o r associate dcomponents , a s needed . 2.3.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.3.4.1 . Identif

y fault y contro l syste mcomponent . 2.3.4.2 . Service/replac e contro l syste mcomponents , as needed . 2.4. Los s o

f Wast e Flow t o PC C Injecto r 2.4.1 . I n cas e o f

mechanical/electrica l failur e o f wast e fee dpump : 2.4.1.1 . Diagnos e pump/driv e failure . 2.4.1.2 . Service/replac e th e pump/drive , as needed . 2.4.1.3 . Restor e electrica l powe r suppl y to th e pump . 2.4.2 . I n cas e o f

lo w nitroge n pressure , se e 1.4 . 2.4.3 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 2.4.3.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 2.4.3.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 2.4.3.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 2.4.4 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 2.4.4.1 . Identif

y caus e o f

actuatio n failure . 2.4.4.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 2.4.4.3 . Service/replac e actuato r and/o r valv e components , as needed . 2.4.5 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.4.5.1 . Identif

y fault y contro l syste mcomponent . 2.4.5.2 . Service/replac e contro l syste mcomponents , as needed . 2.5 . Los s of

Wast e Feedrat

e Contro l t

o PC C Injecto r 2.5.1 . I n cas e o f

los s o f waste pressure/flo w to PC C injector , see 2.4 . Pag e 6 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 2.5.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replac e flo w transmitte r and/o r associate dinstrumentation , a s needed . 2.5.3 . I n cas e o f

actuate dvalv e failure : 2.5.3.1 . Identif

y caus e o f

actuatio n failure . 2.5.3.2 . Service/replace electrica l and/o r pneumati c components , as needed . 2.5.3.3 . Service/replace actuato r and/o r valv e components , a s needed . 2.5.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.5.4.1 . Identif

y fault y contro l syste mcomponent . 2.5.4.2 . Service/replace contro l syste mcomponents , a s needed . 2.6 . Los s o

f Atomizatio n Ai rPressur e t o aPC C Injecto r 2.6.1 . Fo r

atota l los s o f

plant/instrumen t

ai r supply , see 1.3 . 2.6.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 2.6.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 2.6.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 2.6.3 . I n cas e o f

mechanical/physica l failur e o f pressur e contro l valve : Service/replace pressur e contro l valve , a s needed . 2.7 . Los s of

PC C Draf

tContro l (Uni t4

) 2.7.1 . I n cas e o f

I D fa n failure , see 9. 5 2.7.2 . I n cas e o f

physical/electrica l failur e o f kil npressure transmitter : Service/replac e pressure transmitte r and/o r

associate d instrumentation , as needed . 2.7.3 . I n cas e o f

actuate ddamper

failure : 2.7.3.1 . Identif

y caus e o f

actuatio n failure . 2.7.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 2.7.3.3 . Service/replac e actuato r and/o r dampe r components , a

s needed . 2.7.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.7.4.1 . Identif

y fault y contro l syste mcomponent . 2.7.4.2 . Service/replace contro l syste mcomponents , as needed .

Pag e 7 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 2.8. Los s of

PC C Temperature Contro l 2.8.1 . I n cas e o f

los s o f natura l gas pressure/flo w to mai n burner , see 2.1 . 2.8.2 . I n cas e o f

los s o f waste pressure/flo w to PC C injector , see 2.4 . 2.8.3 . I n cas e o f

physical/electrica l failur e o f temperature element : 2.8.3.1 . Service/replac e fault y temperature elemen t and/o r associate dinstrumentation , as needed . 2.8.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.8.4.1 . Identif

y fault y contro l syste mcomponent . 2.8.4.2 . Service/replac e contro l syste mcomponents , as needed . 2.9 . Flam e Failur e 2.9.1 . I n cas e o f

physical/electrica l failur e o f flam e detector : 2.9.1.1 . Identif

y fault y flam e detecto r

component . 2.9.1.2 . Service/replac e flam e detecto r components , as needed . 2.9.2 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.9.2.1 . Identif

y fault y contro l syste mcomponent . 2.9.2.2 . Service/replac e contro l syste mcomponents , as needed . 2.10. Kil n Rotatio n Malfunctio n (Unit4 ) 2.10.1 . I n cas e o f

mechanical/electrica l kil ndriv e system : 2.10.1.1 . Diagnos e driv e failure . 2.10.1.2 . Service/replac e th e drive , a s needed . 2.10.1.3 . Restor e electrica l powe r suppl y to motor . 2.10.2 . I n cas e o f

physical/electrica l failur e o f kil nrotationa l spee d transmitter : Service/replac e transmitte r and/o r

associate d instrumentation , as needed . 2.10.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 2.10.3.1 . Identif

y fault y contro l syste mcomponent . 2.10.3.2 . Service/replac e contro l syste mcomponents , as needed . 2.11 . Bulk/Charg e Fee d Doo rMalfunctio n 2.11.1 . I n cas e o f

mechanical/electrica l failur e o f actuate ddoor : 2.11.1.1 . Identif

y caus e o f

actuatio n failure . 2.11.1.2 . Service/replac e electrical , hydraulic , and/o r pneumati c components , as needed . 2.11.1.3 . Service/replac e actuato r and/o r valv e components , a s needed . 2.11.2 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : Pag e 8 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

2.11.2.1 . Identif

y fault y contro l syste mcomponent . 2.11.2.2 . Service/replac e contro l syste mcomponents , as needed . 2.12. Physical/Mechanical Internal Equipmen tFailur e 2.12.1 . I n cas e o f

refractor y failure , repair/replac e refractor y 2.12.2 . I n cas e o f

as hcollectio n failur e 2.12.2.1 . Diagnos e as hcollectio n syste mfailur e 2.12.2.2 . Service/replac e as hcollectio n syste mcomponents , as

needed . 2.13 . PC C Sea

l Visua l Emissions Monitorin g and Recordin g Syste m 2.13.1 . I n cas e o f

physical/electrica l failur e o f camera , service/replac e camera . 2.13.2 . I n cas e o f

physical/electrica l failur e o f monitor , service/replac e monitor . 2.13.3 . I n cas e o f

physical/electrica l failur e o f recordin g system , service/replac e recordin g system . 2.14. Rapi d Stea

m Generatio n fro m As h Collectio n Syste m Wate r 2.14.1 . I n cas e o f

refractor y failure , repair/replac e refractory . 2.14.2 . I n cas e o f

uncontrolle dmovement/droppin g o f residu e int o as h collectio n syste mwater , inspec t syste mto identify/remov e other suspec t material .

Pag e 9 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

SECONDAR Y COMBUSTIO N CHAMBE R 3.1 . Los s o

f Natura l Gas Pressure/Flo w t o SC C Mai n Burne r 3.1.1 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 3.1.1.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 3.1.1.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 3.1.2 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 3.1.2.1 . Identif

y caus e o f

actuatio n failure . 3.1.2.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 3.1.2.3 . Service/replac e actuato r and/o r valv e components , as needed . 3.1.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.1.3.1 . Identif

y fault y contro l syste mcomponent . 3.1.3.2 . Service/replac e contro l syste mcomponents , as needed . 3.1.4 . I n cas e o f

mechanical/electrica l failur e a t natura l ga s suppl y source : 3.1.4.1 . Identif

y th e caus e o f

th e failure . 3.1.4.2 . Tak e th e necessary action s to restore th e suppl y o f

natura l gas . 3.2. Los s o

f Combustio n Ai rPressure/Flo w t o SC C 3.2.1 . I n cas e o f

mechanical/electrica l failur e o f combustio n ai r

blower : 3.2.1.1 . Diagnos e blower/driv e failure . 3.2.1.2 . Service/replac e th e blower/drive , as needed . 3.2.1.3 . Restor e electrica l powe r suppl y to th e blower . 3.2.2 . I n cas e o f

physica l failur e combustio n ai r duct : 3.2.2.1 . Identif

y th e locatio n o f

duc t failure . 3.2.2.2 . Service/replac e fault y duct , as needed . 3.2.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 3.2.3.1 . Identif

y caus e o f

actuatio n failure . 3.2.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 3.2.3.3 . Service/replac e actuato r and/o r valv e components , a s needed . Pag e 1 0 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 3.2.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.2.4.1 . Identif

y fault y contro l syste mcomponent . 3.2.4.2 . Service/replac e contro l syste mcomponents , as needed . 3.3 . SC C Mai n Burne rIgnitio n Failur e 3.3.1 . Fo r

los s o f natura l ga s pressure/flow , se e 3.1 . 3.3.2 . Fo r

los s o f combustio n ai r

pressure/flow , see 3.2 . 3.3.3 . I n cas e o f

physical/electrica l failur e o f igniter : 3.3.3.1 . Identif

y caus e o f

ignite r failure . 3.3.3.2 . Service/replac e ignite r and/o r associate dcomponents , as needed . 3.3.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.3.4.1 . Identif

y fault y contro l syste mcomponent . 3.3.4.2 . Service/replac e contro l syste mcomponents , a s needed . 3.4. Los s of

Wast e Flo w t o SC C Injecto r(Unit4 ) 3.4.1 . I n cas e o f

mechanical/electrica l failur e o f waste fee dpump : 3.4.1.1 . Diagnos e pump/driv e failure . 3.4.1.2 . Service/replac e th e pump/drive , as needed . 3.4.1.3 . Restor e electrica l powe r suppl y to the pump . 3.4.2 . I n cas e o f

lo w nitroge n pressure , see 1.4 . 3.4.3 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 3.4.3.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 3.4.3.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 3.4.3.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 3.4.4 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 3.4.4.1 . Identif

y caus e o f

actuatio n failure . 3.4.4.2 . Service/replac e electrica l and/o r pneumati c components , a

s needed . 3.4.4.3 . Service/replac e actuato r and/o r valv e components , as needed . 3.4.5 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.4.5.1 . Identif

y fault y contro l syste mcomponent . 3.4.5.2 . Service/replac e contro l syste mcomponents , as needed . 3.5 . Los s of

Wast e Feedrat

e Contro l t

o SC C Injecto r(Unit4 ) 3.5.1 . I n cas e o f

los s o f waste pressure/flo w t o SC C injector , se e 3.4 . Pag e 1 1 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 3.5.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replace flo w transmitte r and/o r associate dinstrumentation , as needed . 3.5.3 . I n cas e o f

actuate dvalv e failure : 3.5.3.1 . Identif

y caus e o f

actuatio n failure . 3.5.3.2 . Service/replace electrica l and/o r pneumati c components , as needed . 3.5.3.3 . Service/replace actuato r and/o r valv e components , as needed . 3.5.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.5.4.1 . Identif

y fault y contro l syste mcomponent . 3.5.4.2 . Service/replac e contro l syste mcomponents , a s needed . 3.6 . Los s of

Atomizatio n Ai rPressur e t o aSC C Injecto r 3.6.1 . Fo r

atota l los s o f

plant/instrumen t

ai r supply , see 1.3 . 3.6.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 3.6.2.1 . Identif

y the locatio n o f

pluggin g o r

lin e failure . 3.6.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 3.6.3 . I n cas e o f

mechanical/physica l failur e o f pressure contro l valve : Service/replace pressure contro l valve , as needed . 3.7 . Los s of

SC C Temperature Contro l 3.7.1 . I n cas e o f

los s o f natura l gas pressure/flo w to mai n burner , se e 3.1 . 3.7.2 . I n cas e o f

los s o f waste pressure/flo w to SC C injector , se e 3.4 . 3.7.3 . I n cas e o f

physical/electrica l failur e o f temperature element : 3.7.3.1 . Service/replace fault y temperature element and/o r associate dinstrumentation , as needed . 3.7.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.7.4.1 . Identif

y fault y contro l syste mcomponent . 3.7.4.2 . Service/replac e contro l syste mcomponents , as needed . 3.8 . Flam e Failur e 3.8.1 . I n cas e o f

physical/electrica l failur e o f flam e detector : 3.8.1.1 . Identif

y fault y flam e detecto r

component . 3.8.1.2 . Service/replace flam e detecto r components , a

s needed . 3.8.2 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 3.8.2.1 . Identif

y fault y contro l syste mcomponent . Pag e 1 2 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

3.8.2.2 . Service/replace contro l syste mcomponents , a s needed . 3.9 . Physical/Mechanical Interna l Equipmen tFailur e 3.9.1 . I n cas e o f

refractor y failure , repair/replac e refractory . 3.10 . Lo w Wate rLeve l i n Slag Collectio n Syste m (Unit4

) 3.10.1 . Fo r

alos s o f proces s wate r

pressure/flow , see 1.6 . 3.10.2 . I n cas e o f

physical/mechanica l failur e o f leve l controller : Service/replac e fault y leve l controlle r and/o r associate d components , a

s needed . 3.10.3 . I n cas e o f

physical/mechanica l failur e o f actuate dvalve : 3.10.3.1 . Identif

y caus e o f

actuatio n failure . 3.10.3.2 . Service/replace pneumati c components , as needed . 3.10.3.3 . Service/replace actuato r and/o r valv e components , a s needed . 3.11 . Emergenc

y Safet y Ven tOpenin g 3.11.1 . Respon dto a

n emergenc y safety ven t openin g i n amanner consisten t

wit hth e Emergency Safety Vent Plan. 3.11.2 . I n cas e o f

mechanica l failur e o f

th e actuator : 3.11.2.1 . Identif

y caus e o f

actuatio n failure . 3.11.2.2 . Service/replace emergenc y safety ven t components , a

s needed . 3.12. Rapi d Stea

m Generatio n fro m As h Collectio n Syste m Wate r 2.14.1 . I n cas e o f

refractor y failure , repair/replac e refractory . 2.14.2 . I n cas e o f

uncontrolle dmovement/droppin g o f residu e int o as h collectio n syste mwater , inspec t syste mto identify/remov e other suspec t material .

Pag e 1 3 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

TEMPERIN G CHAMBE R(UNI T 4 ) 4.1 . Los s of

Temperin g Chambe rExi tGa s Temperature Contro l 4.1.1 . Fo r

alos s o f proces s water

pressure/flow , see 1.6 . 4.1.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replac e flo w transmitter and/o r associate dinstrumentation , as needed . 4.1.3 . I n cas e o f

actuate dvalv e failure : 4.1.3.1 . Identif

y caus e o f

actuatio n failure . 4.1.3.2 . Service/replace electrica l and/o r pneumati c components , a

s needed . 4.1.3.3 . Service/replace actuato r and/o r valv e components , as needed . 4.1.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 4.1.4.1 . Identif

y fault y contro l syste mcomponent . 4.1.4.2 . Service/replac e contro l syste mcomponents , as needed . 4.1.5 . I n cas e o f

nozzl e failure , service/replac e nozzle , as needed . 4.2. Los s o

f Atomizatio n Ai rPressur e t o Nozzl e 4.2.1 . Fo r

atota l los s o f

plant/instrumen t

ai r supply , see 1.3 . 4.2.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 4.2.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 4.2.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed .

Pag e 1 4 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

LIM E SLURR Y SYSTE M 5.1 . Los s o

f Lim e Feed t

o Lim e Slurr y Fee d Tan k 5.1.1 . I n cas e o f

mechanical/electrica l failur e o f lim e slurr y scre w feeder : 5.1.1.1 . Diagnos e feeder/driv e failure . 5.1.1.2 . Service/replac e th e feeder/drive , as needed . 5.1.1.3 . Restor e electrica l powe r suppl y to th e lim e slurr y scre w feeder . 5.1.2 . I n cas e o f

mechanical/electrica l failur e o f lim e bi n activator/vibrator : 5.1.2.1 . Diagnos e lim e bi n activator/vibrato r failure . 5.1.2.2 . Service/replac e th e lim e bi n activator/vibrator , a s needed . 5.1.2.3 . Restor e electrica l powe r suppl y to th e lim e slurr y scre w feeder . 5.1.3 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 5.1.3.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 5.1.3.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 5.1.4 . I n cas e o f

physical/electrica l failur e o f lim e fee dcontrols : Service/replace fault y instrumentatio n and/o r contro l syste m components , as needed . 5.2. Malfunctio n i n Lim e Slurr y Concentratio n 5.2.1 . I n cas e o f

los s o f lim e fee dto lim e slurr y fee dtank , see 5. 1 5.2.2 . I n cas e o f

los s o f wate r flo w to lim e slurr y fee dtank , se e 1. 5 5.2.3 . I n cas e o f

mechanical/electrica l failur e o f lim e slurr y agitator : 5.2.3.1 . Diagnos e agitator/driv e failure . 5.2.3.2 . Service/replac e th e agitator/drive , a s needed . 5.2.3.3 . Restor e electrica l powe r suppl y to th e lim e slurr y agitator . 5.2.4 . I n cas e o f

physical/electrica l failur e o f instrumentation : Service/replace fault y instrumentation , as needed . 5.2.5 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 5.2.5.1 . Identif

y fault y contro l syste mcomponent . 5.2.5.2 . Service/replac e contro l syste mcomponents , as needed .

Pag e 1 5 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

UNIT S 2 AN D 3 SPRA Y DRYE RABSORBE R(SDA ) 6.1 . Los s o

f Lim e Slurr y Flo w t

o SD A 6.1.1 . I n cas e o f

mechanical/electrica l failur e o f lim e slurr y fee dpump : 6.1.1.1 . Diagnos e pump/driv e failure . 6.1.1.2 . Service/replac e th e pump/drive , as needed . 6.1.1.3 . Restor e electrica l powe r suppl y to th e pump . 6.1.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 6.1.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 6.1.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 6.1.2.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 6.1.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 6.1.3.1 . Identif

y caus e o f

actuatio n failure . 6.1.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 6.1.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 6.1.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 6.1.4.1 . Identif

y fault y contro l syste mcomponent . 6.1.4.2 . Service/replac e contro l syste mcomponents , as needed . 6.2 . Los s o

f Lim e Slurr y Flo w Contro l 6.2.1 . I n cas e o f

los s o f slurr y flo w to SDA , se

e 6.1 . 6.2.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replac e flo w transmitte r and/o r associate dinstrumentation , a s needed . 6.2.3 . I n cas e o f

actuate dvalv e failure : 6.2.3.1 . Identif

y caus e o f

actuatio n failure . 6.2.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 6.2.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 6.2.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 6.2.4.1 . Identif

y fault y contro l syste mcomponent . 6.2.4.2 . Service/replac e contro l syste mcomponents , as needed .

Pag e 1 6 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 6.3 . Los s o

f Cit y Wate rFlo w t

o SD A (Unit2 and 3

) 6.3.1 . I n cas e o f

tota l los s o f

cit y wate r

supply , see 1.5 . 6.3.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 6.3.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 6.3.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 6.3.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 6.3.3.1 . Identif

y caus e o f

actuatio n failure . 6.3.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 6.3.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 6.4. Los s o

f Coolin g Ai rFlo w t

o Atomize r 6.4.1 . I n cas e o f

mechanical/electrica l failur e o f atomize r

coolin g ai r blower : 6.4.1.1 . Diagnos e blower/driv e failure . 6.4.1.2 . Service/replac e th e blower/drive , a s needed . 6.4.1.3 . Restor e electrica l powe r suppl y to th e blower . 6.4.2 . I n cas e o f

physica l failur e o f

atomize r coolin g ai r

duct : 6.4.2.1 . Identif

y th e locatio n o f

duc t failure . 6.4.2.2 . Service/replac e fault y duct , a s needed . 6.4.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 6.4.3.1 . Identif

y fault y contro l syste mcomponent . 6.4.3.2 . Service/replac e contro l syste mcomponents , as needed . 6.5 . Los s o

f SD A Exi tGas Temperature Contro l 6.5.1 . I n cas e o f

los s o f cit y wate r

flo w to SDA , see 6.3 . 6.5.2 . I n cas e o f

physical/electrica l failur e o f temperature transmitter : Service/replac e temperature transmitte r and/o r

associate d instrumentation , as needed . 6.5.3 . I n cas e o f

actuate dvalv e failure : 6.5.3.1 . Identif

y caus e o f

actuatio n failure . 6.5.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 6.5.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 6.5.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : Pag e 1 7 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

6.5.4.1 . Identif

y fault y contro l syste mcomponent . 6.5.4.2 . Service/replac e contro l syste mcomponents , as needed . 6.6. Atomize rFailur e 6.6.1 . I n cas e o f

lo w atomizer

lubricatio n oi l flow : 6.6.1.1 . Diagnos e th e failur e i n th e lubricatio n syste m 6.6.1.2 . Service/replac e component s o f th e lubricatio n system , a s needed . 6.6.2 . I n cas e o f

mechanical/electrica l failur e o f atomizer : 6.6.2.1 . Diagnos e atomizer/driv e failure . 6.6.2.2 . Service/replac e the atomizer/drive , as needed . 6.6.2.3 . Restor e electrica l powe r suppl y to th e atomizer . 6.6.2.4 . components , as needed .

Pag e 1 8 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

UNI T 4 SPRA Y DRYE RABSORBE R(SDA ) 7.1 . Los s o

f Lime Slurr y Flo w t

o SD A 7.1.1 . I n cas e o f

mechanical/electrica l failur e o f lim e slurr y fee dpump : 7.1.1.1 . Diagnos e pump/driv e failure . 7.1.1.2 . Service/replac e th e pump/drive , as needed . 7.1.1.3 . Restor e electrica l powe r suppl y to th e pump . 7.1.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 7.1.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 7.1.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 7.1.2.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 7.1.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 7.1.3.1 . Identif

y caus e o f

actuatio n failure . 7.1.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 7.1.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 7.1.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 7.1.4.1 . Identif

y fault y contro l syste mcomponent . 7.1.4.2 . Service/replac e contro l syste mcomponents , as needed . 7.2 . Los s of

Lim e Slurr y Flo w Control/Exi tGas Temperature Contro l 7.2.1 . Incaseoflossofslurryflowt o SDA , se e 7.1 . 7.2.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replac e flo w transmitte r and/o r associate dinstrumentation , a s needed . 7.2.3 . I n cas e o f

actuate dvalv e failure : 7.2.3.1 . Identif

y caus e o f

actuatio n failure . 7.2.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 7.2.3.3 . Service/replac e actuato r and/o r valv e components , a s needed . 7.2.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 7.2.4.1 . Identif

y fault y contro l syste mcomponent . 7.2.4.2 . Service/replac e contro l syste mcomponents , as needed .

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2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 7.3 . Los s of

Atomizatio n Ai rPressur e t o SD A Nozzl e 7.3.1 . Fo r

atota l los s o f

plant/instrumen t

ai r supply , see 1.3 . 7.3.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 7.3.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 7.3.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed .

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2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

CARBO N INJECTIO N SYSTE M (UNI T 4 ) 8.1 . Los s of

Carrie rGas Pressur

e 8.1.1 . I n cas e o f

mechanical/electrica l failur e o f carbo n injectio n ai r blower : 8.1.1.1 . Diagnos e blower/driv e failure . 8.1.1.2 . Service/replac e th e blower/drive , as needed . 8.1.1.3 . Restor e electrica l powe r suppl y to th e blower . 8.1.2 . I n cas e o f

physica l failur e ai r

duct : 8.1.2.1 . Identif

y th e locatio n o f

duc t failure . 8.1.2.2 . Service/replac e fault y duct , as needed . 8.1.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 8.1.3.1 . Identif

y fault y contro l syste mcomponent . 8.1.3.2 . Service/replac e contro l syste mcomponents , a s needed . 8.2 . Loss/Restrictio n of Activate d Carbo n Flo w 8.2.1 . I n cas e o f

los s ofplan t

ai r to carbo n bul k

sack , se e 8. 3 8.2.2 . I n cas e o f

mechanical/electrica l failur e o f carbo n feeder : 8.2.2.1 . Diagnos e feeder/driv e failure . 8.2.2.2 . Service/replac e th e feeder/drive , as needed . 8.2.2.3 . Restor e electrica l powe r suppl y to th e carbo n feeder . 8.2.3 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 8.2.3.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 8.2.3.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 8.2.3.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 8.3. Los s o

f PlantAi rPressure/Flo w t o Carbo n Bul kSac

k 8.3.1 . Fo r

atota l los s o f

plant/instrumen t

ai r supply , see 1.3 . 8.3.2 . I n cas e o f

plugging/physica l failur e o f lin e o r lin e component : 8.3.2.1 . Identif

y th e locatio n o f

pluggin g o r

lin e failure . 8.3.2.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , as needed . 8.3.3 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 8.3.3.1 . Identif

y caus e o f

actuatio n failure . 8.3.3.2 . Service/replac e electrica l and/o r pneumati c components , as needed . Pag e 2 1 o f

2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

8.3.3.3 . Service/replac e actuato r and/o r valv e components , as needed . 8.3.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 8.3.4.1 . Identif

y fault y contro l syste mcomponent . 8.3.4.2 . Service/replac e contro l syste mcomponents , a s needed .

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2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

BAGHOUS E & INDUCE D DRAF T (ID) FA N 9.1 . Torn/Leakin g Ba g 9.1.1 . I n cas e o f

abaghous e lea k

detectio n alarm , follo w the relevan t correctiv e measure s prescribe di n th e Operatio n an dMaintenanc e Plan . 9.1.2 . I n cas e o f

abaghous e leak

detectio n syste mfailure : 9.1.2.1 . Service/replac e torn/leakin g bag(s) , as needed . 9.1.2.2 . Diagnos e th e failur e o f th e baghous e detectio n system . 9.1.2.3 . Service/replac e baghous e leak detectio n system , a s needed . 9.2. Ba g Blinding/High-Hig h Pressur e Dro p 9.2.1 . I n cas e o f

lo w baghous e inle t

ga s temperature : 9.2.1.1 . Follo w th e appropriat e correctiv e action s prescribe db y

paragrap h6. 5 (Uni t

2 an d3 ) 9.2.1.2 . Follo w th e appropriat e correctiv e action s prescribe db y

paragrap h7. 2 (Uni t

4 ) 9.2.1.3 . Perfor mbaghous e inspection . 9.2.1.4 . Service/replac e bag(s) , a s needed . 9.3 . Los s o

f Stac k Gas Flowrat

e Contro l (Uni t2 and 3 ) 9.3.1 . I n cas e o f

I D fa n failure , see 9. 5 9.3.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitter : Service/replace flo w transmitte r and/o r associate dinstrumentation , a s needed . 9.3.3 . I n cas e o f

actuate ddamper

failure : 9.3.3.1 . Identif

y caus e o f

actuatio n failure . 9.3.3.2 . Service/replac e electrica l and/o r pneumati c components , a

s needed . 9.3.3.3 . Service/replac e actuato r and/o r damper components , as needed . 9.3.4 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 9.3.4.1 . Identif

y fault y contro l syste mcomponent . 9.3.4.2 . Service/replac e contro l syste mcomponents , as needed . 9.4. Baghouse Isolation Dampe rMalfunctio n (Unit4 ) 9.4.1 . I n cas e o f

actuate ddamper

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2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

9.4.2 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 9.4.2.1 . Identif

y fault y contro l syste mcomponent . 9.4.2.2 . Service/replac e contro l syste mcomponents , as needed . 9.5. ID Fa n Failur e 9.5.1 . I n cas e o f

mechanical/electrica l failur e o f I D fan : 9.5.1.1 . Diagnos e fan/driv e failure . 9.5.1.2 . Service/replace th e fan/drive , as needed . 9.5.1.3 . Restor e electrica l powe r suppl y to th e I D fan . 9.4.1. 3 9.4.1. 1 9.4.1. 2 Identif

y caus e o f

actuatio n failure . Service/replace electrica l and/o r pneumati c components , as needed . Service/replac e actuato r and/o r damper components , as needed .

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2 6VEOLI A ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

10. 0 CONTRO L SYSTEM/CONTINUOU S MONITORIN G SYSTE M 10.1 . Contro l System/Continuous Monitorin g Syste m Malfunctio n 10.1.1 . A s needed , refe r t o th e CMS

QA/QC Plan fo r

guidanc e an dto ensur e tha t prope r calibration s ar

e performed . 10.1.2 . I n cas e o f

physical/electrica l failur e o f instrumentation : 10.1.2.1 . Identif

y fault y instrumentatio n component . 10.1.2.2 . Service/replac e fault y instrumentatio n components , as

needed . 10.1.3 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 10.1.3.1 . Identif

y fault y contro l syste mcomponent . 10.1.3.2 . Service/replac e contro l syste mcomponents , as needed . 10.1.4 . I n cas e o f

physical/electrica l failur e o f dat aacquisition/availability : 10.1.4.1 . Identif

y fault y datasyste mcomponents . 10.1.4.2 . Service/replac e dat asyste mcomponents , as needed . 10.2. Continuou s Emissions Monitorin g Syste m Malfunctio n 10.2.1 . A s needed , refe r t o the CEMS

QA/QC Plan fo r

guidanc e an dto ensur e tha t prope r calibration s ar

e performe dan dtha t the appropriate performanc e specification s ar e met . 10.2.2 . I n cas e o f

physical/electrica l failur e umbilica l hea t tracing : 10.2.2.1 . Diagnos e failur e o f hea t tracing . 10.2.2.2 . Replace/restor e hea t trace dsampl e umbilical . 10.2.3 . I n cas e o f

mechanical/electrica l failur e o f heate dvacuu mpump : 10.2.3.1 . Diagnos e pump/driv e failure . 10.2.3.2 . Service/replac e the pump/drive , as needed . 10.2.3.3 . Replace/restor e pum p hea dhea

t source . 10.2.3.4 . Restor e electrica l powe r suppl y to heate dvacuu m pump . 10.2.4 . I n cas e o f

plugging/physica l failur e o f sampl e probe/umbilical : 10.2.4.1 . Identif

y the locatio n o f

failure . 10.2.4.2 . Clea r

pluggin g and/o r

service/replac e fault y components , as needed . 10.2.5 . I n cas e o f

mechanical/electrica l failur e o f actuate dvalve : 10.2.5.1 . Identif

y caus e o f

actuatio n failure .

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10.2.5.2 . Service/replac e electrica l and/o r pneumati c components , as needed . 10.2.5.3 . Service/replac e actuato r and/o r valv e components , as needed . 10.2.6 . I n cas e o f

mechanical/electrica l failur e o f analyzer : 10.2.6.1 . Refe r

to manufacturer' s servic e manua l fo r guidanc e o n troubleshootin g an dservicin g analyzer . 10.2.6.2 . Service/replac e analyzer , as needed . 10.2.7 . I n cas e o f

mechanical/electrica l failur e o f associate d instrumentation : 10.2.7.1 . Identif

y fault y instrumentatio n component . 10.2.7.2 . Service/replac e fault y instrumentatio n components , as

needed . 10.2.8 . I n cas e o f

physical/electrica l failur e o f contro l syste mcomponent : 10.2.8.1 . Identif

y fault y contro l syste mcomponent . 10.2.8.2 . Service/replac e contro l syste mcomponents , as needed .

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2 6