( 

( .' 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECfiVE ACTIONS FOR MALFUNCflONS 

1.7.4. In case of mechanical/electrical failure of actuated valve/dlunper: 

1.7.4.1. Identify cause of actuation 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 of 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 PoDotion Control System 

1.8.1 In case o!boles due to corrosion: 

1.8.1.1. Identify location of hole. 

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 location of open port, manway, etc. 

1.8.2.2. Replace cover on open port, manway, etc. 

Page4 of26 

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!· 

VES 004000 
/ 

,:· 

\ r ' •. 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

2.0 PRIMARY COMBUSTION CHAMBER 

2.1. Loss of Natural Gas l'ressun/Fiow to l'CC Main Bllrner 

2.1.1. h1 case of plugging/physical failure ofline or line compon<mt: 

2.1. t.l. Identify the location of plugging 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/electrical failure of actllated valve: 

· 2.1.2.1. Identify cause of actuation 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 system component. 

2.1 .3.2. Service/replace control system components, as needed. 

2.1.4. In case of meobanicallelectrical failure at natural gas supply 

source: 

2.1.4.1. Identify the cause of the failure. 

2.1.4.2. Take the neceswy actions to restore the supply of 

oatur.ll gas. . 

2.2. Loss of Combutloo Air PTessoreiF!ow to l'CC 

2.2.1. In case ofmecbanicaVelectrical failure of combustion air blower: 

2.2.1.1. Diagnose blowerldrive failure. 

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 of physical failure of combustion 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 of physical/electrical failure of control 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 Buner Pilot Failure 

2.3.1. For loss of natural gas pressure/flow, see 2.1. t 

.. 2.3.2. For loss of combustion air pressure/flow, see 2.2. 

2.3.3. 1n case of physicaVelectrical failure of igniter: 

2.3.3.1. Identify cause of igniter failure. 

2.3.3.2. Service/replace igniter and/or associated c~nents, 

as needed. 

2.3.4. In case of physicaVelectrical failure of control system component: 

2.3.4.1. Identify faulty control system component. 

2.3.4.2. Service1replace control system components, as needed. 

2.4. Loss of Waste Flow to PCC Injector 

2.4.1. In case of mechanicaVelectrical failure of waste feed pwnp: 

2.4.1.1. Diagnose pump/drive failure. 

2.4.1.2. Service/replace 'the pump/drive, as needed. (!~\ .. 2.4.1.3. Restore electrical power supply to the pump . . ; ... 

2.4.2. In case oflow nitrogen pressure, see 1.4. 

2.4.3. In case of plnggingfphysical failnre of line or line component: 

2.4.3.1. Identify the location of plugging 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/confirm 'functional heat tracing, if applicable. 

2.4.4. 1n case of mechanical/electrical failure of actuated valve: 

2.4.4.1. Identify cause of actuation failure. 

2.4.4.2. Service/replace 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/replace control system components, as needed. 

25. Loss of Waste Feedrate Control to PCC Injector 

•' 

t 2.5.1. 1n case of loss of waste pressure/flow to PCC injector, see 2.4. 

Page6of26 

VES 004002 
/ 

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( '\ 

.. ...... 

,. 

· .. 

VEOLIA ENVJRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

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. IdentifY faulty control system component. 

2.5.4.2. Service/replace control system components, as needed. 

Loss of Atomization Air Piessure to a PCC Injector 

2.6.1. For a total loss of plant/instrument air Sllj)ply, sec 1.3. 

2.6.2. In case ofplugginglpbysical failuie of line or line component: 

2.6.2.1. Identify the location of plugging 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/replace 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/replace control system components, as ncoded. 

Page 7 of26 

VES 004003 
( 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCFIONS 

Z.8. Loss 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 loss of waste pressure/flow to PCC injector, see 2.4. 

2.8.3. In case of physical/electrical failure of temperature element: 

2.8.3.1. Service/replace faulty temperature element l!J:Id/Or 

associated instnnnentation, as needed. 

2.8.4. In case ofphysicallelectrical failure of control system component: 

2.8.4.1. Identify faulty control system component 

2.8.4.2. Service/replace control system components, as needed. 

Z.9. Flame Fallure 

2.9 .I. In case of pbysicallelectrical failure of flame detector. 

2.9.1.1. Identify filuhy flamedetectorcompouenl 

2.9.1.2. Service/replace flame detector compOnents, as needed. 

2.92. In case ofphysical/electrical·failure of control system component: 

2.9.2.1. Identify faulty control system component 

2.9.2.2. Service/replace control system components, as needed. 

l.lO. K.lbi Rotation Malfunction (Unit 4) 

2.1 O.l.ln case of 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 electrical power supply to motor. 

2.1 0.2. In case of physical/electrical failure of kiln rotational speed 

transmitter: Service/replace tnmsmitter and/or associated 

instrumentation, as needed. 

2.10.3.1n case of physical/electrical failure of control system component: 

2.1 0.3.1. Identify faulty control system component. 

2.1 0.3.2. Service/replace control system components, as needed. 

2.11. BallciCharge Feed Door Malluaclion 

2.11.1. In case of mecbanicallelectric.al failure of actuated door: 

2.1 1.1.1. Identify cause ofactuation failure. 

2.11.1 .2. Service/replace electrical, hydraulic, and/or pneumatic 

components, as needed. 

2.11.1.3. Service/replace actuator and/or valve components, as 

needed. 

2. 112.1n case of physical/electrical failure of control system component: 

Page 8of26 

:: 

VES 004004 
,. 

; 

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. 

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VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

2.11.2.1. Identify faulty oontrol system component. 

2.11.2.2. Service/replace control system components, as needed. 

2.12. PhysicaiiMecbauical Internal Equipment Failure 

2.12.1. In case of refractory failure, repair/replace refractory 

2.12.2. In case of ash collection failure 

2.12.2.1. Diagnose am collection system failure 

2.12.2.2. Service/replace ash collection system components, as 

needed. 

2.13. PCC Seal VIsual Emissions Monltoriag aud Recording System 

2.13.l.lo case of physical/electrical failure of camera, seTVice/n:place 

camera. 

2, 13.2. lo case of physical/electrical failwe of monitor, service/replace 

monitor. 

2.13.3.ln case of physical/electrical failure of recording system, 

service/replace recording system. 

2.14. Rapid Steam Generation from Ash CollectiOn System Water 

2.14.l.ln case of refractory failure, repair/replace refractory . 

2.14.2.ln case oflDlcontrolled movement/dropping of residue into ash 

collection sy;1em water, inspect system to identi.Jy/remove other 

suspect material. 

Page9of26 

VES 004005 
c 

VEOLIA 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 of plnggin&'J>hysical failure ofline or line component: 

3.1.1.1. IdentifY the location of plugging or line failure. 

3.1. 12. Clear line plugging and/or se.JVicelreplace faulty line 

components, as needed'. 

3.12. In case ofmechanicallelectrical failure of actuated valve: 

3. I .2.1. IdentifY cause of actuation failure. 

3.1.2.2. Servicelreplace electrical and/or pneumatic 

components, as needed. 

3.1.2.3. Service/replace actuator and/or valve components, as 

needed. 

3.1.3. In case of physicaVelectrical failure of control system component: 

3 .1.3. J. IdentifY fanlty control system component. 

3.1.3.2. Service/replace control system components, as needed. 

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. Take the necessary actions to restore the supply of 

natural gas. 

3.2. Loss of CombnstioD Air Pressure/Flow to SCC 

3.2.1. In case of mecbanicallelectrical failure of combustion 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 of physical failure combustion air duct: 

3.2.2.1. IdentifY the location of duct failure. 

3.2.2.2. Servicelreplace faulty duct, as needed. 

3.2.3. In case of mechanical/electrical failure of actuated valve: 

3.2.3.1. IdentifY cause of actuation 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 l0of26 

VES 004006 
{ 

. ( ' · . 

\ 

VEOUA ENVffiONMENTAL SERVlCES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

3.2.4, In case of physical/electrical failure of control system component: 

3.2.4.1. Identify faulty 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 of combustion air pressure/flow, see 3.2. 

3.3.3. In case of physical/electrical failure of igniter: 

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 of physical/electrical failure of control system component: 

3.3.4.1. Identify faulty control system component. 

3.3.4.2. Service/replace control system components, as needed. 

3.4. Loss of Waste Flow to SCC IDjector (Unit 4) 

3.5. 

3.4.1. In case ofmecbanical/electrical failwe of waste feed pump: 

3.4.1.1. Diagnose pump/drive failure. 

3.4.1.2. Service/replace the 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 failure 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 functional beat tracing, if applicable. 

3.4.4. In case of mechanical/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/or valve components, as 

needed. 

3.4.5. In case of physical/electrical failure of control system component: 

3.4.5.1. Identify faulty control system component 

3.4.5.2. Service/replace control system components, as needed. 

Loss of Waste Feednte Control to SCC Injector (Unit4) 

3.5.1. In case ofloss of waste pressure/flow to sec injector, see 3.4. 

Page 11 of26 

,. 

? 

VES 004007 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

3.5.2. In case of physicallelectri.cal failure of flow lnlnsmitter: 

Servic~replace flow trunsmitter and/or associated instrumentation, 

as needed. 

3.5.3. In case of actuated valve failure: 

3.5.3.1. Identify cause of acruation failure. 

3.5.3.2. Servic~repl-..ce electrical and/or pneumatic 

components, as needed. 

3.5.3.3. Service/replace actuator and/or valve 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. Servioelreplace control system components, as needed. 

3.6. Loss of Atomi2•tlon Air Pressure to a SCC bljector 

3.6.1. For a total loss of plant/instrument air supply, see 1.3. 

3.6.2. lo case of plugging/physical failure of line or line component: 

3.6.2.1. Identify the location of plugging or line failure. 

3.6.2.2. Clear 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 of SCC Temperatltre Coatrol 

3.7.1. In case of loss of natural gas pressure/llow to main burner, see 3.1. 

3.7.2. lo caseof!oss of waste pressure/flow to sec inject«, see 3.4. 

3.7.3. lo case of physical/electrical failure oftempeoature element: 

3.7.3.1. Service/replace faulty temperature element and/or 

associated inslniaientation, as needed. 

3.7.4. lo case ofphysieallelectrical failure of control system component: 

3.7.4.1. Identify faulty control systein component 

3.7.4.2. Servioelrcplace control system components, as needed. 

3.8. Flame Failllre 

3.8.1. lo case of physicallelectrical 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 of ph)'licallel.wlcal failure of control system component: 

3.8.2.1. Identify faulty control system compcmenl 

Page 12 ofl6 

VES 004008 
( .. 

: •. 

. .. 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE AC'flONS FOR MALFUNCTIONS 

. 3.S.2.2. Service/replace control system components, as needed. 

3.9. PbysiC211Mechauicallnteroal Eqoipmeot Failure 

3.9.1. In case ofn:fractory failure, repair/replace refractory. 

3.10. Low Water Level in Slag Collection System (Uolt4) 

3.10.1. For a loss of process water pressurefflow, see 1.6. 

3.10.2.ln case of physicaVmecbanical failure of level controller: 

Service/replace faulty level controller and/or associated 

components, as needed. 

3.1 0.3.ln case of physicaVmecbanical failure of actuated valve: . 

3.10.3.1. Identify cause of actuation failure. 

3.10.3.2. Service/repl.ace pnewnatic components, as needed. 

3.1 0.3.3. Service/replace actuator ami/or valve components, as 

needed. 

3.1J. Emergency Safety Veot OpelliDg 

3.11.1. Respond to an emergency safety vent opening in a manner 

consistent with the Emergency Safety Y ent Plan. 

3.11.2.ln case of mechanical failure of the al:IUator: 

3.1 1.2.1. Identify cause of actuation failure . 

3.1 1.2.2. Service/replace emergency safety vent components, as 

needed. 

3.12. Rapid Steam Generation Crom Ash Collection System Water 

2.14.1. In case of refractory failure, repair/replace refractory. 

2.14.2.ln case of uncontrolled movement/dropping of residue 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 CORRECflVE AcrJONS FOR MALFUNcrJONS 

4.0 TEMPERING CHAMBER (UNlT 4) 

4.1. Loss of Tempering Chamber E•Jt Gas Temperature Control 

4.1.1. For a loss of process water pressure/flow, see 1.6. 

4.1.2. In case of physicaVelectrical failure of flow lraDSlllitter: 

Service/replace flow transmitter and/or associated instrumentation, 

as needed. 

4.1.3. In case ofactuated 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 of physicaVelectrical failure of control system component: 

4.1.4.1. Identify 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 nozzle, 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 .. 

422. In case of plugging/physical failure of liM or line COJ!lponent: 

4.2.2.1. Identify the location of plugging 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 CORRECTIVE ACTIONS FOR MALFUNc:nONS 

5.0 LJME SLURRY SYSTEM 

5.1. Lou of Lime Feed to Ume Slarry Feed Tllllk . 

5.1.1. In case of mechanical/electrical failure of lime slurry screw feeder: 

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 of lime bin 

activator/vibrator: 

5.1.2.1. Diagnose lime bin activatorlvll>ralor failum .. 

5.1.2.2. SCfVicelrcplace the lime bin activatot'lvibrator, as 

needed. 

5.1.2.3. Restore electrical power supply to the lime slurry screw 

feeder. 

5.1.3. In case ofplugginflphysical failure ofline or line component: 

5.1.3.1. Identify the location of plugging 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 Slurry Concentration 

5.2.1. In case ofloss of lime feed to lime slurry feed tank. see 5.1 

5.2.2. In case ofloss of water flow to lime slurry feed tank, sec 1.5 

5.2.3. In case of mechanical/electrical failure of lime slurry agitator: 

5.2.3.1. Diagnose agitator/drive fallure. 

5.2.3.2. Service/replace the agitator/drive, as needed. 

5.2.3.3. Restore electrical power SUpply to the lime slurry 

agitator. 

5.2.4. In case of physicallelectrical failure of instromeotation: 

Serviceln:place faulty instrumentation, 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/replace control system components, as needed. 

Page 15 of26 

VES 004011 
c· 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

6.0 UNITS 2 AND 3 SPRAY DRYER ABSORBER (SDA) 

6.1. Loss of Lime 'Slurry Flow to SDA 

6.) .1. In case of mechanical/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 ofline or line component: 

6.1.2. I. IdentifY the location of plugging 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 of mechanical/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 system component: 

6.1.4.1. Identify faulty control system component 

6. 1.4.2. Service/replace control system componcmts, as needed. 

6.2. Loss of Lime SllllT)' 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 of actuated valve failure: 

6.2.3.1. Identify cause of actuation 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 of control system component 

6.2.4.1. Identify faulty control system component 

6.2.4.2. Service/replace control system components, as needed. 

Page J6 of26 

VES 004012 
i ' .. 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECITVE ACTIONS FOR MALFUNCTIONS 

6.3. Loss of City Water Flow to SDA (Unit 2 aad 3) 

6.3.1. In case oftotalloss of city water supply, see 1.5. 

6.3.2. In case of plugging/physical failure of line or line component: 

6.3.2.1. Identify the location of plugging or line failure. 

6.3.2.2. Clear line plugging and/or service/replace faulty line 

components, as needed. 

6.3.3. Ill case of mechanicaVe ~cal failure of actwted valve: 

6.3.3.1. 

6.3.3.2. 

Identify cause of actuation failure. 

Service/replace electrical and/or 

components, as needed. 

pneumatic 

6.3.3.3. Service/replace actll3tor and/or valve components, as 

needed. 

6.4. Loss of CooHng Air Flow to 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 blowerldrive, as needed. 

6.4.1.3. Restore electrical power supply to the blower. 

6.4.2. In case· of physical failure of atomizer cooling air duct 

6.4.2.1. Identify the location of duct fail'are. 

6.4.2.2. Service/replace faulty duct, as needed. 

6.4.3. In case ofphysicaVelectrical failure of control system cornpone.ut: 

6.4.3.1. Identify faulty control system component. 

6.4.3.2. Service/replace control system components, as needed. 

6.5. Loss of SDA E:dt Gas Tempenature Control 

6.5.1. In case of loss 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 of actuated valve failure: 

6.5.3.1. Identify cause of actuation failure. 

6.5.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

6.5.3.3. Service/replace actuator and/or valve components, as 

needed. 

65.4. In case ofp~ysicaVelectrical failure of control system component: 

Page 17 of26 

,. 

VES 004013 
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( 

VEOLIA ENVIRONMENTAL SERVICES, INC 

PROGRAM OF CORRECTIVE ACflONS FOR MALFUNCTIONS 

6.5.4.1. Identify faulty control system component. 

6.5.4.2. SCJVice/replate control system components, as needed. 

6.6. Atomizer Fame 

6.6. I . ln case of low 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 of mecbanical/electrical failure of atomizer: 

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 
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c· 

( 

VES 004015 
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1' .. 

VES 004016 
c 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCIIONS 

7.0 UNIT 4 SPRAY DRYER AllSORBER (SDA) 

7.1. Loss of Lime Shlrry Flow to SDA 

7 .1.1 . In case of mechanical/electrical failure of lime slurry feed pump: 

7.1.1.1. Diagnose pump/drive failure. 

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 of line or line component: 

7 .1.2.1. IdentifY the location of plugging 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, if applicable. 

7. 1.3. In case of mechanical/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 of physical/electrical failure of control system component: 

7 .1.4.1. Identify fauhy control system component 

1.1.42. Service/replace control system components, as needed. 

7.2. Loss of Lime Slurry Flow Controi/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 failure of flow transmitter: 

Service/replace flow transmitter and/or associated instrumentation, 

as needed. 

7 2.3. In case of actuated valve failure: 

7.2.3. L Identify cause of actuation failure. 

7.2.32. Service/replace electrical aod/or pneumatic 

components, as needed. 

7.2.3.3. Service/replace actuator and/or valve components, as 

needed. 

7.2.4. In case of physical/electrical failure of control system component: 

12.~. . Identify faulty control system component 

7.2.42. Service/replace control system· components, as needed. 

Page 19 of26 

VES 004017 
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VEOLIA VIYlRONMENTAL SERVICES, INC. 

PROGRAM OF CORREC11VE ACJ10NS FOR MALFUNCI'JONS 

7 .3. Loss of Atomizatloo Al.r Pressure to SDA Nozzle 

7.3.1. For a total loss of plant/instrument air supply, see 1.3. 

7 .3.2. Iu case of plugging/physical failure ofline or line component: 

7 .3 .. 2.1. Identify lhe location of plugging or line failure. 

7.3.2.2. Clear line plugging and/or service/replace faulty line 

components, as needed. 

Pago 20of26 

i 

" 

VES 004018 
'· 

VEOLJA ENVIRONMENTAL SERVICES, JNC. 

PROGRAM OF CORRECfJVE AC110NS FOR MALFUNCfJONS 

8.0 CARBON INJECTION SYSTEM (UNJT 4) 

8.1. Loss of Carner Gas Pressure 

8.1.1. In case of mechanical/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 of duct failure. 

8.1.2.2. Service/replace faulty duct, as needed. 

8.1.3. In case of physicaVeledrical tiulure of control system component: 

8.1.3.1. Identify faulty control system component. 

8.1.3.2. Sc:rvicelreplace control system components, as needed. 

8.2. Loss/Restrictlcra of Activated Ca.rbon Flow 

8.2.1. In case ofloss of plaot 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 ofpluggingfpbysical failure of linC or tiJle compoJ\C1ll: 

8.2.3.1. Identiiy the loc:alion of plugging 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. For a total loss ofplanlf'mstrument air supply, see 1.3. 

8.3:2. In a.~e of plugging/physical fmlure ofline or line component: 

8.3.2.1. Identify tbc location of plugging or line failure. 

8.3.2.2. Clear tiJle plugging and/or service/replace faulty tiJle 

componentS, as needed. 

8.3.3. In case ofmechanicaVelectrical failure of aclllated valve: 

8.3.3.1. ldentify cause of actuation failure. 

8.3.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

Page 21 of26 

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VES 004019 
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1... ... 

VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCDONS 

8.3.3.3. Service/replace 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 
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VEOUA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

9.0 BAGHOUSE & INDUCED DRAFf (ID) FAN 

9.1. Torn/Leaking Bag 

9.1.1. 1n case of a bagbouse leak detection alarm, follow the relevant 

corrective measures prescnl>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 bag(s), as needed. 

9.1.2.2. Diagoose the failure of the 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.re Drop 

9.2.1. 1n case oflow baghouse inlet gas temperature: 

9.2.1.1. Follow the appropriate corrective actions prescribed by 

parngrnph 6.S (Unit 2 and 3) 

9.2.1.2. Follow the appropriate corrective actions prescribed by 

p11111graph 7.2 (Unit 4) 

9.2.1.3. Perform bagbouse inspection. 

9.2.1.4. Service/replace bag(s), as needed. 

9.3. Loss ofSbck Gas Flowrate Cutrol (Unit 2 ud 3} 

93,1. In case of lD fan failure, see 9.5 

93.2. In case of physical/electrical failure of flow transmitter: 

Service/replace flow transmitter and/or 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 of physical/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 Damper Malfuclioo (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 MALFUNCTIONS 

9.4.1.1. IdentifY cause of actuation failure. 

9.4.1.2. Service/replace electrical and/or pneumatic 

components, as needed. 

9.4.1.3. Service/replace actuator and/or damper components, as 

needed. 

9.4.2. ln case of physical/electrical failure of control 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 of mechanical/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 24 of 26 

VES 004022 
I 

VEOLJA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACI10NS FOR MALFUNCI10NS 

10.0 CONTROL SYSTEM/CONTINUOUS MONJTORlNG SYSTEM 

10.1. Control SystemfConlinuous Monitoring System Malfunction 

10.1.1. As needed, refer to the CMS QAIQC Plan for guidance and to 

ensure 1bat proper calibrations are perfonned: 

10.1.2. In case of physicaVelectrical frulure of instrumentation: 

I 0.1.2.1. Identify faulty instrumentation component. 

10.1.2.2. Service/replace faulty instrumentation components, as 

needed. 

1 0.1.3. In case of physical/electrical failure of control system component: 

10.1.3.1. Identify faulty control system component 

1 0.1.3.2. Service/replace control system components, as needed. 

10.1.4. 1n case ofphysicaVelectrical failure of data acquisition/availability: 

10.1.4.1. Identify faulty data sysleD1 components. 

10.1.4.2. Service/replace data system components, as needed. 

1 0.2. COBtiDuous Emissions Monitoring System Malfunctioll 

10.2.1. As needed, refer to the CEMS QAIQC Plan for guidance and to 

ensure that proper calibrations are perfonned and 1bat the 

appropriate performance specifications are mel 

10.2.2.1n case of physical/electrical failure umbilical 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 of heated vacuum pump: 

I 0.2.3.1. Diagnose pmnp!drive failure. 

1 0.2.3.2. Service/replace 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 

pump. 

1 0.2.4. In case of plugging/physical failure of sample probe/umbilical: 

10.1.4.1. Identify the location of failure. 

10.1.4.2. Clear plugging and/or service/replace faulty 

components, as needed. 

10.2.5. In case of mechanical/electrical failure ofactuated valve: 

1 0.2.5.1. Identify cause of aclllation failure. 

Page25 of 26 

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VES 004023 
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VEOUA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECflVE ACI'JONS FOR MALFUNCI'IONS 

I 0.2.5.2. 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 of mechanical/electrical failure of 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 of physicaVelectrical failure of control 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 VENT PLAN 

Prepared for: 

Veolia ES Technical Solutions, LLC 

Sauget, IDinois 

Prepartd by: 

Franklin Engineering Group, Inc. 

Franlclin, 'fennessee 

October 2008 

VES 004025 
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c· 

TABLE OF CONTENTS 

1.0 INTRODUCHON AND BACKGROUND -·····--·-............ ---··-·--..... 1 

1.1 SUMMARY OF FACiliTY INFORMATION ............................. : .................. : ........ ! 

1.1.1 rued Hearth Incinerators ............................................................... ] 

1.1.2 Rotary Kiln lncinerator .................................................................... 3 

1.2 DEsCRIPTION OP 1liE ESV SYsmM ............................................................. .4 

2.0 ESV SYSTEM INVESTIGATION, DOCUMENTATION 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 PROCEDURES DURING AN ESV ..... - ................. - ................................ - ... - 9 

3.1 STOPPING W AS1ll FEED AND SH\1111NG DoWN 1liE COMBUSTOR ................ 9 

3.2 MAINTAINING COMBUSTION CHAMBER Ti!MPERA nJRll. ............................... 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..A TORY REQUIREMENTS FOR AN EMERGI!NCY SAFETY VENT 

0P.ERA TING PLAN AND CORlUlSIONDJNG 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 V eot (ESV) systems, 

and procedures that will be followed 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 of the three 

systems will be clearly identified. 

1.1 Summary of Facility Information 

Brief Sllllliilaries which describe the fixed hearth incinerators and the rotary kiln 

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 
( 

( ' 

( 

Table 1-1 

Regulatory Requirements !or Emer&ency Safety Vent OpenliD& PIID 

a11d Correspo11diog Section tllat Addresses tbe Requirement 

Regulatory Descripdou Plan Sectioo Citatiou 

Documentation in operating record of an 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 if opemtioo remained in 

compllimce considering the emissions during 

theESV 

InfOimation documenting effectiveness of plan's 

63.1206(c)(4)(ii)(B) procedures to maintain combustion chamber Section 3.5 

temperature and pressure, as is reasonably feasible 

63.1206(c)(4)(ii)(B) Detailed pcoced.ures for rapidly stopping waste feed Section 3,1 

63.1206(c)(4)(ii)(B) Detailed procedures for shutting down the 

Section3.4 combustor 

63.1206(c)(4)(ii)(B) Detailed procedures for maintaining temperature in 

Section 3.2 combustion chamber 

63.1206(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 of ESV openings Section 2.2 

63.1206(c)(4)(iv) Reporting of ESV 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 wastes and gaseous feedstreams are thermally treated in the 

fixed hearth incinerators. Solid W83tc is fed to the primary (lower) 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 pr0vide particulate mallet' 

removal. 1be induced draft fan, located t;lownstrcam of the baghouses, moves the 

combustion gas through the sy&em and exhausts 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 fired to a dedicated burner in both the primary and secondary chambers. 

Combustion gas exits the secondary combustion chamber and enters 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 Description of the ESV System 

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 

TRV allows hot combustion gas to vent from the combustion system during emergency 

shutdown events. The purpose of the TRV is 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 present. Alarms 

provide the operator the opportunity to 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 
/ ' Table 1-2 

Tberma1 Relief' Vent Openings 

Parameter Co.ditloa 

1 

Ele<:trical Supply LossofPow" •· 

Air Supply 

Loss of Air Pressure 

(TRV will fail 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 design 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 of start-up, 

shutdown and malfunction is provided in the faciliJy Start-up, Shutduwn, Malfoncticn 

Plan (SSMP). 

6 

VES 004033 
c 

2.0 ESV SYSTEM INVESTIGATION, DOCUMENTATION AND 

REPORTING 

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 cut of!; 

2) lf possible, operate the ID fan, and 

3) lf possible, maintain normal combustion chamber temperatures on na111ral ps. 

lf hazardous 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 of ESV OpenJag 

Each instance in which the emergency 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. 

lf the 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 SSMP), 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 004034 
i 

2.3 ReportiDg of ESV Opening.~ 

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

V eolia wi.ll submit a written ~rt within five days of the ESV event to Dlinois 

Environmental Protection Agency (IEPA), documenting the results 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 004035 
I ' • 

( .. . 

\ 

·. 

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 hazardous waste 

retention time, shutting down the combustor (allowing key components to cool) is 

equally important These items are addressed below. 

3.1 Stopping Waste Feed aad Sbuttlag Down the Combustor 

An ESV opening is likely to be preceded by a A WFCO or safety interlock that causes a 

waste feed cutoff prior to the ESV opening. The ESV position is also interlocked with 

the A WFCO 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 Maintailliog Combustion Ch amber Temperature 

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 of waste ro:naining in the incinerator. 

3.3 MainWaing Negative Combustloa Cllamber 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 oxtcnt 

that is reasonably feasible. II is likely that the opening of the TRV will cause the B}'ltem 

to lose negative pressure (i.e. the ID fan cannot induce a strong draft). For surge vent' 

opening. the positive 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 the 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. If the ESV opening corresponds with a malfunction 

9 

' ' r 

VES 004036 
( 

( . . . . 

event thc:o the COJTective measures taken will be consistent with the procedures 

prescnoed by the SSMP. 

3.5 Documentation of O>mbusrioo Cbamber Pressure and Temperature 

Matateaaoce 

§ 63.1206(cX4)(iiXB) requires that the facility demoilstrate that the procedures of this 

plan are adequate to maintain combustion chamber pressure and temperature while 

hazardous waste remains in the incinerator, if feasible. The occurrence of 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 chamber 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· 

OPERATION AND MAINTENANCE PLAN 

Prepared for: 

Veolia ES Technical Solutions, LLC 

Sauget, lllinois 

' Prepared by: 

Franklin Engineering Group, Inc. 

Franldin, Tennessee 

October 2008 

;. 

' 

.. 

,. 

~ .. 

VES 004038 
TABLE OF CONTENTS 

1.0 INTRODUCTION ..................................................... _. __ , ............ _ ..................... l 

).1 "R!!GIJLATORY REQUJIUlMllNTS .......................... ............................................ 2 

1.2 RECORD KEEPING ........................................................................................... 2 

2.0 NORMAL OPERATIONS OF THE INCINERATORS .................................... 2 

3.0 BAG. LEAK DETECflON SYSTEM ............ - ................................................ ..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:TANI>-BY MODI! OF0PER.A110N .................................................... l2 

5.2 Al'PUCABll!REQUIIUlMENTS ...................................................................... l 3 

( ..... , 

. 

( 

VES 004039 
) 

USTOFTABLES 

TABLE 1-1 OPERATION A'ND MAINTh"NANCil PLAN REouLA TORY Cll:ECKUST .............. 1 

TABLE2-I IJSTOFSTANDARDDIVJSJONALPRAC11CES ................................................ 3 . 

TABLE 3-I BAG/lOUSE l...EAK DBlllCTJON SYS11!M SPECIFICATIONS ..................•........... 6 . 

T Alli.E 4-I lNsPBCilON AND MAINTENANCE TO !'REVBNT MALFUNCilONS.: .....•......... I 0 

ii 

VES004040 
l 

( 

1.0 lNTRODUCI'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 Achievable Control Technologies (MACT), 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 malfunction, 

Veolia ..;;il utilize tbe Startup, Shutdown, and Malfunction Plan (SSMJ>). During periods 

of startup, shutdown, and malfunction, conformance with the SSMP satisfies the duty to 

minimize emissions. Both the O&M plan and SSMP are maintained at tbe facility. 

The purpose of this O&M plan is to: 

• Describe procedures for operating tbe incinerator during nom~ operations. 

• Descnbe procedures for inspection and maintenance of the incinerator. 

• Describe procedures for coJTeetive measures. 

• Establish guidelines designed to ensure that emissions of pollutants, automatic 

waste feed cutoffs (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 of the tbrcc incinerator systems, general references 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 location within this document where each 

requirement is addressed. This table is included to facilitate the expeditious assessment 

of this 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 maintained 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 adjustments and maintenance perfonned on the continuous 

monitoring system (CMS). 

2 

'· 

VES 004042 
Table 1-1 

( Operation aud MaiDteoa.nce Plan Regulatory Cbecldist 

Regulatory Citation Description 

63.6(e)(l)(i) Implement safety and good air poUution control 

practices for minimizing emissions 

63.6(e)(l )(ii) Comply with SSMP and minnnize emissions during 

SSM 

63.6(e)(1)(iii) O&M requimnents CSlablisbcd pursuant to section 

112 of tbe CAA 

63.6(e)(3) Startup, shutdown, and malfuottioo plan 

63.10(b)(l) Maintaining files 

63.1 O(b )(2)(iii) Records of all 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 

63.1206(c)(7)(i)(A) Procedures for opemting combustion system 

components that could affect emissioDS 

63.1206(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 for combustion system 

components that could affect emissions 

63.1206(c)(7)(i)(B) 

Good air pollution control practices for minimizing 

emissions 

63.1206(c)(7)(i)(C) .O&M plan eilsurcs.compl.iance with O&M 

requ.irerncnts of63.6(c) 

63.1206(c)(7)(i)(C) O&M plan minimi1.es emissions of pollutants 

63. I 206( c)(7)(i)(C) O&M plan minimizes A WFCOs 

63. 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, 

SSMP1 

1.0; 2.0 

1.0 

1.0, 2.0 

1.0, 2.0 

1.0, 4.0 

Table4-1 

1.2 

f 

f: 

-

' 

., 

VES 004043 
Table 1-l (continued) 

OpeYalion and Maintenance Plan Regulatory Cbecklist 

Regelatory CitatioD Description 

Locatiota 

Addressed 

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 

63.1206(c)(7)(ii)(A)(4) Comply wilh US EPA guid~ or mannfactma's 

3.0 infonnation for installation and opaation 

63.1206( c )(7)(ii)(A )(5) Initial adjustments of the system: baseline, averagiog 3.0 period, alarm set point and delay time 

63.1206(c)(7)(ii)(A)(6) O&M plan specifies aUowable ad.iustments 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 detection 

3.1 

system alaon 

63.1206{c)(7)(ii)(B)(l) Initiation of procedures 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 NORMAL OPERATIONS OF THE INCINERATORS 

Table 2-1 presents a list of titles for Veolia's Standard Divisional 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, if possible. Operating the incinerator in this manner will minimize the 

occurrence of A WFCOs and minimize the emissions of hazardous 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 applicable. 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 the understanding of alarms, interlocks, as well as the 

automated responses associated with each interlock. Knowledge of alarms and interlocks 

and access to process 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 malfunction, 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 Standard Divisional Practiees 

SDPNUMBER TITLE 

lOll TWI Remedial Action W o:dt Order Program 

2200 Specialty Feeder Operation for No. 2/3 Incinerators 

2201 Startup, Operation and Shutdown of No. 2/3 Incinerators 

2202 Operation of Compressed Gas Cylinder Feeding System 

2203 Operation of Solids Feed Conveyor Systems for No. 2/31ncinerators 

2204 Ash Conveyor Operation for No. 2/3 Inci.neratoiS 

2205 Operation of Liquid Feed InjectoiS for No. 2/3 Incinerators 

2206 No. 2/3 Incinerators Legs Cleanout 

2207 No. 2 Incinerator Upper Chamber Feed System 

( 220& No. 2/3 Incinerators Shutdown Permits, Tagouts and Lockouts 

2209 Operation ofBaghouse Filters for No. 2!3 1ncinerators 

2210 Operation of Compressed Air System for No. 213 JncineratoiS 

2211 Lime Slurry System Operation for No. 2 and 3 Incinerators 

2212 Spray Dryer Absorber Operation for No. 2/31ncine~tors 

2213 Operation of Dry Saubber Solids Conveyor Systems for No. 2/3 Incinerators 

2214 Flushing the Lime Slurry System for No. 2/3 Incinerators 

2215 Operation of Oxygen Gas Cylinder Processing System 

2217 Operation of Specialty Feeder Fwne Hood System for No. 3 Incinerator 

.. 

3 

VES 004046 
\. Table 2-1 (continued) 

List of Standard J)lvisioDal Practices 

SDPNUMBER TITLE 

2219 Lime Storage Loading 

2221 24-Hour Staging of Burnable 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 Slurry System for No. 41ncinerator 

2406 Operation of Liquid Feed ·!Qjectors for No. 4 Incinerator 

2407 Cleaning the Process Water System for No. 4 locinentor 

2408 Operntion of Carbon lnjo:ctioo System for No. 4Jncinerator . . 2416 Lime Sluny System Operation for No. 4 Incinerator 

2417 Start1lp, Operation and Shutdown of No.4 Incinerator 

2418 Spray Dryer Absorber Operation for No. 4Incinerator 

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 DETECTION SYSTEM 

Veolia utilizes a triboelectric bag leak detector to comply with tlte bag leak detection 

requirements 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 duct downstream of the induced draft fan. The bag lealc 

detection system has been certified from manufacturer 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 A WFCO system. The delay times for the alanos 

are based on tbe normal bag cleaning pulse cycles. The bag leak detection system 

settings arc presented in Table 3-1. 

Following initial adjustments (including 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 adjustments made 

consistent with recommendations in Section 5.3 of the US EPA Fabric Filter Bag Leak 

Detection Guidance (EP A-454/R-98-01 5). Periodic adjustments to the bag leak 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 I 00 percent or decreased by 

more than 50 percent, a complete baghouse inspection and necessary repairs will be 

pc:rfonned to assure good operating condition. 

s 

r 

VES 004048 
Table 3-1 

Baghouse Leak Detedioa System Specif"Jcations 

Parameter Unit 2 Unit 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% 

High Alarm Delay Time 3minutes 3 minutes 6minutes 

High-Higb Alann (A WFCO) 30% 300/o 15% 

High-High Alarm Delay Time 6.minutes 6minutes 12 minutes 

\ 

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6 

VES 004049 
( 

( " 

3.1 Corrective Measures for Beg Leak Detection Alarms 

Veolia has implemented the necessary proactive measures to preventhninimize the 

occurrence of bag leak detection al:ums. These proactive measures include im;pections 

and preventive maintenance of the baghouse and the bag leak detection system. 

Additionally, the installation and operation of the bag lealc detection 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 of the 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 will be initiated within 30 

minutes of the time the alarm first sounds. The time and cause of each alsrm will be 

recorded 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 matter loading: 

3.1.1.1 Review process 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 If relative particulate matter loading remains above the high 

alarm set point, take ·actions to reduce the relative particulate 

matter loading (e.g., controll~ 'shutdown of high ash waste 

feeds). 

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 of reoccurring false bag lealc detection alarms: 

3.1.2.1 Clean the bag Jealc detection system probe, and/or adjust the 

sensitivity (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 lo.ading: 

3.1.3.1 Initiate a controlled shutdown of waste feeds. 

3.1.3.2 lnspect bagbouse for leaks, tom or broken filter elements, or 

other internal equipment failures; and repair as needed. 

3.1.3.3 Following inspectioolrepair of bagbouse, clean the bag leak 

detection system probe, and/or adjust the sensitivity {range), 

averaging 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 sysl.em. 

a 

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; 

.· 

VES 004051 
l. 

c· 

4.0 INSPECTION AND MAINTENANCE 

As stated in Sections 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 daily and in accordance with the inspection schedule, contained 

in Appendix 6 of the approved ~t application". Veolia utilizes these inspections and 

additional preventive maintenance activities as proactive measures 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)' 

of the 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 replaced based on the schedules 

indicated on these checldists. These field cbecldists will also be used to document repairs 

or replacements 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 Action Work Order Program-ensures that these non-routine maintenance 

activities are given the appropriate priority and are tracked through completion. Brief 

procedures/instructions for inspection and maintenance activities are provided on field 

checklists. Addition details and procedures for inspection and niaintenancc activities are 

communicated through the following: 

• SDPs for specific process maintenanee procedures (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 affiliated with an equipment manufucturerlvendor. Veolia will include 

documentation of these activities in the operating record. 

Inspection and maintenance requirements are also addressed in other plans required by 

the Interim HWC MACf Standard. Inspection and testing of the A WFCO system are 

described in the Automatic Wa:~te Peed Cutoff Plan.. Inspection. calibration, and . 

po-eventive maintmanoe for the continuous emissions monitoiing systan (CEMS) are 

discussed the CcntUruous Emi.uions Monitoring System Quality A.ssuranCll Plan. 

Discussion on calibration and maintenance for the continuous monitoring system (CMS) 

is prnsented in the Ccntii'IUOJIS Monitoring Synem Quality As.rurance Program. 

9 

.. 

VES 004052 
Table4-l 

I.ospec:tioo aod M.alotenaoce to Pnveot Malfunctions 

l'oteutlal Cause for lospectioos Malo.te.aauce Malfunclioo 

• Cleaning 

• Tigliteoing fasteners and 

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

Mecbanicallelectrical • Lubrication 

• Instnnnentation and alarms for failure of rotating • Alignment current, lubrication, and/or cquipmenL vibration on selected rotating • Scheduled n!ploccment of 

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 of instrument 

air and electrical comections • Cleaning MecbanicaVelectrical 

• Confirmation of fail-safe • Lubrication failure of actuated positious during shutdowns valves/dampers • AF.needed 

• Confirmation of functionality repairs/replacements 

through process variable 

control/indication 

• A WFCO Testing 

•, 

10 

VES 004053 
( 

Table 4-1 (contiDUed) 

Inspection u d Mal•te.auee to Prevent Malfunctio•s 

Pototlal Calise for Jnspedioos Mabateoance Malluoctioo 

• Process variable 

Physical/electrical controlfmdicatioo • Cleaning 

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 of valve fail-safe 

.EleclricaVactuation positions during shutdowns 

• As needed failu.n: of safety • Verification of alarms and repairs/replacements interlocks interlocks during A WFCO 

( '· Testing 

• Internal clcaoing • Daily exterior inspections for Pbysicallmechanical leaks, coaosion, and vibration • Tightening fasteners and 

intemal equipment Interior inspections during supports 

failure • 

shutdowns • As needed 

repairslreplaccm.e:nts 

' '. 

II 

VES 004054 
i 

' 

( . . .' 

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 nonnal 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 

operations; however, a cold shutdown is not required to complete these activities. For 

this reason, V eolia bas defined an alternative mode of operation during which these 

activities can be perfgnned. This mode of operation 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 of operation. 

5.1 Warm Stand-by Mode of Operation 

The wann siand-by mode of operation is utilized to perform inspections and maintenance 

activities that do not warrant a complete cold shutdown. During this mode of operation 

the combustion chamber temperatures are maintained 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 Applicable Reqniremeats 

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 of operation requirements in§ 63.1209{q) 

• NotifiCation, reporting, and recordkeeping requirements of §§ 63.1210 through 

63.1212 

Per the requirement of 63.1206(b)(ii), Ibis section supplies documentation in the 

operating record that V eolia is complying with all "otherwise applieable requirements" 

during warm stand-by mode of operation. Requirements conStitute "otherwise applicable 

requirements" to the extent that they do not arise from Subpart BEE and they are 

otherwise applicable to any of the 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 

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

13 

VES 004056 
( 

FEEDSTREAM ANALYSIS PLAN 

Veolia ES Technical Services, LLC 

Sauget, Illinois 

October 2008 

VES 004057 
( 

( "· 

Feedstream Analysis Plan- October 2008 

TABLE OF CONTENTS 

1.0 INTRODUCTION 

2.0 FEEDSTIU:AM PARAMETERS 

2.1 Chlorine 

2.2 Metals 

2.3 Ash 

3.0 ANALYTICALRATIONA.LE 

3.1 Analysis Pecfon:nod by Vco1ia 

3.2 Analysis Performed by Others 

3.3 Manufacturer Data or Other Published Jnfonnation 

4.0 APPLICATION OF ANALYSIS FOR FEEDRATE COMPUANCE 

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 METHODS 

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 V eolia can sample, 

analyze, and control the incineration of feedstreams 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 of the subieqneot sections specifically addresses 

the six parafppbs under40 CFR63.1206 (c) (2) and three paragraphs under40 CFR 

63.1206 (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 (W AP). The 

W AP is an integral part of the 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 of it (or related documents), 

coofidential business information entitled to protection from disclosure will be clearly 

designated. 

2.0 FEEDSTREAM 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, Cbromimn, Beryllium, and Aisenic) 

3) Ash 

These three constituents will serve as the feedstream parameters of concern in the FAP as 

required by40 CFR63.1206 (c) (2) (l) ofthe HWCMACT Standard. Feedstream data 

applicable to each of these 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 feed rate values 

and control actual feed rates during incineration. 

2 

' r. 

VES 004059 
( 

\ 

' ( .. ' 

Feedstream Analysis Plan - October 2008 

2.2 · Metals 

Feedstream data will provide a parts-per-million concentration for each of the listed 

metals in each of the 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 estimate targeted feed 

rate values and control actual feed rates dllring incineration. · 

2.3 Ash 

Feedstrcam dala will provide a weight-based percentage of ash for eaeh of the waste 

feeds to the incinerators. These results can be used to both estimate targeted feed rate 

values and control actual feed rates during incineration. 

3.0 ANALYilCAL RATIONALE 

In40 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 regulations. There 

are three sources of analytical information 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 data 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 feedstreams are extensively addressed. Many of the analytical procedures 

perfonned as descn'bed in the F AP are also required as part of the 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 those that undergo subsequent blending prior to incineration, and also 

to wastes that are generated at the facility. 

3.1 Analysis Performed by V eolb 

The predominate means applicable to this source of analytical infol!Dation is the 

methodology descn'bed in Section 5.0 of the FAP. Specific analytical methods performed 

in tbt Jilcility' s laboratory are applied to aJli>li<:able feedstreams to produce values for 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 supplemental 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 of the fcedstreams. 

In other instances, the feedslreams are wastes 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 analytical 

methods described in the previous paragraph or by statistically arriving at au average 

valne based on a body of previously analyzed sainples. Wastes generated by the facility 

will have parameters detennined from au average value based on a body of previously 

analyzed samples. 

For many feedstreams, the best soW'Ce of information for the parameters ide.ntified in the 

F AP wiU be obtained using the tecbnical expertise ofV 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 of this F AP is available, V eolia will accept the 

analysis of others in detennining parameter values. This analytical information wiD be 

evaluated and used to control the incineration of feedstreams 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 F AP. 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 of these reference sources in . 

Appendix W AP-F. Examples of these 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 analytical 

information produced at the facility. 

4.0 APPLICATION OF ANALYSIS FOR FE:EDRATE ~OMPLIANCE 

Feedstream 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 documentation of these feedrate compliance methods is required by 40 

CFR 63.1206 (c) (2) (iii) oftbe HWC MACT Standard and outlined in this section of the 

PAP. 

4 

VES 004061 
( 

Feedstream Analysis Plan- October 2008 

Analytical results can be used to both estimate 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 Feedstnams 

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 of feed preparation is 

necessary. This step in the feedstream evaluation process is called process planning; It is 

applied to blending wastes, processing wastes into combustible 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 Control for Feedstreams 

ln order to ensure that feedrate limits for the parameters in the F AP are not exceeded 

during operation of the 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 Control 

Documentation ofproeess planning and control is demonstrated by the extensive body of 

infonnation coUected in the facility's data management system, and, if needed, 

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 of the facility. 

5.0 SAMPLING AND ANALYTICAL METHODS 

The requirerQents in 40 CFR 63.1206 (c) (2) (iv) and (v) of the HWC MACT Standard 

state that a facility must 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 is 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 Samplblg Metlaodologies 

Sampling is performed at the V eolia facility to identify waste shipments and 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 V eolia will have detenniued that sufficient documentation already 

exists that 'identifies information regarding the parameters desaibed in Section 2.0 of the 

FAJ> (see also Section 4.0, Paragraph 4.1.12 (2) of the WAJ>).lo order to obtain a 

representative sample of the waste, specific samjlling procedures that are depc:odent on 

both the nature of the waste sampled and the typo of processes in which the waste will be 

stored or transferred must be performed. Section 2.0 of the facility's W AJ> and pertinent 

appendices in the W AJ> 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 ~ of inteoded containment or proccsscs tlaat can 

impact the sampliog. and guidetincs on bow to ensure that a valid and representative 

sample is oblaincd. 

5.2 Doc11mentalion and Rccordkeeplug Assoclated witb Sampliag 

All samples taken at the facility or sent to the facility for analysis are assigned a lllrique 

sample identification 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 Analy1ltal Metbodolocies 

CHLORINE 

The analytical procedures and EPA approved'mcthods related to determining the amount 

of chlorine in a feed.stream are found in Appendix WAJ>-A to the facility's WAP. 

METALS 

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 listed below. 

Digestion Procedure for Non-Water-Soluble Sample.~ 

Method 305 lA - Microwave Assisted Acid Digestion of Sediments, Sludges, Soils, and 

Oils 

6 

VES 004063 
( 

· .. 

Feedstream Analysis Plan - October 2008 

Proeeclurn for De!mnjning Concentration of Mercury in Sample 

Method 7473 - Mercury in Solids and Solutions by Thennal Decomposition, 

Amalgamation, and Atomic Absorption Spectrophotometiy 

Procedure for Qe!mpjning Concquration of Arsenic. Bervlli!Dll. Cadmi!Dll. Chromjum 

and Lead in Sample 

Method 6010C - Inductively Coupled Plasma-Atomic Emission Spectrometry 

ASH 

The analytical procedures and EPA approved methods related to determining the amoliD.I 

of ash ina feedstream arefolllld in Appendix WAP-Ato the faci.lity's WAP. 

5.4 Documentation and RecordkeepiDg Associated with Sample Analysis 

Documentation of analytical wodc is accomplished by recordiDg it iD laboratory 

logbooks, entering it into the facility's dala management system, and, if needed, 

distn'buted in hard copy form to appropriate personnel. All technical files for waste 

profiles will also include initial laboratory analysis imd any applicable subsequent 

analysis. This information will be retained in the operating record f0r ·the life of the 

facility. 

6.0 FREQUENCY OF ANALYSIS 

In 40 CFR. 63.1206 (c) (2) (vi) of the HWC MACf Standard, a facility is required to 

identify the frequency with which an initial analysis is repeated or reviewed to ensure that 

· it is cum:nt. This F AP wiD require that the analytical information for the feedstreams be 

re-evaluated on a Ji:equency consistent with that descn'bed for aU wastes as described in 

Section 4.1.3 of the facility's W AP. The three events that may trigger a need to update or 

evaluate the analysis of a given feedstream are: 

I) Generator notifies V eolia that a feedstream bas changed 

2) Subsequent analysis for a feedstream used by Veolia is inconsistent with the original 

analysis 

3) Five years have passed since the last assessment of the feedstream 

In order for a feedstream to be considered acceptable again for incineration 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 employs process control systems for the incinerators that monitor, adjust and 

record feedstreams and the key parameters identified in the F AP that are associated with 

1 

VES 004064 
(' 

'· 

•.. 

Feedslream Analysis Plan- October 2008 

than. These systems meet the reqllircments of 40 CFR 63.1206 (c) (4), paragraphs (i), (ii) 

and (iii). The·systems and the rationale that supports these systems are descn'bed in the 

following paragraph. 

7.1 Feed Rate Compliance Systems and Methodology 

A1\er the metals and ash coMentratiODS fo~ feedstreams axe detenniued, they will be 

en1ered into the facility's data management 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 15 second intervals for each ~fie waste 

sttam entering the incinerator, computations are being pcrf01med 10 caJculatc the 

quantities of metals (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 
....... ' .. 

. . .. ' 

··· ... 

r·; ,. . 

. . . . . . . ·-· . .. . . ... . : .. •: .. -- ·... .... ._':-'·.: ' . : __;· . . . . . . . . ·.-.. ·:, ... -; :· ;;~,; _.,,:, ...... .. :- ·;.,::·.: ·.--·.; ;· :,_ .. ~ ··.. . ~:- · .. ·· . . 

JRCAA Tft&t . ·~ .... ·':•:-~; ;,[_: >: .": ,,_;:::.:",. ··:~' :;•.--- 1-'\ -

.~·· ... .. ' \ .· I• .•.•.> . :- ... · .. --':. 

"v; ...... -~·'· 

, .. , . . _;. I· ' ' _., ,d .... ' '"··:':' ... ·.,.;, :-· .· 

Unit 2 .: .. • .• :·.> •. : ,,. · ,_,. ' .. '. ..·.-·: : .. ' -. •. 

.. ; I ISS. c:•.· ·,,·,;_ ·" -' 

.,. _ 

I ' RIInl 1 ... •2 '. Run3 Run4 

-'- ._,_ :..'._{._;._ . ;:' ..... :·· "·:--. ' .. .. ...... . 

lORE . ,,, :. ·.· '· .. _ . 

' . 

.. 

. :. . . 

: Caibiln 

·; 

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·: 

. ' 

1,2, 

·;--:'' ... ···•· ~ ..... : . ·': 

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r . .-

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· .. :-·. 

: 

.. ... , ... -1 ' . · ... ~ ~ ~ ·' ... --· . 9.51 .-· v . .. · ~ . ' lll ,., . >··; .,..- .•· . ; ::· .,, .:· ' .. ; .. . .. ~ ; .. __ , _ 

":. ·011026 .0. :· . . 0.0025[ 0.0028 O.OOZII .. 

' . . . . : ,:·. :. ·~·· -~· .:.-:--·· . '•: ... : ,: . . ·.·.;. ·.: .. .. . 

. -- :· ... _., ·, -- . :-. . ,,; '•, . ·. .. ·: . ,· 

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lORE :. :--.:; .• _:-. r_ . . : 

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~ -, · .. , .. . ''. .- ' :- _ ,_ ... ·"_·.- · u.e ,_ 18; . 10 : 16.3 .. ':' '. :' ,., .... ·. . -· . 

;·. " ·. r:rrkloct' . o.oot: ·• '0.1 ll4 ' 0.1 1.001 

' .. .. •, 

I ..... '.; .... ' '' ·. . . · ..- . . :. . ·;:. :' . . ·:: 1··-.'' .. ·: / 

. lll_rtlt_4- . . ,. .· ,1195 .· -. . 

I . . . .. IDRE . • • 

. . . _,. 

-... .. 

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· : 

I<Zl

.. :•- -7 • ~ <20.1 ~~ 

~-~ 

-· 

: .. :·• .•:- .-,- ~ .:.: 

; . .:·-· •. . 0.0078 _· 0.0074 

.... 

. . ; .- ... ' . . · . .. ·•. . ':, .. .. .. .:• .. 

,, 

\ 

·. 

.. · 

. 

MACT 

· . ., :> 1.9 

. > ~ 

· 32 

. 

- 0.0131 

• 

. 

• 32 

0.01: 

~ > ~ 

32 

: .. 

0.01: 

VES 004066 
Run 

No. 

1 

2 

3 

4 

5 

6 

7 

8 

9 

Date 

611712008 

611712008 

611712008 

611712008 

611712008 

611712008 

6/1712008 

6/17/2008 

6/1712008 

Table 3 

CEMS Relative Accuracy ·CO, J1PrA @ 7% 0, 

Unit 2 Incinerator Exhaust 

Time 

0943-1004 

1023-1044 

1101-1122 

1139-1200 

1240-1301 

1332-1353 

.1409-1430 

1446· 1507 

1521-1542 

Ave11119e: 

Veolla ES Technical Solutions 

Sauget. Illinois 

Reference Facility 

Method CEMS 

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 Accuracy: 

• Not used in avemges and RA calculation 

,. 

Difference 

· 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 004067 
Table 4 

i CEMS Relative Accuracy - o., percent dry (Cosa) 

Unh 2 Incinerator Exhaust 

Veolia ES Technical Solutions 

Sauget, lninois 

,. 

; 

' 

Run Reference Facility 

No. Date nme Method CEMS Difference 

1 611712008 0943-1004 12.9 12.5 0.42 ~ 

' 

2 611112008 1023-1044 13.2 12.8 0.33 

3 611712008 1101-1 122 13.2 12.7 0.47 

4 611712008 1139-1200 13.4 12.8 0.59 

5 6/1712008 1240-1301 13.1 12.5 0.84 

8 6/1712008 1332-1353 12.6 11.9 0.63 

7 6/1712008 1409-1430 13.4 12.7 0.76 

8 611712006 1446-1507 13.4 12.5 0.87 

g · 611712008 1521-1542 13.5 12.6 0.72 

Average: 13.18 12.58 0.60 

Relative Accuracy: 6.6 %ofRM 

• Not used in averages and RA calculation 

VES 004068 
Table 5 

CEMS Relative Accuracy • 0 2, pen:ent wet (Cosa) 

Unit 2 Incinerator Exhaust 

Veolia ES Technical Solutions 

Sauget, IIHnois 

! 

Run Reference Facility 

No. Date Time Method CEliS Difference 

1 611712008 0943-1004 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 1409-1430 6.10 7.94 0.16 

8 6/1712008 1446-1 507 8.15 7.85 0 .30 

9 6/1712008 1521-1542 8.18 7.92 0.26 

Aven~ge: 8.10 7.51 0 .59 

Relative Accuracy: 10.9 %ofRM 

• Not used in averages and RA calculatlon 

,, 

VES 004069 
Table 6 

CEMS Relative Accuracy - Moisture, percent 

Unit 2 Incinerator Exhaust 

Veolia ES Technical Solutions 

Sauget, Illinois 

•. 

Run Reference Faclnty 

No. Date Time Method 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 1139-1200 32.2 40.4 -8.2 

5 611712008 1240-1301 39.8 42.0 -2.2 

6 6/1712008 1332-1353 43.0 44.2 -1.2 

7 6/17/2008 1409-1430 39.6 37.3 2.4 

8 6/1712008 1446-1507 39.2 37.5 1.8 

9 6117/2008 1521-1542 39.5 38.1 1.4 

Average: 38.6 40.3 1.8 

Relative Accuracy: 11..2 %ofRM 

• Not used in averages and RA calculation 

VES 004070 
Run 

No. 

1 

2 

3 

4 

5 

6 

7 

8 

. •. \ 9 

Date 

6/1712008 

611112008 

6/1712008 

6/1712008 

6/1712008 

6/17/2008 

6/1812008 

611612008 

6/1812008 

Table 7 

CEMS Relative Accuracy - CO, ppm @ 7% 0 2 

Unit 3 Incinerator Exhall$t 

nme 

1716-1737 

1801-1822 

1836-1857 

1913-1934 

1948-2009 

2023-2044 

0752..0613 

0825..0646 

0857-0918 

Average: 

Veolla ES Technical Solutions 

Sauget, IUinois 

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 

0.28 

0.29 

0.00 

0.11 

0.03 

0.08 

0.2 ppm @ 1% 02 

VES 004071 
Average: 12.28 11.92 0.38 

Relative Ac:euracy: 5.3 %o1RM 

• 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 Relative Accuracy • 0 2, percent we( (Cosa) 

Unit 3 Incinerator Exhaust 

Veolia ES T echnlcal Solutions 

Sauget, IUinois 

~ 

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 7.12 7.36 -0.24 

611712008 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 0857-0918 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 004073 
Table 10 

CEMS Relatl\le Accurac:y -·Moisture, percent 

Unit 3 Incinerator Exhaust 

Veolla ES Technical Solutions 

Sauget, Illinois 

~ 

Run Reference Facility 

No. Date Time Method 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 6118/2008 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 

Relative Accuracy: 13.8 %ofRM 

• Not used in averages and RA calculation 

VES 004074 
Table 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 1334-1355 2.78 1.10 1.68 

3 611812008 1413-1434 2.70 1.13 1.57 

4 611812008 1456-1517 2.69 1.44 1.25 

5 611812008 1544-1605 2.77 2.26 0.51 

6 611812008 1623-1644 2.29 1.79 0.50 

7 611812008 1700-1721 2.25 1.73 0.52 

8 6118/2008 1732-1753 2.05 1.91 . 0.14 

.· : .) 9 611812008 1806-1827 1.75 2.35 -D.60 

Average: 2.43 1.72 0.71 

Relative Accuracy: 1.3 ppm@7%02 

• Not used in averages and RA calculation 

VES 004075 
Table 13 

CEMS Relative Accuracy - o, percent dry (Cosa) 

Unit 4 Rotary Kiln Exhaust 

Veolla ES Technical Solutions 

Sauget, Illinois 

~ 

Run Reference FaeHity 

No. Date Time Method CEMS Difference 

1 611812008 1257-1318 13.86 13.9 -0.05 ;: 

2 6/1812008 1334-1355 13.45 13.5 -0.08 

3 6/1812008 1413-1434 13.28 13.3 -0.05 

4 611812008 1456-1517 13A6 .13.6 -0.11 

5 6/1812008 1544-1605 13.72 13.9 -0.14 

6 6/1812008 1623-1644 13.45 13.5 -0.01 

7 6/1812008 170()..1721 13.49 13.4 0.06 

8 6/1812008 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% ofRM 

• Nol used In averages and RA calculation 

VES 004076 
' ' 

. ' 

Run 

N.o. 

1 

2 

3 

4 

5 

6 

7 

8 

9 

Date 

611812008 

611812008 

611812008 

611812008 

6/1812008 

6/1812008 

6/1812008 

611 812008 

6/1812008 

Table 13 

CEMS RelatiVe Accuracy - Oz. percent wet (Cosa) 

Unit 4 Rotary Kiln Exhaust 

Veolia ES Technical Solutions 

Sauget; Illinois 

Reference Facility 

Tlme Method CEMS 

1257-1318 8.56 8.36 

1334-1355 7.36 8.03 

14~3- 434 7.55 7 .85 

1456-1517 7.59 8.02 

1544-1605 7.68 8 .. 24 

1623-1644 7.22 7.99 

170()-1721 7.42 7.91 

1732-1753 7.70 7.99 

1806-1827 7.79 8.07 

Average: 7.65 8.05 

RelatiVe Accuracy: 

• N.ot used in averages and RA calculation 

Difference 

o.zo ., 

-0.67 

-0.30 

-0.43 

-0.56 

-0.77 

-0.49 

-0.29 

.-0.28 

0 .40 

8.1 %ofRM 

... 

VES 004077 
Table 14 

') CEMS Relative Accuracy - Moisture, percent 

Unit 4 Rotary Kiln Exhaust 

Vec:ilia ES Technical Solutions 

Sauget, Illinois 

• · 

Run Reference Facility 

No. Date Time Method CEMS Difference 

1 611812008 1257-1318 38.2 40.0 -1.7 .. 

( 

2 611812008 1334-1355 45.3 40.7 4.6 

3 611812008 1413-1434 43.1 41.1 2.0 

4 611812008 1456-1517 43.6 40.9 2.7 

5 611812008 1544-1605 44.0 40.5 3.5 

6 611812008 1623-1644 46.3 40.6 5.7 

7 611812008 1700-1721 45.0 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 celculatlon 

VES 004078 
t ..... 

·' 

: ', } ( ' l ..... 

.. .. . 

~5' ··: . . l 

~: · ~Iissi:.).sipi1i Lhne Company 

: 

Altc>n, !lHnoio 52002 

,, . ': . ' ·~ " : .-; .. '

JdJSSlSSlPPl ROTARY PJ,ANT 

lly,dre.ted Lime . 

. Code MR200 

·. 

:ao . t•1 

~'"'~'~ 4!S-4&•TUl 

..... ~l~et.s Ali'WA and Water ; ,he!"icals Codex Specif1~at1ons 

Chemical Ana lysis 

C,a ( O.ti) 2 • 

Ca.O Eq)livalent 

CaP Tote.~ 

~!lC03 

Caso4 

S Equi vo.len t 

Sio2 

Al2

03 

Fe2 o3 

ldgQ 

Free H2o 

P205 

·MoO 

.. . .. 

·• 

96.0$ to 

,72 . 6 to 

73 . 6 ~0 

0.65 to 

0.05 to 

o:o12 to 

0.38 to 

0 :20· to 

o.o1 .to 

0.40 to 

().so to 

o.oos to 

0.0015 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 .10 

0.024 

0.65 ' 

<1. 30 

0.10 

0.55 

0 .95 

0.012 

0 . 0025 

: 

VES004079 
( · 

69:45 5642757397 

NORIT Americas Inc. """,Odcos +-Fl• Best Perlcrmol>:e. 

DATASHEET 

DARC0°FGL 

POWDERED ACTIVATED CAF!BOI'I .. 

I<EV1N L. KAISER 

I'M 363:!5 · 

Product NO. FGl 

Revised 11-97 

OAACO 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 area_ m Jg 

Hutcapadly 

Tolollll#ur,% 

1gn111on 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 

Pitduena. · . · 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 tor Ptotectlcn against a~ du$·t ~ (Soo COdt cl Federal Regulations - Title .29, # -44>..-> SubP3rtZ.'por,1910.1000, Table Z-3), 

l ', 

· 

Lik.de.n5i~ 0.633'/rf\L 

33 1~t3 

,. 

•' 

' 

I' 

•' 

VES004080 
( ... > 

' 

Solids Residence Time Calculations 

Unit4: 

Based on the equation e-[(0.19L)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 is 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 for the rotlll)' kiln of30 minutes. 

Units 213: 

Since these incinerators are fixed hearth units, residence time is based on the travel length 

of the ash ram which functions to clear the primary combustion chamber of solid waste 

residue. A travel length of 110 inches bas been determined to be the minimum ash ram 

·stroke length required to remove solid waste residue from the primary combustion 

chamber of tbe fixed heartb units. 

VES 004081 
.. -.... MACT TRAINING OUTLINE 

j VEOLIA ENVIRONMENTAL SERVICES - SAUGET, IL 

I. ;environmental and Safety Requirements for. Incineration and Material Handling 

1.1 Environmental Regulations for lncinetation and Material Handlin& 

1.2 Safety Regulations for Incineration and Material Hondling 

2. Science and Tedlnology of Incineration and Air Pollution Control 

~ 2.1 . Combustion ' 

22 Heat &<change 

2.3 Refractory 

2.4 Acid Gas Neutralizatiqn 

2.5 Carbon Absorption 

{) 2.6 Ash and Particulate Removal 

3. Incineration and Air Pollution Control Equipment at Facility 

3.1 Combustion Systems of No.2 and 3 Incineralo<s 

3.2 Combustion System of No. 4 Incinerator 

3.3 Air Pollution Control Equipment of No. 2 and 3 lncin<ntors 

3.4 Air Pqllution Control Equipment of No. 4 Incinerator 

I 3.5 InStrumentation and Stack Gas Monitoring 

. 3.6 Process Control and Data Recording Systems 

' . 

VES 004082 
MACI 'IRAINING OtiTLINE (continued) 

4. Incinerator Feed Systems 

4.1 Natural Gas Buma-s 

4.2 · Bulk Liquids ~ 

4.3 Bulk Solids 

4.4 Cootainerized Solids ' 

4.5 Specialty Liquids 

4.6 Gases and Liquefied Gases 

S. Opention of Facility 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 
.. ~ .... -

:.· .. 

( ' ).. '.• ., 

. . 

Onyx Environmental Services, L.L.C. 

#7 Mobile Avenue · 

Sauge~ ll 62201 

(618) 271·2804 

(618) 271-2128 FAX 

TITLE: 

SUBJECT 

DESC~iON: 

TRAINING DOcUMENTATION 

FORM 

TJWNING q:IDE: -------:,--(lfun,cmain, lurw: h/tmlc) 

'fRAmiNG PROVIDtD 

BY: 

(TnUotT~s DIUIIe P."'Died) 

DATE TRAINED: · . '3·s.-o3 :!.·b ~o~ 

. LENGTH OF TNG: 

A 'l"J'ENN!EES: · 

5. _________ ~~---~-----------~~-----. 

6. _____ ~---------------·· _______ ~------~--

7. ____________ --:--------------~--------------------~ 

8. ____________________ ~-------------~---------

9. _~-----------~----~---------~----~ 

JO . ..:.·--------- -------~----~-- ------ ---

Entered in TRS: --------

.. : 

VES 004084 
,__ ... - '· 

J Onyx Environmental. Services, L.L.C; 

#7 Mobile Avenue · · 

Saugelll 62201 

(618,.271-2804 

(618) 271-2128 FAX 

TITLE: 

·:#ONYX · 

TRAINING DOcUMENTATION 

FORM 

~~~ ON: .. ~i9J.Q cf El\S (~; St~ tf ocl~U<'tiO\ ' ~ 

~~ r~jicn 0*4 Aft r~ tf lW ;)j ~o . 

ll!!d No. &\- I"!l.c, 

TRAINING COD£: (lfoncertllin, leave bltRi/r) 

TRAI}jJNG PROVIDED. 

'BY: 

. (Tralner's oamo prilltcd) 

. ' DATE TliAJII!JD: 

L£NGTB OFTNG: 

ATI'END.IIES: · • 

,fit.; TO 

'TRS bltU/(j); . 

-

5. 

6. ' -

7 • 

. 8. 

9. 

10. 

Entered in TRS: _ __ _ 

VES 004085 
(" :--

; 

< 

\ 

Onyx Environ!f1ental Services, L.L.C. 

117 Mobile Aveoue · 

Sauget. IL 62201 

(618) 271·2804 

. (618) 271-2-128 FAX. 

---------------------------- TITLE: 

TRAINING DOCIJMENTATION . 

FORM 

SUB.rtCT 

DESCRIPTION: · IZfvi01.1 of r't~~ ~i~ ~ ·~~~(~ , S<.iJ.-1& tf 

~ Md r'4 ~fiX" ~ ar.£\. t{\r 

vtA\&011 (Dt\w ~~~ 

TRAII'IlNG COD!: {lfii.IKmain. /tUNe blank} 

TRA.JNING PROVIDED. -"f"" lA 

BY: . .J(fF r~atq. · .-: 

I.J!.NGTH OFU'IG; 

A~Us: · 

· (Tmioer's II3IDe priut<d) 

lle W5 J 

6_. I • 

--------------------~----------~--------~~ 

'·------~------~------~------------------~~~--

~----'------------------------------------------- ?. _________________ :..._ __________________________ __ 

IQ. __________________ --------~:..._----:..._------~:..._~ 

Entered in TRS: -------'-

. · 

,, 

VES 004086 
--

.. 

·--

) Onyx -Environmental Services, L.L.C. ~ONYX . 

. I 

#7 Mobile Avenue • 

· Sauget. IL 62201 

(618) 271-2804 

(618) 271·2128 FAX TRAINING DOCUIIENTA T10N 

FORII 

TITLE: tl\w::f 1wo~9ffio!';. 0Pa:A.!l> ~;._.ltW..ilol(, - '\>~~ \ ~a 

~~~ ON; · .. ~l.)· Of f_I.\S (~\a_\:i()t\$ 1 <:,tjtr{f If ~~\i()\ ooJ 

. - : !1'Aio\ c~1s f <~ · tW1 P..f'C ~-\,~ ~ · · . 

t\)_.;1, t\Q.";) ~ th 1\- 1[1~ · ... 

TRAIN1MG COD I.; ------{ll"'!"'fabo, I~ bfoni) 

s. _____ __: _____ ---:-------------

6 • • 

-~·------ ----- ----------~-----

7.-'-.--------------'----------------'---------

8. __________ _ ________ ~-------:---.;.._~-.,.--

9. _ __________ _:_ ___ ....;....._~ --- .,.--.,.-----.,.--

JO. _____ ~--------------'--'-------~ 

Eotet<d io TRS:-~--

. ' 

. -,. 

.· 

I 

.· 

VES 004087 
\. . --

· .. 

J ·onyic Enviropmental Services, L,L.C. ~ONyX #7 Mobile Avenue · 

Sauge~ IL 62201 

(618) 271·2804 

(618) 271·2128 FM TRAINING DOCUMEN7A n ON 

.FORM 

--------~--------~~~~---

TITL£: 

suilncr 

D!SCIUPTION: · 

WV...C .. :T· L!tlil®06 ~or- f~itl(, .. YA~,-, i ... ~d. 

Rw~M tf r9f'v*i011? , s(iti'(Q ,f il\cj~a\, 1Wil'll4~ 

.. t~\s rf fMblls-\m '"id ~K Si~-\1NIS t\\ ~o. () , · . 

Nil.~ Aoid. t-\o. 4 J11ti~ . 

. 'IltAININC COD&: ______ {If om.-..; lc~blank) 

... · . 6. _____ _:.... _____ ____________ _ 

7: . 

.__,__: ---'---~.,------'-----,.-- ;.._;_----

9. ______ .:......_ _ _ _ _,;:..__~ -----------'-"7" 

19·---------------...,...------~-~~ 

' " 

. . : , 

' 

VES 004088 
I' :--

; " \ " 

; . Onyx Enviropmental Services, L.L.C. -- ~oNYX 

(} 

. .. 

· . . 

117 Mobile Avanue . · 

Sauget. IL 62201 

(618) 271 -2804 

(618) 271-2128 FAX 

TITLE: 

TRAINING DOCUIIIENTATION · 

FORM 

~~ION: ·- .. ~«llitv.> of (~IA\A.\::;O II S, Soi.i (. cf i"~intai\:iol\, . . 

. .. a.,.a "'~a- c~'l>. J . {~ Ao'lirur p:l~Ctl ~\_ 

~\t..s -\ix-No tJo ~ a.d tohA lAd~ . 

TRAII'IING COD&: 

TRAINING PROVIDED . ... 

· ur: · (T'-"inet's IWDO printed) : 

DAT& TRA.INii:D: . • · ~1i:. · 't" I 0 

~) 

i.ENGm OF TNG: 

A~EES · 

. . ·PRINT NAME: 

• 

aoo:l. 

~~ifiPlJT TO · · 

T 

.. 

·~------~~------~--~------~--~~--~----~ . 

. s. 

------------~----------------~~-- ------~ ·. 9. ______________________ ~----------------------------

\ JO: ____ --:----'---'-------..,.----.:.._------------------------..:.....~ 

Entet<d ;.,·TRS: __ ...:.._.~-

•. 

. . 

' 

' . ·.•. 

VES 004089 
' r~· • 

. )" 

Onyx Envfionmental Services, LLC. 

17 Mobile Avenue 

Souget. It 62.201 

(618) 271-2804 

(618) 271·2128 FAX T1'llf8IA'U DOCtAIIBYTA 11'INY 

------------------------------~---~ TITLE: W..C.T Qpeu>.ror. \I!;A)~,~,'='c, - XAf:rs 3 ~ 1 

~~ON: 'ltv't bo\ cf ~~ f~~~ a-d ~~ 1 

II((P'O\ o~ M<l~ 6f ~~ 

TII.A.INlNGCODE: (lfuncutatrr, kavebhm/1) 

~G PROVIDED Jift t14.\\r 

(n:aiot<'s name prinred) 

. DATE TRAINED: . 'fAp;f>3 ft 1Al/lB 

( ) ' Ll!NGmOFTNG: -.l.llp......__,lm;)...,'-------- -

ATTI!NDEES: 

......:...:.:..l.'T-'"""-'~--------:------Pfll&o\-le.=--+.j-;--------

S . .J,:J.J~G.L~!:'d.IJ::L.__,. ___ __:~~JL.¢)~!L--

6. _____ ___ _____ -----~-------- ~----~ 

7. _ _ _ _ ~-~------------- -~-----~ 

·----- ----------------- --- -- 9. ___________ ____________________________ ~-----

10. ___ _________________ __,_ ___ ____ _ 

llnle<Od in TRS: - ---

VES 004090 
\ 

.I 

. {- . , . .. 

·-

.. . 

. . 

Onyx .EnVironmental S8rvic8s. L.L.C~ 

#7 ~e Avenue 

Sauget, ll 62201 

{6181 271·2804 

{6181 271·2128 FAX 7R9/NIMJ DOCU4f.61/TA170H 

--------------------------~-------------------~ 

TI1'LE: 

. . 

SUBJECT 

. · DESCRXP110N: 

TRAJNING CO])lt: 

TRAINING PROVJD.It]) 

BY: 

DAT£ TRAINED: 

LENGTH OF TNG: 

- ------ (ffunurtain, letrnblanJJ 

(TI'\\lncr's name printed) 

ARU\. ;ll~~. O'Q:)3 . I~ \..o>As 

~) ~ : ...... ·· ... :. 

'• • . . .-i •• ~ .. ~, . J; ~ ..J. f; •!.>< ' • ~ ~ 

s. __________ "--_______ ..:..__:_ ___ ~------'--- ........:...---...:.... 

6._· ---- --'----------_.:......;_ ___ ~---

7., _ _...:._:_ _ ___ :..__ ___ -----------.,----

a. ____ ___ .:_____: ___ _;_ _____ _____ _ 

9 . ..:_~- ..,-------------....:.... _ ____ ..:__ 

10. ___ _ _ ___ ____ ___:. ____ _ _ _____ _ 

Entered in TRS: - - --

VES 004091 
j 

;( · 

·•· 

.. 

Onyx Environmental Services, C~ 

#7 Mobile Avenue 

Sauget, ll 62201 

(6181 271·2804 

(6181 271 212~ FAX 77lA/JWNQ JJOcVMENTAT70N FOHN. 

--~----------------------------~ 

TITLE: 

SUIIJECI' 

DISQIIPTION: 

.DATETRAINtD: 

LENGTHOFTNG: 

ATTENDEES: 

<4'1itw f ~ aw1 ~ -id 9f~; ·~ ~ 

il\~ M'$11!X"~ £(¥ful~. M~i ~I~ 

a.J ~\~ urse\s . 

--,--- - -_;·(ifunanoin.leav< blank) 

. •. 

'·---------'------.,-------- ..,........: __ _ s. ______ .....:...; _ _ .:._ _ __:.. ___ .:...:.:_ _____ _;_ __ _ 

9. ____ _ _ ________ _:_ _ __ .:._ ___ .......;:__ 

IO --- -- --------~.:.___:_.,--_:_ ___ _ 

En!£red ui TRS: _ __ _: 

.· . 

VES 004092 
J 

\ .. 

. . . 

' 

Onyx En'llironmirrtal Senices, L.L.C. 

#1 Mobile Avenue 

Sauget, ll, 62201 

(618) 271·2804 

(618) 271·2128 FAX . 77iAW1HG DOCt.IJIU!HrA l1QN . 

--~------~------------------~-AHV 

TITLE: 

S1J1IJECr 

. DESCIUPTIO!I: 

·. 

TRAINING CODE: 

l . 

2. 

: 3. 

4. 

s. 

.6. 

·.'· 

a. 

9. 

10 . 

~"'Act . ]i4o~"tli{ ~ ~fllolb .. ? ~ :!, ~ '+ . 

. f\~llo) rf. ~1\DJ\ ~~ m:d ?f!t~; ~~ ~ 

,~! ,r ~ \, l7 ) : \jl(,~ , 

~h~ ~ ttvk ~~ (x"o14~ ~ r 

--'------(tfrmcmailr. kwe bltml:) 

• 

~ . , &.tmd.inTRS: _ __ _ 

. :: 

VES 004093 
j 

( ): ...... ~ 

Onyx Envlronmeiital Services, LL.C. 17 Mobile Avenue 

Stugllt, IL 62201 

(6181 271-2804 

(6181 271-2126 FAX lJMAIWGIJOCIIMI!NTAni':W 

--------------------------~---~ TtrLE: 

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Onyx Environmental Services, L.L.C . 117 Mobile Avenue · 

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Onyx Environmental Services, L.L.C. W7 Mobile Avenue . . 

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Onyx Environmental Services, L.L.C. 

il7 Mobile Avenue · 

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(618) 271·2804 

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VES 004099 
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G)veouA 

ENVIRONMENTAL SERVICES 

17 Mobile Ave. 

Souget, IL 62201 

TRAINING 

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20Q98NNVALREFRESHERIBAINJNG 

SOCIAL SECURfTY II 

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VES004100