### (



# ( .' VEOLIA ENVIRONMENTAL S ERVICES, INC. P ROGRAM OF CORRECfiVE A CTIONS FOR MALFUNCflONS 1.7.4 . 

### In case 

### ofmechanical/electrical failure ofactuated 

### valve/dlunper : 1.7.4 . 1. Identify 

### cause ofactuation 

### failure. 1.7.4.2. 

### Service/replace electrical and/or 

### pneumatic components, as needed . 1.7 

### .4 .3. Service/replace 

### actuator and/or valve 

### components, as needed . 1.7.5. In case 

### of physical/electrical failure 

### o f control system component: I.

7 .5.1. Identify faulty 

### control system 

### component . I.

7 .5.2 

### Service/replace control system components, as 

### needed . 1 .8.**Rx~e** Air la- leaklge ill Air 

### PoDotio n Control System 1.8.1 

### In case 

### o!boles due to 

### corrosion: 1.8.1.1. Identify 

### location ofhole. 1.8.1.2. Repair system as needed . 1.8.2 

### In caSe 

### of open ports , manways , 

### access ports, etc . 1.8.2.1. Identify 

### loc ati on ofopen port, 

### manway, etc . 1.8.2.2 . 

### Rep l ace cover on 

### open port, 

### manway , etc.



### Page4 of26 

## , . !·

VES 004000/



## ,:· \ r ' •. VEO LIA E NVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECTIVE A CTIO NS FO R MALFUNCTIONS 2 .0 PRIMARY COMB US TIO N CHAMBER 2.1. Loss of Natural Gas l're ss un/Fiow to l'CC Main 

### B llr ne r 2 . 1. 1. h1 case of plugging/physical failure ofline or line compon<mt: 2. 1. t.l. Identify the location ofplugging or line faillll'e . 2.1.1.2. Clear line ptugging and/or service/replace fauhy line cOm.ponents, as needed. 2.1.2. 

### In case of meobanie8l/el ectrical failure ofactllated valve : · 2 . 1.2.1 . Identify 

### cause ofactuatio n failure. 2.1.2 . 2. Service/replace electrical and/or pneumatic components, 

### a.s needed. 2 .1.2.3. Service/replace actuator and/or valve components, as needed. 2.1.3. 

### In case of physical/electrical failure of control system component: 2.1.3.1. Identify faulty control sys tem component. 2.1 .3. 2. Service/replac e control system components, as needed. 2.1.4. In 

### case of meobanicallelectrical failure at natural 

### gas supply source: Identify the cause of the failure . 2.1.4.1. 2.1.4.2 . Take the neceswy actions to restore the supply of oatur.ll gas. . 2.2. Loss o f Combutloo Air PTessoreiF!ow to l'CC 2.2.1. In case ofmecbanicaVelectrical failure of combustion 

### air blower: 2.2.1.1. Diagnose blowerldrive f ailure. 2.2.1 . 2. Service/replace the bloweddrive, as needed. . 2.2.1.3. Restore electrical power supply to the blower . 2.2.2. In case ofphysical fai l ure ofcombu stion air duct: 2.2.2.1. Identify 

### the location of duct failure. 2.2.2.2 . · Service/replace faulty duct, as needed . 2.2.3. 

### In case ofmecbanicallelectrical failure of actuated valve: 2.2.3.1. Identify cause of actuation failure. 2.2.3.2. Service/replace electrical and/or 

### ptlCU11latic compooems, 

### as needed. 2.2 . 3.3. Servicehq>lace actuator and/or valve components, as 

### needed. PageS of26 

## ,. VES 004001

### VEOLIA ENVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTION$ { 2.2.4 . In case ofphysical/electrical failure ofcontrol system component: 2.2.4 . 1. Identify faulty control system component. 2.2.4 . 2. Semcelreplace control system componeats, as needed. 2.3. PCC MaiD 

### Bune r Pil ot Failure 2.3 . 1. For loss of

### natural gas pressure/flow, see 2.1. t 

## .. 2.3.2. For loss ofcombustion air pressure/flow, see 2.2. 2.3.3 . 

### 1n case of physicaVelectrical failure ofigniter: 2.3.3.1. Identify cause ofigniter failure. 2.3.3.2. Service/replace igniter and/or associated**c~nents,** as needed. 2.3.4. In case ofphysicaVelectrical failure ofcontrol system component: 2 . 3.4.1. Iden t ify faulty control system component. 2 . 3.4.2 . Service1replace control system components, as needed. 2 . 4 . Loss of Waste Flo w to PCC Injector 2.4.1. In case ofmechanicaVelectrical failure ofwaste feed p wnp: 2.4.1 . 1. Diagnose pump/drive failure . 2.4 . 1.2. Service/ replace 'the pump/drive, as needed.**(!~ \**  2 . 4.1.3. Restore e lectrica l power supply to the pump . 

### .. 

# . ; . . . 2.4.2. In case oflow nitrogen pressure, see 1.4 . 2.4.3 . In case ofplnggingfphysical failnre of line or line component: 2.4.3.1. Identify the location ofplugging or line failure. 2.4.3.2. Clear line**plu~ ng**  and/or service/replace faulty line components, as needed. 2 . 4.3.3. Restore/co nfirm ' functional heat tracing, 

### ifapp licable. 2.4.4. 

### 1n case ofmechanical/electrical failure of actuated valve: 2.4.4.1. Identify cause of actuation failure. 2.4 . 4 . 2. Service/repl ace electrical and/or pneumatic components, as needed. 2.4.4.3. Service/replace actuator and/or valve components, as 

### neede4. 2.4.5 . In case of physicaVeleetrical frulure of control system component: 2.4.5.1. Identify faulty control system component. 2.4.5 . 2 . Service/repl ace control system components, as needed. 25. Loss of Waste Feed rat e C ontrol to P CC Inj ector

•' 

## t 2.5.1. 

### 1n case of loss of waste pressure/flow to PCC injector, see 2 . 4. Page6of26 VES 004002

### / 

### '



# ( ' \


### .. ......



# ,. · .. VEOLIA ENVJRONMENTAL SERVICES, INC. PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTION S

2.6.

2.7. 2.5.2. In case of physical/electrical 

### failure of fio:N 

### transmitter: Service/replace 

### flow lniOsmitter 

### and/or associated 

### instrumentation, as needed . 2:5.3 . In case of actuated valve failure: 2.5.3.1. 

### Identify cause ofactuation 

### failure. 2.5.3.2 . Service/replace electrical and/or pneumatic components, 

### as needed. 2.5.3.3. Service/ replace actuator and/or valve components, as needed. 2.5.4 . In case ofpbysical!electrical failme ofc:ootrol system component: 2.5.4.1. 

### I dentifY faulty control system component. 2.5.4.2. Service/replace control system components, as needed . Loss of A t omization Air Piess u re to a P C C Injector 2.6 .1. For a total loss ofplant/instrument 

### air Sllj)ply, sec 1.3. 2.6.2. In case 

### ofplugginglpbysical failuie 

### of line or line 

### component : 2.6.2. 1. I dentify the location of

### plu gging or line failure. 2 . 6.2.2 . Clear 

### line plugging and/or service/replace faulty line components, as needed. 2.6.3. In case of mccbanical/physical failure of pressure control valve: Service/replace pressure control valve, as needed. Loss of PCC Draft Coatrol (Unit 4 ) 2.

7.1. In ease ofiD fan**fail~.We,** see 9.5 2.

7 .2. In case of 

### pbysical!ek>clrical failure of kiln pressure 

### tr.msmitter. Service/replace pressure transmitter andlot' 

### associated instrumentation, as needed. 2.7.3. In case of actuated damper failure: 2 .7.3.1. Identify cause of actuation 

### failure. 2 . 7.3.2 . Service/rep lace and/or pneumatic components, as needed. 2.7 .3.3. Service/replace actuator and/or damper components, as needed. 2 . 7.4. In case of physical/electrical failure of

### control system component 2 .7 .4.1. 

### Identify faulty control system component. 2.7. 4 .2. Service/rep lace control system components, as ncoded . Page 7 of26 VES 004003

# ( VEOLIA ENVIRONMENTAL SER VIC ES , INC . PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCFIONS Z.8 . L oss ofPCC Temperature Control 2.8.1. In 

### case ofloss of natural gas 

### pressure/ flow to main burner, see 2.1. 

### 2.8.2. In 

### case of l oss ofwaste p ressure/fl ow to 

### PCC injector, see 

### 2 . 4. 2.8.3 . In 

### case ofphysical/electrical failure oftemperature element: 2.8.3.1. Service/rep l ace f aulty temperature e lement l!J:Id/ Or associated instnnnentation, as 

### needed. 2 .8.4. In 

### case ofphysicallelectric al failure ofcontrol sys t em component: 2.8.4.1. 

### Identify faul t y control system component 2 . 8 . 4.2. 

### Service/rep l ace control system components , 

### as needed. Z.9. Flame Fallure 2.9. I. In 

### case of pbysicallelectrical failure offlame detec tor. 2.9. 1. 1. 

### Identify fil uhy 

### flamedetectorcompouenl 2.9.1.2 . 

### Service/replace 

## flame de tector compOnents, as needed. 2.92. In 

### case ofphysical/electrical · failure ofcontrol system 

### component : 2 . 9.2 .1. Identify fa ulty control sys tem component 2.9 . 2.2. 

### Service/replace control system components, as 

### needed. l.lO . 

### K.lbi Rotati o n Malfunction (Unit 4) 2. 1 O.l.ln 

### case o f mechanical/electrical kiln 

### drive system: 2.10 .1. 1. 

### Diagnose drive failure . 2.1 0 . 1 .2 . 

### Service/ replace the drive, as 

### needed . 2. 10. 1. 3. Restore e lectrical power supply to moto r. 2.1 0.2 . In 

### case of physical/electrical f ailur e of kiln 

### rotational speed 

### transmitter: Service/replace tnmsmitter 

### and/or associated instrumentation, as 

### needed . 2 .10 .3.1n case 

### o f physical/electrical fai l ure o f control system component: 2 . 10.3 . 1 . 

### Identify faulty control 

### system component. 2.1 0.3.2 . 

### Service/repla ce control system components, as 

### needed. 2 . 11. BallciCharge Feed Door Malluaclion 2.11 . 1. In 

### case ofmecbanicall electric . al failure ofactuated door: 2.1 1.1.1. 

### Identify cause 

### ofactuation 

### failure. 2.11.1 . 2 . 

### Service/repl ace electrica l, hydraulic, and/or pneumatic components, as needed . 2.11.1.3. 

### Service/replac e a ctuator and/ or valve components, as needed . 2 . 1 12.1n 

### case ofphysical/electrical f ailure of control system component: Pa ge 8of26 : :

VES 004004

### ,. ;**~·** 

# . . 

# . . VEOLIA ENVIRONMENTAL S ERVICES , INC . PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 2. 1 1.2. 1 . Identify faulty oontrol system component. 2.11.2.2 . Service/replace control 

### system components, as n eeded . 2. 1 2. PhysicaiiMecbauical Internal Equi pment Failure 

### 2. 1 2.1. In case of

### refractory failure, repair / replace refractory 2 .1 2 . 2. In case 

### of ash 

### collection fai lure 2 . 12.2.1. Diagnose 

# am collection system 

### failur e 2.12.2 . 2 . Service/repl ace ash 

### collection system 

### components, as 

### needed. 2.13. PCC Seal VIsual 

### Emissions Monltoriag aud Recording System 

### 2.13 . l.lo case of physic al/electrical failure of camera, seTVice/n:place 

### camera. 2, 13.2 . lo case of physical/e lec trical failwe of 

### monitor, service/replace 

### monitor. 2.13.3.ln case 

### of physical/electrical fai lure of recording system, 

### service/replace recording system. 

### 2.14 . Rapid Steam Generation from Ash CollectiOn System Water 2. 1 4. l .ln case of refractory failure, repair/replace refractory. 2.14 . 2.ln case oflDlcontrolled move ment/dropping o f residue into ash collection sy;1em water, insp ect system to 

### ide n ti.Jy/remove other suspect material.



### Page9of26 VES 004005

# c VEO LIA ENVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 3.0 SECONDARY COMBUSTION CHAMBER 3.1. Loss of Natural 

### Gas Pressure/Flow to SCC Maln Burner 3.1.1. In**~ase** ofplnggin&'J>hysical failure ofline 

### or line component: 3.1.1.1. IdentifY the 

### location ofplugging 

### or line failure. 3.1. 12. Clear line plugging and/or se.JVicelreplace faulty line components, 

### as needed ' . 3 . 12. In case ofmechanicallelectrical failure ofactuated valve : 3. I .2.1. IdentifY cause ofactuation failure. 3.1.2.2. Servicelrepl ace electrical and/or pneumatic components, 

### as needed. 3.1.2.3. Service/repl ace actuator and/or valve components, as needed. 3.1.3 . 

### In case of physicaVelectrical failure ofcontrol system component: 3.1.3. J. IdentifY fanlty control system component. 3.1.3.2. Service/replace control system components, as n eeded. 3.1.4 . In case of mechanicallelectrical failure at natural 8ll$ supply sourre: 3 . 1.4.1. IdentifY the cause of the failure. 3.1.4.2. T ake the necessary actions to restore the supply of natural gas. 3.2. Loss of CombnstioD Air Pr essure/Flow to SCC 3.2.1 . 

### In case ofmecbanicallelectrical failure ofcombustion 

### air blower: 3.2.1.1. Diagnose blower/drive failure. 3.2.1.2. Service/replace the blower/drive , 

### as needed. 3 . 2.1.3. Restore electrical power supply to the blower. 3.2.2. In case ofphysical failure combustion air duct: 3.2.2.1. IdentifY the location ofduct failure. 3.2.2.2. Servicelrepl ace faulty duct, 

### as needed. 3.2.3. In case of mechanical/ electrical failure ofactuated valve: 3.2.3.1. IdentifY cause ofactuation failure. 3.2.3.2. Service/replace electrical and/or pneumatic components, as needed . 3.2.3.3 . Service/replace actuator and/or valve components, as needed. Page l0o f26 VES 004006{



## . 

# ( ' · .

\ VEOUA ENVffiONMENTAL SERVlCES, INC. 

### PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 3.2 . 4, In case ofphysical/electrical failure ofcontrol system component : 3.2 . 4 . 1. Identify fau l ty control system component 3 . 2.4.2 . Serv:icelrep . lace control system components, as needed. · 3.3 . SCC Main Burner lgJJition FIU!ure 3.3 . 1. For . Joss ofnatural 

### gas pressure/flow, 

### see 3 . 1. 3 .3 .2. For loss ofcombustion air pressure/flow, see 3 . 2 . 3.3.3. In case ofphysical/electrical failure ofigniter: 3.3.3.1. Identify cause ofigniter failure. 3.3.3.2. Service/replace igniter · and/or associated components, as needed. 3 .3.4. In case o f physical/electrical failure ofcontrol system component: 3.3.4 . 1. Identify faulty control system 

### component . 3.3.4.2. Service/rep l ace control system 

### components , as needed. 

### 3 .4 . L oss ofWaste Flow to SCC 

### IDjector (U nit 4)



### 3.5. 3.4.1. In case ofmecbanical/electrical failwe ofwaste feed pump: 3 .

4.1.1. Diagnose pump/drive failure . 3.4.1.2. Service/replace th e pump/drive, as needed . 3.4.1.3. Restore electrical power supply to the pump. 3.4.2 . In case of low nitrogen pressure, see 1 .4 . 3 . 4 . 3 . In case of plugginglpbysical fai l ure of line or line component: 3.4.3.1. Identify the location of plugging or line failure . 3.4.3 . 2. Clear line plugging and/or service/replace faulty line components, as needed. 3.4.3.3. Restore/confinn functio nal beat tracing, 

### if applicab le . 3.4.4. In case ofmechanical/electrical failure of actuated valve: 3.4 . 4.1. Identify cause ofactuation failure. 3.4.4.2. Service/replace electrical and/or pneumatic eomponeniS, as needed. 3.4.4.3. Service/replace actuator and/o r valve components, as needed . 3 .4.5 . In case ofphysical/electrical fai lure ofcontrol system component: 3.4.5.1. I dentify fault y control system component 3.4.5 .2. Service/replace control system components, as needed. 

### Loss of W aste Feednte 

### Co ntrol to SCC Inj ector (Unit4) 3.5.1. In case ofloss of waste pressure/flow to 

## sec injector, see 3.4 . Page 11 of26 

## , . ?



### VES 004007VE OLIA ENVIRONMENTAL SERVICES , INC. PROGRAM OF CO RRECTIVE ACTION S FO R MALFUNCTION S 3.5.2. In case of physicallelectri . cal failure of flow lnlnsmitter:**Servic~replace** flow trunsmitter and/o r associated instrumentation, 

### as needed. 3.5.3. In case ofac tuated valv e failure : 3.5.3.1 . Identify 

### cause of acruation failure. 3 . 5.3.2.**Servic~rep l-..ce**  electri cal and/or pneuma ti

c components, 

### as needed. 3.5 . 3.3 . Service/replace actuator 

### and/ or valv e components, 

### as needed. 35.4 . In case ofphysicalfelectrical failure of oootrol system component: 3.5.4 . 1 . Identify faulty control system component 3.5.4.2 . S ervioelreplace control system components, as needed. 3.6. L oss of Atomi2•tlon Air Pressure to a SCC blj ector 3 .6 .1. For 

### a total 

### loss ofplant/instrument 

### air supply, see 1.3. 3 . 6.2 . lo case ofp l ugging/physical failure ofline or line compo nent : 3.6.2.1. Identi fy the location of p lugging o r line fail ure. 3 . 6.2.2. C l ear 

### line plugging and/or**semc~bce** faulty line ( · components , 

### as needed.



### (



## .. 3.6.3 . lo case of mechanicallpbysical failure of pressure control valve: Service/replace pressure control valve, as needed. 3.7. Lon o f SCC Tem p eratltre C oa trol 3.7.1. In 

### case of loss ofnatural gas pressure/llow to main 

### burner , see 3 . 1. 3.7.2 . lo caseof!oss ofwaste p ressure/flow to 

## sec inject«, see 3.4. 3.7.3. lo case ofphysical/electrical failure oftempeoatur e element : 3.7.3.1. Service/ rep lace faulty temperature element and/or associated inslniaientation, as needed. 3 . 7.4. lo case ofphysieallel ectrical failure ofcontrol system componen t: 3.7.4.1. Identify faulty control systein component 3 .

7.4.2. Servioelrcplac e control system components, as needed. 3.8. Flame Failllre 3.8 . 1. lo case of physicallel ectrical failure of flame detector: 3.8. 1 .1. Identify faulty flame detector component 3.8.1.2. Service/replace flame deteeiOr components, as needed. 3.8.2. 

### In case ofph)'licallel.wlcal failure ofcontrol system component: 3 . 8.2.1. Identify faulty control system compcmenl Page 12 ofl6 VES 004008

# ( . . : • .



### . . . VEOLIA ENVIRONMENT AL SERVI CES, INC. PROGRAM OF CORRECTIVE AC'flONS FOR MALFUNCTIO NS

. 3 .S.2 .2 . 

### Service/replace control sys tem components, 

### as needed. 3.9. PbysiC211Me chauica llnt e roal Eqoipmeot Failur e 3.9.1. 

### In case ofn:fract o ry failure, repair/rep l ace refractory. 3. 10 . 

### Low Water Level in 

### S l ag Collection Sys tem (Uolt4) 3 .1 0.1. 

### For 

### a loss of process w ater pressurefflow, 

### see 1.6 . 3 . 10.2 .ln 

### case of physicaV mecbanical failure 

### of level controller: Service/replace faulty level controller and/or associated components , 

### as n eeded. 3.1 0.3.ln 

### case ofphysicaVmecbanical f ailure of actuated valv e : . 3.10.3 . 1 . 

### Identify 

### cause of a ctuation 

### failure. 3. 10.3.2. 

### Service/rep l.ace pnewnatic components , 

### as needed. 3.1 0.3 . 3. 

### Service/r epl ace actuator ami/o r valve components, 

### as needed. 3.1J. 

### Emergency S af ety Veo t 

### OpelliDg 3 . 11. 1. 

### Respond to 

### an emergency safety vent openin g 

### in a manner consistent with the E mergency Safety Y ent Plan. 3 . 1 1 .2.ln 

### case ofmechanical fai l ure of the 

### al:IUator: 3.1 1 .2.1. 

### Identify cause 

### ofactuation fai lure . 3.1 1.2 . 2 . 

### Service/replace emergency safety v ent components, 

### as needed. 3.12 . Rapid Steam Gen e ration 

### Crom As h Collection Sy stem Water 2.14.1. 

### In case ofrefractory failur e, repair/replace refrac tory . 2 . 14.2.ln 

### case ofuncontrolled movement/dropping ofresi due 

### into ash 

### collection 

### system water , inspect system 

### to identify/remove other 

### suspect**mat~**

Page 13 

### of26 

### 1· 1

VES 004009( 

### '



# ( VEOLlA ENVIRONMBNI' 

### AL SERVICES , INC. PROGRAM OF C ORRECfl VE AcrJONS FOR MALFUNcrJON S 4.0 TEMPERING CHAMBER (UNlT 4) 4.1. Loss of T empering Chamber E•Jt Gas Temperature Co ntrol 4 . 1. 1. For a loss ofprocess water pressure/flow, see 1.6 . 4.1.2. 

### In case of phy sicaVelectrical failure of flow lraDSlllitter: Service/replace flow transmitt er and/or associated instrumentation, as needed. 4. 1.3 . In case ofactua ted valve failure: 4.1.3 . !. 

### Identify cause of actuation bilure. 4 . !.3.2.**Servicclrcp ~**  electrical aodlor pneumatic components, as needed. 4.1.3.3. Service/replace actuator and/or valve components, as 

### needed. 4 . 1 . 4 . In case ofphysicaVelectrical 

### failure of 

### control system 

### component: 4.1.4 .1. 

### Iden tify faulty 

### control system component. 4 .1. 4.2 . Service/ replace control system components, as needed. 4.1.5 . In case of nozzle failure, service/replace no zzle, as needed . 4.2 . Loss of Atomization Alr Pressure to Noxzle 4.2 . 1. For a total loss of plantflllSirUment air supply, see 1.3 . . 4 22 . In case ofplugging/physical failure of liM or line COJ!lponent : 4.2.2.1. Identify the location ofplugging ot line failure. 4.222. Clear line plugging and/or**service/rep~** faulty 

### line components, as 

### needed.



### Page 14 of26 VES 004010

# f.' ., "'- · VEOLIA ENVIRONMENTAL SERVICES, INC . PROGRAM O F C ORRECTIVE ACTIONS FOR MALFUNc:nONS 

### 5. 0 LJME S LURRY S YSTEM 5. 1 . Lou o f Lime Feed t o Ume S lar ry Feed Tllllk . 5.1.1. In case ofmechanical/electrical fail ure o f 

### lime slurry 

### screw fee der : 5.1.1. 1 . Diagnose feeder/drive 

### failure. 5.1 . 1 .2. SCJVicelreplace the feeder/drive, as needed. 

### 5 .1.1.3. Restore electrical power supply to the lime slurry**~** feeder. 

### 5.1.2. In case of mechanieal/electrical failure o f lime bin ac tivator/vibrator : 5.1.2.1 . 

### Diagnose lime bin activatorlvll>ralor fai lum . . 5.1.2.2. SCfVicelrcplace the lime bin activatot'lvibrator, as needed. 5.1.2 . 3. Res tore electrical power suppl y to the l ime slurry screw feeder. 

### 5 . 1. 3 . In case ofplugginflphysical failure ofline or line component: 

### 5 . 1.3.1. Identify the location ofplugging 

### or line failum. 5 . 1.3 .2. Clear line plugging 

### and/or sCfVice/rcplace faulty 

### line components, as needed. 5.1.4. In case of physical/electrical failure of lime feed controls: SCfViceln:place faulty instrumentation and/or control system components, as needed. 5.2. M alfunction t. Lime S lurry Conc en tration 5.2.1. In case o fl oss of lime feed to lime s lurry feed 

### tank. see 5.1 5.2.2. In case ofloss ofwater fl ow to lime slurry feed tank, sec 1.5 

### 5.2.3. In case of mechanical/el ectrical fail ure oflime slurry agitator : 5.2.3.1. Diagnose agitator/drive fallure. 5.2.3.2. Service/replac e the agitator/drive , as needed. 5.2 . 3.3. Restore electrical pow er SUpply to the lime s lurry agitator. 5.2.4 . In case of physicallelectrical failure of instromeotation: Serviceln:place faulty instrumenta tion, as needed. 5.2 .5. In case of physicallelectrical failure of control system component: 5.2.5.1. Identify faulty control system componeol 5.2 . 5.2. Service/repl ace control system components, as needed. Page 1 5 of26 VES 004011

# c· VEOLIA ENVIRONMENTAL SERVICES, INC . PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 6.0 UNITS 2 AND 3 S PRAY DRYER ABSORBER (SDA) 6.1. Loss of Lime 'Slurry Flow to SDA 6.) . 1. In case ofmechanical/electrical failure of lime slully feed pllrnp : 6.1.1.1. Diagnose pump/drive failure . 6 . 1.1.2. Service/replace tho pump/drive, 

### as needed. 6.1. 1.3. Restore electrical power supply to the pmnp . 

### 6.1.2 . In 

### case ofplugginglpbysical failure oflin e 

### or line component: 6.1.2. I. 

### IdentifY the location ofplugging or line failure. 6.1.2.2. ·Clear 

### line plugging and/or service/replace faulty line components. 

### as needed. 

### 6.1.2.3. Restorelcontinn functional heat tracing, if applicable . 

### 6. 1.3 , In case ofmechanical/electrical failure of actuated valve: 6.1.3.1. Identify 

### cause ofactuation failure. 6.1.3.2. Service/replace electrical 11t1dlor pneumatic components, as needed . 6.1.3.3 . Service/replace actuator and/or valve components, as needed. 6.1.4 . In case ofphysical/eleclrical failure 

### of control syst em component: 6.1.4.1. Identify faulty control system component 

### 6. 1.4.2 . Servi ce/replace control system componcmts, 

### as needed. 6.2. Loss ofLime S l lllT)' Flow Control 6.2 . 1. In case ofloss of slurry flow to SDA, see 6.1 . 6.2.2. In 

### case of physicallelectrical failure of flow transmitter. Servioe/rq>lace flow 

### transmitter and/or 

### associated iDstrumeotation, · asneeded. 6.2.3. In case ofactu ated valve failure: 6.2.3 . 1. I dentify cause ofactuation failure . 6.2.3.2. Service/replace electrical and/or pneumatic components, as needed. 6.2.3.3. Service/replace actuator and/or valve components, as needed. 6.2.4 . In 

### case ofphysical/eleclrical failure ofcontrol system component 6.2.4.1. Identify faulty control system component 6.2.4.2. Service/rep lac e control system components, as needed . 

### Page J6 of26 VES 004012i

### ' . . VEOLIA ENVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECITVE ACTIONS FOR MALFUNCTIONS 6.3. 

### Loss o f City Water Flow to SDA (Unit 2 aad 3) 6.3.1. 

### In case oftotalloss ofcity water supply, see 1.5. 6.3.2. 

### In 

### case o f plugging/physical failure of line or line com ponent : 6 . 3.2.1. Identify the lo cation ofplugging or line 

### failure. 6 . 3 .2.2. Clear line p lugging and/or service/replace faulty line components, as needed. 6 .3 . 3. Ill 

# case of**mechanicaVe ~cal**  fai lure of actwted valve : 6.3.3. 1. 6.3 .3.2. I dentify ca use of actuation failure . Service/repl ac e electrica l and/or components, as needed . pneumatic 6.3.3.3. Service/replace actll3tor and/or valve com p onents, as needed. 6.4. 

### Loss of CooHng Air Flow t o Atomizer 6.4 . 1. In case of mechan:icaVelectrical failure of atomizer cooling air blower: 6 .4 .1.1. 

### Diagnose blower/drive failure. 6.4.1.2 . Service/replace the blowerldriv e, as needed. 6.4.1 . 3. Restore e lectrical power supply to the blower. 6.4.2. 

### In case· of physi cal failure of atomizer cooling air duct 6.4.2 .1. I d entify the location ofdu ct fail'are. 6.4.2.2. Service/replace faulty duct, as needed. 6 . 4 . 3. In case ofphysicaVelectrica l failure ofcontrol system cornpone.ut: 6.4 . 3.1 . Identify faulty control system component . 6.4.3.2 . Service/replace control sys tem components, as needed. 6.5. 

### Loss of SDA E:dt Gas Tempenatur e Control 6.5.1. 

### In case ofloss of city 

### water flow to SDA, see 6.3 . 6 . 5.2 . 

### In case of physicaVelectrical failure of temperature transmitter: Service/replace temperature transmitter and/or 

### associated instrumentation, as needed . 6.5.3 . In case ofactuated valve failure: 6.5.3.1. Identify cause o f actuation failure . 6.5 . 3.2 . Service/replace electrical and/ or pneumatic components, as needed. 6.5 . 3.3 . Service/repla ce actuator an d/or valve compone nts, as needed. 65.4. In case**ofp~ysicaVelectrical** failure ofcontrol sys tem compo n ent: Pag e 17 of26 

### ,.

VES 004013

# ( ·

( VEOLIA ENVIRONMENTAL SERVICES, 

### INC PROGRAM OF CORRECTIVE ACflONS FOR MALFUNCTION S 6.5.4 . 1. 

### Identi fy fau lt y control system component. 6.5.4.2. SCJVice/replate 

### control system 

### componen ts , as 

### needed. 6.6 . 

### Atomizer Fame 6.6 . I . 

### ln case oflow atomizet: lubrication 

### oil flow: 6.6 . 1. 1. 

### DiagoOl;e the failure in the lubrication system 6.6.1.2 . 

### Service/replace components of the lubrication system, as 

### needed. 6.6.2. 

### ln case ofmecbanical/electrical failure ofatomizer: 6 . 6.2.1. Diagnose atomizer/drive failure . 6 . 6.2.2. Servicefreplace 

### the atomizer/drive, as 

### needed. 6 . 6 .2.3. Restore electrical power supply to 

### the ato!Dizer. 6 . 6.2. 4. 

### components, as needed.

Page 18 of26 VES 004014

## (



# c ·

(

VES 004015I 

### ' f

1' .. VES 004016

# c VEOLIA ENVIRONMENTAL SERVICES, I NC. PROGRAM OF 

### CORRECTIVE ACTIO NS 

### FOR MALFUNCIIONS 7.0 UNIT 4 SPRAY DRYER AllSORBER (SD A) 7.1. Loss of Lime Shlrry Flo w to SDA 7 .1.1 . In case ofmechanical/electrical failure of lime slurry feed pump: 7.1.1.1. Diagnose pump/drive f ailure. 7 . 1.12 . Service/replace the pump/drive, 

### as needed 

### 7. 

## r . l.3. Restore electrical power 

### supply to the pump. 7.1.2 . 

### In 

### case ofplugginlifpbysical failure ofline 

### or line component: 7 .1.2.1. IdentifY the location ofplugging or line failure . . 7.12.2. Clear line plugging and/or service/replace faulty line components, 

### as needed. 7 .1 2.3. Restore/confirm functional heat tracing, i f applicable. 7. 1.3 . In case ofmechanical/electrical failure ofactuated valve: 7.1.3.1. Identify cause ofactuation failure . 7.1-.32. Service/replace electrical and/or pneumatic components, as needed. 7 . 1.3.3. Service/replace 

### actuator and/or valve**compo~ents,** 

### as needed. 7 .1 .4. In case ofphysical/electrical failure of control system component : 7 .1.4.1. Identify fa uhy control system component 1.1.42. Service/replace control system components, 

### as needed . 7.2 . 

### Loss o f Lime S lurry Flow Co ntro i/E.Jit Gas Temperature Control 12.1. In case ofloss of slurry flow to SDA, 

### see 7.1. 7 2.2. In case of physical/electrical f ailure of flow transmitter: Service/replace flow transmitter and/or associated instrumentation, 

### as needed. 72.3 . In case of actuated valve failure: 7.2.3 . L Identify cause ofactuation failure. 7.2.32. Service/replace electrical aod/or pneumatic components, as needed. 7 .

2.3.3 . Service/replace ac tuator and/or valve components, 

### as needed. 7.2.4 . In case o f physical/electrical failure ofcontrol system component:**12.~. .**  Identify faulty control system component 7.2.42. Service/replace control system ·components, as needed. Page 19 o f26 VES 004017

## f



# C'

'

. VEOLIA VIYlRONMENTAL SERVICES , INC. PROGRAM OF C ORREC11VE ACJ10NS FOR MALFUNCI'JO NS 7 .3. 

### Loss o f Atomizatloo Al . r Pressure to SDA Nozzle 7 .3 .1. For a total loss ofplant/instrument 

### air supply , see 1.3. 7 .3.2 . Iu case ofplugging/p hysi cal failure ofline or line componen t: 

### 7 .3 .. 2.1. 

### Identify lhe location of

### plugging or 

### line failur e. 7.3.2 .2. 

### Clear line plugging and/or service/replace 

### fau lty line components, as needed.

Pago 20o f26 i 

### "

VES 0040 18'· VE OLJA ENVIRONME NTAL SERVICES, JNC . PROGRAM OF CO RRECfJ VE AC110N S FOR MALFUNCfJONS 8.0 CARBON INJECTION SYSTEM (UNJT 4 ) 8.1 . Loss of Carner Ga s Pr essu re 8.1.1. In 

### case o f mechanic al/electrical failure of 

### carbon injection 

### air blower : 8.1.1.1. 8.1.1.2 . Diagnose blower/drive failw-e. Service/replace the blowelfdrive, as needed. 8.1.1.3. Restore electrical power supply to the blower. 8.1.2 . In case of physical 

### fail= 

### air duct: 8.1.2.1. Identify the location ofduct failure . 8.1.2.2. Service/replace faulty duct, as needed. 8.1.3 . In case ofphysicaVeledrical tiulure ofcontrol system component: 8.1.3.1. Identify faulty control system component. 8 .1.3.2. Sc:rvicel repl ace control system components, as needed. 8.2 . Loss/Re s trictlcra of Activated Ca.rbon Flow 8.2 .1. In case ofloss ofplaot 

### air to 

### carbon bulk sack, see 8.3 8. 2.2. In case ofmecbanicaVelectrical ,failure of carbon feeder : 8.2.2 . 1. Diagnose 

### feeder/drive failure. 8.2 .2.2. Service/replace the feeder/drive, as needed. 8.2 . 2.3. Restore electrical powez supply to tbe carbon feeder. 8.2.3. In case o fp luggingfpbysical failure o f linC or tiJle compoJ\C1ll : 8.2 .3.1 . Identiiy the loc:alion ofplugging 

### w tiJle failure. 8.2.3.2. Clear line plugging and/or service/replace faulty line components, as needed. 8.2.3.3. Restorelconli.an functional beat tracing. if applicable. 8.3. Loss of Plant Air Pressnrt!Fio'!l' to Carbon Bulk Sack 8 . 3 .1. F o r a total l oss ofplanlf'ms trumen t air supply, see 1.3 . 8 .3:2. In**a.~e** of plugging/ physical f mlure ofline or line component: 8 . 3.2.1. Id entify tbc location ofp lu gging or line fai l ure. 8.3.2.2. C l ear tiJle plugging and/or service/replace faulty tiJle componentS, as needed. 8.3.3 . In 

### case ofmechanicaVelectrical failure ofaclllated valve: 8.3.3.1. ldentify cause ofactuation failure. 8 .3.3.2. Service/replace electrical and/or pneumatic components, as needed. 

### Page 2 1 of2 6

. ..t 

### ., 

## r. ,.



## ..

VES 0 040 19

# ( .. .. .

.

1... ... VEOLIA ENVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECTIVE ACTIONS 

### FOR MALFUNCDONS 8.3.3.3. Service/rep l ace acruator and/or valve**~ts,** as needed. 83.4. In case ofphysicaVelectrical 

### failure of control system component: 83.4.1 . Identify faulty control system component. 8.3 . 4.2. Service/replace control system components, as needed.

Page 22 of 26 i.



### · .

VES 004020; VEOUA ENVIRONMENTAL S ERVI CES, INC. P R OGRAM OF CORRECTIVE A CTIO NS FO R MALFUNCTIONS 

### 9. 0 B A GHOUSE & INDU C ED DRAFf (ID ) 

### FAN 9.1. Torn/Leakin g 

### Bag 9 .1.1. 

### 1n case of a bagbouse l eak detection alarm, follow the relev ant corrective measures p rescnl>od in 

### the Operation and 

### Maintenance Plan_ . 9.1.2. 

### 1n case ofa bagbouse leak detection system failure: 9.1.2.1. Service/replace tom/leaking b a g(s), as needed. 9.1.2.2. 

### Diagoose the failure ofthe bagbouse detec!ion 

### 'ystc:m. 9.1.2.3 . Service/replace bagbouse leak detection $}'$!em. as needed. 9.2. Bag Blindinifmch · Bi&Jl Pn:Ssa.r e Drop 9.2.1. 

### 1n case oflow baghouse 

### inlet gas temperature: 9.2. 1.1. Follow the appr opriate corrective actions prescribed by parngrnph 

### 6.S (U nit 2 and 3) 9.2.1.2. Foll ow the appropriate correctiv e actions prescribed by p11111graph 7.2 (Unit 4 ) 9 .2. 1.3 . Perform bagbouse inspection. 9 . 2.1.4 . Service/repl ace bag(s) , 

### as needed . 9.3. Loss ofSbck Gas Flowra t e C utrol (Un it 2 ud 3} 93 , 1. In case oflD fan failure, see 9 . 5 93.2. In case of physical/electrical failure of flow transmitter: Service/ replace 

### flow transmitter and/o r associated instrumentation, 

### as needed. 9.3. 3. In case of actuated damper failure: . 9.3 .3.1. Identify cause of actuation failure. 9.3.3.2. Service/replace electrical and/or pneumatic components, as needed . 9 .3.3.3. Service/replace actuator and/or damper components, as needed. 9.3.4. · In case ofphysical/electrical failure of control system component: 9.3.4.1. Identify 

### faulty control system component 93.4.2. Servicelrcplace control system components, as needed. 9A. Bagllouse Isolation Damp er M a lfu clioo (Uilit 4} 9.4.1. In case of actuated damper failure: Pagc23 of26 VES 004021' 

### ' 

### '



# C .

•. 

### VEOLIA ENVIRONMENTAL SERVICES, JNC. PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIO NS 9.4 . 1.1. IdentifY cause ofactuation failure. 9.4.1.2. Service/replace electric al and/or pneumatic components, as needed. 9 .

4 . 1.3 . Service/replace actuator and/or damper components, as needed. 9.4.2 . ln case ofphysical/electrical failure ofcontrol system component: 9.4.2 . 1 . IdentifY faulty control system componenl 9.4.2.2. Service/replace control system components, as needed. 95. 

### ID Fan Fallare 9.5.1. ln case ofmechanical/electrical failure ofiD fao: 9.5 .Ll. 9.5 .1. 2. 

### 9.5.1.3. Diagnose fan! drive failme.. Service/replace the fanld:rive, as needed. Restore electrical power supply to 

### the ID fllll.



### Page 2 4 

# of 26 VES 004022I VEO LJA ENVIRONMENTAL S ERVICES , INC. PROGRAM OF CORRECTIVE ACI10NS FOR MALFUNCI10NS 10.0 CONTROL SYSTEM/CONTINUOUS MONJTORlNG SYSTEM 10 .1. Control Sys temfConlinuous Monitoring 

### System Malfunction 10.1.1. As needed, 

### refer to 

### the 

### CMS QAIQC Plan for guidance and 

### to ensure 1bat 

### proper calibra ti ons are per fonned : 10. 1.2. In 

### case ofphysicaVelectrical frulure ofinstrumentation : I 0.1.2 . 1 . 

### I dentify faulty instrumentation component. 10.1 .2.2 . 

### Service/replace faulty instrumentation components, 

### as needed. 

### 1 0. 1 .3. In 

### case ofphysical/electrical failure ofcontrol 

### system component: 10 . 1. 3.1. 

### Id entify faulty control system 

### component 1 0.1.3.2 . 

### Service/replace control system 

### components, as 

### needed. 10 .1. 4 . 1n 

### case ofphysicaVelectrical failure ofdata acquisition/avail ability: 10.1.4.1. 

### Identify faulty 

### data sysleD1 

### components. 10.1.4.2. Service/replace data system components, 

### as needed. 1

0.2 . COBtiDuous E missions Monitorin g 

### Sys tem Malfunctioll 10 .2.1. As needed, 

### refer to the 

### CEMS QAIQC Plan f or guidance and to 

### ensure that p roper calibrations are perfonned and 1bat 

### the appropriate performance specifications are mel 1 0. 2.2.1n 

### case of physical/electrical failure umbi lical heat tracing: 10.2.2.1. 

### Diagnose failure ofbeat 

# tracini 10.2.2.2. 

### Replace/restore heat traced sample umbilical. 10 .2.3. In 

### case ofmecbanical/electrical failure ofheated 

### vacuum pump : I 0 . 2.3 . 1. 

### Diagnose pmnp!drive failure . 1 0 . 2.3.2. 

### Service/r eplace the pwnpfdrive, as needed. 

### 10.2.3.3. Replace/restore pump head beat 

### source. 10.2.3 . 4. 

### Restore electrical power 

### supply to heated vacuUID 

### p ump . 1 0.2 .4 . In case 

### ofp lugging/physical failure 

### of sample prob e/umbilica l : 10.1.4.1. 

### I dentify the location of failure. 1 0.1.4.2 . Clear 

### plugging and/or service/repl ace faulty components, as 

### needed. 10.2.5. 

### In case 

### ofmechanical/electrical failure ofactuated valve : 1 0.2.5 . 1. 

### Identify cause ofaclllation failure . Page25 

### o f 26 

# ' > 

## ..

VES 004023

# c VEOUA ENVIRONMENTAL SERVICES, INC. PROGRAM OF CORRECflVE ACI' J ONS FOR MALFUNCI'IONS 

### I0.2.5.2. 

### Service/replace electrical and/or pneumatic components, as needed. 

### 10.2.5.3. Service/replace actuator and/or valve components, 

### as needed. 

### 10.26. In 

### case ofmechanical/electrical failure o f analyzer: 10.2.6.1. 

### Refer to manufacturer's service manual 

### for guidance on troublcsbooting and 

### servicing analyzer . 

### 10.26 . 2 Service/replace analyzer, as needed. 10.2. 7. In 

### case of mecbanicallelectrical failure 

### of associated 

### instrumentation: 102 . 7.1. 

### Identify faulty 

### instrumentation componenl 10.2.7.2 . 

### Service/replace faulty instrumentation . components, as needed . 10.2 .8 . In 

### case ofphysicaVelectrical failure ofcontrol 

### system component : I 0.2.8.1. 

### Identify faulty control system 

### componenL 10 .2 .8 .2. 

### Service/replace control system 

### components, as needed.

Page26 

### of26 VES 004024

### EMERGENCY SAFETY VEN T PLAN Prepared for: 

### Veolia ES Technical Solutions, LLC Sauget, IDinois

Prepartd by: 

### Franklin Engineering Group , 

### Inc. Franlclin, 'fennessee

October 2008

VES 004025

# '· 

# c · TABLE OF CONTENTS 1 . 0 INTRODUCHON AND BACKGROUND -·····--·- ..... . .. .. .. --- · ·-·-- .. . .. 1 1.1 SUMMARY OF FACiliTY INFO RMATION ..... .. ....... . ........ ..... . : ...... . . .... . .... . : . .. ..... ! 

### 1.1 . 1 

### rued Hearth I ncinerators . .................. . ..................... . .................. . .. ] 1 . 1.2 Rotary Kiln lncinerator ... . ....... .... .... .... .......................... . .. . .. . ............ 3 1.2 DEsCRIPTION OP 1liE ESV SYsmM .. ... ....... .... . ........................ .... .................4 2 . 0 ESV SYSTEM INVESTIGATION, DO CUMENT ATION AND REPORTING ......... .. .......... ........ - .. - .......... ......... _ .._ ....... . -- ... .... ........... ....... 7 2 . 1 ESV INVESTIGATION .... ..... .. ...... .. . ... . ... ... ............. ...... ................ . .... :. .. ....... ... 7 2 .2 DocuMJi:NTATION OFESV OPENING .. .. ... .... .. ..... .. .. . .. . . . ..... .......... . . . .. . .. .. . .... .. 7 2.3 REl'oR11NG OF ESV OPENJNG$ ............... .. . .. ..................... .. .................. . ...... . 8 3. 0 PROCED URES DURING AN ESV ... . .

- ... ...... ... . .. .. - .... .. ................. .. ....... - ... - 9 3.1 STOPPING W AS1ll FEED AND SH\1111NG DoWN 1liE COMBUSTOR ....... .. ...... . 9 3. 2 MAINTAINING COMB U

STION CHAMBER Ti!MPERAnJRll. ..... .. . ..... . . . .. . . .. . . ..... .. 9 3.3 

# c

. 

### 3 . 4 ' MAINTAINING NEGATIVE COMBUSTION CHAMBER PRFsSURE .... .. . .. .. .. ......... 9 SH\1111NG DoWN 1lll! COMBUSTOR . ....... .. ...... . . . . .......... ....... ..... . ... ... .... .... ..... 9 3.5 DOclJMENTATJONOFCOMBUSTIONCHAMBERPR:EsslJREAND 'TEMPERA 11.JRE MAINTJ!NANCE .................. ... ........ .. .... .... ...... ......... . ...... 10



### . . .

· ii VES 004026(' " '. 

### LIST OF TABLES TABLE 1-1 REGUl..ATORY REQUIREMENTS FOR AN EMERGI!NCY SAFETY 

### VENT 0P.ERATING PLAN AND CORlUlS IONDJNG SEcnON THAT ADDRESSES 11 · 1E R.EQl.IJR.EMENT . . . ......... ........ . . . ...... ... ......... .. ... .... . .... .......... .... ....................... ..2 TABL.El-2 'l'HERMAJ.Rl!U:sPVENTOPENJNOS ............................. .. ........ ............ .. ..... ..... S



### iii VES 004027

# ( . . . .

. 

### i.O INTRODUCTION 

### AND BACKGROUND Veolia ES Technical Solutions, LLC (Veolia) owns and operates two fixed hearth incinerators (Units 2 and 3) and a rotary 

### lci1n incinerator (Unit 4) at its facility located in Sauget, TIIinois . These incineratoxs 

### are subject to the National · Emissions Stmdards for Hazardous Air Pollutants (NESHAP) for Hazardous Waste Combustoxs (HWCs), Code of Federal Regulations 

### (CFR), Part 63, Subpart 

### EEE (§§ 63.1200 to 63.1221). The NESHAP for HWCs specifies emissions standards which reflect emissions performance of maximum achievable control teclmologies 

### (MACT), and is commonly referred to as the HWC MACT . Hazardous Waste Combustoxs are required to have an Emergency Safety Vent Plan and to 

### keep the plan in the operating record. The Emergency Safety Vent Plan must follow the requirements described in § 63.1206(cX4). This Emergency Safety Vent Plan demonstrates Veolia's compliance with these requirements. This plan includes information about the facility as it relates to the Emergency Safety Veot (ESV) systems, and procedures that will be fo llowed during 

### an ESV 

### event. Table 1 -1 presents the regulatory refermces related to the required ESV program and the section of this plan**~** addresses each specific requimnent. Due to the general applicability of the ESV requirement and the siruilarity of the incinerator systems, general references to an ESV or incinerator system in this document wiD imply all three systems . Information that is only applicable to one or two ofthe three systems will be clearly identified. 1.1 Summary of Facility Information Brief Sllllliilaries which describe the fixed hearth incinerators an d the rotary 

### k i ln incinerator are presented in this section. 1.1.1 Fixed Hearth lncineratlml Each of the fixed hearth incinerators includes the following components: • Feed equipment 

### • · Primary and secondary combustion chambers • Lime injection system 

### • Spray dryer absorber 

### (SDA) • Fabric filter baghouse I VES 004028

### (



# ( '

( 

### Ta ble 1 -1 Re gul a to ry Re quire ments !or 

### Emer&en cy Safe ty Vent OpenliD & 

### PIID a11d C orr es p o 11dio g Sect io n tllat 

### A ddresses tbe Require ment Regulatory De scripd ou Plan Sectioo

Cita ti o u Documentation in operating record ofan ESV opening while hazardous waste remains in the 

### combustion chamber. 63.1206(c)(4)(i) (l) Record 

### ifESV by - passed APCS Section 2.2 (2) Determine 

### ifopemtioo remained in compllimce considering the emissions 

### during theESV InfOimation documenting effectiveness ofplan 's 63.1206(c)(4)(ii)(B) procedures to maintain combustion chamber Section 3.5 temperature and 

### pressure, as is reasonab l y feasib le 63. 1 206(c)(4)(ii)(B) Detailed pcoced . ures for rapidly stop pin g w aste feed Section 3,1 63. 1 206(c)(4)(ii) (B) Detailed procedures for s hu tting d own the Section3.4 combustor 63. 1 206(c)(4)(ii)(B) Detailed 

### procedures for maintaining 

### tempera ture in Section 3.2 combustion chamber 63.1 206(c)(4)(u)(B) Detailed procedures for maintaining negative Section 3.3 pressure in the 

### combustion chamba 63.1206 ( c)(4)(w) Investigation ofESV**~** 

### Section 2.1 63.1206(c)(4)(rii) Recording ofESV openings 

### Section 2.2 63 . 1 206(c)(4)(iv) Reporting ofESV openings Section 2.3

. 2 VES 004029

### ' · • Solids and ash removal systems • Induced 

### draft (ID) fan and stack • Instrumentation, controls, and data acquisition systems Various solid and liquid was tes and gaseous feedstreams are thermally treated in the fixed hearth incinerators . Solid W83tc 

### is fed to the primary (l ower) combustion chamber via a feed conveyor system and pneumatic tam. Liquid waste from tanks and tanker trucks are fed to the primary combustion chamber through two atomized liquid injectors. Liquid waste from containers are fed to the 

### primary combustion chamber through a 

### specialtY. feed injector. A 

### gaseous fecdstream 

### is fed to the Unit 2 primary combustion chamber directly from 

### gas cylinde:rs . Off gases .from a hooded feed emission control system and from a waste 

### handling glove box are fed directly to the Unit 

### 3 secondary combustion chamber. Combustion chamber temperatures are maintained using natural 

### gas fired to 

### a dedicated burner in both the primary and secondary chambers. Combustion gas exits the secondary combustion chamber and enters the SDA, which provides acid gas removal and cooling of the combustion gas. Combustion gas exits the SDA and is distributed to the . fabric filter baghouses, which pr0 vide particulate mallet' removal. 1be induced draft fan, located t;lownstrcam of the baghouses, moves the combustion gas through the sy&em and e xhausts the gas through the main stack. 1 . 1 .2 Rouuy Kiln lncineraJor The rotary 

### lriln incinerator includes the foUowing components: • Waste feed system • Primary and secondary combustion 

### chambers • Tempering chamber 

### • Lime injection system • Sprny dcyer absorber • Carllon**~ection** system • Fabric 

### filter baghousc • Solids and ash removal systems • lD fan and stack • Instrumentation. controls, and data acquisition systems Various solid and liquid wastes are thermally treated in the rotary kiln incinerator . Solid wastes are fed to a ram feedeo- via a clarnsheU , a dnnn feed conveyor, and an auxiliary 

### 3 VES 004030

# ( · feed conveyor. A hydraulic 

### ram pushes the solid waste into the lciln. liquid waste 

### from tanks and tanker trucks is fed to the primary and secondary combustion chambers through atomized liquid injectors. Combustion chamber temperatures 

### are maintained using natural gas fire d to a dedi cated burner in both th e primary and secondary chambers. Combustion 

### gas exits the secondary com bustion chamber and ent ers the temt)ering chamber, which provides cooling of the combustion gases. The combustion gas 

### exits the tempering chamber and is distributed betwem two identical SDAs, which provide acid gas removal and additional gas cooling. A carbon injection system is utilized for controlling dioxin/furan and mercmy 

### emissions. The activated caroon 

### ia 

### air injected into the 

### combustion gas immediately 

### downstream of the coiJvergence of 

### combustion gases 

### from the 

### SDAs. From !be SDAs, 

### combustion gas is distributed to 

### fabric filler bagboust$, which provide particulate mallcr removal. The ID fan, located 

### doWDStream of the baghouses, moves the combustion 

### gas through the system and exhausts the gas through the 

### main stack. 1.2 D escription of the ES V Sys te m Each incinerator is equipped with 

### nn emergency safety vent (ESV) located at the top of the secondary combustion chamber. 'Ibis ESV is a refractory-lined emergency thennal relief vent (IRV) which is held in the closed position 

### by a pneumatic cylinder . The control valve in the line supplying air to the cylinder and the cylinder vent valve which opens the TRV are located in the control room for each unit. Valve Jocks (with keys attached) are utilized to deter indiscriminate operation of these valves. Opening of the 

### TR V allows hot combustion gas to vent 

### from the combustion system during 

### emergency shutdown events. The purpose of the TRV i s to protect the 

### downstream APCS 

### from excessive tempeoature s.ituatiON. Conditions which may warrant a TRV opening are summarized in Table 2-1. Typically, alanns and/or interlocks wt11 be triggered prior to these conditions being pres ent. Alarms provide the operator the opportunity t o take measures in attempt to restore proper operating conditions . Otherwise, • controlled cutoff of the waste feeds , an A WFCO, or 

### an emergency shutdown may occur prior to opening the 

### TRY . If hazardous waste is being fed at the time the TRV is opened, the 

### TRV position tnnsmitter will detect the TRY 

### opening aod 

### triggec an AWFCO.

4 VES 004031

### / ' Tab le 1 -2 Tberma1 Relief' Vent Openings 

### Parameter Co.ditlo a 1 Ele<:trical Supply LossofPow" 

## •· Air Supply Loss of

### Air Pressure (TRV will f ail open) 

### IDFan Failure/Malftmction SDA Exit Gas Temperature 

### > 500 

### • p Emergency Shutdown Operator's Discretion 1 The operator is permitted to open the TRV 

### if these conditions are present. 

# c

5 VES 004032' .. 

## ' Unit 

### 4 is equipped with a second ESV located at the 

### kiln face. This ESV is referred to as the 

### " surge vent and is 

### kept closed by a weighted louver. The 

### surge vent will only open 

### if 

### tbere is 

### a pressw-e excursion in the kiln sufficient enough to overcome the weighted louver. A deflector separates the 

### escaping combustion gas 

### ftom the 

### feed, and the surge vent angles to a horizontal opening. This d esign minimizes the entraimnent of solid thrnugh the 

### surge vent. An 

### ESV opening 

### may correspond with a malfunction event. Infonnation regarding operation of the incinerator and 

### the associated control equipment during times 

### ofstart-up, 

### shutdown and malfunction is provided in the 

### faciliJy Start-up, Shutduwn, Malfoncticn Plan (SSMP) .



### 6 VES 004033

# c 2.0 ESV SYSTEM INVESTIGATION, DOCUMENTA TI ON AND REP ORTING 2.l ESV Iovestlcation 

### lf an ESV opens for any reason during normal 

### operations, the operator is instructed to: 

### I) Verify !bat all waste f-'.5 to the incinerator are cutof!; 2) 

### lf possible , operate the ID fan, and 3) 

### lf possible, maintain normal combustion chamber temperatures on na111ral 

### ps. lfhazardous waste is in the combustion chamber during a ESV opening. the incinerator supervisor should be notified as soon as possible .**~** incinerator supervisor will coordinate with technical staff to determine potcDtial causes for the event and to estimate excessive emissions . 2 .2**D~>" men** **ation** 

### ofESV O penJ a g Each instance in 

### which the emergenc y vmt opens will be recorded in the facility openting record. 

### This record will, at a minimum, include the date, time, and the operating mode at the time of the ESV opeoio&. This data is automatically documented in the openting record by the CMS . 

### lfthe ESV 

### opens when hazardous waste remains in the combustion chamber (Le., when the hazardous waste residence time has not expired) during an event other than a mall\metion (as defined by the facility SS MP), Veolia personnel will document that an ESV event occurred, determine if the facility remained in compliance with facility emission standards, and record the findings of that determination in the facility operating record. Since the BSV is located upstream from the facility air pollution control devices (APCD), it is undc:rstood that combustion ps by-passes tbese emission control devices during an ESV event. Thi . s by-pass will bo documented in the facility op<nting record. If an ESV 

### opening is attributed to a malfunction and occurs when hazardous waste remains in the combustion chamber, a malfunction recordlcteJ;'ing form will bo completed to document the event

7 VES 004034i 2.3 ReportiDg of ESV**Opening.~** 

### If au 

### ESV opening results in a failure to meet the emission standards for the facility, 

### Veolia 

### wi. ll submit a written**~rt** within five days of the 

### ESV event to Dlinois Environmental Protection Agency 

### ( IEPA), documenting the r esults of the investigation and corrective measures taken. ln most cases when au ESV event occws, it is instantaneous . Therefore, it is practical to assume that diminirous emissioos occur during these instantaneous events.

8 VES 004035I ' •



# ( . . .

\

# ·. 3. 0 PROCEDURES DURlNG AN ESV 

### ln the event of an ESV opening mat occurs while buming waste, it is important that waste 

### feed is stopped npidly, and that combustion chamber temperature and negative pressure are maintained to the extent practical. Following the expiJation of the hazardou s waste retention 

### time, shutting down the combustor (allowing ke y components to cool) is equally important These items are addressed below . 

### 3.1 Stopp ing Waste Feed aad S but tlag D own 

# the Combu stor An ESV opening is likely to be preceded by a AWFCO or safety interlock that causes a waste feed cutoff prior to the ESV 

### opening. The ESV position is also in terl ocked with the AWFCO system. Thellc redundant measures ensure that waste feeds will be stopped dnring an ESV opening. If the A WFCO system fails to cutoff wastes to the incinerator, the waste will be manually cutoff 

### in a quick and safe inanner . Waste burning cannot 

### resume Wllil the ESV is closed, corrective 

### actions taken, pemrission 

### is granted 

### from the incinerator supervisor, and all parameters are within limits. 3.2 

### Maintaillio g Co mbu s tion C h amber T e mpera ture Combustion chamber temperatures 

### are maintained using 

### nanu:al gas 

### fired a dedicated burner in both the primary and secondary combustion chambers. If possible, the burning of natural gas will be used to maintain adequate combustion ch210ber temperatures for the combustion ofwaste ro:naining in the incinerator. 3.3 

### MainWaing Negati ve Com bustloa C llam ber Pre:ssan If possible, the ID fan will be opented during 

### an TRV opeoing to 

### minimize the quantity of combustion gas that**by·p~.s** the air pollution control equipment Operation of the ID 

### fan during an ESV opening will maintain negative combustion 

### pressure to the full oxtcn t that is reasonably feasib le . II is likely that the opening of the TRV will cause the B}'ltem to l ose negative pressure (i .e. the ID fan cannot induce a strong draft) . For surge vent ' opening. the positi ve pressure excursion will be temporary , and the ID fan (if opetable) 

### will be used to restore negative pressure 

### in the primary chamber, as quickly as poss . ibla. 

### 3. 4 Shutting Dowa t he Combustor An event which 

### causes an ESV opening may 

### require 

### a cold shut down of the combustor 

### in order to perform corrective actions. Aftet sufficient effort is taken to minimize emissions by 

### maintaining the tanpcnture and 

### pressure. the incinerator supervisor will decide 

### if a shut down is wananted . Ifthe ESV opening corresponds with a malfunction 

### 9 ' ' 

### r

VES 004036(



### ( 

# . 

# . 

# . . event thc:o the COJTecti ve measures taken will be consistent with the procedures prescnoed 

### by the 

### SSMP . 3.5 Documentation of O>mbusrioo Cbamber Pressu re and T e mperature Mat at e aaoce § 63.1206(cX4)(iiXB) 

### requires that the facil i ty demoilstra te 

### that the procedures of this plan are adequate to maintain comb ustion chamber pressure and temperature whi le hazardous waste remains in the incinerator, if feasible. The occurrence o f m emergency safety vent opening at the Veolia facility is possible only in a select set of circumstances, which ue described in 

### · section 1.2 of this plan. If natural gas 

### cannot lie bwnccl, 

### it is not**feas~ole** to maintain the combustion cham ber temperature during an BSV event Likewise, it is lilcely that the opening of the TRV will result in the loss of negative pressure. The duration of a surge vent opening will typically 

### be brief and only momentarily prevent maintaining the combustion chamber pressure . The procedures presented in this plan will be followed to minimize the effects of such occurrences .



# ..

10 VES 004037

## (



# c · OPE RATIO N AND MAINTENANCE PLAN Prepared 

### for: Veolia ES Technical Solutions, LLC 

### Sauget, lllinois

' Prepared by: Franklin Engineering Group, Inc. Franldin, Tennessee

Octob er 2008 ; . 

### '



# . . ,.**~** 

## ..

VES 004038T ABLE OF CONTENTS 1.0 INTR ODUCTION.. . .................................. . ... . . .... ...... _. __ ,............ _ ..................... l ).1 "R!!GIJLATORY REQ UJIUlMllNTS . .. . ....... . . .. ...... . . . . . .. . . . ... . .. .... ........ . ... .. ... .... .. .. . . .. 2 1.2 RECORD KEEPING . .... .. .. ..................... .. .... .. .. ... ....................... . ...... .. ... ... .... .. ....2 2 . 0 NO RMAL OPERATIONS OF THE INCINERATORS ....................................2 3. 0 BAG. LEAK DETEC fl ON S YSTEM ............- .... ....... ..................................... ..5 3 .I CO!UtEcnVE MEASURES FOR BAG LEAK DE!ECOON ALARMS .. .. .. .... .. ... . .... 7 4 . 0 INSPECTION AND MAINTENANCE ·--···-·-·--··- .. 

# ----- ..9 5. 0 ALTERNATIVE MODE OF OPERATION .... .:

__________ ] 2 5 . 1 WARM 8:T A

NI>- BY MOD I! OF0PER.A110N .... .. ......... .. .... .... ........ .. .. ............... l2 5.2 Al'PUCAB ll! REQUIIUlMENTS .......... ........ .......... .. ...... ................. .. ...... ......... l 3 

# ( ..... 

# , .

(

VES 004039)



### USTOF T ABLES TAB LE 1- 1 OP ERATION A'ND MA INTh"N AN Cil PLAN REouLATORY Cll:ECKUST .... . ......... 1 TABLE2 - I IJSTOFSTANDARDDIVJSJO NALPRAC11CES ...... . ... . . . . . . . . . .. . . . .. ... . ... . .... . ......... 3 . TABLE 3 - I B A G/lOUSE l...EAK DBlllCTJON S Y S11! M S PEC IFIC ATIONS ..... . ........... .•.... . ...... 6 . TAlli.E 4- I lNsPBCilON AND MAINTENANCE TO 

### !'REVBNT MALFUNCilONS. : . ....•... . . .... I 0

i i 

### VES004040

# l



# ( 1. 0 lNTRO DUCI'lON Veolia ES Tecmical Solutions, l.LC (Veolia) owns and operates three hazardous waste incinerators at its facility located 

### in Sauget, Illinois . The incinerators are subject to the National Emissions Standards for Hazardous 

### Air Pollutants (NESHAP) for Hazardous 

### Waste Combustors (HWC) , 40 CFR, Part 63, Subpart 

### EEE (§ 

### 63.1200 to § 

### 63.122 1) . The NESBAP for HWC specifies . emissions standatds 

### which reflect emissions perfonnance ofMaximlllD Achiev abl e Control Technologies 

### (MA CT), and is commonly referred to 

### as the 

### HWC MACT . The 

### Interim HWC 

### MACT Standanl requires that Veolia 

### operate and maintain the incinerators in a manner consistent witb safety and good air pollution control practices for 

### minimizing emissi ()I)S based on parameter limits achieved during tbe comprebcnsive performance tesL To meet 

### this objective, Veolia has developed Ibis operation and maintenance (O&M) plan. Veolia will utilize this O&M plan for periods of nonnal operation of the incinerators . During periods of startup , shutdown, and malfuncti on, Veolia ..;;il utilize tbe 

### Startup, Shutdown, and Malfunction Plan (SSMJ>) . During periods of startup, shutdown, and malfunction, conformance with the SSMP satis fies the duty to minimize emissions. Both the O&M plan and SSMP are maintained at tbe facility. The purpose ofthis O&M plan is to : • Describe procedures fo r operating tbe incinerator during**nom~** operations. • Descnbe p rocedures for inspection and maintenance of the incinerator . • Describe procedures for coJTeetive measures. • Establish guidelines designed to 

### ensure that emissions 

### of pollutants , automatic waste feed cutoff s (A WFCOs ), and malfunctions are minimized. • Satisfy 

### tbe requirements of§ 63.1206(c)(7) and§ 63.6(e), as shown in Table 1-1 of 

### this plan. Due to tbe similarity ofthe tbrcc incinerator systems, general r eferences to an incinerator in Ibis documeut 

### will imply all three incinerator 

### sysiems. Information tbat is only applicable to one or two of tbe three units will be clearly identified.

VES 004041

# ( · . . 1.1 Regulatory Requirements One of the objectives for this document . is to establish a program that will ensure · compliance with relevant sections of the Interim HWC MACf standard. Table 1- I provides the regulatory requirements and l ocation within this document where each requirement is addressed . This tab le is included to facilitate the expeditious assessment ofthis plan's coverage oftbe relevant regulatory requirements. 1.2 Recordkeeplng 

### V

eolia will maintain files to comply with the recordkeeping requirements of the Interim 

### MACT Standards. These requirements 

### are summarized in 

### 40 CFR 63.1211(b). 

### The files relevant to this plan that 

### are m aintained in the operating record include: • This O&M Plan ; • Records of all required preventive and necessary maintenance performed on the air pollution control and monitoring equipment; and • Records of all ad justments and maintenance perfonned on the continuous monitoring system (CMS).

2 

## '·

VES 004042Tab le 1-1 

### ( Operation au d MaiDteoa . nce Plan Regulat ory Cbecldist Regu l a t ory C itation Description 63.6(e)(l)(i ) Implement safety and good air poUution control practices for minimizing emissions 6 3 .6(e)(l )(ii) Comply with SSMP and minnnize emissions during SSM 63.6(e)(1)(iii) O&M requimnents CSlablisbcd pursuant to section 112 o f tbe CAA 63 . 6(e)(3) Startup , shutdown, and malfuottioo plan 63.10(b)(l) Maintaining files 63 . 1O(b )(2)(iii) Records ofall required maintenance of 

### A:PC and monitoring equipment 63 . 10(b)(2)(xi) Records of all adjustrnent. q and maintroance performed onCMS 63. 1206( c)(7)(i)(A} Prepare and opemte under O&M plan 63 . 1 206(c)(7)(i)(A) Procedures for opemting combustion system components that could affect emissioDS 6 3 . 1206(c)(7)(i)(A} Procedures for inspecting combostion systEm COIDpO!leDts that could affect emissions 63 . 1206(c)(7)(i)(A) Procedllres for maintenance combustioo system components that could affect emissions 63 . 1206(c)(7)(i)(A) Corrective measures fo r combustion system components that could affect emissions 63.1206(c)(7)(i)(B) 

### Good air pollution control practices for minimizing emissio ns 63.1206(c)(7)( i)(C) . O&M plan eilsurcs . com pl.ian ce with O&M requ.irerncnt s of63 . 6(c) 63 . 1206(c)(7)(i)(C) O&M plan minimi1.es emissions ofpollutants 63 . I 206(c)(7)(i)(C) O&M p lan minimizes AWFCOs 6 3 . 1206(c)(7)(i)(C) O&M plan minimizes malfunctions 63.1206(c)(7)(i)(D) O&M plan is recorded 

### in operating record Locatio a Addressed

1.0, 2 . 0

1.0 2 . 0 

### I.O , SSMP' 1.2 1.2 1.2 1.0 2.0 Table 2-1 4 . 0 4 .0 2 .

0 , 3 . 1, 

### SSMP 1 1.0 ; 2.0 1.0 1.0, 2. 0 1.0, 2 . 0 1.0, 4.0 Table 4-1 1.2 f f:



# - '

.,

VES 004043Table 1 - l (con ti n u ed ) OpeY alion an d Main t enance Plan Regu la tory Cbecklist R egelatory Cit atio D D escription Locatiota A d dressed 63.1206(c)(7)(ii) If system equipped wilh a bagjlouse, bag leak 3.0 detection system 

### required 63.1'206(c )(7 )(ii)(A)(1) Detect and record PM emissions at adequate 3.0 sensitivity 63.1206(c )(7)(ii)(A)(2) Output rel. ative particulate matter loadings 3.0 63.1206(c)(7)(ii)(A)(3 ) Audible alarm if loading detected over 

### limit 3.0 63 .1 206(c)(7)(ii)(A)(4) 

### Comply wilh 

### US EPA**guid~** or mannfactma's 3.0 i nfonnation for installation and opaation 63.1206(c )(7)(ii)(A)(5) Initial adjustments ofthe system: baseline , averagiog 3.0 period, al arm set point and delay time 63.1206(c)(7)(ii)(A)(6) O&M p lan specifies a U

owable ad. i us tments 3 . 0, 3 .1 63 . 1206(c )(7)(ii)(A)(6) Limits to sensitivity adjustments 3.0 63 .1206(c)(7)(ii)(A)(7) Installation location requirements 3.0 63. 1206(c )(7)(i.i)(B) Procedures for responding to bag leak detec tion 3.1 system alaon 63.1206{c)( 7)(ii)(B)(l) Initiation ofprocedures to determine alarm within 30 3.1 minutes**63.12~c)(7)(ii)(B)(2)** Necessary corrective rneasurc(s) to aUeviate cause of 3.1 alarm

( '•

VES 004044

# ( · · .

. 

### '



# c· 2.0 N ORMAL OPERATIONS OFTHE INCINERATORS T able 2-1 presents 

### a list of titles for Veolia's Standard Divi sional 

### Practices {SOPs) . These SPDs provide 

### procedures for operating the incinerator in 

### a manner consistent with safety and good air pollution control practices. Utilizing these SDPs, 

### process knowledge, and discretion, operators will maintain the incinerator operating 

### parameters within permissible limits, ifpossible . Operating the incinerator in this 

### manner will 

### minimize the occurrence of

### A WFCOs and minimize the emissions ofhazardous air pollutants. 

### All applicable operating requirements for the incinerator, including operating parameter limits {OPLs), 

### are specified in Veolia's 

### I>ocwnentation of Compliance {DOC) 

### or Notification of Compliance, wbichever is currently applicab le . 

### Nonnal operations of the

· incinerator will be in compliance with these 

### requirements. V eolia bas developed Piping and Instrumentation Diagrarns {P&IDs), Process Flow Diagram {PFDs ), and technical descriptions for each incinerator. These resources in conjunction with MS PowerPoint* presentations are integral parts of operating training. 

### With this training, operators gain th e 

### understanding of alarms, interlocks, as well as the automated responses associated with 

### each interlock . Knowledge of alarms and interlocks and access to proc ess variable indication, prepares the operator to perform the appropriate corrective measures should conditions deviate from normal operations. The corrective measures taken will be the operator's efforts to ensure safety and to l)laintain operating parameters within limits, if possible. 

### If deviations from nonnal operations are cansed by a 

### m alfunction, corrective measures will be 

### consistent with the 

### SSMP and the 

### Program of ConectiveActionsfor Malfunctions, Attaclunent 4.0 ofVeolia's SSMP.

2 VES 004045/ 

### Table 2-1 List of S tandard Divisional Practiees SDPNUMBER 

### TITLE lOll TWI Remedial Action W o:dt 

### Order Program 2200 

### Specialty Feeder Operation f or No. 2/3 Incinerators 220 1 Startup, Operation and Shutdown ofNo . 2/3 Incinerators 2202 Operation ofCompressed Gas Cylinder Feeding Syst em 2203 Operation ofSolids Feed Conveyor Syst ems for No. 2/31ncinerators 2204 Ash Conveyo r Operation for No . 2/3 Inci.neratoiS 2205 Operation ofLiquid Feed InjectoiS fo r No . 2/3 Incinerators 2206 No . 2/ 3 Inci nerators Legs Cleanout 2207 No. 2 Incinerator Upper Chamber F eed System 

# ( 220& No. 2/3 Incinerators Shutdown Permits, Ta gouts and 

### Lockouts 2209 Operation ofBaghouse Filters for No . 2!3 1ncin erators 2210 Operation of Compressed Air 

### System for No . 213 JncineratoiS 22 11 Lime 

### S lurry System Operation 

### for No . 2 and 

### 3 Incinerators 2212 Spray Dryer Absorber Operation for No .**2/31ncine~tors** 

### 2213 Operation of Dry 

### Saubber Solids Con v eyor Systems for No . 2/3 Incinerators 221 4 F lu shing the Lime S l urry System for No . 2/3 Incinerators 22 1 5 Operation of Oxygen Gas Cylinder Processing System 2217 Operation o f Specialty Feeder Fwne Hood System for 

### No . 3 Incinerator



# ..

3 VES 004046

### \ . Table 2- 1 ( co ntinued) List of Standard J)lvisioDal Practices S DPNUMB ER TITLE 2219 Lime Storage Lo ading 2221 24-Hour Staging ofBurnab le Containers on No . 213locinenltors 

### Dock 2222 Ash Management for No. 213 Incinerators 2224 No. 213 Incinerators Direct Inject System 2401 No. 4 Incinerator Shutdown Permits, Tagouts and Lockouts 2402 Main Feed Conveyor System Operation for No.4 Incinerator 2403 Clamshell Feed System Operation 2404 Tempering Chamber Operation 2405 Flushing the Lime S lurry System for No. 41ncinerator 2406 Operation ofLiquid Feed · !Qjectors for No . 4 Incinerator 2407 Cleaning the Process Water System for No. 4 locinentor 2408 Operntion ofCarbo n lnjo:ctioo System fo r No. 4Jncinerator

. . 2416 Lime Sluny System Operation for No. 4 Incinerator 24 1 7 Start1lp, Operation and Shutdown ofNo.4 Incin erator 241 8 Sp ray Dryer Absorber Operation for No. 4Inc inerator 2419 Operation ofDirect Inject System for No. 4 Incinemtor 2421 Air Cannon Operation for No . 4 Incinerator 2422 Awciliary Feed Conveyor S)'SI!m Operation for No. 4lncinentor



### (
4 VES 004047

## ( 3.0 BAG LEAK DETECTIO N SYST EM Veolia utilizes a triboelectric bag leak detector to comply with tlte bag leak detection requirement s of63.1206{c) . The installation 

### and on-going operation oftbe lealc detection system is consistent with the US EPA 

### FabrU! Filter Bag Leak

### DeJection Guidance (EPA454/R - 98-01 5). The bag Jealc detection system monitoiS the relative particulate matter loading of the gas in the d uc t d owns tream of the induced draft fan. The bag lealc detection sys tem has been certified from manuf acturer that the system is capable of detecting and recording particulate emissions at conceolrations of 1.0 

### milligram per actual cubic meter. The sensitivity of the bag leak detector is set by selecting tbe relative output range. A IeSpODSe time**(i.e~** averaging period} is utilized to smooth fluctuations in the triboelectie signal. The bag leak detection system titilizes two alarm set p<)illts {high and high-high}, which are set as a percentage of the full scale reading . The alarm set poillts are . based oo a multiple oJ tbe baseline reading considering cleaning cycle peaks, if apparent. Tbe high-high alarm is interlocked with the AWFCO system. The delay times for the alanos are based on tbe normal bag cleaning pulse cycles. Th e bag leak detecti on system settings arc presented in Table 3-1. Following initial adj ustments (inclu ding adjustments made during a 3{)-day trial period) to the bag leak detection system, there will be no adjustments to the sensitivity (range}, averaging period. alarm set point. or alarm delay time except for the adj ustments made consist ent with recommendations in Section 5 . 3 of the US EPA 

### Fabric Filter Bag Leak Detection Guidance (EPA -45 4/R-9 8 - 01 5). Peri odic adjustments to the bag l eak detection system may be warranted to prevent/minimize the OCCUirelli:C of false alanns. If over a 36S day period. the sensitivity is 

### increased by more than I00 percent or decreased by 

### more than 50 percent, a com plete baghouse inspection and nec essary 

### repairs will be pc:rfonned to assure good operating condition.



## s 

# r

VES 004048Ta ble 3- 1 

### Baghous e Leak D e te di oa Sys t e m S p ecif"J ca tions P arameter Unit 2 U nit 3 Un . it4 Range 

### 0-1,000 0-1,000 0-1,000 !. 

### Averaging Period !Oseconds !Oseconds 

### tO seconds 

### High Alarm 

### 20% 200/o 10% Hi gh Alarm Delay Time 

### 3minutes 3 minutes 6minutes High -Higb Alann (AWFCO) 

### 30% 300 /o 15% High-High Alarm Delay Time 

### 6 . minutes 6minutes 12 minutes

\

. . . 6 VES 004049

### (



# ( " 3. 1 Corrective Measures for Beg Leak D e t ectio n Alarms Veolia has im plemented the necessary proactive measures to preventhninimize the 

### occurrence of bag leak detection al:ums. These proactive measure s 

### include im;pections and preventive maintenance of the baghouse and the bag leak detection system. Additionally, the installation 

### and operation of the bag lealc detecti on 

### system is consistent with EPA guidance. Despite these efforts, a false bag leak detection alarm or a bag leak/failure may occur and are considered potential malfimctions. Accordingly, this section is a compooent ofthe 

### SSMP and is referenced 

### by paragraph 

### 9.1.1 of the 

### Program of Correction Actions for Malfimcdons, Attad!ment 4.0 ofVeolia's 

### SSMP. The purpose of this section is to prescribe the procedures for responding to bag leak detection alarms. The procedures specified in this section w ill be initiated within 30 minutes of the time the alarm first sounds. The time and cause of each alsrm will be recorde d on 

### a malfunction recordkeeping 

### form. A blank malfunction recordkeeping form**i~** Attachment3.0 ofVeolia's SSMP. 3.1.1 In 

### case of

### an alarm for lligb relative particulate ma tter loading: 3. 1.1 . 1 Review p rocess data for variations in pressure drop acr06S the bagbouse, the baghouse cleaning cycle, baghouse inlet temperature, or gas flowrate that corresponds with the occUJ'I'ellCe of the bag leak detection 

### a!= If review of this · procc$S data or other 

### f3.ctors (e.g? high humidity, reconditioning) indicates a high probability that the exce5Sive triboelectrie signal is a false indication of a bag leak/failure, then record 

### findings and proceed with normal opemtions 3.1.1.2 I f relative particulate matter loading 

### remains above the high alarm set point, take ·actions to reduce the relative particulate matter loading (e.g.,**con troll~**  ' shutdown of high ash waste f eeds). 3.1.1.3 

### If after 30 minutes of the OCCUITellce of the high alann, the relative particulate matter loading remains above 

### the high 

### alarm set poin1, follow the eorrectivemeasures of3.1.2. 3.1.2 In case ofreoccurring false bag lealc detection alarms : 3. 1 .2.1 Clean the bag Jealc detection system probe, and/or adjust the sensi tivity (range), ave:ragiQg period, alann set points, and/or 

### alarm delay time, as needed. 1 '.

VES 004050

## l 3.1.1.2 lf com:ctive measures of 3.1.2.1 were previously unsuccessful, follow 

### corrective measures of3 . 1 . 3. 3.1.3 lo 

### case of

### an alarm for high-high relative particulate 

### molter l o.ading: 3.1.3.1 Initiate a controlled shutdown ofwaste feeds. 3.1.3.2 lnspect bagbouse for leaks, tom or broken fil ter elements, or other internal equipment failures; and repair as needed . 3 . 1.3.3 Following inspectioolrep air of bagbouse, clean the bag leak detection system probe, and/or adjust the sensitivity {range), averagi ng period, alarm set points, and/or alann delay time, as needed. As stated in the US EPA 

### Fabric Fi!ter Bag LeaA: 

### DetectioiJ Guidance (EPA -4S4/R - 98- 015) , " ...conditioning the [bag leak detection] system to the 

### process environment is critical to reliable and repeatable operation ." Therefore, allowance for reconditioning 

### tbe system to the 

### process environment should be m.ade after cleaning the probe or after making adjustments to the sys l. em .



### a 

## ·.

;.·

VES 004051l .



# c· 4.0 INSPECTION AND MAINTENANCE As stated in Sectio ns V . a.F . and V.b . F . ofVeolia ' s Part B RCRA Permit, each incinerator syS!em unde(goes a "thorough visual inspection for leaks, spills , fugitive emissions, and sign of 

### tampering at least dai ly and in accordance with the inspection schedule, co n tained in 

### Appendix 6 of the approved**~t** app li cation". 

### Veolia utilizes these inspections and additional preventive maintenance activities 

### as proactive measur es for minimizing the potential for malfunctions. To facilitate 

### proper maintenance, a cold shutdown will occur at least once per year for each incinerator system. Table 4-1 presents a gi:oenl SIIIIU113J)' ofthe inspection and maintenance activities that are perfonned to prevent malfunctions. Routine inspection and mainte!lanee activities are scbeduled, communicated , and recorded through the use of field cbeclclists. Parts of tbe incinerator systems that are subject to :wear (e . g., bearings, 0-ringJ , air/oil filters) are rep laced based on the schedules indicated on these checldists. These field cbecldists will al so be used to document repairs or rep l acements of incinerator components tbat may be revealed during inspections . If as-needed repairs cannot be perfonned immediately (withi:o 24-bours ), SDP I 0 II - TWJ Remedial Acti o n Work Order Program-ensure s that these non- ro utine maintenance activities are given the appropriate priority and are tracked through co mpl etion. Brief procedures/instructions for inspection and maintenance activities are provided on field checklists . Ad diti on detail s and procedures for inspection and niaintenancc activities are communicated through the following : • SDPs for specific process maintenanee p rocedures (see Table Z.l ); • Inspection and 

### maintenance procedures 

### from equipmart manufaclllrCrS ; • Training activities for maintenance personnel; and • Shutdown and mainteoance meetings. Selected inspection and maintenance activities may be perfonned 

### bY qualified contractors or associates affiliat ed with an equipment manufucturerlvendor. Veolia will include documen tati on ofthes e activities in the opera ting record. Inspecti on and maintenance requirements are also addressed in other plans required by the Interim HWC MACf Standard. Inspection and testing of the AWFCO system are described in the Automatic**Wa:~t e**  Peed Cutoff Plan.. Inspection. calibration , and . po-eventiv e maintmanoe for the continuous emissions monitoiing systan (CEMS) are discussed the CcntUruous Emi.uions M o nitoring System Quality A.ssuranCll Plan. Discussion on calibration and maintenance for the continuous monitoring system (CMS) is prnsented in the Ccntii'IUOJIS M o nit o ring Synem Quality As.rurance Program.

9 

## ..

VES 004052Ta ble4-l I.ospec:tio o a od M.aloten a oc e to Pn veo t M a lfunctions l'oteutl a l Ca us e for lospectioos Malo.te.aauce Malfunclioo 

## • Cleaning 

## • Tigliteoing fasteners and 

## • Daily inspcc:tions for leaks, supports corrosion. and vibration 

## • Lubrication Mecbanicallelectrical 

## • Instnnnentation and alarms for failure ofrotating 

## • Alignment current, lubrication, and/or cquipmenL vibration on selected rotating 

## • Scheduled n!ploccment o f equipment critical parts 

## • As needed repairs/replacements 

### Daily inspection for leaks, and 

## • Cleaning 

## • Plugging/Mechanical corrosion 

## • Tighteoing supports fa:ilure of 

## • Jntemai equipment inspections 

## • As needed lines/nozzles dnring shutdowns repairslreplact."JJlents 

# ( •· , ; 

## • Process variable indication 

## • Scheduled replacemmt of Mechanical/electrical 

## • Comparison between instruments failure of redundant instruments 

## • As needed instnanentation Calibration checks repairs/replacements 

### • 

## • Daily inspection for leaks, and corrosion 

### • Visual inspection ofinstrument air and electrical comections 

## • Cleaning MecbanicaVelectrical 

## • Confirmation of fai l -safe 

## • Lubrication failure of actuated positious during shutdowns 

## • AF.needed valves/dampers Confirmation of functionality repairs/replacements 

## • through p rocess variab le control/indication 

### • AWFCO Testing



### •, 10 VES 004053

## ( Tabl e 4-1 (contiDUed) In spection 

### u d Mal•te.auee t o Prevent Malfunctio•s Poto tl a l Ca li se for Jn spedio o s Mabateoance Malluoctioo 

## • Process variable Physical/electrical controlfmdicatioo 

## • C leaning fa.iture of control • . Visual inspection of 

## • /uneeded system connections rcpairslrcpl.acanents 

## • AWFCOTming Mecbaoieallelectrical 

## • lnspl:cti.oos of the utility 

## • As needed failure of utility supply source rcpam/rcplacemeots supplies 

## • Conlinootion ofvalve fail-safe

. EleclricaVactuation positions during shutdowns 

## • As needed failu.n: of safety 

## • V erification of alarms and repairs/replacements inter l ocks interlocks during A WFCO 

# ( '· Testing 

## • Internal clcaoing 

## • Daily exterior inspections for Pbysicallmechanical leaks, coaos io n, and vibration 

## • Tightening fasteners and intemal equipment Interior inspections during supports failure 

## • shutdowns 

## • As needed repairslreplaccm.e:nts



### ' '. II VES 004054i

### '



# ( . . .' 5.0 ALTERNATIVE MODE OF OPERATION Veolia routinely perfonns certain inspection and maintenance activities that cannot take place wl;rile operating the incinerator under the requirements of nonn al operation and must be performed more frequently than cold shutdowns. These activities are typically identified during the proactive inspections (see Table 4-1) or when noticeable changes in normal operating pamneters are identified. These inspection and maintenance activities cannot take place wlnle operating the incinerator under the requirements of normal operation s ; however, a cold shutdown is not required to complete these activities. For this reason, Veolia bas defined an alternative mode of operation during which these activities can be perfgnned. This mode ofoperation is referred to as the "warm stand-by 

### mode". The wann stand-by mode of operation is being implemented per the 

### reqnirements in 

### § 63 . 1206(b)(1 )(ii). This mode of operation will only be implemented when hazardous waste is not in the cOmbustion chamber (i.e., the hazardous waste residei!Ce time has tr.mspired) . The remainder of the section describes the wann stand-by mode and the applicable requirements for this alternative mode ofoperation. 5.1 Warm Sta nd-by Mode of Operation The wann siand-by mode ofoperation is utilized to perform inspections and maintenance activities that do not warrant a complete cold shutdown. During this mode of operation th

e combustion chamber temperatures are m aintained utilizing natural 

### gas . This is desirable 

## from a long term operating standpoint to minimize extreme temperature cycles for the refractory which can lead to excessive wear and premature failure. Futther, this provides for shorter duration maintenance periods and a quicker retnm to normal operation**(i.e~** since the CQmbustion chambers are not cooled to ambient conditions, then the "nolll)ll)" operating temperatures can be attained 

### in a shorter duration). Operation in · the wann stand-by mode can only be'gin when hazardous waste is not 

### in the combustion chamber (i.e., the hazardous waste residence time bas tr.mspired). Only natmal gas will be fed to 

### · the main burners to maintain stand-by temperatures of the combustion unit Veolia will document in the operating recotd all times 

### thai the unit is in warm stand-by maintenance operating mode as well as descriptions of any inspection and maintenance activities performed during the warm stand- by 

# mode.

12 , . '

VES 004055

# ( During the warm stand-by mode of operation all combustion gases are ducted through the air pollution control system (APCS) . The APCS, continuous monitoring systems (CMS), and continuous emission monitoring systems (CEMS) are operated per nOilllal operating procedures, unla;s temporarily out-of -service for inspection and maintenance . activities. The automatic waste feed cutoff (A WFCO) system is not operational since there is no hazardous waste feed to the unit Per § 63.1409(q)(2)(iii), Veolia wiD utilize a seamless transition 

### between operating in wann stand -by mode and normal operations. This allows for ealculating rolling averages using data from the previous operating mode. Prior to transitioning to normal operating mode, Veolia wiD ensure that valid data is available for calculating rolling averages and that all parameters are within limits. Normal operations wiD resume with the initiation of hazardous waste to the incinerator. S . :Z Applica ble Reqn ir emeats When operating in the warm stand-by mode the following 

### Interim HWC MACT standards do not apply: • Emission standards in § 63.1203 • Monitoring and compliance standards of§§ 63.1206 through 63.1209, except the modes ofoperation requirements in§ 63.1209{q) • NotifiCati on, reporting, and recordkeeping requirements of §§ 63.1 2 1 0 through 63.1212 Per the requirement of 63.1206(b)(ii), Ibis section supplies documentati on in the operating record that V eolia is complying with all "otherwise applieable requirements" during warm stand-by mode ofoperation. Requirements conStitute "otherwise applicable requirements" to the extent that they do not arise from Subpart BEE and they are otherwise applicab l e to any ofthe emission units when it is ope:ratirtg during warm standby mode. Incinerator Unit 

### :i, Unit 3 , or Unit 4, when operated under warm stand-by m

ode, is not subject to any "otherwise applieable requirements".

13 VES 004056

## ( 

# FEEDSTREAM ANALYSIS PLAN

Veolia ES Technic al Services, LLC Sa u get, Illinoi s

October 2008

VES 004057

# (



# ( " · Feedstream Analysis 

### Plan - October 

### 2008 

## TABLE OF CONTENTS

1.0 INTRODUCTION 2.0 FEEDSTIU:AM P ARAMETERS 

### 2.1 Chlorine 2.2 

### Metals 2.3 

### Ash 3.0 ANALYTICALRATIONA.LE 

### 3 . 1 Analysis P ecfon:nod by Vco1ia 3.2 Analysis Performed by Others 3.3 Manufacturer 

### Data or Other Published Jnfonnation 4 . 0 APPLI CA TION OF ANALYSIS FOR FEEDRATE COMPUAN CE 

### 4.1 Process Planning for Peed.streams 4. 2 

### Process Con1Iol 

### for Fcedstreams 

### 4.3 Docoimentation and 

### Recotdk:eeping for Process 

### Planning and Con1rol 5.0 SAMPLING AND ANALYTICAL METHOD S 

### 5. 1 Sampling Methodologies 

### 5.2 Documentation and 

### Recordkeeping Associated with Sampling 5.3 Analytical Methodologies 

### 5.4 Documentation and 

### Recordkeeping Associated with Sample Analysis 6.0 FREQUENCY OF . ANALYSIS 7. 0 COMPLIANCE WJ11J FEED RATES 

# • ,.

VES 004058

## (



# ( .... . ,.-

i . . Feedslleam Analysis Plan - October 2008 1 . 0 JNTRODUCI10N Pursuant to the regulatory requirements found 

### iD 40 CFR 63.1206 (c) oftheHWC MACT Standard, Veolia 

### ES Technical Solutions, 

### LLC (Veolia) has developed a 

### Feedstream Analysis Plan (F AP). Its purpose is to provide a system wberd>y Veolia can sample, analyze, and control the i ncineration offeedstreams that may contain constituents 

### requiring feedrate limits as.**~ed** 

### iD the HWC MACT 

### Standard. The FAP also 

### addresses how 

### these activities will be 

### recorded in the 

### facility's operating record. 

### This FAP is organized sud! that each ofthe subieqneot sections specifically addresses the six parafppbs under40 CFR6 3 . 1206 (c) (2) and three paragraphs under40 CFR 63. 1 206 (c) (4) 

### iD the order in which they are 

### preseoted in the HWC MACT Standard. In many insfancM, this FAP will ref= the facility 's Wam Analysis Plan (WAP). The W AP is an integral part ofthe RCRA Part B Permit, the Pcrmit Application, ond any subsequent revisioos or addenda to the Part B Pcrmit or Permit Application. 

### As required by sections 63.6 (e)(v) and 63 . 6 (e)(VJ) of the HWC MACT Standard, tho F AP and other documents containing procedures or infonnation referred to · in the F AP will be made available for inspection wbcu requested by the Administrator. The F AP , correspondence with the Administrator concerning the F AP, and any subsequent additions or modifications to the F AP will be kept in the facility's Operating Record. lf Veolia is required to submit copies ofU1cFAP or portions ofit (or related documents), coofidential business information entitled to protection from disclosure will be clearly designated. 2.0 FEEDS TREAM PARAMET.EM 'I'bae are three feedstream constituents that are specified in the HWC MACT Standard for emission and/or fee<lrale Jilnitalions and that may be preseot in any given feedstream . These three are: · 

### I) Chlorine 2) Metals (MctCUT)', 

### Lead. Cadmium, 

### Cbro mimn , Beryllium, and Aisenic) 

### 3) Ash These three constituents will serve as the 

### feedstream parameters ofconcern in the FAP as required by40 CFR63 . 1206 (c) ( 2 ) (l) ofthe HWC MACT Standard . Feedstream data applicable to each ofthese parameters will be obtained for all feedstreams in order to control the incineration of them and remain within the feedrate limits set for thern . 

### 2 . 1**~oriae** Fcedstream data will provide a weight-based percentage of chlorine for each waste feed to the incinerators . These results ean be used to both estimate targeted f eed rate values and control actual feed rates during incineration.

2 

### ' r.

VES 004059( \

'



# ( . . ' Feedstream Analysis Plan - October 2008 2.2 · M etal s Feedstream data will provid e a parts-per-million concentration for each ofthe listed metals in each ofthe waste feeds to the incinerators . For analytical results 

### that show less than detection limit concentrations, l-S the detection limit value will be used for incinerator feed computations . These results can be used to both estima te targeted feed rate values and control actual feed rates dllring incineration. · 2.3 Ash Feedstrcam dala will provide a weight-based percentage o f ash for eaeh of the waste feeds to the incinerators. These results can be used to both estima t e targeted feed rate values and control actual feed 

### rates during incineration. 3. 0 ANAL YilC AL RA TIO NALE In 40 CFR63.1206 (c) (2) (ii)oftheHWCMAC'f Standard, a facility is required to identifY bow it will obtain the necessary analysis to comply with these regul ations. There are three sources of analytical inf ormation that V eolia can use in evaluating the feedstream pararneters 

### as descn'bed in Section 2 . 0 of the F AP . They are: I) Analysis perfonned by 

### v eolia · 2) Analysis perfonned by others 3) Manufacturer d ata or other publi.<hed information These sources are also referenced in the facility's W

### AP and the ways in which they can be applied to feeds treams are ex t ensively addressed. Many ofthe analytical procedures perfonned 

### as descn'bed in the F 

### AP 

### are also required 

### as part ofthe waste acceptance and management process at V eqlia The information derived ftom these procedures can then be used in complying 

### \vith the feedstream limitations for the parameters identified in the 

### FAP . The three analytical sources can be applied to generator wastes received at the V eolia facility, including th ose that undergo subsequent blending prior to incineration, and also to wastes that are generated at the faci lity. 3.1 Analysis Performed by Veolb The predominate means applicable to 

### this source ofanalytical infol!Dation is the methodology desc n 'bed in Section 5.0 

### of the 

### FAP . Specifi c analytical methods perf ormed in 

### tbt Jilcility' s laboratory are applied to aJli>li<:able feedstreams to produce values fo r the required parameters. Typically, the 

### feedstream is a waste profile from a generator that bas been accepted according to the facility's W 

### AP guidelines. This waste will hnve had analytical work performed on a sample for au initial acceptance decision and supplementa l analysis as 3 

## , .**:**



### ,.

VES 004060

# ( · . ·-
.**~** 

# .. Feedslream Analysis Plan :- October 2008 required for subsequent shipments of the waste. This analytical work 

### wiD include information on the parameter.; identified in the F AP and can be used to cootrol the incineration ofthe fcedstreams . 

### In other instances, the feedslreams are was t es blended togetber at the facility (e .g., bulk liquids and bulk solids) or wastes genernted by the facility (e.g., laboratory wastes, incinerator ash). Feedstreams that are the result ofblending or other on-site**p~** steps prior to incineration 

### can have parameters deteonined 

### .from the same analytic al methods described in the previous paragraph or b y statistically arriving at au average valne based on a body ofpreviously analyzed sainples. Wastes generated by the facility 

### will have parameters detennined from au average value based on a body of previous ly analyzed samples. For many feedstreams, the best soW'Ce ofinformation for the parameters ide.ntified 

### in the 

### F

AP 

### wiU be obtained using the tecbni cal expertise o fV eolia personnel Examples of these types of feedstreams are labpacks, controlled substances and empty container.;. The facility's WAP listssomeofthesereference sources in Appendix WAP-F. 3.2 ADalysis Pmormed by Others 

### In situations where V eolia cannot 

### perf0110 the necessary analysis due to the uature of the feedstream (e.g., gases, some reactive materials) or when previous outside analysis of feedStreams that meets the standards ofthis F AP 

### is available, V eolia 

### will accept the analysis ofothers in detennining parameter values. This analytical information wiD be evaluated and used to control the incineration offeedstreams in the same manner as analytical information produced at the factlity. 3.3 M.ann . factuer Data or Other Publl.slaed Infol'lll2tion Many feedstreams have pre-existing information applicable to them that can be used to determine the values of the parameters as identified in the FAP. This can take the form of manufacturer specifications and data, Material Safety 

### Data Sheets, reference SOW'CCS or other published infonnation. The facility's W AP lists some ofthese reference sources 

### in . Appendix W AP-F. Examples ofthese types of feedslreams include commercial products, pharmaceuticals, chemical 

### reagents, and 

### gas cylindels. This information 

### will be evalnated and used to control tbe incineration of these feedstreams in the 

### same lD8llllef as an alytical information produced 

### at the facility . 

### 4.0 APPLICATION OF ANALYSIS 

### FOR FE:EDRATE**~OMPLIANCE** 

### F

eedstream data 

### Will be 

### used to maintain comp.liaDce for !be feedrate limitations to 1he incinerators. This analysis wiD be completed prior to the feeding of any material to the incinerators. The doc umentation ofthese feedrate compliance methods is required by 40 CFR 63.1206 (c) (2) (iii) oftbe HWC MACT Standard and outli ned in this section ofthe PAP .

4 VES 004061

# ( Feedstream Analysi s Plan - October 2008 Analytical results can be used to both estimat e targeted 

### feed rate values and control actual feed ratea 

### during incineration. 

### Analysis from**laboratory~** at the facility, analytical 

### results from others, published infonnation, and technical evalualiollS by Veolia personnel can all be used in complying with feedrate limitations for the parameters idcnti 6ed in the FAP.ln addition, these analytical information 

### sources can be used for wastea 

### from generators , wastes blended at the facility , and wastea generated at the facility . 4.1 

### Proem Plunillg for Feedstna ms When evaluating analytical results and any additional information applicable to a potential feedstream, a decision must 

### be made whether parameters for that feedstream are

· acceptable for 

### feeding to the incinerators or 

### if some level o f feed preparation is necessary. 

### This step in the feedstream evaluation 

### process 

### is called 

### process planning; It is applied to blending wastes, processing wastes into combusti ble cbargea, and determining if

wastes can**~fed** directly to the incinerators as initially received at the facility. 1'bis plaaning is per!O<med based on information from analytical resnlts, incinerator perfonnance capabilities, process operation 

### history, and the toclmical expertise of the process planning penonnel involved. 4.2 

### Process Co ntrol f or Feedstreams ln order to ensure that feedrate limits fo r the parameters in the F AP are not exceeded during operation ofthe incinerators, automatic systems must be in place to control the 

### incineratoc process. These systems continuously track the feedstream parameters as they 

### are introduced into the incineralars and make the necessary . feed adjustments or cut-<>ffs for compliance. Section 

### 7 . 0 of the 

### FAP addresses these systems and the ratiooale behind their operation in**g~eateo-** detaiL 4.3 Documentation and Recordkeepluc for Proeess Plnnlug ud C ontrol Documentati on ofproeess planning and contro l is demonstrated by the extensive body of infonnation coUected in the facility's data management system, and, ifn eeded, distributed in bard copy form to appropriate personnel. 

### Tliis includes laboratory analysis llSed for feed preparation, bulk waste storage data, processing directions, and related infonnation . Aetual incinerator operatio . ns data is recorded in printed 

### summaries, recorded onto digital data 

## stonge systems, and is also selectively available oo-tine . 1'bis infolDlation will be retained in the operating record for the life ofthe facility . 5. 0 SAMPLING AND ANALYTICAL METHODS The requirerQents in 40 CFR 63.1206 (c) (2) (iv) and (v) ofthe HWC MACT Standard state that 

### a facility m ust identifY the sampling and test methods used for anulydng the feedstreams . The sampling methodology and much of the analytical methodology that is 

### described in Sections 2.0 and 3.0 of the facility's Waste Analysis Plan i s applicable to the 

### F

AP. Additional sampling and testing infonnation is included in the following paragraphs of this section. 

## s VES 004062

### (



# C .. ; 

## .· Feedstream Analysis Plan - October 2008 S . l S amplblg M etlaodologies Sampling is performed at the Veolia facility to identify waste shipments an d also by the genmtor at their location when making ao initial detennination on the Keeplability of the waste at VeoliL 1o some inslaoces , an actual sample will not be required because technical persoDDel 

### at Veolia will have detenniued that sufficient documentation 

## already exists that ' identifies information regarding the parameters desaibed in Section 2.0 ofthe FAJ> (see also 

### Section 4.0, Paragraph 4.1.12 (2) ofthe WAJ>).lo order to obtain a representative sample of the waste, specific samjlling procedures that are depc:oden t on both the nat ure ofthe waste samp led and the typo ofprocesses in w hic h the waste will be st

ored or transferred must be performed. Section 2.0 ofthe facility's WAJ> 

### and pertinent appendices in the WAJ> list these procedmcs and the ASTM method number (or other EPA approved llldhod} on whicb they are based. This section in the W AP also addresses the sampling equipment used, the**~** ofinteoded containment or proccsscs tlaat can impact the sampliog. and guidetincs on bow to ensure that a valid and representative sample is oblaincd. 5.2 Doc11menta li o n 

## and Rcc ordkeeplug Assoclated w itb S am pliag All samples taken at the fac i lity or sent to the facility for analysis are assigned a lllrique sample i dentification number. 1bese identification numbers are recorded in a chain-ofcustody log and used for tracking the sample through the facility's data collection system. 

### Each sample alao has a label affixed to it identifying its contents, the date the sample was taken, and the penon who took the sample. 5 .3 Ana l y1ltal M etbodolocies CHLORINE The analytical procedures and EPA approved ' mcthods related t o determining the amount ofchlorine in a feed.stream are foun d in Appendix WAJ>-A to the faci lity's WAP . MET ALS Feedstrearns that require analysis for the metals specified in the HWC MACT Standard will either 

### contain these metals in a non - water-soluble form or a water-soluble funn. Samples offecdstreams iu a non - water-soluble form wiU require additional preparation steps prior to analysis . The analytical procedures 

### and EPA approved methods related to 

### determining the amount of listed metals in a focdstteam are l isted below . Digestion Procedure for Non-Water-Solubl e**Sample.~** Method 305 lA - Microwave Assis ted Acid Digestion of Sediments, Sludges, Soi l s, and Oils

6 VES 004063( 

## · 

## .. Feedstream Analysis Plan - Octobe r 2008 

### Proeeclurn for De!mnjning Concentration of

### Mercury in Sample Method 74 73 - Mercury in Soli ds and Solutions by Thennal Decompositio n, Amalgamation, and A tomic Absorption Spectrophotometiy Procedure for Qe!mpjning Concquration o f 

### Arsenic. Bervlli!Dll. Cadmi!Dll. Chromjum 

### and Lead in Sample Method 60 10C - Induc tively Coupled Plasma-Atomic Emission Spectrometry ASH The analytical procedures and 

### EPA approved 

### methods related to determining the amoliD.I ofash ina feedstream arefolllld in Appendix WAP -Ato the faci.lity's WAP. 5 .4 Documentation a nd RecordkeepiDg Associated with Sample Analysis Documentation of analytical w odc is accomp li shed by 

### recordiDg it iD laboratory logbooks, entering it 

### into the facility 's dala management 

### system, and, ifneeded, di stn'b uted in hard copy form to appropriate personnel. All technical files for waste profiles will also include initia l laboratory analysis imd any applica ble subsequent analysis. This information will be retained 

### in the operating record f 0 r · the life of the facility . 6. 0 FREQUENCY OF ANALYSIS 

### In 40 CFR. 63.1 206 (c) (2) (vi) ofthe HWC MACf Standard, a facility is required to identify the freq uency with which an initial analysis i s repeated or reviewed to ensure that · it is cum:nt . This F AP wi Drequire that the analytical information for the feedstreams be re-evaluated on a Ji:equency consistent with that d escn'bed for aU wastes as described 

### in Section 4.1.3 o f the facility's W AP. The three events that may trigger a need to update or evaluate the analysis ofa given feedstream are: I ) Gen erator notifies V eolia that a feedstream bas changed 2) Subsequent analysis for a feedstream used by V eoli a is 

### incons istent with the original analysis 3 ) Five years have passed since the last assessment ofth e feedstream 

### In o rder for a feed stream to be considered acceptable again for incineratio n after one of these events has occurred, the evaluation process as described in this F AP must be completed. 7 .0 COMPLIANCE WITH FEED RATES V

eolia emp loys process control systems for the incinerato rs that m onitor, adjust 

### and record feedstreams and the k ey parameters i dentified in the F AP that are associated with 1 VES 00406 4

## (' ' ·



### •.. Feedslream Analysis Plan- October 2008 

### than. These systems meet the 

### reqllircments of40 CFR 63.1206 (c) (4) , paragraphs (i) , (ii) and (iii). The ·systems and the rationale that 

### supports these systems are descn'bed in the fo llowing paragraph. 7.1 Feed Rate Compl iance Sys t ems and Methodology A1\er the metals and ash coMentratiODS**fo~** feedstreams axe detenniued, they will 

### be en1ered into the facility's data manag ement systems. These feedstreams are identified in the system under a site tracking number, bulk pit number, or tank nwnber. Once this information is in the waste 

### tracking system, 

### the incinerator control systems we able 10 iroport and store 

### the data for use as the waste slrC3mS are processed at the incina'ators . All 

### waste introduced into the incincraton; has an associated site identifialtion designation (receiver number, etc.) so it QD be refcrc:nced 10 the appropriate data from the waste tracking system. As weights are recorded at 1 5 second intervals for each**~fie** w aste sttam entering the incinerator, computations are being pcrf01med 10 caJculatc the quantities ofmetals (as low volatile metals, 

### semi volatile metals, and men:ury) and ash that are being incinerated. These quantities are ctisplayed, totalized, and reoorded in a manner that will show compliance with the established operating parameter limils for the metals categories and ash. One hour and 12 hour rolling totals are displayed for the incinerator operators for monitoring of these feeds.

8 VES 004065

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### VES 004066R un N o . 1 2 3 4 5 6 7 8 9 D ate 611712008 611712008 611712008 611712008 611712008 611712008 6/1712008 6/17/2008 6/1712008 T a ble 3 CE M S Relat ive Accuracy ·CO, J1PrA @ 7% 0, Unit 2 Inci nera tor Ex h aust

Time 0943-1004 1023-1044 1101 - 11 22 1139-1200 1240-1301 1332-1353

. 1409-1430 1 446 · 1507 1521-1542



### Ave11119e : V eolla ES Tec hn ica l So l u tion s Sauget. Il li n ois
R e f erence F acility

M ethod CEM S

0 . 03 2.10 0 . 00 2.03 0 . 00 1 .34 1.15 1 . 01 0 . 00 1.50 0 . 00 0.94 0 . 00 2 . 27 0.41 1.33 0 . 00 1 . 76

0 . 18 1 . 59 Relative Acc u ra cy :

• Not used i n avemges and RA calculation 

## ,.

Di ff erence

· 2 . 07

- 2 .03

- 1 . 34 0 . 14

- 1 . 50 -0 . 94 -2 . 27 -0 . 92

- 1 . 76

1 . 41 2.0 ppm@ 7% 02

' .

VES 004067Table 4 

### i CE M S Relative Accuracy - 

## o ., percent dry (Cos a ) U nh 2 Incinerator Exhaust Veolia ES Technica l Solutions Sauget, l ninoi s 

## ,. ; 

## ' Run Refe rence Facility No . Date nme M ethod CEMS D ifference

1 611712008 0943-1004 12 . 9 12 . 5 0 .42**~** 

### ' 2 611112008 1 023-1044 13 .2 12.8 0 . 33 3 611712008 1101 -1 1 22 13 . 2 12.7 0 . 47 4 611712008 1139-1200 1 3 . 4 12.8 0 . 59 5 6/1712008 1240-1301 13 . 1 12 .5 0 . 84 8 6/1712008 1332- 1353 1 2. 6 11 . 9 0 . 63 7 6/1712008 1409-1430 13.4 12.7 0 . 7 6 8 61 1 712 006 1 446-1507 13.4 12.5 0 . 8 7 g · 61 1 712008 1521-1542 13 . 5 12.6 0 .72

Average : 13 . 18 12.58 0 . 60 Relative Accura cy: 6 . 6 %ofRM

• Not used in averages and RA ca l culation

VES 004068Ta bl e 5 CE M S Relative Accuracy • 0 2 , pen:ent wet (Cosa) U n i t 2 Incinerat o r Exhaust Veolia ES Tech n ica l Solutio n s Sa u get, IIHn ois 

### ! R u n Refe r ence Facility No . Date Time Method CE li S Difference 1 611712008 0943- 1 004 7 . 83 7.31 0.52 2 611712008 1023-1044 8.22 7. 50 0 . 72 3 611712008 1101-1122 8 . 28 7 . 53 0 . 75 4 611712008 1139- 1200 9 . 07 7 .63 1 . 44 5 6/1712008 1240-1301 7.89 7.23 0 . 66 6 6/1712008**1~2 1353**  7 . 16 6.66 0 . 50 7 6/1712008 1 409 - 1430 6.10 7 . 94 0 . 16 8 6/1712008 1 446 -1 507 8 . 1 5 7 . 85 0 . 30 9 6/1712008 1521-1542 8 . 1 8 7. 92 0.26**Aven~ge :**  8 .10 7.51 0 . 59 Relative Accuracy : 1 0.9 %ofRM
• Not used in averages and RA calculatlon



### ,,

VES 004069Table 6 CEMS Relative Accuracy - Moisture, percent Unit 2 Inc inerator Exhaust Veol i a ES Technical Solutions Sauget, Ill i nois •. Run Reference Faclnty N o. Date Time M ethod CEMS Difference · 1 611712008 0943-1004 39.3 41 . 5

- 2.2 2 611712008 1023-11144 37 . 5 41.5 -4 . 0 3 611712008 1101 -1122 37 . 0 40.7 -3 .6 4 6117/2008 1 139- 1200 32 . 2 40.4 -8 . 2 5 611712008 1240-130 1 39 . 8 42 . 0 -2.2 6 6/ 1712008 1332- 1 353 4 3 . 0 44.2

- 1 .2 7 6/17/2008 1409- 1 430 39 . 6 37 . 3 2 .4 8 6/1712008 1446-1507 39.2 3 7 . 5 1 .8 9 6117/2008 1521-1542 3 9 . 5 38 . 1 1.4

Average : 38.6 40.3 1 . 8 Relative Accuracy : 11..2 %ofRM

• Not used i n averages and RA calculation

VES 004070Run No. 1 2 3 4 5 6 7 8



# . •. \ 9 Date 6/1712008 611112008 6/1712008 6/1712008 6/1712008 6/ 17 /200 8 6/1812008 611612008 6/1812008 Table 7 CEMS Rel ative Accuracy - CO, ppm @ 7% 0 2 Unit 3 Incinerator Exhall$t



## nme 1716-1737 1801-1822 1836-1857 1913-1934 1948- 2009 2023-2044 07 52..0 61 3 0825 ..0 646 0857-0918

Average : Veolla ES Technica l Solutions Sauget, IU i nois
Reference Facility

Method CEMS

0.00 0 .00 0 . 00 0 . 00 0 . 00 0 . 00 0 . 00 0 .00 0 . 28 0 . 00 0 . 29 0.00 0 . 00 0.00 0 . 11 0 . 00 0 . 03 0 . 00

0 . 08 0 . 00 Relative Accuracy :
• Not used in averages and RA calculation Difference 0 . 00 0 . 00 0 . 00 0 . 00 0 .2 8 0 . 29 0 . 00 0 . 11 0 . 03

0 . 08 0.2 ppm @ 1% 02

VES 004071Average : 12.28 11.92 0 . 38 Relative Ac:euracy : 5 . 3 %o 1RM
• Not used in averages and RA calculation

VES 004072!

. ··

.


### . ' . J •'

\

i Run No. 1 2 3 4 5 6 7 8 9 Table 9 CEMS Relativ e Accuracy • 0 2 , percent we( (Cosa) Un it 3 Incinerator Exha ust Veolia ES T echnlcal Solutions Sauget, IUinoi s**~** Reference Facility Date Time Method CEMS Difference 611712008 1716-1737 6 . 73 7.46 -0.73 611712008 1601 -1622 6 . 63 6 .79 -0.16 611712008 1836-1857 6 . 49 6.63 · 0.14 611712008 1913-1934 7 . 87 7.41 0.46 611712008 1948-2009 7 .1 2 7 . 36 -0 . 24 611 7 12008 2023-2044 7.12 7.25 -0.13 6118/2008 0752-0813 4.97 5. 41 -0 .44 611812008 0825-0846 5.54 6 . 00 -0.48 611812008 085 7-0918 5 . 91 6.33 -0 .42

Average : 6.49 6 . 74 0.25 Relative Accuracy: 7.8%ofRM

• Not used in averages and RA calculation

VES 004073Table 10 CE M S Relatl\le Accurac:y - · M oisture, percent Unit 3 Incinerator Exhaust Veolla ES Technical Solutions Sauget, Illinois

## ~ Run Reference Facility 

### No. Date Time M ethod CEMS Difference

1 6/1712008 1710-1737 47 . <4 36.8 10 . 5 

# ,.**~** 2 6/1712008 1801-1822 46 . 5 40 . 2 6 . 3 3 611712008 1836-1857 48 . 9 44.4 2.5 4 611712008 1913-1934 39 . 5 42 . 1 -2 . 6 5 6/1712008 1948-2009 44 . 8 42.1 2 . 7 8 6/17/2008 2023-2044 44 . 3 42.5 1 . 9 7 61 1 8/2008 0752-0813 53 . 6 48 .4 5.3 8 6/1812008 0825-0846 52.4 48.3 4 . 1 

### ' 9 6/18/2008 0857-()918 51 . 0 . 47.4 3.5 I Avet"!je : 47 . 4 43.6 3 . 8 Re l ative Accuracy: 1 3 . 8 %ofRM
• Not used in averages and RA calculation

VES 004074Table 11 CEMS Relative Accuracy - CO, ppm @ 7% 0 2 Unit 4 Rotary Kiln Exhaust Voolla ES Technical Solutions Sauget, Illinois
Run Reference Facility No. Date Time Method CEliS Difference

1 611812008 1257-1318 2 . 59 1 . 74 0 . 85 ; 2 611812008 1334- 1 355 2 . 78 1 . 10 1 . 68 3 611812008 1413-1 4 34 2 . 70 1 . 13 1 . 57 4 611812008 1456-1517 2 . 69 1 .44 1.25 5 611812008 1544-1605 2 . 77 2 . 26 0 .5 1 6 611812008 1 623-1644 2 . 29 1 .79 0 . 50 7 611812008 1700-1721 2.25 1.73 0 . 52 8 6118/2008 1732- 1753 2. 0 5 1.91 . 0 . 14

.· 

# :.) 9 611812008 1806-1827 1.75 2.35 -D.60
Average: 2.43 1 . 72 0 . 7 1 Relative Accuracy: 1 . 3 ppm@7%02

• Not used i n averages and RA calc ulation

VES 004075Table 1 3 CEMS Relative Accuracy - 

## o, percent dry (Cosa) Unit 4 Rotary Kiln Exhaust Veolla ES Technical Solutio n s Sauget, Illinois

## ~ Run Reference Fae Hity No. D ate Time M ethod CEMS Diffe rence

1 61 1 812008 1257-1318 13 . 86 13.9 -0 . 05 ; : 2 6/1812008 1334- 1355 13 . 45 13.5 -0 . 08 3 6/1812008 14 13-1434 13 . 28 13.3 -0 . 05 4 611812008 1456-1517 1 3 A6 . 13 . 6 - 0 . 11 5 6/1812008 1544-1605 13.72 13.9 -0 . 14 6 6/1812008 1 623-1644 13.45 13. 5
-0 . 01 7 6/1812008 170()..1721 13.49 13.4 0 . 06 8 6/ 1 812008 1732- 1753 13 . 59 13.6 0 . 03 9 611812008 1806-1827 13 . 61 13 . 6 0 . 06

Average: 13 . 55 13.56 0 . 03 Relative Accuracy : 0 . 6% of RM

• Nol used In averages and RA calcu l ation

VES 004076

### ' '

. ' Ru n N.

o . 1 2 3 4 5 6 7 8 9 Date 611812008 61181 2 008 61 1 812008 61 1 812008 6/1812008 6/1812008 6/1 812008 611 812008 6/ 1 812008 Table 1 3 C E MS Re l atiV e A cc uracy - O z. pe r cent wet (Cosa) Unit 4 Rotary Kiln E xhaust Veo l ia ES T ech n ical So l u t ion s Sauge t; Illinoi s
Refe re nce F a cil ity Tlm e Meth od C E M S 1 257 - 1318 8 . 56 8.36 1 334- 1 35 5 7 . 36 8 . 0 3**14 ~3-** **434** 7 . 55 7 . 85 1456- 1517 7 . 59 8 . 02 1544-1605 7 . 6 8 8 . . 2 4 1 623-1644 7 . 22 7 . 99 170()-1 721 7 .4 2 7 . 91 1732- 1 753 7. 70 7 . 99 1806- 1 827 7 . 79 8 . 0 7

Average : 7 . 65 8 . 05 R el atiV e Ac curacy :

• N. ot used i n ave ra ges a n d RA calculation D iff erence 

## o

. zo . , -0.67 -0.30

- 0 . 4 3 -0 . 56 -0 . 77 -0.49 -0 . 29

. -0.28

0 .

40 8 . 1 %ofRM



### . ..

VES 004077Table 14 ' ) CEMS Relative 

### Ac curacy - Mo isture, 

### percent Unit 4 Rotary Kiln Exhaust Vec:i l ia ES Tech n ica l Solutions Sauget, Illinois 

# •**·** Run Reference Facility No. Date Time Method CE M S Differen ce 1 611812008 1257 - 1318 38 .2 40.0 - 1 .7 

# .. ( 2 611812008 1334- 1355 45 . 3 40.7 4 . 6 3 611812008 14 13-1434 43 . 1 4 1 . 1 2 . 0 4 611812008 14 56-1517 43 . 6 40 . 9 2 . 7 5 611812008 1544-1605 44 . 0 40.5 3 . 5 6 611812008 1623- 1644 4 6 . 3 40 . 6 5 . 7 7 61 1 812008 1700-1721 4 5 . 0 41.1 3 . 9 6 6/1812008 1732- 1753 43 . 3 41 . 1 2 . 2 9 611812008 1806- 1827 42 . 8 40 . 5 2 . 3

Average : 43 . 5 40.7 2.8 Relative Accuracy: 10 . 1% ofRM

• Nol used in averages and RA celcu l atlon

VES 004078

### t .. . . .

· '

: 

### ' , }



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### . . .. .**~5'** · · : . . 

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# ·.**:ao .**  t•1**~'"'~'~** 4! S-4& •TUl

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### to 1'ypica:l Physical Analysis 

### Minus . 100 mesh Lt1n)Js · 200 ' me&h Minu .s 325 mesh Densit:f 3.**Po~nda** per ft 

### (D<opend1ng upon

compaction)**10{).0~** 96.5 92.0 20 to 32 degree of 

### 97.2% 73.6 74.3

1. 75 0 .1 0 0.024 0.65 ' <1 . 30 0.10 0.55 0 . 95 0.012 0 . 0025

:



### VES004079

# ( · 69:4 5 5642757397 

# NORIT Americas Inc.

""" , Odcos 

# +- Fl • Best Perlcrmol>:e. 

# DATASHE E T DARC0 °FG L POWDERED ACTIVATED CAF!BOI'I 

# . . I<EV1N L. KAISER

I'M 363:!5 · Product NO . FGl Revised 11-97 O

AACO F'GL Is o llg1Wt coal based odMllled cwbon**~ sv** **·d6~** for lhe - ol '-"!'-and

- c:oo\ilrnlnanb**~found** In lndner.llor IIUe gas omission 

### a-. 

# Its_. pch**~** and tr.e pMide slz8 pt<mits 111e rapid lOdso<ption of gaseous mett:ury, dlcodns {PCIJO) and furons (PCDF), 

### ..:net. Is cril!atllor good**obtOIP~Ve** petfc<mance In flue gas SVUIYI$ ..... ccntac:lllmes .. 

### oho!t . · . O.MCO FGL is o**free~** powclenod cat1>0n will mlr*nal**~** 1111-ocles wl1ich 

# m- lldeal for aUIOmo6c dosing systems Will\ dry 01 wet lnjacdcn**<~redly** into lhe lluo gao t:trcom. a is maoofacllJred"""' JJ vO¥y tigh Ignition · temperature to pomlit sale opemtlon ot 111e elevated teinpemtunls**~in** lnclne<ator**~olJOS** strums. · s l!lgtlom

-- dea>lortzing elllclo'lC)', %**~.%** asped<od Mesh ol%e:**~than~.,_,** ( 45**""'~** " G !fllfJI**Cl!o"'~dolles"** St.ttflrce are a_ m Jg Hutcapadly Tolollll#ur,% 1 gn111on ternperotute . 

## ·c ..

• F« gonemt lr'lamalion ody, not to be used u purcha$0 

### .,.,..alit3b&. -40 min. 8"""" 90 min.**~ ~**  o.22

0.6 oC50 

### Pitduen a . · . · Stontlan! paduiga Is 40 lb.**~** 50 begs !'<If pillet lor o 1101 pallet ,..lght of 

## :zoob..,.. Allomate**PI~""** - bulk tra1ors. and owown polyl)lc>pyio•• bulk baG&. 900 lbs . 

### net. w!lh o**~** plasllc liner.**~** . . CAV!ION: Wet!IQM>tod - dopletes oxygen from' .U and,**Iller~.** ·dolngerously low lellels of**o~n** may be oncounlerod. Whenowr workoro**..-a_,..,~** lldlvaled car!xln. lhe vessel'o .._., corMnt S1'.outd be detonrined and -" proce<b9s lot potentlaly Jaw Dll)llen ateas should be f<litowod . }\pproprlale protecdve equipment shOuld be worn. AYOid inhalodon of exOMS!ve carbon cluot. No ·protllomo 1ro known lo be

. ."'sodatod In 

### handltn9 thlo momiel . 1-"'-"!r, Wilt may 

### C0f1!Ut gteater then 1.0% oilica (quw). i.<>ngwrm •· · . ' · ·• · · · ' inl\aiOiion of high cl.st cCncenor.rtions can leod to**res~** impeitment. use forced- or a dusl mas)t**'.r** _ ..,.**~n n~sary**  t or Ptotectlcn against**a~** du$ · t**~** (Soo COdt cl Federal Regulations - Title .29, # -44>. .-> SubP3rtZ.' por,1910.1000, T able Z-3),



## l ',**·**

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### VES004080

# ( ... > 

### '



### Solids R es i dence Time Calculati ons Unit4: Based on the equation e- [(0 . 1 9L)I(NDS)], where : 

# e is the residence time in minutes, L is the kiln length in feet, N is the rotational speed in revolutions per minute, 

### S is the kiln slope in feet per feet, and D i s the internal diameter in feet, ( \ and inserting the known values for L (35), N (2), S (0 . 0174), and D (6 .5) result in a

. ·• residence time f or the rotlll)' kiln of30 minutes . Units 

### 213 : S i nce these incinerators are fixed hearth units , residence time is based on the trave l length of the ash ram which functions to clear the primary combustion chamber of solid waste residue. 

### A travel length of 1 1 0 inches bas bee n determined to be the minimum 

### ash ram ·stroke length required to remove solid waste residue from the primary co mbusti on chamber oftbe fixed heartb units .

VES 004081

### .. 

## - .... 

### MACT TRAINING OUTLINE j 

### VEOLIA ENVIRONMENTAL S ERVICES - SAUG E T , IL I. ;environmenta l and Safety Requirements for. I ncineration and Material Handling 1.1 Environmental Regulations for ln cineta tion and Material H andlin & 1. 2 S af ety Regu l ations for Incineration and Material Hondling 2 . Science and Tedlnology of Incineration and Air Pollution Control

## ~ 2.1 . Combustion 

### ' 22 H eat &<change 2.3 Refractory 2. 4 Acid Gas Neutralizatiqn 2.5 Carbon Absorption 

# { ) 2 .6 Ash and Particulate Remov al 3 . Incineration and Air Pollution Control Equipment at Facility 3 . 1 Combustion Systems of No.2 and 3 Incineralo<s 3.2 Combustion System ofNo . 4 Incinerator 3.3 Air Pollution Control Equipment ofNo . 2 and 3 lncin<ntors 3.4 Air Pqllution Control Equipment ofNo. 4 Incinerato r I 3.5 InStrumentation 

### and Stack Gas Monitoring

. 3.6 Process Control an d Data Recording Systems ' .

VES 004082

### MACI 'IRAINING OtiTLINE (continued) 4. Incinerator Feed Systems 

### 4 .1 Natural Gas Buma-s 

### 4 .2 · Bulk Liquid s

## ~ 4 .3 Bulk Solids 4.4 Cootainerized Solids 

## ' 4.5 Specialty Liquids 4.6 

### Gases and Liquefied Gases 

### S. Opention ofFacility Incinerators

.5.1 Startup and Shutdown - No . 

### 2 and 3 Incinerators 5:

2 Startup 

### and Shutdown - No . 4 Incinerator 

# ) 5.3 Normal Operations 

## ' 5.4 l'rocessing Scenarios 

### 5

. 5 Main1mance and Inspection 

### 5 . 6 Troubleshooting and Response to Process Upsets


### JdrniMACftrainoutline04



### > .

VES 004083

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