# VE S 001918.pd fVEOLI A E S TECHNICA L SOLUTIONS , L.L.C . RESPONSE S T O TH E UNITE D STATE S ENVIRONMENTA L PROTECTIO N AGENCY' S REQUES T T O PROVID E INFORMATIO N PURSUAN T T O TH E CLEA N AI RAC T DATE D JANUAR Y 29 , 200 9



# Exhibit s A - B

### A

V E S 00191 S

### ONY X ENVIRONMENTA L SERVICE S SAUGET , I L DOCUMEN T O F COMPLIANC E NATIONA L EMISSIO N STANDARD S FO R HAZARDOU S AI R POLLUTANT S FRO M HAZARDOU S WAST E COMBUSTOR S

40 CF R PAR T 63 , SUBPAR T EE E

JUN E 30 , 200

4

# ONX X ONYX ENVIRONMENTA L SERVICE S

SAUGET , I L DOCUMEN T O F COMPLIANC E NATIONA L EMISSIO N STANDARD S FO R HAZARDOU S AI R POLLUTANT S FRO M HAZARDOU S WAST E COMBUSTOR S

4 0 CF R PAR T 63 , SUBPAR T EE E JUN E 30 , 200

4 Ony x Environmenta l Service s certifie s that : (i ) Require d CEM s an d CM S ar e installed , calibrated , an d continuou s operatin g i n complianc e wit h th e requirement s o f thi s subpart ; an d (ii ) Base d o n a n engineerin g evaluatio n prepare d unde r m y directio n o r supervisio n i n accordanc e wit h a syste m designe d t o ensur e tha t qualifie d personne l properl y gathere d an d evaluate d th e informatio n an d supportin g documentation , an d considerin g a t a minimu m th e design , operation , an d maintenanc e characteristic s o f th e combusto r an d emissio n contro l equipment , th e types , quantities , an d characteristi c o f feedstreams , an d availabl e emission s data :

' (A ) Onyx Environmenta l Service s i s i n complianc e wit h th e emissio n standard s o f thi s subpart ; an d (B ) Th e limit s o n th e operatin g parameters unde r 63.120 9 ensur e complianc e wit h th e emissio n standard s o f thi s subpart .

Genera l Manage r Ony x Environmenta l Services , L.L.C . # 7 Mobil e Avenue , Sauge tI L 6220 1 Tel : 61 8 27 1 280

4 • Fax : 61 8 27 1 2128 Environmen t V E S 00192 1

### DOCUMEN T O F COMPLIANCE TABL E O F CONTENT Applicable Emissio n Standard s Section 1 An d Operatin

g Parameter

s Start-up , Shutdow

n an d Section 2 Malfunctio

n Pla n Operatin g an d Maintenanc

e Pla n CM S Pla n ES V Pla n AWFC O Pla

n Feed Strea

m Analysi s Pla

n CEM s Pla

n (QA/Q C Plan

) Relativ e Accurac

y TestAudi

tSection 3 Fo r CEM s Specificatio n Sheet

s for Hydrate

d Lim e Section 4 Specificatio n Sheet

s fo r Carbo

n Residenc

e Tim e Calculation

s Operato r Certification Trainin

g Section 5

## HW C MAC T Emission Standard s

Paramete r Dioxin/Fura n (D/F ) Mercur y (Hg ) * Semivolatil e Metal s (SVM ) Cadmium , Lea d* Lo w Volatil e Metal s (LVM ) Arsenic , Beryllium , Chromiu m* Carbo n Monoxid e (CO ) Mydroge n Chloride/Chlorin e tHCl/C12 ) Particulate Unit s Standar d ng/dsc mTE Q 0.2 0 ug/dsc m ug/dsc m ug/dsc m ppmv ppmv mg/dsc m 13 0

24 0 9 7 10 0 7 7 3 4 Metho do f Complianc e Operatin g Paramete

r Limit s Operatin g Paramete

r Limit s Operatin g Paramete

r Limit s Operatin g Paramete

r Limit s Continuou s Emission s Monito r Continuou s Emission s Monito r Operatin g Paramete

r Limit s

* Base do n incinerato r

performanc e testin g result s fo r emission s o f

th e thre e metal s classifications , fee d limitation s for

Hg , SVM , andLV M hav e been linearl y extrapolate dt o aleve l equivalent t o eight y percen t o f the respectiv e emissio n standard .

V E SUNIT S 2/ 3 OPERATIN G PARAMETER S

Operatin g Paramete

r Unit s Limit s Dat ai n Lie u Tes t Performanc e Standard s Maximu mTota l Pumpabl e TLb/ia 312 3 Waste (Hourl y Rollin g Total ) Maximu mTota l Hazardou s Lb/h r 430 1 Wast e (Hourl y Rollin g Total ) Maximu mStac k

Ga s Flo w Acf m15,53 4 Rat e (Hourl y Rollin g Average ) Minimu mPrimary Combustio n Deg F 171 2 Chamber Temperatur

e (Hourl y Rollin g Average ) Mmimu mSecondar

y Combustio n De g F 184 5 Chambe r Temperatur

e (Hourl y jollin g Average ) Maximu mBaghous e Me t De g F 42 0 Temperatur

e (Hourl y Rollin g Average ) Maximu mLo w Volatil e Metal s Lb/h r 1264 Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mSemi Volatil e Mend s Lb/h r 347 7 Feedrat e (.1 2 Hou r

Rollin g Total ) -Maximu mMercury Feedrat e Lb/h r

0.007 3 (1 2 Hou r Rollin g Total ) ' Maximu mChlorin e Fee drat e Lb/h r

. " 23 7 (1 2 Hou r Rollin g Total ) Maximu mAs h Fee dRat e (1 2 Lb/h r

. 67 3 Hou r Rollm g Total ) May , 200 4 May , 200 4 Sept. , 200 3 May , 200 4

Tes t Report from1/21/9 7 May , 200 4 ' . Sept. , 200 3 Sept. , 200 3 May , 2004 . Tes t Repor t •fro m1/21/9 7 Tes t Repor t from1/21/9 7 DRE , D/ F DRE , D/ F DRE , D/F , Part. , SVM , L V M DRE , D/- F

DRE , D/ F

D/F j SVM , L V M L V M S V M H g SVM , LV M Part .

V E SUNI T 4 OPERATIN G PARAMETER S

Operatin g Parameter Unit s Limit s Dat ai n Lie u Tes t Performanc e Standard s Maximu mTota l Pumpabl e Lb/h r 426 2 Waste (Hourl y Rollin g Total ) Maximu mTota l Hazardou s Lb/h r 14,80 2 Wast e (Hourl y Rollin g Total ) Maximu mStac k

Ga s Flo w Acf m43,90 0 Rat e (Hourl y Rollin g Average ) Minimu mPrimar y Combustio n De g F 1507 Chambe r Temperatur

e (Hourl y Rollin g Average ) Minimu mSecondar

y Combustio n Deg F 188 6 hamber Temperatur

e (Hourl y tollin g Average ) Maximu mBaghous e Inle t De g F 43 5 Temperatur

e (Hourl y Rollin g Average ) Maximu mLo w Volatil e Metal s Lb/h r 120 Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mSemi Volatil e Metal s Lb/h r 11 7 Feedrat e (1 2 Hou r

Rollin g Total ) Maximu mMercur y Fee d rat e Lb/h r

0.06 7 (1 2 Hou r Rollin g Total ) Maximu mChlorin e Fee drat e Lb/h r

27 4 (1 2 Hou r Rollin g Total ) Maximu mAs h Fee dRate (1 2 Lb/h r 877 7 Hou r Rollin g Total ) ^^o n Injectio n Feedrat e Lb/h r

6 iourl y Rollin g Average ) Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 Sept. , 200 3 Cond . 1 May , 200 4 Sept. , 200 3 Cond . 1 Tes t Report from2/22/9 6 May , 200 4 DRE , D/ F

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

DRE , D/ F

D/F , SVM , L V M L V M S V M H g SVM , LV M Part . D/F , H gComplianc e wit h the Hydroge n Chlorid e an dChlorin e Ga s Standar di n $63.120 9 (o ) (4 ) Th e HW C MAC T Rul e emissio n limi t fo r HC1/C1 2i s 7 7 ppm . Veoli a demonstrate dcomplianc e wit h thi s emissio n limi t o n Unit s 2 , 3 , an d4 . HCI /CI 2 emission s durin g thes e test s wer e wel l belo w the 7 7 pp mUmit . Actua l emission s durin g thes e test s wer

e les s tha n 2 2 pp mfo r

al l thre e incinerators . Utilizin g dat a fromthes e tests , operatin g parameter s hav e been develope dtha t provid e apoint

o f complianc e wit h §63.120 9 (o ) (4) . Belo w i s asummar

y o f th e relativ e tes t

datafromthes e tests . Uni t .23 4 Tes t Date Jan . 199 3 Nov . 199 6 Dec . 199 5 Averag e Lim e Slurry Flo w 6. 5 gp m6. 6 gp m16. 8 gp m Averag e Chlorin e Fee d21 8 lb/h r 23 3 lb/hr

74 6 lb/h r Rati o o f Averag e Chlorin e Fee d33. 5 35. 3 44. 4 t o Averag e Lim e Slurr y Flo w Minimu msorben

t an dcarrie r

fluidflo w i s establishe dbase do n the rati o ofth e averag e chlorin e fee dt

o th e averag e lim e slurry flow fo r th e test s conducted . Th e maximu mrati o a

t whic h a n incinerato r

ca n operat

e i n complianc e an di n accordanc e wit h th e tes t

performanc e i s 33.5,35. 3 an d44.4 , respectivel y fo r Unit s 2 , 3 , an d4 . Thi s metho dutilize dthe tes t datat o establis h aminimu mslurry flow rat e base do n chlorin e fee drate . Thi s rati o i s calculate di n th e contro l system s o f eac h uni t o n areal-tim e basi s usin g th e rati o o f hourl y rollin g tota l chlorin e fee d divide db y the hourl y rollin g averag e lim e slurry flow . Operatin g paramete r limit s (OPL's ) ar

e se t a t th e maximu mrati o value s state dabov e a t al l three unite ;

### STARTUP , SHUTDOW N AN D MALFUNCTIO N PLA N Prepare d for : Ony x Environmenta

l Services , Inc

. Sauget , Illinois

Prepare d by : Franklin Engineering Group , Inc . Franklin , Tennesse

e

Jun e 200

4TABL E O FCONTENT S

1. 0 INTRODUCTIO N . ~ 1 1 - 1 REGULATOR Y REQUIREMENT S 2 l . 2 RECORDKEEPIN G AN D REPORTIN G PROCEDURE S 2 1.2.1 Records 4 1.2.2 Reports = i 2. 0 ENGINEERIN G DESCRIPTIO N 6 3. 0 STARTU P AN D SHUTDOW N PROCEDURE S 1 3 3. 1 STARTU P ; 1 3 3. 2 NORMA L SHUTDOW N ; 1 5 4. 0 MALFUNCTION S - ——1 6 4. 1 MEASURE S t o MINIMIZ E TH E FREQUENC Y O FMALFUNCTION S .-. 1 6 4. 2 MEASURE S T O MINIMIZ E TH E SEVERIT Y O FMALFUNCTION S .....1 8 4. 3 CORRECTIV E MEASURE S 1 9

i

V E S 00192 fLIS T O FTABLE S TABL E 1 - 1 OVERVIE W O FREGULATION S REGARDIN G STARTUP , SHUTDOW N AN D

MALFUNCTIO N . - . 3 TABL E 4- 1 SUMMAR Y O FPOTENTIA L MALFUNCTION S AN D CAUSE S : 1 7 TABL E 4- 2 REDUNDAN T EQUIPMEN T AN D SYSTEM S FO RMINIMIZIN G TH E FREQUENC Y

O RSEVERIT Y O FMALFUNCTION S 2 0

LIS T O FFIGURE S FIGUR E 2- 1 FIXE D HEART H INCINERATOR , UNIT2 , BLOCKFLO W DIAGRA M 7 FIGUR E 2- 2 FIXE D HEART H INCINERATOR , UNI T 3 , BLOCKFLO W DIAGRA M ; 8 FIGUR E 2- 3 ROTAR Y KIL N INCINERATOR , UNI T 4 , BLOCKFLO W DIAGRA M 1 1

LIS T O FATTACHMENT S ATTACHMEN T 1 STARTU P RECORDKEEPIN G FOR M ATTACHMEN T 2 SHUTDOW N RECORDKEEPIN G FOR M ATTACHMENT S MALFUNCTIO N RECORDKEEPIN G FOR M ATTACHMEN T 4 PROGRA M O FCORRECTIV E ACTION S FO RMALFUNCTION S

i i1. 0 INTRODUCTIO N Ony x Environmental Services , Inc . (Onyx ) own s an doperate s tw o fixe dheart h incinerator s (Unit s 2 and3 ) andarotar y kil n incinerato r

(Uni t 4 ) a t it s facilit y locate di n Sauget , Illinois . Th e incinerator s ar

e subjec t t o th e Nationa l Ernission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r

Hazardou s Wast

e Combustor s (HWC) , codifie da s 4 0 CFR , Par

t 63 , Subpar

t EE E ( § 63.120 0 to § 63.1213) . Th e NESHA P specifie s emission s standard s whic h reflec t emission s performanc e o f

Maximu mAchievabl e Contro l Technologie s (MACT) , andi s commonl y referre d t o a s th e HW C MACT . Th e HW C MAC T Standar ddefine s th e contro l o f emission s durin g normal , day-to-da y operations . I n orde

r t o addres s th e contro l o f emission s durin g transien t periods , th e developmen

t o f aStartup , Shutdown , an dMalfunctio n Pla n (SSMP ) i s require dStartup , shutdown , an dmalfunctio n (SSM ) ar e defme di n

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

portio n o f

an affecte dsourc e fo r any purpos e

• Shutdown - th

e cessatio n o f

operatio n o f

a n affecte dsourc e o r

portio n o f

a n affecte d sourc e fo r

any purpos e

• Malfunction - any sudden , infrequent , an dnot 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 n anormal o

r usual manne

r whic h causes , o r

ha s th e potential t

o cause , th

e emissio n limitation s i n a

n applicabl e standar

dt o b e exceeded . Failure s tha t ar e cause di n par

t b y poo r mamtenanc 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 h it s SSMP . Therefore , durin g period s o f

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

wil l b e consisten

t wit h the 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 exten t 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 , andmalfunctio n tha t ar e consistent

wit h safety 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 h period 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) , a s show n i n Tabl e 1- 1 1Du e t o th e similarit y o f

the three incinerato r

systems , genera

l reference s t

o an incinerato r

i n thi s documen t wi l impl y al l thre

e incinerato r

systems . Irrformatio n tha t i s onl y applicabl e t

o one o r tw o o f th e three unit s wil l b e clearl y identifie deithe r parentheticall y o r

delineate db y th

e sectio n heading . A s require db y § § 63.6(e)(v ) an d6"3.6(e)(vi) , thi s pla n an dothe r document s containin g procedure s o r

informatio n referre dt

o i n thi s pla n wil l b e made availabl e fo r inspectio n whe n requeste db y the Adininistrator . I f Ony x i s requhe 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 ) confidential busines s informatio n entitle dt o protectio n from disclosure wil l b e clearl y designated . Th e remainde

r o f thi s sectio n provide s a n overvie w o f regulator

y requhement s andaprogra mfo r complianc e wit h th 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

th e incinerato r

system . Sectio n 4. 0 addresse s potential 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 t o estabhs h aprogra mtha t wil l ensur

e comphanc e wit h relevant

section s o f

th e Interi mMAC T Standards . Tabl e 1- 1 include s th e regulator

y reqmrement s an dth

e locatio n o f

eac h requirement

addressed herein . 1. 2 Recordkeepin g an dReportin g Procedure s Thi s sectio n addresse s th e recordkeepin g an dreportin g requhement s relate dt o period s o f SSM . Th e startup , shutdown , an dmalfunctio n report s discusse di n thi s plan ensur e tha t Ony x i s satisfyin g th

e genera l dut y to mmimiz e emission s an ddocumen t tha t action s taken durin g thos e period s ar

e consisten

t wit h thi s plan . Thes e report s an drecord s provid e th e necessar

y documentatio n to shiel dtransien t event s fromth

e HW C MAC T emissio n standard s impose do n steady-stat

e operations . A s lon g as action s taken durin g atransient even t sufficientl y maintai n th e incinerato r

syste m withi n limits , ther

e i s no justificatio n i n distmguishin g tha t even t fromsteady-stat

e operations . Fo r example , problem s ma

y aris e tha

t mee t th e definitio n o f

amalfunctio n yet

do not impac t th e abilit y t o maintai n th

e incinerato r

syste mwithi n limits . I n thes e cases , mamtaimn g th e incinerato r

syste mwithi n hmit s substantiate s tha t th e action s take n sufficientl y me t the objective s o f

thi s SSM P andminimize demission s t o agreate

r degree tha

n require db y regulations .Tabl e 1- 1 Overvie w o f

Regulation s Regardin g Startup , Shutdow n an d Malfunctio n Regulator y Citatio n Descriptio n SSM P Sectio n S 63.6(e)(3)(i

) Purpos e ofth e SSM P 1. 0 § 63.6(e)(3Xi

) • Procedure s fo roperatin

g an d maintainin

g th e sourc e durin g startu p 3.1 , Table 3-

1 § 63.6(e)(3)(i

) Procedure s foroperatin

g an d maintainin

g th e sourc e durin g shutdow n 3.2 , Table 3- 1 §63.6(e)(3)(i ) Procedure s fo roperatin

g an d maintainin

g th e sourc e durin g malfunctio

n Attachmen t4 § 63.6(e)(3)(i

) A progra m o f correctiv e actio n fo rmalfunctionin

g proces s Attachmen t4 § 63.6(e)(3)(ii

) Durin

g SSM , operat

e an d maintai

n sourc e i n accordanc

e wit h SSMP 1.

0 § 63.6(e)(3)(iii

) Record s an d report s whe n action s confor m wit h SSM P 1.2.1 §63.6(e)(3)(iv ) Record s an d report s whe n action s d o no tconfor m wit h SSM P an

d resul tin a n exceedanc

e 1.2. 2 §63.6(e)(3)(v

) Availabilit y o f curren tan d supersede

d SSMPs ' 1. 2 § 63.6(e)(3)(vi

) Us

e an d availabilit

y o f othe r plan s 1. 0 § 63.6(e)(3Xviii

) Revision

s t o .th e SSM P 1.2. 2 § 63.10(b)(1) Maintainin g file s 1. 2 § 63.10(b)(2)(i

) Recor

d occurrenc

e an d duratio n o f eac h startu p an d shutdow

n 1.2. 1 §63.10(b)(2)(ii

) Recor

d occurrenc

e an d duratio n o f eac h malfimctio

n 1.2. 1 § 63.10(b)(2)(iv

) Record

s o f action s inconsisten

twit h SSMP . 1-2. 1 § 63.10(b)(2)(v

) •Record

s demonstratin

g conformanc

e wit h SSM P 1.2. 1 §63.10(b)(2)(vi

) Recor

d period s o f malfunctionin

g CM S 1.2. 1 § 63.10(d)(5)(i

) Periodi

c startup , shutdown

, an d malfunctio

n report s 1.2. 2 § 63.10(d)(5)(ii

) Immediat e startup , shutdown

, an d malfunctio

n report s 1.2. 2 § 63.1206(c)(2)(ii)(A

) Descriptio

n o f potentia l cause s o f malfunction

s Table 4-1 , Attachmen

t4 § 63.1206(c)(2)(xi)(A

) Action

s t o minimiz

e th e frequenc

y an d severit y o f malfunction

s 4.1,4. 2

Table 4- 2 Attachmen

t4 § 63.1206(c)(2)(ii)(C

) Change

s t o th e pla n 1.2. 2 § 63.1206(c)(2)(iii

) Projecte

d oxyge n correctio

n factor t o us e durin g startu p an d shutdow n 3. 0 § 63.1206(cX2)(iv

) Recor

d pla 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 d evaluatio

n o f excessiv e exceedance

s durin g malfunction

s .

. . 1.2. 2 §63.1206(c)(2)(v)(AX3X 0 Revision

s t o SSM P du

e t o excessiv

e exceedance

s durin g malfunction

s 1.2. 2 §63.1206(c)(2)(v)(A)(3)(ii ) Recor d result s from investigatio

n an d evaluatio

n o f excessiv e exceedance

s 1.2. 2 § 63.12006(c)(2)(v)A(3Xii ) Addition

s t o exces s emission

s repor t[ § 63.l0(eX3) ] du

e t o excessiv e exceedance

s durin g malfunction

s 1.2. 2 §63.1206(c)(2)(v

)(BX D Wast

e fee d restriction

s an d othe r OPL s durin

g startu p an d shutdow

n 3.

0 § 63.1206(c)(2)(v)(BX2 ) Interloc

k OPL s o

f (c)(2)(vXB)(l ) wit

h AWFC O syste

m 3. 0 §63.1206(c)(2)(v)(BX3 ) AWFC O du e t o exceedanc

e o f startup/shutdow

n OP L 3. 0

3

V E S 00193 2Accordingly , 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 h ther

e i s areasonabl e expectatio n tha t a n OP L o r emissio n standar

dca n no t b e met . Thi s include s al l startup s fro mcol dconditions , al l shutdown s to col dconditions , an dmalfunction s tha t resul t i n a n exceedanc e o f

a n operatin g limi t

or emissio n standard . Malfunction s tha t prevent th e abilit y t o documen

t on-goin g complianc e ar

e als o subjec t

to recordkeepin g an dreportin g requhements . Thi s plan , al l revision s to 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 five years . 1.2.1 Records SS M record s wil l includ e th e following :

• Dat e an dtim e o f

each SS M

• The duratio n o f

eac h SS M

• Documentatio n to demonstrat e tha t action s take n durin g period s o f SS M ar e consisten t wit h thi s SSM P

• Descriptio n o f

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

t ar e no t consistent wit h procedure 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 blank recordkeepin g form s fo r startups , shutdowns , an d malfunctions , respectively . Th e infonnatio n recorde do n thes e form s wil l b e utilize dt o documen t conformanc e wit h the SSM P an dt o compl y wit h th e reportin g requirements . Th e startup , shutdown , an dnialfunctio n reportin g requirement s ar e describe di n th e nex t section . 1.2.2 Reports Revision s t

o thi s SSM P ma

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 dt

o mee t th e regulator

y requirements . An y suc h revision s mad e durin g asemiannua

l reportin g perio dwil l b e submitte dwit h th e periodi c SS M report . Revision s t

o thi s plan—whic h alter th e scop e o f

activitie s durin g astartup , shutdown , o r

malfunction—wil l not

tak e effec t unti l awritte n notice , describin g the revisions , i s submitte dt

o th e penmttin 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 approval b y th e Administrator . A writte n reques t fo r approva l o f th e change s an dthe revise dSSM P wil l b e submitte dt o theAdministrato r withi n 5 day s afte r

makin g suc h achang e t o thi s plan . Shoul dan SS M even t occu r tha t i s no t addressed ' o r

inadequately addressedi n thi s SSMP , Ony x wil l mak e th e appropriat

e revision s t

o thi s pla n withi n 4 5 day s afte r the even t A n investigatio n andevaluatio n wil l b e performe do n eac h se t o f 1 0 exceedance s o f

a specifi c emissio n standar do r aspecifi c operatin g paramete r limi t tha t occur durin g malfunction s withi n a6 0 da y period . Withi n 4 5 day s o f th e 10 t hexceedance , th e investigatio n wil l determine plausibl e cause s fo r eac h excessiv e exceedance . Th e evaluatio n wil l conclud e ho w t o minimiz e th

e frequency , duration , an dseverity 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 asummar

y o f eac h investigatio n an devaluatio n requhe ddurin g th e semiannual reportin g period . I n addition , th e excessiv e emission s repor t wil l includ e any change s to thi s plan 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 dt o 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 tak e th e for mo f

aletter to the Adniinistrato 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 consistent

wit h the procedure s give n i n thi s SSM P

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

eac h malfunctio n

• Th e name , title , an dsignatur e o f the owner/operator

(o r othe r responsibl e official ) certifyin g th

e accurac y o f

th e repor

t A n immediat

e SS M repor

t wil l b e submitte di f

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

consisten

t wit h thi s plan ; an da

n OP L o r

emissio n standar

di s exceeded . Withi n tw o workin g day s afte r suc h an action , th

e Administrato r

wil l b e advise dvi a telephone or

fax . Within . 7 workin g day s after suc h an action , alette r t o th e Administrato r

wil l b e delivere do r

postmarked . Th e letter

wil l explai n the event , reason s fo r not followin g thi s plan , an ddescription s ofth e exces s emission s and/or operatin g paramete r monitorin g exceedance s believe dt o hav e occurred . Th e letter wil l als o includ e th e name , title, an dsignatur e o f th e owner/operator

(o r othe r responsibl e official ) certifyin g th

e accurac y o f

th e report .

5

V E S 00193 42. 0 ENGINEERIN G DESCRIPTIO N Brie f description s o f

th e fixedheart

h incinerator s andth e rotar y kil n incinerato r

ar e presented i n thi s section . A detaile dengineerin g descriptio n o f the 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 the Uni t 4 incinerator s i s provide db y Technical Description, Transportable Rotary Kiln Incinerator Unit No. 4. Drawin g numbers PFD-2000 , PFD-3000 , PFD-400 0 ar e the proces s flo w diagram s fo r thes e incinerators . Thes e document s an ddrawing s ar e incorporate dher

e b y reference . 2. 1 Fixe dHeart h Incinerator s Eac h o f th e fixedheart

h incinerator s include s th e followin g components :

• Fee dequipmen

t • Primary an

dsecondar

y combustio n chamber s • Lim e injectio n system • Spra y drye r absorbe r (SDA )

• Fabri c filte r

baghous e . • Solid s andas h remova l system s • Induce ddraf

t (ID ) fa n an dstac k

• Instrumentation , controls , an ddataacquisitio n system s Figur e 2- 1 presents abloc k flow diagramo f

the Uni t 2 incinerato r

system . Th e bloc k flow diagra

mfo r Uni t 3 i s presente d i n Figur e 2-2 . A variet y o f solid , liquid , an dgaseou s waste s ar e thermall y treate d i n th e fixedheart h incinerators . Soh dwast e i s fe dto th e primary (lower) combustio n chambe r vi aafee d conveyo r systeman dpneumati c ram . Liqui dwast e fro mtank s an dtanker

truck s ar e fe d to the primary combustio n chambe r throug h tw o atomize dliqui dinjectors . Bot h Unit s 2 and3 ar

e equippe dwit h aspecialt y wast e fee dsystems . Th e Uni t 2 primar y wast e fromliqui dcontainer s an dga s cylinder s ar e fe dt o th e Uni t

2 primar y combustio n chambe r throug h aspecialt

y fee dport . Wast

e fromhqui dcontainer s i s fe dfrom a hoode dfee dsyste

mt o th e Uni t 3 primar y combustio n chambe r throug h aspecialt

y fee d injector . Of f

gase s fromth e hoode dfee demissio n contro l systemar e fe ddhectl y t oTAN KFARM ^ DIREC T INJECT . IIII I I I I I I COMBUSTIO N M R BLOW S

TAN KFAR M R L O W B T U DIREC T INJEC T T UOAIIS S \ f m

UOU O CONTAINERS ^ GASCYLMER S SPECIALT Y • •FEEDE R

\ PRIMAR Y V INCINERATO R UPPE R CHAMBE R

WE TAS H . DUMPSTE R U M E PREPARATIO N SYSTE M

SPRA Y O R Y ABSORBE R STUKS K

BAGHOUS E 1.0 . FA N

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

FUELSAiOU O WAST E FLO W » - COMBUSTKJ N AI Rno w » STAC K

OA S FLO W AS H FLO W IOOOO» > SOU O WAST E FLO W

' > - LIM E 3UHM T FLO W

Figur e 2- 1 Fixe dHeart h Incinerator , Uni t 2 , Bloc k Flo w Diagra m

< m w 

### o o CO COI I I I I IIII I TTTT T COMBUSTIO N Ali i • BLOWE R

TAN K FAR M ( LO W

BT U Liang s DIREC T INJEC T , LO W

BT U Liang s LO W BT U Liang s K I T / SE C INCINERATO R LOWER CHAMBE R

SPECIALT Y FEEDE R FUM EHOO D EMISSIO NCONTRO L SYSTE M \ PWMAR F \ _ INCINERATO R UPPE R CHAMBE R I f f

w r AS H OUMPSTE R UM E PREPARATIO N SYSTE M

SPRA Y DR Y ABSORBE R

IDRY SCRUBBE R SOUD S ( DS S j i EN D DUM PI BAGHOUS E 1.0 . FA N

DR Y SCRUBBE R SOUD S ( DS S ) l E N 0 DUM P

GLOV EBO X EMISSIO NCONTROL ) SYSTE M FUELS/UOUH J WASr E FLO W

——-F - COMBUSTIO N AI RFLO W » STAC K

OA S FLO W aXCCO

- AS M FLO W ,0000» > SOU O WAST E no w

UM E SLURR Y FLO W

Figur e 2- 2 Fixe dHeart h Incinerator , Uni t 3 , Bloc k Flo w Diagra m

< m co 

### o o CO COth e Uni t 3 secondar

y combustio n chamber . Of f gase s from awast

e handlin g glov e bo x ar e als o fe ddirectl y t

o the Uni t

3 secondar

y combustio n chamber . Th e primar

y combustio n chambe

r mai n burner

an dthe secondar

y combustio n chambe

r mai n burne

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

r andente

r int o th e secondar

y combustio n chamber , whic h serve s a s a n afterburner . Combustio n gase s exi t th e secondar

y combustio n chambe

r an d ente r th e SDA . Th e secondar

y combustio n chamber

i s equippe dwit h a

n emergenc y stack . Lim e slurr y an dwate

r ar e fe dt o th e SD A atomizer . Th e atomize r ha s arapidl y spiimin g whee l tha t atomize s th e lim e slurry an dwate r int o aclou do f

fin e droplets . Combustio n gase s ar e directe dupwardthroug h adisperser i n the SD A an dint o th e clou do f

fin e droplet create db y th e atomizer . Thi s provide s aci dga s removal an dcoolin g o f th e combustio n gas . Drie dspen t chemical s an das h settl e to th e botto mo f th e SD A andar

e discharge dt

o th e as h remova l system . Combustio n ga s exit s the SD A andi s distribute dto the 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 filter modules . Combustio n ga s passe s throug h Teflon-coate dfiberglass clot h bags . Particle s i n th e combustio n gase s ar

e deposite do n th e outside o f eac h ba g i n th e filte r

module . Durin g the ba g cleanin g cycle , aburs t o f a h i n th e dhectio n opposite to th e gas flo w dislodge s particulate matte r from th e bag . Th e induce ddraf

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

baghouse . Th e induce d draf t fa n move s th

e combustio n ga

s throug h the syste man dexhaust s the ga s throug h th e mai n stack . Hot , wet ga s i s extracte ddownstrea mofth e baghous e throug h acontinuou s emission s momtorin g system . Thi s systemfeature s amulti-componen t infrare dgas analyzer

tha t detects hydroge n chloride , carbo n monoxide , an dwater vapo r concentrations . A n integrate dzhconiu moxide-base danalyze r detect s oxygei i concentrations . 2. 2 Rotar y Kil n Incinerato r Th e rotar y kil n incinerato r

include s th e followin g components :

• Wast e fee dsystem• Primary an dsecondar

y combustio n chamber s • Temperin g chambe

r • Lim e injectio n syste m • Spra y dryer absorbe r • Carbo n injectio n syste m • Fabri c filte r

baghous e • Solid s an das h remova l system s • Induce ddraf

t (ID ) fa n an dstac k

• Mstrumentation , controls , an ddataacquisitio n system s Figur e 2- 3 present s abloc k flo w diagra

mofth e Uni t

4 incinerato r

system . A variet y o f soli dan dliqui dwaste s ar e thermall y treate d i n th e rotar y kil n incinerator . Soli dwaste s ar

e fe dt o aramfeeder

vi aaclamshell , adru mfee dconveyo r an da n auxiliar y fee dconveyor . A hydrauli c rampushe s the soh dwast e int o th e kiln . Liqui d wast e fromtanks an dtanke r truck s i s fe dt

o the primary andsecondar y combustion . chambers through atomize dliqui dinjectors . Th e primar

y combustio n chambe

r mai n burner

an dthe secondar

y combustio n chambe

r mai n burne

r ar e use dt o maintai n temperature s p n natura l gas . Combustio n gase s exi t th e primary combustio n chambe r an dente

r int o th e secondar

y combustio n chamber , whic h serve s a s a n afterburner . A surg e ven t i s locate da

t th e front ofth e kil n an dthe secondar y combustio n chambe

r i s equippe dwit h athermal relie f vent . Combustio n gase s exi t

the secondar

y combustio n chambe

r an dente

r th e temperin g chamber . Proces s water

i s fe dt o temperin g chambe

r throug h a h atomize dspra y nozzles . Combustio n ga

s i s coole da

s i t passe s throug h the spra y o f water . Th e water

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

r an di s distribute dbetween tw o identica l SDAs . Lim e slurry i s fe dt

o eac h SD A throug h a h atomize dspra y nozzles . Combustio n gase s ar e directe ddownwar

dthroug h aduc t

i n th e SD A an

dthe n disperse dsymmetricall y int o the clou do f

atomize dlime . Thi s provide s aci dga s remova l an dcoolin g o f th e combustio n gas . Drie dspen t chemical s an das h settl e t o th e botto mo f

the SD A an dar

e discharge dt

o th e as h remova l system .

1 0TAN K FARM ^ DIREC T INJECT ,

SOUO S MAI N ' AUX . BUL K

TAN K FAR M > LO W

BT U ' DIREC T INJEC T f LIQUID S

\PRIMAR Y \ _

Figur e 2- 3 Rotar y Kil n Incinerator , Uni t 4 , Bloc k Flo w Diagra m



### < r n co 

### o o 1 1 C D O R r SCRUBBE R [SOUD S ( DS S ) | EN D DUM P 

# a

CARBO N INJECTIO N SYSTE M

OR r SCRUBBE R [SCUD S { OS S ) j EN D DUM P FUELS/LIQUI D WAST E FLO W COMBUSTIO N A RFLO W STAC K CA S FLO W AI H no w rOOOO* " SOU D WAST E FLO W

UM C SLUflR Y FLO WA carbo n injectio n syste mi s utilize dfo r controllin g dioxin/fura n andmercur y emissions . Th e activate dcarbo n i s ai r injecte dint o th e combustio n gas immediatel y downstrea mo f th e convergenc e o f

combustio n gase s fromth e SDAs . Combustio n gase s exi t

the SDA s an dar

e distribute dt o tw o fabri c filte r modules . Eac h modul e ha

s thre e compartments , i n paralle l contentin g multipl e fabri c bags . Combustio n ga s passe s throug h th

e fabri c bags . Particle s i n the combustio n gase s ar e deposite do n th e outside o f

each bag . Durin g th

e ba g cleanin g cycle , aburs t o f ai r i n m e dhectio n opposit e t o th e gas flo w dislodge s particulat e matte r fromth e bag . Th e induce ddraf

t fa n i s locate ddownstrea mofth e fabri c filte r

baghouse . Th e induce d draf t fa n move s th

e combustio n gas throug h th e syste man dexhaust s the ga s throug h th e mai n stack . Hot , we t ga s i s extracte ddownstrea mo f th e I D fa n throug h acontinuou s emission s monitorin g system . Thi s syste mfeature s amulti-component irifrare dga s analyzer

tha t detects hydrogen chloride , carbo n monoxide , an dwater vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detects oxyge n concentrations .

1 23. 0 STARTU P AN D SHUTDOW N PROCEDURE S Th e purpos e o f

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

p an dshutdow n ofth e incinerato r

system . Thi s sectio n als o clarifie s whic h action s ar e withi n th

e scop e o f

th e regulator y definitio n o f

startu p an dshutdown . T o satisf y the requhement s o f

§ 63.1206(c)(2)(v)(B) , wast e fee drestrictio n an doperating , limit s hav e bee n impose dto startup s an dshutdowns . Durin g astartup , th e feedin g o f hazardou s wast

e t o the incinerato r

wil l no t b e initiate dunti l al l operatin g parameters ar e withi n limits : Hazardou s wast e wil l no t b e fe ddurin g ashutdow n even t Consistent

wit h the requirement s o f § ' 63.1206(c)(2)(iii) , Ony x wil l utiliz e a n oxyge n correctio n facto r

o f 2 (i.e. , 14 % 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 ca n occur durin g stotu p an d shutdow n due t

o change s i n the oxyge n concentration . Th e oxyge n correctio n facto r o f 2 i s basedo n th e highes t

oxyge n correctio n facto r observe ddurin g norma l operation s ofth e incinerators . Thi s "default " oxyge n correctio n facto r can onl y b e utilize dwhe n th e wast e residenc e tim e i n the primary combustio n chamber has expired . Ony x has develope dstandar ddivisio n practice s (SDPs ) fo r th e operatio n o f

eac h incinerato r

syste man dancillar y equipment an dsystems . Th e SDP s containin g startu p 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 Startu p A l l startup s ar

e precede db y ashutdow n i n whic h th e primar y combustio n chambe

r wa s allowe dto cool . Dependin g o n th e purpos e o f

th e precedin g shutdown , portion s ofth e a h pollutio n contro l systemma y b e i n servic e upo n commencin g astartup . Thi s wil l b e reflecte do n th e startu

p record(see Attachment s 1) . Durin g astartup , wast e 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 d onc e wast e i s introduce dan dal l operatin g parameter s ar e withi n limits . Onyx' s startu

p procedure s ar

e representativ e o f

safet y an dgoo da h pollutio n contro l practices . Th e procedure s ar e designe dt o minimiz e the potentia l fo r exces s emission s b y ensurin g tha

t al l equipmen

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

to th e introductio n o f

hazardou s wast

e t o th e system . Adherenc e t o thes e startu

p procedure s 1 3wil l emplo y the knowledg e aa dskill s demonstrate d throug h th e implementatio n o f

th e Operato r Trainin g an dCertificatio n Program .

1 43. 2 Norma l Shutdow n A l l shutdown s wil l allo w th e primary combustio n chambe r t o cool . Prio r

to ever y shutdown , th e incinerato r wil l b e burnin g auxiliar y fue l onl y an dth e hazardou s wast

e residenc e time wil l hav e transpired . A shutdow n wil l b e initiate dwit h th e shutof f o f auxiliar y fue l t

o th e incinerator . Portion s ofth e a h 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 h the subsequen t startup . Onyx' s shutdow n procedure s ar e representativ e o f

safety andgoo da h pollutio n contro l practice . Th e procedure s ar e designe dt

o minimiz e the potential fo r exces s emission s b y ensurin g tha

t th e hazardou s wast

e residenc e tim e has transphe dprio r t o th e shutdow n o f the incinerato r

system . Adherenc e t o thes e shutdow n procedure s wil l emplo y th e knowledg e an dskill s demonstratedthroug h th e implementatio n o f

th e Operator

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

1 54. 0 MALFUNCTION S Th e purpos e o f

thi s sectio n ofth e Startup , Shutdow n an dMalfunctio n Pla n i s to :

• Defin e potential malfunction s an dthei r cause s • • Describ e measure s t o ndriimiz e the 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 to correc t the caus e o f

amalfunctio n A summar

y o f potential malfunction s an dthe h cause s i s give n i n Tabl e 4-1 . Thi s lis t o f potential malfunction s i s arrange daccordin g t o uni t operations . Th e occurrenc e o f any even t hste di n Tabl e 4- 1 shoul db e responde dto as amalfunctio n an damalfunctio n recordkeepin g form , include da s Attachmen t

3 , shoul db e initiated . Durin g th e respons e to thes e events , i t

wil l b e detenriine di f

th e even t meets th e regulator

y definitio n o f

a malfunction . 4. 1 Measure s to Minimiz e the Frequenc y o f Malfunction s Th e followin g measure s contribut e to preven

t malrunctions :

• Incinerator

systemdesig n consistent wit h safet

y an dgoo dengmeerin g practice s • Hazard s an

doperability studie s o f

th e incinerator s • Appropriate frequency o f preventativ e mamtenanc e an dinspectio n • Goo doperatin g practice s • Wel l traine dan dqualifie dpersonne l Onyx' s performanc e history , thi s document , an dthe followin g regulator y document s serv e a s evidenc e o f

Onyx' s proactiv e measure s t o rninLimiz e th e frequency o f malrunctions . .

• 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 an d Cause s Potentia l Malfunction s fo r Unit s 2,3 , and 4 Potentia l Cause s fo r a Malfunctio n GENERA L

- Los s o f

Electrica

l Powe r Suppl y

- Loss o f

Instrument/Plan

tAi r Supply.

- Los s o f

Plan tNitroge n Suppl y

- Los s o f

City Wate

r Suppl y

- Los s o f

Proces s Wate r Pressure/Flo

w (Unit4

)

- Malfunctio n of

Safet y Interloc

k o r Automati

c Wast e Fee d ' Cutofflnterloc k PRIMAR Y COMBUSTIO N CHAMBE R

- Loss o f

Natura l Ga s Pressure/Flo

w t o PC C Mai n Burne

r

- Loss o f

Combustio

n Ai r Pressure/Flo

w t o PC C

- PC C Mai n Burne

r PilotFailur

e

- Loss o f

Wast e Flow t o PC C Injecto

r

- Los s o f

Wast e Feedrat

e Control t

o PC C Injecto

r

- Los s o f

Atomization Ai r Pressur e t o a PO C Injecto

r

- Los s o f

PC C Draf

tContro l (Unit4 )

- Los s o f

PC C Temperatur

e Control

- Flam e Failur e

- Kil n Rotatio

n Malfunction (Unit4

)

- Bulk/Charge Feed Door - Malfunctio n

- Physical/Mechanica

l Interna l Equipmen

tFailur e

- PC C Sea

l Visua l Emission

s Monitoring an

d Recording Syste

m SECONDAR Y COMBUSTIO N CHAMBE R

- Los s o f

Natura l Ga s Pressure/Flo

w t o SC C Mai n Burne

r

- Los s o f

Combustio

n Ai r Pressure/Flo

w t o SC C

- SC C Mai n Burne

r Ignitio n Failur e

- Loss o f

Wast e Flo w t o SC C Injecto

r

- Los s o f

Wast e Feedrat

e Control t

o SC C Injecto

r

- Los s o f

Atomization Ai r Pressur e t o a SC C Injecto

r

- Los s o f

SC C Temperatur

e Control

- Flam e Failur e

- Emergenc

y Safet y VentOpenin

g

- Physical/Mechanica l Interna l Equipmen

tFailur e

- Lo w Wate

r Leve l i n Sla

g Collectio n Syste

m (Unit4

) TEMPERIN G CHAMBE R(UNI T 4 )

- Loss o f

Temperin

g Chambe

r Exi tGa

s Temperatur

e Contro l

- Los s o f

Atomizatio

n Ai r Pressur

e t o Nozzle LIM E SLURR Y SYSTE M .

- Los s o f

Lim e Fee

d t o Lim e Slurr

y Fee d Tan k

- Malfunctio n i n Lime 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 t o SD A

- . Loss of

Lim e Slurr

y Flo w Contro

l

- Loss o f

Cit y Wate r Flo w t o SD A

- Los s o f Coolin g Ai r Flo w t

o Atomize

r

- Loss of

SD A Exi tGa

s Temperatur

e Contro l

- Atomize

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

- Loss o f

Lime Slurr

y Flo w t o SD A

- Los s o f

Lim e Slurr

y Flo w Control/ExitGa s Temperatur

e Contro l

- Loss of

Atomizatio

n Ai r Pressur

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

- Loss o f

Carrie r Ga s Pressur e

- Loss/Restrictio

n of Activate d Carbo n Flo w

- Loss o f

Plan tAi r Pressure/Fl

o w t o Carbo n Bul k Sac

k BAGHOUS E & INDUCE D DRAF T (ID) FA N

- . Torn/Leaking Ba g

- Bag Blinding/High-High Pressur e Dro p

- Los s o f

Stac k Ga s Flowrat e Contro l (Uni t2 an d 3 )

- Baghous

e Isolatio n Dampe r Malfunction (Uni

t4 )

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

- Contro

l System/Continuou

s Monitorin

g Syste m Malfunction

- Continuou

s Emission

s Monitorin

g Syste m Malfunction 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 of 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

tfailur e

1 7Despite thes e efforts , equipmen t failure s an dothe

r operatin g anomalie s ca n occur . Withi n th

e scop e o f

regulator

y requirements , the operatin g recordwil l contai n the appropriat

e documentatio n t o establis h tha t poo r maintenanc e o r

careles s operation s ar

e no t contributin g factor s t

o th e caus e o f

amalfunction . 4. 2 Measure s t o Minimiz e the Severit y o f Malfunction s Th e followin g measure s contribute t o mimmiz e m

e severit y o f malt o

• 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

the incinerato r

syste m Typically , a

n even t tha t meet s the definitio n o f

amalfunctio n wil l trigger a n alarm . A n alarminform s th

e operator

o f th e situatio n an dmay provid e a n opportunit

y t o avoi dan exceedance . I f

condition s become unsaf e o r excee doperatin g hmits , interlock s ar e i n plac e fo r a n automatedrespons e tha t i s specifi c t

o th e triggerin g condition . Refe r t o Onyx' 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 mamtaine do n pipin g an diristrumentatio n diagram s (P&IDs ) Th e mos t critica l ke y t

o nrinimizin g th

e severit y o f malfunction s i s th e functionalit y o f AWFC O interlocks . Accordingly , Ony x perform s testin g o f the AWFC O system , a s describe di n fhe AWFCO Plan. Thi s testin g confirm s astat e o f readines s t o respon dto a malfunctio n i n amanne

r tha t wil l mimmiz e the releas e o f hazardou s ai r

pollutants . Throug h trainin g an djo b experience , the operator wil l hav e th

e proces s knowledg e tha t qualifie s hi mto us e discretio n i n respondin g t o malfunctions . Du e to the unusua l an d dynami c condition s tha

t ar e presen t durin g amalfunction , operator discretio n i s essentia

l to minimizin g the severit y o f malfunctions. A n operator ca n evaluat

e proces s condition s an dalarm s an dchoos e th e bes t respons e t

o avoi dan exceedance , i f possible . I f

th e nxalfunctio 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 th

e situatio n an drespon dappropriately . I n th e even t tha t th e malfunctio n affect s th

e abilit y to automaticall y cutof f waste , th

e operator

wil l manuall y cutof f wast e feed s a s quickl y a

s possible .

1 8Th e desig n o f the each incinerato r

syste mals o ensure s tha t the severit

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

actuated valves , andredundan

t instrumentatio n andproces s equipment . Also , the desig n o f eac h incinerator' s instrumentatio n an dcontrp l system s provide s th e operator convenient

acces s to proces s variabl e indication , mcludin g positio n indicatio n o f selecte dactuatedvalves . Thi s i s essentia

l t o providin g th e operato r th e informatio n require dto bes t evaluat e systemcondition s andresponses . Tabl e 4- 2 hst s potentia l malfunction s andassociate d redundan t equipmen

t an dsystem s tha

t ar e availabl e t

o prevent thes e malfunction s o r

t p minimiz e th

e potential fo r

asignifican t

releas e o f

hazardou s a h pollutants . 4. 3 Correctiv e Measure s Th e Program of

Corrective Actions for

Malfunctions i s Attachment 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 hste d fo r

eac h portio n o f

the incinerato r

system . Th e malfunction s ar e events tha

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

alarms , the operator

wil l appl y discretio n an dattemp t t o maintai n the incinerato r

syste mwiflii n regulatory limits . I n th e programo f

correctiv e actions , potential cause s o f

eac h malfunctio n ar

e listed ; Th e operator wil l utiliz e proces s knowledge , jo b experience , and , i f needed , assistanc e fro mothe r personne l t o identif

y th e caus e o f th e malfunction . Fo r

eac h potential cause , action s t o correc t th e failur e ar

e listed . Th e correctiv e action s prescribe dma y require th

e collaboratio n o f

multi

discipline dpersonne l wh o ar e quahfie dto retur

n th e incinerato r

syste mto proper

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

1 9Tabl e 4- 2 Redundan t

Equipmen t

an dSystem s fo r Minimizin g th e Frequenc y o r Severit y o f

Malfunction s Redundan t

Equipment/System s 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 , andcontro 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 nmning.an don e compresso r o n ho t standb y (Uni t

2 an d3) . Los s o f Instrument/Plant

Ai r Suppl y Dua l Proces s Wate

r Pump s Los s o f Proces s Water

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 t

o 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 t

o SC C Multipl e Temperin g Chambe r Nozzle s Los s o f Temperin g Chamber

Exi t Ga s Temperatur

e Contro l Los s o f Atomizatio n Ai r

Pressur e t o Nozzl e Dua l Slurry Fee dPump s (Uni t 4 ) Share dBack-u p Pum

p (Uni t 2 and3 ) Los s o f Slurr y Fee dt o SD A Off-lin e Spar

e 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 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 Off-lin e Spar

e Baghous e Modul e (Uni t 2 ) Torn/Leakin g Ba g Tw o baghous e module s wit h three compartment s each . 5 compartments provid e sufficien t particulate removal s o tha

t on e ofth e 6 compartment s can b e isolate da s aspare . (Uni t

4 ) TorrVLeakin g Ba g

2 0

### ATTACHMEN T 1

STARTU P RECORDKEEPIN G FOR MONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 1 o f 3 ) Tin s reportpertain

s t o a startu

p o f Uni t2/3/ 4 (circle one) . Th e startu p even toccurre d on : __ . - (Month/Day/Year, Hour s : Minutes) Th e tota l duratio n o f thi s startu p even twas : (Hours : Minutes ) Attache d t o thi s for m i s a checklis

ttha tsummarize

s th e approve

d startu p procedure

s reference

d i n Onyx' s Startup, Shutdown, and Malfunction Plan (SSMP) . The operationa l step s tha thav e bee n checke d documen

ttha t th e detaile d startu p procedure

s wer e followed . Wer e al l action

s associate

d wit h thi s startu p even ti n conformanc

e wit h th e SSMP ? Ye s /

No (circle.one) . I f no , describ

e th e inconsisten

taction s below .

WeretiereanyexceeclmcesofanoperaJiigpararnete r .hmt ? Ye s / N o (circle one) . I f

yes , pleas

e list/describe. I f an y action s wer e no tconsisten

twit h th e SSM P an

d a n operatin

g paramete

r limitwa

s exceeded

, a n immediat

e SS M repor

ti 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 )ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 2 o f 3)

Uni t2 an d 3 Incinerato r Startu p Checklis t Initials Verif y tha tpre-startu

p ha s bee n complete

d Chec k therma l relie f ven t(TRV ) Star tcombustio

n ai rfa n Star tPC C mai

n burne r an d temperatur

e ramp-u p Star tSC C mai

n burne r an d temperatur

e ramp-u p Chec k stac k ga s flow an

d SD A temperature

s contro l setting s Star tI D fan . Monitor SD A temperatur e whil e rampin g u p stac k ga s flowrat e Clos e TR V Star tlim e slurr y Establis h al l operatin

g parameter

s withi n limit s Operator' s Notes :

• • • ' -

Note : Certai

n airpollutio

n contro l an d ancillar

y equipmen

tma y b e operationa

l prior t o startu p (Date ) (Signatur

e of Shif tLeade r o rDesignee

)ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 3 of3 )

Uni t4 Incinerato r Startup Checklis t Initials Verif y tha tpre-startu

p ha s bee n complete

d Chec k therma l relief ven t(TRV ) Star tI D fa n an d se tkil n draf

t(star to f purg e cycle) Star tSC C combustio

n ai rfa n Star tth e kil n combustio

n ai r fa n (purg e cycl e complete

) Star tSC C mai

n burne r an d temperatur

e ramp-u p . . Star tPC C mai

n burne r an d temperatur

e ramp-u p Star tkil n rotatio

n before . 500 . ° F Star tth e kil n sea

l air Star tth e SC C conveyo

r Se tu p th e temperin

g chambe

r fo r operatio

n Se tu p lim e slurr y injectio n syste m Se tu p th e SDA s fo r operatio

n Se tu p th e as h collection syste

m Se tu p th e baghouse

s for operatio

n Slowly ramp-u

p th e temperin

g chambe

r exi ttemperatur

e Continu e PC C an

d SC C ternperature ramp-u p Se tu p th e ai r canno n Star tth e kil n sea

l conveyo

r Establis h al l operatin

g parameter

s withi n limit s Operator' s Notes :

Note : Certai

n ai rpollution contro

l an d ancillar

y equipmen

tma y b e operationa

l prio r to startup

. (Signatur e o f Shif tLeade r o r Designee

) (Date )

### ATTACHMEN T 2

SHUTDOW N RECORDKEEPIN G FOR MONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 1 o f 3 ) Thi s repor tpertam s t o a sbuMow

n o f Uni t2 7 3 /

4 (circl e one) . Th e shutdow

n even ttha toccurre d on : (Month/Day/Year , Hour s : Minutes

) Th e total duratio

n o f thi s shutdow

n even twas : (Hours : Minutes ) Attache d t o thi s for m is a checklis

ttha tsummarize

s th e approve

d shutdow

n procedure

s reference

d i n th e Onyx Startup, Shutdown, and Malfunction Plan (SSMP) . Th e operationa

l step s tha thav e bee n checke d , documen

ttha t th e detaile d shutdow

n procedure

s wer e followed . Wer e al l action

s associate

d wit h thi s shutdow

n even ti n conformanc

e wit h th e SSMP ? Ye s /

N o (circle one) . If no, describ

e th e inconsisten

taction s below .

Wer e ther e an y exceedance

s o f a n operatin

g paramete

r limit ? Ye s /

N o (circl

e one) . If

yes , pleas

e list/describe. I f an y action s wer e no tconsisten

twit h th e SSM P an

d a n operatin

g paramete

r limi twa s exceeded, ' a

n immediat

e ' SS M repor

ti s required.

Notes/Recommendations :

Th e following signatur

e certifie s th e accurac

y o f thi s record : (Name ) (Title) (Signature

) (Date )

V E S 00195 5ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 2 of3 )

Uni t2 and 3 Incinerato r Shutdow n Checklis t Initials Verif y tha tth e hazardou

s wast e residenc

e time ha s transpire

d Monitor CEM S outpu

tto verif y stabl e condition

s Ope n th e stac k ca p Sto p th e ID fa n Shu tof f wate r an d lim e slurr y flow to th

e atomize

r Remov e atomize

r an d positio n li d Operator' s Notes :

Note : Certai

n ai r pollutio

n contro

l an d ancillar

y equipmen

tma 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 tLeade r o rDesignee

) (Date )ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 3 o f 3 )

Uni t4 Incinerato r Shutdow n Checklis t Initial s Verif y tha tth e hazardou

s wast e residenc

e tim e ha s transpire

d Ven tth e ai rcannon

s Shu tof f th e kil n burne

r an d SC G burne

r Shu tof f th e kil n an d SC C combustio

n ai rfan s Reduc e th e temperin

g chambe

r outle ttemperatur

e t o 50 0 ° F Shutdow n SD A (a tappropriat

e temperatures) Shutdow n temperin

g chambe

r (a tappropriat

e temperatures

) Afte r PC C an

d SC C reac

h the . appropriat

e temperature

, shu tof f th e I D fa n Operator' s Notes :

Note : Certai

n ai r pollutio

n contro

l an d ancillar

y equipmen

tma y remai n operationa

l throughou

t shutdown

. Once th

e hazardou

s wast e residenc

e tim e ha s transpired

, operator' s discretio

n ca n b e applied . (Signatur e of Shif tLeade r o r Designee

) (Date )

### ATTACHMEN T 3

MALFUNCTIO N RECORDKEEPIN G FOR M

V E S 00195 8ONY X ENVIRONMENTA L SERVICES , INC . MALFUNCTIO N RECOR D

(Pag e 1 o f 1 ) Tm s repor

tpertain s t o a malfunctio

n of Uni t2/3/4 . (circle one) . Th e malfunctio

n even ttha toccurre d on : - (Month/Day/Year, Hours : Minutes) Th e tota l duratio n o f thi s malfunctio

n even twas : (Hours : Minutes) Th e Onyx Program of

Corrective Actions forMalfunctions mus tb e adhere d t o fo r th e operatin

g an d mamtainin

g o f th e incinerato

r syste m an d fo r correctin

g th e caus e o f tlie malfunctio n Describ e th e malfunction, th

e automate d and/o r operato r response

, th e potentia

l caus e o f th e malfunction, an

d th e correctiv

e action s taken :

Wer e al l action

s associate

d wit h thi s malfunctio

n even ti n conformanc

e wit h th e SSMP ? Ye s /

N o (circl e one) . If no , initiat e a n immediat

e startup , shutdown

, an d malfunctio

n repor t List/describ e th

e exceedance

s tha toccurre d (o rbelieve d t o hav e occurred

) du e t o thi s malfunction :

Notes/Recommendations :

Th e followin g signatur e certifie s th e accuracy

, 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 d Maintainin

g th e Syste m durm g Malfunction

s 1. 2 Los s o f

Electrica

l Powe r Suppl y 1. 3 Los s o f

Instrument/Plan

tAi r Suppl

y 1. 4 Los s o f

Plan tNitroge n Suppl y 1. 5 Loss o f

Cit y Wate r Suppl y 1. 6 Los s o f

Proces s Wate r Pressure/Flo

w (Unit4

) 1. 7 Malfunction of

Safet y Interloc

k o r Automati

c Wast e Fee d Cutof

f Interloc k 2. 0 PRIMAR Y COMBUSTIO N CHAMBE R 2. 1 Los s o f

Natura l Ga s Pressure/Flo

w t o PC C Mai n Burne

r 2. 2 Los s o f

Combustio

n Ai r Pressure/Flo

w to PC C 2. 3 PC C Mai n Burne r Pilo tFailur

e 2. 4 Los s o f

Wast e Flo w t o PC C Injecto

r 2. 5 Los s o f

Wast e Feedrat

e Contro l t o PC C Injecto

r 2. 6 Los s o f

Atomizatio

n Ai r Pressur

e t o a PC C Injecto

r 2. 7 Los s ofPC C Draf tContro i (Unit4 ) 2. 8 Los s o f

PC C Temperatur

e Contro l 2. 9 Flam

e Failur e 2.10 Ki m Rotatio

n Malfunction (Unit4

) 2.1 1 Bulk/Charg

e Fee d Doo r Malfunction 2.1 2 Physical/Mechanica l Interna l Equipmen

tFailur e 2.1 3 PC C Sea

l Visual Emission

s Monitoring an

d Recordin

g Syste m 3. 0 SECONDAR Y COMBUSTIO N CHAMBE R 3. 1 Los s o f

Natura l Ga s Pressure/Flo

w t o SC C Mai n Burne

r 3. 2 Los s o f

Combustio

n Ai rPressure/Flo

w to SC C 3. 3 SC C Ma m Burne r Ignitio n Failur e 3. 4 Loss o f

Wast e Flo w t o SC C Injecto

r (Unit4 ) 3. 5 Loss ofWast

e Feedrat

e Control t

o SC C Injecto

r (Unit4 ) 3. 6 Los s o f

Atomizatio

n Ai r Pressur

e t o a SC C Injecto

r 3. 7 Los s o f

SC C Temperatur

e Control 3. 8 Flam

e Failur e 3. 9 Physical/Mechanica l Interna l Equipmen

tFailur e 3.10 Lo w Wate

r Level i n Sla

g Collectio n Syste

m (Uni t4 ) 3.1 1 Emergenc

y Safet y Ven tOpenin g 4. 0 TEMPERIN G CHAMBE R(UNI T 4 ) 4. 1 Loss o f

Temperin

g Chambe

r Exi tGa s Temperatur

e Control 4. 2 Los s o f

Atomizatio

n Ai rPressur

e t o Nozzl e 5. 0 LIM E SLURR Y SYSTE M 5.1 . Los s o f

Lim e Fee d to Lim e Slurr

y Fee d Tan

k 5.2 . Malfunction i n Lim e Slurr y Concentratio

n 6. 0 UNIT S 2 AN D 3 SPRA Y DRYE RABSORBE R(SDA ) 6.1 . Loss o f

Lim e Slurr y Flo w t o SD A 6.2 . Los

s o f Lim e Slurr y Flo w Control 6.3. Loss o f

Cit y Wate r Flo w to SD A (Unit2 an d 3 ) 6.4 . Los s o f

Cooling Ai rFlo w t

o Atomizer

V E S 00 16.5 . Los s o f SD A Exi tGa

s Temperatur

e Control

. 6.6 . Atomizer Failur

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

Lime Slurr

y Flo w t o SD A 7.2. Los s o f

Lim e Slurr

y Flo w Control/Exi tGa s Temperatur

e Contro l 7.3 . Loss o f

Atomizatio

n Ai rPressur

e t o SD A Nozzl e 8. 0 CARBO N INJECTIO N SYSTE M (UNI T 4 ) 8.1 . Loss o f

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

Plan tAi rPressure/Flo

w t o Carbo n Bul k Sac

k 9. 0 BAGHOUS E & INDUCE D DRAF T (ID) FA N 9.1 . Tom/Leaking Ba g . 9.2 . Bag Blmding/High-Hig h Pressur

e Dro p 9.3 . Loss o f

Stac k Ga s Flowrat

e Control (Unit2 an

d 3 ) 9.4 . Baghous

e Isolatio

n Dampe r Malfunctio n (Unit4

) 9.5 . I

D Fan Failur

e 10. 0 CONTRO L SYSTEM/CONTINUOU S MONITORIN G SYSTE M 10.1 . Contro

l System/Continuou

s Monitoring Syste

m Malfunction 10.2 . Continuou

s Emission

s Monitorin

g Syste m Malfunctio n

V E S 0019 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

GENERA L 1.1 . Operatin g an dMaintainin g th e Syste mdurin g Malfunction s 1.1.1 . Du e t

o th e sudden , infrequent , an dunusua l condition s associate d wit h malfunctions , continuall y evaluat e th e situation . Usin g discretion , respon di n amanne r consisten

t wit h safet

y an dgoo da h pollutio n contro l practices . 1.1.2 . Tak e fh e followin g action s t o minimiz e fh e releas e o f hazardou s a h pollutant s 1.1.2.1 . Cutof

f al l wast e feed s and/o r

confir mtha

t the automati c wast e fee dcutof

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

apphcable , follo w th e procedure s provide db y th e Emergency Safety Vent

Plan. 1.1.3 . Kee p superviso r and/o r maintenanc e superviso r informed , a s appropriate . 1.1.4 . Identif

y the malfunctio n an dpotentia l cause . 1.1.5 . Implemen

t correctiv e action s involvin g the troubleshootin g o f failure s an dth e servicin g and/or replacin g o f

components , a s needed . Refe r

t o manufacture' s troubleshootin g an dservic e recommendations , as needed . 1.1.6 . Recor dthe appropriate informatio n usin g amalfunctio n recor d form . 1.2 . Los s o f

Electrica l Powe r

Suppl y 1.2.1 . Verif y proper

failur e positio n o f

actuate dvalves . 1.2.2 . Identif

y lin k i n powe r suppl y pat

h tha t i s no t operational . 1.2.3 . Tak e th

e necessary " action s t

o restor e the suppl y o f

electrica l power. - 1.3 . Los s o f

Instrument/Plan t

Ai r Suppl y 1.3.1 . Verif y proper

failur e positio n o f

actuate dvalves .

. 1.3.2 . I h 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 instrument

a h 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 of2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O FCORRECTIV E ACTION S FO RMALFUNCTION S ; 1.3.3 . I n cas e o f

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

y caus e o f

actuatio n failure . 1.3.3.2 . Service/replac e electrica l and/or pneumati c components , as needed . 1.3.3.3 . Service/replac e 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 ofth e failure . 1.3.4.2 . Tak e the necessar y action s t

o restor e the suppl y o f instrument/plant

air . 1.4 . Los s o f

Plan t Nitroge n 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 . Clear

lin e plugging and/or

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 d valve : 1.4.2.1 . Identif

y caus e o f

actuatio n failure . 1.4.2.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 1.4.2.3 . Service/replac e actuator and/o r valv e components , a s 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 tli e caus e o f

th e failure . 1.4.3.2 . Tak e th e necessar y action s t

o restor e fh e suppl y o f nitrogen . 1.5 . Los s o f

Cit y Wate r

Supply ' 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 or

lin e failure . 1.5.1.2 . Clea r

lin e pluggin g and/or

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

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

y caus e o f

actuatio n failure .

. 1.5.2.2 . Service/replac e electrica l and/or pneumati c components , as needed . Pag e 2 o f 2 6

V E S 00196 4ONY X 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 , a

s needed . 1.5.3 . I n cas e o f

mechanical/electrica l failur e a t cit y water

suppl y source : 1.5.3.1 . Identif

y th e caus e o f

th e failure . 1.5.3.2 . Tak e the necessar y action s t o restor

e the suppl y o f

cit y water . 1.6 . Los s o f

Proces s Wate r

Pressure/Flo w (Uni t

4 ) 1.6.1 . Fo r

los s o f cit y water

suppl y t o proces s wate

r tank , se e 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 the pump/drive , a s needed . 1.6.2.3 . Restore electrica l powe r suppl y t o 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 or

lin e failure . 1.6.3.2 . Clea r

lin e pluggin g and/or

service/replac e fault y lin e components , as needed . 1.6.4 . Incas e o f

mechanical/electricalfailur e o f actuate d valve : 1.6.4.1 . Identif

y caus e o f

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

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

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

Safet y Interloc k

o r Automati c Wast e Fee d Cutof f Interloc k 1.7.1 . I f safety interloc k

o r AWFC O interloc k

wa s erroneousl y triggered , procee dwit h correctiv e actions . 1.7.2 . I f safety o r

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

f wast e fee d a s quickl y a s possible , the n procee d wit 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/replac e fault y instrumentatio n components , as

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

mecharucal/electrical 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/or pneumati c components , a

s needed . 1.7.4.3 . Service/replac e actuator and/or valv e components , a s 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 mcomponen t 1.7.5.2 . Service/replac e contro l syste mcomponents , a s needed .

Pag e 4 o f 2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

2. 0 PRIMAR Y COMBUSTIO N CHAMBE R 2.1 . Los s o f

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

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 , a s needed . 2.1.4 . I n cas e o f

mechanical/electrica l failur e a t natural gas suppl y source : 2.1.4.1 . Identif

y th e caus e o f

the failure . 2.1.4.2 . Tak e the necessar y action s t

o restor e th e suppl y o f natural gas . 2.2 . Los s o f

Combustio n Ai r

Pressure/Flo w t o PC C 2.2.1 . I n cas e o f

mechamcal/electrical failur e o f combustio n air-blower . 2.2.1.1 . Diagnos e blower/driv e failure . 2.2.1.2 . Service/replac e the blower/drive , a s needed . 2:2.1.3 . Restore electrica l powe r suppl y t o the blower . 2.2.2 . In cas e o f

physica l failur e o f

combustio n ai r

duct : 2.2.2.1 . Identif

y fh e locatio n o f

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

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

y caus e o f

actuatio n failure . 2.2.3.2 . Service/replac e electrica l and/or pneumati c 2.1.2 . 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

plugging o r

lin e failure . 2.1.1.2 . Clea r

lin e pluggin g and/or

service/replac e fault y lin e components , a

s needed . I n cas e o f

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

y caus e o f

actuatio n failure . 2.1.2.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 2.1.2.3 . Service/replac e actuato r and/or valv e components , a

s needed .

2.2.3.3 . components , as needed .

Service/replac e actuato

r and/or valv e components , as needed . Pag e 5 o f 2 6

V E S 00196 7ONY X 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 systemcomponent . 2.2.4.2 . Service/replac e contro l systemcomponents , a s needed. " 2.3 . PC C Mai n Burne r Pilo t Failur e 2.3.1 . Fo r

los s p f natura l ga s pressure/flow , se

e 2.1 . 2.3.2 . Fo r

los s o f combustio n ai r

pressure/flow , se

e 2.2 . 2.3.3 . In 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/or 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 systemcomponen t 2.3.4.2 . Service/replac e contro l systemcomponents , a s needed . 2.4 . Los s o f

Wast e Flo w 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 , a

s needed . 2.4.1.3 . Restor

e electrica l power

suppl y t o 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 . Clear

lin e pluggin g and/o

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

apphcable . 2A4 . I n cas e o f

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

y caus e o f

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

physical/electrica l failur e o f conho 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 , a s needed . 2.5 . Los s p f

Wast e Feedrat e Contro l to PC C Injecto r 2.5.1 . I n cas e o f

los s o f wast e pressure/flo w to PC C injector , se e 2.4 . Pag e 6 o f 2 6ONY X 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 tr^smitte r and/o r associate dmsmrmentation , a s needed . 2.5.3 . I n cas e o f

actuate d valv e failure : 2.5.3.1 . Identif

y caus e o f

actuatio n failure . 2.5.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 2.5.3.3 . Service/replac e actuato r and/or valv e components , as 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/replac e contro l system.components , a s needed . 2.6 . Los s o f

Atomizatio n Ai r

Pressur e to aPC C Injecto r 2.6.1 . Fo r

atota l los s o f

plant/instrumen

t ai r supply , se

e 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 the 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 faulty lin e components , a

s needed . 2.6.3 . I n cas e o f

mechanical/physical failur e o f pressur e contro l valve : Service/replac e pressur

e contro l valve , as needed . 2.7 . Los s o f

PC C Draf t

Contro l (Uni t

4 ) 2.7.1 . I n cas e o f

I D fa n failure , se

e 9. 5 2.7.2 . I n cas e o f

physical/electrica l failur e o f kil n pressur

e transmitter : Service/replac e pressur e transmitte

r and/or

associate d instrumentation , a

s needed . 2.7.3 . I n cas e o f

actuated dampe

r failure : 2.7.3.1 . Identif

y caus e o f

actuatio n failure . 2.7.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 2.7.3.3 . Service/replac e actuato r and/or 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 mcomponen t 2.7.4.2 . Service/replac e contro l syste mcomponents , a s needed .

Pag e 7 o f 2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 2.8 . Los s o f

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

los s o f natura l ga s pressure/flo w t

o mai n burner , se

e 2.1 . 2.8.2 . I n cas e o f

los s o f wast e pressure/flo w t

o PC C injector , se

e 2.4 . 2.8.3 . I n cas e o f

physical/electrica l failureo f temperatur

e element : 2.8.3.1 . Service/replac e fault y temperatur e elemen

t and/or associate dmstrumentation , a s needed . 2.8.4 . I n cas e o f

pbysical/electrica l failur e o f contro l systemcomponent : 2.8.4.1 . Identif

y fault y contro l syste mcomponent . 2.8.4.2 . Service/replac e contro l syste mcomponents , a s 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 detector

component . 2.9.1.2 . Service/replac e flam e detector components , a

s needed . 2.9.2 . I n cas e o f

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

y fault y contro l syste mcomponent . 2.9.2.2 . Service/replac e contro l syste mcomponents , a s needed . 2.10 . Kil n Rotatio n Malfunctio n (Uni t 4 ) 2.10.1 . I n cas e o f

mechanical/electrica l kil n driv 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 . Restore electrica l power suppl y t o motor . 2.10.2 . I n cas e o f

physical/electrica l failur e o f kil n rotational spee d transmitter : Service/replac e transmitte r and/or associate d mstrumentation , 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 mcomponen t 2.10.3.2 . Service/replac e contro l syste mcomponents , a s needed . 2.11 . Bulk/Charg e Fee dDoo r Malfunctio n 2.11.1 . I n cas e o f

mechanical/electrica l failur e o f actuated door : 2.11.1.1 . Identif

y caus e o f

actuatio n failure . 2.11.1.2 . Service/replac e electrical , hydraulic , and/or pneumati c components , as needed . 2.11.1.3 . Service/replac e actuator and/or 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 mcomponentPag e 8 o f 2 6ONY X 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 control.syste mcomponents , a s needed . 2.12 . Physical/Mechanica l Interna l Equipmen t Failur e 2.12.1 . I n cas e o f

refractor y failure , re

p air/replac e refractory . 2.12.2 . I n cas e o f

as h collectio n failur e 2.12.2.1 . Diagnos e as h collectio n systemfailur e 2.12.2.2 . Service/replac e as h collectio n syste mcomponents , as

needed . 2.13 . PC C Sea l Visua l Emission s Monitorin g an dRecordin 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 .

Pag e 9 o f 2 6ONY X 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 Ga s 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 or

lin e failure ; 3.1.1.2 . Clea r

lin e pluggin g arxL/p

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 actuated valve :

. 3.1.2.1 . Identif

y caus e o f

actuatb n failure . 3.1.2.2 . Service/replac e electaica l and/pr

pneumati c components , a s 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 systemcomponents , as needed . 3.1.4 . I n cas e o f

mechanical/electrica l failure.a t natural ga s suppl y source : 3.1.4.1 . Identif

y th e caus e o f

th e rfailure . 3.1.4.2 . Tak e th e necessar y action s t

o restor e the suppl y o f natural gas . 3.2 . Los s o f

Combustio n Ai r

Pressure/Flo w to SC C 3.2.1 . I n cas e o f

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

blowe r 3.2.1.1 . Diagnos e blower/driv e Mure . 3.2.1.2 . Service/replac e th e bibvrer/drive , a

s needed . 3.2.1.3 . Restore electrica l powe r suppl y toithe blower . 3.2.2 . I n cas e o f

physica l failur e combustio n a h duct : 3.2.2.1 . Identif

y the locatio n o f

duc t failure . 3.2.2.2 . Service/replac e faulty dart , a s needed . 3.2.3 . I n cas e o f

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

y caus e o f

actuatio n failure . 3.2.3.2 . Service/replac e electrica l and/or pneumati c components , a s 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 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 3.2.4 . Incas e o f

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

y fault y contro l systemcomponent . 3.2.4.2 . Service/replac e contro l systemcomponents , a s needed . 3.3 . SC C Mai n Burne r Ignitio n Failur e 3.3.1 . Fo r

los s o f natura l gas pressure/flow , se

e 3.1 . 3.3.2 . Fo r

los s o f combustio n ai r

pressure/flow , se

e 3.2 . 3.3.3 . I n cas e o f

pbysical/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/or associate dcomponents , a s 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 systemcomponent . 3.3.4.2 . Service/replac e contro l syste mcomponents , a s needed . 3.4 . Los s o f

Wast e Flo w to SC C Injecto r (Uni t 4 ) 3.4.1 . I n cas e o f

mechanical/electrical failur e o f wast e fee dpump : 3.4.1.1 . Diagnos e pump/driv e failure . 3.4.1.2 . Service/replac e tb e pump/drive , a s needed . 3.4.1.3 . Restor

e electrica l power

suppl y to th e pump . 3.4.2 . I n case.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 or lin e component : 3.4.3.1 . ' Identif

y m e locatio n o f

pluggin g or

lin e failure . 3.4.3.2 . Clea r

lin e pluggin g and/or

service/replac e fault y lin e components , as needed . 3.4.3.3 . Restore/confirmfunctiona l hea t tracing , i f

applicable . 3 .4.4 . I n cas e o f

mechanical/electrical 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/or pneumati c components , a

s needed . 3.4.4.3 . Service/replac e actuato r and/or valv e components , a s 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 systemcomponen t 3.4.5.2 . Service/replac e contro l systemcomponents , a s needed . 3.5 . Los s o f

Wast e Feedrat e Contro l t o SC C Injecto r (Uni t 4 ) 3.5.1 . I n cas e o f

los s o f wast e pressure/flo w t

o SC C injector , se

e 3.4 . Pag e 1 1 o f

2 6ONY X 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 flow transmitter : Service/replac e flow transmitter and/or associate dinstrumentation , as needed . 3.5.3 . I n cas e o f

actuate d valv e failure : 3.5.3.1 . Identif

y caus e o f

actuatio n failure . 3.5.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 3.5.3.3 . Service/replac e actuator and/or valv e components , a

s 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 o f

Atomizatio n Ai r

Pressur e t o aSC C Injecto r 3.6.1 . Fo r

atota l los s o f

plant/instrument

ai r supply , se

e 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 . Identifyth e locatio n o f pluggin g o r

lin e failure . 3.6.2.2 . Clea

r lin e pluggin g and/or

service/replac e fault y lin e components , a

s needed . 3.6.3 . I n cas e o f

mechanical/physica l failur e o f pressur e contro l valve : Service/replac e pressure contro l valve , a s needed . 3.7 . Los s o f

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

los s o f natural gas pressure/flo w to mai n burner , se e 3.1 . 3.7.2 . Incas e o f

los s o f wast e pressure/flo w t

o SC C injector , se

e 3.4 . 3.7.3 . In cas e o f

physical/electrica l failur e o f temperatur

e element : 3.7.3.1 . Service/replac e fault y temperatur e elemen

t and/o r associate dinstrumentation , a s 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 systemcomponent . 3.7.4.2 . Service/replac e contro l syste mcomponents , a s needed . 3.8 . Flam e Failur e 3.8.1 . I n cas e o f

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

y fault y flam e detector

componen t 3.8.1.2 ; Service/replac e 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 mcomponentPag e 1 2 o f

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

3.8.2.2 . Service/replac e contro l syste mcomponents , a s needed . Physical/Mechanica l Interna l Equipmen t Failur e 3.9.1 . In cas e o f

refractor y failure , repair/replac e refractory . Lo w Wate r

Leve l i n Sla g CoUectio n Syste m(Uni t 4 ) 3.10.1 . Fo r

alos s o f proces s water

pressure/flow , se

e 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/or associate d components , a

s needed . . 3.10.3 . I n cas e o f

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

y caus e o f

actuatio n failure . 3.10.3.2 . Service/replac e pneumati c components , a s needed . 3.10.3.3 . Service/replac e actuato r and/or valy e components , a

s needed , 3.11 . Emergenc y Safet y Ven t Openin g 3.11.1 . Respon dt

o a n emergenc y safet y ven t openin g i n amanne r consisten t wit h th e Emergency Safety Vent Plan. 3.11.2 . In cas e o f

mechanical 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/replac e emergenc y safet y ven t components , a

s needed . 3.9 . 3.10 .

Pag e 1 3 o f 2 6ONY X 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 o f

Temperin g Chambe r

Exi t Ga s Temperatur e Contro l 4.1.1 . Fo r

alos s ofproces s water

pressure/flow , se

e 1.6 . 4.1.2 . I n cas e p f

physical/electrica l failur e o f flo w transmitter : Service/replac e flo w transmitter and/o r associate dmstrumentation , a s needed . 4.1.3 . In cas e o f

actuate d valv e failure : 4.1.3.1 . Identif

y caus e o f

actuatio n failure . 4.1.3.2 . Service/replac e electrica l and/or pneumati c components , as needed . 4.1.3.3 . Service/replac e actuato r and/o r valv e components , a

s 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 , a s needed . 4.2 . Los s o f

Atomizatio n Ai r

Pressur e t o Nozzl e 4.2.1 . Fo r

atotal los s o f

plant/mstnnnen 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 the 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 faulty lin e components , a

s needed .

Pag e 1 4 o f

2 6ONY X 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 Fee dt o Lim e Slurr y Fee dTan k 5.1.1 . I n cas e o f

mechanical/electrical failur e o f iim 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 , a s needed . 5.1.1.3 . Restor

e electrica l powe r

suppl y t o the lim e slurry 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 the lim e bi n activator/vibrator , a s

needed . 5.1.2.3 . Restor

e electrica l powe r

suppl y t o me lim e slurry scre w feeder . 5.1.3 . I n cas e o f

plugging/physica l failur e p f lin e or 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 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 5.1.4 . I n cas e o f

physical/electrica l failur e o f lim e fee dcontrols : Service/replac e fault y mstrumentatio n and/o r contro l syste m components , a

s 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 dt

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

los s o f water flow t o lim e slurr y fee dtank , se e 1.5 5.2.3 . h i cas e o f

mechanical/electrical failur e o f lim e slurry agitator : 5.2.3.1 . Diagnos e agitator/driv e failure . 5.2.3.2 . Service/replac e the agitator/drive , a s needed . 5.2.3.3 . Restor

e electrica l powe r

suppl y t

o th e lim e slurr y agitator . 5.2.4 . I n cas e o f

physical/electrica l failur e o f mstrumentation : Service/replac e fault y instrumentation , a s needed . 5.2.5 . In 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 6ONY X 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

mechamcal/electrical 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 , a s needed . 6.1.1.3 . Restor

e electrica l powe r

suppl y t o 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/or

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

applicable . ' 6.1.3 . I n cas e o f

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

y caus e o f

actuatio n failure . 6.1.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 6.1.3.3 . Service/replac e actuator 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 systemcomponents , a s 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 slurry flo w t

o SDA , se

e 6.1 . 6.2.2 . I n cas e o f

physical/electrica l failur e o f flo w transmitte r Service/replac e flow.trarisrmtter and/or associate dinstrumentation , a s needed . 6.2.3 . b acas e o f actuatedvalv 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/or pneumati c components , a s needed . 6.2.3.3 . Service/replac e actuator and/or valv e components , a s

. 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 conho l syste mcomponen t 6.2.4.2 . Service/replac e contro l syste mcomponents , a s needed . Pag e 1 6 o f

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

Cit y Wate r

Flo w t o SD A (Uni t

2 an d3 ) 6.3.1 . I n cas e o f

total los s o f

cit y water

supply , se

e 1.5 . 6.3.2 . I n cas e o f

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

y the locatio n o f

plugging 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 , a

s needed . 6.3.3 . meas e o f

mechanical/electrica l failur e o f actuated valve : 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 , a

s needed . 6.3.3.3 . Service/replac e actuator and/or valv e components , a

s needed . 6.4 . Los s o f

Coolin g Ai r

Flo w t o Atomize r 6.4.1 . I n cas e o f

mecharhcal/electrical failur e o f atomize r coolin g ai r blowe r 6.4.1.1 . Diagnos e blower/driv e failure . 6.4.1.2 . Service/replac e the blower/drive , a s needed . 6.4.1.3 . Restor

e electrica l powe r

suppl y t o th e blower . 6.4.2 . I n cas e o f

physica l failur e o f

atomizer coolin g a h 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 mcomponen t 6.4.3.2 . Service/replac e contro l syste mcomponents , as neede d 6.5 . Los s o f

SD A Exi t

Ga s Temperatur e Contro l 6.5.1 . I n cas e o f

los s o f cit y water

flo w to SDA , se

e 6.3 . 6.5.2 . I n cas e o f

physical/electrica l failur e o f temperatur

e transmitter : Service/replac e temperatur e fransmitter

and/or associate d instrumentation , a

s 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/or pneumati c components , as needed . 6.5.3.3 . Service/replac e actuato r and/or valv e components , as needed . 6.5.4 . I n cas e o f

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

2 6ONY X 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 , a s needed . 6.6 . Atomize r

Failur e 6.6.1 . meas 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 ofth e lubricatio n system ,

as 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 th e atomizer/drive , a

s needed . 6.6.2.3 . Restore electrica l powe r suppl y t o me atomizer . 6.6.2.4 . components , as needed .

Pag e 1 8 o f

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

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

Lim e 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 slurry fee dpump : 7.1.1.1 . Diagnos e pump/driv e failure . 7.1.1.2 . Service/replac e th e pump/drive , a s needed . 7.1.1.3 . Restore electrica l powe r suppl y t o 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 the locatio n o f

pluggin g o r

lin e failure . 7.1.2.2 . Clear

lin e pluggin g and/o r

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

applicable . 7.1.3 . In cas e o f

mechanical/electrica l failur e o f actuated valve : 7.1.3.1 . Identif

y caus e o f

actuatio n failure . 7.1.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 7.1.3.3 . Service/replac e actuato r and/or valv e components , a s needed . 7.1.4 . I n cas e o f

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

y fault y contro l syste mcomponent . 7.1.4.2 . Service/replac e contro l syste mcomponents , a s needed . 7.2 . Los s o f

Lim e Slurr y Flo w Control/Exi t Ga s Temperatur e Contro l 7.2.1 . I n cas e o f

los s o f slurry flo w t

o SDA , se

e 7.1 . 7.2.2 . In : 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 , a s needed . 7.2.3 . I n cas e o f

actuate d valv 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/or pneumati c components , as needed . 7.2.3.3 . Service/replac e actuato r and/or 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 , a s needed . Pag e 1 9 o f

2 6

V E S 00198 1ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 7.3 . Los s o f

Atomizatio n Ai r

Pressur e t o SD A Nozzl e 7.3.1 . Fo r

atotal los s o f

plant/instrument

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

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

y th e locatio n o f

plugging o r

lin e failure . 7.3.2.2 . Clear

lin e plugging and/o r

service/replac e fault y lin e components , a

s needed .

Pag e 2 0 o f

2 6ONY X 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 o f

Carrie r Ga s Pressur e 8.1.1 . I n cas e o f

mechanicaiyelectrical 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 , a

s needed . 8.1.1.3 . Restore electrica l powe r suppl y t o 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 , a s 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 mcomponen t 8.1.3.2 . Service/replac e contro l syste mcomponents , a s heeded . 8.2 . Loss/Restrictio n o f Activate dCarbo n Flo w 8.2.1 . I n cas e o f

los s o f plan t ai r t o carbo n bul k

sack , see 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 , a

s needed . 8.2.2.3 . Restore electrica l powe r suppl y t o the 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 or

lin e failure . 8.2.3.2 . Clea r

lin e plugging and/o r

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

applicable . 8.3 . Los s o f

Plan t Ai r Pressure/Flo w t o Carbo n Bul k Sac k 8.3.1 . Fo r

atota l los s o f

plant/instrument

a h supply , se

e 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/or

service/replac e fault y lin e components , a

s 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/or pneumati c components , as needed . Pag e 2 1 o f

2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O FCORRECTIV E ACTION S FO RMALFUNCTION S

8.3.3.3 . Service/replac e actuator and/or 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 , as needed .

Pag e 2 2 o f

2 6

V E S 00198 4ONY X 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 th e 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 tom/leakin g bag(s) , as needed . 9.1.2.2 . Diagnos e fh e failur e o f th e baghous e detectio n system . 9.L2.3 . Service/replac e baghous e lea k detectio n system , as 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

gas temperature : 9.2.1.1 . Follo w fh e appropriat e correctiv e action s prescribe db y paragrap h 6. 5 (Uni t

2 an d3 ) 9.2.1.2 . Follo w the appropriat e correctiv e action s prescribe db y paragrap h 7. 2 (Uni t

4 ) 9.2.1.3 . Perfor mbaghous e inspection . 9.2.1.4 . Service/replac e bag(s) , as needed . 93 . Los s o f

Stac k Ga s Flowrat e Contro l (Uni t 2 an d3 ) 9.3.1 . I n cas e o f

I D fa n failure , se

e 9. 5 9.3.2 . 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 . 9.3.3 . I n cas e o f

actuate d dampe

r failure : 9.3.3.1 . Identif

y caus e o f

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

s needed . 9.3.3.3 . Service/replac e actuato r and/or dampe r components , a s 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 , a s needed . 9.4 . Baghous e Isolatio n Dampe r Malfunctio n (Uni t

4 ) 9.4.1 . I n cas e o f

actuate ddampe

r failure : Pag e 2 3 o f

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

9.4.1.1 . Identif

y caus e o f

actuatio n failure . 9.4.1.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 9.4.1.3 . Service/replac e actuator and/or dampe r components , a s needed . 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 systemcomponents , a s needed . 9.5 . I D 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/replac e th e fan/drive , a

s needed . 9.5.1.3 . Restore electrica l powe r suppl y t o fh e I D fan .

Pag e 2 4 o f

2 6

V E S 00198 6ONY X 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/Continuou s Monitorin g Syste mMalfunctio n 10.1.1 . A s needed , refe r fo th e CM S QA/QC

Plan fo r

guidanc e andt o 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 mstrumentation : 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 systemcomponent : 10.1.3.1 . Identif

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

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

y fault y dat asyste mcomponents . 10.1.4.2 . Service/replac e dat asyste mcomponents , as needed . 10.2 . Continuou s Emission s Momtorin g Syste mMalfunctio n 10.2.1 . A s needed , refe r t o the . CEMS

QA/QC Plan fo r

guidanc e an dt

p ensur e tha t prope r calibration s ar

e performe dan dtha

t th e appropriat

e perfonnanc e specification s ar e met . 10.2.2 . I n cas e o f physical/electrica l failur e umbilica l bea t tracing :

. 10.2.2.1 . Diagnos e failur e o f hea t tracing . 10.2.2.2 . Replace/restore hea t trace d sampl e umbihcal . 10:2.3 . I n cas e o f

mechanical/electrica l failur e o f heated vacuu mpump ; 10.2.3.1 . Diagnos e pump/driv e failure . 10.2.3.2 . Service/replac e th e pump/drive , a s needed . 10.2.3.3 . Replace/restore pum p head hea

t source . 10.2.3.4 . Restore electrica l powe r suppl y to heated vacuu m pump . 10.2.4 . In cas e o f

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

y th e locatio n p f

failure . 10.2.4.2 . Clea r

pluggin g and/o r

service/replac e fault y components , a

s needed . 10.2.5 . I n cas e o f

mechanical/electrica l failur e o f actuated valve : 10.2.5.1 . Identif

y caus e o f

actuatio n failure .

Pag e 2 5 o f

2 6 V E S 00198 7ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

10.2.5.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 10.2.5.3 . Service/replac e actuator and/or 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 , a s 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 , a s needed .

Pag e 2 6 o f

2 6

### STARTUP , SHUTDOW N AN D MALFUNCTIO N PLA N Prepare d for : Ony x Environmenta

l Services , Inc

. Sauget , Elinoi s

Prepare d by : Franklin Engineering Group , Inc . Franklin , Tennesse

e

Jul y 200 5TABL E O FCONTENT S

1. 0 INTRODUCTIO N 1

1 . l REGULATOR Y REQUIREMENT S - 2 1. 2 RECORDKEEPIN G AN D REPORTIN G PROCEDURE S 2 1.2.1 Records • . - 4 1.2.2 Reports . 4 2. 0 ENGINEERIN G DESCRIPTIO N , 6 3, 0 STARTU P AN D SHUTDOW N PROCEDURES . .1 3 3. 1 STARTU P , • • 1 3 3. 2 NORMA L SHXTTOOW N ~ 1 5 4. 0 MALFUNCTIONS........ . » 1 6 4. 1 MEASURE S T O MINIMIZ E TH E FREQUENC Y O FMALFUNCTION S 1 6 4. 2 MEASURE S T O MINIMIZ E TH E SEVERIT Y O FMALFUNCTION S 1 8 4. 3 CORRECTIV E MEASURE S 1 9

i

V E S 00 1LIS T O FT ABLE S TABL E 1 - 1 OVERVIE W O FREGULATION S REGARDIN G STARTUP , SHUTDOW N AN D

MALFUNCTIO N 3 TABL E 4- 1 SUMMAR Y O FPOTENTIA L MALFUNCTION S AN D CAUSE S 1 7 TABL E 4- 2 REDUNDAN T EQUIPMEN T AN D SYSTEM S FO RMINIMIZIN G TH E FREQUENC Y

O RSEVERIT Y O FMALFUNCTION S 2 0

LIS T O FFIGURE S FIGUR E 2- 1 FIXE D HEART H INCINERATOR , UNI T 2 , BLOCKFLO W DIAGRA M 7 FIGUR E 2- 2 FIXE D HEART H INCINERATOR , UNI T 3 , BLOC K FLO W DIAGRA M 8 FIGUR E 2- 3 ROTAR Y KIL N INCINERATOR , UNI T 4 , BLOC K FLO W DIAGRA M 1 1

LIS T O FATTACHMENT S STARTU P RECORDKEEPIN G FOR M SHUTDOW N RECORDKEEPIN G FOR M MALFUNCTIO N RECORDKEEPIN G FOR M PROGRA M O FCORRECTIV E ACTION S FO RMALFUNCTION S ATTACHMEN T 1 ATTACHMEN T 2 ATTACHMENT S ATTACHMEN T 4

i i1. 0 INTRODUCTIO N Ony x Environmental Services , Inc . (Onyx ) own s an doperate s tw o fixe dhearth , incinerator s (Unit s 2 an

d3 ) an darotar

y kil n incinerato r

(Uni t 4 ) a t it s faciht y locate di n Sauget , Illinois . Th e incinerator s ar

e subjec t t o th e Nationa l Ernission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r

Hazardou s Wast

e Combustor s (HWC) , codifie das 4 0 CFR , Par t 63 , Subpar

t EE E ( § 63.120 0 t

o § 63.1213) . Th e NESHA P specifie s emission s standard s whic h reflec t emission s performanc e o f

Maximu mAchievabl e Contro l Technologie s (MACT) , an di s commonl y referre d t o a s th e HW C MACT . Th e HW C MAC T Standar ddefine s fh e contro l o f emission s durin g normal , day-to-day operations . I n orde

r t o addres s th

e contro l o f

emission s durin g transient periods , th

e developmen

t o f aStartup , Shutdown , an dMalfunctio n Pla n (SSMP ) i s required . Startup , shutdown , an

dmalfunctio n (SSM ) ar

e definedi 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

a n affecte dsourc e fo r an y purpos e

• Shutdown - the 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

any purpos e

• Malfunction —an

y sudden , irifrequent , an dnot reasonabl y preventabl e failur e o f a h pollutio n contro l an dmomtorin g equipment , proces s equipment , o r aproces s to operat

e i n anormal o r

usual manne

r whic h causes , o r

ha s the potential t

o cause , th

e emissio n limitation s i n a

n apphcabl e standar

d to b e exceeded . Failure s tha t ar e cause di n par

t b y poor 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 h it s SSMP . Therefore , durin g period s o f

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

wil l b e consistent

wit h the 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 , t

o th e exten

t 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 th e incinerato r system s durin g period s o f startup , shutdown , an dmalfunctio n tha t ar e consistent

wit h safety an dgoo da h pollutio n contro l practice s

• .Describ e measure s fo r the preventio n an dminimizatio n o f exces s ernission s durin g period s o f

startup , shutdown , an dmalfunctio n

• Reduc e th

e reportin g burde n associate dwit h period 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) , a s show n i n Tabl e 1- 1 1Du e to th e similarit y o f

th e three incinerato r

systems , genera

l reference s t

o a n incinerato r

i n thi s documen t wil l impl y al l three incinerato r systems . Informatio n tha t i s onl y apphcable-to on e o r tw o o f th e three unit s wil l b e clearl y identifie deithe r parentheticall y o r

delineate db y th e sectio n heading . A s requhe db y § § 63.6(e)(v ) an d63.6(e)(vi) , thi s pla n an dothe r document s contahiin g procedure s or

informatio n referre dt

o i n thi s pla n wil l b e mad e availabl e fo r

mspectio n whe n requestedb y th

e Administrator . I f

Ony x i s require dt

o submi t copie s o f

thi s pla n o r

portion s o f thi s pla n (or

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

r o f thi s sectio n provide s a

n overvie w o f

regulator

y requhement s an daprogra mfo r complianc e wit h the recordkeepin g andreportin g requhements . Sectio n 2. 0 reference s a n engmeering descriptio n o f th e incinerator , a h pollutio n contro l system , an dcontinuou s momtorin g system . Sectio n 3. 0 addresse s the startu p an dshutdow n o f

th e incinerato r

system . Sectio n 4 . 0 addresse s potential malfunction s ofth e incinerato r system . 1. 1 Regulator y Requhement s On e o f th e objective s fo r

thi s documen

t i s t o estabhs h aprogra

mtha t wil l ensur

e complianc e . with relevan

t section s o f

th e Interi mMAC T Standards . Tabl e 1- 1 include s the regulatory requirement s an dthe locatio n o f eac h requirement

addressedherein .

. .1. 2 Recordkeepin g an dReportin g Procedure s Thi s sectio n addresse s th e recordkeepin g an dreportin g requhement s relate dt o period s o f

SSM . Th e startup , shutdown , andmalfunctio n report s discusse di n thi s pla n ensur e tha t Ony x i s satisfyin g th

e general dut

y t o minimiz e emission s an ddocumen t tha t action s take n durin g thos e period s ar

e consistent

wit h thi s plan . Thes e report s an drecord s provid e th e necessar

y documentatio n to shiel dtransien t event s fromthe HW C MAC T emissio n standard s imposedo n steady-stat

e operations. . A s lon g a

s action s take n durin g atransien t even t 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 even t fromsteady-stat

e operations . Fo r example , problem s ma

y aris e tha

t mee t th e definitio n o f

amalfunctio n ye t

d o 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 the action s take n sufficientl y met th e objective s o f

thi s SSM P andminimize demission s t o agreate

r degre e than requhe db y regulations .Tabl e 1- 1 Overvie w of Regulation

s Regarding Startup , Shutdow n an d Malfunctio n Regulator

y Citation Descriptio n SSM P Sectio n § 63.6(e)(3)(i

) Purpos e ofth e SSM P 1. 0 § 63.6(e)(3)(i

> Procedure s for operatin

g arwi . maintainin

g th e sourc e durin g startu p 3.1 , Table 3- 1 § 63.6(e)(3)(i

) Procedure s fo r operatin

g an d mamtainin

g th e sourc e durin g shutdow n 3.2 , Table 3- 1 § 63.6(e)(3)(i

) Procedure s fo r operatin

g an d maintainin

g th e sourc e durin g malfunctio

n Attachmen t4 •§63.6(e)(3Xi ) A progra m o f correctiv

e actio n fo r iriaUimctioningjiroces s Attachmen t4 § 63.6(e)(3Xii

) During SSM , operat e an d maintai

n sourc e i n accordanc

e wit h SSM P 1.

0 § 63.6(e)(3)(iii

) Record s an d report s whe n action s confor m wit h SSMP 1.2. 1 §63.6(eX3Xiv ) Record s an d report s whe n action s d o no tconfor m wit h SSM P an

d resul ti n a n exceedanc

e 1.2. 2 §63.6(eX3Xv ) Availabilit y o f curren tan d supersede

d SSMPs 1. 2 §63.6( e )(3)(vi ) Us e an d availabilit

y o f othe r plan s 1. 0 §63.6(eX3XviH ) Revision s t o th e SSM P 1.2. 2 § 63.10(b)(1 ) Mamtainin g files 1. 2 § 63.10(b)(2)(i

> Recor d occurrenc

e an d duratio n o f eac h startu p an d shutdow

n 1.2. 1 § 63:i0(b)(2)(ii

) . Recor

d occurrenc

e an d duratio n o f eac h malfunctio

n 1.2. 1 §63.10(b)(2)(iv ) Record s o f action s inconsisten

twit h SSM P 1.2. 1 § 63.10fb)(2)(v

) Record

s demonstratin

g conformanc

e wit h SSM P 1.2. 1 § 63.10(bX2)(vi

) , Recor

d periods ' o f

maJbfmtctionin

g CM S 1.2. 1 §63.10(d)(5)(i ) Periodi c startup , shutdown

, an d malfunctio

n report s 1.2. 2 §63.10(d)(5Xii ) Immediat e startup , shutdown

, an d malfunctio

n report s 1.2. 2 § 63.l206(c)(2)(ii)(A ) Descriptio n o f potentia l cause s o f malfunction

s Tabl e 4-1 , Attachment

s §.63.1206(c)(2Xii)(A ) Action s t o minimiz

e th e frequenc

y an d severit y o f malfunction

s 4.1,4. 2

Table 4- 2 Attachmen

t4 § 63:i206(c)(2Xii)(C ) Change s t o th e pla n 1.2. 2 § 63.1206(c)(2)(iii

) Projecte

d oxygen.correctio

n facto r t o us e durin g startu p an d shutdow n . 3. 0 § 63.1206(cX2)(iv

) Recor

d pla 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 d evaluatio

n o f excessiv

e exceedance

s durin g malfunction

s 1.2. 2 §63.1206(c)(2)(vXA)(3Xi ) Revision s to SSMP du

e to excessiv

e exceedance

s durin g malfunction

s 1.2. 2 § 63.1206(c)(2)(v)(A)(3Xii ) Recor

d result s fro m investigatio

n an d evaluatio

n o f excessiv e exceedance

s 1.2. 2 § 63,12006(c)(2)(v)A(3Xii ) Addition

s t o exces s emission

s repor t[ § 63.10(e)(3)] du

e t o excessiv e exceedance

s durin g malfunction

s 1.2. 2 § 63.l206(c)(2)(v)(B)(l) Wast e fee d restriction

s an d othe r OPL s durin

g startu p an d shutdow

n 3. 0 §63.1206(c)(2)(v)(BX2 ) Interloc k OPL s of

(c)(2)(v )(B )(l ) wit

h AWFC O syste

m 3.0 § 63.1206(c)(2)(v)(B)(3 ) AWFC O du

e t o exceedanc

e o f startup/shutdow

n OP L 3. 0Accordingly , the recordkeepin g an dreportin g requirement s presente d i n thi s sectio n ar e onl y applicabl e to period s o f SS M i n whic h ther

e i s areasonabl e expectatio n tha t a n OP L or emissio n standar

dcan 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 a n exceedanc e o f

a n operatin g limi t

o r emissio n standard . Malfunction s tha

t preven t th e abilit y t

o documen

t on-goin g comphanc e ar e als o subjec t

t o recordkeepin g an dreportin g requirements . Thi s plan , al l revision s t o thi s plan , andal l record s an dreport s describe di n thi s sectio n wil l b e retaine di n th e operatin g recordfo 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 h SS M

• Th e duratio n o f

eac h SS M

• Documentatio n t

o demonstrat

e tha t action s take n durin g period s o f SS M ar e consisten t wit h thi s SSM P

• . Descriptio n o f

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

t ar e not consisten

t with procedure 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 malrunctions , respectively . Th e informatio n recorde do n thes e form s wil l be . utilize dto documen t conformanc e wit h the SSM P an dto compl y wit h the reportin g requhements . Th e startup , shutdown , an dmalfunctio n reportin g requhement s ar e describe di n th e next section . 1.2.2 Reports Revision s to thi s SSM P ma y b e mad e withou t prio r agenc y approva l t

o reflec t change s i n equipmen t an dprocedure s an dt

o mee t the regulator

y requhements . An y suc h revision s mad e durin g asemiannua l reportin g perio dwil l b e submitte dwit h th e periodi c SS M report . Revision s t

o thi s plan—whic h alter th e scop e o f

activitie s durin g astartup , shutdown , o r

malfonction—wil l not

tak e effec t unti l awritte n notice , describin g the revisions ^ i s submitte dt o th e permittin g authority . Change s made t o thi s pla n tha t ma y significantl y increas e emission s ar e subjec t t o approva l b y th e Administrator . A writte n reques t fo r approval o f

th e change s an dth

e revise dSSM P wil l b e submitte dt o th e 4

V E S 00199 5Administrato r withi n 5 day s afte r

makin g suc h achang e t o thi s plan . Shoul da n SS M even t occur tha t i s not . addresse do r

inadequately addresse di n thi s SSMP , Ony x wil l mak e th e appropriat

e revision s t

o thi s pla n withi n 4 5 day s afte r th e event . A n investigatio n an devaluatio n wil l b e performe do n eac h se t o f 1 0 exceedance s o f

a specifi c emissio n standar do f aspecifi c operatin g paramete r limi t tha t occur durin g malfunction s withi n a6 0 da y period . Withi n 4 5 day s o f th e 10 t hexceedance , tb e investigatio n wil l determin e plausibl e cause s fo r eac h excessiv e exceedance . Th e evaluatio n wil l conclud e ho w to minimiz e fh 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 asummar

y o f eac h investigatio n andevaluatio n requhe ddurin g the semiannual reportin g period . I n addition , the excessiv e emission s repor t wil l mclud e any change s t o 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 SSM . report s wil l b e submitte dt o th e Administrato r

semiannually , i f

astartup , shutdown , or

malfunctio n occurre ddurin g tha t semiannual reportin g period . Thi s repor t wil l tak e th e for mo f aletter to . th e Administrato r

an dmclud e th

e followin g infonnation :

• A statemen

t tha t action s taken durin g al l period s o f startup , shutdown , or malfunctio n wer

e consisten

t wit h th e procedure s give n i n thi s SSM P

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

eac h malfunctio n

• Th e name , title, ari dsignatur e ofth e owner/operator

(o r othe r responsibl e official ) certifyin g the accurac y o f th e repor t A n immediate SS M repor t wil l be submitte di f

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

consistent

wit h thi s plan ; an da

n OP L o r

emissio n standar

di s exceeded . Withi n tw o workin g day s afte r suc h a n 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 h an action , aletter t o th e 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/or operatin g paramete r monitorin g exceedance s believe dt o hav e occurred . Th e letter wil l als o includ e th e name , title, an dsignatur e o f th e owner/operator

(o r othe r responsibl e official ) certifyin g the accurac y o f the report .2. 0 ENGINEERIN G DESCRIPTIO N Brie f description s o f

th e fixe dhearth , incinerator s an dth e rotar y kil n incinerato r

ar e presente d i 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 dengmeerin g descriptio n ofth 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 dher

e b y reference . 2. 1 Fixe dHeart h Incinerator s Eac h o f the fixe dheart

h incinerator s include s th e followin g components :

• Fee dequipmen

t • Primar y an dsecondar y combustio n chambers • Lim e injectio n system • Spra y drye r absorbe r (SDA )

• Fabri c filte r

baghous e • Solids , an das h removal system s • Induce ddraf

t (TD ) fa n an dstack

• mstrumentation , controls , an ddata.acquisitio n system s Figur e 2- 1 present s abloc k flo w 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 d i n Figur e 2-2 . A variety o f

sohd , liquid , an dgaseou s waste s ar e thermall y treate d i n the fixedheart h incinerators . Soli dwast e i s fe dt o th e primary (lower) combustio n chambe r vi aafee d conveyo r syste man dpneumati c ram . Liqui dwast e fromtank s an dtanke

r truck s ar e fe d to the primary combustio n chambe r throug h tw o atomize dliqui dinjectors . Bot h Unit s 2 an d3 ar

e equippe dwit h aspecialt y wast e fee dsystems . Th e Uni t 2 primary wast e fromliqui dcontainer s an dga s cylinder s ar

e fe dt o th e Uni t

2 primary combustio n chambe r throug h aspecialt

y fee dport . Wast

e fromliqui dcontainer s i s fe dfroma hoode dfee dsyste mt

o fh e Uni t

3 primary combustio n chambe r throug h aspecialt

y fee d injector . Of f

gase s fromth

e hooded , fee demissio n contro l syste mair e fe ddhectly . t o

6

V E S 00199 7HIG H 81 U U(MO S

SOUO S (III I

I I I I I T T T t T COMBUSTO N AI R ROWE R T "

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BT U DIREC T INJEC T , LIQUID S 

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WE T AS H DUMPStE R U M E PREPARATIO N SYSTE M

SPRA Y OR Y ABSORBE R

OR Y SCRUBBE R SOUD S ( DS S ) EN D DUM P' MAI NSTAC K •

DR Y SCRUBBER , MUD S ( DS S ) EN D DUM P

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- SOU O WAST E FLO W

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Figur e 2- 2 Fixe dHeart h Incinerator , Uni t 3 , Bloc k Flo w Diagra m

< m 0 5 

### o o C D C Dthe Uni t 3 secondar

y combustio n chamber . Of f gase s fro mawast

e handlin g glov e bo x ar e als o fe ddirectl y t

o the Uni t

3 secondar

y combustio n chamber . Th e primary combustio n chambe r mai n burner

an dth e secondar

y combustio n chambe

r mai n burne

r ar e use dt o maintai n temperature s o n natural gas . Combustio n gase s exi t th e primary combustio n chambe r an dente

r int o the secondar

y combustio n chamber , whic h serve s as a

n afterburner . Combustio n gase s exi t th e secondar

y combustio n chambe

r an d ente r th e SDA . Th e secondar

y combustio n chamber

i s equippe dwit h a

n emergenc y stack . Lim e slurry an dwate

r ar e fe dt o th e SD A atomizer . Th e atomizer has arapidl y spimun g whee l tha

t atomize s th

e lim e slurry andwater

int o aclou do f

fin e droplets . Combustio n gase s ar e directe dupwardthroug h adisperser 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 dgas ' remova l an dcoohn g o f th e combustio n gas . Drie dspen t chemical s an das h settl e t o the botto mofth e SD A andar e discharge dt

o the as h removal system . Combustio n ga s exit s the SD A an di s distribute dt o th e fabri c filte r

modules . Uni t

2 ha s fou r fabri c filte r

module s andUni t

3 ha s three fabric ' filte r modules . Combustio n ga s passe s throug h Teflon-coate dfiberglass clot h bags . Particle s i n th e combustio n gase s ar

e deposite do n th e outside o f eac h ba g i n th e filter

module.. . Durin g th

e ba g cleanin g cycle , aburs t o f ai r i n th e directio n opposite t o th e ga s flo w dislodge s particulate matte r from th e bag . Th e induce ddraf

t fa n i s locate ddownstrea mo f fh e fabri c filter

baghouse . Th e induce d draf t fa n move s the combustio n gas throug h the syste man dexhaust s th e ga s throug h th e mai n stack . ' Hot , we t ga s i s extracte ddownstrea mo f th e baghous e throug h acontinuou s emission s momtorin g system . Thi s systemfeature s amulti-componen t infrare dgas analyzer

tha t detects hydroge n chloride , carbo n monoxide , andwater vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations . 2. 2 Rotar y Kil n Incinerato r Th e rotar y kil n incinerato r

include s th

e followin g components :

• Wast e fee dsystem• Primar y an dsecondar y combustio n chambers • Temperin g chambe

r • Lim e injectio n syste m • Spra y dryer absorbe r • Carbo n injectio n syste m • Fabri c filte r

baghous e • Solid s an das h remova l system s • Induce ddraf

t (ID ) fa n andstack

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

th e Uni t 4 incinerato r

system . A variety o f

soh dan dliqui dwaste s ar e thermall y treate d i n fh e rotar y kih aincinerator . Soli dwaste s ar

e fe dto ara mfeeder

vi aaclamshell , a<hu mfee dconveyo r

anda n auxiUar y fee dconveyor . A hydrauli c ra mpushe s the soh dwast e into th e kiln . Liqui d wast e fro mtank s an dtanke r truck s i s fe dt

o th e primar y andsecondar y combustio n chambers throug h atomize dliqui dinjectors . Th e primary combustio n chambe r mai n burne

r andth e secondar

y combustio n chambe

r mai n burne

r ar e use dt o maintai n temperature s o n natural gas . Combustio n gase s exi t the primary combustio n chambe r an dente

r int o the secondar

y combustio n chamber , whic h serve s a s a h afterburner . A surg e vent i s locate da

t the front ofth e kil n an dth e secondar y combustio n chambe

r i s equippe dwit h athermal relie f vent . Combustio n gase s exi t

the secondar

y combustio n chambe

r an dente

r th e temperin g chamber . Proces s water

i s fe dto temperin g chambe r throug h a h atomize dspra y nozzles. Combustio n ga

s i s copie da

s i t passe s throug h th e spra y 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 dbetween tw o identica l SDAs . Lim e slurry i s fe dt o eac h SD A throug h a h atomize dspray nozzles . Combustio n gase s ar e directe ddownwardthroug h aduc 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 dga s remova l an dcoolin g o f

the . combustio n gas . Drie dspen t chemical s an das h settl e t o the botto mofth e SD A an dar e discharge dt

o the as h remova l system .

1 0V E S 00200 5A carbo n injectio n syste mi s utilize dfo r controllin g dioxin/fiira n andmercur y emissions . Th e activate dcarbo n i s a h injecte dint o the combustio n ga s immediatel y downstrea mo f th e convergenc e o f

combustio n gase s fro mfh e SDAs . Combustio n gase s exi t

th e SDA s an dar

e distribute dt

o tw o fabri c filte r

modules . Eac h modul e ha s three compartment s i n paralle l containing , multipl e fabri c bags , Combustio n gas passe s throug h the fabri c bags . Particle s i n the combustio n gase s ar e deposite do n th e outsid e o f

eac h bag . Durin g th

e ba g cleanin g cycle, , aburs t o f a h i n the dhectio n opposit e t o fh e gas flo w dislodge s particulate matte r fromth e bag . Th e induce ddraf

t fa n i s locate ddownstrea mofth e fabri c filte r

baghouse . Th e induce d draf t fa n move s th

e combustio n gas throug h the syste man dexhaust s the gas throug h the mai n stack . . Hot , we t ga s i s extracte ddownstrea mo f th e I D fa n throug h acontinuou s emission s monitorin g system . Thi s systemfeature s amulti-componen t infrare dga

s analyzer

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

1 23. 0 STARTU P AN D SHUTDOW N PROCEDURE S Th e purpos e o f

thi s sectio n i s t o prescrib e procedure s fo r the startu

p an dshutdow n ofth e incinerato r

system . Thi s sectio n als o clarifie s whic h action s ar e withi n th

e scop e o f

th e regulator y definitio n o f

startu p an dshutdown . T o satisf y th e requhement s o f

§ 63.1206(c)(2)(v)(B) , wast e fee drestrictio n an doperatin g limit s hav e been impose dt o startup s an dshutdowns . Durin g astartup , the feedin g o f hazardou s wast

e t o th e incinerato r

wil l no t b e initiate dunti l al l operatin g parameters ar e withi n limits . Hazardou s wast e wil l no t b e fe ddurin g ashutdow n event . Consisten t

wit h th e requirement s o f § 63.1206(c)(2)(iii) , Ony x wil l utiliz e a n 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 ca n occu r durin g startu

p an dshutdow n du e t

o change s i n the oxyge n concentration^ Th e oxyge n correctio n facto r o f 1. 6 i s base do n th

e 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 utiUze dwhe n th e wast

e residenc e tim e i n the primary combustio n chambe r has expire d an dwhe n th e incinerato r i s i n startu

p o r shutdown . Ony x has develope dstandar ddivisio n practice s (SDPs ) fo r th e operation ; o f

eac h incinerato r

syste man

dancillar y equipmen

t an dsystems . Th e SDP s contoiriin g startu p an dshutdow n procedure s fo r the incinerator s are :

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

No. 2/B Incinerators

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

No. 4 Incinerator 3. 1 Startu p A l l startup s ar

e precede db y ashutdown . Dependin g o n the purpos e o f the precedin g shutdown , portion s o f

th e a h 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 startu p recor d(se e Attachment s 1) . Durin g astartup , wast

e wil l no t

b e introduce dunti l al l operatin g parameter s ar e withi n hmits . A startu

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

e withi n limits . Onyx' s startu

p procedure s ar

e representative , o f

safety andgoo da h pollutio n contro l practices . Th e procedure s ar e designe dt

o mimrniz e the potentia l fo r exces s ernission s b y ensurin g tha

t al l equipmen

t i s full y operational (withi n permi t limits ) prior

t o th e 1 3introductio n o f hazardou s wast

e t o th e system . Adherenc e to thes e startu p procedure s wil l emplo y "th

e knowledg e an dskill s demonstrate dthroug h the implementatio n o f the Operato r Trainin g an dCertificatio n Program .3. 2 Norma l Shutdow n Som e shutdown s wil l allo w th e primar y combustio n chamber to cool . Prio r

to thes e shutdowns , the incinerato r wil l b e burnin g auxiliar y fue l onl y an dth e hazardou s wast e residenc e tim e wil l hav e transpired : A shutdow n wil l b e initiate dwit h th e shutof f o f auxiliary fue l t

o th e incinerato r

o r b y shutof

f o f m e I D fan . Other

shutdown s wil l b e

. initiate dwit

h the cessatio n o f

al l wast e feed s b y th

e operato r

to stabiliz e syste moperatin g parameters . Portion s o r al l o f the a h pollutio n contro l syste mma y remai n i n operatin g mode a t th e conclusio n o f

ashutdow n throug h th

e subsequen

t startup . Onyx' s shutdow n procedure s ar e representativ e o f

safet y an dgoo da h pollutio n contro l practice . Th e procedure s ar e designe dt

b mimmiz e th

e potentia l fo r

exces s ernission s b y ensurin g tha

t al l wast e feed s ar

e of f arid/o r the hazardou s wast

e residenc e time has transpire dprior

t o th e shutdow n o f

th e incinerato r

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

th e Operator

Trainin g an dCertificatio n Program . Procedure s fo r emergency 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 ofth 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 t o minimiz e m e frequency an dseverit

y • Prescrib e procedure s fo r operatin g an dmaintainin g th e incinerato r

durin g malrunction s • Prescrib e action s t

o correc t th e caus e o f

amalfunctio n A summar

y o f potentia l malfunction s an dthei r cause s i s give n i n Tabl e 4-1 . Thi s hs t o f potential malfunction s i s arrange daccordin g t o uni t operations . Th e occurrenc e o f an y even t hste di n Tabl e 4- 1 shoul db e responde dt o a s amalfunctio n an damalfunctio n recordkeepin g form , include da s Attachment

3-, shoul db e initiated . Durin g the respons e t o thes e events , i t

wil l b e determine di f

th e even t meets th e regulator

y definitio n o f

a malfunction . 4. 1 Measure s t

o Minimiz e tb e Frequenc y o f Malfunction s Th e followin g measure s contribute t o prevent malfunctions :

• Incinerato r

systemdesig n consistent wit h safet

y an dgoo dengineerin g practice s • Hazard s an doperability studie s o f th e incinerator s • Appropriat e frequency o f preventativ e maintenanc e an dinspectio n • Goo doperatin g practice s • Wel l traine dan dqualifie dpersonne l • Onyx' s performanc e history , thi s document , an dth e foUowing regulator y document s serv e as . evidenc e o f

Onyx' s proactiv e measure s t o minimiz e the frequency 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 an d Cause s Potentia l Malfunction s fo r Unit s 2,3 , and 4 .



## < m o o 

### o o r o o o c o GENERA L

- Los s o f

Electrica

l Powe r Suppl y

- Los s oflnstrument/Plan tAi r Suppl

y

- Los s o f

Plan tNitroge n Suppl y

- Los s o f

Cit y Wate r Suppl y

- Los s o f

Proces s Wate r Pressure/Flo

w (Unit4

)

- 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 Pollution 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 n Burne

r

- Los s o f

Combustio

n Ai r Pressure/Flo

w t o PC C

- PC C Mai n Burne

r Pilo tFailur

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

Atomization Ai r Pressur e t o a PC C Injecto

r

- Los s o f

PC C Draf

tContro l (Uni t4 )

- Loss o f

PC C Temperatur

e Contro l

- Flam e Failur e

- Kil n Rotatio

n Malfunction (Uni

t4 )

- Bulk/Charge Fee

d Door Malfunction

- Physical/Mechanica l Interna l Equipmen

tFailur e

- PC C Sea

l Visua l Emission

s Monitoring an

d Recordin

g Syste m

- Rapi d Stea

m Generatio

n from As h Collection Syste m Wate r SECONDAR Y COMBUSTIO N CHAMBE R

- Los s o f

Natura l Ga s Pressure/Flo

w t o SC C Mai n Burne

r

- ' Los s o f

Combustio

n Ai r Pressure/Flo

w t o SC C

- SC C Mai n Burne

r Ignitio n Failur e

- Los s o f

Wast e Flo w t o SC C Injecto

r

- Los s o f

Wast e Feedrat

e Contro l t o SC C Injecto

r

- Los s o f

Atomization Ai r Pressur e 't o a SC C Injecto

r

- Los s o f

SC C Temperatur

e Control

- Flam e Failur e . .

- Emergenc

y Safet y Ven tOpenin g

- Physical/Mechanica

l Interna l Equipmen

tFailur e - Lo w Wate r Leve l i n Sla

g Collectio n Syste

m (Uni t4 )

- Rapid Stea

m Generatio

n fro m As h Collection Syste m Wate r TEMPERIN G CHAMBE R(UNIT 4 )

- Loss o f

Temperin

g Chambe

r Exi tGa

s Temperatur

e Contro l

- Loss o f

Atomizatio

n Ai r Pressur

e t o Nozzle LIM E SLURR Y SYSTE M

- Loss o f

Lim e Fee

d t o Lim e Slurr

y Fee d Tan k

- Malfunction i n Lime 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 t o SD A

- Los s o f Liirjf i Slurr y Flo w Control ,

- Los s o f Cit y Wate r Flo w t o SD A

- Los s o f Coolin g Ai r Flo w t

o Atomizer

- Los s o f SD A Exi tGa

s Temperatur

e Contro l

- Atomize

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

- Loss of

Lim e Slurr

y Flo w t o SD A

- Loss of

Lim e Slurr

y Flo w Control/ExitGa s Temperatur

e Contro l

- Los s of 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 d Carbo n Flow

- Loss of

Plan tAi r Pressure/Flo

w t o Carbo n Bul k Sac

k BAGHOUS E & INDUCE D DRAF T (DD ) FA N

- Tom/Leaking Ba

g

- Bag Blmding/High-Hig h Pressur

e Dro p

- Loss of

Stack.Ga

s Flowrat

e Contro l (Uni t2 an d 3 )

- Baghous

e Isolatio n Dampe

r Malfunction (Uni

t4 )

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

l System/Continuou

s Monitoring Syste

m Malfunction

- ' Continuou

s Emission

s Monitoring Syste

m Malfunction .1 7 Potential Cause s fo r a Malfunctio n

Mechanical/electrica

l failur e o f rotatin g equipment

. Plugging/physica

l failur e of | lines/nozzle

s Physical/electrica

l failur e o f mstrumentatio

n MechanicaVelectrica

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

tfailur eDespite thes e efforts , equipmen t failure s an dothe

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

regulator

y requirements , th

e operatin g recor dmi l contai n th e appropriat

e documentatio n to establis h tha t poo r maintenanc e o r

careles s operation s ar

e not contributin g factor s t

o th e caus e o f

amalfunction . 4. 2 Measure s t o Minimiz e th e Severit y o f Malfunction s The followin g measure s contribute t o mirihniz e th

e severity 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 dandquahfie dpersonne l

• Desig n o f

me incinerato r

system Typically , an even

t tha t meets th e definitio n o f

amalfunctio n wil l trigger a n alarm . A n alar minform s the operator

o f the situatio n andma

y provid e a n opportunit

y t o avoi da n 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 a n automate drespons e tha t i s specifi c t

o the triggerin g condition . Refe r to Onyx' s Documentation of Compliance OT

Notification pf

Compliance, whicheve r i s currentl y apphcable , 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&EDs ) The mos t critica l ke y t

o mininiizin g th e severit y o f malfunction s i s the fimctionality o f AWFC O interlocks . Accordingly , Ony x perform s testin g o f th e AWFC O system , as describe di n th

e AWFCO Plan. Thi s testin g confirm s astat e o f readines s t o respon dt o a malfunctio n i n amanne

r tha t wil l minimiz e th e releas e o f hazardou s ai r

pollutants . Throug h trainin g an djo b experience , th e operator wil l hav e the proces s knowledg e tha t qualifie s hi mt

o us e discretio n i n respondin g t o malfunctions . Du e to th e unusual an d dynami c condition s tha

t ar e presen t durin g a'malfunction, operator discretio n i s essential to minimizin g the severit y o f malfunctions. " A n operato r ca n evaluat

e proces s condition s and . alarm s an dchoos e th e bes t respons e to avoi da

n exceedance , i f

possible. ; I f

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

fai l saf e positions , the operato

r mus t recogniz e the situatio n an drespondappropriately . I n th e even t tha t th e malfunctio n affect s th

e abilit y to automaticall y cutof f waste , the operator

wil l manuall y cutof f wast e feed s as quickl y a

s possible .

1 8Th e desig n o f th e eac h incinerato r

syste mals o ensure s tha t th e severity 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 dredundan

t 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 the operator convenient

acces s to proces s variabl e indication , includin g positio n indicatio n o f selecte dactuate dvalves . Thi s i s essentia

l t o providin g th

e operator

th e hiformatio n require dto bes t evaluat e systemcondition s andresponses . Tabl e 4- 2 list s potentia l malfunction s an dassociate d redundan t equipmen

t an dsystem s tha

t ar e availabl e t o preven

t thes e malfunction s o r

t o minimiz e the potential fo r asignifican t

releas e o f

hazardou s ai r

pollutants . 4. 3 Correctiv e Measure s The.Program of

Corrective Actions for

Malfunctions i s Attachmen t 4 o f thi s documen t Thi s progra

maddresse s ho w .th

e incinerato r

wil l b e operate dandmaintaine ddurin g malfunctions . I n thi s program , potentia l malfunction s ar e liste dfo r

eac h portio n o f

fh e incinerato r

system . Th e malfunction s ar e events tha

t wil l b e recognize db y th e operator , o r indicate db y a

n alarm , an dthreate

n t o caus e a

n exceedance . I n fh e respons e to th e malfunctio n and/or

alarms , the operator

wil l appl y discretio n andattempt t o maintai n th e incinerato r

syste mwithi n regulator y limits . I n the progra mo f correctiv e actions , potential cause s o f

eac h malfunctio n ar

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

y th e caus e o f th e malfunction . Fo r

eac h potential cause , action s t o correc t th e failur e ar

e hsted . Th e correctiv e action s prescribe dma y require the collaboratio n o f multi

discipline dpersonne l wh o ar e qualifie dt

o retur n the incinerato r

syste mto proper

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

1 9 V E S 00201 0Tabl e 4- 2 Redundan

tEquipmen

tan d System

s fo r Minimizin g th

e Frequenc

y o r Severit

y o f Malfunction s Redundan

tEquipment/System

s Potentia

l Malfunctions 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 a h compressor s runnin g andon e compresso r o n ho t standb y (Uni t

2 an d3) . Los s o f mstrument/Plant

A h Suppl y Dua l Proces s Water

Pump s Los s o f Proces s Wate r

Pressure/Flo w Dedicate dPC C combustio n a h fa n (Uni t 4 ) Los s o f

Combustio n A h Pressure/Flo w t o 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 A h Pressure/Flo w to SC C Multipl e Temperin g Chamber Nozzle s Los s o f Temperin g Chamber

Exi t Ga s Temperatur

e Contro l Los s o f Atomizatio n Ai r

Pressur e t o 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 Spar

e Lim e Slurr y Atomize r

(Uni t 2 & 3 ) Atomize r

Failur e -DualSDAs(Unit4 ) Los s o f Lim e Slurr y Flo w fo SD A Los s o f Lim e Slurr y Flo w Control /Exit Ga s Temperatur

e Contro l Los s o f Atomizatio n A h Pressur e t o SD A Nozzl e Off-lin e Spar

e Baghous e Modul e (Uni t 2 ) TorriVLealdh g Ba g Tw o baghous e module s wit h three compartment s each . 5 compartment s provid e sufficien t particulate removal s o tha

t one o f th e 6 compartment s can b e isolate da s aspare . (Uni t 4 ) Tom/Leakin g Ba g

2 0 V E S 00201 1

### ATTACHMEN T 1

STARTU P RECORDKEEPIN G FOR M

V E S 00201 2ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 1 o f 3 ) This repor

tpertain s t o a startu

p o f Uni t2/3/4 . (circle one) . Startu p even tinitiate d on : .

(Month/Day/Year, Hours : Minutes ) Startu p even tconclude

d on : (Month/Day/Year, Hours : Minutes ) Th e tota l duratio n o f thi s startu p even twas : (Hours : Minutes ) Attache d t o thi s for m is a checklis

ttha tsummarize

s th e approve

d startu p procedure

s reference

d i n Onyx' s Startup, Shutdown, and Malfunction Plan (SSMP) . The operationa l step s tha thav e bee n checke d documen

ttha t th e detaile d startu p procedure

s wer e followed . Wer e al l action

s associate

d wit h thi s startu p even ti n conformanc

e wit h th e SSMP ? Yes /

N o (circl

e one) . I f no, describ

e th e inconsisten

taction s below .

Wer e ther e an y exceedance

s o f a n operatin

g paramete

r lirnit? Yes /

N o (circle one) . If

yes , pleas

e list/describe. I f an y action s wer e no tconsisten

twit h th e SSM P an

d a n operatin

g paramete

r lirni twa s exceeded

, a n immediat

e SS M repor

ti s required.

Notes/Recommendations :

Th e following signatur

e certifie s th e accurac

y o f thi s record : (Name ) (Tide) (Signature

) (Date )

V E S 00201 3ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 2 o f 3)

Uni t2 an

d 3 Incinerato r Startup Checklis t Initial s Verif y tha tpre-startu

p ha s bee n complete

d Chec k therma l relie f ven t(TRV ) Star tcombustior

i airfa n - Star tPC C mai

n burne r an d temperatur

e ramp-u p Star tSC C mai

n burne r an d temperatur

e ramp-u p Chec k stac k ga s flo w an d SD A temperature

s contro l setting s Star tD ) fan ; Monitor SD A temperatur e whil e rampin g u p stac k ga s flowrate Close TR V Star tlim e slurr y Establis h al l operatin

g parameter

s withi n limit s Operator' s Notes :

Note : . Certai

n airpollutio

n contro l an d ancillar

y equipmen

tma y b e operationa

l prio r t o startu p (Signatur e o f Shif tLeade r o rDesignee

) (Date )

V E S 00201 4ONY X ENVIRONMEN T A L SERVICES , INC . INCINERATO RSTARTU P RECOR D

(Pag e 3 o f 3 )

Uni t4 Incinerato r Startu p Checklis t Initial s Verif y tha tpre-startu

p ha s bee n complete

d Chec k therma l relie f ven t(TRV ) Star tF D fa n an d se tkil n draft'(star

to f purg e cycle ) Star tSC C combustio

n ai r fa n

. Star tth e kil n combustio

n ai r fa n (purg e cycle complete

) Star tSC C mai

n burne r an d temperatur

e ramp-u p Star tPC C mai

n burne r an d temperatur

e ramp-u p Star tkil n rotatio

n befor e 50 0 ° F Star tm e kil n sea

l ai r Star tth e SC C conveyo

r Se tu p th e temperin

g chambe

r foroperatio

n Se tu p lim e slurr y injectio n syste m Se tu p th e SDA s fo

r operatio

n Se tu p th e as h collection syste

m Se tu p th e baghouse

s for operatio

n Slowl y ramp-u p th e temperin

g chambe

r exi ttemperatur

e > Continu

e PC C an

d SC C temperatur

e ramp-up

, Se tu p th e ai r canno n Star tth e kil n sea

l conveyo

r Establis h al l operatin

g parameter

s withi n limit s Operator' s Notes :

Note : Certai

n ai r pollutio

n contro l an d ancillar

y equipmen

tma y b e operationa

l prior t o startup . (Signatur e of Shif tLeade r o rDesignee

) (Date )

### ATTACHMEN T 2

SHUTDOW N RECORDKEEPIN G FOR M

j

V E S 00201 6ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 1 o f 3 ) Thi s repor

tpertain s t o a shutdow

n o f Unit2/3/ 4 (circle one) . Shutdow n even tinitiate d on : (Montb/Day/Year, Hours : Minutes) Shutdow n even tconclude

d on : (Month/Day/Year, Hours : Minutes) Th e tota l duratio n o f thi s shutdow

n even twas : (Hours : Minutes ) Attache d t o thi s form is ' a checklis

ttha tsummarize

s th e approve

d shutdow

n procedure

s reference

d i n th e Onyx Startup, Shutdown, and Malfunction Plan (SSMP) . The operationa l step s tha thav e bee n checke d documen

ttha t th e detaile d shutdow

n procedure

s wer e followed . Wer e al l action

s associate

d wit h thi s shutdpw

n even ti n conformanc

e wit h th e SSMP ? Yes /

N o (circl e one) . If no , describ

e th e inconsisten

taction s below .

Wer e ther e 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 were ' no tconsisten

twit h th e SSM P an

d a n operatin

g paramete

r limitwa

s exceeded

, a n immediat

e SS M repor

tis required.

Notes/Recommendations :

The foUowin

g signatur

e certifie s th e accurac

y p f thi s record : (Name ) (Title) (Signature

) (Date )

V E S 00201 7ONY X ENVIRONMENTAJ L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 2 o f 3 )

Uni t2 an d 3 Incinerato r Shutdown Checklis t Initial s Verif y tha tal l wast

e feed s ar e of f and/or tha

tth e hazardou

s wast e residence tim e ha s transpire

d Monito r CEM S outou

tt o verif y stabl e condition

s Open th e stac k ca p Sto p th e I D fa n

. Shu tof f wate r an d lim e slurr

y flow to th

e atomize

r

' Remov e atomize

r an d positio n li d Operator' s Notes :

Note : Al l o

r certai n air pollution contro

l an d ancillar

y equipmen

tma 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 tLeader o rDesignee

) (Date )ONY X ENVIRONMENTA L SERVICES , INC . INCINERATO RSHUTDOW N RECOR D

(Pag e 3 of 3 )

Uni t4 Incinerato r Shutdow n Checklis t Initial s Verif y tha tal l wast

e feed s ar e of f and/or ma

tth e hazardou

s wast e residenc e tim e ha s transpire

d

• Ventth

e ai rcannon

s Shu tof f th e kil n burne

r an d SC C burne

r Shu tof f fh e kil n an d SC C combustio

n ai rfan s Reduc e th e temperin

g chambe

r outle ttemperature t

o 50 0 ° F Shutdow n SD A (a

tappropriat

e temperatures

) Shutdow n temperin

g chambe

r (a tappropriat

e temperatures

) Afte r PC C an

d SC C reac

h th e appropriat

e temperature, shu

tof f th e I D fa n Operator' s Notes :

Note : Al l o r certai

n air pollutio

n contro l an d ancillar

y equipmen

tma y remai n operationa

l throughou

t shutdown

. • Onc e fh e liazardou

s wast e residenc

e tim e ha s transpired, operator' s discretio n car tb e applied . (Signatur e of Shif tLeade r o rDesignee

) (Date )

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

(Pag e 1 o f 1 ) Tru s repor tpertam s t o a malfunctio

n o f Unit2/3/ 4 (circl

e one) . The malfunctio

n even toccurre d on : (Monlh/Day/Year , Hours : Minutes ) . The malfunctio

n even tconclude

d on : (Month/Day/Year, Hours : Minutes ) Th e tota l duratio n o f thi s malfunctio

n even twas : (Hours : Minutes ) Th e Onyx Program of

Corrective Actions forMalfunctions mus tb e adhere d t o fo rth e operatin

g an d mamtainin

g o f th e incinerato

r syste m an d fo r correctin

g th e caus e o f th e malfunction. Describ e th e malfunction, th

e automate d and/o r operato r response

, th e potentia

l caus e ofth e malfunction, an d th e correctiv

e action s taken :

Wast e Feed s of f Tim e — Incinerato

r "Clea r o f Waste " Time - Wer e all action

s associate

d wit h thi s malfunctio

n even ti n conformanc

e wit h th e SSMP ? Ye s /

N o (circle.one) . If no , initiat

e a n irnmediat

e startup , shutdown

, an d malfunctio

n repor t List/describe th

e exceedance

s tha toccurre d (or believe

d to hav e occurred

) du e t o mi s malfunction :

Notes/Recommendations :

' Th e followin

g signatur

e certifie s th e 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 d Maintainin

g th e Syste m durin g Malfunction

s 1. 2 Los s o f

Electrica

l Powe r Suripl y 1. 3 Los

s o f Instrument/Plan

tAi rSuppl

y 1. 4 Los

s o f Plan tNitroge n Suppl y 1. 5 Loss o f

Cit y Wate r Suppl y 1. 6 Los

s o f Proces s Wate r Pressure/Flo

w (Unit4

) 1. 7 Malfunction o f

Safet y Interloc

k o rAutomati

c Wast e Feed Cutof

f Interloc k 1. 8 Excessiv

e Ai rIn-leakag

e i n Ai rPollution Control Syste m 2. 0 PRIMAR Y COMBUSTIO N CHAMBE R 2. 1 Los s o f

Natura l Ga s Pressure/Flo

w to PC C Mai n Burne

r 2. 2 Los s o f

Combustio

n Ai r Pressure/Flo

w to PC C 2. 3 PC C Mai n Burne r PilotFailur

e 2. 4 Loss o f

Wast e Flo w to PC C Injecto

r 2. 5 Los s o f

Wast e Feedrat

e Contro l to PC C Injector

. 2. 6 Loss o f

Atomizatio

n Ai rPressur

e t o a PC C Injecto

r 2. 7 Los s o f

PC C Draf

tContro l (Uni t4 ) 2. 8 Los

s o f PC C Temperatur

e Contro l 2. 9 Flam

e Failur e 2.10 Ki m Rotatio

n Malfunction (Uni

t4 ) 2.1 1 Bulk/Charg

e Fee d Doo r Malfunctio

n 2.1 2 Physical/Mechanica l Interna l Equipmen

tFailur e 2.1 3 PC C Sea

l Visua l Emission

s Monitoring an

d Recordin

g Syste m 2.14 Rapid Stea

m Generatio

n fro m As h Collectio n Syste m Wate r 3. 0 SECONDAR Y COMBUSTIO N CHAMBE R 3. 1 Los s o f

Natura l Ga s Pressure/Flo

w t o SC C Mai n Burne

r '3. 2 Los s o f

Combustio

n Ai rPressure/Flo

w t o SC C 3. 3 SC C Mai n Burne r Ignitio n Failur e 3. 4 Loss o f

Wast e Flo w t o SC C Injecto

r (Unit4 ) 3. 5 Los s o f

Wast e Feedrat

e Contro l t o SC C Injecto

r (Uni t4 ) 3. 6 Loss o f

Atomizatio

n Ai rPressur

e t o a SC 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

tFailur e 3.1 0 Lo w Wate

r Leve l i n Slag Collection Syste m (Unit4

) 3.1 1 Emergenc

y Safet y Ven tOpenin g 3.12 Rapi d Stea

m Generatio

n fro m As h Collectio n Syste m Wate r 4. 0 TEMPERIN G CHAMBE R(UNI T 4 ) 4. 1 Los s o f

Temperin

g Chambe

r Exi tGa s Temperatur

e Contro l 4. 2 Los s o f

Atomizatio

n Ai rPressur

e t o Nozzl e 5. 0 . LIM E SLURR Y SYSTE M 5.1 . Los s o f

Lim e Fee

d t o Lime Slurr

y Feed Tan

k 5.2 . Malfunction i n Lim e Slurr y Concentratio

n 6.0 - UNIT S 2 AN D 3 SPRA Y DRYE RABSORBER.(SDA ) 6.1 . Los s o f

Lim e Slurr

y Flo w t o SD A

V E S 00202 36.2. Loss o f Lim e Slurr

y Flo w Contro

l 6.3 . Loss o f

City Wate

r Flow t o SD A (Unit2 an

d 3 ) 6.4. Loss o f

Coolin g Ai rFlow t

o Atomize

r 6.5 . Los

s o f SD A Exi tGa

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 t o SD A 7.2. Loss o f

Lim e Slurr

y Flo w Control/Exi

tGa s Temperatur

e Contro l 7.3. Loss o f

Atomization Ai rPressur e t o SD A Nozzl e 8. 0 CARBO N INJECTIO N SYSTE M (UNI T 4 ) 8.1 . Los s o f

Carrie r Ga s Pressur e 8.2 . Loss/Restrictio

n of-Activate

d Carbo n Flo w 8.3. . Los

s o f Plan tAi r Pressure/Flo

w to Carbo

n Bul k Sac

k 9. 0 BAGHOUS E & INDUCE D DRAF T (ID ) FA N 9.1 . Torn/Leakin

g Ba g 9.2. Bag Blinding/High-Higb . Pressur e Dro p 9.3 . Los

s o f Stac k Ga s Flowrat

e Contro l (Unit2 an

d 3 ) 9.4. Baghous

e Isolatio

n Dampe

r Malfunctio

n (Unit4 ) 9.5. I

D Fa n Failur e 10. 0 CONTRO L SYSTEM/CONTINUOU S MONITORIN G SYSTE M 10.1 . Contro

l SystenyCtontinuou

s Monitorin

g Syste m Malfunction 10.2 . Continuou

s Emission

s Monitorin

g Syste m Malfunction

V E S 00202 4ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

GENERA L 1.1 . Operatin g an dMaintainin g th e Syste mdurin g Malfunction s 1.1.1 . Du e to the sudden , infrequent , an dunusual condition s associate d wit h malfunctions , continuall y evaluat e th e situation ; Usin g discretion , respon di n amanne r consistent

wit h safet

y an dgoo dai r pollutio n contro l practices . 1.1.2 . Tak e th e followin g action s t o minimiz e th

e releas e o f

hazardou s ai r pollutant s 1.1.2.1 . Cutof

f al l wast e feed s and/or

confir mtha

t th e automati c wast e fee dcutof

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

applicable , follo w the procedure s provide db y th e Emergency Safety Vent

Plan. 1.1.3 . Kee p superviso r and/or maintenanc e superviso r informed , a s appropriate . 1.1.4 . Identif

y the malfunctio n andpotentia l cause . 1.1.5 . Implement

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 dthe appropriat e informatio n usin g amalfunctio n recor d form . 1.2 . Los s o f

Electrica l Powe r

Suppl y 1.2.1 . Verif y prope r

failur e positio n o f

actuate dvalves . 1.2.2 . Identif

y lin k i n power suppl y pat

h tha t i s no t operational . 1.2.3 . Take th e necessar y action s to restor

e th e suppl y o f

electrica l power . 1.3 . Los s o f

Instrument/Plan t

Ai r Suppl y 1.3.1 . Verif y proper

failur e positio n p 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 the restrictio n o f instrument

a h flow . 1.3.2.2 . Clea r

lin e pluggin g and/or

service/replac e fault y lin e components , as needed . Pag e 1 of2 6ONY X 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 d valve : 1.3.3.1 . Identif

y caus e o f

actuatio n failure . 1.3.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 1.3.3.3 . Service/replac e actuator and/or valv e components , a s . 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 . Take th e necessar y action s t o restor

e th e suppl y o f instrument/plant

air . 1.4 . Los s o f

Plan t Nitroge n 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 the location/caus e o f

th e restrictio n o f

nitroge n flow. 1.4.1.2 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 1.4.2 . I n cas e o f

mechamcaVelectrical failur e o f actuate d valve : 1.4.2.1 . Identif

y caus e o f

actuatio n failure . 1.4.2.2 . Service/replac e electrica l and/or pneumati c components' , a

s needed . 1.4.2.3 . Service/replac e actuator and/or valv e components , a s 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

the failure . 1.4.3.2 . Take th

e necessar

y action s t

o restor e th e suppl y o f nitrogen . 1.5 . Los s o f

Cit y Wate r

Suppl y 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 . Clear

lin e pluggin g and/or

service/replac e fault y lin e components , a

s needed . 1.5.2 . I n cas e o f

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

y caus e o f

actuatio n failure . 1.5.2.2 . . Service/replac e electrica l and/or pneumati c components , a

s needed . Pag e 2 o f 2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O FCORRECTIV E ACTION S FO RMALFUNCTION S

1.5.2.3 . Service/replac e actuator and/o r valv e components , a

s needed . 1.5.3 . I n cas e o f

mechanical/electrical failur e a t cit y wate r

suppl y source : 1.5.3.1 . Identif

y th e caus e ofth e failure . 1.5.3.2 . Tak e th

e necessar

y action s to restor

e th e suppl y o f

cit y water . 1.6 . Los s o f

Proces s Wate r

Pressure/Flo w (Uni t

4 ) 1.6.1 . Fo r

los s ofcit y wate

r suppl y t o proces s water

tank , se e 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 t o fh 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 the locatio n o f

pluggin g or

lin e failure . 1.6.3.2 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 1.6.4 . I n cas e o f

mechanical/electrica l failur e o f actuate d valve : 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 , a

s needed . 1.6.4.3 . Service/replac e actuator and/o r valv e components , a

s 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 Interloc k

o r Automati c Wast e Fee d Cutof f Interloc k 1.7.1 . I f safet y interloc k

or AWFC O interloc k

wa s erroneousl y triggered , procee dwit h correctiv e actions . 1.7.2 . I f safet y or AWFC O conditio n exist s bu t automate d respons e failed , cutof

f wast e feed as quickl y as possible , the n procee d wit 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/replac e fault y instrumentatio n components , as

needed . Pag e 3 o f 2 6ONY X 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/electrical 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/or pneumati c components , a

s needed . 1.7.4.3 . Service/replac e actuator and/or valv e components , a

s 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 mcomponen t 1.7.5. 2 Service/replac e contro l syste mcomponents , a s needed . 1.8 . Excessiv e Ai r

In-leakag e i n Ai r

Pollutio 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

systemas.needed . 1.8. 2 I n cas e o f

open 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 6ONY X 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 o f

Natura l Ga s 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 o r 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 . Clear

lin e pluggin g and/or

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

mechamcal/electrical failur e o f actuate d valve : 2.1.2.1 . Identif

y caus e o f

actuatio n failure . 2.1.2.2 . Service/replac e electrica l and/or pneumati c components , as needed . 2.1.2.3 . Service/replac e actuator 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 . LIdentif

y fault y contro l syste mcomponen t 2.1.3.2 . Service/replac e contro l syste mcomponents , a s needed . 2.1.4 . I n cas e o f

mechahical/electrica l failur e a t natural ga

s suppl y source : 2.1.4.1 . " Identif

y th e caus e o f

the failure . 2.1.4.2 . Take th

e necessar

y action s t

o restor e the suppl y o f natura l gas . 2.2 . Los s o f

Combustio n Ai r

Pressure/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, a s 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 a h 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 , a s needed . 2.2.3 . I n cas e o f

mechanical/electrica l failur e o f actuate d valve : 2.2.3.1 . ' Identif

y caus e o f

actuatio n failure . : 2.2.3.2 . Service/replac e electrica l and/or pneumati c components, , a

s needed . . 2.2.3.3 . Service/replac e actuator and/o r valv e components , as needed . Pag e 5 o f 2 6ONY X 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 , a s needed . 2.3 . PC C Mai n Burne r Pilo t Failur e 2.3.1 . Fo r

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

los s o f combustio n ai r

pressure/flow , se

e 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/or 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 syster

h component . 2.3.4.2 . Service/replac e contro l syste mcomponents , a s needed . 2.4 . Los s o f

Wast e Flo w 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 , a s needed . 2.4.1.3 . Restor

e electrica l power

suppl y to th e pump . 2.4.2 . I n cas e o f

lo w nitroge n pressure , see 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/or

service/replac e fault y lin e components , a

s needed . 2.4.3.3 . Restoreyconfir 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 d valve : 2:4.4,1 . Identif

y caus e o f

actuatio n failure . 2.4.4.2 . Service/replac e electrica l and/or pneumati c components , as needed . 2.4.4.3 . Service/replac e actuator and/or 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 , a s needed . 2.5 . Los s o f

Wast e Feedrat e Contro l t o PC C Injecto r 2.5.1 . Incas e o f

lossio f wast e pressure/flo w to PC C injector , see 2.4 . Pag e 6 o f 2 6ONY X 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 flow transmitter : Service/replac e flo w transmitter and/o r associate d mstrumentation , a s needed . 2.5.3 . I n cas e o f

actuate d valv e failure : 2.5.3.1 . Identif

y caus e o f

actuatio n failure . 2.5.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 2.5.3.3 . Service/replac e actuator and/or 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/replac e contro l syste mcomponents , a s needed . 2.6 . Los s o f

Atomizatio n Ai r

Pressur e to aPC C Injecto r 2.6.1 . Fo r

atota l los s o f

plant/instrument

ai r supply , se

e 1.3 . 2.6.2 . I n cas e o f

plugging/physica l failur e o f lin e or 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 line , pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 2.6.3 . I n cas e o f

mechanical/physica l failur e o f pressur e contro l valve : Service/replac e pressur

e contro l valve , a

s needed . 2.7 . Los s o f

PC C Draf t

Contro l (Uni t

4 ) 2.7.1 . Incas 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 n pressur

e transmitter : Service/replac e pressur e transmitte

r and/or

associate d mstrumentation , as needed . 2.7.3 . meas e o f

actuate d dampe

r failure : 2.7.3.1 . Identif

y caus e o f

actuatio n failure . 2.7.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 2.7.3.3 . Service/replac e actuator and/or dampe r coinponents , as 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/replac e contro l syste mcomponents , a s needed .

Pag e 7 o f 2 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 2.8 . Los s o f

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

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

los s o f wast e pressure/flo w t o PC C injector , se e 2.4 . 2.8.3 . I n cas e o f

physical/electrica l failur e o f temperatur

e element : 2.8.3.1 . Service/replac e fault y temperatur e elemen

t and/o r associate dinstrumentation , a s 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 , a s 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 detector

component . 2.9.1.2 . Service/replac e flam e detector components , a

s 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 , a s needed . 2.10 . Kil n Rotatio n Malfunctio n (Uni t 4 ) 2 A 0.1 . I n cas e o f

mechanical/electrica l kil n driv e system : 2.10.1.1 . Diagnos e driv e failure . 2.10.1.2 . Service/replac e the drive , as needed . 2.10.1.3 . Restore 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 n rotational spee d transmitter : Service/replac e transmitter and/or 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 , a s needed . 2.11 . Bulk/Charg e Fee dDoo r Malfunctio n 2.11.1 . I n cas e o f

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

y caus e o f

actuatio n failure . 2.11.1.2 . Service/replac e electrical , hydraulic , and/or pneumati c components , a

s needed . 2.11.13 . 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 of2 6ONY X 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 , a s needed . 2.12 . Physical/Mechanica l Interna l Equipmen t Failur e 2.12.1 . I n cas e o f

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

as h collectio n failur e 2.12.2.1 . Diagnos e as h collectio n syste mfailur e 2.12.2.2 . Service/replac e as h collectio n syste mcomponents , a s needed . 2il3 . PC C Sea l Visua l Emission s Monitorin g an dRecordin g Syste m 2.13.1 . In 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 dStea mGeneratio n fro mAs h Collectio n Syste mWate r 2.14.1 . In 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 into as h collectio n syste mwater , inspec t syste mto identify/remov e other suspect material .

Pag e 9 o f 2 6ONY X 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 Ga s Pressure/Flo w to 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 faiiure . 3.1.1.2 . Clea r

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 3.1.2 . I n cas e o f

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

y caus e o f

actuatio n failure . 3.1.2.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 3.1.2.3 . Service/replac e actuator and/o r valv e components , a

s 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 , a s 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 necessar y action s t

o restor e the suppl y o f natural gas . 3.2 . Los s o f

Combustio n Ai r

Pressure/Flo w to SC C 3.2.1 . I n cas e o f

mechanical/electrica l failur e o f combustio n a h blower . 3.2.1.1 . Diagnos e blower/driv e failure . 3.2.1.2 . Service/replac e the blower/drive, as needed . 3.2.1.3 . Restore electrica l powe r suppl y t o the blower . 3.2.2 . I n cas e o f

physica l failur e combustio n a h 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 , a s needed . 3.2.3 . I n cas e o f

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

y caus e o f

actuatio n failure . 3.2.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 3.2.3.3 . Service/replac e actuator and/o r valv e components , as needed . Pag e 1 0 o f

2 6ONY X EFTvTRONMENTA 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 , a s needed . 3.3 . SC C Mai n Burne r Ignitio n Failur e 3.3.1 . Fo r

los s o f natura l gas pressure/flow , see 3.1 . 3.3.2 . Fo r

los s o f combustio n ai r

pressure/flow , se

e 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 d components , a s 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 o f

Wast e Flo w to SC C Injecto r (Uni t 4 ) 3.4.1 . I n cas e o f

mechanical/electrica l failur e o f wast e fee d pump : 3.4.1-1 . Diagnos e pump/driv e failure . 3.4.1.2 . Service/replac e tb e pump/drive , a s needed . 3.4.1.3 . Restore electrica l powe r suppl y t o m e 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 or fine component : 3.4.3.1 . Identif

y tb e locatio n o f

pluggin g o r

lin e failure . 3.4.3.2 . Clea r

lin e pluggin g and/or

service/replac e fault y lin e components , as 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 d valve : 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 actuator.and/o r valv e components , a

s 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 , a s needed . 3.5 . Los s o f

Wast e Feedrat e Contro l t o SC C Injecto r (Uni t 4 ) 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 6ONY X 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/replac e flo w transmitte r and/or associate d instrumentation , a s needed . 3.5.3 . I n cas e o f

actuate d valv e failure : 3.5,3.1 . Identif

y caus e o f

actuatio n failure . 3.5:3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 3.5.3.3 . Service/replac e actuator and/or valv e components , as needed . 3.5.4 . . In 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 systemcomponent . 3.5.4.2 . Service/replac e contro l systemcomponents , a s needed . 3.6 . Los s o f

Atomizatio n Ai r

Pressur e t o aSC C Injecto r 3.6.1 . Fo r

atota l los s o f

plant/instrument

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 m e locatio n o f

pluggin g o r

lin e failure . 3.6.2.2 . Clear

lin e plugging and/or

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

mechanical/physica l failur e o f pressur e contro l valve : Service/replac e pressur

e contro l valve , a

s needed . 3.7 . Los s o f

SC C Temperatur e Contro l 3.7.1 . meas e o f

los s o f natural ga s pressure/flo w t o mai n burner , see 3 .1 . 3.7.2 . I n cas e o f

los s o f wast e pressure/flo w t

o SC C in j ector , see 3.4 . 3.7.3 . I n cas e o f

physical/electrica l failur e o f temperatur

e element : 3.7.3.1 . Service/replac e fault y temperatur e elemen

t and/o r associate d instrumentation , a s 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 systemcomponents , a s 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 detector

componen t 3.8.1.2 . Service/replac e flam e detector 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 6ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

3.8.2.2 . Service/replac e contro l syste mcomponents , as needed . 3.9 . Physical/Mechanica l Interna l Equipmen t Failur e 3.9.1 . In cas e o f

refractory failure , repair/replac e refractory . 3.10 . Lo w Wate r

Leve l i n Sla g Collectio n Syste m(Uni t 4 ) 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 . In cas e o f

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

y caus e o f

actuatio n failure . 3.10.3.2 . Service/replac e pneumati c components , as needed . 3.10.3.3 . Service/replac e actuato r and/or valv e components , a

s needed . 3.11 . Emergenc y Safet y Ven t Openin g 3.11.1 . Respon dt

o a n emergenc y safet

y ven t openin g i n amanne r consisten t wit h the Emergency Safety Vent Plan. 3.11.2 . I n cas e o f

mechanical 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/replac e emergenc y safet y vent components , a s needed . 3.12 . Rapi dStea mGeneratio n fro mAs h Collectio n Syste mWate r 2.14.1 . I n cas e o f refractory 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 systemwater , inspec t systemto identify/remov e othe r suspect material .

Pag e 1 3 o f

2 6

V E S 00203 7ONY X 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 o f

Temperin g Chambe r

Exi t Ga s Temperatur e Contro l 4.1.1 . Fo r

alos s o f proces s water

pressure/flow , se

e 1.6 . 4.1.2 . I n cas e • o f

physical/electrica l failur e o f flow transmitter : Service/replac e flo w transmitte r and/o r associate d instrumentation , a s needed . 4.1.3 . In cas e o f

actuate d valv e failure : 4.1.3.1 . Identif

y caus e o f

actuatio n failure . 4.1.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 4.1.3.3 . Service/replac e actuato r and/or valv e components , a

s needed . 4.1.4 . I n cas e o f

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

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

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

Atomizatio n Ai r

Pressur e t

o Nozzl e 4.2.1 . Fo r

atota l los s o f

plant/instrument

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 the locatio n o f

pluggin g or

lin e failure . 4.2.2.2 . Clea r

lin e pluggin g and/or

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

Pag e 1 4 o f

2 6ONY X 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 Fee dto Lim e Slurr y Fee dTan k 5.1.1 . In cas e o f

mechanical/electrical failur e o f lim e slurr y screw feeder : 5.1.1.1 . Diagnos e feeder/driv e failure . 5.1.1.2 . Service/replac e th e feeder/drive , a

s needed . 5.1.1.3 . Restore electrica l powe r suppl y to m

e lim e slurry ser

e 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 . Restore electrica l powe r suppl y t o the lim e slurry 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 , a

s needed . 5.1.4 . I n cas e o f

physical/electrica l failur e o f lim e fee dcontrols : Service/replac e fault y mstrumentatio n and/or control , syste m components , a s needed . . 5 .2 . Malfunctio n i n Lim e Slurr y Concentratio n .5.2.1 . I n cas e oflossoflim e fee dt o time slurr y fee dtank , se e 5. 1 5.2.2 . I n cas e o f

los s o f wate r flo w t o 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 slurry agitator : 5.2.3.1 . Diagnos e agitator/driv e failure . 5.2.3.2 . Service/replac e the agitator/drive , as needed . 5.2.3.3 . Restore electrica l powe r suppl y to the lim e slurry agitator . 5.2.4 . I n cas e o f

physical/electrica l failur e o f instrumentation : Service/replac e 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 faulty contro l syste mcomponent . 5.2.5.2 . Service/replac e contro l syste mcomponents , a s needed . Pag e 1 5 o f

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

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 A 6.1.1 . In cas e o f

mechanical/electrical failur e o f lim e slurry fee dpump : 6.1.1.1 . Diagnos e pump/driv e failure . 6.1.1.2 . Service/replac e th e pump/drive , a s needed . 6.1.1.3 . Restor

e electrica l powe r

suppl y t o 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.L2.2 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed . 6.1.2.3 . Restore/confirmfunctiona l hea t tracing , i f

applicable . 6.1. 3 . I n cas e o f

mechanical/electrical failur e o f actuate d valve : 6.1.3.1 . Identif

y caus e o f

actuatio n failure . 6.1.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . 6.1.3.3 . Service/replac e actuator and/or valv e components , a

s needed . ' 6.1.4 . In 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 mcomponen t 6.1.4.2 . Service/replac e contro l syste mcomponents , a s 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 slurry flo w t

o SDA , see 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/p r associate dinstrumentation , a s needed . 6.2.3 . I n cas e o f

actuated valv 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/or pneumati c components , a

s needed . 6.2.3.3 . Service/replac e actuator and/or valv e components , a s 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 faulty contro l syste mcomponent . 6.2.4.2 . Service/replac e contro l syste mcomponents ; a s needed . Pag e 1 6 o f

2 6

V E S 00204 0ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 6.3 . Los s o f

Cit y Wate r

Flo w to SD A (Uni t

2 an d3 ) 6.3.1 . I n cas e o f

total 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 m e locatio n o f

pluggin g o r

lin e failure . 6.3.2.2 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s 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 , a

s needed . 6.3.3.3 . Service/replac e actuato r and/or valv e components , as needed . 6.4 . Los s o f

Coolin g Ai r

Flo w t o Atomize r 6.4.1 . I n case " 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 t o 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 ttie locatio n o f

duc t failure . 6.4.2.2 . Service/replac e fault y duct , a s needed . 6.4.3 . Incas 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 , a s needed . 6.5 . Los s o f

SD A Exi t

Ga s Temperatur e Contro l 6.5.1 . I n cas e o f

los s o f cit y water

flo w t o SDA , se e 6.3 . 6.5.2 . I n cas e o f

physical/electrica l failur e o f temperatur

e transmitter : Service/replac e temperatur e transmitter

and/or

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

actuatedvalv 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 , a s 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 6ONY X 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 , a s needed . 6.6 . Atomize r

Failur e 6.6.1 . I n cas e o f

lo w atomizer

lubricatio n oi l flow : 6.6.1.1 . Diagnos e the failur e i n the 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 , a s needed . 6.6:2.3 . Restore electrica l powe r suppl y t o th e atomizer . 6.6.2.4 . components , a s needed .

Pag e 1 8 o f

2 6ONY X 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

Lim e Slurr y Flo w t o SD A 7.1.1 . I n cas e o f

mechamcaVelectrical 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 , a

s needed . 7.1.1.3 . Restore electrica l powe r suppl y t o the 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 or

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 d valve : 7.1.3.1 . Identif

y caus e o f

actuatio n failure . 7.1.3.2 . Service/replac e electrica l and/or pneumati c components , a s needed . 7.1.3.3 . Service/replac e actuato r and/o r valv e components , a s 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 mcomponen t 7.1.4.2 . Service/replac e contro l syste mcomponents , a s needed . 7.2 . Los s o f

Lim e Slurr y Flo w Control/Exi t Ga s Temperatur e Contro l 7.2.1 . I n cas e o f

los s o f slurr y flo w t

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 transmitter and/o r associate dinstrumentation , a s needed . 7.2.3 . I n cas e o f

actuate d valv 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 , a

s needed . 7.2.3.3 . Service/replac e actuator and/or 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 , a s needed . Pag e 1 9 o f

2 6ONY X ENVIRONMEN T A X SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S 7.3 . Los s o f

Atomizatio n Ai r

Pressur e to SD A Nozzl e 7.3.1 . Fo r

atotal los s o f

plant/instalmen t

ai r supply , se e 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 the locatio n o f

pluggin g o r

lin e failure . 7.3.2.2 . Clear

lin e pluggin g and/o r

service/replac e fault y lin e components , a

s needed .

Pag e 2 0 o f

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

S. O CARBO N INJECTIO N SYSTE M (UNI T 4 ) 8.1 . Los s o f

Carrie r Ga s 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 the blower/drive , a s needed . 8.1.1.3 . Restore electrica l powe r suppl y t o 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 , a s needed . 8.1.3 . I n cas e o f

physicaVelectrica 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 o f Activate dCarbo n Flo w 8.2.1 . I n cas e o f

los s o f plan t ai r t o 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 , a s needed . 8.2.2.3 . Restore electrica l powe r suppl y to the carbp n feeder . 8.2.3 . I n cas e o f

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

y the 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 , a

s needed . 8.2.3.3 . Restore/confir mfunctiona l hea t tracing , i f

applicable . 8.3 . Los s o f

Plan t Ai r Pressure/Flo w t o Carbo n Bul k Sac k 8.3.1 . Fo r

atotal los s o f

plant/instrument

ai r supply , see 13 . 8.3.2 . In 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 . 83.2.2 . Clea r

lin e plugging and/o r

service/replac e fault y lin e components , a

s needed . 83.3 . I n cas e o f mechanical/electrica l failur e o f actuate d valve : 8.3.3.1 . Identif

y caus e o f

actuatio n failure . 8.3.3.2 . Service/replac e electrica l and/or pneumati c components , a

s needed . Pag e 2 1 o f

2 6

V E S 00204 5ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

8.3.3.3 . Service/replac e actuator and/or valv e components , a s 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 .

Pag e 2 2 o f

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

BAGHOUS E & INDUCE D DRAF T (TD ) 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 relevant 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 lea

k detectio n syste mfailure : 9.1.2.1 . Service/replac e torn/leakin g bag(s) , a s needed : 9.1.2.2 . Diagnos e the failur e o f the baghous e detectio n system . 9.1.2.3 . Service/replac e baghous e lea k detectio n system , as needed . 9.2 . Ba g Bunding/High-Hig h Pressur e Dro p 9.2.1 . I n cas e of'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 h 6. 5 (Uni t

2 an d3 ) 9.2.1.2 . Follo w th e appropriat e correctiv e action s prescribe db y paragrap h 7. 2 (Uni t

4 ) 9.2.1.3 . Perfor mbaghous e inspection . 9.2.1.4 . Service/replac e bag(s) , as needed . 93. Los s o f

Stac k Ga s Flowrat e Contro l (Uni t 2 an d3 ) 9.3.1 . I n cas e o f

E D fa n failure , se

e 9. 5 9.3.2 . I n eas e o f

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

actuate ddampe

r failure : 9.3.3.1 . Identif

y caus e o f

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

s needed . 9.3.3.3 . Service/replac e actuato r and/or dampe r 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 , a s needed . 9.4 . Baghous e Isolatio n Dampe r Malfunctio n (Uni t

4 ) 9.4.1 . I n cas e o f

actuate ddampe

r failure : Pag e 2 3 o f

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

9.4.1.3 , 9.4.1. 1 9.4.1.2 . Identif

y caus e o f

actuatio n failure . Service/replac e electrica l and/or pneumati c components , as needed . Service/replac e actuator and/or dampe r components , as needed . 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 , a s needed . 9.5 . I D Fa n Failur e 9.5.1 . I n cas e o f

mechanical/electrica l failur e o f E D fan : 9.5.1.1 . Diagnos e fan/driv e failure . 9.5.1.2 . Service/replac e the fan/drive , a s needed . 9.5.1.3 . Restore electrica l powe r suppl y t o th e E D fan .

Pag e 2 4 o f

2 6ONY X 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/Continuou s Monitorin g Syste mMalfunctio n 10.1.1 . A s needed , refe r to th e CMS

QA/QC Plan fo r

guidanc e andt o ensur e tha t prope r cahbration 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 mstrumentatio 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 mcomponen t 10.1.3.2 . Service/replac e contro l systemcomponents , as needed . 10.1.4 . In cas e o f

physical/electrica l failur e o f dataacquisition/availabihty : 10.1.4.1 . Identif

y fault y datasystemcomponents . 10.1.4.2 . Service/replac e datasystemcomponents , a s needed . 10.2 . Continuou s Emission s Monitorin g Syste mMalfunctio n 10.2.1 . A s needed , refer to th e CEMS

QA/QC Plan fo r

guidanc e an dt o ) ensur e tha t prope r calibration s ar

e performe dan dtha

t th e appropriat

e performanc e specification s ar e met . 10.2.2 . h i 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/restore hea t trace d sampl e umbilical . 10.2.3 . I n cas e o f

mechanical/electrica l failur e o f heated vacuu mpump : 10.2.3.1 . Diagnos e pump/driv e failure . 10.2.3.2 . Service/replac e th e pump/drive , a

s needed . 10.2.3.3 . Replace/restore pum p hea d hea t source . 10.2.3.4 . Restor

e electrica l power

suppl y to heate d vacuu 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 th e locatio n o f

failure . 10.2.4.2 , Clear

pluggin g and/or

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

mechanical/electrica l failur e o f actuated valve : 10.2.5.1 . Identif

y caus e o f

actuatio n failure .

Pag e 2 5 o f

2 6

V E S 00204 9ONY X ENVIRONMENTA L SERVICES , INC . PROGRA M O F CORRECTIV E ACTION S FO RMALFUNCTION S

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

mechamcaVelectrical failur e o f analyzer : 10.2.6.1 . Refe r

t o manufacturer' s servic e manual fo r guidanc e o n troubleshootin g an

dservicin g analyzer . 10.2.6.2 . Service/replac e analyzer , a s 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 mcomponen t 10.2.8.1 . Identif

y fault y contro l syste mcomponen t 10.2.8.2 . Service/replac e contro l syste mcomponents , a s needed .

Pag e 2 6 o f

2 6

### OPERATIO N AN D MAINTENANC E PLA N

Prepare d for : Ony x Environmenta

l Services , Inc. Sauget , Illinoi s

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

Jun e 200 4TABL E O FCONTENT S

1. 0 INTRODUCTION . . 1 1 . l REGULATOR Y REQUIREMENT S 2. 1. 2 RECORDKEEPIN G 2 2. 0 NORMA L OPERATION S O FTH E INCINERATORS... . 2 3. 0 BA G LEA K DETECTIO N SYSTE M , . . 5 3. 1 CORRECTIV E MEASURE S FO RBA G LEA K DETECTIO N ALARM S 7 4. 0 INSPECTIO N AN D MAINTENANC E 9 5. 0 ALTERNATIV E MOD E O FOPERATIO N . . 1 2 5. 1 WAR M STAND-B Y MOD E O FOPERATIO N 1 2 5. 2 APPLICABL E REQUIREMENT S 1 3

V E S 00205 2LIS T O FTABLE S TABL E 1- 1 OPERATIO N AN D MAINTENANC E PLA N REGULATOR Y CHECKLIS T 1 TABL E 2- 1 LIS T O FSTANDAR D DIVISIONA L PRACTICE S 3 TABL E 3- 1 BAGHOUS E LEA K DETECTIO N SYSTE M SPECIFICATION S 6 TABL E 4- 1 INSPECTIO N AN D MAINTENANC E T O PREVEN T MALFUNCTION S 1 0

i i

V E S 00205 31. 0 INTRODUCTIO N Ony x Environmental Services , Inc . (Onyx ) own s an doperate s thre e hazardou s wast e incinerator s a

t it s facilit y locate di n Sauget , Illinois . Th e incinerator s ar e subjec t to the Nationa l Emission s Standard s fo r Hazardou s Ai r

Pollutant s (NESHAP ) fo r Hazardou s Waste Combustor s (HWC) , codifie das 4 0 CFR , Part 63 , Subpar

t EE E ( § 63.120 0 t

o § 63.1213) . Th e NESHA P fo r HW C specifie s emission s standard s whic h reflec t emission s performanc e o f

Maximu mAchievabl e Contro l Technologie s (MACT) , an di s commonl y referre dt o a s th e HW C MACT . Th e mteri mHW C MAC T Standar drequire s tha

t Ony x operat

e an dmaintai n th e incinerator s i n amanne

r consistent

wit h safet

y an dgoo dai r

pollutio n contro l practice s fo r minimizin g emission s base do n paramete r limit s achieve ddurin g th e comprehensiv e performanc e test . T o mee t thi s objective , Ony x ha s develope dthi s operatio n an d maintenanc e (O&M ) plan . Ony x wil l utiliz e thi s O& M pla n fo r period s o f

norma l operatio n o f

the incinerators . Durin g period s o f startup , shutdown , an dmalfunction , Ony x wil l utiliz e th e Startup, Shutdown, and Malfunction Plan (SSMP) . Durin g period s o f startup , shutdown , an dmalfunction , conformanc e wit h th e SSM P satisfie s the dut y t o nnnimiz e emissions . Bot h th e O& M pla n an dSSM P ar e maintaine da

t the facihty . Th e purpos e o f

thi s O& M pla n i s to :

• Describ e procedure s fo r operatin g the incinerato r durin g norma l operations . • Describ e procedure s fo r inspectio n an dmaintenanc e o f tb e incinerator . • Describ e procedure s fo r correctiv e measures . • Estabhs h guideline s designe dt o ensur e tha t emission s o f

pollutants , automati c wast e fee dcutoff

s (AWFCOs) , an dmalfunction s ar e minimized . • Satisf y the requirement s o f

§ 63.1206(c)(7 ) an d§ 63.6(e) , a s show n i n Tabl e 1- 1 o f thi s plan . Du e to the similarit y ofth e thre e incinerato r systems , genera

l reference s to a

n incinerato r i n thi s documen

t wil l impl y al l three incinerato r systems . Informatio n tha t i s onl y apphcabl e t

o on e o r tw o ofth e three unit s wil l b e clearl y identified .

11. 1 Regulator y Requirement s On e o f th e objective s fo r

thi s documen

t i s to establis h aprogra mtha t wil l ensur

e complianc e wit h relevan t section s o f

the Interi mHW C MAC T standard . Tabl e 1- 1 provide s th

e regulator

y requhement s an dlocatio n withi n thi s documen t wher e eac h requirement

i s addressed . Thi s tabl e i s include dt o facilitat e fh e expeditiou s assessmen t o f thi s plan' s coverag e o f

th e relevant

regulator y requirements . 1 . 2 Recordkeepin g Ony x wil l maintai n file s t o compl y wit h th e recordkeepin g requirement s o f th e Interi m MAC T Standards . Thes e requhement s ar e summarize di n 4 0 CF R63.1211(b) . Th e files relevant to thi s pla n tha

t ar e maintaine di n th e operatin g recor dinclude :

• Thi s O& M Plan ; • Record s o f

al l requhe dpreventiv e andnecessar y maintenanc e performe do n th e ai r pollutio n contro l an dmonitorin g equipment ; an d

• Record s o f

al l adjustment s an dmaintenanc e performe do n th e continuou s monitorin g syste

m(CMS) .

2

V E S 00205 5Tabl e 1- 1 Operatio n an d Maintenanc

e Pla n Regulator

y Checklist Regulator y Citatio n Descriptio n Locatio n Addresse d 63.6(e)(l)(i ) Implemen t safet y an dgoo dai r

pollutio n contro l practice s fo r

mimmizin g emission s 1.0,2. 0 63.6(e)(l)(ii ) Compl y wit h SSM P an dminimiz e emission s durin g SS M 1. 0 63.6(e)(l)(iii ) O & M requirement s establishe dpursuant to sectio n 11 2 ofth e CA A 2. 0 63.6(e)(3 ) Startup , shutdown , an dmalfunctio n pla n 1.0 , SSMP 1 63.10(b)(1 ) Mamtahun g file s 1.2 63.10(b)(2)(iii ) Record s o f al l requhe dmaintenanc e o f AP C an d monitorin g equipmen

t 1. 2 63.10(b)(2)(xi ) Record s o f al l adjustment s an dmaintenanc e performe d o n CM S 1.2 63.1206(c)(7)(i)(A ) Prepar e an doperat

e unde r O& M pla n 1. 0 63.1206(c)(7)(i)(A ) Procedure s fo r operatin g combustio n system component s tha

t coul daffec t

emission s 2. 0 Tabl e 2- 1 63.1206(c)(7)(i)(A ) Procedure s fo r inspectin g combustio n system component s tha

t coul daffec t

emission s 4. 0 63.1206(c)(7)(i)(A ) Procedure s fo r maintenanc e combustio n system component s tha

t coul daffec t

emission s 4. 0 63.1206(c)(7)(i)(A ) Correctiv e measure s fo r combustio n syste m component s tha

t coul daffec t

emission s 2.0,3.1 , SSMP 1 63.1206(c)(7)(i)(B ) Goo dai r pollutio n contro l practice s fo r minimizin g emission s 1.0 , 2. 0 63.1206(c)(7)(i)(C ) O & M pla n ensure s comphanc e wit h O& M requhement s o f

63.6(e ) 1. 0 63.1206(c)(7)(i)(C ) O& M pla n minimize s emission s o f pollutant s 1.0 , 2. 0 63.1206(c)(7)(i)(C ) O & M pla n minimize s AWFCO s 1.0,2. 0 63.1206(c)(7)(i)(C ) O & M pla n minimize s malfunction s 1.0 , 4. 0 Tabl e 4- 1 63.1206(c)(7)(i)(D ) O& M pla n i s recorde di n operatin g recor d 1.2

1 Th e Startup, Shutdown

, an d Malfunctio

n Pla n (SSMP) i

s a stand-alon

e document

, incorporate

d b y reference

.

V E S 00205 6Tabl e 1- 1 (confirmed ) Operatio n an dMaintenanc e Pla n Regulator y Checklis t Regulator y Citatio n Descriptio n Locatio n Addresse d 63.1206(c)(7)(h ) I f systemequippe dwit h abaghouse , ba g lea k detectio n systemrequhe d 3. 0 63.1206(c)(7)(ii)(A)(l ) Detec t an drecordP M emission s a t adequat e sensitivity 3. 0 63.1206(c)(7)(ii)(A)(2 ) Output relativ e particulate matte r loading s 3. 0 63.1206(c)(7)(ii)(A)(3 ) Audibl e alar mi f loadin g detecte d over

limi t 3. 0 63.1206(c)(7)(ii)(A)(4 ) Compl y wit h U S EP A guidanc e o r manufacturer' s informatio n fo r

installatio n an doperatio n 3. 0 63.1206(c)(7)(ii)(A)(5 ) Initia l adjustment s o f the system : baseline , averagin g period , alar

mse t poin t an ddela y tim e 3. 0 63.1206(c)(7)(ii)(A)(6 ) O & M pla n specifie s allowabl e adjustment s 3.0,3. 1 63.1206(c)(7)(ii)(A)(6 ) Limit s to sensitivity adjustment s 3. 0 63.1206(c)(7)(ii)(A)(7 ) Installatio n locatio n requhement s 3. 0 63.1206(c)(7)(ii)(B ) Procedure s fo r respondin g to ba g leak

detectio n systemalar

m 3. 1 63.1206(c)(7)(ii)(B)(l ) Initiatio n o f procedure s to determine alarmwithi n 3 0 minute s 3. 1 63.1206(c)(7)(ii)(B)(2 )

• Necessar y correctiv e measure(s ) to alleviat e caus e o f alar m 3. 1

12. 0 NORMA L OPERATION S OFTH E INCINERATOR S Tabl e 2- 1 presents alis t

o f title s fo r Onyx' s Standar

dDivisiona l Practice s (SDPs) . Thes e SPD s provid e procedure s fo r operatin g the incinerato r i n amanne

r consistent

wit h safet

y an dgoo dai r

pollutio n contro l practices . Utilizin g thes e SDPs , proces s knowledge , an d discretion , operator s wil l maintai n th e incinerato r operatin g parameters withi n permissibl e limits , i f

possible . Operatin g the incinerato r i n thi s manne

r wil l minimiz e th

e occurrenc e o f

AWFCO s an dmhhmiz e the emission s o f hazardou s ai r

pollutants . A l l applicabl e operatin g requirement s fo r tb e incinerator , includin g operatin g paramete r limit s (OPLs) , ar

e specifie di n Onyx' s Documentation of Compliance (DOC ) o r Notification of

Compliance, whicheve r i s currentl y applicable . Norma l operation s ofth e incinerato r

wil l b e i n compliance ' wit h thes e requirements . . Ony x ha s develope dPipin g an dLnstrumentatio n Diagram s (P&IDs) , Proces s Flo w Diagram(PFDs) , an

dtechnical description s fo r eac h incinerator . Thes e resource s i n conjunctio n wit h M S PowerPoint ® presentation s ar e integral part s o f

operatin g training . Wit h thi s framing, operator s gai n the understandin g o f alarms , interlocks , a

s wel l a s the automatedresponse s associate dwit h eac h interlock . Knowledg e o f alarm s an dinterlock s an dacces s t o proces s variabl e indication , prepare s th e operator

t o perfor mthe appropriat e correctiv e measure s snout dcondition s deviate fromnorma l operations . Th e correctiv e measure s taken wil l b e the operator' s effort s t o ensur e safet y an dto maintai n operatin g parameters withi n limits , i f possible . I f

deviation s fromnorma l operation s ar e cause db y amalfunction , correctiv e measure s wil l b e consistent wit h th e SSM P an dth

e Program of Corrective Actions for

Malfunctions, Attachmen t 4. 0 o f Onyx' s SSMP .Tabl e 2- 1 Lis t o f Standar dDivisiona l Practice s SD P NUMBE R TITL E 101 1 TW I Remedia l Actio n Wor k Order Program 220 0 Specialt y Feede r Operatio n fo r

No . 2/ 3 Incinerator s 220 1 Startup , Operatio n an dShutdow n o f No . 2/ 3 Incinerator s 220 2 Operatio n o f Compresse dGa s Cylinde r Feedin g Syste m 220 3 Operatio n o f Solid s Fee dConveyo r

System s fo r

No . IA Incinerator s 220 4 As h Conveyo r Operatio n fo r

No . 2/ 3 Incinerator s 220 5 Operatio n o f Liqui dFee dInjector s fo r No . 2/ 3 Incinerator s 220 6 No . 2/ 3 Incinerator s Leg s Cleanou t 220 7 No . 2 Incinerator Uppe r Chambe r Fee dSyste m 220 8 No . 2/ 3 Incmerator s Shutdow n Permits , Tagout s an dLockout s 220 9 Operatio n o f Baghous e Filter s fo r

No . 2/3 Incinerators . 221 0 Operatio n o f Compresse dAi r

Syste mfo r

No . 2/3 Incinerator s 221 1 Lim e Slurr y Syste mOperatio n fo r No . 2 an d3 Incine

r ator s 221 2 Spra

y Drye r Absorbe r

Operatio n fo r

No . 2/3 Incinerator s 221 3 Operatio n o f Dr y Scrubber

Solid s Conveyo r

System s fo r

No . 2/ 3 Incinerator s 221 4 Flushin g the Lim e Slurr y Syste mfo r No . 2/ 3 Incinerator s 221 5 Operatio n o f Oxyge n Ga s Cylinde r

Processin g Syste m 221 7 Operatio n o f Specialt y Feeder

Fume Hoo dSyste mfo r No . 3 Incinerato rTabl e 2- 1 (continued ) Lis to f Standar d Divisiona

l Practice

s SD P NUMBE R . . _ .

TITL E 221 9 Lim e Storag e loadin g 222 1 24-Hou r Stagin g o f

Burnabl e Container s o n No . 2/ 3 Incinerator s Doc k 222 2 As h Managemen t fo r No . 2/ 3 Incinerator s 222 4 No . 2/ 3 Incinerator s Direc t

Injec t Syste m 240 1 No . 4 Incinerato r Shutdow n Permits , Tagout s andLockout s 240 2 Mai n Fee dConveyo r Syste mOperatio n fo r

No . 4 Incinerator 240 3 Clamshel l Fee dSyste mOperatio n 240 4 Temperin g Chambe r Operatio n 240 5 Flushin g the Lim e Slurr y Syste mfo r No . 4 Incinerato r 240 6 Operatio n o f Liqui dFee dInjector s fo r No . 4 Incinerator 240 7 Cleanin g th e Proces s Water

Syste mfo r

No . 4 Incinerator 240 8 Operatio n o f Carbo n Injectio n Syste mfo r No . 4 Incinerator 241 6 Lim e Slurr y Syste mOperatio n fo r No . 4 Incinerato r 241 7 Startup , Operatio n an dShutdow n o f No . 4 Incinerator 241 8 Spra

y Drye r Absorbe r

Operatio n fo r

No . 4 Incinerator 241 9 Operatio n o f Direc t Injec t Syste mfo r

No . 4 Incinerato r 242 1 Ai r

Canno n Operatio n fo r

No . 4 Incinerator 242 2 Auxiliar y Fee dConveyo r Syste mOperatio n fo r

No . 4 Incinerator3. 0 BA G LEA K DETECTIO N SYSTE M Ony x utilize s atriboelectri c bag lea k detector t o compl y wit h th

e ba g lea

k detectio n requirement s of63.1206(c) . Th e installatio n an don-goin g operatio n ofth e lea k detectio n systemi s consistent

wit h the U S EP A Fabric Filter Bag Leak

Detection Guidance (EPA

454/R-98-015) . Th e ba g lea k detectio n syste mmonitor s th e relativ e particulat e matte r loadin g o f

th e ga s i n th e duc t

downstrea

mo f th e induce ddraf

t fan . Th e ba g lea

k detectio n systemha s bee n certifie dfro mmanufacturer tha t the systemi s capabl e o f detectin g andrecordin g particulate emission s a t concentration s o f

1. 0 milligra mpe r actua l cubi c meter . Th e sensitivity o f

th e ba g lea k detector i s se t b y selectin g th e relativ e outpu t range . A respons e tim e (i.e. , averagin g period ) i s utilize dt o smoot h fluctuation s i n th e triboelecti c signal . Th e ba g lea

k detectio n systemutilize s tw o alar mse t point s (hig h an

dhigh-high) , whic h ar e se t a s apercentag e o f

the ful l scal e reading . Th e alar mse t point s ar e base do n amultipl e o f

th e baselin e readin g considerin g cleanin g cycl e peaks , i f apparent . Th e high-hig h alar

mi s interlocke dwit h th

e AWFC O system . Th e dela y time s fo r

the alarm s ar e base don th e norma l bag cleanin g puls e cycles . Tb e ba g lea k detectio n syste m setting s ar

e presente di n Tabl e 3-1 . Followin g initia l adjustment s (includin g adjustments , mad e durin g a30-da

y tria l period ) t o the ba g lea

k detectio n system , ther

e wil l b e n o adjustment s t o the sensitivity (range) , averagin g period , alar

mse t point , or

alarmdelay tim e excep t fo r the adjustments made consistent

wit h recommendation s i n Sectio n 5. 3 o f the U S EP A Fabric Filter Bag Leak Detection Guidance (EPA-454/R-98-015) . Periodi c adjustment s t o th e bag lea

k detectio n systemmay b e warrante dt o pievent/mirumiz e th

e occurrenc e o f

fals e alarms . I f

over a 36 5 da y period , the sensitivit y i s increase db y more tha n 100 percen

t o r decrease db y mor e than 5 0 percent , acomplet e baghous e inspectio n an dnecessar y repair s wil l b e performe dt

o assur e goo doperatin g condition .Tabl e 3- 1 Baghouse Lea k

Detectio n Syste mSpecification s Paramete r Uni t 2 Uni t

3 Uni t

4 Rang e 0-1,00 0 0-1,00 0 0-1,00 0 Averagin g Perio d 1 0 second s 1 0 second s 1 0 second s Hig h Alar m 20 % 20 % 10 % Hig h Alar mDela y Tim e 3 minute s 3 minute s 6 minute s ffigh-High Alar m(AWFCO ) 30 % 30 % 15 % High-Hig h Alar mDela y Tim e 6 niinute s 6 minute s 1 2 minute s

6

V E S 00206 23.1 Correctiv e Measure

s fo r Ba g Leak Detectio

n Alarm s Ony x has implemente dthe necessar y proactiv e measure s t o prevent/mhhmiz e th e occurrenc e o f

ba g lea k detectio n alarms . Thes e proactiv e measure s includ e inspection s andpreventiv e maintenanc e o f th e baghous e an dth e ba g lea k detectio n system . Additionally , th e installatio n an doperatio n o f the ba g lea k

detectio n syste mi s consisten t wit h EP A guidance . Despit e thes e efforts , afals e ba g lea k detectio n alarmo r

aba g leak/failur e may occu r

andar e considere dpotentia l malfunctions . Accordingly , thi s sectio n i s acomponen

t o f the SSM P andi s reference db y paragrap h 9.1. 1 o f th e Program of Correction Actions for

Malfunctions, Attachmen t 4. 0 o f Onyx' s SSMP . Th e purpos e o f

thi s sectio n i s t

o prescrib e the procedure s fo r respondin g t

o ba g lea k detectio n alarms . Th e procedure s specifie di n thi s sectio n wil l b e initiate dwithi n 3 0 minute s o f

the tim e th e alar

mfirs t sounds . Th e tim e an dcaus e o f eac h alarmwil l b e recorde do n amalfunctio n recordkeepin g form . A blan k malfunctio n recordkeepin g for m i s Attachmen

t 3. 0 o f Onyx' s SSMP . 3.1. 1 I n cas e o f

a n alar mfo r hig h relativ e particulat e matte r loading : 3.1.1. 1 Revie w proces s datafo r variation s i n pressur

e dro p acros s th e baghouse , the baghous e cleanin g cycle , baghous e inle t temperature , o r

ga s flowrat e tha

t correspond s wit h th e occurrenc e o f

th e ba g lea

k detectio n alarms . I f

revie w o f

thi s proces s dat

ao r othe r factor s (e.g. , hig h humidity , reconditioning ) indicate s ahig h probabilit y tha t th e excessiv e triboelecrri c signa l i s afals e indicatio n o f aba g leak/failure , the n recordfinding s an dprocee dwit h norma l operation s 3.1.1. 2 I f

relativ e particulate matter loadin g remain s abov e th e hig h alarmse t point , tak

e action s to reduc e th

e relativ e particulate matte r loadin g (e.g. , controlle dshutdow n o f hig h as h wast

e feeds) . 3.1.1. 3 I f

afte r 3 0 minute s o f

th e occurrenc e o f

th e hig h alarm , th e relativ e particulate matte r loadin g remain s abov e th e hig h alarm se t point , follo w th

e correctiv e measure s o f 3.1.2 . . 3.1. 2 I n cas e o f

reoccurrin g fals e ba g leak detectio n alarms : 3.1.2. 1 Clean th

e ba g lea k detectio n syste mprobe , and/or adjus t the sensitivity (range) , averagin g period , alar mse t points , and/or alar mdela y time , a s needed .3.1.2. 2 I f correctiv e measure s o f

3.1.2. 1 were previousl y unsuccessful , follo w correctiv e measure s o f 3.1.3 . 3.1. 3 I n cas e o f

a n alar mfo r high-hig h relativ e particulat e matte r loading : 3.1.3. 1 Initiat

e acontrolle dshutdow n o f wast e feeds . 3.1.3. 2 Inspect

baghous e fo r

leaks , tor n o r

broke n filte r

elements , o r othe r internal equipmen

t failures ; an d repai r

as needed . 3.1.3. 3 Followin g inspection/repai r o f baghouse , clean th e bag lea k detectio n systemprobe , and/or adjus t th e sensitivit y (range) , averagin g period , alarmse t points , and/or

alarmdelay time, a s needed . A s stated i n the U S EP A Fabric Filter Bag Leak

Detection Guidance (EPA-454/R-98

- 015) , "...conditionin g the [ba g lea k detection ] syste mt o th e proces s envhonment i s critical to reliabl e an d repeatable operation. " Therefore , allowanc e fo r reconditionin g th e syste mto th e proces s environmen

t shoul d b e mad

e afte r cleanin g th e prob e o r

afte r makin g adjustment s to th e system .4. 0 INSPECTIO N AN D MAINTENANC E A s state d i aSection s V.a.F . an dV.b.F . o f Onyx' s Par

t B RCR A Permit , eac h incinerato r systemundergoe s a"thoroug h visua l inspectio n fo r leaks , spills , fugitiv e emissions , an d sig n o f tamperin g a

t leas t dail y an di n accordanc e wit h the inspectio n schedule , containe d i n Appendi x 6 o f

the approve dpermi t

application" . Ony x utilizes thes e inspection s an d additional preventiv e maintenanc e activitie s as proactiv e measure s fo r mimmizin g th e potential fo r

malfunctions . T o facilitat e proper maintenance , acol dshutdow n wil l occu r a t leas t onc e pe r yea r fo r eac h incinerato r

system . Tabl e 4- 1 present s agenera l summar y ofth e inspectio n an dmaintenanc e activitie s tha t ar e performe dto preven

t malfunctions. Routin e inspectio n an dmaintenanc e activitie s ar e scheduled , communicated , an d recorde dthroug h th

e us e o f fiel dchecklists . Part s o f th e incinerato r

system s tha

t ar e subjec t to wea r (e.g. , bearings , O-rings , air/oi l filters ) ar e replace dbase do n the schedule s indicate do n thes e checklists . Thes e fiel dchecklist s wil l als o b e use dt o documen

t repair s o r replacement s o f

incinerato r

component s tha

t ma y b e reveale ddurin g inspections . I f as-needed repair s cannot b e performe dimmediatel y (withi n 24-hours) , SD P 1011— TW I Remedial Action Work

Order Program —ensures tha t thes e non-routin e maintenanc e activitie s ar

e give n th

e appropriat

e priorit y an dar

e tracke dthroug h completion . Brie f procedures/instruction s fo r inspectio n an dmaintenanc e activitie s ar e provide do n fiel d checklists . Additio n detail s an dprocedure s fo r inspectio n an dmaintenanc e activitie s are communicate dthroug h the following :

• SDP s fo r

specifi c proces s maintenanc e procedure s (see Tabl e 2-1) ; • Inspectio n andmaintenanc e procedure s fromequipmen t manufacturers ; • Trainin g activitie s fo r maintenanc e personnel ; an d

• Shutdow n andmaintenanc e meetings . Selecte dinspectio n an dmaintenanc e activitie s ma y b e performe db y qualifie dcontractor s o r associate s affiliate dwit h a n equipmen

t manufacturer/vendor . Ony x wil l includ e documentatio n o f

thes e activitie s i n the operatin g record . Inspectio n an dmaintenanc e requirement s ar e als o addressedi n othe r plan s requhe db y th e Interi mHW C MAC T Standard . Inspectio n an dtestin g o f the AWFC O syste mare describe di n the Automatic Waste Feed Cutoff Plan. Inspection , calibration , an d preventiv e maintenanc e fo r th e continuou s emission s monitorin g system(CEMS ) ar e discusse dth

e Continuous Emissions Monitoring System Quality Assurance Plan. Discussio n o n calibratio n an dmaintenanc e fo r th e continuou s monitorin g system(CMS ) i s presente d i n the Continuous Monitoring System Quality Assurance Program.Tabl e 4- 1 Inspectio n an d Maintenanc

e t o Preven tMalfunctions Potentia l Caus e fo r Malfunctio n Inspection s Maintenanc e

MechamcaVelectrica l failur e o f rotatin g equipment . • Dail y inspection s fo r leaks , corrosion , andvibratio n • Instrumentatio n an d alarm s fo r current , lubrication , and/o r vibratio n o n selecte d rotatin g equipmen

t • Cleanin g

• Tightenin g fastener s an d support s • Lubricatio n • Alignmen t • Schedule dreplacemen t o f critica l part s • A s neede d repairs/replacement s Plugging/Mecbariica l failur e o f lines/nozzle s • Dail y inspectio n fo r leaks , an d corrosio n • Internal equipmen

t inspection s durin g shutdown s • Cleanin g • Tightenin g support s • A s neede d repafrs/replacement s Mechanical/electrica l failur e o f mstrumentatio n • Proces s variabl e indicatio n • Compariso n between redundan t instrument s • Calibratio n check s • Schedule dreplacemen t o f instrument s • A s neede d repairs/replacement s

Mechanical/electrica l failur e o f actuated valves/damper s • Dail y inspectio n fo r leaks , an d corrosio n • Visua l inspectio n o f

instrument ai r an d electrica l connection s • Confirmatio n o f

fail-saf e position s durin g shutdown s • Confirmatio n o f

functionalit y throug h proces s variabl e control/indicatio n • AWFC O Testin g • Cleanin g • Lubricatio n • A s neede d repairs/replacement s

1 0

V E S 00206 6Table 4-1 (continued ) Inspectio n an d Maintenanc

e t o Preven tMalfunctions Potentia l Caus e fo r Malfunctio n Inspection s Maintenanc e Physical/electrica l failur e o f contro l system • Proces s variabl e control/indicatio n • Visua l inspectio n o f connection s • AWFC O Testin g • Cleanin g • A s needed repairs/replacement s Mecbanical/electrica l failur e o f utilit y supphe s • Inspection s ofth e utilit y suppl y sourc e • A s needed repairs/replacement s

Electrical/actuatio n failur e o f safet y interlock s • Corifnmatip n o f valv e fail-saf

e position s durin g shutdown s • Verificatio n o f

alarm s an d interlock s durin g AWFC O Testin g • A s neede d repairs/replacement s

Physical/mechanica l internal equipmen

t failur e • Dail y exterio r inspection s fo r leaks , corrosion , an d vibratio n • Interior

inspection s durin g shutdown s • Interna l cleanin g • Tightenin g fastener s an d support s • A s needed repairs/replacement s

1 15. 0 ALTERNATIV E MOD E O FOPERATIO N Ony x routinel y perform s certai n inspectio n an dmaintenanc e activitie s tha t canno t tak e plac e whil e operatin g th e incinerato r under th e requhement s o f

norma l operatio n an d mus t b e performe dmor

e frequentl y tha

n col dshutdowns . Thes e activitie s ar e typicall y identifie ddurin g the proactiv e inspection s (se e Tabl e 4-1 ) o r

whe n noticeabl e change s i n norma l operatin g parameters ar e identified . Thes e inspectio n an dmamtenanc e activitie s canno t tak e plac e whil e operatin g th e incinerato r

unde r th e requhement s o f

norma l operations ; however , acol dshutdow n i s no t requhe dto complete thes e activities . . Fo r thi s reason , Ony x ha

s define da

n alternativ e mod e o f

operatio n durin g whic h thes e activitie s ca

n b e performed . Thi s mod e o f operatio n i s referre dto a s th e "war mstand-b y mode" . Th e warmstand-b y mod e o f operatio n i s bein g implemente dper th e requhement s i n § 63.1206(b)(1)(h) . Thi s mode o f operatio n wil l onl y b e implemente dwhe n hazardou s wast e i s no t i n th e combustio n chambe r (i.e. , the hazardou s wast e residenc e time ha s transpired) . Th e remainde r o f th e sectio n describe s the war mstand-b y mod e andth e applicabl e requhement s fo r thi s alternativ e mod e o f operation . 5 . 1 War mStand-b y Mod e o f Operatio n Th e war mstand-b y mod

e o f operatio n i s utilize dt o perfor minspection s an dmaintenanc e activitie s tha

t d o no t warran t acomplet

e col dshutdown . Durin g thi s mod e o f operatio n th e combustio n chambe r temperature s ar

e maintaine dutilizin g natural gas . Thi s i s deshabl e from alon g termoperatin g standpoint t o mimmiz e extrem

e temperatur

e cycle s fo r the refractory whic h ca n lea dt o excessiv e wea

r an dprematur

e failure . Further , thi s provide s fo r

shorte r duratio n maintenanc e period s an daquicke r retur n t o norma l operatio n (i.e. , sinc e th

e combustio n chamber s ar e no t coole dt o ambien

t conditions , the n th e "normal " operatin g temperature s ca n b e attaine di n ashorte

r duration) . Operatio n i n the war

mstand-by mode ca

n onl y begi n whe n hazardou s wast e i s not i n th e combustio n chambe

r (i.e. , the hazardou s wast e residenc e time ha s transpired) . Onl y natural ga

s wil l b e fe dto th

e mai n burner s to maintai n stand-b y temperature s o f th e combustio n unit . Ony x wil l documen t i n th e operatin g recor dal l time s tha t th e uni t i s i n war mstand-b y maintenanc e operatin g mod e a s wel l a s description s o f an y inspectio n an d maintenanc e activitie s performe ddurin g th e war mstand-b y mode .

1 2Durin g th e warmstand-b y mod

e o f operatio n al l combustio n gase s ar e ducte d throug h tb e a h pollutio n contro l syste m(APCS) . Th e APCS , continuou s momtorin g system s (CMS) , an dcontinuou s emissio n monitorin g system s (CEMS ) ar e operate d pe r

norma l operatin g procedures , unles s temporaril y out-of-servic e fo r inspectio n an d maintenanc e activities . Th e automati c wast

e fee d cutof

f (AWFCO ) syste mi s no t operational sinc e ther

e i s n o hazardou s wast

e fee dt o the uni t Pe r § 63.1209(q)(2)(iii) , Ony x wil l utiliz e aseamles s transitio n between operatin g i n warmstand-b y mod e an d normal operations . Thi s allow s fo r calculatin g rollin g average s usin g datafromth e previou s operatin g mode . Prio r t o fransitioning to norma l operatin g mode , Ony x wil l ensur

e tha t vah d datai s availabl e fo r calculatin g rollin g average s an d tha t al l parameter s ar

e withi n limits . Norma l operation s wil l resum e wit h the initiatio n o f hazardou s wast

e to th e incinerator . 5. 2 Apphcabl e Requirement s Whe n operatin g i n the warmstand-b y mod e th e followin g Interi mHW C MAC T standard s d

o no t apply :

• Emissio n standard s i n § 63.120 3

• Monitorin g an d complianc e standard s o f § § 63.1206"through 63.1209 , excep t the mode s o f operatio n requhement s i n § 63.1209(q )

• Notification , reporting , and recordkeepin g requhement s o f § § 63.121 0 throug h 63.121 2 Pe r th e requiremen

t o f 63.1206(b)(ii) , thi s sectio n supplie s documentatio n i n th e operatin g recor d tha

t Ony x i s complyin g wit h al l "otherwis e applicabl e requhements " durin g war

mstand-b y mod e o f

operation . Requhement s constitut e "otherwis e applicabl e requirements " t o the exten t tha t they do'no t

aris e fromSubpar

t EE E an d the y ar

e otherwis e apphcabl e t

o any o f fh e emissio n unit s whe n i t i s operatin g durin g warmstand

b y mode . Incinerato r

Uni t 2 , Uni t 3 , or Uni t 4 , whe n operate d unde r warmstand-b y mode , i s no t

subjec t to an y "otherwis e apphcabl e requirements" .

1 3

### CONTINUOU S MONITORIN G SYSTE M QUALIT Y CONTRO L PROGRA M

Prepare d for : Ony x Environmenta

l Services , Inc

. Sauget , Illinoi s

Prepare d by : Franklin Engineering Group , Inc. Franklin , Tennesse

e

Jun e 200

4TABL E O FCONTENT S

1. 0 INTRODUCTIO N AN D BACKGROUN D 1 1. 1 SUMMAR Y O FFACILIT Y INFORMATIO N 4 1.1.1 Fixed

Hearth Incinerators 4 1.1.2 Rotary Kiln Incinerator. —- ...... 5 1. 2 CM S INSTRUMENTATIO N ,„..„ • 6 2. 0 CM S CALIBRATIO N AN D PREVENTIV E MAINTENANC E 1 3 2. 1 CM S CALIBRATIO N • —1 3 2.1.1 Initial

CMS Calibration : .....13 2.1.2 Subsequent

CMS Calibration 13 2.1.3 CEMS

Calibration Audits and

Calibration ....14 2. 2 CM S CALIBRATIO N AUDIT S • -1 4 2. 3 PREVENTIV E MAINTENANC E : - 1 9 3. 0 CM S RECORDKEEPIN G AN D REPORTIN G ... . 2 0 3. 1 RECORDKEEPIN G 2 0 3. 2 REPORTIN G '• 2 1 4. 0 CM S CORRECTIV E ACTION S 2 4

i i V E S 00207 1INDE X O FTABLE S TABL E 1 - l REGULATOR Y CHECKLIS T FO RTH E CM S Q A PROGRA M TABL E 1-

2 CM S INSTRUMEN T SPECIFICATION S „.. , ... . TABL E 2- 1 CM S CALIBRATIO N AUDI T REQUIREMENT S ." . TABL E 3- 1 REPORTIN G REQUIREMENT S :

ii i1. 0 INTRODUCTIO N AN D BACKGROUN D Ony x Environmenta l Services , Inc . (Onyx ) own s an doperate s tw o fixe dheart h incinerator s (Unit s 2 an d3 ) an darotar y kil n incinerato r

(Uni t 4 ) 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 A h Pollutant s (NESHAP ) fo r Hazardou s Waste Combustor s (HWC) , codifie d a s 4 0 CFR , Par

t 63 , Subpar

t EE E ( § 63.120 0 t o § 63.1213) . . . Th e NESHA P specifie s emission s standard s whic h reflec t emission s performanc e o f Maximu mAchievabl e Contro l Technologie s (MACT) , andi s commonl y referre dto a s th e HW C MACT . Hazardou s wast

e combustor s ar

e requhe d(pe

r § 63.8(d)(2) ] t

o establis h an dimplemen t a Continuou s Monitorin g Syste m(CMS ) Quaht y Contro l (QC ) Program . Th e purpos e o f th e Q C Programi s to outlin e procedure s use dt o verif y tha t th e CM S ar

e properl y installed , calibrated , an dcollectin g accurat e dat ao n a n ongoin g basis . Th e CM S performanc e evaluatio n tes t pla n wa s submitte da s par t o f th e Comprehensiv e Performance . Tes t

Plan . Th e Q C Progra

mdemonstrate s Onyx' s comphanc e wit h th e requhement s se t fort h i n § 63.8(d)(2) , a

s wel l a s the additional quality assuranc e (QA ) requirements . Th e Q C Progra mi s require dto contai n description s o f initia l an dsubsequen

t CM S cahbration , calibratio n drift , preventiv e maintenance , datarecording , calculation s an dreporting ; an d acorrectiv e actio n pla n fo r malfunctionin g CMS . Tabl e 1- 1 present s th e regulator

y reference s relate dto th

e Q C program , followe db y fh e sectio n o f thi s pla n tha t addresse s each specifi c requirement . Som e reference s ar

e mad e t o othe r HW C MAC T requhe dfaciht y operating plans . Thi s Q C Programi s intende dto fulfil l th e requhement s o f § 63.8(d)(2) , an dinclude s informatio n relate dto th e procedure s fo r eac h o f th e followin g operations :

• Initia l an

dsubsequen

t cahbration o f

th e CM S

• Determinatio n an dadjustmen t o f th e cahbratio n drif

t ofth e CM S

• Preventiv e maintenanc e ofth e CMS , includin g spar e parts inventor

y • Dat arecording , calculations , an dreportin g • Progra

mo f correctiv e actio n fo r

malfimctionin g CMS .

1Tabl e 1- 1 Regulator y Checklis t

fo r th e CM S Q A Progra m Regulator y Citatio n Descriptio n Pla n Sectio n § 63.8(c)(l)(i ) Operatio n andmaintenanc e o f eac h CM S Sectio n 1.2,2. 3 O& M Pla n CEM S Pla n §63.8(c)(l)(iii ) Startup , shutdown , an dmalfunctio n pla n fo r CM S SSMPPla n § 63.8(c)(3 ) Verificatio n o f operational statu s CM S PE T Pla n §63.8(c)(7)(ii ) Out-of-contro l CM S dat awil l no t b e use di n average s an dcalculations . Sectio n 4. 0 § 63.8(c)(7)(h ) Correctiv e action s fo r a n out-of-contro l CM S Sectio n 4. 0 and SSMPPla n § 63.8(c)(8 ) Out-of-contro l CM S informatio n t o b e submitte d Sectio n 4. 0 § 63.8(d)(2 ) Develo p an dimplement Q C portio n o f

CM S Q A progra m Sectio n 1. 0 § 63.8(d)(2 ) Q A progra minclude s .th

e development

an dsubmittal o f m e performanc e evaluatio n tes t pla n Sectio n 2.1, 1 §63.S(d)(2)(i ) Develo p writte n procedure s fo r initia l an dsubsequen

t calibration s Section s 2.1.1 , 2.1. 2 §63.8(d)(2)(ii ) Develo p writte n procedure s fo r determinatio n and adjustment

o f calibratio n drift s Sectio n 2. 2 § 63.8(d)(2)(iii ) Develo p writte n procedure s fo r preventiv e maintenanc e andspar e part s inventory Sectio n 2. 3 § 63.8(d)(2)(iv ) Dat arecording , calculations , an dreportin g Section s 3.1,3. 2 • § 63.8(d)(2)(vi ) Correctiv e action s fo r malfunctionin g CM S Sectio n 4. 0 § 63.8(e)(3 ) Performanc e evaluatio n o f CM S CM S PE T Pla n § 63.8(g ) Reductio n o f monitorin g data Sectio n 3. 2 § 63.10(b)(1 ) Mamtehiin g files . ' Sectio n 3. 1 § 63.10(b)(2)(ix ) Maintai n record s o f measurement s fromperformanc e evaluation s Sectio n 3. 1 § 63.10(b)(2)(vi ) Maintai n record s o f eac h perio ddurin g whic h aCM S i s malfunctioning , o r

inoperativ e andout

o f contro l Sectio n 4. 0 an d SSM P Pla n § 63.10(b)(2)(vii ) Maintai n record s o f measurement s t

o demonstrat

e complianc e Sectio n 3. 1 § 63.10(b)(2)(viii ) Maintai n record s o f result s o f

CM S performanc e evaluation s andopacit

y an dvisibl e emissio n observation s Sectio n 3. 1 §63.10(b)(2)(x ) Maintai n record s o f CM S calibratio n check s Sectio n 2.1. 2

2 V E S 00207 4Tabl e 1- 1 (continued ) Regulator y Checklis t

fo r th e CM S Q A Progra m Regulator y Citatio n Descriptio n Pla n Sectio n §63.10(b)(2)(xi ) Maintai n record s o f al l adjustment s an dmaintenanc e perfbrme do n th e CM S Sectio n 3. 1 §63.10(c)(1 ) Recordkeepin g requhement s fo r CM S measurement s (includin g unavoidabl e breakdown s an dout-of-contro l situations ) Sectio n 3. 1 §63.10(c)(13 ) Maintai n record s o f tota l proces s operatin g time durin g th e reporting perio d Sectio n 3.1 . §63.10(c)(14 ) Develo p an dhnplemen t CM S Q A programprocedure s Sectio n 1.0 §63.10(c)(5 ) Maintai n record s o f dat e andtim e fo r

CM S inoperabihty (excep t

fo r zero an dhigh-leve l checks ) Sectio n 3. 1 § 63.10(c)(6 ) Maintai n record s o f dat e an dtim e fo r

CM S out-of

contro l period s Sectio n 3. 1 . § 63.10(c)(8 ) Maintai n record s o f identificatio n o f

eac h time perio d o f exceedance s - doe s no t

includ e period s o f

Startup , Shutdown , Malfunctio n (SSM ) Sectio n 3. 1 §63.10(e)(3)(i ) Submitta l o f semiannua

l exces s emission s an dCM S performanc e repor

t Sectio n 3: 1 j §63:10(e)(3)(v ) Content an dsubmittal datao f

exces s emission s an d CM S performanc e repor t Sectio n 3. 2

• § 63.10(e)(3)(vi ) Content o f summar y repor t require db y (e)(3)(vii ) an d (e)(3)(viii ) t o thi s sectio n Sectio n 3. 2 § 63.10(e)(3)(vii ) Conditio n fo r submittin g onl y th

e summar

y repor t . Sectio n 3. 2 § 63.10(e)(3)(viii ) Conditio n fo r submittin g both th

e summar

y repor t an d exces s emission s an dCM S performanc e repor t Sectio n 3. 2 § 63.1209(b)(2)(i ) Calibratio n o f thermocouple s andpyrometer s Sectio n 2. 1 § 63.1209(b)(3 ) Frequenc y o f CM S samphng ; evaluation , computing , an drecordin g o f

regulate dparamete

r Sectio n 3. 1 § 63.1209(b)(5 ) Calculatio n o f rollin g average s Sectio n 3. 1 § 63.1209(f)(1 ) § 63 .12 1 l(c ) requhe s tha t CM S ar e installed , calibrated , an doperationa l b y th e complianc e dat

e CM S PE T Pla n

Notes : PE T Performanc

e Evaluatio

n Tes t SSM P Startup

, Shutdown

, Malfunction Pla

n SD P Standar

d Divisio n Practice

sTh e datacollecte dfro mCM S mstrumentatio n i s use dto demonstrat e th e unit' s complianc e wit h th

e performanc e requirement s promulgate di n th e mteri m.HW C Maximu mAchievabl e Contro l Technolog y (MACT ) standard . Th e Q A Progra moutline s procedure s use dt

o verif y tha t tb e CM S ar

e properl y cahbrate dan dcollectin g accurat e datao n an ongoin g basis . Du e to th e similarit y o f

th e three CM S system s (on e fo r eac h incinerato r

system) , genera

l reference s to aCM S systemo r incinerato r

systemi n thi s documen t wil l impl y al l thre e systems . Informatio n tha t i s onl y apphcabl e to one o r tw o o f th e thre e system s wil l b e clearl y identified . Thi s documen

t i s organize das follows : . SectionT. O Introductio n an dBackgroun d Sectio n 2. 0 CM S Calibratio n an dPreventiv e Maintenanc e . Sectio n 3. 0 CM S Recordkeepin g an dReportin g Sectio n 4. 0 CM S Correctiv e Action s Thi s plan als o assimilate s informatio n an dprocedure s foun di n othe r documents . A s require db y § 63.6(e)(3)(vi) , othe r document s containin g procedure s o r informatio n referre dt o i n thi s pla n wil l b e mad e availabl e fo r

inspectio n whe n requeste db y th e Administrator . Th e remainde

r o f thi s sectio n provide s a

n overvie w o f

the incineratio n syste mfollowe d b y adiscussio n o n th

e CM S mstrumentation . Sectio n 2. 0 discusse s CM S initia l an d continuin g cahbratio n an dpreventiv e maintenanc e requhements . Sectio n 3. 0 addresse s requirement s relate dt

o facilit y documentatio n an dreporting . Sectio n 4. 0 define s an d discusse s nonstandar

doperation s ofth e CM S an dapplicabl e correctiv e actions . 1. 1 Summar y o f

Facilit y Informatio n Brie f summarie s whic h describ e the fixedheart h incinerator s an dthe rotar y kil n incinerato r

ar e presente di n thi s section . 1.1.1 Fixed

Hearth Incinerators Eac h o f th e fixedheart

h incmerator s include s the followin g components :

• Fee dequipmen

t• Primary an dsecondar y combustio n chamber s

. • Lim e injectio n syste m • Spra y drye r absorbe r (SDA )

• Fabri c filte r

baghous e • Solid s an das h remova l system s • Induce ddraf

t (ED ) fa n an dstack

• Instrumentation , controls , an ddat aacquisitio n system s Variou s soli dan dliqui dwaste s an dgaseou s feedstream s ar e thermall y treated i n tbe . fixe dheart

h incinerators . Soh dwast e i s fe dt o th

e primary (lower ) combustio n chambe r vi aafee dconveyo r

syste man dpneumati c ram . Liqui dwast e fromtank s an dtanker truck s ar e fe dt o th e primary combustio n chambe r throug h tw o atomize dhqui dinjectors . Liqui dwast

e fro mcontainer s ar

e fe dto th e primary combustio n chambe r throug h a specialty fee dinjector . A gaseou s feedstrea mi s fe dt

o th e Uni t

2 primary combustio n chambe r dhectl y fromga

s cylinders . Of f

gase s from ahoode dfee demissio n contro l syste man dfrom awast e handlin g glov e bo x ar e fe ddhectl y t

o th e Uni t 3 secondar

y combustio n chamber . Combustio n chambe r temperature s ar

e maintaine dusin g natura l ga s firedt o adedicate dburne

r i n bot h the primar y an dsecondar y chambers . Combustio n ga

s exit s th e secondar

y combustio n chambe

r an denter

s th e SDA , whic h provide s aci dgas removal an dcoolin g ofth e combustio n gas . Combustio n ga s exit s th e SD A andi s distribute dt o th e fabri c filter

baghouses , whic h provid e particulat e matte r removal . Th e induce ddraf t fan , locate ddownstrea mo f th e baghouses , move s th e combustio n ga

s throug h th

e systeman dexhaust s th e gas throug h the mai n stack . Hot , we t ga s i s extracte ddownstrea mo f th e baghous e throug h acontinuou s emission s monitorin g system . Thi s systemfeature s amulti-component infrare dgas analyzer

tha t detect s hydroge n chloride , carbo n monoxide , an dwate r vapo r concentrations . A n integrate dzirconiu moxide-base danalyze r detect s oxyge n concentrations . 1.1.2 Rotary Kiln Incinerator Th e rotar y kil n incinerato r

include s th

e followin g components :

• Wast e fee dsystem • Primary an dsecondar y combustio n chamber s • Temperin g chambe

r • Lim e injectio n system • Spra y drye r absorbe r• Carbo n injectio n syste m. • Fabri c filte r

baghous e • Solid s an das h removal system s • I D fa n an dstac

k '

• mstrumentation , controls ^ an ddat aacquisitio n system s Variou s soli dan dliqui dwaste s ar e thermall y treate d i n the rotar y kil n incinerator . Soh d waste s ar e fe dt p aramfeeder

vi aaclamshell , adru mfee dconveyor , an da n auxiliar y fee dconveyor . A hydrauli c rampushe s th e soh dwast e int o the kiln . Liqui dwast e fro m tanks an dtanke

r truck s i s fe dto th

e primar y an dsecondar

y combustio n chambers throug h atomize dliqui dinjectors . Combustio n chamber temperature s ar

e maintaine dusin g natura l gas fired to adedicate dburne r i n bot h the primar y an dsecondar y chambers . Combustio n ga

s exit s th

e secondar

y combustio n chambe

r an denters the temperin g chamber , whic h provide s coolin g o f th e combustio n gases . Th e combustio n ga s exit s the temperin g chambe

r andi s distribute dbetwee n tw o identical SDAs , whic h provid e aci d gas remova l andadditional ga s coohng , A carbo n injectio n syste mi s utilize dfo r controllin g droxin/furan an dmercury emissions . Th e activate dcarbo n i s ai r injecte dint o the combustio n ga s immediatel y downstrea mof-th e convergenc e o f combustio n gase s fro mthe SDAs . Fro mth e SDAs , combustio n ga s i s distribute dto fabri c filter baghouses , whic h provid e particulate matte r removal . Th e I D fan , locate ddownstrea mo f the . baghouses , move s th

e combustio n gas throug h th e syste man dexhaust s the gas throug h the mai n stack . Hot , wet ga s i s extracte ddownstrea mo f Ih e I D fa n throug h acontinuou s emission s monitorin g system . Thi s systemfeature s amulti-componen t infrare dga s analyzer

tha t detects hydroge n chloride , carbo n monoxide , an dwater vapo r concentiations . A n integrate dzhconiu moxide-base danalyzer detect s oxyge n concentrations . 1 . 2 CM S Instrumentatio n Thi s sectio n describe s the CM S instrument s use dmonito r regulate dproces s parameter s fo r demonstratin g on-goin g complianc e wit h the Interi mHW C MAC T emissio n standards . A summar

y o f specification s fo r

CM S instrumentatio n i s provide di n Tabl e 1-2 . Th e Interi mHW C MAC T standar drequire s al l CMS' s be installe di n location s tha t provid e representativ e measurements o f emission s or

proces s parameters . Al l CM STabl e 1- 2 CM S Instrumen t

Specification s Applicatio n Instrumen t Ta g Numbe r Manufacture r Mode l Operatin g Rang e Locatio n Uni tNo . 2 | Hig h BT U Liqui d Feedrat e Mas

s Fl o wmete

r FT-21 5 Micr o Motio n D 40S-S S 0-3,60 0 lb/h r Feed Lin e Hig h BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-215D I Weigh-Troni x WI-.130 0-60,00 0 l b Fee

d Lin e | Lo w BT U Liqui d Feedrat e Mass Flowmete r FT-21 6 Micr o Motio n D 40S-S S 0-3,60 0 lb/h r Fee

d Lin e 1 Low BT U Liqui d Direc tInjectio n • Feedrat e Scale WT-215D I Weigh-Troni x WI-.13

0 0-60,00

0 l b Fee

d Lin e Specialt y Fee d Weigh t Weigh Scale WT-204 Toledo 814 0 EX P 0-4,00 0 l b #20

4 Specialt

y Feede r Drumme d an d Bul k Solids Fee

d Weigh t Weig h Scal e WT-21 0 Toled o A14 0 0-40 0 I b Soli d Charg e Conveyo r Cylinde r Ga

s Feedrat

e dPCel l FT-21 7 Yokogaw a YA11 F • • 0-10 in . w.c . (0-6 0 lb/min ) Cylinder Ga

s Fee d Syste m PC C Temperatur

e Type K

Thermocoupl

e TT-200A/

B Modico n B883-2O 0 0-250

0 ° F Primar y Chambe r SC C Temperatur

e . Type K

Thermocoupl

e TT-219A/

B Modico n B883-20 0 . 0-250

0 ° F Secondar y Chambe r PC C Pressur

e Pressur e Transmitte

r • PT-20 0 Rosemon t 1151D

P . : -7.

5 t o 2. 5 in . w.c . Primar y Chambe r ES V Position Position Switc h , ZS-22

4 Square-

D 900

7 CG2B 2 open/clos e Emergenc

y Stac k Baghous e Inle tTemperatur

e Type K

Thermocoupl

e TT-27 0 Modico n 833-20 0 0-250

0 ° F SD A Outle t Combustio

n Ga s Flo w Rat

e dPCel l FT-28 3 Rosemoun t 1151D

R 0-20,00.

0 acfm . Stac

k Stac k Ga s Oxygen

, Concentratio

n Zi f ranhirn Oxide Analyze r AT-28 9 CO S A ZFN-11YA1-2Z 1 0-25 % . CEM S

Buildin g Stac k Ga s Carbo n Monoxide Concentratio

n Multicomponen t Infrared. Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyzer AT-288 E EcoChem MC 3 0-20 0 / 0-300 0 ppm v CEM S Buildin g Stac k Hydroge

n Chloride Concentratio

n Multicomponen t Infrared. Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyzer AT-288 E EcoChem MC 3 0-100 0 ppm v CEM S

Buildin g Stac k Ga s Moistur

e Concentratio

n Multicomponen

t Infrared. Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyzer AT-288 E EcoChem MC 3

' 0-60 % CEM S

Buildin g Stac k Ga s Oxyge n Concentratio

n Multicomponen

t Infrared. Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyzer AT-288 E EcoChem MC 3 0-25 % CEM S

Buildin gTabl e l -2 (continued ) CM S Instrumen t

Specification s | Applicatio n Instrumen t Ta g Numbe r Manufacture r Mode l Operatin g Rang e Locatio n | Uni tNo . 3 High BT U Liqui d Feedrat e Mas

s Flowmete

r FT-31 5 Micr o Motion DS-040 0-3,60 0 lb/hr Fee

d Lin e High BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-31 5 D I Weigh-Troni x WI-13

0 0-60,00

0 l b Fee

d Lin e Lo w BT U Liqui d Feedrat e Mass Flowmete r FT-31 6 Micr o Motion . DS-040 0-3,60 0 lb/hr Fee

d Lin e Lo w BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-315D I Weigh-Troni x WI-13

0 0-60,00

0 l b Fee

d Lin e Specialt y Fee d Weigh t Weig

h Scal e WT-304 Toled o AI40 EX P 0-2,00 0 l b #30

4 Hoode d Feede r Drumme d an d Bul k Solids Fee

d Weigh t Weig h Scal e WT-31 0 Toledo A14 0 0-40 0 l b Solid Charg e Conveyor PC C Temperatur

e Type K

Thermocoupl

e TT-300A/

B Modico n 883-20 0 0-250

0 °F . Primar y Chambe r SC C Temperatur

e Type K

Thermocoupl

e TT-319A/

B Modico n 883-20 0 0-250

0 ° F Secondar y Chambe r PC C Pressur

e Pressur e Transmitte

r PT-30 0 Rosemoun t 115

1 d P -7.

5 t o 2.5 . in . w.c . Fee

d Lin e TR V Position Position Switc h ZS-32

4 Square-D 900 7 CG2B 2 open/clos e Emergenc

y Stac k Baghous e Inle tTemperatur

e Type K

Thermocoupl

e TT-37 0 Modico n 833-20 0 0-250

0 P F SD A Outle t Combustio

n Ga s Flo w Rat

e d

P Cel l FT-38 3 Rosemoun t 115

1 P R 0-20,00 0 acfm ! • Stac

k Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxid e Analyzer AT-38 9 COS A ZFN-11YA1-2Z 1 0-25 % CEM S

Buildin g Stac k Ga s Carbo n Monoxid e Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyze r AT-388 E EcoChem MC 3 0-200/0-300 0 ppm v "CEM S

Buildin g Stac k Hydrogen.Chloride Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyze r AT-388 E EcoChem MC 3 0-100 0 ppm v "CEM S

Buildin g Stac k Ga s Moistur

e Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyze r AT-388 E EcoChem MC 3 0-60 % "CEM S

Buildin g Stac k Ga s Oxyge n Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxid

e Oxyge n Analyze r AT-388 E EcoChem MC 3 0-25% . "CEM S Buildin g

< m tn 

### o o h oTabl e 1 (continued ) CM S Instrumen t

Specification s Applicatio n Instrumen t Ta g Numbe r Manufacture r Mode l Operatin g Rang e Locatio n Uni tNo . 4 Wast e Feedrat

e t o X-1 0 Nozzl e Mas s Flowmete

r FT-12 9 Micro Motio n DS100 S 12 8 0-7,00

0 Ib/h r Feed Lin e Wast e Feedrat

e t o X- l 1 Nozzl e Mas s Flowmete

r FT-13 8 Micro Motio n D100S-H Y 0-6,00 0 lb/h r Feed Lin e Wast e Feedrat

e t o X-1 2 Nozzl e Mas s Flowmete

r FT-14 5 Micr o Motion DL100S-S S 0-8,00 0 lb/h r Fee

d Lin e Wast e Feedrat

e t o X-2 2 Nozzl e Mas s Flowmete

r FT-21 2 Micro Motio n , D1D00S-S S 0-7,00 0 lb/hr Fee

d Lin e Clam Shel l Fee

d Weigh t (shredde d solids) Load Cel l WT-00 1 Toledo 814 0 0-2,00 0 l b Ra

m Feed Hoppe r Drum Conveyor Solids Weigh t Load Cel l WT-014 A . Toledo 814 0 0-1,00 0 l b ' Drum

Conveyor Auxiliary Conveyor Solids Weigh t Loa d Cel l WT-14 B Toledo 814 0 0-20

0 l b Auxiliary

Conveyor PC C Temperatur

e Pyromete r TT-305A/ B Irco

n Modline

4 44-99-F 1-0-1- 0-3,00 0 ° F Kil n Outle t SC C Temperatur

e Type R

Thermocoupl

e TT-317A/

B . Chesse

l 351 0 0-3,00 0 ° F SC C Outle t PC C Pressur

e Pressur e Transmitte

r PT-30 0 Rosemoun t 1151DR2

F -9.0 t

o 1. 0 in . w. c Kil n Hoo d Surg e VentPosition Position Switc h ZSC-02 6 Square- D . 9007CG2B 2 open/clos e Kil n Face TR V Position Position Switc h ZSC-31 6 Square- D 9007CG2B 2 open/clos e Emergenc

y Stac k Carbon Feedrat

e Feede r C-1 7 K-Tro n K2T3 5 0-10 0 Carbo

n Inject . Syste m Carbo n Injectio

n Carrie r Ga s Suppl y Pressur

e Pressur e Switc h PSL-438 A Dwye r 333

0 Tri p Points :

± 5 in . w;c

. Carbo

n Injectio n Lin e Cavbo n Feede r Discharg

e Pressur

e Pressur

e Switc h PSH-438 B Dwye r 3215 . Tri p Points : < 3 psi g > 1 3 psi g Carbo n Injectio n Lin eTabl e 1 (continued ) CM S Instrumen t

Specification s 

## 1 Applicatio n Instrumen t Ta g Numbe r Manufacture r Mode l Operatin g Range Locatio n Uni tNo . 4 (continued

) SD A X-1 8 Outle

tTemperatur

e (Baghous

e Inle tTemperature

) Type K Thermocoupl

e TT-417A/

B Modico n B883-20 0 0-2,50

0 ° F SD A X-1 8

Outle t 1 SD A X-1 9 Outle

tTemperatur

e (Baghous

e Inle tTemperature

) Type K Thermocoupl

e TT-418A/

B Modico n B883-20 0 0-2,50

0 ° F SD A X-1 9

. Outle t Combustio

n Ga s Flowrat

e Pito

tTube/d P Cel l FT-559A/

B . Automatio

n Servic e 115IDRF228

3 0-55,00

0 acf m Stac

k Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxide Analyze r AT-560A/ B COS A ZFN-11YA1-2Z 1 0-20 % CEM S .

Buildin g Stac k Ga s Carbo n Monoxide Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyzer AT-556 E EcoChem MC 3 0-200/ . 0-300 0 ppm v CEM S Buildin g Stac k Hydroge

n Chloride Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyzer AT-556 E EcoChem MC 3 0-100 0 ppmv . CEM S

Buildin g Stac k Ga s Moistur

e Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyzer AT-556 E EcoChem MC 3 0-60% CEM S Buildin g Stac k Ga s Oxyge n Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyzer AT-556 E EcoChem MC 3

0-25 % CEM S

Buildin g

< m c o 

### o o r o o C O 1 0operatin g paramete r measuremen

t device s a

t th e Ony x facilit y ar

e installe d i n comphanc e wit h thi s requirement . A descriptio n ofth e type s o f CM S instrumentatio n follows : Mass/Feedrat

e Monitors : Liqui dwast e feedrate s fromtank s ar e measure d b y corioli s mas s flowmeters . Direc t

injec t liqui dfeedrate s fromtanke r truc k ar e calculate dusin g the continuousl y monitore dweigh

t ofth e tanker . Al l soh d waste charge s ar e weighe dusin g ascale/loa dce u prio r t o bein g fee dt

o th e incinerator . Thes e measurement s ar e use d to calculate pumpabl e waste , tota l waste , an d constituen

t feedrates . Fo r Uni t 4 , th e outpu t o f acalibrate d feede r

i s utilize dt o calculate the feedrat e o f powdere d activate dcarbon , whic h i s injecte dint o the plenu mupstrea mofth e baghouses . Pressure/Differentia

l Pressur

e Monitors : Primar y combustio n chambe r pressur e i s measure d b y diaphrag mactuated pressur e transmitters . Th e positio n ofth e dampe r immediatel y upstrea

m o f th e I D fa n i s varie d f

o contro l stac k

ga s flowrat e an d t

o maintai n kil n combustio n chambe r negativ e pressur

e (draft) . Th e primary combustio n chambe r pressur e i s interlocke dwit h waste feeds . Fo r Uni t 2, pressur

e dro p i n th

e cylinde r

ga s feedstrea

mi s measure d and converte dto afeedrate . Th e feedrate i s use d to calculate thi s feedstream' s contributio n to the chlorine , lo w volatil e metals , an d semivolatil e metal s feedrate s to the incinerator . Fo r Uni t 4 , pressur

e switche s ar

e utilize dto ensur

e that th e carbo n feede

r discbarg e pressure , an d th e carbo n injectio n ai r

blowe r discharg e pressure ar

e withi n th

e desig n limits . Th e pressur

e dro p acros s apito t

tub e i n th e stac k

i s continuousl y monitore dan d use d t o calculat e th e stac k ga s flowrate . Temperatur

e Monitors : Fo r

Unit s 2 an d 3 , redundan t thermocouple s ar

e use d to measur

e the temperatur

e i n bot h combustio n chambers . A thermocoupl e i s als o locate d a t the exi t t o th e SD A andi s th e primar

y elemen t fo r th e SD A exi t

temperatur

e contro l loop . Uni t 4 i s equippe d with redundan t pyrometer s i n th

e primary chambe

r and redundan

t thermocouple s i n the secondar y chamber . Eac h SD A outle t i s equippe d with redundant thermocouple s used fo r

temperatur

e contro l an d monitorin g o f th e baghous e inle t

temperature .

1 1Emergenc y Safet y Ven t Positio n Monitors : Th e positio n ofth e emergenc y safet y vent (ESV ) i s indicate da

s ope n o r close db y apositio n transmitter : N o wast e o r fue l can b e fe di f

th e ES V positio n i s "open" . Th e Emergenc y Safety Ven t (ESV ) Pla n provide s detail s o n the ES V systems . Ba g Lea k

Detectio n System : • A triboelecrri c senso r i s locate ddownstrea

mo f th e I D fa n an d monitor s th

e relativ e particulate matte r loadin g o f

th e combustio n gas exitin g th e baghouses . Alamo s an dinterlock s base d o n thi s relativ e measuremen t ar e indication s o f

apotentia l ba g lea

k o r failure . Procedure s fo r

setu p an dadjustment s t o the ba g lea k detectio n syste mar

e no t covere d b y thi s Q C program . Th e Operatio n an dMamtenanc e Pla n provide s detail s o n th e ba g lea k detectio n system . Continuou s Emission s Monitorin g System : Th e CEM S continuousl y sample s an danalyze s stack ga s fo r th e concentration s o f

carbo n monoxid e (CO) , Hydroge n Chlorid e (HCI) , an d moisture usin g amulticomponent infrare dphotometer . Th e oxyge n concentratio n ofth e sample d gas i s analyze dsimultaneousl y usin g an integrate d zhconiu moxid e analyzer . A back-up zhcomu moxid e O

2 analyze

r als o monitor s stac k

gas O 2 concentration . Thes e dat aar e use dt o calculate th

e stack ga s C O an dHC I concentration s o n adr y basis , correcte dt

o 7 % O2 . Th e CEM S Q A Pla n provide s additiona l detail s o n th e CEMS . .

1 22. 0 CM S CALIBRATIO N AN D PREVENTIV E MAINTENANC E Thi s sectio n discusse s th e cahbratio n an dpreventiv e maintenanc e requhement s to meet th e requirement s o f

§ 63.8(d) . . 2. 1 CM S Calibratio n T o ensur e ongoin g complianc e wit h the mteri mHW C MAC T standard , i t i s essential tha

t th e datacollecte dfromth

e CM S b e measure dan drecorde di n an accurat e manner . Initia l calibrations , subsequen

t cahbration , an dCEM S cahbration s ar e describe di n thi s section . 2.1.1 Initial

CMS-Calibration A s par t o f Onyx' s Quality Contro l Program , the CM S instrument s wer e initiall y calibrate dprio r t o the Interi mHW C MAC T comphanc e date . Cahbratio n prio r t o th e complianc e dat

e i s require ds o tha

t al l collecte ddataar

e reliabl e an daccurate . Al l initia l cahbratio n dat aar e par t o f the operatin g record . Initia l calibration s o f new/replacement

instruments , wil l b e performe dpe r th e manufacture' s writte n procedures . I n lie u o f a n initia l calibratio n fo r new/replacemen

t instrument s o r

instrumen

t components , th

e facilit y ma y us e amanufacturer' s certification . 2.1.2 Subsequent

CMS Calibration Subsequen

t calibration s o n CM S instrumentatio n wil l b e performe da s neede dan di n accordanc e wit h the manufacture' s writte n procedures . Cahbration s wil l b e performe das correctiv e measure s fo r

hig h cahbratio n drift . Calibration s may b e require dwhe n restorin g CM S instrument s after

maintenanc e o r

repairs . Al l cahbratio n adjustment s wil l b e documente db y record s ofth e calibratio n drif t deterrriine dbefor e an dafte r tb e instrumen

t wa s serviced . Some instrument s suc h a s differentia l pressur

e cells mus t

b e remove dfromservic e an dbenc h calibrated . T o minimiz e downtime thes e instrument s may b e replace dwit h acalibrate dspare . Th e Uni t 4 primar

y combustio n chambe

r pyrometer s wil l b e replace da t leas t armuall y wit h a factor y cahbrate dpyrometer . Electroni c check s an dreplacement s o f thermocouple s wil l b e performe dpe

r th e facility' s Thermocoupl e Calibration , Operation , an dReplacement Procedure . A calibratio n recordfor mi s availabl e fo r eac h CM S instrument

an dwil l b e use dt

o documen

t calibratio n audits , cahbrations , an dreplacements . Th e mos t recentl y complete dcahbratio n recor ddocument s tha

t th e instrumen

t i n servic e meet s th

e quality contro l criteri ase t forth b y thi s program . Thes e calibratio n record s contai n "calibratio n notes " whic h provid e th e instrument technicia n wit h procedure s specifi c to agive n mstrument . Th e calibratio n recordform s fo r CM S instrument s ar

e incorporate di n thi s Q C Programb y reference .

1 32.13 CEMS Calibration Audits and

Calibration CEM S QA/QC

procedure s ar

e provide db y th e Continuous Emission Monitoring System Quality Assurance Plan. Thes e procedure s ar e maintaine da

t the faciht y anddescrib e the requirement s fo r CEM S drif

t checks , audits , cahbrations , preventiv e maintenance , andrecordkeeping . 2. 2 CM S Calibratio n Audit s CM S cahbratio n audit s ar e performe dt

o detennin e the cahbratio n drif t (CD ) o f

CM S instruments . Calibratio n Drift (CD ) i s th e bia s betwee n th e CM S instounent readin g an da cahbratio n reference . Tabl e 2- 1 present s th e requhement s fo r CM S calibratio n audits . Eac h CM S mstrumen

t wil l b e subjecte dacahbratio n audi t a t the frequenc y indicate di n Tabl e 2-1 . Th e calibratio n audi t

wil l b e performe da

t the low-leve l (zero ) an dhigh-leve l check s indicated . Th e calibratio n chec k

wil l confir mtha

t al l proces s variabl e indication s (e.g. , loca l reading , contro l roo mdisplay ) a

t th e high-leve l valu e agre e wit h the calibratio n referenc e withi n ofth e require dtolerance . Calibratio n adjustments/correctiv e action s mus t b e take n i f

thi s calibratio n • drif t i s greate r tha n Vi o f the requhe dtolerance . I f the calibratio n drif

t exceed s th

e requhe d tolerance , the instrumen t i s considere dout-of-'control . Sectio n 4. 0 describe s th e correctiv e action s fo r

out-of-control , inoperative , an dmalfunctionin g CMS . I f the accurac y o f

aCM S instrumen

t i s i n question , the C D i s determine dan ddocumente dprio r to performin g maintenance , repairs , o r adjustments . Th e troubleshooting/cahbration s o f CM S instrument s wil l b e performe di n amanne r consistent

wit h th e manufacturer' s writte n procedure s an drecornmendations . Th e C D determine dafte r calibrations/correctiv e action s hav e been take n wil l documen

t the effect s ofth e adjustment s an ddemonstrat e tha t the mstrumen

t i s performin g properly . Calibratio n record s wil l documen t CD , whic h i s a

n indicato r

o f th e stabilit y o f

th e CM S cahbratio n ove

r time . Th e amoun

t o f drif t an dstabilit y i s dependan t o n th e typ e o f

instrument an dth e cahbratio n frequency. Ony x ma y increas e o r

decreas e the frequenc y o f particula

r calibratio n audit s t o the exten t warrante db y an assessmen t o f a n instrument' s stability . Ony x wil l maintai n regularl y schedule dcalibratio n audi t interval s fo r

eac h CM S instrument . Calibration s wil l b e performe dt o preven t excessiv e C D an dt o maintai n th e validit y o f

th e data collecte dfrom, th

e monitorin g system .

1 4Tabl e 2

- 1 CM S Calibratio n Audi t Requirement s 

## 1 Applicatio n Instrumen t Ta g Numbe r Frequency o f Calibratio n Audi t Lo w Leve l Chec k Point Hig h Leve l Chec k Poin t Toleranc e Uni tNo . 2 Hig h BT U Liqui d Feedrat e Mass Flowmete r FT-21 5 Annuall y 0-

5 lb/mi n 15-2 5 lb/min 10 % Hig h BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-215D I Quarterl y 01b 25,0001 b . 10 % Lo w BT U Liqui d Feedrat e Mas

s Flowmete

r FT-21 6 Annuall y 0-

5 lb/min 15-2 5 lb/mi n 1.0 % Lo w BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-215D I Quarterl y 01

b 25,00 0 I b 10

% | Specialt

y Fee d Weigh t. Weig

h Scal e WT-204 Quarterl y . 01

b -50 0 l b 10 % Drumme d an d Bul k Solid

s Fee d j Weigh t Weigh Scal e WT-21 0 Quarterl y 01b -5 0 lb . 10 % J Cylinde r Ga

s Feedrat e dPCel l FT-21 7 Annuall y 0 in . w.c . 1

0 in . w.c . 10 % Primar y Combustio

n Chambe

r Temperatur

e Type' K• Thermocoupl

e TT-200A/

B Refer t

o th e Thermocoupl

e Calibration, Operation, an d Replacemen

tProcedur

e Secondar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-219A/

B Refer t

o th e Thermocoupl

e Calibration, Operation, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe

r Pressur e Pressur e Transmitte

r PT-20 0 Quarterl y -7.

5 t o -6. 5 1.

5 t o 2. 5 i n w.c . 10

% ES V Position Position Switc h ZS-22

4 Annually AWFC O interloc k energize

d whe n ope n Pas

s Baghous e Inle tTemperature. Type K Thermocoupl

e TT-27 0 Se e Calibratio

n Recor d For m Combustio

n Ga s Flo w Rat

e dPCel l FT-28 3 Annually 0-0.0 5 in . w.c . 0.45-0.5

0 in . w.c . Stac k Ga s Oxyge n Concentratio

n Zirconium Oxide Analyze r AT-28 9 • Pe r CEM S Q A Pla

n \ Stac k Ga s Carbo n Monoxide Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyze r . AT-288 E Pe r CEM S Q A Pla

n Stac k Hydrogen Chloride Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyze r . AT-288 E Pe r CEM S Q A Pla

n Stac k Ga s Moistur

e Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyze r . AT-288 E Pe r CEM S Q A Pla

n Stac k Ga s Oxyge n Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconium Oxide Oxyge n Analyze r . AT-288 E Pe r CEM S Q A Pla

n

1 5Tabl e 2- 1 (continued ) CM S Calibratio n Audi t Requirement s Applicatio n Instrumen t Ta g Numbe r Frequenc y o f Calibratio n Audi t Lo w Leve l Chec k Point Hig h Leve l Chec k Poin t Toleranc e 1 UnitNo. 3 | High BT U Liqui d Feedrat e Mas

s Flowmete

r FT-31 5 Annuall y 0-

5 lb/min 15-2 5 lb/min 10 % 1 Hig h BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-315D I Annuall y 01b 25,00 0 l b 10

% | Lo w BT U Liqui d Feedrat e Mas

s Flowmete

r FT-31 6 Annually • 0- 5 lb/hr 15-2 5 lb/min 10 % 1 Lo w BT U Liqui d Direc tInjectio n Feedrat e Scal e WT-315D I Annuall y 01b 25,0001 b 10 % Specialt y Feed Weigh

t Weig

h Scal e WT-304 Quarterl y 01

b -20 0 l b 10 % Drumme d an d Bul k Solids Feed Weigh t Weig h Scal e WT-31 0 Quarterl y 01

b -5 0 l b 10 % Prunar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-300A/

B Refer t

o th e Thermocoupl

e Calibration, Operation , an d Replacemen

tProcedur

e Secondar y Combustio

n Chambe

r Temperatur

e Type K Thermocoupl

e TT-319A/

B Refe

r t o th e Thermocoupl

e Calibration , Operation, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe

r Pressur e Pressur e Transmitte

r PT-300 Quarterl y -7.

5 t o -6. 5 1.

5 t o 2. 5 i n w.c . 10

% ES V Position Position Switc h . ZS-32

4 Annually AWFC O interloc k energize

d whe n ope n Pas

s Baghous e Inle tTemperatur

e Type K

Thermocoupl

e TT-37 0 Refe r t o th e Thermocoupl

e Calibration , Operation , an d Replacemen

tProcedur

e Combustio

n Ga s Flow Rat

e d

P Cel l FT-38 3 Annuall y 0-0.0

5 in . w.c . 0.45-0.5 0 in . w.c . 10

% Stac k Ga s Oxyge n Concentratio

n Zirconiu

m Oxide Analyze r AT-38 9 Pe r CEM S Q A Pla

n Stac k Ga s Carbo n Monoxide Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconiu m Oxid e Oxyge n Analyze r AT-388E . Pe r CEM S Q A Pla

n Stac k Hydroge

n Chloride Concentratio

n Multicomponen t Infrare d Photomete

r wit h Integrate d Zirconiu m Oxid e Oxyge n Analyze r AT-388E . Pe r CEM S Q A Pla

n Stac k Ga s Moistur

e Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconiu m Oxid e Oxyge n Analyze r AT-388E . Pe r CEM S Q A Pla

n Stac k Ga s Oxyge n Concentratio

n Multicomponen

t Infrare d Photomete

r wit h Integrate d Zirconiu m Oxid e Oxyge n Analyze r AT-388E . Pe r CEM S Q A Pla

n

1 6Tabl e 2- 1 (continued ) CM S Calibratio n Audi t Requirement s

J Applicatio n Instrumen t Ta g Numbe r Frequency o f Drif t Check/Accurac y Audi t Lo w Leve l Chec k Point Hig h Leve l Chec k Poin t Toleranc e Uni tNo . 4 Wast e Feedrat

e t o X-1 0 Nozzl e Mass Flowmete r FT-12 9 Annuall y 0-

5 lb/min 15-2 5 lb/mi n 10 % Wast e Feedrat

e t o X- l 1 Nozzl e Mass Flowmete r FT-13 8 Annuall y 01b 21,00 0 l b 10

% Wast e Feedrat

e t o X'1 2 Nozzl e Mass Flowmete r FT-14 5 Annuall y 0-

5 lb/mi n 15-2 5 lb/mi n 10 % Wast e Feedrat

e t o X-2 2 Nozzl e Mas s Flowmete r FT-21 2 Annuall y 01

b 21,0001b 10 % Clam Shell Fee d Weigh t (shredde d solids ) Loa d Cel l WT-00 1 Quarterl y 01b - -20 0 l b 10

% | Drum Conveyor Solid s Weigh t Loa d Cel l WT-014A Quarterly . 01b • ~ 10 0 l b 10

% Auxiliary Conveyo

r Solids 1 Weigh

t Load Cel l WT-14 B Quarterl y . . 0 l

b -5 0 l b 10

% Primar y Combustio

n Chambe

r Temperatur

e Pyromete r TT-305A/ B Replac e a tleas tannuall y wit h factor y calibrate

d Pyromete

r Secondar y Combustio

n Chambe

r Temperatur

e Typ e R Thermocoupl

e TT-317A/

B Refer t

o th e Thermocouple ' Calibration , Operation, an d Replacemen

tProcedur

e Primar y Combustio

n Chambe

r Pressur e Pressur e Transmitte

r PT-300 Quarterl y -9.0 t

o -8. 0 in . w.c. 0 t

o 1. 0 in. , w.c. 10 % Surg e VentPositio

n Position Switc h ZS-026 Annually AWFC O interloc k energize

d whe n ope n . Pas

s ES V Positio n Position Switc h ZS-32

4 Annuall

y AWFC O interloc k energize

d whe n ope n Pas

s Carbon Feedrat

e Feede r WT-43 8 Quarterl y 0 lb/min 6-3 0 lb/min , 10 % J Carbon Injection'Carrie r Ga s Lo w Pressur e Pressur e Switc h PSL-438 A Annuall y Energiz e Switc h Pas s Carb6 n Injectio

n Carrie r Ga s Hig h Pressur

e Pressur e Switc h PSH-438B Annually Energiz e Switc h Pas s

< m c o 

### o o r o o 0 0 C O 1 7Tabl e 2- 1 (continued ) CM S Calibratio n Audi t Requirement s Applicatio n Instrumen t Ta g Numbe r Frequenc y of Drif t Check/Accurac y Audi t Lo w Leve l Chec k Point Hig h Leve l Chec k Point Toleranc e Uni tNo.' 4 (continued) SD A X-1 8 Outle

tTemperatur

e (Baghous

e Inle tTemperature

) Type K Thermocoupl

e TT-417A/

B Refer t

o th e Thermocoupl

e Calibration , Operation , an d Replacemen

tProcedur

e SD A X-1 9 Outle

tTemperatur

e (Baghous

e Inle tTemperature

) Type K Thermocoupl

e TT-418A/

B Refer t

o th e Thermocoupl

e Calibration , Operation , an d Replacemen

tProcedur

e Combustio

n Ga s Flowrat

e Pito

tTube/d P Cel l FT-559A/

B Annuall

y 0 in . w.c . 1.7

4 i n w.c. 10 % Stac k Ga s Oxyge n Concentratio

n Zirconiu m Oxide Analyzer AT-560A/ B Pe r CEM S Q A Pla

n Stac k Ga s Carbo n Monoxide Concentratio

n Stac k Hydroge

n Chlorid

e Concentratio

n Stac k Ga s Moistur

e Concentratio

n Stac k Ga s Oxyge n Concentratio

n Multicomponen t Infrared l Photomete

r wit h Integrate

d Znconium Oxide Oxyge n Analyzer AT-556 E Pe r CEM S Q A Plan2. 3 Preventiv e Maintenanc e Ony x take s dail y proactiv e measure s to assur e tha t potential problem s wit h th e CM S ar e quickl y identifie dan davoided , i f possible . Dail y maintenanc e check s mclude :

• Verificatio n tha

t proces s variable s are reasonabl e • Compariso n o f

reading s fro mredundan t instrument s • Cleanin g an dvisua l chec k o f monitorin g equipmen

t • Communicatio n betwee n operator s an dinstrument technician s Thes e check s ar

e documente do n adail y logsheet fo r eac h incinerator. " Th e preventiv e maintenanc e o n th e CM S als o include s th e cahbratio n audit s previousl y described . Al l necessar y part s fo r routin e repair s o f

the affecte dCM S equipmen t ar e made readil y availabl e onsite . A spar e part s inventor

y fo r eac h componen

t o f the CM S i s include di n th e record s maintaine db y the Maintenanc e Department . Additiona l detail s regardin g preventiv e maintenanc e applicabl e t o th e CM S ar

e provide di n the facility' s Operatio n an dMaintenanc e Pla n an dth e CEM S Q A Plan .

1 9

V E S 00209 13. 0 CM S RECORDKEEPIN G AN D REPORTIN G Thi s sectio n discusse s recordkeepin g an dreportin g requirement s fo r CM S instrumentatio n a

s specifie db y . § 63.1211 . 3. 1 Recordkeepin g Ony x wil l follo w the recordkeepin g requirement s a s specifie di n § 63.10(b), . includin g the semiannua

l exces s emission s an dCM S performanc e repor t Ony x wil l maintai n thes e record s o f

CM S datafo r

ammimu mo f

5 year s followin g tb e dat e o f eac h occurrence , measurement , maintenance , correctiv e action , report , o r record . A t

aminimum , th e mos t recen t 2 . years o f

datawil l b e retaine donsite . Belo w i s abrie f summar y o f thes e requirements . Ony x wil l maintai n record s o n th e following :

• The . occurrenc e an dduratio n o f eac h startup , shutdown , o r malfunctio n o f operation . • The occurrenc e andduratio n o f eac h malfunctio n o f

th e a h pollutio n contro l andmonitorin g equipment . Maintenanc e performe do n th e ai r pollutio n contro l an dmonitorin g equipment • Action s taken durin g period s o f startup , shutdown , an dmalfunctio n (includin g correctiv e action s t

o restor e th e proces s o r

a h pollutio n contro l systemto normal operation ) whe n suc h action s ar e differen t

th e procedure s outline di n th e SSM P

• Al l infonnatio n necessar y t o demonstrat

e conformanc e wit h th

e SSM P

• Eac h perio di n whic h aCM S i s malfunctionin g o r inoperativ e (includin g out of-contro l periods )

• Al l requhe dmeasurement s neede dt o demonstrat e complianc e wit h arelevant standard . • Al l result s o f

performanc e tests , CM S performanc e evaluations , andopacity an dvisibl e emissio n observation s • Al l CM S cahbratio n check s • Al l adjustment s an dmaintenanc e performe do n CM S

• Al l require dCM S measurement s (includin g datarecorde ddurin g unavoidabl e CM S breakdown s an dout-of-contro l periods ) . • Th e dat

e an dtime identifyin g eac h perio ddurin g whic h the CM S wa s inoperativ e except

fo r zer o (lo w level ) andhig h leve l check s

2 0• Th e dat e an d tim e identifyin g eac h perio ddurin g whic h th e CM S wa s out-of

contro l as define db y § 63.8(c)(7 )

• Th e specifi c identificatio n (dat e an d time o f

commencemen

t an d completion ) o f eac h perio d o f

exces s emission s and paramete r monitorin g exceedances , a s define di n th e relevant

standard , tha

t occur s durin g period s other than startup , shutdowns , an d malfunctions.

• Tb e natur

e an d caus e o f

any malfunctio n • Th e correctiv e actio n take n o r preventiv e measure s adopted

• Th e natur

e o f th e repair s p r

adjustment s to fh e CM S tha t wa s inoperativ e o r out-of-contro l

• Th e tota l proces s operatin g time durin g the reportin g perio d

• Al l procedure s tha t ar e par t o f quaht y contro l progra

mdevelope d an d implemente d fo r

CM S unde

r § 63.8(d) . A l l CM S mstrumentatio n wil l b e operated o n acontinuou s basis . Th e detector respons e wil l b e evaluate d a

t leas t ever y 1 5 seconds , an d thes e value s wil l b e use d t o calculat e regulate d parameters . Fo r parameter s interlocke dwit h th e AWFC O syste mo n an hourl y rollin g average basis , ra w dat awil l b e average d an d recorde d a t leas t onc e per

minute . On e minut

e average s wil l b e use d to calculate th e hourl y rollin g averages . Th e pumpabl e waste , total waste , and constituent feedrat e operatin g paramete

r limit s ar e base s o n rollm g total s i n lie u o f

rollm g averages . A n integral par

t o f the CM S i s the dat

aacquisitio n an d datahistorian systems , whic h record s al l operatin g datagenerate d b y th e CM S instruments . Th e dat ahistoria n an d associate d archiv e files ar e par t o f th e operatin g record . CM S instrumen t calibrations , maintenanc e activities , an d correctiv e action s ar e recorde d an d kep t

i n th e operatin g record . Al l datacollecte d durin g CM S PET s ar e recorde d and kep t

i n the operatin g record . . 3. 2 Reportin g Ony x wil l follo w th

e reportin g requhement s a s specifie di n § 63.10 . I n addition , Ony x wil l develop an d includ e i n the operatin g recor d aDocumentatio n o f Complianc e (DOC ) pe r § 63.1211(c) . Th e DO C mus t includ e asigne d and dated certificatio n tha t the CEM S andCM S ar

e installed , calibrated , and continuousl y operatin g i n comphanc e wit h the requirement s o f

Subpar t EEE .

2 1Ra w dat afromthe CM S wil l b e collected , reduce das describe din . § 63.8(g) , an d include di n the CM S PE T report . Thi s dat awil l b e analyze dto determin e compliance . wit h the HW C MAC T andfh e result s wil l b e submitte da s par t o f th e notificatio n o f complianc e requhe db y § 63.1207(j) . Th e conten

t an ddeadlin e requirement s fo r the exces s emission s an dmonitorin g syste m performanc e report s ar

e specifie di n § 63.10(e)(3)(v) . Th e requhement s fo r th e summar

y repor t ar e give n i n § 63.10(e)(3)(yi) . A s note di n § 63.10(e)(3)(vii) , Ony x i s require dt o onl y submi t

th e summar

y repor t i f the total duratio n o f

exces s emission s o r

proces s o r

contro l systemparamete r exceedance s fo r the reportin g perio di s les s than on e percent o f th e total operatin g tim e fo r th e reportin g period , andCM S downtim e fo r the.reporting , perio di s les s tha n five percent

o f th e tota l operatin g tim e fo r

th e reportin g period . Conversely , additiona l reportin g i s requhe db y § 63.10(e)(3)(viii ) i f

th e tota l duratio n o f

exceedances , or

the total CM S downtim e durin g th e reportin g period , i s greate r tha n th e allowabl e percentag e o f th e reportin g period . Tabl e 3-1 . provide s alis t

o f Onyx' s reportin g requirements .

2 2Tabl e 3- 1 Reportin g Requirement s Regulator y Citatio n Descriptio n Frequenc y § 63.1211(c ) Recor dDocumentatio n o f Complianc e i n th e operatin g record Onc e § 63.10(d)(2 ) Befor e Titl e V permi t ha s bee n issued , owner

operato r mus t submi t result s o f

performanc e test . B y the 60t h day followin g every performanc e tes t § 63.10(d)(2 ) Afte r

Titl e V permi t

ha s bee n issued , owne

r operato r mus t submi t result s o f

requhe dperformanc e tests . B y th e 60t h da y followin g requhe d performanc e tes t § 63.1.0(d)(4) Progres s report s A s specifie di n writte n extensio n o f complianc e § 63.10(d)(5)(i ) Periodi c startup , shutdown , an dmalfunctio n report s

(durin g reportin g period ) Submitte d simultaneou s wit h exces s emissio n repor

t § 63.10(d)(5)(ii ) Startup , shutdown , an dmalfunctio n report s whe n

action s ar e take n tha

t ar e inconsistent

with SSMP . 2 workin g day s from•

commencemen

t o f action , followe dwit h a letter explainin g exten

t withi n 7 workin g days . § 63.10(e)(3)(i ) Submittal o f semiannual exces s emission s andCM S performanc e repor

t Semiannuall y - b y th e 30t h da y followin g th e en do f eac h calenda

r hal f perfomianc e tes t

2 3

V E S 00209 54. 0 CM S CORRECTIV E ACTION S I f aCM S i s foun dt

o b e out-of-control , inoperative , o r malfunctioning ; correctiv e action s mus t b e taken t

o retur n the CM S t

o norma l operation . Definition s use di n determinin g the typ e o f

correctiv e actio n require dar e give n below . Out-of-control: A CM S i s out-of-contro l if :

• Th e zero (lo w level) , mid-level , o r high-leve l calibratio n drif t exceed s tw o time s th e applicabl e C D specificatio n i n th e applicabl e performanc e specificatio n o r

procedure ; o r

. • The CM S fail s aperformanc e tes t audit , relativ e accurac y audit , relativ e accurac y tes t

audit , o r hhearity tes t

audit . Th e onl y applicabl e performanc e specificatio n t o the CM S i s Performanc e Specificatio n (PS ) 4 B o f

4 0 CF RPar

t 63 , Appendi x B . P S 4 B applies't o fh e 0 2an dC O CEMS . Th e requhement s o f

P S 4 B an dadditional requhement s Ony x impose s o n th e CEM S ar e detaile di n th

e CEM S Q A Plan . I n th e absenc e o f

promulgate dperformanc e specificatio n applicabl e t

o non-CEM S CM S instruments , Ony x has self-impose dahigh-leve l C D specification , as describe di n Sectio n 2.0 . Whe n aCM S i s out-of-control , Ony x wil l take th e necessar y correctiv e actio n an dshal l repea t al l necessar

y tests whic h indicat e tha t th e systemi s out-of-control . Correctiv e action s an dretestin g wil l continu e unti l th e CM S i s returne dt o normal operation . Th e -beginnin g o f

the out-of-contro l perio di s th e hou r tha t th e cahbratio n drif

t indicate s tha

t the CM S has exceede dit s perfonnanc e specifications . Th e endo f th e out-of-contro l perio di s th

e hou r followin g the completio n o f correctiv e actio n an dsuccessfu l demonstratio n tha

t the CM S i s withi n it s allowabl e hmits . Durin g the perio dthe CM S i s out-of-control , recorde ddatashal l no t b e use di n dat

aaverage s an dcalculations , o r t o

. mee t any dat aavailabihty requiremen t establishe dunde

r thi s part . Ony x wil l submit

al l infonnatio n concernin g out-of-contro l periods , includin g star t an d en ddate s andhours , anddescription s o f correctiv e action s taken , i n the exces s emission s an dcontinuou s monitorin g systemperformanc e repor t require db y § 63.10(e)(3) . Malfunction: Fo r

us e i n thi s plan , malfunctio n i s define das an y sudden , infrequent , an d no t reasonably preventabl e failur e o f ai r pollutio n contro l o

r monitorin g equipment .

2 4Malfunctio n als o include s th e failur e o f aproces s o r

any proces s equipmen

t to operat

e i n anorma l or

usua l manner . Failure s tha t ar e cause d i n par

t b y poor maintenanc e o r careles s operatio n ar

e no t malfunctions . Th e Program of

Corrective Actions for

Malfunctions i s Attachment 4 o f the SSM P Plan . Thi s progra

maddresse s ho w the incinerato r wil l b e operate dan

dmaintaine ddurin g malfunctions . I n thi s program , potential malfunction s ar e hsted . fo r

each portio n o f

th e incinerato r

system . Th e malfunction s ar e event s tha

t ar e recognize db y the operator , o r indicate db y a n alarm , an dthreate n to caus e an exceedance . I n th e respons e t

o th e malfunctio n and/or

alarms , th e operator

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

syste mwithi n regulator y , limits . I n th

e progra mo f correctiv e actions , potentia l cause s o f

eac h malfunctio n ar

e hsted . Th e operato

r wil l utiliz e proces s knowledge , jo b experience , and > i f needed , assistanc e fromothe r personne l t

o identif y th e caus e o f th e malfunction . Fo r

each potentia l cause , action s t o correc t th e failur e ar

e hsted . Th e correctiv e action s prescribe dma y requh e th e collaboratio n o f multi

discipline dpersonne l wh o ar e quahfie dt

o retu mth e incinerato r

syste mt o proper workin g condition s (i.e. , maintenanc e personnel , instrument technicians , engineering) .

2 5