Figure 2,3 

..... 

no 

...,., 

(M:f~ f 

.Ulrgg ~ 

') ":'W""' '>------

Rotary Klln Incinerator, lJnit 4, Bloc.k Flow Diagram 

11 

- rllruJft,!IIWI w.:l!t" ~ 

--- - · flM.'OIG ~-"""~ .. I\.W 

~ Aftilr\Otl' 

ooooo- ~ 'INI$1'! 1>\0<1' 

~ I- So.U'<fiY A.Chf 

VES012200 
A carbon injection system is utilized for controlling dioxiiJifuran and mercury emissions. 

The activated carbon is air injected into the combustion gas immediately downstream of 

the convergence of combustion gases from the SO As. 

Combustion gases exit the SDAs and are distributed to two fubric ftlter modules. Each 

module has three compartments in parallel containing multiple fahric bags. Combustion 

gas passes through the fabric bags. Particles in the combustion gases are deposited on the 

outside of each bag. During the bag cleaning cycle, a burst of air in the direction 

opposite to the gas flow dislodges particulate matter from the bag. 

The induced draft tim is located downstream of the fabric filter bagbouse. The induced 

draft fan moves the combustion gas through the system and exhausts the gas through the 

main stack. 

Hot, wet gas is extracted downstream of the ID fan through a continuous emissions 

monitoring system. This system features a multi-component infrared gas analyzer that 

detects hydrogen chloride, carbon monoxide, and water vapor concentrations. An 

integrated zirconium oxide-based analyzer detects oxygen concentrations. 

12 

VES012201 
3.0 STARTUP AND SHUTDOWN PROCEDURES 

The purpose of this section is to prescribe procedures for the startup and shutdown of the 

incinerator system. This section also clarifies which actions are within the scope of the 

regulatory definition of startup and shutdown. 

To satisfy the requirements of§ 63.1206(c)(2)(v)(B), waste feed restriction and operating 

limits have been imposed to startups and shutdowns. During a startup, the feeding of 

hazardous waste to the incinerator \\~U not be initiated until aU operating parameters are 

within limits. Hazardous waste will not be fed during a shutdown event. 

Consistent with the requirements of§ 63.1206(c)(2)(iii), Veolia Mll utilize an oxygen 

correction factor of 1.6 (i.e., 12.3% 02) during periods of startup and shutdown. This 

will eliminate wide variations in corrected CO concentration that can occur during startup 

and shutdown due to changes in the oxygen concentration. The oxygen correction factor 

of 1.6 is based on the average oxygen correction factor observed during normal 

operations of the incinerators. This "default" oxygen correction factor can only be 

utilized when the waste residence time in the primary combustion chamber has expired 

and when the incinerator is in startup or shutdown. 

Veolia has developed standard division practices (SOPs) for the operation of each 

incinerator system and ancillary equipment and systems. The SDPs containing startup 

and shutdown procedures for the incinerators are: 

• SDP 2201 

• SOP 2417 

3.1 Startup 

Startup, Operation, and Shutdown of No. 213 Incinerators 

Startup, Opera/ion, and Shutdown of No. 4 Incinerator 

AU startups are preceded by a shutdown. Depending on the purpose of the preceding 

shutdown, portions of the air pollution control system may be in service upon 

commencing a startup. This will be reflected on the startup record (see Attachments 1). 

During a startup, waste will not be introduced until all operating panuneters are within 

limits. A startup event is concluded once waste is introduced and all operating 

parameters are within limits. 

\I eolia's startup procedures are representative of safety and good air pollution control 

practices. Tl1e procedures are designed to minimize tbe potential for excess emissions by 

ensuring that aU equipment is fully operational (within permit limits) prior to the 

13 

VES012202 
introduction of hazardous waste to the system. Adherence to these startup procedures 

will employ the knowledge and skills demonstrated through the implemenlalion of the 

Ope!'lllor Training and Certification Program. 

14 

VES012203 
3.2 Normal Shutdown 

Some shutdowns will allow the primary combustion chamber to cool. Prior to these 

shutdowns, the incinerator will be burniug auxiliary fuel only and the hazardous waste 

residence time will have transpired. A shutdown will be initiated with the shutoff of 

auxiliary fuel to the inciuerator or by shutoff of the ID fan. Other shutdowns will be 

initiated .,.;th the cessation of all waste feeds by the operator to stabilize system operating 

parameters. Portions or all of the air pollution control system may remain in operating 

mode at the conclusion of a shutdown through the subsequent startup. 

Veolia's shutdown procedures are representative of safety and good air pollution control 

practice. The procedures are designed to minimize the potential for excess emissions by 

ensuring that all waste feeds are off and/or the hazardous waste residence time has 

transpired prior to the shutdown of the incinerator system. Adherence to these shutdown 

procedures will employ the knowledge and skills demonstrated through the 

implementation of the Operator Training and Certification Program. Procedures for 

emergency shutdown are described in the next section regardiug malfunctions. 

15 

VES012204 
4.0 MALFUNCTIONS 

The pwpose of this section of the Startup. Shutdown and Malfunction Plan is to: 

• .Define potential malfunctions and their causes 

• .Describe measures to minimize the frequency and severity of malfunctions. 

• Presctibe procedures for operating and maintaining the incinerator during 

malfunctions 

• Prescribe actions to correct the cause of a malfunction 

A summary of potential malfunctions and their causes is given in Table 4-1 . This list of 

potential malfunctions is arranged according to unit operations. The occurrence of any 

event listed in Table 4-1 should be responded to as a malfunction and a malfunction 

recordkeeping fonn, included as Attacbment 3, should be initiated. During the response 

to these events, it will be detennined if tlte event meets the regulatory definition of a 

malfunction. 

4.1 Measures ro Minimize the Frequency ofMalfiUlctions 

The following measures contribute to prevent malfunctions: 

• Incinerator system design consistent with safety and good engineering practices 

• Hw..ards and operability studies of the incinerators 

• Appropriate frequency of preventative maintenance and inspection 

• Good operating practices 

• Well trained and qualified personnel 

Veolia's performance history, this document, and the following regulatory documents 

serve as evidettce of Veolia's proactive measures to minimize tlte frequency of 

malfunctions. 

• Operation and Maintenance Plan 

• Operating Training and Certification Program 

• Continuous Emissions Monitoring System QUtJiity Assurance Plan (GEMS QA 

Plan) 

• Continuous Monitoring System Quality Co!llrol Plan (CMS QC Plan) 

• Automatic Waste Feed Cutoff System Operability T-est Procedures 

16 

VES012205 
Table 4-1 Summary of Potential Malfunctions and Causes 

Potential Malfunctions for Units 2, 3, and 4 Potentia! CalLus for a 

l\lalfu coon 

GENERAL ·· Low Wator Level in Slag C<>Uection System (Unit 4) 

- Loss of Eleclrical Power Supply ··Rapid Steam Gc:uc:rniion from Ash Collection System Water 

- Loss oflu..'i>trumentJPlant Air Supply TEMPERING CIIAIItliER (UNIT 4) 

- Loss of Plant Nitro&en Supply - Loss ofTempering Chamber Exit Gas Temperature Control 

- Loss of City Water Supply - Loss of Atomization Air Pressure to Nozzle Mecbanical/eleetrical 

- Loss of Pro~ Water Pressure/Flow (Unit 4) LIME SLURRY SYSTEM failure of rotating 

- Malfunction of Safety Interlock or Automatic Waste Feed - Loss of Lime Feed to Limo Slurry Feed Tank equipment. 

CUtofflntorlock - Malfunction in Lime Slurry Concentration 

- Excessive Air In-leakage in A iT PoUution Control System UNITS 2 AND 3 SPRAY DRYER .ABSORBER (SDA) Phtgging/physical failure of 

PRIMARY COMBUSTION CflAM.BER - Loss of Lime Slurry Flow to SDA 

- Loss of Natural Gas Pre""-ure/Flow to PCC Main Bumer - Loss of Lime Slurry Flow Control 

lines/nozzles 

- Loss of Combustion AiT Pressure/Flow to PCC - LossofCityWaterFiowtoSDA 

- PCC Main Burner Pilot Failure - Loss of Cooling A.ir Flow to Atomiz,cr Physical/electrical failn"' 

- Loss ofWa."e Flow to PCC lrtieetor - Loss ofSDA Exit Gas Temperarure Control of instrumentation 

- Loss ofWasteFeedt"ate Control to PCC Injector - Atomiu.c Failure 

- Loss of Atomization Air Pressorc to a PCC 1J1iector UNITS 4 SPRAYDRYER ABSOIUJER (SDA) Mechanical/electrical 

- LossofPCCDraftControl (Unlt4) - Loss ofLime ShuYy Flow to SDA failure of actUated 

- Loss ofPCC Tewper•ture Control - Loss ofLime Slurry Flow Control!E:tit Gas Temperlllll"' valves/dampers 

- Flame Failure Control 

- Kiln Rotation Malfuncti011 (Unit 4) - Loss of Atomization AiT Pressure to SDA Nozzle Physical/electrical failure 

- Bulk/Charge Feed Door Malfunction CARBON INJECTION SYSTEM (UNIT 4) of control system 

- Physical/M.ccbaoicallntemal Equipment Failure - Loss of Cw:rier Gas Pr<>s>ur<> 

- PCC Seal Visual Emissions Monitoring and Recording System - Loss/Restri<:tion of Activated Carbon Flow 

- Rapid Steam Geu.erntion from Ash Collection System Water - Loss of Plant A.ir Pressure/Flow to Carbon Bulk Sack Mechanical/electrical 

SECONDARY COl\tliUSTION CllAl"dBER BAGBOUSE & INDUCED DRAFT (ID) FAN failure of utility supplies 

- Loss ofNatural Gas Pressure/Flow to SCC Main Burne:< - Tom/Leaking Bag 

- Loss of Combustion A.ir Pressure/Flow to SCC - Bag Blinding/High-High Pressure Drop ElectricaVactuation failure 

- SCC Main Burne< Ignition Failure - Loss of Stack Gas Flowrate Control (Unit 2 and 3) of safe\y interlocks 

- Loss of Waste Flow to SCC Injector - Baghouse Isolation Damper Malfunction (Unit 4) 

- Loss of Wasto Fcedratc Control to SCC Injector - ID Fan failure Physieallmechanicnl 

- Loss of Atomization Air Pressure to a SCC Injector CONTROL SYSTEM/CONTINUOUS M.ONlTORINC internal equipment failure 

- Loss of SCC Temperature Control SYSTEM 

- Flame Failure· - Cootrol System/CootinuoU$ Monitoring System MalfWtCtion 

- Emergency fe~y Vent Opening - Continuous Emis.'lions Monitoring System Malfunction 

- Pbysicai/Mecbanical Internal Equipment failfi(<) 

17 

VES012206 
Despite these efforts, equipment failures and other operating anomalies can occur. 

Within the scope of regulatory requirements, the operating record will contain the 

appropriate documentation to establish that poor maintenance or careless operations are 

not contnouting factors to the cause of a malfunction. 

4.2 Measures to Minimize the Senrity of Malfunctions 

The following measures contribute to minimize the severity of malfunctions: 

• Alanns and interlocks 

• A WFCO testing 

• Failure positions for critical equipment 

• Well trained and qualified personnel 

• Design of the incinerator system 

Typically, an event that meets the definition of a malftmction will trigger an alarm. An 

alann infonns the operator of the situation and may provide an opportunity to avoid an 

exceedance. If conditions become unsafe or exceed operating limits, interlocks are in 

place for an automated response that is specific to the triggering condition. Refer to 

Veolia's Documentation of CompliJ:Jnce or Notification of Compliance, whichever is 

currently applicable, for details on A 'vVFCO conditions. Additional details on alamts and 

interlocks are maintained on piping and instrumentation diagrams (P&IDs) 

The most critical key to minimizing the severity of malfunctions is the functionality of 

A WFCO interlocks. Accordingly, V eolia performs testing of the A WFCO system, as 

described in the AWFCO Plan. This testing confirms a state of readiness to respond to a 

malfunction in a manner that will minimize the release of hazardous air pollutants. 

Through training and job experience, the operat.or will have the process knowledge that 

qualifies him to use discretion in responding to malfunctions. Due to the Wlnsual and 

dynamic conditions that are present during a malfunction, operator discretion is essential 

to minimizing the severity of malfimctions. An operator can evaluate process conditions 

and alarms and choose the best response to avoid an exceedance, if possible. If the 

malfunction adversely affects the functionality of alanns, interlocks, or fail safe positions, 

the operator must recognize the situation and respond appropriately. [n the event that the 

malfunction affects the ability to automatically cutoff waste, the operator will manually 

cutoff waste feeds as quickly as possible. 

18 

VES012207 
The design of the each incinerator system olso ensures that the severity of malfunctions 

will be minimized. This includes alarms and interlocks, the fail safe position of actuated 

valves, and redundant instnnnentation and process equipment. Also, the design of each 

incinerator's instrumentation and control systems provides the operator convenient access 

to process variable indication, including position indication of selected actuated valves. 

This is essential to providing the operator the information required to best evaluate 

system conditions and responses. Table 4-2 lists potential malfunctions and associated 

redundant equipment and systems that are available to prevent tbese malfunctions or to 

minimize the potential for a significant rclellSe of hazardous air pollutants. 

4.3 Corr ective Measures 

The Program of C<!rreCJive Accions for Mo/fonction.s is Attachment 4 of this document. 

This program addresses how tbe incinexator will be operated and maintained during 

malfunctions. In this program, potential malfunctions are listed for each portion of the 

incinerator systCllJ. The malfunctions are t."Vents that will be recognized by the operator, 

or indicated by an alarm, and threaten to cause an exceedance. In the response to the 

malfunction aodlor alanns, the operator will apply discretion and attempt to maintain the 

incinerator system within regulatory limits. In the program of corrective actions, 

potential causes of eac-h malfunction are listed. The operator will utilize process 

knowledge, job experience, and, if needed, assistance from other personnel to identify the 

cause of the malfunction. For each potential cause, actions to correct tbe fuilure are 

tisted. The corrective actions prescribed may require the collaboration of multidisciplined personnel wbo are qualified to return the incinerator system to proper working 

conditions (i.e., maiotenance personnel, control systern technicians, engineering). 

l9 

VES012208 
Table 4-2 

Redundant Equipment and Systems for 

Minimizing the Frequency or Severity of Malfunctions 

Redundant Equlpmenr/Sy5tem5 l'otential Malfunctions Prevented/Minimized 

Emergency generator (Unit 4) Loss of Electrical Power Supply 

Universal Power Supply (UPS) system powers Loss of Electrical Power Supply computers, monitors, and control systems 

Two compressors are on hot standby (Unit 4) 

Three air compressors running and one compressor 

on bot standby (Unit2 and 3). 

Loss of Instrument/Plant Air Suppl y 

Dual Process Water Pumps Loss ofProcess Water Pressure/Flow 

Dedicated PCC combustion air fan (Unit 4) Loss of Combustion Air Pressure/Flow to PCC 

Dedicated SCC combustion air fan (Unit 4) Loss of Combustion Air Pressure/Flow to SCC Spare SCC combustion air fan (Unit 4) 

Loss ofTempering Chamber Exit Gas Temperature 

Multiple Tempering Chamber Nozzles Control 

Loss of Atomization Air Prcssun: to Nozzle 

Dual Sluny Feed Pumps (Unit 4) Loss of Slurry Feed to SDA Shared Back-up Pump (Unit 2 and 3) 

Off-line Spare Lime Slurry Atomizer (Unit 2 & 3) Atomizer Failure 

Loss of Lime Slurry Flow to SDA 

Dual SDAs (Unit 4) Loss of Lime Slurry Flow Control/Exit Gas 

Temperature Control 

Loss of Atomization Air Pressure to SDA Nozzle 

Off-line Spare Baghouse Module (Unit 2) Tom/Leaking Bag 

Two baghouse modules with three compal1ments 

each. 5 compartments provide sufficient particulate Tom!Leaking Bag removal so that one of the 6 compartments can be 

isolated as a spare. (Unit 4) 

20 

VES012209 
ATTACHMENT 1 

STARTUP RECORD KEEPING FORM 

VES012210 
VEOUA E-NVIRONMENTAL SERVICES, INC. 

INCINERATOR STARTUP RECORD 

(Pogo I of3) 

This report penoins to astottup ol' Unit 2 I 3 I 4 (cirele one). 

Starrup event initiated on: 

(}.lootb/Day/Y""', Ho..,. : Millutes) 

StartUp ewnt CXltiCIUded oo: 

(Month!Oay/Year, Hours : Min"tes) 

'The total durn lion of this startup event wa~: 

(Hours : Mioutes) 

Attacll<ld to this fonn is a cbeekJ.i>1 that sununariz.el the iiJ>PI'O"cd siannp procedure~ referenced in Voolia'• 

Slartup, Shwdow., and Ma/fonc:lum Plan (SSMP). The opetational steps thAt ba\'e boeu checked documc:nt that 

the dclailed SW111p procedun:$ were followed. 

W.n all actio .. nssociated wilh this startup .-.. nt in oonfurmancc with the SSMP? Yes I No (cirele one). U 

no, describe tho lnconsistent actions below. 

Were there any oxecedances of an opcraliog p.,..meter limit? Yes ! No (tm:le one). If y .. , please lis<idescn'bc. 

lf any :~.ction.s were no1 coosistent with the SSMP and an operating parameter limit wxs exceeded. an immediatQ 

SSM report Is required. 

The following signature certifies the accuracy oflbis record: 

(Name) (fitle) 

(SiJ!Dature) (Date) 

VES012211 
VEOLIA E IVIRONMENTAL SERVICES, INC. 

INCJN£RA TOR STARTUP RECORD 

(Page 2 of3) 

Uait 2 and 3 lnclnen~tor Startup Cheddut 

Verify that pre-startup hos been completed 

Check tltennal relief vent (TR. V) 

Stal.1 combustion air fan 

Smrt PCC main burner and ttmpen~ture J'1JDI>"up 

sran sec main burner and 1<mpetlltun: r.unp-up 

Check stack gas Dow and SOA temperotu~CS control se<tings 

Sta1.1 ID fim. Monitor SDA 1empe111tutt wllile r>mpini up stack gas llowrate 

CloscTRV 

Start time slWl')l 

Estabtish aU operating porameters within limits 

Open tor's Notes: 

Jnltinb 

Note: Cenain air pollution trol and ancillory oquipment mAy be operational prior to stanup 

(Signature of Shill Leader or Dc:oisnoe) (Dote) 

VES012212 
''EOLIA ENVIRONMENTAL SERVICES, INC. 

INCINERATOR STARTUP RECORD 

(Pogcl of3) 

Unit 4btctncntor Startup Cbccklfst 

Verify that pre·startup has been oontpleted 

Check thermal relief -t (TR V) 

Sl4n ID fun and set kiln droft {s!Jirt of purge cycle) 

Stat! SCC combustion air fan 

Sl4rt tho kiln combustion air fun (purge cycle complete) 

Stan sec main b~ and t<mpcnture Bmp-up 

Starti'CC main butner lind ltmperature temj>-up 

Start kiln rotation be foro SOO ' F 

SIAn tho kiln seal air 

Stan the sec cnnveyor 

Set up the l<rnpering chamber for operation 

Set up lime slurry injection system 

Set up the SOAs for npcration 

Set up the ash collection sysleln 

Set up the bagbous<s for opcratioo 

Slowly ramp-<>p the tonporing cbamber exit tcmpentture 

Continue PCC and sec temperature romp-up 

Starl tlte kiln sc-aJ conveyor 

E£tabliJ;h all oper•ting perameters within Ji.Uu 

Opnator,s Notes.: 

Initials 

I 

Note: Certain •ir palluuon control and WlCillary equipment moy be oper>tional prior to starwp. 

{Sianature of Shift l..eader or Designee) (Date) 

VESOJ2213 
ATTACHMENT2 

SHUTDOWN RECORD .KEEPING FORM 

VES012214 
\'EOLIA ENVIRONMENTAL SERVICES, INC. 

INCINERATOR S.BlJTDO"\\'N RECORD 

(Page I of3) 

Tbis report p..'ltoin"o a shutdown of Unit 2 I 3 I 4 (circle ooe). 

Shutdown event initiated on: 

(MoniM>ay/Year, Hours: Min11te0) 

Shutdo\<11 event conetudod on; 

(MontiVDay/Year, HOUTS: Minutes) 

The total dun\lion ofthjs shutdown event wnl': 

-.,.,(lt.,..o-tllS-: M=in-utes ,....,-}-

Attached o UUJ: form is a cbecklist tluu $Urnmarizcs tbe approved shutdown procedures referenced in the Veolta 

Startup, Shurdtnvn. a11d Ma/fw!Clit>n Plan (SS ~1P). The opentional steps !hat have been chedcod do=nent that 

tbe detail«! shutdown p.ocedu.,.. were fullo\\..1 

Were allaetiODS assoeial<ld with tbis shutdown e•'Cill in c:onfolliiADCe with the SSMP? Yes I No (citcle one}. If 

no, describe the lnconsistc:ot aeliom below. 

Wore th¢re any ••cecdanccs of an opemtinj\ paramc!ter limit? Yes I No (circle one). If yes, please li.stldcaoribe. 

If any actions were not consistent with tho SSMP and an operating parameter limit was exceeded, au immediate 

SSM report ls requited. 

Notes!Rccommeodations; 

Tbe following •lgnnture certifies the accumcy of tbls rocord: 

(Name) (l'i o} 

(S """"""} (Date} 

VESOI2215 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

INCINERATOR SHUTDOWN RECORD 

(Page 2 of3) 

UD.it 2 and 3 luciDe.rator Shutdown Checl<.Ust 

Verify lhat all was!¢ feeds are off and/or lhat the hazardous waste residence 

time has transpired 

Monitor CEMS output to verify stable oonditions 

Open the stack cap 

Stop the ID fun 

Shu\ off water and lime slurry flow to the atomizer 

Remove atomizer and position tid 

Operator's Notes: 

Initials 

Note: All or certain air pollution contrOl and ancillary equipment may remain operational throughout 

shutdown. Once the hazardous waste residence time has tranSpired, operator's discretion can be 

applied. 

(Signature of Shill Leader or Designee) (Date) 

VES012216 
VEOLIA ENVIRONMEl'fT AL SERVICES, INC. 

INCINERATOR SHUTDOWN RECORD 

(Page 3 o£3) 

Unlt 4lncinerator Sbutdowu Chetklist 

Verify that all wasrc feed• ore off and/or that !he hazardous waste 

residence time bas irnnspired 

Shot off the kiln burner and SCC bun1er 

Shut off the laln &nd sec eombWihOD •ir fans 

Reduce tbe tempcriDg chamber outlet tempernture to 500 •f 

Sbuulown SDA (at IJlP"'I)Mie tcmpera!W'eS) 

Shutdown tempering chambct (at appropriate tempcratun:s) 

After PCC and SCC reach the oppropriato tenJperature. shut off the ID fan 

Ope-rator's Notes: 

loltlab 

Note: All or certain air pollution con1r0l and ancillocy equipment may reDUiio operatiOO:II throughO<Jt 

shutdown. Once the hnzttrdnu.-, wM1e residence time has transpired, operatOr's di!;crction CM be 

applied. 

(Signature of Shift Leader or DcsigD<e) (Date) 

VES012217 
ATTACHMENT 3 

MALFUNCTION RECORD KEEPING FORM 

VES012218 
VEOLIA ENYm.ONMENT AL SERVICES, INC. 

I\-1ALFUNCDON RECORD 

(Page I oft) 

This report POI"tains to . malfunction or Unit 2 I 3 I 4 (circle one). 

The malfunction event occurred oo; 

(MoothiOay!Year, Hows: Minutes) 

'The malfunction event ooocJuded oo: 

{Month!D'•y!Year, Hours: Minutes) 

The total duration of this malfunction evcnl was: 

(Hours : Minutes) 

The Voolia Program Qj Correcri"e Acrioru for Malfunctions must be adhered to for the operating and maimaining 

of the incinentor >)'>~em and for correcting tho cause of the malfu:action. De•cribe lbe malfunction, the 

automated audlor operator response, the potential cause of the malfunction, and the corrootive actioas W:en: 

Waste Focd3 off Time -

l.ttcinerator "CCear of \Vasto" Time 0 0 

Wore all actioOJ OW<J<:iated with this malfunction event in conformance ,..itb the SSM.P'I Yes I No (circle one). 

If no. iniLJatc an immediate starrup. sbutdo"'n, ond malfunction report. 

Ustldescribc dle cxceedances that oeeurrod (or believed to bave occurred) due to tl1is rnulfunction: 

Notes/Rccommeodations: 

The following oignature certifies the accuracy of this record: 

(JIIame) 

(Si&DAture) (Date) 

VES012219 
ATIACHMENT 4 

PROGRAM OF CORRECTIVE 

ACTIONS FOR .MALFUNCTIONS 

VES012220 
1.0 GENllRAL 

PROGRAM OF CORRECTIVE 

ACTIONS FOR MALFUNCTIONS 

TABLE OF CONTENTS 

1.1 Operuing and Maintaining the S)'l'tem during Malftmetioos 

I .2 Loss of Electrical Pow.r Supply 

1.3 l..oss of Wirumeni/Piant Air Supply 

1.4 Loa of Plant NitrOgen Supply 

l.S Loss of City Watet Supply 

1.6 Los• of Process Water Pressure/Flow (Unh 4) 

I .7 Mnlllmctioo of Safety Interlock or Automatic Waste Feed Cutoll' Interlock 

I .8 Jlxc:euivc Air In-leakage in Air Pollution Control System 

2.0 PRIMARY COMBUSTION CHAMBER 

2.1 l..c><o of Natural Gas Prcssurell'low 10 PCC Main Burner 

2.2 Loa of Combustion Air l'ressur<IFJow to PCC 

2.3 PCC Main Burner Pilot Failuro 

2.4 Loss of Waste Row to PCC Injector 

2.S Loss ofWute feedr.lte Control to PCC 1'1iector 

2.6 L<>ss of Atomi2>tion Air Pressure to • PCC Jn,jector 

2.7 L<>ss ofPCC Draft Control (Unit 4) 

2.8 Loss ofPCC Temperature Conorol 

2.9 f lame Failure 

2.10 Kiln .Rotation Malfunction (Unit 4) 

2.11 BullciCharge Feed Door Malfunction 

2.12 PhysicaliMecbanieal lntcmal Equipment Failure 

2.13 PCC Seal Visual Emissions Monitoring and Recording S)'l'tcm 

2.14 Rapid Steam Generation from Asb Collection System Wota 

3.0 SECONDARY COMBUSTION CHA"IBER 

3.1 L<>ss ofNarural Gas Prcssurei'Flow to SCC Main Burner 

3.2 1..<>55 of Combustion Air Pressurei'Flow to SCC 

3.3 sec Main Burner l&nition Failure 

3.4 L.OSI of Waste· Flow "' sec Injector (Unit 4) 

3.S LoM of Waste Feedrato Control to SCC Injector (Unit 4) 

3.6 Loto of Atomization Air Pros.sure to a SCC lqjcotor 

3.7 J..oos of SCC Temperature Control 

3.8 Flame Failure 

3.9 Physicai/Mecbanical lntemal Equiptnetll Failure 

3.10 L<>w Wa1<:r LeYe! in Stag Collection S}'Siem (Umt 4) 

3.11 Emugeooy Safety V<nt Opening 

3.12 R.opid Steam Gtneration from Ash Collnction System Water 

4.0 TEMPERING CHAMBER (UNJT 4} 

4. J Lo.s ofTempcring Chamber &it o., Temperature Control 

4.2 Loss of Atomization Air Pressore to Nozzle 

5.0 LIME SLUlUlY SYSTEM 

5.1. l.o.<• of Lime Feed to lime Slurry f <ed l'snk 

S.2. Molf\mction in Lime Slurry Concentration 

6.0 UNITS 2 AND 3 SPRAY DRYE!t ABSORBER (SDA) 

6.1. Loss of Lime Sluay Flow to SDJ\ 

VESOI2221 
6.2. Los. of Lime Sluny flow Conlrol 

6.3. l.oos of Crty Water Fk>w 10 SDA (Unil 2 at>d 3) 

6.4. Loos of Cooling Air Flow 10 Atomizer 

6.5. Loss ofSDA Exit Gas Temperature Corurol 

6.6. AlOmizcr Failllnl 

7.0 UNIT4 SPRAY DRYER ABSORBER (SDA) 

7.1. Loss ofUn>e StunyFlowto SDA 

7 .2. Lo .. of Lime Sluny Flow Con~rol1Elti1 Gu Temperature Conttol 

7.3. loss of Atomi2ation AirPressu"' 10 SOA Nozzle 

8.0 CARBON INJECTION SYSTEM (UNIT 4) 

8.1. l.os• of Carrier Gas Pressure 

8.2. l.c<ls/Reslricrion of Activated Carbon Flow 

8.3. Loss of Plant Air Pressure/Flow to Carbon Bulk Sock 

9.0 BAGHOUSE & INDUCED DRAFT (!D) FAN 

9 .I. Tonlll..calcin8 Bag 

9.2. a., Blindio&fliigb-Higb l'rcssln Drop 

9.3. loss ofSillc.k. Gas Flowrate ContJOI (Unit 2 and 3) 

9.4. B•gbouse Isolation Damper Malfunction (Uni1 4) 

9.5. m Fan failure 

I 0.0 CONTROL SYSTEM/CONTINUOUS MONITORING SYSTEM 

JO. 1. Cootrol SystcmfContinuous Monitoring System Malfunction 

10.2. Contlnoous Emissions Monitoring System Mol function 

VES012222 
VEOLJA ENVIRONMENTAL SERVICES, INC. 

PROGRAM: OF CORREC fiVE ACflONS FOR MALFUNCTTONS 

1.0 GENERAL 

1.1. Opera ting and Maintaining the System during Malfunctions 

1.1.1. Due to the sudden, .infrequent, and unusual conditions associated 

with malfunctions, continually evaluate the situation. Using 

discretion, respond in a manner consistent with safety and good air 

pollution control practices. 

1.1.2. Take the following actions to minimize the release of hazardous air 

pollutants 

1.1.2.1. Cutoff all waste feeds and/or confirm that tiJc automatic 

waste feed cutoff system functioned properly. 

1.1.2.2. 

1.1.2.3. 

Maintain operating parameters within limits, if possible. 

If applicable, follow the procedures provided by the 

Emergency Safety Vent Plan 

1.1.3. Keep supervisor and/or maintenance supervisor informed, as 

appropriate. 

J.l.4. Identify the malfunction and potential cause. 

1.1.5. Implement corrective actions involving the troubleshooting of 

failures and the servicing and/or replacing of components, as 

needed. Refer to manufacture's troubleshooting and service 

recommendations, as needed. 

1.1.6. Record the appropriate information using a malfw1etion record 

form. 

1.2. Loss of Electrical Power Supply 

1.2.1. Verify proper failure position of actuated valves. 

12.2. Identify link in power supply path that is not operational. 

1.2.3. Take the necessary actions to restore the supply of electrical 

power. 

1.3. Loss of Instrument/Plant Air Supply 

1.3.1. Verify proper failure position of actuated valves. 

1.3.2. In case of plugging/physical failure of line or line components: 

1.3.2.1. Identify the location/cause of the restriction of 

instrument air flow. 

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

co ponet~ts, as needed. 

Page I of26 

VES012223 
\ 'EOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

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

1.3.3.1. Identify cause of actuation failure. 

1.3.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

I .3.3.3. Service/replace actuator and/or valve components, as 

needed. 

I .3.4. In case of mechanical/electrical fuilure at air supply source: 

1.3.4.1. Identify the cause of the fuilure. 

1.3.4.2. Tnke the necessary actions to restore the supply of 

instrument/plant air. 

1.4. Loss of Plant Nitrogen Supply 

1.4.1. In case of plugginglph)'l>ical failure of line or line components: 

1.4. 1.1 . Identify the location/cause of the restriction of nitrogen 

flow. 

1.4.1.2. Clear line plugging andfor service/replace flmlty line 

components, as needed. 

1.4.2. fn case of mechanical/electrical failure of actuated valve: 

1.4.2.1. Identify cause of actuation failure. 

1.4.2.2. Service/replace electrical and/or pneumatic 

components, as needed. 

1.4.2.3. Service/replace actuator and/or wive components, as 

needed. 

1.4.3. 1n case of mechanical/electrical failure at nitrogen supply source: 

1.4.3.1. Identify the cause of the failure. 

1.4.3.2. Take the necessary actions to restore the supply of 

nitrogen. 

1.5. Loss of City Wntcr Supply 

1.5.1. In case of plugging/physical failure of line or line components: 

1.5.1.1 . ld.cnttfY the location ofpiugging or line f11ilw·e. 

1.5.1.2. Clear line plugging and/or servicclrcplacc faulty line 

components, as needed. 

I .5.2. In CIISC of mcchnnicallel~cal failure of ac.tuated valve: 

1.5.2. I. Identify cause of nctuation failure. 

1.5.2.2. Service/replace electrical andlo.r pneumatic 

components, as needed. 

Page 2 of26 

VES012224 
VEOLlA RNVlROllo'l\fEJ\'TAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MA.LFUNCTIONS 

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

needed. 

1.5.3. In case ofmecbanicaVelectrical failure at city water supply source: 

1.5.3.1 . Identify the cause oftbe failure. 

1.5.3.2. Take the necessary actions to restore 01e SUI>ply of city 

water. 

1.6. Loss of Process Water Pr essure/Flow (Unit 4) 

1.6.1. For loss of city water supply to process water tank, see I.S. 

!.6.2. In case of mecbanicaVelectrical failure of process wnter pwnp: 

1.6.2. 1. Diagnose pwnp/drive failure. 

1.6.2.2. Service/replace the pump/drive, as needed. 

1.6.2.3. Restore electrical power supply to the pump. 

1.6.3. 1n case of plugging/physical failure of line or line components: 

1.6.3.1. Identify the location of plugging or line faih1re. 

1.6.3.2. Clear line plugging and/or service/replace faldty line 

components, as needed. 

1.6.4. In case of mechanicaVelectrical failure of actuated valve: 

1.6.4.1 . Identify cause of actuation fuilure. 

1.6.4.2. Service/replace electrical and/or pneumatic 

components, as needed. 

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

needed. 

1.6.5. 1n case of pbysicaVelectrical fuilure of control system component: 

1.6.5.1. Identify fuuliy control system component. 

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

1.7. Malfunction of Safety Interlock or Automatic Waste Feed Cutoff 

Interlock 

1.7 .I. If safety interlock or A WFCO interlock was erroneously triggered, 

proceed with corrective actions. 

1. 7 .2. If safety or A WFCO condition exists but automated response 

failed, cutoff waste feed as quickly as possible, then proceed with 

corrective actions. 

1.7 .3. 1n case of physical/electrical failure of instrwncntalion: 

1.7.3.1. Identify fuulty instrumentation component. 

1.7.3.2. Service/replace fuulty instrumentation components, as 

needed. 

Page3 of26 

VES012225 
VEOUA ENVIRONMENTAL SERVICES, INC. 

ROGRAM~ OF CORRECTIVE ACfiONS FOR MALFUNCTIONS 

1.7 .4. In case of mechanicaVelectrical failure of actuated valve/damper: 

1.7 .4.1. ldwti fy cause of actuation failure. 

1.7.4.2. Service/replace electJical and/or pneumatic 

components, as needed. 

1.7 .4.3. Service/replace actuator and/or valve components, as 

needed. 

1.7.5. In caseofphysical/cl.ecbical failure of control system component: 

1.7.5.1. Identify faulty control system component. 

1.7.5.2 Service/replace control system components, as needed. 

1.8. Excessive Air ln-lea.kage in Air Poll11tion Control Systrm 

1.8.1 In case of 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, man ways, 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. 

Page 4 of26 

VES012226 
VEOLIA £ NVIRONJ\Il£NTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTlONS 

2.0 PRIMARY COMBUSTION CEIAI\IDER . 

2.1. Loss of Na tural Gas Pressure/Flow to PCC Main Burner 

2.1.1. ln. case of plugging/physical fitilure of line or line component: 

2.1.1.1. Identify the location of plugging or line failure. 

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

components, as needed. 

2.1.2. In case o f mechanical! electrical failure of actuated valve: 

2.1.2.1. Identify cause of actuation failure. 

2.1.2.2. Service/replace electrical and/or pneumatic 

components, as needed. 

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

needed. 

2.1.3. In case ofphysical/olcctrical 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 mechanical/electrical failure at natural gas supply 

scurce: 

2.1.4.1. Identify tbe cause of the failure. 

2.1.4.2. Take the necessary actions to restore the supply of 

natural gas. 

2.2. Loss of Combustiou Air Pressure/Flow to PCC 

2.2.1. Jn case of mcchanical!electrical failure of combustion air blower: 

2.2. 1.1. Diagnose blower/drive failure. 

2.2.1.2. Service/replace the blower/drive, 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 o f mechanical/electrical failure o f actuated valve: 

2.2.3.1. Identify cause of actuation fitilure. 

2.2.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

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

needed. 

Page 5 of26 

VES012227 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTLY£ ACTIONS FOR M..4LFU CTfONS 

2.2.4. In case ofphysicaVelectrical failure of control system component: 

2.2.4.1. Identify faulty control system component 

2.2.4.2. Service/replace control syste1n components, as neildcd. 

2.3. PCC Main Bumcr Pilot Failure 

2.3.1. For loss ofoarural gas pressure/flow, see 2.1. 

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

2.3.3. In case of physicalfelectrical failure of igniter: 

2.3.3.1. Identify cause of igniter failure. 

2.3.3.2. SCI'\oicelreplace igniter and/or associated components, 

as needed. 

2.3.4. In ca.<~e of pbysicaVelectrical failure of control system component: 

2.3 .4.1. Identify faulty control system component. 

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

2.4. Loss of Waste Flow to l'CC Injector 

2.4.1. In case of mechanical/electrical failure of waste feed pump: 

2.4.1.1 . Diagnose pump/drive failure-. 

2.4.1.2. 

2.4.1.3. 

Service/replace th.e pump/drive, as needed. 

Restore electrical power supply to the pump. 

2.4.2. In coseoflow nitrogen pressure, see 1.4. 

2.4.3. In case of pluggiuglphyl;ical failure ofline or line component: 

2.4.3.1. Identify the location of plugging or line foilure. 

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

components, as needed. 

2.4.3.3. Restore/confirm functional heat tracing, if applicable. 

2.4.4. In case ofmecbanicol/electrical failure of actuated valve: 

2.4.4.1 . Identify cause of actuation fuilure. 

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 

needed. 

2.4.5. In case of pbysicaVelectrical failure of control system component: 

2.4.5.1. Identify faulty control system component. 

2.4.5.2. Service/replace cont'rol system components, as needed. 

:2.5. Loss of Waste Feedrate Control to PCC Injector 

2.5.1. In case of loss of waste. preasurelflow to PCC injector, see 2.4. 

Page 6 of26 

VES012228 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM O F CORRECTIVE ACTIONS FOR MALFUNCTIONS 

2.5 .2. In case of physicallelectrical failure of flow transmitter: 

Service/replace flow transmitter and/or associated instntmentation, 

a~ needed. 

2.5.3. In case of actuated valve failure: 

2.5.3.1. Identify cause of actuation fuilure. 

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 of ph)'llical/electrical failure of control system component: 

2.5.4.1. Identify fuulty onntrol system component. 

2.5.4.2. Scrvicelrcplace control system components, as needed. 

1.6. Loss of Atomlzadon Air P ressure to a PCC Injector 

2.6.1. For n total loss of plant/instrument air supply, see 1.3. 

2.6.2. In case of pluggiog/physical failure of line or line component: 

2.6.2. I. Identify the location of plugging or line filihn'l). 

2.6.2.2. Clear line plugging and/o( service/replace faulty line 

components, as needed. 

2.6.3. In case of mecbanicallphysical failure of pressure onntrol valve: 

Service/rep! Bee pressure control valve, as needed. 

2.7. Loss or PCC Draft Control (Urut 4) 

2.7 .I. In case ofiD fan failure, see 9.5 

2. 7 .2. In case of ph}'llical/electrical failure of kiln pressure transmitter: 

Service/replace pressure transmitter and/or associated 

instrumentation, as needed. 

2.7.3. ln case ofuctuated damper failure: 

2.7.3.1. Identify cause of actuation failure. 

2.7.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

2.7.3.3. Service/replace actuator and/or damper onmponents, as 

needed. 

2.7.4. lo case ofph)'llicallelectrical failure of control system onmponeot: 

2.7.4.1. Identify faulty control system onmponenl 

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

Page 7 of26 

VES012229 
VEOLIA ENVIRONMENTAL SERVICF.S, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

2.8. Loss of PCC Temperature Control 

2.8.1. In case of loss of natural gas pressure/flow to main burner, see 2.1. 

2.8.2. In case ofloss of waste pressure/flow to PCC injector, see 2.4. 

2.8.3. In case of physical/electricnl fltilure of temperature elt.1nent: 

2.8.3.1. Service/replace faulty temperature element and/or 

associated instrumentation, as needed. 

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

2.8.4.1. Identify faulty control system component 

2.8.4.2. Service/replace control system compon.ents, ns needed. 

2.9. Flame Failure 

2.9.1. In case of physical/electrical failure of flame detector: 

2.9.1.1. Identify faulty flame detector component. 

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

2.9 .2. In case of physieal/electrical failure of control system component 

2.9.2.1. Identify faulty control system component. 

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

2.10. KJJn Rotation M alfunction (Unit 4) 

2.1 0.1. In case of mechnnicalfelectrical kiln drive system: 

2.10.1.1. Diagnose drive failure. 

2.1 0.1.2. Servicclreplace the drive, as needed. 

2.1 0.1.3. Restore electrical powa supply to motor. 

2.10.2. ln case of physicalfelectrical failure of kiln rotational speed 

transmitter: Servicefreplace traru.'mitter andfor associated 

ins1.rwnentation, as needed. 

2.1 0.3. In case of pbysicaVelectrical failure of control system component: 

2.1 0.3. J. Identify faulty control system component. 

2.10.3.2. Service/replace control system components, ns needed. 

2.11. Bulk/Charge Feed Door Malfunction 

2.1 1.1. In case of mecbanicalfelectrical failure of actuated door: 

2.11.1.1. ldenti fy cause of actuation failure. 

2.11. 1.2. Serviec/replace electrical, hydraulic, andfor pneumatic 

components, as oeeded. 

2.1 1.1.3. Service/replace actuator andfor valve components, as 

needed. 

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

PageS of26 

VES012230 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAi'f. OF CORRECT£\'E ACTIONS FOR MALFUNCTIONS 

2.11.2. 1. Identify faulty control system component. 

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

2.12. Physicai/Mecb•nlcallntcroal Equipment Failure 

2.12.1. In case of refractory failure, repair/replace refracto•y 

2.12.2. In case of ash coll~ction failure 

2.12.2.1. Diagnose ash collection system failure 

2.12.2.2. Service/replace ash collection system components, as 

needed. 

2.13. PCC Seal Visual Emissions Monitoring and Recording System 

2.13.1. In case of physical/electrical failure of camera, service/replace 

camera. 

2.13.2. In case of physical/electrical failwe of monitor, servicc!replace 

monitor. 

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

service/replace recording system. 

2.14. Rapid Steam Generation f•'Om Ash Collection System Water 

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

2.14.2. In case of uncontrolled movement/dropping of residue into ash 

collection system water, inspect system to identify/remove other 

suspect material. 

Page 9 of26 

VES012231 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

3.0 SECONDARY COMBUSTION CHAMBER 

3.1. Loss of Na tural Gas Pressun/ Ftow to SCC Main Burner 

3.1.1. In case of pluggjoglpbysical failure ofline or line component: 

3.1.1.1. Identify the location of plugging or line failure. 

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

components, as needed. 

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

3.1.2.1. 

3.1.2.2. 

Identify cause of actuation failure. 

Service/replace electrical and/or 

components, as needed. 

pnew:natic 

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

needed. 

3.1 .3. In case ofphysical!electrical failure of control system component 

3.1.3. I. Identify faulty control system component. 

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

3.1.4. In case of mechanical/electrical failure at natural gas supply 

source: 

3.1.4.1. 

3.1.4.2. 

Identify the cause of the failure. 

Toke the necessary actions to restore the supply of 

natural gas. 

3.2. Loss of Combustion Air Pressure/Flow to SCC 

3.2.1. In case of mechnnical!clectrical failure of combustion air blower: 

3.2.1.1. Diagnose blower/drive failure. 

3.2.1.2. SeJVicelrcplace the blower/drive, us needed. 

3.2.1.3. Restore electrical power supply to the blower. 

3.2.2. In case of physical failure combustion air duct: 

3.22.1. Identify the location of duct failure. 

3.2.2.2. Service/replace faulty duct, as needed. 

3.2.3. In case ofmcchan.ical!electrical failure of actuated valve: 

3.2.3.1. Identify cause of actuation failure. 

3.2.3.2 . Servicc/roplaco electrical and/or pneumatic 

components, as needed. 

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

needed. 

Page 10of26 

VES012232 
VEOLIA "ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECflVE ACTIONS FOR 1\>IALFUNCTlONS 

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

3 .2.4. 1. Identify faulty coutrol system component. 

3.2.4.2. S~'t'Vice/replace control system components, as needed. 

3.3. SCC Main Burner Ignition Failure 

3.3.1. For loss of natural 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 pbysical/electrical failure of igniter: 

3.3 .3 .I. Tdeoti fy cause of igniter fai l:ure3.3.3.2. Service/replace igniter and/or associated components, 

as needed. 

3.3.4. In case of pbysicaUe\cctrical 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 ofWnste Flow to SCC Injector (Unit 4) 

3.4.1. In case ofmecbunicaVelectrical failure of waste feed pump: 

3.4. 1.1. Diagnose pump/drive failure. 

3.4. I .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 plugging/physical failure of line or line componoot: 

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/confirm functiorull heat tracing, if applicable. 

3.4.4. In case of meclJanical/electrical failure of actuated valve: 

3.4.4.1. Identify cause of actuation failure. 

3.4.4.2. Service/replace electrical and/or pneumatic 

components, 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. I. Identify tautly control system component. 

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

3.5. Loss of Waste Feed rue Control to SCC Injector (Unit 4) 

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

Page II of26 

VES012233 
VEOLIA E!li'VTRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

3.5.2. In case of physicaVelectrical failw-e of flow transmitter: 

Service/replace flow transmitter and/or associated instrwnentation, 

as needed. 

3.5.3. In case of actuated valve failure: 

3.5.3.1. Identify cause of actuation failure. 

3.5.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

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

nocded. 

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

3.5.4.1. Identify fauJty control system component. 

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

3.6. Loss of Atomization Air Pnssure to a SCC Injector 

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

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

3.6.2.1. ldeutify the location of plugging or line failure. 

3.6.2.2. Clear line plugging and/or service/replace fdulty line 

components, as needed. 

3.6.3. In case of mecbanicallphysical failure of pressure control valve: 

Service/replace pressure control valve, as needed. 

3.7. Loss ofSCC Temperature Control 

3.7.1. In case ofloss of natural gas pressure/flow to main burner, sec 3.1. 

3.7 .2. ln case ofloss of waste pressure/flow to sec injector, see 3.4. 

3.7.3. In case ofphysicaVelectrical failure of temperature elemc.tt: 

3.7.3.1. Service/replace faulty temperature element and/or 

associated instrumentation, as needed. 

3.7.4. [n case of physicaVelectrical failure of contr:ol systen1 component: 

3.7.4.1. Identify fuulty control system componeot. 

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

3.8. Flame Failure 

3.8.1. In case of physicaVclectrical faiJure of flame detector: 

3.8.1.1. Identify faulty flame detector componcnt. 

3.8.1.2. Service/replace flame detector components, as ucedcd. 

3.8.2. In case of physicallelectrical failure of control system component: 

3.8.2.1. Identify faulty control system component. 

Page 12 of26 

VESOI2234 
VEOLIA ENVIRONMENTAL SERVfCES, INC. 

PROGR<\1'\'1 OF CORRECTIVE ACTIONS FOR M ALFONCTJONS 

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

3.9. Pbysicai/Mccbaolcal In ternal Eq uipment Failure 

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

3.10. Low Water Level in Slag Collection System (Unit 4) 

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

3. 10.2. In case of physical/mechanical failure of level controller: 

Service/replace faulty level controller and/or associated 

components, as needed. 

3.10.3. Io case of physical/meclumjcal failure of actuated valve: 

3. 10.3.1. Identify cause of actuation failure. 

3.10.3.2. Service/replace pneumatic com.poncnts, as needed. 

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

needed. 

3.11. Emergency S afety Vent Opening 

3.11.1 . Rcspoud to an cmergettcy safety vent opening in a matUter 

consistent with the Emergency Safety Vent Pla11. 

3.11.2. In case of mechanical failw-e of the actuator: 

3.11.2.l. Identify cause ofactuation failure. 

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

needed. 

3.U. Rapid Steam Genera tion from Ash Collection System Water 

2.14.1. fn case of refrnctory failure, repair/replace refractory. 

2.14.2. In case of uncootroUed movement/dropping of residue into ash 

collection system water, inspect system to identify/remove other 

suspect materi ul. 

Page 13 of26 

VES012235 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRA!\1 OF CORREC11VE ACTIONS FOR !MALFUNCTIONS 

4.0 TEMPERING CHAI\>lBER (UNIT 4) 

4.1. Loss of Tempering Chamber Exit Gas Temperattu·e Control 

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

4.1.2. In case of pbysical/electrical fuilure of How transmitter: 

Sen~cclreplacc flow transmitter and/or associated instrwnentatioo, 

as needed. 

4.1.3. In case of actuated valve failure: 

4.1.3.1. Identify cause of actuation fuilure. 

4. 1.3.2. Scrvicclreplace electrical and/or pneumatic 

components, as needed. 

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

needed. 

4.1.4. In case ofphysicaVelectrical failure of control system component: 

4. 1.4.1. Identify faulty control system component. 

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

4.1 .5. In case of no22.lo failure, service/replace nozzle, as needed. 

4.2. Loss of Atomlzatlon Air Pressure to Noule 

4.2.1. For a tolalloss of plant/instrument air supply, see 1.3. 

4.2.2. In case of plugging/physical failure of line or line component 

4.2.2.1. Identify the location of plugging or line failure. 

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

components, as needed. 

Page 14 of26 

VESOI2236 
VEOLIA ENVIRONMEI\'TAL SERVICES, INC. 

PROGRAM OF CORRECflV£ ACfiONS FOR M ALFUNCfiONS 

5.0 LIME SL URRY SYSTEM 

5.1. Loss ofLlme Feed to Lime Slurry Feed Tank 

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

5.1.1.1. Diai.'IIOSC feeder/drive failure. 

5.1.1.2. Service/replace 1he feeder/drive, as needed. 

5.1.1.3. Reston: electrical power supply to the lime slurry screw 

feeder. 

5.1 .2. In case of mechaoical/electrical failure of lime bin 

activator/vibrator: 

5.1.2.1. Diagnose lime bin activator/vibrator failure. 

5.1.2.2. Service/replace the lime bin activator/vibrator, as 

needed. 

5.1.2.3. Restore electrical power supply to the lime slurry screw 

teeder. 

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

5.1.3.1. Identify the location of plugging or line f-ailure. 

5. 1.3.2. Clear line plugging and/or service/replace faulty line 

components, as needed. 

5.1.4. In case of physical/electrical failure of lime feed controls: 

Sm~ce/replace faulty instrumentation and/or control system 

components, as needed. 

5.2. Malfunction in 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 o f loss of water flow to lime slurry feed tanlc, sec 1.5 

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

5.2.3.1. Diagnose agitator/drive failure. 

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

5.2.3.3. Restore electrical power supply to lho lime slurry 

agitator. 

5.2.4. ln case of physical/electrical failure of insttumentation: 

Service/replace faulty instrumentation, as needed. 

5.2.5. In ease of physical/electrical failure of control system component: 

5.2.5.1. Identify faulty control system component. 

5.2.5.2. Servioelreplace control system components, as needed. 

Page 15 of26 

VES012237 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR IVIALFUNCTIONS 

6.0 UNITS 2 AND 3 SPRAY DRYER ABSORBER (SDA) 

6.1. U!ss ofUme Slurry Flow to SDA 

6.1 .I. In case of mechanicallelectrical failure of lime slurry feed pump: 

6. I. I. I. Diagnose pump/drive failure. 

6.1. 1 .2. Service/replace the pump/drive, ns needed. 

6.1.1.3. Restore electrical power supply to the pump. 

6.1.2. In case ofpluggiogiphysical failure ofline or line component: 

6.1.2.1. Identify the location of plugging or line failure. 

6.1.2.2. Clear line plugging and/or service/replace taulty line 

components, as needed. 

6. 1.2.3. Restore/confirm functional heat tracing, if applicable. 

6.1.3. In case of mechanicallelectrical fuilure. of actuated valve: 

6.1.3.1. Identify cause of actuation failure. 

6.1.3 .2. Service/replace electrical and/or pneumatic 

componenl;l, as needed. 

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

needed. 

6.1.4. In ease of physicallclectrical failure of control system component: 

6.1.4. I. Identify faulty control system component. 

6.1.4.2. Service/replace control system componenlli, as needed. 

6.2. 'Loss of Lime Slurry Flow Control 

6.2.1. ht case of loss of slurry flow to SDA, see 6.1. 

6.2.2. In case of physical/electrical failw-e of flow transmitter: 

Service/replace flow tmnsmitter and/or associated instrumentation, 

as needed. 

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. Servicelrepluce actuator and/or valve components, as 

needed. 

6.2.4. In case of pbysicallelectrical failure of control system component: 

6.2.4. I. Identify faulty control system component 

6.2.4.2. Servicc/reploce control system components, as needed. 

Page 16of26 

VESOl 2238 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

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

6.3.1. In case of total loss of city water supply, see 1.5. 

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

6.3.2. I. ldcnti fy the location of plugging or line failure. 

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

components, as needed. 

6.3.3. In case of mechanicaVelcctrical failure of actuated valve: 

6.3.3. I. 

6.3.3.2. 

Identify cause of actuation failure. 

Service/replace electrical and/or 

components, as needed. 

pneumatic 

6.3.3.3. Sm'icelreplace actuator and/or valve components, as 

needed. 

6.4. Loss of Cooling Air Flow to Atomizer 

6.4. I. In case of mecbanical/electrical fililure of atomizer cooling air 

blower: 

6.4. 1.1. 

6.4. 1.2. 

Diagnose blower/drive failure. 

Service/replace the blower/drive. as needed. 

6.4.1.3. Restore electrical power supply to the blower. 

6.4.2. Ill case of physical fililure of atomizer cooling air duct: 

6.4.2.1. Identify the location of duct failure. 

6.4.2.2. Service/replace faulty duct, as needed. 

6.4.3. In ease of physical/electrical fuilure of control system component: 

6.4.3. I. Identify faulty control system component. 

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

6.5. Loss ofSDA Exit Gas Temperature Control 

6.5.1. In case of loss of city water flow to SDA, see 6.3. 

6.5.2. In case of physical/electrical failure of temperature transmitter: 

Service/replace temperature transmitter and/or nssa<:iated 

instrumentation, as needed. 

6.5.3. Ill case of actuated valve failure: 

6.5.3. I. 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. 

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

Page 17 of26 

VES012239 
VEOLIA ENVfRONMENTAL SERVICES, lNC. 

PROGRAM OF CORRECTIVE ACTI ONS FOR MALFUNCTIONS 

6.5.4.1. ldeotify faulty control system component. 

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

6.6. Atomizer Fallu•·e 

6.6.1. In case of low utomi;oor lubrication oil flow: 

6.6.1.1. Diagnose Ute failure in the lubrication system 

6.6.1.2. Service/replace components of the lubrication syst<.'tll, 

ns needed. 

6.6.2. In case of mccllanicallelectrical failure of atomizer: 

6.6.2.1. Diagnose atomizro'drive failure. 

6.6.2.2. Scrvicclrcplace Ute atomizer/drive, as needed. 

6.6.2.3. Restore electrical power supply to the atomizer. 

6.6.2.4. components, as needed. 

Page 18 of26 

VES012240 
\'EOLIA ENVlRONl\lENTALSERVlCES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

7.0 UNIT 4 SPRAY DRYER ABSORBER (SDA) 

7.1. IA>ss of Lime Slurry Flow to SDA 

7. J .1. In case of mechanical/electrical failure oflime slurry feed pump: 

7 .1.1. I. Diagnose pwnpldrive failure. 

7.1.1.2. Service/replace the pump/drive, as needed. 

7.1.1.3. Restore electrical power supply to the pmnp. 

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

7.1.2.1. Identify the location of plugging or line failure. 

7.1.2.2. Clear line plugging andlor service/replace faulty line 

componentS, as needed. 

7.1.2.3. Restore/confirm fimctional heat tracing, if a.pplicable. 

7.1.3. In case of mcebanicaVelectrical failure of actuated valve: 

7.1.3.1. Identify cause of actuation failure. 

7 .1.3.2. Service/replace electrical and/o•· pneumatic 

components, as needed. 

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

needed. 

7 .1.4. In case of physical/electrical failure of control system component: 

7.1.4.1. Identify faulty control system component. 

7. 1.4.2. Service/replace control system con1poncots, as needed. 

7.1.. Loss of Lime SIDJTY t1ow Control/Exit Gas Temperarurc Control 

7.2.1. In case ofloss of slurry flow to SDA, see 7.1. 

7.2.2. In case of physicallelet:trical failure of flow trao~"lllitter: 

Service/replace flow transmitter and/or associated instnunentatioo, 

as needed. 

7.2.3. In case of actuated valve failure: 

7 .2.3.1. Tdcntify cause of actuation failure. 

7 .2.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

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

needed. 

7 .2.4. In case of physicaVclectrical failure of control system component: 

7.2.4. I. Identify faulty control system component. 

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

Page 19 of26 

VESOI2241 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ActiONS FOR MALFUNCTIONS 

7.3. Loss of Atomization Air Pressure to SDA Nozzle 

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

7 .3.2. In case of pluggj1lg/pbysical failure ofline or line component 

7.3.2.1. Jdentify the location of plugging or line failure. 

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

components, as needed. 

Page 20 of26 

VES0 12242 
VEOLIA ENVlRONMEJ\'TALSERVICES, INC. 

PROGRAM OF CORRECIWE ACf!ONS FOR MA.LFUNCfJONS 

8.0 CARBON INJECTION SYSTEM (UNIT 4) 

8.1. Loss of Carrier Gas Pressure 

8.1.1. In case of rnechanicnl/electrical failure of carbon iJ1jcction air 

blower: 

8.1.1.1. Diagnose blower/drive failure. 

8. I . 1.2. Service/replace the blower/drive, as needed. 

8.1.1.3. Restore electrical power supply to the blower. 

8.1.2. In case of physical failure air duct 

8.1 .2.1. Identify the location of duct fnilure. 

8.1.2.2. Service/replace faulty duct, as needed. 

8.1.3. In case of physical/electrical frulure of control system component: 

8.1.3 .1. Identify faulty control system component. 

8.1.3.2. Service/replace control system components, ns needed 

8.2. Loss/Restriction of Activated Carbon Flow 

8.2.1 . In case of loss of plant air to carbon bulk sack, sec 8.3 

8.2.2. In case of mochanical/electrical 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 power supply to the carlx>n feeder. 

8.2.3. In case of pluggingfpbysical failure of line or line component: 

8.2.3.1. Identify the location of plugging or line failure. 

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

components, as needed. 

8.2.3.3. Restore/confirm functional heat tracing, if RJ>plicable. 

8.3. Loss of Plant Alr Pressure/Flow to Carbon Bulk Sack 

8.3.1. For a total loss of plant/instrument air supply, sec 1.3. 

8.3.2. In case ofpluggingfpbysical failure ofline or line component: 

8.3.2.1. Identify the location of plugging or line failure. 

8.3.2.2. Clear line plugging aod/or service/replace faulty line 

components, as needed. 

8.3.3. lo case of mechanical/electrical failure of actuated valve: 

8.3.3.1. Identify cause of actuation failure. 

8.3.3.2. Service/replace electrical and/or pneumatic 

components, as needed. 

Page 21 of26 

YES012243 
VEOLIA ENVTROl\'1\ NTAL SERVICES, INC. 

PROGRAM OF CORRECTI VE ACTIONS FOR MALFUNCTIONS 

8.3.3.3. Service/replace aelllator andJ'or valve components, as 

needed. 

8.3.4. In caw of physical/electrical failure of control system component: 

8.3.4 .I. Jdeotizy faulty control system component. 

8.3.4.2. Service/replace control system components, ns oeedcd. 

Page22 of26 

YES012244 
VEOUA ENVIRONMENTAL SERVICES, lNC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

9.0 BAGHOUSE & INDUCED DRAFT (ID) FAN 

9.1. Toro/I.Alaking Bag 

9.1.1. In case of a baghouso leak detection alarm, follow the relevant 

corrective measures prescribed in tbe Operation and MaintenWlce 

Plan. 

9.1.2. In case of a baghouse leak detection system failure: 

9.1.2.1. Servieelreplace tom/leaking ba,g(s), as needed. 

9.1.2.2. 

9.1.2.3. 

Diagnose the failure of tbe bsghouse detection system. 

Service/replace baghouse leak dCicetion system, as 

needed. 

9.2. Bag Bllildiog/High-Big}J Pressure Drop 

9.2.1. In case of low baghouse inlet gas temperature: 

9.2.1 .1. Follow the appropriate corrective actions prescribed by 

paragraph 6.5 (Unit 2 and 3) 

9.2.1.2. Follow tbe appropriate corrective actions prescribed by 

paragraph 7.2 (Unit 4) 

9.2.1.3. Perfonn baghouse inspection. 

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

9.3. L-oss of Stack Gas Flowrate Control (Unill and 3) 

9.3.1. In case ofiD fun failure, see 9.5 

9.3.2. In case of pbysieal/electrical failure of flow lTansmitter: 

Service/replace ·flow transmitter and/or associated instn~mcntation, 

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 oomponcnt 

9.3.4.1. Identify faulty control system component 

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

9.4. Bagbouse Isolation Damper M.alfunction (Unit 4} 

9.4. I. In case of actuated damper failure: 

Page 23 of26 

VES012245 
VE.OLIA ENVIRONI\1ENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACfiONS 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. In case of physicaVelectrical fai.lure of control system component: 

9.4.2.1. Identify faulty control system component. 

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

9.5. ID Fan Failu.re 

9.5.1. In case ofmecbarucallelectrical failure ofiD fan: 

9.5.1 . 1. Diagnose fan/drive failure. 

9.5.1 .2. Service/replace the fan/drive, as needed. 

9.5. 1 .3. Restore electrical power supply to the lD fan. 

Page24 of26 

VES012246 
VEOLIA ENVIRONMENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS 

10.0 CONTROL SYSTEM/CONTINUOUS MONITORING SYSTEM 

10.1. Control System/Continuous Monitoring System Malfunction 

I 0.1. I. As needed, refer to the CMS QAIQC Plan for guidance and to 

ensw·e that proper calibrations are perfonned. 

I 0.12. In case of physical/electrical failure of instrumentation: 

I 0. 1.2.1. IdentifY faulty instrumentation component. 

10.1.2.2. Service/replace faulty instrumentation components, as 

needed. 

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

10.1.3.1. IdentifY faulty control system component. 

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

I 0.1.4. In case of physicallelectrical failure of data acquisition/availability: 

10.1.4.1. Identify faulty data system components. 

I 0.1.4.2. Service/replace data system components, as needed. 

10.2. Continuous Emissions MonJtorlng System Malfunction 

1 0.2.1. As needed, refer to the CEMS QAIQC Plan for guidance and to 

ensure that proper calibrations are performed and that t11e 

appropriate performance specifications are met. 

I 0.2.2. In case of physical!electrical failure wnbilical heat tracing: 

I 0.2.2.1. Diagnose failure of heat tracing. 

I 0.2.2.2. Replace/restore heat traced sample umbilical. 

I 0.2.3. In case of mechanical/ele<.irical failure of heated vacuum pump: 

10.2.3. I. Diagnose pump/drive failure. 

I 0.2.3.2. Service/replace the pump/drive, as needed. 

10.2.3.3. Replace/restore pump head heat source. 

10.2.3.4. Restore electticnl power supply to heated vacuum 

pump. 

I 0.2.4. In case of plugging/physical failure of sample probelnmbilical: 

1 0.2.4. I. Identify the location offailure. 

10.2.4.2. Clear plugging and/or service/replace faulty 

components, as needed. 

l 0.2.5. In case of mechanicnl/electrical failure of actuated valve: 

1 0.2.5.1. Identify cause of actuation failure. 

Page25 of 26 

VES012247 
VEOLL"\ EI'I'VJ:RONl\1ENTAL SERVICES, INC. 

PROGRAM OF CORRECTIVE ACI'IONS FOR MALFUNCTIONS 

I 0.2.5.2. Service/replace electrical and/or pneumatic 

componeniS, as needed. 

10.2.5.3. Service/replace actuator and/or valve componeniS, as 

needed. 

I 0.2.6. h1 case of mechanical/electrical failure of analyzer: 

I 0.2.6. I. Refer to manufacturer's service manual for guidance on 

troubleshooting and servicing analyzer. 

I 0.2.6.2. Scn~celrep ace analyzer, as needed. 

10.2.7. In case of mecbanicaVelectrical failure of associated 

insnumcntation: 

I 0.2. 7.1, Identify faulty instrumentation component. 

1 0.2.7.2. Service/replace faulty instrumentation components, as 

needed. 

10.2.8. In ca.o;e of physical/electrical failure of control system oomponcot: 

I 0.2.8.1. Identify fiwlty control system component 

I 0.2.8.2. Service/replace control system components, as needed. 

Puge26 of26 

VES012248 
VES012249.pdf 
APl'ENDIXH 

AUTOMATIC WASTE FRED CUTOFF l'LAN 

VES012249 
AUTOMATIC WASTE FEED CUTOFF PLAN 

Prepared for: 

Veolia ES Technical Solutions, LLC 

Sauget, illinois 

Pn.,nred by. 

Franklin Engineering Group, Inc. 

Franklin, Tennessee 

Octobtr 2008 

VESOI2250 
TABLE OF CONTENTS 

1.0 INTRODUCTION A.'iD 11.<\CKCRotJ:-ID ............................ _ ... , .... - ......... - ........ _ .... , ..... 1 

1.1 SUMMARY OF FACILITY INFORMATION ......................................................... I 

1.1.1 Fixed Hearth Incinerators ............................................................... I 

1.1.2 Rotary Kiln lncineraror .................................................................... 2 

1.2 DESCIUJ"l'JON OF THE A WFCO SYSTEM ....................................................... .5 

2.0 AWFCO OPERAlliLITY 'fEST PROCEDURES ................ - .......... - ....... - ......... - ......... 11 

3.0 JU:SPONCE TO AN AWFCO EVENT ........... - .. - ...... - .... - .......... - .......... - ..................... 12 

3.1 REPORTING REQUlREM.EI<TS ....................................................................... 13 

4.0 MANUAL WASTE FEED Clff·OFF PROCEDCR.ES-.... - ........... - .... - ........... - .- · ... 14 

ii 

VES01225 1 
UST OF TABLES 

TABLE 1-1 REGULATORY REQUIREMENTS FOR AN A WFCO PLAN AND 

CORRllSPONDINO SECTION THAT ADORJ>SSES THE REQUIR£Milm' ............... .4 

TABLE 1-2 AUTOMA'fiCWASTE FilED CUTOFF INTF.RI.OCKS .......................................... 6 

iu 

VESOI2252 
1.0 INTRODUCfiON AND BACKGROUND 

Veolia ES Technical Solutions, LLC (Vcolia) owns and operates two fixed hearth 

incinerators (Units 2 and 3) and a rotary lciln incinerator (Unit 4} at its facility located in 

Sauget, Illinois. These incinerators are subject to the National Emissions Standards for 

Hazardous Air Pollutants (NESHAP) for Hazardous Waste Combustors (HWCs), Part 63, 

Subpart EEE (§§63.1200 to 63.1221). The NESEIAP for HWCs specifies anissions 

standards which reflect emissions perfonnance of maximum achievable control 

technologies (MACI'), and is conunonly referred to as the HWC MACf. 

Hazardous Waste Combustors are required to have a functioning system that immediately 

and automatically cuts off the hazardous waste feed under certain conditions. The 

Automatic Waste Feed Cut-Off (A WFCO) System must follow the requirements 

described in 40 CFR 63.1206(c)(3). This Automatic Waste Feed Cut-Off Plan 

demonstrates Veolia's compliance with these requirements. 

This plan includes iufom1ation about A WFCO systems, procedures for responding to an 

A WFCO event, and procedures for testing the operability of the A WFCO systems. Table 

1·1 presents tl:le regulatory references related to A WFCO Plans and the section of this plan 

that addresses each specific reqoirement. 

Due to the similarity of the three AWFCO systems (one for each incinerator system}, 

general references to an A WFCO system or incinerator system in this document will 

imply all three systems. Information that is only applicable to one or two of the three 

systems "ill be clearly identified. 

1.1 Summary of Facility Information 

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

incinerator are presented in this section. 

1.1.1 Fixed Hearth lndllerators 

Each of the fixed hearth incinerators includes the following components: 

• Feed equipment 

• Primary and secondary combustion chambers 

• Lime injection system 

• Spray dryer absorber (SDA) 

I 

VES012253 
• Fabric filter baghousc 

• Solids and asb removal systems 

• Induced draft (ID) fan and stAclc 

• Instrumentation, controls, and data acquisition systems 

Various solid and liquid wastes and gaseous ftedstreams are thermally treated in the 

fixed hearth incinerators. Solid waste is fed to the primary (lower) combustion chamber 

via a feed conveyor system and pneumatic ram. Liquid waste from tanks and tanker 

1n1cks 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 fccdstrcam is fed to the Unit 2 primary combustio.o 

chamber directly from gas cylinden. Off gases from a hooded feed emission control 

system and from a waste handling glove box are fed dinctly to the Unit 3 secondary 

combustion chamber. Combustion chamber temperatures ere maintained using natural 

gas fired to a dedicated burner in both tho primnry and secondary chambers. 

Combustion gu~ exits the secondary combustion chamber and enters the SDA, which 

provides ucid gas removal and cooling of the combustion gas. Combustion gas exits the 

SDA and is distributed to the fabric filter bagbouses, which provide particulate matter 

removal. The induted draft fan, located downstream of the ba,ghouses, moves the 

combustion gas through the system and exhausts the gas through the main staclL 

Hot, wet gas is extracted downstream of tho bagl1ouse through a continuous emissions 

monitoring system. This system features a multi-component infrared gas analyzer that 

detects hydrogen chloride, carbon monoxide, and water vapor conoontrntions. An 

integrated zirconium oxide-based analyzer detects oxygen concentration.~ . 

1.1.2 Rotary Kiln Incineralor 

The rotary kiln incinerator includes the following components: 

• Waste feed system 

• Primary and secondary combustion chambers 

• Tempering chainber 

• Lime iJ\iection system 

• Spray dryer absorber 

• Carnon injection system 

• Fabric filter bagbouse 

2 

VESOJ2254 
• Solids and ash removal systems 

• 10 :fun and stack 

• Instrumentation, controls, and data acquisition systems 

Various solid and liquid wastes are thennally treated in the rotary kiln incinerator. Solid 

wastes are fed to a ram feeder via a clarosheU, a dnnn feed conveyor, and an auxiliary 

feed conveyor. A hydraulic ram pushes the solid waste into the kiln. 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 tempering 

chamber, which provides cooling of the combustion gases. TI1e combustion gas exits tbe 

tempering chamber and is distributed between two identical SDAs, which provide acid 

gas removal and additional gas cooling. A carbon injection system is utilized for 

controlling dioxinlfuran and mercury emissions. The activated carbon is air injected into 

the combustion gas immediately downstream of the convergence of combustion gases 

from the SDAs. From the SDAs, combustion gas is distributed to fabric filter bagbouses, 

which provide particulate matter removal. The ID fan, located downstream of the 

baghouses, moves the combustion gas through the system and exhausts the gas through 

the main stack. 

Hot, wet gas is extracted downstream of the 10 fan through a continuous emissions 

monitoring system. This system features a multi-component infrared gas analyzer that 

detects hydrogen chloride, carbon monoKide, and water vapor concentrations. An 

integrated zirconium oxide-based analyzer detects oxygen concentrations. 

3 

VES012255 
Table 1·1 

Regulatory Requirements for A WFCO Plan and 

Corresponding Section that Addresses the Requirement 

Regulatory Citation Description 

§ 63.1206(c)(3)(i) Facility must have a functioning A WFCO system 

System must cut off waste when any of 1he 

§ 63.1206(c)(3)(i)(A) 

following are exceeded: 

(I) Operating Parameter Limit 

(2) Emission standard monitored by CEMS 

{3) Allowable Combustion Chamber Pressure 

§ 63.1206{c)(3)(i){B) System must cut off waste when span value of any 

CMS detector is met or exceeded 

§ 63.1206(c)(3)(i)(C) System must cut off waste upon malfunction of n 

CMS monitoring an OPL or emission level 

§ 63.1206(c)(3)(i)(D) 

Waste cut-off must occur "1ten any component of 

the A WFCO system filils 

§ 63.1206(c)(3)(ii} Dueling of cotnbu~1ion gases 

§ 63.1206{c)(3)(iii) Restarting waste feed 

§ 63.1206(c)(3)(iv) Failure of A WFCO system 

§ 63.1206(c)(3)(v) Corrective m=urcs 

§ 63.1206{c)(3)(vi) Reporting e.xccedancc of emission standard or 

operaling requirement 

§ 63.1206{c)(3)(vii) A WFCO system testing 

§ 63.1206( c}(3)(viii) Rum ping down waste feed 

§ 63.1209(b)(4) 

Interlock s-pan of non-CEMS CMS into tho A WFCO 

system 

4 

Plan Section 

Section 1.0 

{I) Section 1.2 

{2) Section 1.2 

(3) Section 1.2 

Section J .2 

Section 1.2 

Section 1.2 

Section 3.0 

Section 3.0 

Section 4.0 

Section 3.0 

Section 3.1 

SeL'Iion 2.0 

NA 

Section 1.2 

VES012256 
1.2 Description of tlte A WFCO System 

The A WFCO system includes aU hardware and software (i.e., control logic) necessary to 

inunediately and automatically cutoff waste feeds to the incinerator in the event that an 

AWFCO interlock is triggered. Table 1-2 lists the parameter and setpoint for each 

required A WFCO interlock. In addition to the interlocks specified in Tables I -2, the 

following conditions are interlocked with each A WFCO system: 

• The span value of each CMS instrument (except fur a CEMS instrument) 

• CMS Malfunction 

• A WFCO System Malfunction 

A WFCO interlocks ensure that the pneumatically actuated waste feed block valves 

cannot open or remain open wlless aU regulated operating parameters and conditions are 

within limits. Additionally, the waste feed block valves will fail in the closed position if 

there is a loss of electrical power or instrument air supply. The parameters interlocked 

with the A WFCO system are described below in further detail. 

• Max.inturu Pumpable Hazardous Waste Feedrate - Each pumpable hazardous 

waste feed lioe to the incinerator is equipped with a mass flowmeter. The 

pumpable hazardous waste feedrate is continuously calculated as the sum of the 

individual flowrates. Jfthe hourly rolling total (HR1) pumpable hazardous waste 

feedrate meets or exceeds its limit, au A WFCO interlock is triggered. 

• Maximum Total Hazardous Waste Feedr11te - For Units 2 and 3, solid waste is 

fed to the primary combustion chamber via a feed conveyor and pneumatic ram. 

A scale in the feed conveyor monitors the weight of each charge of solid waste. 

For Unit 4, solid wastes are fed to a ram feeder via a clamshell, a drum feed 

conveyor, and an auxiliary feed conveyor. The clamshell empties into a hopper 

equipped with a load cell that monitors each charge weight. The solid feed 

conveyors are· equipped with weigh scalos. For each incinerator, the time between 

charges is used to convert these charge weights to a solid waste feedrate. The 

solid waste feedrate is summed with the pumpable hazardous waste feedrate to 

calculate the total hazardous waste feedrate. lf the HRT of the total hazardous 

waste feedrate meets or exceeds its limit, an A WFCO interlock is triggered. 

5 

VES012257 
Table 1-2 

Automatic W:l!tt Feed Cutoff Inte.rlocks 

Operatl•ll: Paran~er 

Maximum Pumpoble w.,te Fecdtate 

Ma).imuro Tout! Waste Feed Rate 

Mllltlmum Ash Fcod 1\llte 

Max.imum Cltloriuc/CWoride Feedrate 

Maxitnum Mercury fecdratc Limit 

MO>imum Semi Volatile MemlsFeedrate 

Maximum Total l..ow Volatile Metals feedtate 

Muimum l'wopoble Low Volatile M ... ts f eednne 

Maximum Primary Combustion Cbaroba P,...,.. 

Minimum Prinwy Combus1ioo Cbambcr Temp= tun: 

Mini ~m S«:oodary Combu>rion Cbamber Ternpcnture 

£meraenoy S11fcty Vent Positioo 

Ma.<imum D-sbouse Inlet Tempenuure 

M11xim,un Baa l..eak Oete<:tot Output 

Miounum Carbon Feedrute 

Minimu1n t~rbon feeder Ex.it Pra!S$UTe 

Mrutimum Corboo ClUTier Gas Supply PrtSiUfe 

Maximum Stack OM Flow Rate 

SUlek Gas Carbon Moi.UlXide Coooentration 

Minimum Sotbent Feed Rate 

Minimum Carrier flu:id Flow .Rate 

Not<a: llR.A 

HRT 

12-HRT 

TRV 

- - -

Hoarly Rollil1s AY<nfe 

Hourly Rolling Totol 

12-Hoor Rolling Total 

Tbermal Relief Vent 

A ••••«J.as Period Uuiu 

l{R.T 1blbr 

HR.T lblhr 

12-H.RT lbibr 

12-J·ntt lblhr 

12-J-fRt lblbr 

12-HRT lblhr 

12-10!1' lblhr 

12-HRT iblltr 

IMwn&oeous in. '9.'.C.. 

HRA •r 

HM Of 

JDMI\ntaneollS .. 

HRA •f 

10 ICCOndt %of scale 

Hlt.A lblhr 

Jo Ui i..1000 S psig 

rnstOniCUMJOliS in. w.c. 

Illt.A acfm 

I1RA ppmdv@7%01 

Hlt.A Lbnb Cl2 

llR.A GalllbCI2 

6 

AWFCO lntu!oclc Sttpoiot 

Ullil1./3 Oait4 

3,107 PCC·32561SCC.1 006 

4,017 PCC· 13,7%/SCC-1006 

673 s.1n 

218 252 

0.0047 0.031 

63 6S 

46 $5 

41 47 

>O,OforS- >O.OforSocroods 

1,734 J,so7 

1,849 1,886 

TRY Open Swge Vent Open 

TRVOp0<1 

420 434 

> 30 % for 6 minute:< > 15% for 12 m.in\ltes 

- 6.2 

- 4 

- I 

IS,I47 38,086 

100 100 

1.76 1.01 

1.70 1.61 ---- - - - - -

VESOl2258 
• Ma:dmum Asb Feedrate - The ash concentration of each waste feed is 

detemrined in accordance with the Feedstream Analysis Plan. The CMS uses the 

waste ash concentration and the continuously monitored waste feedrate to 

calculate the ash feedrate of each waste stream. If the 12-hour rolling total (12· 

HRT) of the combined ash feedrate meets or exceeds its limit, an A WFCO 

interlock is triggered. 

• Maximum Chlorine/Cbloride Feedrate • Tho chlorine/chloride concentration of 

each waste feed is detetmined in accordance with the Feedstream Analysis Plan. 

The CMS uses the chlorine/chloride concentration and the continuously 

monitored waste feedrate to calculate the chlorine/chloride feedrate of each waste 

stream. If the 12-HRT of the combined chlorine/chloride feedrate meets or 

exceeds its limit, an A WFCO interlock is triggered. 

• Maximum Mercury Feedrate -The concentration of mercury in each waste feed 

is determined in accordance with the Feedstream Analysis Plan. The CMS uses 

the mercury concentration and the continuously monitored waste feedrate to 

calculate the mercury of eacl1 waste stream. If tho 12-HRT of the combined LVM 

feedrate meets or exceeds its (jmit, an A WFCO interlock is triggered. 

• Maximum SVM Feed.ratc - The concentrations of cadmium and lead in each 

waste teed is determined in accordance with the Feedstream Analysis Plan. The 

semi volatile metals (SVM) concentration io each waste stream is the sum of these 

metal concentrations. The CMS uses the SVM concentration and the 

continuously monitored waste feedrate to calculate the SVM feedrate of each 

waste stream. lflhe 12-HRT of the combined SVM feedrate meets or exceeds its 

limit, an A WFCO interlock is triggered. 

• Maximum Total LVM Feedrate • Tbe concentrations of arsenic, beryllimn, and 

chromium in each waste feed is determined in a<:COrdancc with the Feedstream 

Analysis Plan. The low volatile metals (LVM) concentration in each waste 

stream is the sum of these metal concentrations. The CMS uses the L VM 

concentration and the continuously monitored waste feedrate to calculate the 

LVM feedratc of each waste stream. If the 12-HRT of the combined LVM 

feedrate meets or exceeds its limit, an A WFCO interlock is triggered. 

7 

VES012259 
• Maximum Pumpable LVM f'ced ratc - The LVM feedratc from pumpable 

waste fccdstreams are summed to obtain the combined pumpable L VM feedrate. 

If the 12-HRT pumpable LVM feedrate meets or exceeds its limit, an AWFCO 

interlocl< is triggered. 

• Maximum Primary Combustion Cbamber Pressure -The primary chambers 

for Units 2 and 3 are totally sealed. Both the feed ll!ld disclulrgc cods of the kiln 

(Unit 4) are equipped with nn air pressurized double seal system that is comprised 

of steel spring plates with self-lubricating seal shoes. Fugitive emi:;sions are 

prevented by these measures a.nd the negative primary combustion chamber 

pressure maintained by the ID fan. An A WFCO interlock will be triggered if the 

primary combustion chamber pressure meeiS or exceeds the maximum limit (0.0 

in. w.c_ gauge) for greater than five seconds. Continuous video survc:illancc of 

the combustion chamber exterior is utiliud to detemtine if an A WFCO caused by 

high primary combustion chamber pressure corresponds with fugitive emissions. 

There must be visual evidence of ft•gitive emissions from the primary combustion 

chamber fur a positive pres!!llrc cv~nt to be considered an excccdnnce. 

• Mlnlmum Primary Combustion Chamber Temperature - The temperature of 

combustion gas inside the primary chamber is monitored by redundant 

thennocouples. [fthe hourly rolling average (HRA) primary combustion chamber 

temperature meets or Cllceed.• its limit, an A WFCO interlock is triggered. 

• Minimum Secondary Combustion Chamber Temperature - TI1e temperature 

of combustion gas ioside the secondary chamber is monitored by redw1dant 

thermocouples. If the HRA secondary combustion chamber temperature meets or 

exceeds its limit, an A WFCO interlock is triggered. 

• Emergency Safely VMI Position - Each incinerator's secondary combustion 

chtunber is equipped with an emergency stack and emergency safety vent (ESV), 

which is also referred tons the thermal relief vent (TRV). The TRY ollows bot 

combustion gas to vent from lhc combustion system during certain scenarios to 

protect the downstream APCS frorn excessive temperdture situations. Unit 4 is 

also equipped with a second ESV located at the kiln face. This ESV is referred to 

as the surge vent and provides emergency pressure relief of tl1c kiln. To minimize 

excessive emissions during an ESV opening. Ute output from tbo ESV position 

8 

VESOI2260 
transmitteo- is interlocked \\~th the A WFCO system. If the ESV position is 

detected as open, an AWFCO interlock is triggered. 

• Maximll.lll Bagbouse Inlet Temperature - For Units 2 and 3, the baghouse inlet 

temperature (i.e., spray dryer absorber exit gas temperature) is continuously 

monitored by a tltermocouple. Unit 4 is equipped with redtmdant thermocouples 

at the exit of each SDA. If the HRA bagbouse inlet temperature meets or exceeds 

its limit, an A WFCO interlock will occur. 

• Maxbn.um Bag Leak Detector Output - A triboclectric sensor is located in tbe 

duct downstream of the lD fan and continuously monitors the relative patticulate 

matter loading of the gas. An A WFCO interlock will be triggered if the bag leak 

detector output remains at or above it high-high setpoint for tbe duration of the 

alann delay time. 

• Minimum Carbon Feed rate- Powdered activated carbon is air injected into the 

plenum inunediately upstream of the Unit 4 baghouses. A calibrated feeder is 

used to continuously monitor the addition rate of carbon to the carbon-air stream. 

If the HRA carbon feedrate meets or exceeds its limit, an A WFCO interlock is 

triggered. 

• Carbon Injection System Operadng Pre$sures - The Unit 4 carbon injection 

system is equipped with a high level pressure switch located between tbc carbon 

feeder aod the eductor. A low level pressure switch is located downstream of the 

blower that supplies air as the carbon canier fluid. Both pressure switches have 

two setpoints, which define the permissible operating raoge at each location. 

These setpoints are interlocked with A WFCO system. 

• Maximum Stack Gas Flow r ate-The pressure drop aetOsS a pi tot tube located in 

tbe Cllhaust stack is utilized to continuously monitor the stack gas flowrate. If the 

HRA stack gas flowrate meets or exceeds it limit, an A WFCO interlock is 

triggered. 

• M aximum Stack Gas Carbon Monoxide Concentration - The CEMS 

continuously samples and analyzes stack gas fur the concentrations of carbon 

monoxide (CO), and moisture using a multicomponent infrared photometer. The 

oxygen concentration of the sampled gas is analyzed simultaneously using a 

9 

VESOI2261 
zirconium oxide analyzer. A back-up zirooniwn oxide 02 analyzer also monitors 

stack gas 0 2 concentration. These data are used to calculated the stack gas CO 

concentration on a dry basis, corrected to 7% 02. If the CO concentration meets 

or exceeds the HWC MACf emission standard for CO (I 00 ppm dry volume, 

corrected to 7% oxygen), an AWFCO interlock is triggered. 

10 

VES012262 
2.0 A WFCO OPERABILITY TEST PROCEDURES 

The AWFCO interlocks are tested bi-weekly, as weekly testing would unduly interfere 

with operations, cause excessive downtime, and substantially increase operating costs. 

Testing of the A WFCO system is a time-consuming and manpower intensive process. 

The current testing program has been in place under the RCRA pennjt for a number of 

years and has proven to be adequate in detecting problems. 

A WFCO system operability testing is conducted by manually simulating input of process 

conditions to the programmable logic controller (PLC). The simulated input for each 

OPL will be set outside oflimits to trigger the A WFCO interlock and associated alarms. 

The point at which the simulated input activates the control logic for the closure of the 

waste feed block valves will be observed and documented. Waste feed valves will not 

actually close during AWFCO testing. In addition to this A WFCO system control logic 

testing, the functionality of the waste feed block valves are confirmed during startups, 

shutdowns, actual A_ WFCO conditions, and when transitioning to and from warm standby mode 

Tests of the A WFCO system interlocks and associated alarms are documented an a 

AWFCO Testing Log and are maintained separately as part oftbe unit's operating record. 

11 

VES012263 
3.0 RESPONCE TO AN AWFCO EVENT 

While an AWFCO event will trigser an alarm, and automatically (and immediately) 

cutoff waste feed to the incinerator, the other portions of the· incinerator syslom will 

remain operational and functioning (the APCS, CEMS, etc). Combustion chamber 

temperatures will be maintained on naturol gas fired to the main burners, if possiblo. 

An A WFCO event is initiated in the following manner: 

I) An alarm is activated at a level below the pemtit limit in the case of a 

ma"<imum limit or above tho permit limit in the case of a minimum opcmting 

condition. This alarm indicates tlUll the system is approaching a regulatory set 

point. The alarm also indicates a potential malfunction. 

2) At this point, the operator reviews the situation and rakes action to correct the 

situation, up to and including a manual shutdown of the affected system. 

These corre.-i:ive actions will be consistent with the· Startup, Shutdown, and 

Malfunction Plan (SSMP). 

3) If !be corrective actions 11\ken are not effective, and tlte opet·ating parumeter 

reaches its permit limit or a permit preemptive· set point, an A WFCO is 

initiated. An A WFCO Los form wiU be used to document the event. 

If an A \VFCO event corresponds with an e:tceedance while hazardous was1c rell)ains in 

the combustion chamber, it must be detennined if the event meets the regulatory 

definition of a malfunction. If such an event is a malfunction, a malfunction 

recordkeeping fonn will be used. Regardless of whether the hazardous waste residence 

time bas tranSpired, if there is an exccedance that corresponds "ith an AWFCO event the 

follo"~ng actions will be taken: 

• Investigate the cause of the A WFCO; 

• Take appropliate corrective measures to minimize futuro A WFCOs; 

and 

• Record the findings and corrective measures in the operating record. 

Alter an A V.'FCO has oecurred, all operating parameters must be within limits prior 10 

restarting hazardous waste feeds. 

12 

VESOI2264 
3.1 Reporting Requirements 

For each set of ten1 exceedances of an emission standard or operating parameter limit, 

and each exceedaru:e occurs while hazardous waste remains in the combustion chamber, 

a written report will be submitted by Veolia to the Illinois Environmental Protection 

Agency (JEP A). The written report will be submitted within five calendar days of the 

tenth' exceedance and will document lhe exceedances and results of the investigation and 

corrective measures taken. 

J Exeeedances occtll'l'in,g ~ malfuuctfon are not included ia this tally. ~ Startup, Shutdown, and 

Malfiloctkm Pian swnmarizes tbe repottin~ requirementt;, associated with exooedaooes occurring during 

malfunctions. 

13 

VES0l2265 
4.0 MANUAL WASTE FEED CUT-OFF PROCEDURES 

If an A WFCO interlock fails to cutoff the feed of hazardous waste to the incinerator, the 

operator will manuaUy cutoff all waste feeds to the incinerator in a quick and safe 

manner. This response is consistent with the procedure prescribed by the SSMP and mil 

be documented on a malfunction recordkeeping fonn. Th.e Program of Corrective 

Actions for Ma/fimcti<ms, Alfachment 4 to the SSMP, will be followed for the restoring 

the A WFCO system. 

14 

VESOJ2266 
VES012267 .pdf 
APPENDIX I 

ESV OPERATING PLAN 

VES012267 
EMERGENCY SAFETY VENT PLAN 

Prepared for: 

Veolia ES Technical Solutions, LLC 

Sauget, Illinois 

Prepared by: 

Frauklin Engineering Group, Inc. 

Franklin, Tennessee 

October 2008 

VES012268 
TABLE OF CONTENTS 

1.0 INTRODUCTION AND BACKGROUND ......................................................... ! 

1.1 SUMMARY OF FACILITY INFORMATION ............•......•........•............................ ! 

1.1.1 'Fixed Hearth Incinerators ............................................................... ] 

1.1.2 RotQJy Kiln lncinerator .................................................................... 3 

1.2 DESCRIPTION OF THE ES V SYSTllM ............................................................. .4 

2.0 ESV SYSTEM INVESTIGATION, DOCUMENTATION AND 

REPORTING ......................................................................................................... 7 

2.1 ESV INVESTIGATION .................................................................................... 7 

2 .2 0 0CUMENTATIONOPESV0PENING ............................................................. 7 

2.3 REPORTING OF ESV 0PENINGS ..................................................................... 8 

3.0 PROCEDURES DURING AN ESV ..................................................................... 9 

3.1 STOPPING WASTE FEED AND SHUTTING 0 0\IIN THE CO~ffiUSTOR ................ 9 

3.2 MAINTAINING COMBUSTION CHAMBER TEMPERATURE ................................ 9 

3.3 MAINTAINING NEGATIVE COMBUSTION CHAMBERPRESSIJRE ...................... 9 

3.4 SHUTTING DOWN TilE COMBUSTOR .............................................................. 9 

3.5 DOCUMENTATION OF COMBUSTION CHAMBER PRESSURE AND 

TEMPERATURE !VfAINTENANCE ............................................................. 1 0 

ii 

VES012269 
TABLE 1-1 

LIST OF TABLES 

REGULATORY REQUIREME~TS FOR AN EMERGENCY SAFETY VENT 

OPERATING PLAN AND CORRESPONDING SECTION THAT ADDRESSES ll!E 

REQUIREMENT .............................................................................................. 2 

TABLE 1-2 TlffiRMAL RELIEF VENT 0PENINGS ............................................................... 5 

111 

VES012270 
1.0 INTRODUCTION AND BACKGROUND 

V eolia ES Teclmical Solutions, LLC (Veolia) owns and operates two fixed hearth 

incinerators (Units 2 and 3) and a rotary kiln incinerator (Unit 4) at its fu.cility located in 

Sauget, Illinois. These incinerators are subject to the National Emissions Standards for 

Hazardous Air Pollutants (NESHAP) for Hazardous Waste Combustors (HWCs), Code 

of Federal Regulations (CFR), Part 63, Subpart BEE(§§ 63.1200 to 63.1221). The 

NESHAP for HWCs specifies emissions standards which reflect emissions performance 

of maximum achievable control technologies (MACD, and is commonly referred to as 

the HWC MACT. 

Hazardous Waste Combustors are required to have an Eme.·gency Safety V cnt Plan and 

to keep the plan in the operating record. The Emergency Safel)l Vent Plan must foUow 

the requirements described in § 63. 1206(c)(4). This Emergency Safel)l Vent Plan 

demonstrates Veolia's compliance with these requirements. This plan includes 

information about the facility as it relates to the Emergency Safety Vent (ESV) systems, 

and procedures that will be foUowed during an ESV event. Table 1-1 presents the 

re&'lliatory references related to the required ESV program and the section of this plan that 

addresses each specific requirement. 

Due to the general applicability of the ESV requirement and the similarity of the 

incinerator systems, general references to an ESV or incinerator system in this document 

will 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 summaries which describe the fixed hearth incinerators and the rotary kiln 

incinerator are presented in this section. 

1.1.1 Pixed Hearth Incinerators 

Each of the fixed hearth incinerators includes the following components; 

• Feed equipment 

• Ptimary and secondary combustion chambers 

• Lime injection system 

• Spray dryer absorber (SDA) 

• Fabric filter baghouse 

VES012271 
Table 1-1 

Regulatory Requirements for Emergency Safety Vent Operating Plan 

and Corresponding Section that Addresses the Requirement 

Regulatory 

Citation 

Description Plan Section 

Documentation in operating record of an ESV 

opening while hazardous waste remains in the 

combustion chamber: 

63. 1206(c)(4)(i) (1) Record ifESV by-passed APCS 

(2) Determine if operation remained in 

Section 2.2 

compliance considering the emissions during 

theESV 

Infonnation 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( eX 4)(ii)(B) Detailed procedures for rapidly stopping waste feed Section 3.1 

63.t206(cX4)(ii)(B) 

Detailed procedures for shutting down the 

combustor 

Section 3.4 

63.1206( c)( 4)(ii)(B) 

Detailed procedures for maintaining temperature in 

combustion chamber 

Section 3.2 

63.1206( c)( 4)(ii)(B) 

Detailed procedures for maintaining negative Section 3.3 

pressure in the combustion chamber 

63.1206( c)( 4)(iii) Investigation ofESV openings Section 2.1 

63.1206(c)(4)(iii) Recording of ESV openings Section 2.2 

63.1206(c)(4)(iv) Reporting of ESV openings Section 2.3 

2 

VES012272 
• 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 waste is fed to the primary (lower) combustion chamber 

via a feed conveyor system and pneumatic ram. 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 feedstream is fed to the Unit 2 primary combustion 

chamber directly fi'Om gas cylinders. Off gases from a hooded teed emission contml 

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 provide particulate matter 

removal. The induced draft fan, located downstream of the baghouses, moves the 

combustion gas through the system and exhausts the gas through the main stack. 

1.1.2 Rotary Kiln Incinerator 

The rotary kiln incinerator includes the following components: 

• Waste feed system 

• Primary and secondary combustion chambers 

• Tempering chamber 

• Lime injection system 

• Spray dryer absorber 

• Carbon injection system 

• Fabric filter baghousc 

• Solids and ash removal systems 

• ID 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 feeder via a clam.sbeU, a drum feed conveyor, and an anxiliary 

3 

VESOJ2273 
feed conveyor. A hydnrulic ram pushes the solid waste into the kiln. 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 ellits the secondary combustion chamber and enters the tempering 

chamber, which pro,~ des cooling of the combustion gases. The combustion gas exits the 

tempering chamber and is distributed between two identical SDA.s, which pro~de acid 

gas removal and additional gas cooling. A carbon injection system is utilized for 

controlling dioxin/furan and mercury emissions. The activated carbon is air injected into 

the combustion gas inunediately do\\nstream of the convergence of combustion gases 

from the SDA.s. From the SDAs, combustion gas is distributed to fabric filter baghouses, 

which provide particulate matter removaL The ID fan, located downstream 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 an emergency safety vent (ESV) located at the top of 

the secondary combustion chamber. This ESV is a refractory-lined emergency thermal 

relief vent (TRV) 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 vah•e which 

opens the TRV are located in the control room for each unit Valve locks (\\~th keys 

attached) are utilized to deter indiscriminate operation of these valves. Opening of the 

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

shutdown events. Tite purpose of the TRV is to protect the downstream APCS from 

excessive temperature situations. 

Conditions which may warrant a TR V opening are summarized in Table 2-1. Typically, 

alarms and/or interlocks will 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, a controlled cutoff of the waste feeds, an A WFCO, or 

an emergency shutdown may occur prior to opening the TRV. (f hazardous waste is 

being fed at the time the TRV is opened, the TRV position transmitter will detect the 

TRV opening and trigger an A WFCO. 

4 

VES012274 
Table 1-2 

Thermal Relief Vent Openings 

Parameter Condition 1 

Electrical Supply Loss of Power 

Air Supply 

Loss of All Pressure 

(TRV will f.ail open) 

IDFan Failure/lVIal function 

SDA Exit Oas Temperature > 500 •f 

Emergency Shutdown Operator's Discretion 

1 The operator is permitted to open the TRY if these conditions are present. 

5 

VESOI2275 
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 

there is a pressure excursion in the kiln sufficient enough to overcome the weighted 

louver. A deflector separates the escaping combustion gas from the feed, and the surge 

vent angles to a horizontal opening. This design minirrllzes the entrainment. of solid 

through the surge vent. 

An ESV opening may correspond with a malfunction event. Information regarding 

operation of the incinerator and the associated control equipment during times of start-up, 

shutdown and malfunction is provided in the facility Start-up, Shutdown, Ma/fimction 

Plan (SSMP). 

6 

VES012276 
2.0 ESV SYSTEM 

REPORTING 

2.1 ESV Investigation 

INVESTIGATION, DOCUMENTATION AND 

If an ESV opens for any reason during nomtal operations, the operator is instructed to: 

1) Verify that all waste feeds to the incinerator are cutoff, 

2) If possible, operate the ID fan, and 

3) If possible, maintain normal combustion chamber temperatures on natural gas. 

If hazardous waste is in the combustion chamber during a ESV opening, the incinerator 

supervisor should be notified as soon as possible. The incinerator supervisor will 

coordinate with teclutical staff to determine potential causes for the event and to estintate 

excessive emissions. 

2.2 Documentation of ESV Opening 

Each instance in which the emergency vent opens will be recorded in the facility 

operating record. Titis record will, at a minimum, include the date, time, and the 

operating mode at the time of the ESV opening. Titis data is automatically documented 

in the operating record by the CMS. 

If the ESV opens when hazardous waste remains tn the combustion chamber (i.e., when 

the hazardous waste residence time has not expired) during an event other than a 

malfunction (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 staudards, and record the findiugs of that detennination in the facility operating 

record. Since the ESV is located upstream from the facility air pollution control devices 

(APCD), it is understood that combustion gas by-passes these emission control devices 

during an ESV event. Tlus by-pass will be documented in the facility operating record. 

If an ESV opening is attributed to a malfunction and occurs when hazardous waste 

remains in the combustion chamber, a malfunction recordkeeping tbrrn will be completed 

to document the event. 

7 

VESOJ2277 
2.3 Reporting of ESV Openings 

If an ESV opening results in a failure to meet 01e emission standards for the facility, 

Veolia will submit a written report 'il'ilhin five days of the ESV event to Illinois 

Environmental Protection Agency (IEP A), documenting the results of the investigation 

and corrective measures taken. In most cases when an ESV event occurs, it is 

instantaneous. TI1erefore, it is practical to assume that diminimus emissions occur during 

these instantaneous events. 

8 

VESOL2278 
3.0 PROCEDURES DURING AN ESV 

In the event of an ESY opening that occurs while burning waste, it is important that waste 

feed is stopped rapidly, and that combustion chamber temperature and negath•e pressure 

are maintained to the extent practical. Following the expiration 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 and Shutting Down the Combnstor 

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

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

the A WFCO system. These redundant measures ensure that waste feeds will be stopped 

during 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 manner. Waste burning cannot 

reswne until the ESY is closed, corrective actions taken, pernrission is granted from the 

incinerator supervisor, and all parameters are within limits. 

3.2 Maintaining Combustion Chamber Temperature 

Combustion chamber temperatures are maintained using natural gas fired a dedicated 

burner in both the primary and secondary combustion chambers. If possible, the buming 

of natural gas will be used to maintain adequate combustion chamber temperatures for 

the combustion of waste remaining in the incinerator. 

3.3 Maintaining Negative Combustion Chamber Pressure 

If possible, the ID fan will be operated during an TRY opening to minimize the quantity 

of combustion gas that by-pass the air pollution control equipment. Operation of the ID 

fan during an ESY opening will maintain negative combustion pressure to the full extent 

that is reasonably feasible. It is likely that the opening of the TRY will cause the system 

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 operable) 

will be used to restore negative pressure in the primary chamber, as quickly as possible. 

3A Shutting Down the Combustor 

An event which causes an ESV opening may require a cold shut down of the combustor 

in order to perform couective actions. After sufficient effort is taken to minimi7..e 

emissions by maintaining the temperature and pressure, the incinerator supervisor will 

decide if a shut down is warranted. If the ESV opening corresponds "~th a malfunction 

9 

VES012279 
event then the corrective measures taken will be consistent wilh the procedures 

prescribed by lhe SSMP. 

3.5 Documentation of Combustion Ch.liJI)ber Pressure and Temperature 

Maintenance 

§ 63.1206(c)(4)(ii)(B) requires that the facility demonstrate that the procedures of this 

plan are adequate to maintain combustion chamber pressure and temperature willie 

hazardous waste remains iu the incinerator, if feasible. The occurrence of an emergency 

safety vent opening at the V eolia facility is possible only iu a select set of circumstances, 

which are descnlx:d in Section 1.2 of this plan. If natural gas cannot be burned, it is not 

feasible to maintain the combustion chamber temperature during an ESV event. 

Likewise, it is likely that the opening of the TRV will result in lhe loss o f negative 

pressure. The duration of a surge vent opening will typically be brief and only 

momentarily prevent tnaintaining the combustion chamber pressure. The procedures 

presented in this plan will be followed to minimize the effects of such occurrences. 

10 

VESOJ2280 
VES012281 .pdf 
APPENDIXJ 

FEEDSTREAM ANALYSIS PLAN 

VES012281 
FEEDSTREAM ANALYSIS PLAN 

Veolia ES Technical Services, LLC 

Sauget, Jllinois 

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October 2008 

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Feedstream Analyais Plan- October 2008 

TABLE OF CONTENTS 

1.0 INTRODUCTION 

2.0 FEEDSTREAMPARAMETERS 

2.1 Chlorine 

2.2 Metals 

2.3 Ash 

3.0 ANALYTICAL RATIONALE 

3.1 AnalysisPerformedbyVeolia 

3.2 Analysis Performed by Othel's 

3.3 Manufacturer Data or Other Published Jn:formation 

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4.0 APPLICATION OF ANALYSIS FOR FEEDRATE COMPLIA.~CE i 

------·-· .. ·------·----- ·---·---- ---t4.1 Process Planning for Feedstreams 

4.2 Process Control for Feed streams 

4.3 Docwnentation and R.ecordkeeping for Process Planning and 

Control 

S.O SAMPLING AND ANALYTICAL METHODS 

5.1 Sampling Methodologies 

5.2 Documentation and Recordkeeping Associated with Sampling 

5.3 Analytical Methodologies 

5.4 Documentation and R.ecordkeeping Associated with Sample 

Analysis 

6.0 FREQUENCY OF A."'iALYSIS 

7.0 COI\fi'LIANCE WITH FEED RATES i 

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Feedstream Aunlysis Plan- October 2008 

1.0 INTRODU<-"TION 

Pursuant to the regulatory requirements found in 40 CFR 63. 1206 (c) of the HWC MACT 

Standard, Veolia ES Technical Solutions,ILC (V eolia) has developed a Feed.strcam 

Analysis Plnn (F AP). Its pwpose is to provide a system whereby Veolia can sample, 

analyze, and control the incineration of feedstreams that may contain constituents 

requiring feedrate limits as specified in the HWC MACT Standru:d. The F AP also 

addresses how these activities will be recorded in the :fucility's operating record. 

This FAP is organi2ed such that ~ch of the sut>sequent sections specifically addresses 

the six paragraphs under 40 CFR 63.1206 (c) (2) and three paragraphs under 40 CFR 

63.1206 (c) (4) in the orderin which they are presented in theHWC MACT Standard. In 

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many instances, this F AP will ref-erence the facility's Waste Analysis Plan (W AP). The ; . 

WAP is an integral part oftheRCRA Part BPermit, the Permit Application, and any . 

subsequent revisions or addenda to the Part B Permit or Permit Application. ! ·: 

As required by sections 63.6 (e)(v) and 63.6 (eXvi) of the HWC MACT Standard, the ! 

F AP and other docwnents containing procedures or information referred to in the FAP ~ · 

will be made available for inspection when requested by the Admlnistrator. The FAP, 1,:,; 

correspondence with the Administrator concerning the F AP, and any subsequent 

add.itions or modifications to the F AP will be kept in the :fucility's Operating Record. If ''· 

Veolia is required to submit copies of the F AP or portions of it (or related documents), ~ ------ ~al-bus~ill:formalion-entit ed-to-protection-ftor:rrdisclosure'Wiltire'clearly'-···· ----- --+ 

designated. ' 

2.0 FEEDSTREAM PARAMETERS 

There are three feedstream consiiluents that are specified in the HWC MACT Standard 

for emission and/or feed.rate limitations and !bat may be present in any given feedstream. 

These three are: 

I) Chlorine 

2) Metals (Mercury, Lead, Cadmium, C'hrotnium, Beryllitu:n, and Arsenic) 

3) Ash 

These three constituents will serve as the feedstrearn parameters of concern in the F AP as 

required by 40 CFR 63.1206 (c) (2) (1) oftheHWC MACT Standard. Feedstream data 

applicable to each of these parameters will be obtained for all feed.streams in order to 

control the incineration of them and remain within the feedmte limits set for them. 

2.1 Chlorine 

Feedstream data will provide a weight-based percentage of chlorine for eaclt waste feed 

to the inciuerators. These results can be used to both estimate targeted feed rate values 

and control actual feed rates during incinera1ion. 

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.Feedsn·eam Analysis Plan - October 2008 

2.2 M•tals 

Fcedsll'eam data will provide a parts-per-million concentration for each of1he listed 

metals in each of the waste feeds to the incinerators. For analytical results til3t show less 

than detection limit concentrations, Y:i the detection limit value will be usod for 

incinerator feed computations. These results can be used to both estimate targeted feed 

rate values and control actual feed rates during incineration. 

2.3 Ash 

Feedslream data will provide a weight-based percentage of ash for each of the waste 

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

values and conll'Ol actual feed rates during incineration. 

3.0 ANALYTICALRATlONALE 

ln 40 CF'R 63.1206 (c) (2) (ii) of the HWCMACf Standard, a facility is required to 

idelllifY how it" " 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 parameters as described in Section 2. 0 of the F AP. Thoy are: 

A n•l¥sis pel'fo!;Qled.b;<.¥oolia -·-------.. ·-·-- ... 

2) Analysis performed by others 

3) Manufacturer data or other published information 

These SOlli'CeS are also referenced in the facility's W AP and the ways in which they can 

be applied to reedstreams w-e extensively addressed. Many of the analytical procedures 

performed as described in the F AP are also required as part of the waste acceptance and 

management process at Veolia. The information derived from these procedures can then 

be used in complying with the feedstre= limitations for the parameters identi£ed in the 

PAP. 

The three analytical sources can be applied to generator wastes received at the V eolia 

facility, including those that undergo subsequetJt blending prior to incineration, and also 

to wastes that are generated at the facility. 

3.1 Allalysis Performed by Veolla 

The predominate means applicable to this source of analytical information is tbe 

methodology described in Section 5.0 of the FAP. Specific analytical methods performed 

in the facility's labomtory are applied to applicable feedstreams to produce values for the 

required parameters. 

Typically, the feedstream is a waste profile from a generator that has been accepted 

according to the facility's W AP guidelines. This waste will have had analytical work 

performed on a sample for an initial acceptance decision and supplemental analysis as 

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Feeestream Analysis Plan - October 2008 

required for subsequent shipments of the waste. This analytical work will include 

information on the parameters identifi<!d in the F AP and can be used to control the 

incineration of the feedstreams. 

In other instances, the feedstrearos are wastes blended together at the facility (e.g., bulk 

liquids and bulk solids} or wastes generated by the facility (e.g., laboratory wastes, 

incinerator ash). Feedstreams that ate the result of blending or other on-site processing 

steps prior to incineration can have parameters determined from the same analytical 

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

value based on a body of previously analyzed samples. Wastes generated by the facility 

will have parameters determined from an average value based on a body of previously 

analyzed samples. 

For many fcedstreams, the best source of infonnation for tbe parameters idontified in the 

FAP wiU be obtained using the tecbJUcal expertise ofVeolia persotmel. Examples of 

these types of feedstrcams are labpaclcs, controlled substances and empty containers. The 

facility's WAP lists some of these reference sources in Appendix W AP-F. 

3.2 Analysts Performed by Others 

In silu.ations where Veolia cannot perform the necessary analysis due to the nature of tho 

fecdstrcam (e.g., gases, some reactive materials) or when previous outside analysis of 

----.f~1he-mnda~ds of tttis F:t\:Pis-availabie;-Vea!ilrwi:lllll:l:'epnh:e 

analysis of others in determining parameter values. This analytical iufonnation will be 

evaluated and used to control the incineration of feedstreams in the same manner as 

analytical information produced at the facility. 

3.3 Manufactur er Datu or Other Published Information 

Many feedstreams bsve pre-existing infomtation applicable to them that can be used to 

detcr:mine the valuw of the parameters as identified in the F AP. This can take the fonn of 

manufactnrer specifications and data, Material Safety Data Sheets, reference sources or 

other published infonnation. The facility's WAP lists some of these reference sources in 

Appendix W AP-F. Examples of these types of feedstreams include commercial products, 

phrumaceuticals, chemical reagents, snd gas cylindCI'S. This information will be evaluated 

and used to control the incineration of these feed streams in the same manner as analytical 

infomtation produced at the facility. 

4.0 APPLICATION OF ANALYSIS FOR FEEDRATE CO.MPLIANCE 

Feedstream data will be used to maintain compliance for the feedrate limitations to the 

incinerators. This analysis will be completed prior to the feeding of any material to the 

incinerators. Tbe documentation of these feedrate compliance methods is roquir<!d by 40 

CFR 63.1206 (c) (2}(iii) oftheHWCMACT Standard and outlin<!d in tbiJ; section oftbe 

FAP. 

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VESOI2286 
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Feedstream Analysis Plan- October ZOOS 

Analytical results can be used to both estimate targeted feed rate values and control actual 

feed rates during incinerAtion. Analysis from laboratory testing at the facility, analytical 

results from others, published infolllllltiou, and technical evaluations by Veolia personnel 

can all be used in complying with feedrate limitations for the parameters identified in tbe 

F AP. In addition, these analytical information sources can be used for wastes from 

generators, wastes blended at the facility, and wastes generated at the facility. 

4.1 Process Planning for lleedstreams 

When evaluating analytical results and any additional infom1ation applicable to a 

potential fecdstream, a decision must be made whether parnmeters for that feedstream are 

acceptable for feeding to the incinerators or if some level of feed preparation is 

necessary. This step io the feedsneam evaluation process is called process pla:tlning. It is 

applied to blending wastes, processing wastes into combustible charges, and determining 

if wastes C3ll be fed directly to the incinerators as initially received at the facility. This 

planning is performed based on infonnation from analytical results, incioerator 

perfonnance capabilities, process operation history, and the technical expertise of the 

process planning personnel involved. 

4.2 Process Control for Feedstreams 

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

-------ilditltlriri:n:ll~·'Oftbe ineines:atws, automatic SJSlems mustbe-irrpfaee to wnndl tlfe------··-

incioerator process. These systems continuously track the feedstream parameters as they 

are introduced ioto the incinerators and make 1he necessary feed adjustments or cut·offs 

for compliance. Section 7.0 of the FAP addresses these systems and the rationale behind 

their operation in greater detaiL 

4.3 Documentation and Recordkeeping for Proc.ess Planning and Control 

Documenlalion of process planning and control is demon.strated by the extern.-ive body of 

ioformation collected in the facility's data management system, and, if needed, 

distributed in hard copy form to appropriate personnel. This includes laboratory analysis 

used for feed preparation, bulk waste storage data, processiog directions, and related 

iofonnation. Actual iociuerator operations data is rocorded in printed summaries, 

recorded onto digital data storage systems, and is also selectively available on-line. This 

iofonnation will be retained in the operating record for the life of the facility. 

5.0 SAMPLING AND ANALYTICAL METHODS 

The requirements in40 CFR 63.12.06 (c) (2) (iv) and (v) of the HWCMAcr Standard 

state that a facility must identify 1he sampling and test methods used for analyzing the 

feedstreams. The sanqJiing methodology and much of the analytical methodology that is 

described in Soctious 2.0 and 3.0 of the facility's Waste Analysis Plan is applicable to the 

FAP. Additional sampling and testing infonnation is included io the following paragraphs 

of this section. 

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Feedstream Analysis Plan - October 2008 

5.1 Sampling 1\feth.odologies 

Sampling is perfonned at the Veolia facility to identify waste slripments and also by the 

generator at their location when malcing an initial determinati011 on the acceptability of 

the waste at Veolia. In some instances, an actual sample will not be required beeause 

technical personnel at Veolia will have determined that sufficient documentation already 

exists that identifies information regarding the parameters described in Section2.0 of the 

FAP (see also Section 4.0, Paragraph 4.1.12 (2) of theW AP). In order to obtain a 

representative sample of the waste, specific sampling procedures that are dependent 011 

bofh fhe natUieofthe waste sampled and the type of processes in which the waste wiU be 

stored or transferred must be performed. Section 2.0 oftbe facility's WAP and pertinent 

appendices in the W AP list fhese procedures and the ASTM method number (or other 

EPA approved method) on which they are based. This section in the W AP also addresses 

the sampling equipment used, the types of intended containment or processes that can 

impact the sampling, and guidelines on how to ensure that a valid and representative 

sample is obtaioed. 

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5.2 DocomentaUon a11.d Recordkeeping Associated with Sampling :· 

All samples taken at the facility or sent to the fucility for analysis are assigned a unique I, 

sample identification number. These identification numbers are recorded in a chain-of- f --.. ----ettSI'edy-log-and'113ed-fortracking1he sample tlnouglt lhei\il::tlity':rdata~:-- ---.. -1 

Each s;unple also has a label affixed to it identifying its contents, the date the sample was i 

taken, and the person who took the sample. 

5.3 Analytkal Methodologies 

CHLORINE 

The analytical procedures and EPA approved methods related to determining the amount 

of chlorine in a feedstream are found in Appendix \V AP-A to the facility's WAP. 

METALS 

Feedstreams that require analy!ris for the metals specified in the HWC MACf Standard 

will either contain thes,e metals in a non-water-soluble form or a water-soluble form. 

Samples of feedatreams in a non-water-soluble fonn will require additional preparation 

steps prior to analysis. The analytical procedures and EPA approved methods related to 

determining the amount of listed metals in a feedstream are listed below. 

Digestion Procedure for Non-Water-Soluble Samples 

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

Oils 

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VES012288 
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Feedstream Analysis Plan - October 200& 

Procedure for Detennjning Concentration of Mercury in Sample 

Method 7473 -Mercury in Solids and Solutions by TheiiDal Deromposition, 

Amalgamation, and Atomic Absorption Spectrophotometry 

Proce4ure for Pctennining Concentration of Arsenjc. Bervmum. Cadmium. Chromium 

and Lead in Sarople 

Method 601 OC- Inductively Coupled Plasma-Atomic Emission Spectrometry 

AS II 

The analytical procedures and BP A approved methods related to determining the amouot 

of ash ina feedstrearn are found in Appendix WAP-Ato the facility's WAP. 

5.4 Documentation and Re.cordkeeplug Associated with Sample Analysis 

Documentation of analytical work is accomplished by recording it in laboratory 

logbooks, entering it into the facility's data management system, and, jf needed, 

distributed in hard copy fotm to appropriate personnel. All technical files for waste 

profoles will also inolude initial laboratory analysis and any applicable subsequent 

------~;:~~~~- Thi_s_infi _onnation will be re~".~. in_tbe operating record f~r ~<:life o::.f.::th::"---·-·---·--

6.0 FREQUENCY OF ANALYSIS 

ln40 CFR63.1206 (c) (2) (vi) oftheHWCMACT Standard, a facility is required to 

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

it is cuuent. This F AP will require that the analytical iofonnation for the feedstreams be 

re-evaluated on a frequency consistent with that described for all wastes as deooribed in 

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

evaluate the analysis of a given feedstream are: 

1) Geuerator notifies Vcolia that a feedstream has changed 

2) Subsequent analysis for a fecdstream nsed by Veolia is inconsistent with tbe original 

analysis 

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

In order for a fecd&1ream to be con~'idercd acceptable again for incineration after one of 

these events bas occurred, the evaluation process as described in this F AP must be 

completed. 

7.0 CO?tfPUANCE WfllJ FEED RATES 

Veolia employs process control systems for the incinerators that monitor, adjust and 

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

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Feedslream Analysis Plan- October 2008 

theJa These systems meet tbc requirements of 40 CFR 63.1206 (c) (4), paragraphs (i), (ii) 

and (iii). TI1e systems and the rationale that supports these systems are described in the 

following paragraph. 

7.1 ).<'eed Rate Compliance S)·stems and Methodology 

After the metals and ash concentrations for feedstreams are d.erermined, they will be 

entered into the facility's data management systems. These fcedstreams are identified in 

the system under a site tracking number, bulk pit number, or tank number. Once this 

information is in tho waste tracking system, tbe incinerator control systems are abl" to 

import and store tbe data for use as the waste streams are processed at the incinerators. 

All waste introduced into the incinerators has an associated site identification designation 

(receiver number, etc.) so it can be referenced to tb.e appropriate data from the waste 

tracking system. As weights are recorded at 15 second intervals for each specific waste 

stream entering the incinerator, computations are being performed to calculate the 

quantities of metals (as low volatile metals, semi volatile metals, and mercury) and ash 

that are being incinerated. These quantities are displayed, totalized, and recorded in a 

manner that will show compliance with the established operating parameter liroits for the 

metals categories and ash. One hour and 12 hour rolling totals are displayed for the 

incinerator operators for monitoring of these .feeds. 

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VES012290 
VES012291 .pdf 
APPENDIXK 

TITLE V ITEMS TO BE REMOVED 

VES012291 
~c lia Snvironra9ntal Se rvices 

Permi: No .: v-rL- l716300l03- 08- 01 

Page: 7 of 176 

2 . 1 Hazardous Waste Combustors, Units 2, 3 and 4 

(A) Emission Limitations a nd Standards 140 C. F. R. 

§ 7 1.6(ii) (1) ] 

The Pe rmittee shall c omply with the follo«ing requirentents 

for each individual incinerator un less specified ot:1"•€!''·" i se : 

1 . Visible emi ssion Limitation . 

(al The Perm~t tee shall nor; cause o r allo" t he 

er.lission of smoke o.r othe r particulate matter, •.d th an 

cpacity g reate r than 30 pe.rce nt , i nto the a tmosphere 

from any emission source, except as allowed by 3S IAC 

212.223 (b) a~d 21 ~. (35 lAC 212.123(a) J 

(b) The Permittee shall not cause or allo" the 

emission of fugitive parti cul ate mar;ter from any 

p~ocess , including any materi a l ~~n li ng o r to~age 

activity, that is visible by an observer looking 

generally overhea<i a" a point beyond t he property line 

of the scurce ~~less the wind speed is 9r ea ter than 

40 . 2 kilometers per hour {2S miles per hour.) [ 3!, IAC 

212 . 301 and 212.31'1 

2 . Sulfur Dioxi de Limi tacion. 

Total sul fur dioxide emissions from the facil ity shal l 

not exceed 7. 7 tons per year for uni•s 2 and 3 and 

50 . 76 tons per year for unit 4 . {Construc t ion pe rmi ts 

87100024 and 88010001 1 

3 . Carbon Non<>xide Lirr.i tation. 

{a) The Per:mitt .::e sha l l not allow emissions of car bon 

monoxide in excess of 100 parts per million by vo: ume, 

over an ho urly rolling average (monitored continuously 

\Vi th a cor.tinuous emissions monitori ng system:•, d r y 

b a s i s and correcced to 7 percen t oxyqen . The Permi.ttee 

must also document that, during the destruction and 

remova l effi~iency (OR&) test runs or their equivalent 

as provi d e d by §63 . ! 206(b) {7 ), hydroca r bons do not 

ezceeti 10 part s per million by volume during those ~ns, over on hourly rolling average (monito:::ed 

continuously tr;ith a continuo us emissions monit.o rirH:! 

s ystem), dry basis, corrected to 7 percent oxygen, and 

r~t>orted a s ;>ropane . {40 c.r. R. 63.~-5 al (5 ) ] 

/J! 7 

VES012292 
veolia Environmental Services 

ermi~ No .: V- IL- 1716300103-08-01 

!?age: B of 176 

(b) The Fermi ttee shall not allol< emissions of carbon 

monoxide emissions from t he incine rator in excess o f 

500 ppm corrected t o 50% excess air. !35 lAC 216 . 141, 

Construction pe r mi ts 83120053, 8710002 4, and 88010001 ) 

(c) The Permittee s hall not allow emissi ons of carb on 

monoxide emissions from the facility in exceSs of 6.6 

tons per year f or units 2 and 3 and 13.86 tons per 

year for unit 4 . !Construction permits 87 10002g and 

88010001) 

4 . Par ticulate Ha tter Limitation. 

(a) The Permittee shall not c aus e or allot" the 

emission of particu.l~te ma t ter into t he atmosphere 

from any inciner a tor burning more t han 0.907 megag,am 

per hour (l1g/hr; 2 , 000 pound per hour (lb/hr) l b ut 

less than 27. 2 Mg/hr (60, 000 lb/hr) of n~fuse to 

exceed 183 milli g rams ~r standard c ubic te~ 

(mg/scm; 0 . 08 grain per standard cubic foot (g r / scf) ) 

of effl uent gases correct ed to 12 percent carbon 

di oxide (35 lhC 212 .18l(b) j . 

-(-!>-) Pri9li te Oete~er u, 2QGB, tJ:ie Pe o:mittee si ... H Rot 

o liQ•·• ooOliuiGns of !_>a<tieYlate matte>' !'rem tlle 

gc ~ 1 j.;..y ~ n ey ""' ~ t;·f 3<1 ::11 -t 11 igrams per d~:y aRda..r.d~ 

- et1bl:e mecer (m l&selli)~G--;:e 7 pelo'Goot Cl<l'g:e.n .. 

--f4&-G7f'-7t\-. '; 6Z <1293 (a,-{"'H· 

(c) On and after October 14, 2008 , t he Pe rmi t tee -shall 

not allow emissions of particulate matter from the 

facility i n excess of 0 . 013 grain per standard cubic 

foot (gr/scf) , correccecl to 7 percent oxygen. (40 

C. f.R . § 63.1219(a) ('l) j 

(d) 'l'be Permittee shall not a llo>J emissions of total 

s uspended sol i d emissio:)S from t he facility i n e xcess 

of 15 .0 tons per year fot' units 2 cmd 3 and 16.92 tons 

per year for unit 4 . !Construc tion permits 87lOOOZ4 

and 880100011 

5. Volatile Orqeni c Compounds Limitati on . 

(a) 'l'he Permittee shall net cause or all O\\' the 

discha"ge of more than 3 . 6 kg/hr (8 lbs/hr) of organic 

material into the a~rnosphere from any emission unit, 

VES012293 
Veo lia Envil·cnroental Services 

t'ermit No . : V-!L- 1716300103- 08-01 

Pagt'l : 9 of 17£ 

-except that, if no ector nuisance exi sts, t his 

limi~ation s hall apply only 1:0 photochemically 

r eac tive ma terial. Al ternatively, Pe rmittee may use a 

control device to reduce such emi ssi ons either to 10 

ppm equivalent methane (molecular 'Ieight 16i or less, 

or to convert 85 pe rcent of the hydroca~bons to carbon 

dioxide and wat er. [35 ! AC 219. 301, 219. 302) 

(bl Orgenic mater ial emissions from the facility shall 

O'lOt exceed 0. 9 t ons 9er year for units 2 and 3 and 3 . 1 

t ons per ~rea r for unit. 4. (Const ructi on permits 

87100024 and 88010001) 

6 . Ni t:ogen 0:-;ide l .. imitation. 

Nitro9en Ox i de e mi ssions f rom ·t he facility shal l not 

e;; cead 4 . 0 tons per year for units 2 and 3 and 61 .6 

~ens per year for unit 4. {Cons t ruction permits 

87100024 and 880100011 

'· !-!azarclous Ai r Poll utant Limitati o ns. 

~! Prior t o Gct-obe-r--l~Q~e . .&e r,mi~ tee-s.lla.J..l-R <>.t 

_..j,l.Qw_f40~~:t ~~~·~.C....l'-·R.. 

-5-6-~ ...... 1-2·~ ~ .. -~.;. 

-<+t-~e~-a-l'>d-f~ s4<><l s-i-!1 E ,. Ge s r of 0 .2.0~'>9 

'f£9/eesm eeneeteoi te 1 pereeRt eny\jen+ 

(+i-}- ~c"'l' ><0 665 ~-:h>Q~r,o,.~~ r-r· 

·-etal*la-"~ -c..,.b.,i.;;-meter t> gids=~~.....l:o 

--"'--pe rce~ :..-o.;<¥9e.t).; -O.X:. 

..W..i.~l.eacLat>d .. =.d!IW.lm......W:.-e>:.ces.s-o.:f-UO 1'9 ldscm, 

C"mb j ne.cLemi.s.siru1 c: • c o r re c!:.e.cL_:.0-7_pe.r.c.e-n.t 

oxygaR: 

-(h") ,....ornJ> i nQd e!;l "'s~ lr:t$ Qf ~•;eAic, tO's¥yl~ffiT-~

cmi m~-e..,.c o. ss of S? ;.;qJG!~-4;G.o· 

.., fA "'CW-'1-t-o~.Q..I:h.. 

<b) On and a fter October 14, 2008 [40 C.f.R. 

S 63.1219\a) l : 

( i} The Permittee shall not. allo\-t emissions of dioxi n 

and f urans f r om the faci lity in excess of 0 .20 ng 

~EQ/dscm, corrected to 1 percenL c x ygen; 

VES012294 
veol ia Environmental Services 

Permit No.; V- IL- 1716300103- 08- 01 

?age: 10 of :76 

(iilThe ?ermittee shall rJot alloi<~ emissi ons of 

mercury from the facility i n excess of 130 

pg/ds cm, corrected to 7 percent oxygen; 

(iii)'!'he ?e rmi ttee shall not allow emissions of 

cadmium and lead from the facility ir. excess of 

230 }Jg/dscm, combined emissions, C·':lrrect ed t o 7 

percent o>:ygen; 

(i\t) TfH~ Pe rmi t t ee shall not allc\v emissions of 

a rsenic , be ryllium, and chromium from t he 

facility i n e:<cess of 92 pg/dscm, combined 

emissions, corrected to 7 percent oxygen; 

te l The Permittee sha:.l design, inst all. operate, and 

maintain a t reatment proc ess that destroys benzene in 

the ~;aste stream by i ncinerating the waste in a 

combustion unit that. achieves a dest~uct:i on efficiency 

of 99 percent or greater for benzene ( 40 C.P.R. 

S 61.348 tal t lJtiiiJ) . 

(d) P.ll joints o < s eams between t he pipe sections of 

any t ransfer system that consists of conti nuous hardpipi ng shall be permanently or semi- permanently sealed 

(e . g . , a welded joint bet,;een t HO sec~ions of metal 

pipe or a bol t ed and gasket ed f lange) (40 C.F.R. 

~ 63.6S9(c) (2)]. 

S . Hydrogen Chloride Limitations. 

-l-a) Prier tG O*eser ~ !40 c r:: .'t .. 

'.: 63 .1:00;§ ta.H-' 

~P.e!miHcc :ilall Ret .:: l-l~:f€k-*'M..Qx1g. ao;:i d ~nd 

~1 11 or i r. ~-~mi "'s i e~.s : r.;I1T-t>!.~;;-i-l."-t-)'-i.<>--e.xce ss . ..of 

-+=1--p-ai!...t:-&-~y vely;;a, coMit::~*i'O pmj ss'aos., 

e::10 resse€1-a·s-<wcll;9al:ll"ri c ,;c i<i G<;YiY3~ts, drr ba.s.i..s 

....,_a,(-'1,1 .ccrr&.--"tlid to 1 ps· .... ce .. .i~· C >':./9&J1 . 

(b) On and after Oc tober 14 , 2008 !40 C.F.R. 

§ ~3 . 1219 (a) l : 

'!'he Permittee shall not. allo" hydrogen chloride and 

chlorine gas <to t a l chlor ine ) emissions from the 

facility i n excess of 32 par ts per million by vclurne, 

VESOI2295 
As df tr:het( 

i~ S'ec&'-""' Tlf. b 

vf th• .tv(, I,;;.~;? 

~ff I; N~h·'" (t·;...{ 

Veolia En vironmenta l Services 

Permit No.: V- IL- 11!6300103- 08- 01 

I? age: 13 of 17 6 

2. the. Permitt ee mu st operate Un its ? 3, and 4 under t~ ~·9 

operating pa r ameters limits (OPL' s) demonstrate 

complianc e •,;ith Subpart EEE . is'h~J '" 1l.<, vN~rd.J· NOC- c;i l'~ ()( f ,, . APt t Ec . ~h l cf '"'" pruvi 

•·. "" ;'tj· ' lll. •X 

Operat.inq Pa rametoe rs 

t'1 !r.it~tum pr~ ~b ty c ombt1S t.1 on ' ~ 

Chi: n'.bt;~' ;~mpE- ature 

(63 .12C9t 7> <U . (); } ( Z}) 

·i+-1· -Uni..b-#4 

' ' 

AWE' CO 

N!r •.tmum 

ho~,;l'l y 

t:ollinq 

cv~raote 

'he~ 

A,fcib'(it.' .-1-... 

~ Sec.fie-o. C. !.''-

o{'fM-

'I l•lin.ir.,Jr.'! se·:-crodary <:cmb u$tiO:'i ch amb e r 

. O< . ' < H.lnimum 

hourl)• 

rolling 

~r~:b c~ A\ 

c(. c r;!o ... r e .. 

wrffv ~~-~~ 

~\. 

clc:~-: .... JH,,., o( 1;,,;,1, 

till 

c0rr:pE rat u :'9 

(63 . 120$(' ) (!), l k} (2)] av;:>rage I 

<i~ rn:;;r. fh:e gas flew!:' ate -- ! ~ -:.· ' ~ hourly ' ' - t ., C I 

or pr u.;;;;.ic .;"~ a:~e -~ . .. ' I r olli n'l t' I (63 1209( ) (2 ) ), (k)(3) , avcn:..!;9·::s 

(!ll) (2 ). {n ) (.SJ 1 (0 ) ( 2) ) 

l'le!Y. ililUin i"ta;:o:;.r dcH;s ,_.i!~r.e ' • r. ~~..l.2- ll~ourl:,.· 

pwnhlabl~ feed~::.te L'atP. for . . . "' I .. - ' .. • ~ l r:ol l ing , 1!'3Ch COI'fi!'>U r: t ion (:hbntbgr f'CC and av~!'b9e:'i 

(63. 1209 (:) 1 131 . l k) f41) 1,"!'~ ':' ; 

lbs/h.r t or 

sec 

Ma:r.imum haz.ttr d otl.s. waste ' -4 I - • -- ~ hout:'ly 

total feedrate rate fer . ~ r ollin<] 

each comJ>~.:: on i:Pb~r. ?CC t~r.6 .;:ve r~ g:e 

tG: . l ZO!i!j) {3}. CkJ {I) ) ) l , i S-:.' bi:s!-s 

lb.'J/hr fo~;· 

sec 

Opera;;ivn of '::4l~te firin<J ' I . ,. " .:-~ .. nst~n:an 

syst.em for eli ell l o cati on - F.' OS? .. . €:0US 

Er~ was t t• is fed t o the t ... . 1 --.... . - i - pi; i.~J;: 

inc!n~ratc.t G~.l109 j/ !41) .-eo.;, <l:1 0 ~ • "., .. .. 

' . - - : .. 'fir .. ' 

1< . . . ·:; ... - .. .. . •. . H.axb\Uln t~r: r& rtc of the ' • "' " "c hou.rl 'l -· . ... 

9•• !:J:': tho : n :et: ro llioq 

(G.; . 1209 ( 1. 1 U i >. {ol O l l C. tl'l! '<~ 

M!nim•J!!l. ca!l>!':"l it1ject 1o1: ,, ' " ... -+-ll>s+tw- h ot:dy 

rat9 {61 ' !2(}~ (}~} t6) ( 1) ) :<.1Uio.9 

~IVer=..·~e 

!1in i:nur:t car~ier fluir.i (gfJ;; 1-i/-A- '·' .. .. I . ... ·- or liquid) f l O\'H'oHe or • ~ I -.. pr~ssure 

((:;3 ' 1209 (

d

k

r

) 

o

<6

p 

) (ii; j 

~ l -4 • Ma:~ i!llu m lc.•w hourl;t 

:re~st:.:- .;;: rol1ing 

1 inch H·O a·.:2rag~ 

The b::-and i.": .• •; I ,, ,_ 

r.ufac -:: u::- ~r) ar1ct ty,?G ot "'.::-~ ri a= 

Cill'bC!I us ~ ·:Su i~9 tl\$ ~ 

co:np..::ehensive per or~,e: nc<i) r,:AA<;:v rs:. 

test (~J ll09 ) (6) (iii) ) 

l ~~l:ilt-'2 cr !nercur.y 12'- t'oC·lll' 

VES012296 
Veolia Envi ronmental Servi ces 

Pe rmit No . : V- l L- 1716300103- 08-01 

I Ooeratina Parametors 

(63 . 120 9(1) (l) ( i)) 

I·Ht ~ i fCIUJII ••h f ed& rat.& . -= (63 12 (m)(JJ) 

! l'ota l .t' ~d:rat e ot I I semi volatile mo:::-'l l :s I j (63.Uv91n J (~) rUJ J -----

i r t'otal f~~d r. t~ o'f l eu1 

1 vola tilE c~ta s 

I <63 . 1209 <nJ <2 l (Hl ) 

f'ee.:lr a t e limit.s !o ! lO\>f 

vo l a t ile ta ~ i n pumpabl e 

f~ed.stream:s 

(63.1209 (r>J (2 ) (vii) J 

Feed .rate o f t otal ch lorine - . 

- ar,d chloride i n .;!I 

fel!d Stce.lms {(~3 1209 n) ( 4) , 

(Ol{l )i 

f.l ir~i mnm sor>uen t: l~e tt' • 

H

(63 

i nim

. 120

l,im 

9 

~,r:

(0 ) 

rier 

(4 ) (i

fl

)) 

uid 

~ 

f'lo..,.r-at e o:: O('J:!.:tle pr: ssurt:: 

drop :for the Sp!:<l:f d t;y J 

old$Orber ( 63.1209 I 

(0 ) (4 ) ( 11)) • 

The bta.n<i ( i. e: ., .. " - - tner.uf.acc;u re:- r ) a:nd type o! sorbe-nt USG d durinq the c .. m&reh n:o:i ve p€r£or:Mnce • - t9St {63.1209 1.:.n.e G&el.s 

(O) (4 ) (ili) IAJ I , .... 

!?a g e: l4 oE 176 

~ AWFCO 

t e lling 

a1.reraq~ 

..... . 12 •J ~ 

- - .. - r o lling 

i a vE!raqe 

i 12 - hOUc I rollir.g 

avera9e 

1 limits 

12- hour rolling 

~verage 

l i r.U.ts 

::.2- hmsr 

olling 

~.,,.. rag'! 

l im.it!< 

- 12-hO\lr -· - - - - ... :: lin ~ 

;;,verage I 

·--

0 ' .. : - ' ' -. - . -·--" .. 

. 

. 

- - ~ .. ~" .. ,.. 

"';::.~ .. Ha::. imurn ccrnbus tion c ham.t>e.::.- ! .41- ~. ' -. o ' ' ., ' .. ~ 

pr.assu re {t:). l20 3i p ) ) ! 01 r. 

" . ·-- -H~l-·--·· --

i 

3. Comp liance \;ith standards ( 40 C.F . R. § &3 . l206 (b ) (1 1 ) 

The emi ssi cn sta!"lda rds and eperating requirements set 

f orth derived f rom Subpart EEE appl y at all time s 

except : 

(a) Durin9 periods of s tanup , shut down, and 

ma lfunc t ion; a nd 

(l>J When hazardous waste is not in the combusti on 

chamber (i.e., the hazardous ~1as e feeci to the 

combustor has been cut off for a period of t i me not 

.. ... ;; Z.P. Ei 3 

~4--

... : 

£0ll.!<-b.i: 

.!.!.1~ 

VES012297 
Veolia EnYironmental Ser...-ices 

Permit No . : V-iL-1716300103- 08- 01 

Page: 86 of l?~ 

{c) The Pe rmittee may petition t he Administrator to 

obtain \Yt"itten approval to bU.(n hazardous t<7aste prior 

to submitting ~ Notification of Compliance for 

pu~poses other than test ing o r pretesting. The 

Permittee must specify operating requirements, 

inc l udi ng limi ts on operating paramete rs, that the 

~ermittee determines wil l ensure compliance t-.•ith the 

emission standards of thi s subpart bused on available 

information i ncluding data from the failed performance 

test. The Adminis trator \-! i ll revie•.v, modi fy as 

necessary, and approve :.f warranted t he inter.i.rr. 

operating requirements. .•.n approval cf interim 

operating r equirements ttlill include c. s chedul e for· 

submitting a Notification of Compliance . 

15 . Surr:mary of recordkeeping requirements unde r Su.bpart 

EEE [40 C.F.R. § 63. 1 2 1l(b)) : 

The Permittee must retain t he foll >~ing in the 

ope rating reco.t"ds applicable to the Hazardous t-1aste 

Incinerators operated at this site: 

Reference Document, Da t a, or I :1forma tion 

40 C. t' . R. §§ 63. 1200, General. Information required to 

63 . 1C{b) and (c ) document and ma intain compl iance totith 

the regulations of Subpart EEE, 

i ncluding data recorded b y CMSs , and 

copies of all notifications, reports, 

pl ans, anci other documents submitted 

to the ~.dministrator . 

4Q C,f.'_..;"". ·m~~-O-li opar~tion . ~-~fct-H>.+tH ef::.aF.~es .f-.e~~-i~:· -9--'",;..i..:E-lt--~\.b~ 

~= , 

- ~ > O.t<;IJ-+J+.{.ii-) ,;;;,• . miHa . 

- .. - <>.t.a.t.ion 0~ c cmp l .i.anr;:. w i t h i"h.e 

§ § 9J-...t.2.94{.d.)..(.l} -{.i i+~ -e~.s.s.i,.on-,a,veragi n.g_re'"pd ment~ fo r 

63.l:~~9fdl m . . .eP. e lEHAS Ill~ ~!=!: H Ae :fe~;.-m~ . - ' .. ~~~~R~~pli~RCQ "ith the 

~.:h.~-(~+2-H-i-_i+ . -e;nj,.s.s.f.-OA-Jl • 'e r iVJ j n.g-r.eq.u.i.J;.e.tn.e.n.t.S-f.O r 

6' 12;l0 (<ill (.2+-( ' \\ ..p.::Ql:l~>~ to;;~ 0:£: pteboa4e~£p~era~sx 

!!HAS '..<!I::A El>;a l s.ea.e>l<s . 

40 c.r.R. If the Permittee elects to comply 

§ 63.1206 (b ) (1) {ii) with all applicable requi rerr ents and 

s t andards promt;lgated under authority 

of t he Clean Air 1\ct , including 

Sections 112 ar.d 129 , in lieu of the 

' 

VES012298 
Veolia Environmental SerJices 

~ermit tJo.: v-IL-17163001.03- oe - Ol 

!?age : 104 of 176 

hours of the initial survey, conduct a t e st using EPA 

Refe r ence Method 9 <see 40 c . F.R. part 60, appendi x 

A) . 

(a) If any of the visible emissions observations 

i ndicate visibl e emi ssions greater t han 20t opacity, 

the Permittee shall conduct Hethod 9 visi ble emissions 

observations of the emission point in question for 

thirty minutes each day, until two consecutive daily 

observations indicate visible emissions of 20% opacity 

or less. 

(b)If the Me t hod 9 visible emissions observation or if 

-cwo consecutive daily observations i ndicate visible 

emissi ons of 20% opacity or l ess, t he Permittee shall 

conduct >reekl y visibl e emissions ohservations of t he 

er:dssion point for three addit.i onal v1eeks . 

(E) Recordkeeping and Reporting [40 C.F.R. § 71 . 6(a) (3) ) 

1. The Permittee shall ma i ntain re cords of the total 

numbe r of d r ums crushed (d rums/ ho"r and drums/year) 

:or the drum crushe r, pursuant to 40 C. F. R. § 

7 1 . 6 (a) (i) (3) (Bl : 

2 . The l?erroittee shall calculate and keep r ecor ds of VOM 

emi ssions from the d r um c rusher based on the emission 

factor equal to 9 9n4 lb VOM/1 drum c r ushed. This 

emission factor is based on the conservati ve 

assumption that only methanol residue (•,;ith the 

highest vapor pressure) is released from the crushed 

drums. 

3 . The Permittee shall ma intain the fol lowi ng records of 

t he fugi t ive emissions : {40 CFR § 7L6(a) (3) (i) (8) J 

(a) ::~etails of. each visual su.r;rey or visible emissions 

obse ~vation, including date, t i me, obser~er and 

results for each emission unit and any other pollutant 

emitting activi ty; 

(b)Date, time and type of any investi gation conducted; 

u,ou< tt.S 

describ<'tl In 

S-edi,•-r- II.G. 

of .Afr; I, 2 C/.~ 

O.ff I ; m.fll)f'\ , 

VES012299