Figure 2 ,3 

## ..... no 

# ...,. ,**(M:f ~**  f .Ulrgg

## ~
') ":'W""' 

# '>--- ---

Rotary Klln In c in erator , lJnit 4 , Bloc . k Flow Diagram

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

# --- ·**~-"""~** - flM.'OIG
.. I\.W**~** A ftilr\Otl ' ooooo-**~** 'INI$1'! 1>\0<1'**~** I

- So.U'<fi Y A. Chf



### VES012200A carbon injection system is utilized for controlling dioxiiJifuran and mercury emissions. The activated carbon is a ir injected into the combustion gas immediately downstream of th e convergence of combustion gases from the SOAs . Combustion gases exit the SDAs and are distributed to two fubric ftlter modules. Ea c h module has three compartments in parallel containing multip l e fahric bags. Combustion gas passe s through the fabric bags. Particles in the combustion gases are deposited on the outs i de of each bag . During the bag cleaning cycle, a burst of air in the direction opposite to th e gas flow dis lodges particul ate matter from the ba g. 

### The induced draft 

### tim is located downstream of the fabric filter bagbouse. The indu ced draft fan moves th e 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 moni to ring system. This system features a multi

- component i nfrared gas analyzer that detects hydrogen chloride, carbon monoxide, and water vapor concentrations . 

### An integrated zirconi um oxide-based analyzer detects oxygen concentrations.



### 12 

### VES012201

### 3.0 STAR TUP AN D S HUTDOWN PROCEDURES The purpose of thi s s ection is to prescribe procedures for the startup and s h utdown of the incinerator system. This section also clarifies which actions are within the scope of the r egulatory definition of startup and shutdow n . To satisfy the requirements of§ 63.1206(c)(2)(v)(B) , waste feed restricti on and operating limits have 

### been im p osed to startups and shutdowns. During a startup, the f eeding of hazardou s 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 wi th the requirements of§ 63.1206(c)(2)(iii), Veolia Mll utilize 

### an oxygen correction factor of 1.6 (i . e., 12.3% 

### 0 2) during periods of startup and shutdown. This will elimina te wide variations i n corrected CO concentratio n 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 i ncinerators. This "default" oxygen correction factor 

### can only b e util i zed when the waste res i dence time in the primary combustion chamber has expired and when the incinerator is in startup or shutdown. Veolia has deve l oped standard division practices (SOPs) for the operation of each incinerator system and an cillary equipmen t and systems. The SDPs containing startup and sh u tdown procedures for the incinerators are:

• SDP 2201 • SOP 2417 

### 3.1 S tartup 

### 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 po llution control system may b e in servi ce upon commencing 

### a startup . 

### Thi s will be reflected on the startup record (see Attachments 

### 1) . During 

### a startup, waste will not be introduced until a ll operating panuneters are within limits. A startup event is concluded once waste is intro duced and all operating parameters are within limits . \I

eolia's 

### startup p rocedures are representative of safety and good 

### air pollution control practices. Tl1e procedures are designed to minimize tbe potential for exce ss emiss i ons by ensuri n g th at 

### aU equipme n t is fully operatio n al (within permit limits) prior 

### to the
13 

## VES0 12 202introduction of hazardous waste 

### to the system. Adherence 

### to these startup procedures will employ th e knowledge and skills demonstrated through the implemenlalion of the Ope!'lllor Training and Certification Program .

14 

## VES012203

### 3.2 

### N orma l S h u t down Some shutdowns will allow the primary comb u stion chamber to cool. Prior to t h ese shutdow n s, the incinerator will be burniug auxiliary fuel onl y and 

### the hazardous waste residence time wi ll have transpired . A shutdown will b e in i tiated with the shutoff of auxili ary fue l 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 al l of the air pollu tion co n trol system m ay remain i n operating mode at the conclusion ofa shutdown through the subsequent startup. Veolia 's shu tdown procedu res are representative of safety and good air pollution control practice . The p rocedures are designed to minimize the potential f or excess emiss i ons by ensuring that all waste feeds are off and/or the hazardous waste residence time has transpired prior to the shut down of the inci n erator sys tem. Adh e rence to these shutdown procedures wil l employ the knowledge and skills demonstrated through the implemen tatio n of the Opera tor Trai n ing and Cert i fication Program. Procedures for emergency shutdown are des cribed i n the next section regardiug malfunctions .



### 15 

## VES012204

### 4 .0 MALFUN CTIO N S The pwpose of this section o f th e Startup . Shutdown and Malfunctio n Plan is to:

• .Define po tentia l malfunc t i ons an d their causes • .Describe measures to minimize 

### the frequency and sever i ty o f malfu n ctions. • Presc t ibe procedures for operating and maintaining the inc inerator during mal funct i ons • Prescribe actions to correct the cause of a malfunction A s ummary of potential malfunctions and their 

### causes is giv en in Table 4-1 . This list of potential malfunc ti ons is arranged accordi ng to unit operations. The occurrence of any ev e nt listed in Table 

### 4-1 shoul d be responded to as 

### a malfunction an d 

### a malfunctio n recordkeep in g fonn, inc l uded as Attacbment 3, sho u ld be initiated. During the response to these events, it will 

### be de tenni ned if tlte event m eets the regulatory definition of 

### a malfunction . 

### 4.1 Me a s ures ro Minimi z e th e Frequ enc y ofM a lfiUl ct i o n s The following measures contribute to prevent malfunctions:

• Incinerator system des i gn consistent with safety and good engineering practices • Hw..ards and operability studie s of the inc i nerators • Appropriate frequency of preventative maintenance and ins p ectio n • Good operating practices • We ll trained and qualified personnel Veolia's performance history, this document, and the following regulatory documents serve as evid e ttce of Veolia ' s pro activ e measures to minimize tlte fr equency of mal funct i o ns . 

### • Operation and Maintenance Plan • Operating Tra ining and Certification Program • Continuous Emissions Monitoring System QUtJiity Assurance Plan (GEMS QA Plan) • Continuous Monitoring System Quality Co!llrol Plan (CMS QC Pl an) 

### • Automatic Waste Feed Cutoff System O p erability T-est Procedures

16 

## VES0122 0 5

### Tabl e 4-1 Summary of P o t e

ntial Malf u nc ti ons and C auses Potentia l Malfunc ti ons for U nits 2, 3, and 4 P otenti a! C a lLus fo r a l\

lalf u coon 

### G

ENERAL ·· Low Wato r Level in Slag C<>Uection System (Unit 4)

- Loss of Eleclrical Power Supply ··Ra pid Steam Gc:uc:rniion from Ash Collection S ystem Water

- Loss of l u..

'i>trumentJP lant Air Supply T EMPERING CIIAIItliE R (UNIT 4)

- Loss o f Plant Nitro&en Supply - Loss ofTemperi ng Chamber Exit Gas Temperature Control

- Loss o f City Water Supply - Loss ofAtomization Air Pressure to Nozzle Mecbanical/eleetrical

- Loss of**Pro~** Water Pressure/Flow (U ni t 4) LIME S LURRY SYSTEM failure o f rotating

- Mal functio n of Safety Interlock or Automatic Was t e Feed - Loss of Lime Feed to Limo Slurry Feed Tank equipment. CUtofflntor l ock - Malfunction in Lime Slurry Concentration

- Excessive Air In

- leakage in A iT PoUution Control System UNITS 2 AND 3 SPRAY DR YER .ABSORBER (S D A) Phtgging/physical fa ilure of PRIMARY COMBUSTION CflAM .B E R - Loss of Lime S l urry Flow to SDA

- Loss of Natural Gas Pre""-ure/Flow to PCC Main Bumer - Loss ofLime Slurry Fl ow Contro l l ine s/ n ozzles

- Loss o f Combustion AiT Pressure/Flow to PCC - LossofCityWaterFiowtoSDA

- PCC Main Burner Pilot Failure - Loss ofCoo l ing A.ir Flow to Atomiz,cr Physical/el ectrica l failn"'

- Loss ofWa."e Flow to PCC lrtieeto r - Loss ofSDA Exit Gas Temperarure Contro l of instrumentat ion

- Loss ofWasteFeedt"a t e Con trol t o PCC Inje ctor - Atomiu.c Failure

- Loss ofA to m ization Air Pressorc to a PCC 1 J1iec to r UNI T S 4 SPRAY DRYER ABSOIUJER (SD A) Mechanical/elect rical

- Lossof P CCDraftControl (Unlt 4 ) - Loss ofLime ShuYy Flow to SDA fa i lure o f actUated

- Loss ofPCC Tewper • ture Control - Loss ofLime S l urry F l ow Control!E:ti t Gas Temperlllll"' val ves/dampers

- Flame Fail ure Contro l

- Kiln Rotatio n Malfunct i 011 (Uni t 4) - Loss of A tomizat ion AiT Pressure to S DA No zz l e Physi cal/electrical fa i lur e

- B u lk/Charge Feed Door Malfunct ion CARBO N INJECTION S Y S TEM (UNIT 4) ofcontrol sys tem

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

- PCC Seal V isual Emissions Monitoring and Recording System - Loss/ Restri<:tion of Activ ated Carbon Flow

- Rapid Steam Geu .erntio n from Ash Collection S ys tem Water - Loss ofPlant A.ir Pressure/F l ow t o Carbon Bulk Sack Mechanical/electrical SECO N DARY CO l\

tli USTI ON C llAl"dBER BAGBOUSE & INDUCED DRAFT ( ID) FAN failure ofutility supplies

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

- Loss of Combustion A.ir Pressure/Flow to SCC - Bag Blinding/High-High Pressure Drop E l e ctricaV a ctuation failur e

- SCC M ain Burne< Ignition Failure - L o ss of Sta ck Gas Flowrate Contro l (Unit 2 and 3 ) of s a fe\y interl ocks

- Loss ofWas t e Flow to SCC In j ector - Baghouse Isolation Damper Malfunction (Unit 4)

- Loss of Wasto Fcedra t c Contro l to SCC Injector - ID Fan failure Physieallmechanicnl

- Loss of Atomization Air Pressure to a SCC Injec to r CONTROL SYSTEM/C ONTINUO US M. ONl T ORINC internal equipment fai l ure

- Loss of SCC Temperature Control SYSTEM

- Flame Fai lure · - Cootro l System/CootinuoU$ Monitoring System MalfWtCtion

- E m ergency**fe~y** Vent Opening - Continuous Emis.'lions Monitoring System Malfunction

- Pbysica i/

Mecbanical Internal Equi pm ent failfi(<) 17 

### VES01 2206

### Despite these efforts, equipment fai l ures and other operating anomali es can occur. W ithin the scope of regulatory requirements , t he operating record wil l contain the appropriate documentati on to estab lish that poor maintenance or careless operations are no t contnouting factors to the cause of 

### a malfunction . 4 .2 Meas ures to Minimize th e Senri ty o f Malfun ctions The following measures contribute to mi n imize the severity of malfunctions:

• Alanns and interlocks • A WFCO 

### testing • Failure positions for critical equipmen t • We ll trained and qualified personnel • Design ofthe incinerator system Typically, an event that m eets th e definit i on of a malftmction will trigger an alarm. 

### An alann infon n s the operator of the s ituation and may provide an opportunity to avo i d an exceedance . If 

### conditions become unsafe or exceed operating limits , interlocks are in place for an automated response that is specific to t he triggering condit ion. Refer to Veolia's Documentation of CompliJ:Jnce 

### or Notification of Compliance , 

### whichever is currently applicable , for details on A 'vVFCO 

### con d itions. Additional detail s on alamts and inter l ocks are maintained on piping and i ns trumentation diagrams (P&IDs) The mo s t critical key to minimizing the severity of malfunc t ions is 

### t he functionality of A WFCO interlocks. Accordi ngly, 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 m anner that will minimize the re lease of hazardous air pollutants. Through traini ng and job experience, the operat . or will h ave the process knowledge that qualifies him to use di scret i on 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 malfimctio n s . 

### An operator can evaluate process conditions and alarms and 

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

### th e malfu n ction adversely affects t h

e functiona lity of alanns, interlocks , or fail safe positions, the operato r must recogniz e the situa t ion and respo n d appropriately. [n 

### the event that the malfunction affects the ability to auto m atically cu toff waste, the operator will manually cutoff waste feeds as quickly as possible.

18 

### VES012207

### The design of the each inc inerator system o l so ensures th at the severity o f malfunctions will be minimized. This includes alarms and inter locks, the fail sa fe position of actuated valves , and redundant instnnnentation and proce ss equipment. Also, the design of each i ncinerator's instrumentation and control systems provides the operator conveni ent access to pro cess variable indic a tio n , including position indication of selected actuated valves . Thi s is essen t ial to providing the operator the informati o n required to best e valuate sys tem conditions and responses. Table 4- 2 lists potential m alfunctions and associated r edu n dant equipment and system s that are available to preven t tbe se malfunctions or to minimiz e th e potential for a sign i ficant rc l ellSe of hazardous 

### air pollutants. 4.3 Cor r ect i ve Measur es Th e 

### Program of C<!rreCJive Accions for Mo/fon ction.s is Attachment 4 of this document . This program addresses how tbe incinexator 

### will be operated and maintained during malfunctions . In this program, potential malfun cti ons are listed for each portion of the incinera tor systCllJ . The malfunctions are t."Vent s that will be recognized by the op erator, or indicated by an alarm, and 

### threaten to cause an exceedance. In 

### the response to the malfunct ion aodlor alanns , the op e rat or 

### w ill app l y discreti on and attempt to m aintain the incinera tor sys te m withi n regulat ory li mits. In the program of corrective actions , po tential causes of eac - h malfunction are lis t ed. The operator 

### will u t ilize proces s knowledge, job exp erience, and , if needed, assistance from oth er personnel to identi fy 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 multidiscipl i ned personnel wb o are qu a l ified t o return the incinerator system to proper working condition s (i. e ., maiotenance personnel, control sys tern techni c i a ns , engineering ) .



### l9 

### VES01 22 08

### Tabl e 4-2 

### R e dundant Equipment and Syst em s f or Minimizing t h e F reque n cy or Severity of Malfunc ti ons Redund a nt Equ l pmenr / Sy5tem 5 l'otential Malf uncti on s Preve nte d / Minimized Emergency generator (Unit 4) Loss of Electrical Power S upply Universal Power Supply (UPS) sys tem powers Loss ofElectrical Pow er Su pply computers, monitors, an d control systems Two compressors are on hot standby (Unit 4) Three 

### air co mpressors running an d one compressor on bo t standby (Unit2 and 3). Loss of Instrument/P l ant Air S uppl y Dua l Process Water Pumps Loss ofProcess Water Pressure/Flow Dedic ated PCC combustion air fan (Unit 4) Loss o f Combust i on Air Pre ss u re/ F lo w to PCC Dedicated SCC combus t io n air fan ( Un i t 4) Loss of Combustion Air Pre ss ure/Fl ow to SCC Spare SCC combustion air fan (Unit 4) Loss ofTempering Chamber Ex it Gas Temperature Mul t iple Tempering 

### Chamber N ozzl es Contro l Loss ofAtomization Air 

### Prcssun: to N ozzle Dual Sluny Feed Pumps (U nit 4) Loss of Slurry Feed to SDA Shared Ba c k-up Pump (Unit 2 and 

### 3) Off-line Spar e Lime Slurry A t omizer (Unit 2 & 

### 3) Atomizer Failure Loss of Lime Slurry Fl ow t o S DA Dual S DAs (Unit 4) Loss ofLi me Slurry F l ow Co nt rol/Exi t Gas Temperature Control Loss of Atomization Air Pressur e to SDA Nozzl e Off

- li n e S pare Baghouse Module (Un i t 2) Tom/Leaking Bag Two b agh ouse modules with three 

### compal1ments each. 

### 5 compartments provide sufficient particul ate Tom!Leaking B ag removal so that one of the 6 compartments can be 

### isolated as a spare. (Unit 4)



### 20 

### VES012209

### ATTACHMENT 1
STARTUP RECORD KEEPING FORM

VE S012210

### VEOUA E -NVIRO N MENTAL S ERVICES, 

### IN C. INCINERAT OR STARTUP RE C ORD (Pogo I of3) This report penoins t o astottup ol' Unit 2 I 3 I 4 (cirel e one) . Starrup event ini tiated on: (}.lootb/Day/Y""' , Ho..,. : Millutes) StartUp ewnt CXltiCIUded oo: (Month!Oay/Year, Hours : M i n"tes) 'The to tal durn l ion ofthi s startup even t**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 (SS MP) . 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, d escribe tho lnconsistent actions below.

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

l ease lis<idescn'bc. lf any**:~.ction.s** were no1 coosis t ent with the SSMP and an o p erating parameter limit wxs exceeded. an immediatQ SSM report I s requ i r ed.

The following signature cert i fies the a cc uracy oflb is record: (Name) (fitle) (SiJ!Dat ure) (D ate)



### VE S0 1 22 11

### VEOLIA E IVIRONME NTAL S ERVICES , INC. INCJN£RA TOR S TARTUP RECORD (Page 2 of3)

Uait 2 and 3**lnclnen~tor** Startup C heddut

Verify th at pre-sta rtu

p h os been comp leted Check tl tennal relief vent (TR. V) Stal.1 co mbu s ti on a i r 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 . M on

itor SDA 1empe111tutt wllile r>mpini up stack gas ll owrate CloscTRV Start time slWl')l Estabtish aU o perati n g poramet ers withi n limits Open tor's Notes: J nltinb

Note: Cenain a ir polluti on**trol** and ancillory oquipment mAy be op erati onal prior t o stanup ( Signatur e of Shill Leader or 

### Dc:oisnoe) (Dote)



### VES012212

### ''EOLIA ENVIRO NMENTAL SERVI CES, INC . I NCINERAT OR S T ARTUP REC ORD (Pogcl of3)
Unit 4btctncntor Startup Cbccklfst

Verify that pre · startup has been oo n tpleted Check thermal re l i

ef -t (TR V) Sl4n ID fun and set kiln droft {s!Jirt of purge cycle) Stat! S CC combustion a ir fan Sl4rt tho kiln combustion air fun (purge cycle complete) Stan 

## sec main**b~** and t<mpcnture B mp-up Starti 'CC main butner lind ltmperature temj>-up Start k iln rotat ion be f oro SOO ' F SIAn t ho kiln seal air Stan the 

## sec cnnveyor Set up the l<rnpering chamber for operation Set up lime s lurry injec t ion system Set up the SOAs fo r npcration Se t up the ash collecti on sys leln Set up the bagbous<s for opcratioo S l

owly ramp-<>p the tonporing cbamber exit t cmpentture Cont inue PCC and 

## s ec temperatur e romp-up Starl tlt e kiln sc-aJ conveyo r E£tabliJ;h all oper• ting perameters within J i.Uu Opnator , s Notes . : Initials 

# I

N ote: Certain •ir palluuon con t ro l and WlCillary equipment moy be oper> ti onal prior t o starwp . {Sia nature of Shift l..eader o r Designee) (Dat e)



### VESOJ2213

### ATTACHMENT2 

## S HUTDOWN RECORD 

## .KEEPING FORM



## VE S012214

### \ 'E OLIA E NVIRONMENT A L S ERVIC E S, IN C. INC I NERA T OR S .BlJTDO"\\'N RECORD (Page I of3) Tbis repo rt p..'ltoin"o a shutdown ofUnit 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 to tal dun\li on ofth j s s h utdown event wnl': -.,.,(lt.,..o-t llS -: M=in

- utes

,....,-}- Attached**o** UUJ: form is a cbecklis t t lu

u $Urnmarizcs tbe approved shutd own 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 ael i om below.

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

any a ctions were not consistent with th o SSMP and an operating parameter limit was exceeded, au immediate SSM report ls requited .

Notes!R cco mmeodations;

Tbe followin g •lgn nture c ertifies the a c cumcy of tbls rocord: (Name)**(l'i o}**  (S """"""} (Date}



## VESOI2215

### VE O LIA ENV IRO NMENTAL SER V I CES, INC. INC I NERAT OR S HUTDOWN RECORD (Page 2 of3)

UD.i t 2 and 3 l uciDe . r a tor Shutdo wn Checl<.Ust Verify lhat all was!¢ feeds are off and/or lhat the hazardous waste residence time has transpired Monitor CEMS output t o verify stable oonditions Open the stack cap Stop the ID fun Shu\ off water and l i me slurry flow to the atomizer R

emove atomizer and positi on tid Operator' s Notes: Initials

Note: All or certain air pollution contrOl and ancillary equipment may remain operational thro ughout s hutdown. Once the hazardous waste res i dence t im e has tranSpired, operator's discretion can be app l ied .

(Signature of Shill Leader or Designee ) (Date)



### V E S0122 16

### VEOLIA ENVIRONMEl'fT AL SERVIC ES, INC. INCINERATOR S HUTDOWN RECORD (Page 3 o£3)

Unlt 4lncinerator S butdo w u C h et klist Verify t hat al l wasrc feed• o re off and/or t hat !he hazardous waste residence time ba s irnn spired Shot offthe ki ln bu rn er a nd SCC bun1 er Shut offthe 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. sh ut off the ID fan Ope-rator ' s Notes: loltlab

Note : All or certain air pollut ion con1r0l and ancillocy equipment may reDUiio opera t iOO:II t hroughO<Jt shutdo wn. Once the hnzttrdnu.-, wM1e residence time has transpired, ope r atOr's di!;crction C M be applied . (S ignature of Shift Leader or DcsigD<e) (Dat e)



### V E S012217

### ATTACHMENT 3
MALFUNCTION RECORD KEEPING FORM

VES012218

### VE OLIA ENYm.O N MENT AL SER V I C ES, INC. I\-1ALFUNCDO N RECORD (Page I oft) This report POI " tains t o . malfunction or Uni t 2 I 3 I 4 (circle one ). The malfunction event occurred oo; (Moo t hiOay!Year, Hows: M inutes) 'The malfunction event ooocJuded oo : {Month!D'•y!Year, Ho ur s: Minute s) The total duration ofthis malfun ction evcnl was : (Hours : M inut es) The Voolia Program QjCorrecri"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 ofthe malfunction, and the corroot i ve actioas W:en:

Waste Focd3 off T ime

- l.ttcinerator "CCear of\Vasto" Time 0 0 Wore all actioOJ OW<J<:i ated with this malfunction event in conformance ,..it b the SSM.P'I Yes I No (circle one). I f no . iniLJatc an immediate starrup . sb u tdo"'n, ond malfunction report. Ustldescribc dle cxceedances th a t oeeurrod (or beli eved to ba ve oc curred) d ue t o tl 1 is r nu lf unc t ion:

Notes/Rccommeodations :

The following oignature certifies the accuracy ofthis record : (JIIame) (Si&DAture) (Date)



## VES012219

### ATIACHMENT 4 PROGRAM OF CORRECTIVE ACTIONS FOR . MALFUNCTIONS



## VES0122201.0 GENllRAL 

### PROGRAM OF CORRECTIVE ACTIONS FOR MALFUNCTIONS TABLE OF C ONTENTS 1 . 1 Operuing and Maintaining th e S)'l'tem during Malftmetioos I .2 Loss ofE l ectrical Pow.r Supply 1.3 l ..oss of Wirumeni/P iant Air Supply 1.4 Loa of Plan t NitrOgen Supply l. S Los s of City Watet Suppl y 1. 6 Los• of Process Water Pressure/Flow (U nh 4) I .7 Mnlll mct ioo of Sa fety Inte rlock o r Automatic Waste Feed C utoll' Interl ock I .8 Jl xc:euivc Air In -leakage in Air Pollu ti on Co n tro l System 2.0 PRIMARY CO MBUSTION 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 ofWaste Row to PCC Injector 2.S Loss ofWute feedr.lte Contro l t o PCC 1 '1iector 2.6 L<>ss ofA t omi2>ti on Air Pressure to • PCC Jn,j ector 2. 7 L<>ss ofP CC Draft Contro l (Unit 4) 2 .8 Loss ofPCC T empera ture Conoro l 2.9 f la me Failure 2. 10 K i ln .Rota tion Malfunction (Unit 4) 2 .11 BullciCharge Feed Door Malfuncti on 2 .12 Physical i Mecbanieal lntcmal Equi pmen t 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 CO MBUSTION CHA"IBER 3 .1 L<>ss of Narural Gas Prc ssurei'Fl o w t o SCC Main Burner 3.2 1..<>55 o f Combusti on Air Pressurei'Fl ow t o SCC 3.3 

## sec Main Burner l&nitio n Fai lure 3.4 L.O SI o f Waste ·Flow "' 

## sec Inj ector (Unit 4) 3.S LoM o f Was te Feedrato Cont r o l t o SCC I njec t or (Unit 4) 3 .6 L oto of A to mization Air Pros.sure to a SCC lqjcoto r 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 o fT e mp c rin g Chamber &i t o., Te mperature Cont ro l 4 .2 Loss of A t omi zation Air Pressore t o Nozz le 5.0 L IME SLUlUlY SYSTEM 5. 1. l.o.<• of Li m e Feed to lime S lurry f <ed l ' snk S .2. Molf\mc t ion in Lime Slurry Concentration 6 .0 UNITS 2 AND 3 SPRAY DRYE!t ABSORB ER (S DA) 6 . 1. Loss of Lime Sluay Flow to SDJ\



## VES OI222 16.2. Los. ofLime S l uny flow Conl ro l 6.3. l.oos of Crty Water Fk>w 10 SDA (Unil 2 at>d 3) 6.4 . Loos ofCooling Air Flow 10 Atomizer 6.5. Loss ofSDA Exit Gas Tempera ture Coruro l 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"' 1 0 SOA Nozzle 8 .0 CARB ON INJEC TI ON SYSTEM (UNIT 4) 8.1. l.os• ofCarr ie r Gas Pres sure 8 .2 . l.c<ls/Reslricri on ofActivated Ca r bon Flow 8.3 . Loss of Pla nt 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 Ma l functi on (Uni1 4) 9.5. 

### m Fan fa i lure I0. 0 CONTR OL SYSTEM/CONTINUOUS MONITORING SYSTEM JO. 1 . Cootrol Sys tcmfContinu o

us M onito ring System Malfunc ti on 10.2 . Cont lnoous Emissions Monitoring Sys t em Mol func t ion



## VE S0 1 2222VEO LJA ENVIRONMENTAL SERVICES , INC. PRO GRAM: OF CORREC fiVE ACf l ONS FOR MALFUNCTTON S

1.0 GENERAL 

### 1.1. Oper a tin g an d M aintai ning the Sys tem during M a l f un ctio n s 1.1.1 . Due to the s udd en, .infrequent, and unusual conditions associated with malfunctions, continua lly 

### evaluate th e situation . 

### U sing di scret i o n , respond 

### in a manner consistent wi th safety 

### and good 

### air pollution co ntrol practices. 1.1 .2. Take th e 

### following actions to minimize the rel ease 

### of hazardous air pollutants 1 .1.2.1. Cutoff 

### all waste feeds 

### an d/or confirm that tiJc automatic 

### was t e feed 

### cutoff system functioned properly . 1.1. 2 . 2. 1.1.2.3. 

### Maintain operating parameters within l i mits, i f poss ible . 

### I f ap p lica ble, follow the pro cedures provided by the 

### Emerge n cy Safety 

### Vent Plan 1.1. 3 . 

### K eep supervisor and/or maintenance 

### supervisor informed , 

### as appropriate. 

### J.l.4. I dentify th e ma l f unction 

### and potenti a l 

### ca us e . 1.1 . 5 . Imp lement corrective 

### actio n s inv olving th e troubleshooting of 

### failures and 

### th e servicing and/or replac ing 

### of components, 

### as needed . Re fer t o manufa cture ' s troubleshooting and service recomm endations, 

### as needed. 1.1.6. 

### Record th e appropriate information using 

### a 

### malfw1eti on record 

### form. 1.

2. Loss 

### of Elec trical Power S upp ly 1.2.1. Verify p roper 

### fail u re positi on of actuat ed valves. 

### 12 . 2. I denti fy link in power s up p ly path that is not operational. 1. 2.3. Take the necessary actio ns to 

### restore the s upp ly of el ectrica l 

### power. 1.3. Loss of In stru m en t/P l ant Air Su p ply 1 .3 .1. Verify proper fai lure position of actu ated valves . 1.3.2. In case 

### of plugging/physical fai lure ofline or line components: 1.3.2.1. Identify the 

### location/caus e of th e 

### restriction of instrument air flow. 1.3.2.2. Clear line plugging an d/

or service/replace faul ty l ine**co po** **net~ ts,**  as needed. 

### Page I of26 

### VES012223\ 'EOL IA ENVIRO NMENTAL SERVICES , IN C. PRO GRAM O F CORRECTIVE ACTIONS FOR MALFUNCTI ONS 1.3.3. 

### I n case of 

### mechanical/electrical failure of actuated valve: 

### 1.3 .3. 1 . Identify 

### cause of actuatio n 

### failure. 1.3 .3.2. Service/rep lace electric a l and/or 

### pneuma t ic components, as needed . 

### I .3. 3.3. Serv i ce/replace actuator and/or v a l ve components, 

### as 

### needed. I .3.4. I n case of

### mechanical/ electrical fuilure at ai r s uppl y 

### source: 1. 3.4.1. I dentify the 

### cause of

### the fui lure . 1.3.4.2. Tnke the 

### necessary actions to restore th e 

### supply of instrument/plant air. 1 .4. Loss of P lan t Nitrogen S upply 

### 1.4. 1. In case 

### of plugginglph)'l>ical failur e of 

### li ne or 

### l ine components: 1. 4. 1.1 . Identify the location/cau se of 

### the restricti on of 

### nitrogen 

### flow. 1.4 . 1. 2 . 

### C l ea

r l ine pluggi ng andf or 

### service/replace flm lty line compo nents, 

### as needed . 1.4.2. fn case 

### of mechanical/electrical fai l ure of

### actu a ted v a lve: 

### 1 .4.2. 1 . Identify cause ofac tuati on failure. 

### 1.4 . 2.2 . Service/replace electrical and/or 

### pneumatic components, as 

### needed. 1.4.2.3. Service/replace actuato r an d/o r wive components, 

### as 

### needed. 1.4.3 . 

### 1n case ofmechanical/electri cal failure at nitrogen supply source: 

### 1.4 .3. 1 . Ident ify th e cause of th e failure. 

### 1. 4.3.2. Take 

### the necessary actions to res tore the su pp ly of 

### nitro gen. 1.5. Loss o f City Wntc r S uppl y 

### 1.5.1 . In case of plugging/physical failure of

### l i n e or line co mponents: 1.5.1.1 . 

### ld. cnttfY the locati on ofpi uggi ng or 

### line f11ilw·e. 1.5.1. 2. C l ear line plugging an d/o r s ervicclrcp l acc faulty line com p onents, as 

### needed . I . 5 .2. 

### I n CIISC of**mcchnnicallel~cal** fail ure of 

### ac.tuated valve: 1.5.2. I . Identify cause ofnctuation failure . 1.5 .2.2. Service/replace electrical andlo . r pneumatic 

### compo nents, as needed. 

### Pag e 2 of26 

## VES012224

### VEOLlA RNV l RO llo ' l\fEJ\'TAL SE R

VIC E S, INC. P

ROGRAM O F C ORR ECTIVE ACTIO NS FO R MA . L FUNCT I ONS 1.5.2.3. Service/replace actuator and/or valve components, 

### as needed. 1 .5.3. In case 

### ofmecbanicaVelectrical failur e at ci t y water supply source: 1. 5 .3 .1 . 

### Ide ntify the cause oftbe failure. 1.5.3.2. Take 

### the necessary actions to restore 01e SUI>ply of city water. 1.6 . Loss 

### o f Pro cess Water P r essure/Flow (Un i t 4) 1 .6.1. 

### For loss of city 

### water supply to 

### process water 

### tank, see I.S. !.6.2. 

### In case 

### ofmecbanicaVelectrical failure ofprocess wnter pwnp : 1 .6.2. 1. 

### Diagnose pwnp/drive failure. 1. 6.2.2. Service/replace the pum p/drive, as needed . 1.6.2.3 . 

### Restore electrical power supply to the 

### pump. 1 . 6.3. 1n 

### case of plugging/physical failu r e of line 

### or line compo n e

nt s: 1.6 . 3. 1. 

### Identify the l ocation ofp luggi ng or line faih1re. 1.6.3.2. 

### C l ear line plugging and/or service/rep l ace faldty line components , as needed. 1 .6 .4. 

### In 

### case ofmechanicaVelectrical f ailure of actu a t ed valve : 1.6.4.1 . 

### I dentify cause 

### of actuation fuilu r e. 1.6.4.2. 

### Service/replace e lectrica l and/or pneumat ic 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 contro l system 

### component. 1. 6.5.2. Service/repl ace control system components , 

### as needed . 1. 7. 

### M alf u n cti on of Safety I nter l ock or Au to matic Waste Feed C utoff Inte rl ock 1. 7 .I. If 

### safety interlock or A WFCO 

### interlock was erroneous ly triggered, proceed with corrective actions. 1. 7 . 2. If 

### safety or A WFCO 

### condition exists b u t automated response failed, cutoff was te feed as 

### quickly as 

### possible, then proceed 

### with correcti ve actions. 1.7 .3. 1n case 

### of

### phy sical/electrical failure 

### of instrwncntali o n : 1 .7.3.1. 

### Identify fuulty instrumentation component. 1.

7.3 .2 . Service/rep lace fuulty instrumentation components, as needed. Page3 

### of26 

### VES012225

### VEOUA ENV I RO NMENTAL S ERVICES , INC.**ROGRAM ~**  

### OF CORRECT I V E A CfiONS FO R MAL FUNCTIO NS 1 . 7 .4. 

### In case of mechanicaVelectrical failure of actu ated val ve/damper: 1.7 

### .4 . 1. l dwti fy cause ofactuation 

### failure. 1. 7.4.2. Service/rep la

ce e l ectJical and/or pneumatic com ponents, as needed. 1.7 .4.3. Service/re place actu ator and/ or valve components, as ne eded. 1. 7.5. 

### In caseofphysical/cl . ecbica l fa ilure of control system compo nen t: 

### 1.7.5.1. Identify faulty contro l system component. 

### 1.7.5.2 Service/replace contro l 

### system components, 

### as needed. 1. 8. Exc ess i ve Air ln- l ea.kage in 

### Air P oll 11tion Control Sys t rm 1. 8.1 

### In 

### case of bo l es due to corrosio n : 1. 8 . 1.1. Id entifY locatio n of ho le . 1.8.1.2. Repair sys tem as needed . 1 .8.2 

### In case ofopen p orts, man ways, access port s, e tc. 1 .8.2. 1. Identify locati on of open 

### port, manway , etc. 1 .8.2.2. Re p l ace cover on open port , manw ay, 

### etc .

Page 4 of26 

### VES012226VE OLIA £ NVIR O NJ\I l £NTAL SERVI CES , INC. PRO GRAM O F C ORRECTIVE A CTI ONS FO R MALFUNCT l ON S

2.0 PRIMAR Y C OMB USTION CEIAI\ ID E R . 2 . 1 . L oss o f N a tu ra l Gas Pr ess ure/ Fl ow t o P C C Ma i n Burner 2.1.1. ln . ca se of p l ug ging/p hysical fitilure of l ine or line component: 2 . 1.1.1. Identify 

### the location ofp l ugging or line failure. 2.1.1 . 2 . Clear line plugging and/or service/replace faulty line components, as n eeded. 2.1 .2. In case o f mechanical! electrical failure ofa ctuated valve : 2.1.2 .1. I dentify 

### cause ofactuation 

### failure . 2.1.2.2. Service/ replace electrical and/or pneuma tic components , as needed. 2. 1 .2 . 3 . Service/replace actuator an d/o r valve components , as nee ded . 2.1.3 . In 

### case ofphysical / olcctrica l failure of control system compo nent: 2.1 . 3 . 1. I dentify fau l ty contro l sy stem component. 2.1.3.2. Service/ replace control system components, 

### a s ne ed ed. 2 . 1.4. 

### In case of mechanical/ electrical fai l ure at natural gas s upply sc ur ce: 2.1 .4 . 1. Identify tbe cause of the failure . 2 . 1.4.2 . Take 

### the necessary acti ons to restore the supply o f natural 

### gas. 2.2. L oss o f Combustiou Ai r Pressure/Flow to P CC 2.2 . 1. Jn case of mcchanical!electrical failure ofcombustion air blower: 2.2. 1 .1. Diagn ose b lo wer/drive failure. 2 .2. 1 .2. Service/replace the blower / drive , as needed . 2 .2 . 1 .3. R es tore electrical power supply to the blower. 2 . 2 .2. In case of physical failure ofcombustion a i r duct: 2.2.2. 1. Identify the location of duct failure. 2.2.2.2. Service/ rep la

ce fau l ty d uct, as n eeded. 2.2.3. In case o f mec hanical/electrical failure o f actuated va l ve: 2 . 2.3 . 1 . Identi fy cause of actuation fitilure. 2.2.3.2 . Service/replace electrical and/or pneumatic components, as n eeded . 2.2.3.3 . Service/replace actuator an d/o r val ve components, as needed . Page 5 of26 

## VES012227VEOLIA ENVIRO N MEN TAL S ERVI CES , INC. PROGRAM OF CORRECTLY£ ACT IO NS FOR M..4L FU CTfONS 

### 2.2.4. In 

### case ofphysicaVelectrica l failure ofcontrol system compo n ent: 2.2.4.1. 

### Ide n t ify faulty control sys t em component 2 .2.4 . 2. Serv i ce/ replace control sys t e1n components, as neildcd. 2.3 . PC C 

### Mai n Bum cr Pilot Failure 2.3.1. 

### For loss ofoarural gas pressure/flow , see 2 .1. 2.3 .2. 

### Fo r lo ss of com bustion air pressure/flow , see 2.2 . 2.3.3. 

### In case ofphysica lfe lectri cal failure of igniter: 2.3.3.1. 

### I dentify cause o f igniter failure. 2.3.3.2. 

### SCI'\oicelreplace igniter and/or associated components, as 

### needed. 2.3.4. In**ca.<~e** 

### of pby sicaVelectrical failure ofcontrol sys tem co m ponent: 2.3 .4. 1. Identify 

### faulty con t rol system component. 2.3.4.2. Service/replace contro l sys tem co mponent s, as 

### needed . 2.4. 

### L oss of Wa s t e 

### F l ow to l' CC Inj ect or 2.4 .1. 

### I n ca se of mechanical/electrica l failure ofwaste feed pump: 2.4 .1 .1 . Diagnose pump / drive failure

- . 2.4.1.2 . 2.4.1.3 . 

### Service/repla ce th . e pump/ d rive, 

### as needed. Restore electrical power suppl y to the 

### p u mp . 2.4.2. In 

### coseof l ow nitrogen pressure, see 1.4. 2.4.3. 

### In case of pluggiuglphyl;ical f ailure ofline o r line 

### component : 2.4.3.1. Identify the 

### location ofplugging or line foilure. 2.4.3.2. Clear 

### line p lugging and/or service/replace faulty line components, as 

### needed . 2.4.3.3. 

### Restore/confirm functional heat traci n g, if a pplicable. 2.4.4 . 

### In case ofmecb anicol/electrical f ailure o f a ct uated valve: 2.4.4.1 . Identify ca use of actuation fuilure. 2.4.4. 2 . Service/replace electrical and/or pneumatic components , as needed . 2 .4.4.3. 

### Service/repl ace actuator and/or valve co mponents , 

### as n

eeded. 2.4.5. 

### In case ofpbysicaVelectrical failure o f control 

### system component: 2.4.5. 1 . Id entify faulty control system 

### component. 2.4.5.2 . 

### Service/replace cont'rol system components, as needed. :2.5 . Loss of W aste Feedrate Co n trol t o PCC In jector 2.5. 1. 

### In case 

### of l oss of waste . preasurelflow to PCC 

### injector , see 2.4. 

### Page 6 of26 

### V E S012228VEO LIA ENVIRO N MENTAL SERVICES, INC . PROGR AM O F CORRECTIVE ACTIO NS FOR MALFUN CTION S 

### 2. 5 .2. In 

### case of physicallelectri cal failure of flow transmitter: S erv ice/ r ep l ace fl ow t rans mitter an d/or ass oc i a ted in s tntm enta ti on ,**a~** 

### needed. 2.5 . 3 . 

### I n cas e o f a c tu at ed valve fa ilure: 2 . 5.3.1. 

### I dent i f

y c aus e of a c tuation fuilure. 2. 5 .3.2. Service/replace electrica l and/ o r pn eum atic com p o nen ts, 

### as n eeded . 

### 2.5.3.3. Service/replace a ctuator an d/o r valve components, 

### as needed. 2 .5 . 4 . In 

### case ofph)'llical/electrical failure of 

### control system component: 2.5. 4 . 1 . I dentify fuulty onntro l system 

### component. 2.5.4.2. 

### Scrvicelrcpl ace co ntr ol sys t em compo n ents , as needed. 

### 1.6. Lo ss of Atomlzadon Air P ressure to 

### a P CC Injector 

### 2 . 6 . 1 . For n 

### total l oss of p la n t/ instrument air 

### s uppl y, see 

### 1 .3. 2.6 . 2 . In 

### cas e o f 

### plu ggiog/ physical failu r e of line or lin e c o m po n ent: 2 .6. 2 . I. I de ntify the location ofplugging o r line filih n 'l). 2.6 .2 .2. 

### Clear line plu gging and / o( servic e/repl ace f au lty line 

### co m po nents, as n eeded. 2 .6.3 . In 

### case o f mecban icallphysi cal fai lure of p ressure onntro l valve: Service/rep ! Bee 

### press u re contro l v al ve, as 

### needed. 2.7. 

### L os s o r P CC D raft Co n trol (Urut 4) 2.7 .I. 

### I n case ofiD fan 

### failure, see 9.5 

### 2. 7 . 2. In 

### case of p h }'llical/e lectrical fail u r e of kiln 

### pressure transmitte r : Service/ re

p lace press ure transmi tt er an d/o r associa t ed ins tru me n tat io n, as 

### needed. 2.7 . 3. ln 

### cas e of u c tu ated dam p er fa il ure: 2.7 . 3.1. 

### I d entify 

### c ause of actuation failure . 2.7.3.2. Service/ replace electrica l and/ o r pneuma tic components, 

### as needed . 2.7.3.3. Service/rep l a

c e actu a tor an d/ or damp er onmp o n e

nt s, as needed. 2 . 7 .4 . l o case 

### ofp h)'llicall e lectric al failure of contro l system onmponeot: 2.7. 4 . 1 . I dentify faulty control sys t em onmponenl 2.7.4.2. Service/replace co n trol system components , 

### as needed .

Pa ge 7 o f26 

## VES0 1 2229

### VE O LIA ENVIRONMENT AL SERVICF.S, INC. PROGRAM OF CORRECTIVE ACTI O NS F OR MALFUNCTION S 2.8 . Lo ss of P CC 

### T e mp erature Contro l 2.8.1. 

### In 

### case of

### l oss of 

### natural gas pressure/ flow to main burner , see 2. 1. 2.8.2. 

### In case o fl oss 

### of waste press u re/flow to PCC 

### injector, 

### see 2.4. 2 . 8.3. 

### In 

### case of physical/electricnl fltilur e 

### oftemperature e lt.1nent: 2 . 8.3 . 1. 

### Service/replace faulty temperature element and/or associated instrumen tation , as 

### need ed. 2.8.4 . In case 

### of physica l / electrical failure ofcontro l system 

### component: 2.8 .4 . 1. 

### Identif y faulty contro l system component 2 . 8.4.2. 

### Service/replace control system 

### compon . ents , 

### ns needed . 2.9. Flam e Failure 2.9 .1. 

### In case 

### ofphysical/electrical failure 

### offlame detector: 2.9. 1 .1. 

### Identify faulty flame detector component. 2.9. 1.2. 

### Service/replace flame detecto r com p on ents, as needed. 

### 2 .9 . 2. In 

### case ofphysieal/electrica l failure ofcontrol system component 2.9.2.1. 

### Id e nti fy faulty 

### control system component. 2.9.2.2 . 

### Service/repl ac e control system components, ns 

### needed . 2. 1 0. 

### KJJn Rotation M alfunction (U nit 4) 2.1 0.1. 

### In 

### case ofmechnnicalf electrical kiln dri v e system : 2. 1 0.1.1. 

### 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 assoc iated ins1.rwnentation, as needed. 2 .1 0.3. 

### In 

### case ofpby s i caVelectrical fa ilure of contro l system co m ponent: 

### 2.1 0.3. 

### J . I dentify faulty contro l system component. 2. 1 0 . 3 . 2. 

### Service/rep l ace control system components, ns need ed . 2 . 11 . Bulk/Cha rge Feed D oor Malf unction 2 .1 1 . 1 . 

### In case ofmecbanicalfelectri cal failure ofactuated d oor: 2.11.1.1. ldenti 

### fy cause of actuation failure. 2.11. 1.2 . 

### Serviec/ replace electrical, 

### hydraulic, an dfor pneumatic components , as oeeded . 

### 2 .1 1.1.3. 

### Service/ re

pl ace actuator andfor valve components, as 

### needed. 2. 1 1.2. 

### In case 

### ofphysica Velectrical failure ofcontrol system compo nent : PageS of26 

## VES012230

### VEOLIA ENVIRO NME NT AL SERVICES , INC . PROGRAi'f. OF C ORRECT£\'E ACTIO NS FOR MALFUN CTIO NS 2.11.2. 1. Id entify faulty co ntr ol system component. 2 .11. 2.2. Service/ repl ace control system co mp one n ts, as need ed. 2.12. Physicai/M ecb •nlcalln t croal 

### E q uipmen t Failur e 

### 2.12 . 1. I n case 

### of refrac tory f ai lure, re pa ir/replace refrac to•y 2.12 .2. 

### In 

### case ofas h**co ll~** **ction** 

### fail ure 2.12 . 2.1. Diagnose ash collection sys t em fai l ure 

### 2.12.2.2 . Service/repla ce ash 

### collection sys tem 

### components, as 

### needed. 2 . 1 3. 

### P CC Seal V i sual Emi ssio n s 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/electrica l failwe of monitor , serv i cc!rep l ace monitor . 2.13.3. ln case of phys i cal/e l ectrica l f ail ure of recording system, service/repl ace r ecord ing sy stem. 2.14. 

### Rapid Steam Ge n e r ation 

### f • 'Om Ash 

### Co ll ectio n System Wat er 2 .14 .1. In 

### case of refrac to ry fai lur e , repair / replace refractory. 2.14.2. In case ofun contro lled movement/drop p ing of residue into ash collection system water , inspect system to i dentify / remove other suspect material .

Page 9 of26 

## VES012231VE OL IA E NVIRO NMENTAL SERVIC ES, IN C. PROGRAM O F CORRE CTIVE AC TIO NS FOR MAL FUNCTI O NS


### 3.0 SEC O NDARY C OMB USTION C HAMB ER 3. 1 . Loss o f Na t ural Ga s Pressun / Ftow to S C C Main B urner 3.1.1. In case ofpluggjoglpbysical failure ofline or line component: 3.1.1.1. Identify the l ocation ofplu gging or line failure. 3.1.1.2. Clear line plugging and/or service/replace faulty l ine 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 e l ectrical 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 ofcontrol system component 3.1.3. I. Identify faulty control system component. 3.1 . 3.2 . Servi ce/repl ace control system components, 

### as needed . 3. 1. 4. In case of m echanical/electrical failure at natural gas supply 

### source: 3.1.4.1. 3.1.4.2. Identi fy the cause of the failure . Toke the necessary actions to restore the supply of natural 

### gas. 3 .2. L oss of C om b u st ion Air Press u re

/Fl ow to SCC 3.2.1. In case ofmechnni c al! cl ec trical failure of combu s tion air b l ow er : 3.2. 1 .1. Diagno se blower/drive fa ilure . 

### 3.2.1.2 . SeJVicelrcpl ace the blo w er /drive , 

### us needed. 3 .2.1 .3. Rest ore electrical power suppl y to the blower. 

### 3.2.2. 

### In case ofphysical failure combustion air duct: 3.22.1. Ident ify the location ofduct failure. 3.2.2.2. Service/replace faulty duct, as needed . 3.2 . 3 . In cas e ofmcch an.ical!e lectric a l failu r e ofactuated 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 

### VES012232VEOLIA "ENVIRO NME NTAL S E RVI CES, INC . P ROGRAM O F C ORRE CflVE ACTI ONS FOR 1\> IALFUNCTlO NS 

### 3.2 . 4 . In 

### case of physical / electrical failure of contro l sys tem component: 3 .2.4. 1. I dentify faulty coutro l system component. 3.2.4.2.**S~'t'V ice/** **replace** 

### contro l system components, as needed. 3.3. SCC Mai n Bu rn er Ignition F ail ure 3.3.1. 

### F or l oss ofna t ural gas 

### pressur e/flow, see 3.1. 

### 3.3 . 2. For los s ofcombust i on air pressure/flow, see 3.2. 3.3.3. In 

### case of pbys ical/electrica l failure of igniter: 3.3 .3 . I. 

### Tdeoti fy 

### cause ofi gniter fai l:ure

### 3.3.3 .2. Service/replace igniter and/or associated components, as needed. 3.3.4 . In 

### case of pbysi caUe\cctrical failure of control sys tem component: 3.3.4.1. Identify faulty control system 

### component. 3 . 3.4.2 . Service/replace control system components, as 

### needed. 3.4. 

### L oss ofWn ste Flow to SCC Inj ec t or (U ni t 4 ) 3.4 . 1. 

### In 

### case ofmecbunicaVelectrical 

### fa ilur e of 

### waste feed pump: 3.4. 1.1. Diagnose pump/drive failure. 3.4 . I .2. Service/replace the pu mp / 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 ofplugging 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 functi orull h eat tracing, if applicable. 3.4.4. In 

### case of meclJanical/electrica l failure ofactuated va l ve: 3.4.4 . 1. Identify cause of ac tuati on failure. 3. 4.4.2 . 

### Service/repl ace electrical a nd

/or pneumatic com ponents, as n eeded. 3.4.4.3 . 

### Service/rep lace actuator and/or valve components, 

### as needed. 3.4.5. In case 

### of physical /e

lectrical 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 Wa ste Feedrue Contro l to SCC 

### Inj ector (Un it 4 ) 3.5 . 1. In case 

### of loss of waste pressure/flow to 

# sec in jector, sec 3.4. 

### Page II of26 

## VES012233

### VEOLIA E!li'VTRONMENT AL SE R VI CES , IN C. PROGRAM OF C ORRECTIVE ACT IO NS FOR MALFUNCTIO NS 3.5.2. 

### In case of physicaVel ectrical failw-e of flow transmitter: Service/replace flow transmitter and/o r assoc i ated instrwnentation, 

### as needed . 3. 5.3 . In 

### case of actuat ed valve failure: 3.5.3.1. I d entify caus e ofa ctuati on failure. 3.5.3.2. 

### Service/replace e le ctri cal and/or pneumatic compo nents , as 

### needed. 3.5.3.3. Service/replace actuato r and/or valve components, as 

### nocded . 3.5.4. 

### In 

### case ofphysical/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. 

### L o ss of Atomizatio n Air 

### P nss u re to a 

### SCC Injecto r 3 . 6.1. 

### For 

### a total l oss 

### ofplant/instrument air supply, 

### see 1.3. 

### 3 . 6.2. In 

### case ofplugging/physical fail ure of line or 

### line component: 

### 3.6.2 . 1. l deutify the 

### lo c ati on o f plugging o r line failure. 3.6.2 .2. C le ar l ine plugging and/or service/replace fdulty line components, as 

### needed . 3 . 6.3. 

### In case of mecbanicallphys i cal failure of pressure control valve: Service/replace pressure 

### control valve, as 

### n eeded. 3.7. Loss 

### ofSCC T em p e r ature Co ntrol 3.7.1. I n case 

### ofloss of natural gas 

### pressure/flow to main burner , sec 3.1. 3.7 .2. ln 

### case ofloss o f waste pressure/flow to 

# sec injector, see 3.4. 3 . 7.3 . In 

### case ofphysicaVelectrical failure oftemperature elemc.tt: 3.7.3.1. Service/replace fau lty temperature elemen t and/or associated instrumentation, as n eeded. 3.7.4. 

### [n case of phys i caVel ectrical failure of contr:ol sys ten 1 compo n en t: 3.7.4 . 1 . 

### I dentify fuulty control s ystem componeot. 3.7.4 . 2. Service/replace control system componen ts, 

## as needed. 3 . 8. 

### Fl ame F ailur e 3 .8. 1 . 

### In case 

### ofp h ysicaVclectrical faiJure 

### o f flame 

### detector: 3.8.1.1 . 

### Identify faulty flame 

### detector componcnt. 3.8.1.2. Service/replace flam e detector components, as ucedcd. 3.8.2. 

### In case of physicallelectrical failure of control system component: 3.8.2.1. 

### Identify fau lty control system component . Page 12 of26 

### VESOI2234VE OLIA ENV I RO N MENTAL SER VfC ES , INC. PROGR <\1

'\'1 OF C ORRECTIVE ACTIO NS FOR M AL FONCTJONS 3.8.2.2. Service/replace control s ystem compo nents, as needed. 3.9 . P bysicai/M cc b a o lcal I n ternal E q uipme nt Failure 3.9.1 . In 

### case of refractory fai l ure , repai r / r eplace r efractory. 3 .1 0 . L ow Wate r Le vel in S lag Co ll ec ti on Sys tem (Uni t 4) 3 . 1 0 . 1. For a lo ss of pro cess water pressure/flow , see 1.6. 3. 10. 2 . In case of physical/mecha ni cal fa i lure of l eve l contro ller: Service/replace faulty le ve l controller and/or associated components , 

### as needed. 3.10.3 . 

### Io case of physical/meclumjcal failure 

### ofactuated valve: 3. 10.3.1. Identify caus e 

### of actuation fail ure . 3.10.3.2. Service/replace pneumatic com . poncnts , as needed. 3 . 10.3.3. Service/r eplac e ac tu a tor and/ or valv e co mp one nt s, as n eeded. 3. 11 . Eme rgen cy S af ety Ve nt Op ening 3 . 11.1 . Rcspoud to an cmergettcy safety vent ope ning i n a matUter consistent with the 

### Em e rg

e

n cy Safety Vent Pla11. 3 . 1 1.2 . 

### I n case o f mechanical 

### failw-e of

### t he actuato r : 3. 11. 2.l. Ident ify 

### ca u

se ofac tuatio n failur e. 3.1 1.2.2. Service/repl ace emergency safety vent compo ne n ts , as 

### needed. 3. U. R apid Stea m Gen era tion fr om As h Collection Sys t e m W ater 2. 14 .1. fn case of r efrnctory failure , repair/replace refrac to r y. 2.14.2. In case of un co otro Ued movemen t/

dropping of residu e into ash collection sys tem water, inspect sys t em to identify / remov e other 

### sus p ect materi ul.



### Page 1 3 of26 

### VES012235VE OLIA ENVIRONMENTAL S ERVICES , INC. P ROGRA!\1 OF C ORREC11VE ACTIONS FOR ! MALFUN CTION S

4.0 TEMPERING C HAI\>lB E R (UNIT 4) 4. 1. Loss ofTemp ering Cha mb er Exi t Gas Temperattu ·e Control 4 .1. 1. For 

### u l oss 

### of process 

### w ater pr ess ure/flow , see 1.6. 4 .1.2. I n case of pbysical /electrical fuilure of How tran smitter:**Sen~ cclre** **placc** flow 

### transmitter and/o r associated instrwnentatio o , as needed. 4.1.3. 

### In case of actuated val ve fai lure : 4 .1.3.1. Identify cause of actuation 

### fuilure. 4 . 1.3.2. Scrvicclreplace electri cal an d/o r pneumatic compo nents, as needed. 4 .1.3 .3. Service/replace actuator an d/or val ve components, as nee d ed . 4.1.4 . 

### In 

### case ofphysicaV elec trical failure of control sys tem co mponent : 4. 1. 4 .1. Identify faul ty co ntrol s y stem co mponent. 4 . 1.4.2. Service/replace con tr ol 

### sys tem components, 

### as needed. 4.1 . 5 . 

### In case o f no22 .lo fai l ure, service/replace n ozzle , as ne eded . 4.2. Loss o f Atomlzatlon Air Pressure to Noule 4.2.1. For 

### a to l alloss ofp l ant/instrument 

### air supp ly, see 1.3. 4. 2 . 2. In case of plugging/phys ical failure of line or line component 4.2 .2. 1. Ident ify 

### the location o f plugging o r 

### line failure . 4. 2.2.2 . Clear line plugging and/o r service/replace faulty l ine compo nent s, as ne eded.

P age 1 4 o f26 

### VESOI2236VE OLIA ENVIRO N MEI\ 'TAL SER VICE S, INC. PROGR A M OF C O RRE Cf l V£ A Cfi O NS FOR M ALFUNCfiO NS 

### 5. 0 LIME SL URR Y S YS TEM 5.1 . Lo ss o fLlm e F eed to L im e S lurry Fe ed Tank 

### 5 . 1 . 1 . 

### In cas e of mec han ical / e l ectrical f ail ure of l i me s lurry sc r e w f e ed er: 5 . 1.1.1. D i ai.'IIOSC f ee der/driv e fa ilure . 

### 5.1. 1 .2. Service/r ep

l a c e 

### 1h e f eeder / dri v e , 

### as n eeded. 5 .1.1. 3 . Res t o n : electrical power sup ply to 

### th e l i m e s lu rry screw feeder. 

### 5 .1 .2. 

### In case of mechaoical/electri cal failure of lime bin activator /vi brator: 5.1.2.1. Diagnose lime bin activator / vibrator fail ure. 5.1.2.2. Service/repla ce th e lime bin activato r /vibrator, 

### as needed. 5. 1. 2.3. R estore el ectrica l po w er supp l y to th e li me s lurry sc r ew 

### t eeder. 5.1.3 . In c a se o f plu gging/ ph ys ica l fai lu r e of line or line co mponent: 

### 5 . 1 .3. 1 . Ide n tif y th e locatio n of plu ggi ng or line f-ai l ure. 5. 1 .3 . 2. C l e ar li n e p l u gging an d/or s ervi ce/ r ep l ace fa ulty line co m ponents, 

### as n eeded. 5 . 1.4. I n case of phys i cal/el ectri cal failur e o f lime 

### feed controls:**Sm~ce/replace** faulty ins trumentation and/or control system compo n ents, 

### as needed. 5 . 2. Malfun ctio n in L ime S lurry Co n cen tr a tion 5.2 . 1. 

### In case o fl oss of lime 

### feed t o lime s l urry 

### f eed tank, see 5.1 5. 2.2 . 

### In c as e o f l oss ofwate r fl o w to li me slurry 

### f eed tanlc , sec 1 .5 

### 5 .

2.3 . In 

### c ase o fm echuni cal/ electric al f a ilure o f l ime slurry ag itator : 5 .2.3 . 1 . Diagnos e agi t ator /driv e failure . 5.2 .3 . 2. Service/ r epl a ce th e agitator / dri v e, 

### as needed. 5.2.3.3. Resto r e el e ctric al pow e r supp l y to 

### lho lime s lurry agitato r . 

### 5 .2.4. ln 

### case of physical/ el ectri cal failure of insttumentation: S ervice/repl ace faulty instrumenta tion, 

### as needed. 5 .2 .5 . 

### In 

### ease ofphysical/electrical 

### failure of control system component: 5.2.5.1. Identify faulty contro l system component. 5.2.5.2. Servioelrep l ace contro l sys tem co mponents , as 

### needed .
Pag e 

### 15 of 26 

## VES 0 1 2237

### VEOLIA ENVIRONMENTAL S ERVICE S, IN C. PRO GRAM OF CORRECTIVE ACTIONS FOR IVIAL FUNCTIO NS

6.0 

### UNITS 

### 2 AND 3 

### S PRA Y DRYER ABSORBER (SDA) 6. 1 . U!ss ofUme Slurry Fl ow to 

### S DA 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 e le ctric al power supply to the pump. 6.1.2. In case ofpluggiogiphys i cal failure ofline or line component: 6.1.2.1. 

### Identify th e location of plugging or line failure. 6.1.2 . 2. Clear lin e plugging and/or service/replace taulty line components, as needed. 6. 1.2.3. 

### Resto re/confirm functional heat tracing, if applicable. 6.1.3. In 

### case ofmechanicallelectrical fuilure . of actuated valve: 6 .1. 3.1. 

### Identify cause ofactuation failure. 6. 1.3 

### . 2 . Service/replace e lect rical 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 ofphysicallclectrical failure of control sys tem component: 6.1.4. I. 

### Identif y faulty 

### control system 

### component. 6.1.4.2. Service/replace control system componenlli, as 

### needed. 6.2 . ' Lo ss 

### of Lime Slurry F l ow Co ntrol 

### 6.2.1. ht 

### case of l oss of s lurry flow to SDA, see 

### 6.1. 

### 6.2.2. In 

### case of physical/elect rical failw-e of flow transmitter: Service/repl ace flow tmnsmitter and/or a ssociated instrumentation, as needed. 6.2.3. In 

### case ofactuated valve failure: 6.2.3.1 . Identify cause ofactuation failure . 6.2 .3.2. 

### Service/replace electrical and/or pneumatic components , 

### as needed. 6.2.3.3. Servicelrepluce actuator and /or valve compo n ents, as needed. 6.2.4. In 

### case ofpbysicallelectrical failure of control system component: 6 . 2.4. I. Identify fault y contro l system 

### co mponent 6.2.4.2. 

### Servicc/reploce control system 

### components, as 

### needed. 

### Page 16of26 

### VESO l 2238

### VEOLIA ENVIRONME NTAL SE RVI CES, INC. PROGRAM OF C ORRECTIVE ACTIONS FOR MALFUNCTIO NS 

### 6.3. Loss of C ity Water Flow t o S D A (Unit 2 and 3) 6.3 . 1. In case oftota l loss of c it

y wa t er s u pply , see 1.5. 

### 6. 3.2. In case of plugging/ physical failure of line or line component: 6. 3.2. I. 

### ldcnti fy the 

### l ocation ofplugging 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 mechanicaVelcctrica l failure of ac tuat ed valve: 6.3.3. I. 

### 6.3.3.2. Identify cause of actuatio n failure. Service/replace electrica l and/or components, as needed . pneumatic 6.3 . 3.3. Sm'icelreplace actuator and/or valve components, as needed. 6.4. 

### Lo ss of Cooling Air F low to Atomizer 

### 6.4. I. 

### In 

### case of mecbanical/electrical fililure of at om i zer cooli n g 

### air bl ower : 6.4. 

### 1. 1. 6.4. 1.2 . 

### Diagnose blower/drive failure . Service/replace the blower / drive. as need ed . 6.4 . 1.3 . 

### Restore electrical power supply to the bl ower . 6.4.2 . Ill 

### case ofphys ical fililure ofatomizer cooling air duct: 6.4.2.1. 

### Identify the 

### l ocation of du ct 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. Lo ss of S DA E x it Gas T emperature Control 6 .5.1. 

### In case of l oss of city 

### water flow to SDA, see 6.3 . 6.5 . 2. In case of physical/el ec tri cal failure of temp era tu re transmitter: Service/rep l ace 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 p h ysical/electrical fai l ure of control system 

### component: Page 17 of26 

### VES012239VE OLIA E NV fR ONMENT AL SERVICES, lNC. PROGRAM OF C ORR ECTIVE A CTI ONS FOR MALFUNCT I O NS 6.5.4.1. ldeo tify faul t y 

### control system 

### component. 6.5.4.2. 

### Service/replace co ntrol system components, as needed. 6 . 6 . 

### Atomizer 

### Fa llu • ·e 6.6. 1 . In 

### case of low utomi;oor lubrication 

### oil flow: 6.6.1.1. Diagnose Ute fa ilure 

### in the lubrication system 6.6.1.2 . Service/replace compo nents 

### of the l ubrica ti on syst<.'tll, 

### ns needed . 6.6.2. 

### In case ofmccllanicallelectrical 

### 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. Re s to re electrical 

### power supply 

### to the atomizer . 6.6.2.4. components, as needed.



### Page 18 of26 

## VES012240\'EOL IA ENVlRONl\lENTALSERVlCES , IN C. PROGRAM O F C ORRECTIVE A CTI O NS 

### FOR MALFUNCT I ONS


### 7 .0 UNIT 4 S PRAY DRYER AB S ORBER 

### (S D A) 7.1. IA>ss of Lime S lurry F l o w to S D A 7. 

### J .1. I n ca se ofmechanical/electrical fai lure oflim e slu rry feed pump: 

### 7 .1.1. I. Diagnose pwnpldrive failure. 7. 1.1. 2. Service/replace 

### th e pump/d rive, as needed . 7 .1. 1.3. Restore electric al power supply to the pmnp. 7 . 1.2. In case ofplugging/ physical fai l ure ofline or line component: 7.1.2.1. Identify the l ocatio n ofplugging or line failure. 7.1.2.2 . 

### Clear line plugging andlor servi ce/ replace faulty line componentS, 

### as needed. 7 . 1.2.3 . Resto re/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 actua tion fai lure. 7 .1.3 .2. Service/replace e l ectrical and /o • · pneumatic components, 

### as needed . 7.1.3.3. Service/replace actuator and/or valve compo ne nts, as needed. 

### 7.1.4. In case 

### of physical/electrical failure ofcontro l system component: 7.1.4.1. Identify fau lty contro l system component. 7. 1 . 4 .2. Service/replace control system con1poncots , 

### as needed . 7.1.. L oss o f Lime SIDJTY t 1ow Control/Exi t Ga s T emp era rurc C ontro l 7 .2.1. In 

### case ofloss of slurry flow to SDA, 

### see 7.1. 7.2 .2. In case of p hysicall elet:trical failure of flow**trao~"lllitter:** Service/replace flow transmitter and / o r associated instnunentatioo , as needed. 7.2.3. In case of actuated 

### valve failure: 7 .2.3.1. Tdcntify cause of actuation fai l ure. 

### 7.2 .3.2. Service/replace electrica l and /o r pneumatic componen t s, 

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

### as needed . 

### 7.2.4. I n case ofphysicaVclectrical failure 

### ofcontrol system component: 7.2.4. I . Identify faul ty control system component. 7 .2.4 . 2. Service/rep lace contro l system components, as needed. 

### Page 19 of26 

### V E SOI 2241VEOLIA E NV IRO N M E NTAL SER VICE S, IN C. PRO GRAM OF CORREC TIV E Act i ONS FOR MALFUN C TIO NS 7. 3. Loss of A t omiza tion Ai r P re ss ure to SDA Nozzle 7.3.1. For a total l oss of pl ant/instru ment 

### air supply, see 1 .3. 

### 7 .3.2. In 

### case ofpluggj1 lg/pbysical failure ofline or l ine 

### component 7.3.2.1. Jdentify the location ofpl ugging or line failure. 7 . 3.2 . 2. Clear line plugging and/or service/replace faulty line 

### compo n ents, as needed.

Page 20 of26 

## VES0 1 2242

### VE OLIA ENVl RONMEJ\'TALSERVI CES , IN C. PROGRAM OF CORRECIWE ACf!ONS FOR MA . L FUNCfJONS


### 8.0 CARBO N INJEC T I ON SYS TEM (UNIT 4) 8. 1. Loss of Car rier Gas Pr essure 8 .1. 1. In case of rnechanicnl/electri cal fai lure of carbon iJ1jcction air b lo wer : 8. 1 .1. 1 . Diagnose blower/ drive fai lure . 8. I . 1.2. Service/replace the blower /drive, as needed. 8. 1. 1.3 . Restore e l ectrical power supply to the blower. 8 .1.2. 

### In 

### case of physical failure air duct 8.1 . 2 . 1. Identify the location ofduct fnilure . 8.1.2.2. Service/replace faulty duct, 

### as needed . 8 . 1.3. In case of phys i cal/electrical fru lure of control system component: 8.1.3 . 1 . 

### Id entify faulty con trol system component. 8 .1. 3.2. Service/repla ce contro l system components, ns n eeded 

### 8.2. Loss/Res tri c ti on o f 

### Activate d C a rbon Flow 8.2.1 . I n case of l oss of plant air to carbon bulk sack, sec 8.3 8 . 2.2 . 

### In case ofmoch anical/electrical f ailur e 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 e l ectrical pow er supp l y to the carlx>n feeder. 8.2.3. 

### In case ofpluggingfpbysical failure ofline or line component: 8.2 . 3.1. Identify the location ofplugging or line failure. 8.2.3.2. C l ear line plugging an d/o r service/replace faulty line components, as need e d . 8.2.3.3. Restore/confirm func t ional heat tracing, if R J >p li cab le . 8.3. Loss o f Plant Alr Pressure/F l ow to Carbon B u lk Sack 8 . 3.1. For a to ta l loss of pl ant/instrumen t a i r sup ply , sec 1.3. 8.3.2 . 

### In case ofpluggingfpbysical fa ilure ofline or lin e co mpon ent: 8.3 . 2.1. Identify the l ocation ofplu ggi ng or line failure. 8.3.2.2 . C l ear line plugging ao d/or service/replace fau l ty line components , as need ed . 8.3.3. l o case ofmechanical/electrical failur e ofactuated 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 

### YES0 1 2243VEOLIA**ENVTRO l\'1\** **NTAL** SE RVIC ES , INC. PRO GRAM OF CORRECTI VE ACT IO NS FOR MAL FUNCT I ON S 

### 8.3 . 3.3. Service/repl ace aelllator andJ'or 

### valve components, as needed . 

### 8.3.4. In caw of 

### p hy sica l/electrical failure of control system component: 8.3.4 . I . Jdeotizy fau l ty 

### control system component. 

### 8.3.4.2. Service/repl ace control system component s, ns 

### oeedcd.

Page22 of26 

### YES012244VEO UA ENVIRONMENTAL S ERVICES , lN C. PROGRAM OF CO RR ECTI VE ACTIONS FO R MALFUNCTIO NS 

### 9.0 B AGHOUSE & I NDUCED DRAFT ( ID ) FAN 

### 9.1. Toro/ I.Alaking Ba g 9. 1.1. In 

### case of 

### a baghouso l ea k d etection alarm, follow the relevant corrective measures prescribed in 

### tbe Operation and MaintenWlce Plan. 9.1.2. In case 

### ofa 

### 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. D i agnose 

### the failure of tbe bsghouse detection system. Servic e/ replace baghouse leak dCicetion system, 

### as needed. 9.2. Bag 

### Bllildio g/High-Big}J Pres s ure 

### 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 Con trol (U nill 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/rep lace · flow transmitter and/or associated**instn~mcntation,** 

### as needed . 9.3.3. 

### In 

### case ofactuated damper failure: 9.3.3.1. IdentifY cause of actua ti on failure. 9.3 .3.2. 

### Service/ replace e lectri cal and/or pneumatic components, 

### as needed. 9.3.3 . 3 . Servi ce/ rep l ace actuator and/or damper compo nent s, as needed. 9.3.4. 

### In 

### case o f physical/electrical failure ofcontrol 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 D amper M. alfunction (U nit 

### 4 } 9.4. I. In 

### case of actuated damper failure: Page 23 of26 

### VES012245VE.O LI A E NVIRONI\1ENT AL SERVICES, IN C. PROGRAM OF C ORR ECT I VE ACfiONS F OR MAL FUNCTI O NS 9.4.1.1. Identify 

### cause of actuation 

### failure . 9 . 4.1.2 . Service/ replac e electrical and/or pneumatic components, as needed . 

### 9.4.1.3. Service/ r eplace actuator and/or damper components, 

### as needed. 9.4 .2. In 

### case of phys i caVe lectrical 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. I n case ofmecbarucallelectrical failure ofiD fan : 9.5 .1 . 1. Diagnose fan/drive failure. 9.5.1 . 2 . Service/replace t h e fan/drive, as n eeded. 

### 9.5. 1.3. Restore electrical power supp ly to the lD fan.

Page24 of2 6 

## VES012246

### VE OLIA E N VIRO NMENTAL SE RVICES, INC . P RO GRAM OF C ORRECTI VE ACTIO NS FO R MAL FUNCTIO NS
1 0. 0 CONTROL SYS T EM/C O NTINUOUS MO NITORING S Y STEM 1 0. 1 . Cont rol System/ Co n ti nu ous M onit ori n g System M alfun ctio n I0.1. I. 

### As needed, refer to the CMS QAIQC Plan 

### for guidance and 

### to ensw·e that proper calibratio ns 

### are perfonned. 

### I 0.12. 

### In case ofphysica l/ e l ectrical 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 ofdata acquisition/availability: 10.1. 4 .1. Ident i fy faulty data 

### system components. I 

### 0.1.4.2. Service/repl ace data system compo n ents , 

### as needed . 1 0.2. C ontinu ous Emiss i on s MonJ torl n g Sys tem Malfunction 1 

### 0.2.1. As 

### needed, refer to the CEMS QAIQC Plan 

### for gu idance and to ensure that proper calibrations are 

### performed and that t11e appropriate performance specifications are met. I 

### 0.2.2. In 

### case ofphysical!el ectrical failure wnbilical heat tracing: I 

### 0.2.2 . 1. Diagnose failure ofheat tracing. I 0.2.2.2 . Replace/restore heat traced sam p le umbilical. I 0.2.3 . In 

### case ofmechanical/ e le<.irica l failure ofheated vacuum pump: 10.2.3. I. 

### Diagno se pump/drive failure. I 

### 0.2 . 3 . 2 . Servi ce/rep l ace the pump/drive, as need e d. 10.2 . 3.3. Replace/restore pump head heat source. 10.2.3.4. Restore e l ectticnl power supply to heated vacuum pump. I 

### 0.2.4. In case ofplugging/physical failure of sample probelnmbilical: 1 

### 0 . 2 . 4. I. 

### Identify the 

### location offailure. 10.2.4.2. C l ear p lugging and/or service/replace faulty components, as needed . l 

### 0 . 2.5 . 

### In case ofmechanicnl/el ectrica l failure of actuated valve: 1 

### 0 . 2 . 5 . 1. Identify 

### cause of a ctuation failure.

Page25 o f 26 

### VES012247

### V EOLL "\ EI'I ' V J:R ONl\1ENTAL S ERVIC E S, INC. P ROG R AM OF CORRECTI VE ACI' IO NS FOR M AL F UN CTI ONS I 0.2.5.2. Service/rep lace e l ectrical 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 

### ofmechanical/electrical 

### failure ofanalyzer : 

### I 0.2.6. 

### I. Refer to man u facturer'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 instrumenta tion components , as needed . 10.2.8. 

### In ca.o;e 

### of physical/electrica l fail u re 

### of control sys tem oomponcot: 

### I 0.2.8.1. 

### Ide ntify fiw lt y control system 

### component I 0.2.8.2. Service/repl ace contr ol system components, as needed.

Puge26 

### of26 

### VE S0122 4 8

# VES012249
. pdfA Pl' E NDIXH AU TOM A TIC WA S TE FRED C UTOFF l'L AN



### VES012249

### A UTOMATI C W ASTE FE ED CUTOFF PLAN Prepared f or: Veo l ia ES Technical Solutions , LLC Sauget, illinois

Pn.,nred by. Franklin E ngineering G r oup, Inc. Frankli n, Tennessee

O ctobt r 2008



### VESO I 2250TABLE O F CONTE N T S 1. 0 INTR O DUCT IO N A.'iD 11.<\CK C RotJ:-ID ... . . .. . . .. . . . . . . . .. . . . . ... ._ ... , .. . . - . ..... ... - .. .. . . . . _ .... , .... . 1 1 . 1 S U MMARY OF FACILITY INFORMATION .......... .. ............................................. I 1.1.1 Fixed Hea r th Incinerators ................. . .. ........ .. .. .. ... .. .. ...... . ... .. ... . ...... I 1.1. 2 Rotary Kiln lncineraror .................. .. ........... . ................. . .................. 2 1.2 DESCIUJ"l'JON OF THE A 

### WFC O SYSTEM ..... .. ........................... . .................... .5 2. 0 AW FCO O P ERAlliLITY 'fEST P ROCEDURES . ...... . .. .. .... - ... .. ... .. - ....... - ..... . ... - .... .. .. . 11 3.0 JU:SPO N CE TO AN AWFCO EVEN T .. ..... .... - .. - .. .... - . .. . - .. .. . .... . - ..........- ..... .. . .... . . .. .. . .. 1 2 3.1 REPORTING REQUlREM.EI< TS
.... . ............................................ .. .. .... .... .. ........ 13 4. 0 M ANU AL WASTE FEED C lff · OFF PROCEDCR.ES- .. .. - .... ... .. .. - . .. . - .. .. . ...... - . - · .. . 1 4

ii



### VES012 25 1UST OF TAB L ES TABLE 1- 1 REGULA TO R Y R EQUIREMENTS FOR AN A WFCO P LAN AND CORRllSPONDINO SECTION THAT A DORJ>SSES TH E REQUIR£Milm'
.............. . .4 TABLE 1-2 AUTOMA'fiCWASTE FilED CUTO F F INTF.RI.OCKS .......... ................................ 6



## iu

V E SOI22521 . 0 INTROD UCf iO N AN D B AC K G RO UN D Veolia ES Technical Solution s , 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 Po llutants (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 contro l 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 was t e 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 P lan 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 P lans and the section of this plan that addresses each specific reqoirement. Due to the similarity of t he 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 t hat is only applicable to one or two of the three systems "ill be c l early identified. 1 . 1 S ummary o f F ac ility Informatio n Brief sununaries which describe the fixed hearth incinerators and t he rotary kiln incinerator are presented in this section. 1.1.1 Fixed Hearth lndllerators Each of the fixed hearth i n cinerators includes the following components:

• Feed equi pment 

### • Primary and secondary combustion chambers • Lime injection system • Spray d ryer absorber (SDA) I



### VES012253• Fabric fi l ter baghousc • Solids and asb removal systems • Induced draft (ID) fan and stAclc • Instrumentation, controls, and data acquisition systems Various sol id and liquid wastes and gaseous ftedstreams are thermally treated in the fixed hearth incinerators. Solid waste is fed to the primary (lower) combus ti on chamber v

i a 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 c ham ber 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 th o 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 sys tem . This system features a multi-compo nent infrared gas analyzer that detects hydrogen chloride, carbon monoxide, and water v a por co noontrntions. An integrated zirconium oxi de-based analyzer detects oxygen**concentr ation.~** **.** 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 remo v al systems • 10 :fun an d s t ack • Instrumentation, contro ls , and data acqui si t ion systems Various solid an d liqui d wastes are thennally treated in the rotary kiln incinerat or. Solid wastes are 

### fed to a ram feede r via a clarosheU, a dnnn feed conveyor, and an auxiliary 

### feed conveyor. A hydraul ic ram pushes the solid waste i nto t he kiln. Liquid waste from tanks and tanker trucks is fed to the primary and secondary combustion chambers through a tomized liqui d in j ectors. Combustion c hamber temperatures are maintained using natural gas fired to a dedicated burner in both the primary and secondary chambers. Com b ustion gas exits the secondary combustion chamber and enters the t empering chamber , which pro vides cooling o f the combustion gases. TI1e combustion gas exits tbe tempering chamber and is distributed between two identical SDAs, which provide aci d gas removal and additional gas cooling . A carbon i njection system is utilized for controlling dioxinlfuran and mercury emis si o n s . The activated carbon is air injected into the combustion gas immediately downstream of the convergence of com b ustion gases from the SDA s . From the SDAs, combustion gas is distributed to fabric filte r bagbouses , which provide p articula te matter removal. The ID fan, located downstream of the baghouses, moves the combustion gas through the system and exhausts the gas through th e 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 in t egrated zirconium oxi de-ba sed analyzer detects oxygen concentrations.

3



### VES012255T ab l e 1· 1 R eg ulat o r y R equirem ents fo r A WF CO Plan a n d Cor r e s p o n di n g Sectio n that Ad dre sses th e R e quire m ent R eg ul a tor y Citation Descrip ti on § 63.1206(c)(3)(i) Facility must have a functioning A WFCO system System must cut offwaste 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 offwaste when span value ofany CMS detector is met or exceeded § 63.1206(c)(3)(i)(C) System must cut off waste upo n malfunction of n CMS monitoring an OPL or emission level § 63 .1 206(c)(3)(i)(D) Waste cut-offmu s t occur "1ten any com p onent of the A WFCO system filils § 63.1206(c)(3)(ii} Dueling of**co tnbu** **~1ion** gases § 63. 1206{c)(3)(iii ) Restarting waste feed 

### § 63.1206(c)(3)(iv) Failure ofA 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)(vi ii ) Rum ping down waste feed § 63.1209(b)(4) Interlock s-pan ofnon-CEMS CMS into tho A WFCO system

4 Plan Sect i o n 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 Sect i on 1.2



### VES0122561.2 Descripti on o f tlt e AWFCO System The A WFCO system include s aU hardware and software (i.e., control logic) necessary to inunediately and automatica lly cutoff waste feeds to the incinerator in the event that an AWFCO interlock is triggered. T able 1-2 lists the parameter and setpoint for each required A WFCO interlock. In a d dition to the interlocks specified i n Tables I -2, th e fo ll owing conditions are i nterlocked with each AWFCO system:

• The span value of each CMS i nstrument (except fur a CEMS i nstrument) • CMS Malfunction • A WFCO System Malfunction AWFCO interlocks ensure that the pneumatically actua ted waste feed block v alves canno t open or remain open wlless a U regul ated operating parameters and conditions are within limits. Additionally , t he waste feed b lock valves will fail in the closed position if there is a loss of electrica l power or instrument air supply. The parameters interlock ed with the A WFCO system are des cribed below in further detail.

• Max.inturu Pumpable Hazardou s Waste Feedrate

- Each pumpable hazardous waste feed lioe to the incinerator is equipped with a mas s flowmeter. The pumpable hazardous waste feedrate is continuously calculated as the sum o f the individual flowrates . Jfthe hourly rolling total (HR1) pumpable hazar dous waste feedrate meets or exceeds its limit, au AWFCO interlock is triggered.

• Maxim um T otal H az ard o us Wa ste Fee dr11te - For Units 2 and 3, solid waste i s fed to t h e primary comb ustion chamber via a feed conveyor and pneumatic ram . A scale in the feed conveyor moni to rs 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 empti es into a hopper equipped with a load cell that moni tors each charge weight. The solid feed conveyors are · equipped with weigh scalos. For each incinerator , the time b e tween c harges is use d to convert these charge weights to a solid waste feedrate. The solid waste feedrate is summed with the pumpable hazardous waste feedrate to calc ulate t he total hazardous waste feed rate. 

### lf the HRT of the total hazardous waste feedrate meets or exceeds its limit, an A WFCO inter lock is triggered.

5



### VES012257T able 1

- 2 Automatic W:l!tt F eed Cutoff Inte . rlocks Operatl•ll:**Paran~er** Maximum Pumpoble 

### w.,te Fecdtate Ma).im uro Tout! Waste Feed Rate Mllltlmum As h F co d 1\llt e Max.imum C ltl or iu

c/CWoride Feedrate M

axit num Mercury fecdratc Limit MO>imum Sem i Volatile M emlsFeedra te Maximum Total l..o w Vo la tile Metals feedtate Muimum l'wopoble Low Volatile M... ts f eednne Maximum Primary Combustion Cbaroba P,...,.. Minimum Prinwy C o mbus1ioo Cbambcr Temp= tun:**Mini ~m**  S«:oodary Combu>rion Cbamber Ternpcnture £meraenoy S 11fcty Vent Positioo Ma.<imum D-sbouse Inlet Tempenuure M11 xim,un B a a l..eak Oete<:tot Output M

ioun um Carbo n Feed rute M

inimu1 n**t~ rbo** **n** feede r Ex . it Pra!S$UTe Mrutimum Corboo ClUTier Gas Supp ly PrtSiUfe Max i m

um 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 1 2 -HR T T

RV - - - Hoarly 

### Rollil1s AY<n fe Hourly Rolling Totol 12

- Hoor Rolling Total Tbermal Relief Vent A

## ••••«J.as Period Uuiu l{R.T 1 blbr HR.T lblh r 12

- H.RT lbibr 1 2- J

·ntt lblhr 1 2-J-fRt lblb r 1 2-HRT lblhr 1 2- 10!1' lblhr 1 2- HRT iblltr IMwn&oeous in. '9.'.C.. HRA 

### •r HM Of JDMI\ntaneollS 

# .. HRA •f 10 ICCO n dt %ofscale Hlt.A lblhr**Jo Ui** **i..1 000** **S** psig rnstOni CUMJO li S in . w.c. Illt.A acfm I1RA ppmd v@7%0 1 Hlt.A Lbnb Cl2 llR.A GalllbCI2

6 AWFCO lntu!oclc S ttpoiot Ullil1./3 Oait4

3, 107 PCC · 32561SC C. 1 006 4,017 PC C · 13,7%/SCC

- 100 6 673 

## s.1n 218 2 52 0.0047 0 .03 1

63 6S 46 $5 41 4 7 >O, OforS- >O. OforSocroods 1 ,

73 4 J,so7 1,84 9 1,886 TRY Open Swge Ven t Open TRVOp0<1 420 434 > 30 % for 6 minute:< > 15 % for 12 m.in\ltes



# - 6.2



# - 4



# - I I S,I47 38,086

100 1 00 1.76 1. 01 1.7 0 1.61

--- - - - - - -



### VESOl2258• M a:dmum As b Feedrate

- The ash concentration of each waste feed is detemrined i n accordance w i th the Feeds tream Analysis P l an. The CMS uses the waste 

### ash con centration and the continu o usly monitored was t e feedrate to calculate the ash feedrate of eac h waste stream. If the 1 2-hour rolling total (1 2 · HRT ) o f th e com b ined ash feedra t e meets or exceeds its limi t, an AWFCO interlock is triggered.

• Maxim um Chlori n e/C bl or ide Feed ra te • Tho c hl orine / chl oride concentration of each waste feed is detetmi ned in accordance with the Feedstream Analysis Plan. The CMS use s the chlo rine / chloride concentration and the continuously moni t ored was t e feedra t e to cal cula t e the chlorine/chloride feedrate of each waste stream. I f th e 1 2

- HRT of the combined chlorine/chloride feedrate meets or exceeds i ts limit, an AWFCO inter l ock is triggered.

• Maximum Mercury Feedrat e -The concent ration ofmercury i n each waste feed is determined in accordance wi t h the Feedstream Anal ysi s Plan. The CMS uses the mercury concentration an d the continuously monitored waste feedrate to calculate the mercury of eacl1 waste stream. Iftho 12-HRT of the combined LVM feedrate meets or exceed s its (j mit, an AWFCO interlock is triggered.

• Max imum SVM Feed.ratc

- The concentrations of cadmium and l ead i n each wa s te teed is determined i n accordance w i th th e Feedstream Analysis Plan. The semi vo lati le me t als (SVM) concent r ati on io each waste stream is the sum of these metal concentrations. T he CMS uses t he SVM concentration and the continuously monitored waste feedrate to calcula te the SVM feedrate o f each waste stream. lflhe 12-HR T of the comb ined SVM feed r ate meets or exceeds its limit, an AWFCO interl ock is triggered.

• Maximum Total LVM Feedrate • Tbe concentrations of arsenic, beryllimn , and chrom i um in each waste feed is determined i n a<:COrdancc 

### with the Feedstream Analysis Plan . The low vo l atile metals ( LVM) concentrat i on i n each was t e stream is the sum of these metal concent r ations. The CMS uses the LVM concentration and the continuously monitored waste feedrate to calcul ate the LVM fee d ratc of each waste stream . If the 12-HRT of the combined LVM feedrate meets or exceeds its l imit, an AWFCO int erlock i s triggered.

7



### VES012259• Maximum Pumpable LVM f'ced r a tc - The LVM feedratc from pump ab le waste fccdstreams are summed to obtain the combined pumpable L VM feedrate. If the 12

-HRT pumpable LVM feedrate meets or ex ceeds its limit, an AWFCO interlocl< is triggered.

• Maximum Primary Combustion C bam ber Pressure -The 

### primary chambers for Units 2 and 3 are totally sea l ed. Both the feed ll!ld disclulrgc cods of the kiln (Uni t 4) 

### ar e equipped with 

### nn a ir pressurized doub le seal system that 

### is comprised of s teel spring pl ates with self

- lubri cating seal sho es. Fugit ive emi:;sions are 

### p revented 

### by these measur es a . nd the 

### negative pri mary 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. Continuou s video survc:illancc of the combustion chamber exterior is utiliud to detemtine if an A WFCO caused by h i

gh primary combustion chamber pressure corresponds with fugitive emissions. There must 

### be visual evidence of ft • gi tive emissions from the primary combustion chamber fu r a positive pres!!llrc**cv~nt** to be consider ed an excccdnnce . • Mlnlmu m Primary Combu stio n C hamber 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 Ch amber Temperature

- TI1e temperature 

### of com bus tio n gas ioside th e seco n dary chamber is monitored by red w 1da nt thermoco up l es. If th e HRA secondary combustion chamber t empera ture meets or exceeds its limit, an A WFCO interlock i s triggered.

• Emergen cy Safely VMI P osition

- 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 T RY ollows bot combustio n gas to v ent from lhc combustion system during certa in scenarios to protect the downstre am AP CS frorn excessive temperdture s i tu ations. Unit 4 is also equipped with a sec ond 

### ESV l ocated at the kiln face. This ESV is refer r ed to as the s urge vent and provides emergency pressure relief of tl1 c kiln. To minimize excessive emissions during an ESV opening. Ute output from tbo ESV position



### 8



### VESO I 2260transmitteo- i s interlocked**\\~th** t he A W FCO system. 

### If the ESV position is detected as open, an AWFCO interlock is triggered.

• Maximll.lll Bagb o u se Inl et T e mp eratur e - For Unit s 2 and 3, the baghouse inlet temperature (i.e., spray dryer absorber exit gas temperature) i s continuously monitored by a tltermocouple . Unit 4 is e q

uipped with redtmdan t thermocoup les at the exi t o f each SDA. If the HRA bagbouse inlet tempera ture meets or exceeds its limit, an A WFCO i nterlock will occur.

• Maxbn . um Ba g Leak D e t ector Output

- A triboc lectri c sensor is located in tbe duct downstream of the lD fan an d continuously monitors the r elative patticula te matter l oading of the gas. An A WFCO interlock will be triggered if the bag lea k detector o ut put remains at or above it high-high setpoint for t be duration of the alann de l ay time . • Mi nimum Carbo n Feed rate- Powdered activated carbon is a i r injected into the plenum inunediately upstream of the Unit 4 baghouses. A calibrated feeder is used t o continuously moni t or the additi on r ate of carbon to the carbon- a ir stream. If the HRA carbon feedrate meets or exceeds its limit, an A WFCO i nt erlo ck is triggered.

• C arbon Inj ec tion Sys tem Operad n g Pr e$s ur es - The Unit 4 carbon injection system is equipped with a high l evel pressure switch located between tbc car b on feeder aod the eductor . A low level pressure switch is located downstream ofthe b lower that supp lie s air as th e carbon canier fluid . Both pressure switche s have two setpoints, which define the permissible operating raoge at each location . Thes e setpoints are interlocked with A W FCO system.

• Maximum Stack Gas F l owr a te- The pres s ure drop aetOsS a p i to t tube lo ca te d in tbe Cllhaust stack is u tilized to continuously monitor the stack gas flowrate. If the HRA stack gas flowrate mee ts or exceeds i t limit , an A WFCO interlock is triggered.

• M aximum S tac k G as Ca rbon M on oxide Concentration

- The CEMS continuously samples and analyzes stack gas fur the concentrations of c arbon monoxide (CO), and mo i sture using a multicomponent infr ared photometer. The oxygen concentration of the samp l ed gas is analyzed simultaneously using a 9



### VESOI2261zirconium oxide analyzer. A back

- up zirooniwn oxide 02 analyzer also monito rs stac k gas 0 2 concentration . These data are used to calculated the stack gas C O 

### 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 tri ggered.

10



### VES0122622.0 AWFCO 

### OPERA B

IL I TY T ES T P ROCE D URES The AWFCO interlocks are tested bi

- weekly, as weekly testing would undu ly interfere w it h operations, c ause excessive downtime, and subs t antial ly increase operating costs. Testing of the AWFCO system is a time-consuming and manpower intensive process. The current testing program has b een in place under the RCRA pennjt for a n umber of years and has proven to be adeq u ate in detecting problems. AWFCO system operability t esting is conducted by manually simulating input of process cond i tions to the programmable logic controller (PLC). The simulated input for each OPL will be set outside oflim i ts to tr igger the AWFCO interlock and associated alarms. The point at which the simula ted input acti vates the control l og ic for the closure of the waste feed block val ves wil l be observed and documented . Waste feed valves 

### will not actual l y close during AWFCO t es ting. In addition to this A WFCO system contro l logic testing, the func tionali ty of the waste feed block valves are confirmed d uring startups, shutdowns, actu al 

### A_ WFCO condition s , and when transitioning to and from warm standby mode Tests of th e A WFCO system inter l ocks and associated alarms are documented an a AWFCO Testing Log and are maintained separately as part oftbe uni t's operating record.

11



### VES0122633.0 RESPONCE TO AN AWFCO EVENT While an AWFCO event will trigser an alarm, an d automatically ( and immediately) cutoff waste feed to th e incinerator, the o th er portio ns of the · inci nerato r syslom wi ll rema in operationa l and functionin g ( th e APCS, CEMS, etc) . Com b us ti o n chamber tempera tur es will be maintained on naturol gas fired to the main burners, if possiblo. An 

### A WFCO ev ent is initiated in 

### the f o llowing 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 potent i al malfunction. 2) A t this point , the opera t or reviews the situation and rak es action to correct the situa ti on, up 

### to and i ncluding a manual shutdown of th e affected sys tem. These corre.-i:ive actions wi ll be consistent with the · Sta rtup, Shutd own, an d Malfunctio n P l an (SSMP). 3) 

### If !be correcti ve actions 11\ken are not effective, an d tlte opet ·a

ti ng parumet er reac h es its perm i t li mit or a permit preemp ti ve · set point , an A WFCO is initiated. An A WF CO Los form wiU b e used to document the event. If an A \VFCO event corresponds with an e:tceedance whi l e 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 recordkeep ing fonn wil l be used . Regardless of w heth er the hazardous waste residence time bas tranSpired , if there 

### is an exccedance that corresponds "ith an AWFCO event the**follo "~ng**  actio ns will b e taken:

• In vest igate the cau se of th e A W

FCO; • Take appro plia te corrective measures to minimi ze futuro A 

### WFCOs; an d • R ecord 

### the findings and corrective meas ures in the oper a

tin g reco rd . Alter an A V.'FCO has oecurred, all operating parameters must be within limits prior 10 restarting hazardous waste 

### feeds .

12



### V ESOI22643. 1 Repo rti ng R eq uire men ts For each set of ten 1 exceedances of an emission standard or operating parameter l imit, and each exceedaru:e occurs while hazardou s waste remains in the combu stion chamber, a written repo rt 

### will be submitted by Veolia to the Illinois Environmental Pro tect i on Agenc y (JEPA) . The written report will be submitted within five calendar days of the tenth' 

### exceedance and 

### will do cument lhe 

### exceedances and 

### results of

### the investigation and 

### corrective measures taken.

J Exeeedance s occtll'l'in,g**~** malf u uctfon ar e no t included ia this tally.**~** Startup, Shutdown, and Malfiloctkm Pian swnmarizes tbe**repottin~** requirementt;, associated with exooedaooes occurring during malf unctions. 13



### VES0l22654 .0 MANUAL W ASTE FEED CUT-OFF PROCEDURES If 

### an A WFCO i nterlock 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 t he resto ring the A WFCO system .

14



### VESOJ2266

# VES012267
. pdf

### APPENDIX I ESV OPERATING PLAN



### VES012267

## EMERGENCY SAFETY VENT PLAN Prepared for: Veolia ES 

## Tec hnical Solutions, LLC Sauget, I llinois

Prepared by: 

### Frauklin Engineering Group, Inc . 

### F

ranklin , Tennessee

October 2008



### V ES012268

### T AB LE OF CONTENTS
1.0 I NTRO D UC TIO N AND BACKG RO UND . .. . ... . . .. . .... ... . .... . ..... . ....................... .. . 

### ! 1.1 SUMMARY OF FAC I LITY 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 E SV SYS TEM 

### INVES TIGATION , DO C UM ENT ATION AND RE PORTING ............................. .... .. ..... ... . .. .. .. .. ................... .. ........... . ............ .... .. ..7 2.1 ESV INVESTIGATION ................................................................ .. .. . ............ . . .7 2 .2 0 0CUMENTATIONOPESV0PENING ....................................................... . ..... 7 2.3 REPORTING OF ESV 0PENINGS ..................................................................... 8 

### 3. 0 P R OCEDURES D URING 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 NEGAT IVE COMBUSTION CHAMB ER P RE SSIJRE ................ .. .. ..9 3.4 SHUTTING DOWN TilE COMBUSTOR . . . ..... .. ...... .... ........... . .. .. .. . ...................... .9 

### 3.5 DOCUMENTATI ON OF COMB USTION CHAMBER P RESSURE AND TEMPERATURE !VfAINTENANCE ... . ............ .. ..... ....... . ... . ........ . ....... .. .... .... 10

ii 

## VES012269TABLE 1-1 

### LI ST OF TABLES RE GULA T

ORY**REQUIREME~TS** FO R AN EMERGENC Y SAFETY VENT OP E RATING PLAN AND CORRESPONDING SECTION THAT ADDRESSE S ll!E R EQU IREMENT ...... . . . ................... . .................................. . ....... ..... . ...... . .. .. . .. . ..2 TABLE 1-2 TlffiRMA L RELIEF VENT 0P ENING S
.... .. ...... .. . .. . .. .. .. .. .. .......................... .. ..... .. 5

111 

### VES0122701.0 INTRODUCTIO N AND BACKGROUND 

### Veolia ES Teclmical Solutions , LLC (Veolia) ow n s and operates two fixe d hearth inc i nerators (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 Pollutan ts (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 

### E me. ·gency Safety Vcn t Plan and to keep the plan in the operating record. The Emergency Safel)l Vent Plan 

### must foUow the requirements descri bed in 

### § 63. 1206(c)(4). This Emergency Safel)l Vent Plan 

### demonstrates Veoli a'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. Tab l e 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 referen ces to 

### an ESV 

### or incinerator 

### system in this document will i mply a ll three systems. Information that is only app li cable to one or two of the three systems will be 

### clear l y identified . 

### 1.1 S ummary of Facility Information Brief summaries which describe the fixed hearth incinerators and the rotary kiln incinerator are presented in thi s section. 1.1.1 Pixed Hearth Incinerat o rs 

### Each of the fixed hearth incinerators includes the fo llow ing components; 

### • Feed equipment 

### • Ptimary and 

### secondary combust i on chambers 

### • Lime injection system • Spray dryer absorber (SDA) • Fabric filter baghouse



## VES012271Tab l e 1 -1 Regulatory Re q uire ments fo r E m ergency Safety Ve nt Op erating Plan and Corresponding Sec ti on that Addresses th e Requiremen t R eg ulatory

C i t ation Descr i p t io n Pl an Section Documentat i on in operating record of an ESV opening while hazar dous waste remains in the combustion cham ber : 63. 1206(c)( 4 )(i) (1) Record if ESV by-passed APCS (2) Determine ifoperation remained in Section 2 .2 com pliance considering th e emissio ns during theESV I nfo n natio n documenting effectiveness ofplan's 63 . 1206(c)(4)(ii)(B) procedures to m aintain combustion chamber Section 3. 5 tempe rature and pressure , as i s reasonably feasible 63.12 0 6( eX 4) ( ii )( B) De tai l ed procedures fo r rapidly stopp i ng was te feed Section 3.1 63.t206(cX4)(ii)(B) Deta il ed proc edures fo r shutti ng down the combustor S ecti on 3.4 63.1206( c)( 4 )(ii)(B) Detail ed p r ocedures fo r maintaining temperature in com bus tion cham b er Secti on 3. 2 63.1206( c)( 4)(ii)(B) Detail ed procedures for maintai n ing negative Section 3.3 p ressure in th e combus ti on chamber 63. 1206( c)( 4)(iii ) Investigation ofESV o pening s Section 2.1 63. 1206(c)(4)(iii ) Reco r ding o f ESV openings Section 2. 2 63. 1206(c)(4)(iv) Repo rting of ES V openings Section 2 .3



### 2 

### VES0 1 2272• Solids and ash removal systems • Induced draft (ID) fan and stack • Instrumentation, controls, and data acquisition sys tems Various solid and liquid wastes and gaseous feedstreams are therma lly treated in the fixed hearth i ncinerators. Solid waste is fed to the primary (lower) combustio n chamber via a feed conveyor system and pneumatic ram. Liquid waste from 

### tanks and tanker trucks are fed to the primary combustio n chamber thro ugh two atomized liq uid injectors. Liquid waste from containers are fed to the primary combus ti on chamber through a spec ialty feed i njector. A gaseous feedstream i s fed to the Unit 2 primary combustion chamber directly fi'Om gas cylinders. Off gases fro m a hooded teed emission contm l sys tem and from a waste handling glove box. a re fed direct l y to the Unit 3 secondary combustion chamber . Comb u st i on chamber temperatures are maintained using natural gas fired to a dedicated burner in both the primary and secondary chambers . Combustion gas exits the secondary combustio n chamber and enters the SDA, whic h provi des acid gas removal and cooling of the combus t ion gas . Combustion gas ex its the SDA and i s distributed to the f abric filter baghouses , which provide p articulate matter removal. The i nduced draft fan , located downstream of the bagho u ses, moves th e combustion gas through the system and exhausts the gas through the main stack. 

### 1.1 . 2 Rotary Kiln Incinerator The ro tary kiln inc inera t o

r includes the following component s:

• Waste feed syste m • Primary and secondary combustion chambers • Tem pering chamber • Lime injection system • Spray dryer absorber • Carbon injecti on system • Fa bric filter baghousc • Solids and ash removal systems • ID f an and stack • Instr umentation, con tr

ols, and data acquisition sys tems Various solid and liquid wastes are thermall y treated in the rotary kiln i ncinerator. So li d wastes are fed to a r am feeder via a c l am . s beU, 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 dedi cated burner in both the primary and secondary chambers. Combustion gas ellits the secondary combustion chamber and enters the tempering chamber, which**pro,~**

### des coo l ing of the combustion gases . The combustion gas exits the tempering cham ber and is distributed between two identical SDA.s, which**pro~de** 

### acid gas removal and additional gas cooling. A carbon injection sys tem is utilized for controlling d i oxin/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 D escr iptio n of the ESV System Each i ncinerator 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 an d the cylinder vent vah•e which opens the TRV are located in the control room for each unit Valve locks**(\\~th** 

### keys attached) are utili zed to 

### deter indiscriminate operation of these valves. Opening of the T RV allows bot combustion gas to vent from the combustion sys t em 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 s u mmarized 

### 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 meas ures in att empt to restore proper operating conditions. Ot herwise, a controlled cutoff of the waste feeds, an AWFCO, 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 

## VES012274Table 1 -2 Thermal Relief Ve nt Op ening s Paramete r 

### Condition 1 

### E

lectrical Supply 

### L o ss ofPower Air 

### S upply 

### Loss ofAll Pressure (TRV w ill 

### f.ail 

### open ) IDFan 

### Failure/lVIal function SDA Exit Oas T emperature 

### > 500 

### •f 

### Emergency Shutdown 

### Operator ' s Discretion
1 

### The operator is permitted to 

### open the 

### TRY if 

### these conditions 

### are presen t.

5 

### VESO I2275Unit 4 is equipped with. a second E SV 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 overco me the weighted louver . A deflector separates the escaping combustion gas from the feed , and the surge vent angles to a horizontal opening. This design mi nirrll zes the entrainment . of solid thro ugh the surge vent. An ESV opening may correspond with a malfunction event . Information regarding operation o f the incinerator and the associated control equipme nt during times of start-up, shutdown and malfunc tion i s prov ided in the facility 

### Start-up, Shutdown, Ma/fimction Plan (SSMP) .



### 6 

### VES0122 76

### 2.0 ESV SYSTEM REPORTIN G 2.1 ESV In vesti gation INVESTIG ATION, DOCUMENTATION 

### AND

If an ESV opens fo r any reason d u ring nomtal op erations, the ope r ator is instructed to: 1) Verify that all waste 

### feeds to the incinerator a re cutoff, 2) Ifposs i ble, operate the ID fan, 

### and 3) Ifpossib le, maintain normal combustion chamber t emperatures on natural gas. If hazardo us 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 staffto deter mine poten tial causes for the event and to estin t ate excessive emissions. 

### 2.2 Do c umentation of ESV 

### Opening Each ins tance in whic h t he emergenc y vent opens will be recorded in the facility operating recor d. Titis record will, at a 

### minimum, include the date, time, and the operating mode 

### at the time of th e ESV open ing. Titis data is automatically docume n ted in the operating record by the CMS. If the ESV opens when hazardous waste remains 

### tn the combustion chamber (i.e., when the hazardo us waste residence time has not expired) during an event other than a malfunction (as defined by the facility SSMP), Veolia personnel 

### will document th a t an ESV even t 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 u pstream from the facility air pollution control devices (APCD), i t 

### is understood that combustion gas by

-pas ses these emission contro l devices during an ESV event. Tlus by-pass will be 

### documented in the facility operating record. If an ES V openi ng 

### is attributed to a malfunction and occurs when hazardous was te remains in th e combustion chamber, a malfunction recordkeeping tbrrn will be completed to document the event.



### 7 

### VESOJ22772 .3 R eporting of ESV Op e nin gs 

### If an 

### ESV opening 

### results in a 

### failu re to m eet 

### 01e emission standards for the facility, Veolia 

### will subm i t a 

### written report 'il'ilhin five 

### days of the ESV event to Illinois Environmenta l 

### Protection Agency (IEP A), documenting 

### the results of the investigation and corrective 

### meas u res taken . 

### In most 

### cases when an ESV event 

### occ u rs , i t is 

### instantaneous. TI1erefore, it is practical to assume that diminimus emiss i ons occur during these instantaneous events.

8 

## V E SOL2278

### 3.0 PROCEDURES DURING AN ESV In 

### the event of an ESY opening that occurs while burning waste, it is important that was te feed is stopped rapidly, and that comb ustion chamber temperature 

### and n egath•e pressure are m aintained to the extent practical. Following the expiration of the hazardous was te retention time , shutting down the com b ustor (allowing key co mponents to cool ) i s equally i mportant These item s are addressed below. 3.1 

### Stopp ing Wast e F ee d an d S hu tting Down th e Co mbn s tor An ESY opening is likely to be preceded by a AWFCO or safety interlock that ca uses a waste feed cu t off prior to the ESY opening. The ESY position is also interlocked with the AWFCO system . These redundant measures ensure that waste f eeds will be 

### s toppe d during an ESV o peni ng . If the AWFCO system fails to cutoff wastes to the incinerator, th e waste will 

### be manually cutoff in a quick a n d sa fe manner . Waste burni n g cannot reswne u ntil the ESY i s closed, corrective ac tions 

### taken, pernrission is granted from the incinerator supervisor, and 

### all parameters 

### are within 

### limits. 3.2 Ma inta ining Co mbus ti on C hamber Temper atur e Comb ustion chamber temperatures are m aintained using natural gas 

### fired 

### a dedicated burner in both the primary and secondary combust i on chambers . Ifpossible, the buming o f natural gas w ill be used 

### to maintain adequate combustion chamber temp e ratures for the com bustion of waste remainin g in the i n cinerator . 3.3 Mainta in i n g Negative Co mbustion C hamb e r Press u re 

### Ifpossib l e, the ID 

### f an will be operated d uring 

### an TRY opening to minimize the q uantity of combustio n gas 

### that by-pass 

### the air pollution co n trol equipment. Operati on of th e 

### ID fa n during an 

### ESY opening will maintain negati v e combustion pressure to the 

### full extent th at is reasonably feasibl e. It is likely th at the opening of the TRY w i ll cause th e system to l ose negative pressure 

### (i.e. the 

### ID 

### fan canno t induce a strong draft) . For surge vent opening, the positive pressure excursio n will be te m porary, and th e ID 

### fan (if operable) will be used to restore negative pressure in the primary chamber, as quickly as possible. 3A Shutting Dow n th e Comb u s tor An event which causes an ESV opening may requi re a cold shut down of the combustor i n order to perform couective actions. After sufficien t effort is taken to 

### minimi7..e emissions by mai ntaining the te mperatur e and pressur e , t he incinera tor supervisor will decide 

### if a shut down is warranted. 

### If 

### the ESV opening corresponds**"~ th**  

### a m alfunction
9 

### VES012279event then the correct i ve measures taken will be consistent wilh the procedures pr escribed by lh e 

### SSMP. 3.5 Document atio n of 

### Co mbu stion Ch.liJI)ber Pres s ure and 

### Temperature Maintenance 

### § 63.1206(c)(4)(ii)(B) requires that the facility demonstrate that the procedures of this p l an are adequate to maintain combustion cham ber pressure and temperature willie hazardous waste rem ai n s iu th e incinerator, 

### if feasible. The occurrence of an emergency safety vent opening at the V eolia facility is poss i ble 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 n ot feasib l e to maintain the combustion chamber temperature during an ESV event. L ikewise, it is likely that the opening of the TRV will resu l t in lhe loss o f negative pressure. The duration of a surge vent opening will typically be brief and only momentarily preven t tnaintaining the combustion chamber pressure. The procedures presented in this plan 

### will be followed to m i nimize the effects of such occurrences.

10 

## VESOJ2280

# VES012281
. pdf

### A PPENDIXJ 

### FEE D STREAM ANALYS I S PLAN



## VE S01228 1

# FEEDSTREAM ANALYSIS 

# PLAN

Veolia ES Tec hni ca l S ervice s, L LC Sauget, Jllinois 

# ....

· --------- -·--

Octo b er 2 008**·~** 

# '" ' 

# f

' '

. 

### L

.

' 

### ;

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# I 

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### I 

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# i 

# t V

E S012282**~** 

### .... ; 

# ... . .... . .. .; . . .

· ,. 

### Feedstream Analyais P l an - October 2008 

## TABLE OF CONTENTS

1.0 INTRODUCTION 2.0 FEED STREAMPARAMETERS 2 .1 Chlorine 2 .2 Metals 2 .3 

### Ash 3.0 ANALYTI C AL RATIONALE 3 .1 

### AnalysisPerformedbyVeolia 3.2 Analysis Performed by Othel's 3.3 Manufacturer Data or Other Published Jn:formation . . ,• · 

# I , I

l 

### • 

# i 

# I
, : ·



### , · : 

## J

: 4.0 APPLICATION OF ANALYSIS 

### FOR FEEDRATE

### COMPLIA.~CE 

## i

· ---·- -- - ---t

# ------·-· .. 

## ·-- --- - ·- -- -- 4 . 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."'i ALY S I S 7.0 COI\fi'LIANCE WITH FEED RATES 

# i I • 

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## " l· j . · I; 

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. VES012283

### - ,, . . . : ::;.**·~** .. ' • . ........ .,1 

### Feedstream Aunlysis Plan

- October 2008 1.0 INTR OD U<-"TIO N Pursuant 

### to the regulato ry re quirements found in 40 CFR 63. 1 206 (c ) 

### ofthe HWC MACT Standard, Veolia ES Technical Solut ions ,ILC (V eolia) has de ve l oped 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 

### con tain 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 suc h that**~ch** 

### ofthe sut>sequent sections specificall y address es 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 . I n ,•,,.,; .. .. . ;



## ..


## . '



# ·· .. 

### many i nstance s , thi s F AP will ref-erence the facility's Waste Analysis Plan (W 

### AP). The ; . WAP is an integral part oftheRCRA Part BPerm it, the Permit Application, and any**.** 

### subsequent revisi ons or addenda to the Part B Permit or Permit Application. 

### ! ·: As required by 

### sections 63 . 6 (e) (v ) an d 63.6 (eXvi) ofthe HWC MACT Standard, the 

# ! F

AP and other docwnents containing procedures or information referred to 

### in the FAP**~** 

### · will 

### be made availab l e fo r inspection when requested by 

### the Admlnistrator. The FAP, 1 ,:,; 

### correspondence with the A dmini stra tor concerning the F AP, and any sub seque nt add . itions or modifications to th e F AP will 

### be kep t in the :fucility's Operati n g Record. If ' '· Veolia i s required to 

### submit copies ofthe F AP or portions of i t (or related documents),

## ~**------ ~al-bus~ill:formalion-entit** **ed-to-protection-ftor:rrdisclosure 'Wilt** **ire'clearly'- ····** **----- --+**  

### designated. ' 2.0 FEEDSTRE A M PARAMETERS There are three feedstream consiiluents that are specified in 

### the HWC MACT Standard for emission and/or feed.ra te li mitations and !bat may be present in 

### any given feedstream. These three are: I) Chl orine 2) Metals (M e r cury, Lead , Cadmium, C'hrotni um, Beryllit u:n, and 

### Arsenic) 3) Ash These three constituents 

### will serve as the feedstrearn parameters o f concern in the F AP as req u

ired by 40 CFR 63.1206 (c) (2) ( 1) oftheHWC MACT Standar d. Feedstream data 

### app li cab le to 

### eac h of these parameters 

### will be obtained for all feed.s treams i n order to control the inc i n

erati on of them and rema in within the feedm te limits set for them. 

### 2 . 1 Chlorine Feedstream data will 

### provide a weight- based percentage ofchlorine for eaclt 

### waste feed to the inciuerators . These r esults can be used 

### to bo th estimate targeted feed 

### rate values and control ac tual feed rates during incinera1ion.

2 

## ' (

. i

i,

i . 

### VE$012284: •• < ........ . . . _J ( j • • ..**~** • •**~** 

### .Feedsn·eam An a lysis Plan

- 

### Oc tober 2008 

### 2. 2 M• tals Fcedsll'eam data will provide a parts -per - million concentration for each of1he listed metals in each 

### ofthe waste feeds to the incinerators . For analyti cal results til3t sho w less than d etection limit concentrations, Y:i 

### the detection l i mit value 

### will be usod 

### for incinerator feed computations. These results can be 

### used to both estimate targe ted feed rate 

### values and contro l actual feed rates during inc i nera tion. 

### 2. 3 A sh Feedslream data 

### will provi de a weight-based percentage of ash f or each of the 

### wa ste feeds 

### to the incinerators. These results 

### can be us ed to both estimate targeted feed rate 

### values and conll'O l actual feed 

### rates during incineration. 3. 0 

### ANAL YTICALRAT lONALE ln 40 

### CF'R 63. 1206 (c) (2) ( ii) 

### ofthe HWCMACf 

### Standard, a 

### facility is required to idelllifY how**it" "**  

### obtain the necessary 

### analysis to comply with these regulatio n s. There are t hree 

### sources of anal ytical information that V eolia can us e in evaluating the feedstream parameter s as described in Section 2. 0 of the F AP . Th o

y a re : 

### 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 a ddressed . 

### Many ofthe analytical procedures performed as described 

### in the F 

### AP are also required as part 

### ofth e waste acceptance and m anagement process at Veolia . The information derived from these procedure s can the n be 

### used i n 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 

### Veolia facility , including those that undergo sub sequetJt blending prior to incinerat i on, and a l so to wastes that are generat ed 

### at the facility . 3.1 Allal y sis 

### Pe rf

ormed b y 

### V eolla 

### The predom i nate 

### means applicable to this source of analytical information 

### is tbe metho dology described in Section 

### 5.0 of

### the 

### FAP . Specific an a lytical methods performed in the f a

cility's labomtory are applied to applicab l e feedstreams to produce values for the required parameters. Typically, the feedstream is a waste profile from a generator that has be en accepted according to the facility ' s W AP gui d e

l ines. This waste will have had anal ytical work performed on a samp l e for an initial acceptance decision and supp l emental analysis as 3 • I , ; ' • ':-: 

## I ! I i f · l l; 

# I !: 

# ! .

. .. .



## ' ' ·



## .. I' 

### VES012285•• , • d • I o 

## . , . 

### - ,. ,· . . . 

### Feeestream Analysis Plan

- October 2008 required for s u bseq uent shipments of the waste. This analytical work will 

### include i nformation on th e parameters identifi<!d in the F AP and can be 

### used to contro l the incineration of th e feedstream s. 

### In other instances, the feedstrearos are wastes bl ended together at the facility (e.g., bulk liquids and bulk solids} or wastes generated by the facility (e.g. , l aboratory wastes , incinerator ash). Feedstreams that ate the result ofbl ending or other on - si te processing steps prior to incineration can have parameters determined from t he same analytical methods described in the previous para graph or by statistically arriving at 

### an average val ue based on a body ofpreviously analyzed samples. Wastes generate d by 

### the facility will have parameters determined from an average value based on a body ofpreviously analyzed samp l es. For many fced st reams, the best source of infonnation for tbe parameters idontified i n the FAP 

### wiU be 

### obtained using the tecbJUcal expertise ofVeolia persotmel. Example s of these types offeedstrcams are labpaclcs , controlled sub stances and empty containers. The facility ' s WAP lists some of these reference sources in Appendix W AP

- F. 3 . 2 

### A n alyst s Perf or me d by Ot hers In silu.at i ons where Veolia cannot perform the necessary analy s is due to the nature of tho fecdst rcam (e.g., gases, some reactive ma t eri a ls ) or when previous outside analysis of**---- .f~1he-mnda~ds**  

### of 

### tttis F:t\:Pis-availabie;-Vea!ilrwi:lllll:l:'epnh:e 

### a

n a lysis of others in determini n g parame ter values. This ana l ytical iufonnation will be evaluated and use d to contro l the incineration of feedstreams in the same manner as analytical information produced at th e faci li ty . 3 .3 Manufa ctur e r Datu or Ot h er Pub lis hed Information Many feedstreams bsve pre -existing infomtat i on app l icable to 

### them t hat can be used to 

### de t cr:mine the 

### valuw ofthe parameters as identified in th e F AP. Thi s can take the fonn of manufactnrer specifications and data, Material Safety Data Sheets, reference sources or other pub li shed infonnation. The facility's WAP lists some ofthese reference sources in Appendix W AP-F . Examp l es ofthese types of feedstreams include commercial products, phrumaceutica l s, chemical reagents, snd 

### gas cylindCI'S. This information will be evaluated and used to contro l the incinera t ion ofthese f ee dstreams in th e same manner as analytical infomtation p roduced at t h

e facility. 4 .0 APPLI C ATIO N OF ANAL YSIS FOR FEE DRA TE C O . MPLIANCE 

### F

eedstream data wi ll 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 ofthese feedrate compliance methods is roquir<!d by 40 CFR 63.1206 (c) (2}( iii ) oftheHWCMACT Standard and outlin<!d in tbiJ; 

### section oftbe 

## FAP.

4 .. .. . ::**~ ~~**  , . . 1 

### i



### .. i 

# I I !

1. !. 

# ' •·**~·** . '· 

### ' 

## ' i ' . !· ;,; ;;,



## VESOI2286. . : .. : ... : · . . .:: 

### Feed stream Analysis P l an - Oc tober ZOOS Ana l ytical results can be 

### used to both estimate targeted feed 

### rate values and control a ctual feed rates d uring 

### incinerAt i on. Analysis from laboratory testing at th e facility, analytical results from others , published infolllllltiou, and technical evalua tions by Veolia personne l can all b e 

### used in 

### complying with 

### feedr ate limitat i ons for t h e 

### parameters i dentified i n 

### tbe F



### AP . In 

### a dd i tion, th ese anal ytical information sources can be used f or wastes from generators, wastes blended 

### at the facility, and wastes generated at 

### the facility. 4. 1 P rocess Plannin g 

### for lleedstreams 

### When evalu ating anal ytical results and any 

### ad ditional infom1ation app licab l e to a potential fecdstream, a decision must be 

### made whether parnmeters for that feedstr eam are acceptable 

### for feeding to the inci n erators or if so me l evel of feed preparati on 

### is necessary . This step io the feedsneam evaluation process is called process p l a:t lning. It 

### is applied to blendi ng was t es, proces sing wastes into comb ustible char ges, and 

### d e

te

rmining if



### wastes C3ll 

### be fed directly to the incinerators 

### as initially received at the facility. 

### This planning i s performed 

### based on infonnation fro m an alytical results , incioerator perfonnance ca p abilities, pro cess operation history , and 

### the technical expertise of

### the p

roc ess pl anni n g personnel involved. 4.2 

### Pro cess Contro l f

or 

### Feedstream s bJ 

### order to ensure that feedrate limit s for the parameters in the 

### F AP are no t exceeded**------ -ilditl** **tlriri:n:ll ~·'Oftbe**  

### i neines:atws, automatic SJSlems mustbe-irrpfaee t o wn n dl tlfe --- ---· ·- 

### incio erator process . These sys tems continuously track 

### the feedstream parameters as they are 

### i ntroduced ioto the 

### incinerators and make 

### 1he nece ssary 

### f eed adju stments or cut ·offs for compliance. Section 7 . 0 

### ofthe FAP a ddresses 

### th ese sys t ems an d the rationale behind their operation in 

### greater d etaiL 4.3 D o cu mentati on andRec ordkeeping for 

### Proc. ess Planning and Co n tro l 

### Documenlalion of process planning and control is demo n.strated by the extern. -ive body of ioform ati on co ll ected in the f a

cility's data management system, and , 

### ifneeded, distributed in 

### hard cop y form 

### to ap p rop riate personnel. 

### Th i s includes laboratory anal ysis used for f eed p reparation, b ulk waste storage data, 

### processiog directions, and related iofonnation. A ctua l iociuera tor operati ons data 

### is rocorded in 

### prin ted s ummaries, 

### reco rded on to d igital data storage systems, and i s also 

### selectively available on-line. 

### This iofonnation will 

### be retained in th e operating record for th e life 

### ofthe facility. 5.0 SAMPLING AND ANALYTICAL METHO D S 

### Th e requirements in40 CFR 63. 12.06 (c) (2 ) 

### (iv) and (v) ofthe HWCMA cr 

### S tandard state tha t 

### a facilit y must identif y 1he sam pling and tes t me thods used for anal yzing the feedstreams . Th e sanqJi i ng methodology and much of the analytical methodology that 

### is d

e scri bed in 

### Soctious 2.0 and 3 .0 ofth e fa cility's Was te 

### A n alysis Plan is ap p l

i ca ble to the 

### FAP . Addi tio nal sampling and test ing inf onnat ion i s incl ud ed io the following paragraphs of this 

### section.

5 

# I r 

# i 

# I ; .



# I 

# I . I**~** 

### VES0 12287... ) • : . • , .'• • • '**~·** * ' ; , , ; ,,. .·,•• . . .. . . .. ., ., ,_..; I 

### Feedstream Analysis Plan

- October 2008
5.1 

### Samplin g 1\ f e th . odologies Sampl in g is perfonned a t the Veolia facility to ident ify waste slripments and also by the g enerator at their location when malcing an initia l determinati011 on the acceptability of the waste 

### at Veolia. In some ins t ances, an actual samp l e will not be 

### required beeause technical personnel at Veoli a will 

### have de termined that sufficient documentation already exists that identifies information regarding the parameters described i n Section2 .0 ofthe FAP (see also Section 4.0, Paragraph 4.1.12 (2) oftheW AP) . 

### In order to obtain a representative samp l e of the 

### waste, specific sampling proc edures that are dependent 011 bofh fhe natUieofthe waste sampled and the typ e of processes in which the waste wiU be stored o r transferred must be 

### performed. Secti on 2.0 oftbe facility's WAP and pertinent appendices in the W AP list fhese procedures and th e ASTM method number (or other EPA approved method) on which they are based. 

### This section in the W AP also addresse s the sampling equipment used, the types o f intended containment or processes that can i mp act the sampling, and guidelines on how to ensure that a valid and representative sample is obtaioed. ; 5.2 

### DocomentaUon a11.d R ecordkeeping Associated with 

### S amp ling :· 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;un ple also has a label affixed to i t 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 rel ated to determining the amount ofchlorine in 

### a feedstream are found i n 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 con tain thes, e metals in a no n-water -soluble form or a water-soluble form . Samples offeedatreams in a non-water - soluble fonn will 

### r equire additional preparation steps prior to 

### analysis. The anal ytical procedures and 

### EPA approved methods related to determining the amount of listed metals in a feedstrea m are listed below. Digestio n Procedure for Non

- Water -S olub l e Samples Me thod 305 LA

- Microwave Assisted Acid Digestion of Sediments, S l udges, Soils, and 

### Oils

6 

## fi 

## '



## : j

, ; I. 

### ' = :



# . 

# I

VES0 1 2288· · '· . ·

.. :.· . : · 

### .. . .. ..**~** • •••• " < • 

# .. .**~. ..** **.** '.**·,·~** 

## . . · .· · • : . .

: 

# ..**,.~;· ·**  

### .... ; ;·: 

### Feedstream Analysis Plan

- October 200& Procedure 

## for Detennjn i ng Concentration ofMercury 

### in Samp l e 

### Met hod 7473 -Mercury in Solids and Solutions by TheiiDal Deromposition, Amalgamation, and 

### Atomic Absorption Spectrophotometry 

### P

roce4ure for Pctennining 

### Concentration ofArsenjc. Bervmum. Cadm ium. Chromium an d Lead in Sarople Method 601 OC

- Inductively Coupled P lasma- A tomic Emission Spectrometry AS II The analytical procedures and 

### BP A approved metho ds related to 

### determining the amouot of 

### ash ina feedstrearn 

### are found in 

### Appendix WAP-Ato the facility's 

### WAP. 5.4 D oc umentati o n an d R e.cordkeeplug Ass o ci a ted wi t h 

### Sa m pl e A n a l ys i s Documentation of analytical work is accomplished by recor d

ing it in laboratory lo gbo oks , entering it into the 

### facili ty's data management system, and, jf 

### needed, distributed 

### in hard copy fotm to appropriate personnel. All 

### technical fi l es for waste profoles will also inolude initia l laboratory analysis and any applicable su bsequent

### ----**-- ~;:~~~~-**  Thi

_ s_infi

_onna ti on will b e

### re~".~**.** in_tbe operating record

### f~**r ~<:life**  o::.f.:: th::"

-- -·- ·--- ·- - 6. 0 FRE Q UENCY O F ANALYS I S ln40 CFR63.1206 

### (c) (2) (vi) 

### oftheHWCMACT Standard, a facility i s req uire d to identify 

### the frequency with which an initial analysis is repeated 

### or reviewed to ensure that 

### it is cuuent. Thi s F AP 

### will require that the analytical iofonn ati on for the feedstreams be re-evaluated on a frequency consistent with t ha

t described for all wastes as deooribed in Section 4.1.3 o f the fucility' s W AP. The three events that m a

y trigger a nee d 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 Veo li a is inconsistent with tbe original analysis 3) Five years have passed si nce !he last asse s sment ofth e feeds tream 

### In order f or a fecd&1ream to b e**con~'idercd** 

### a cceptable again for incineration after one of these events bas occurred, the evaluati on process as described in 

### this F 

### AP must be completed. 7.0 C O ?t fP UANCE WfllJ FEED RA T ES Veolia employs process contro l systems for the inc inerators that monitor, ad just and record feedstreams and th e key parameters identified in the FAP that are associated with

7 

# 1 , . I i i.

j I 

## I . 

## ' i 

# j j 

# r i ! .' 

### ; : 

# t

:

VE S012289..**-.., ·~** **:"** .,.;:.· · · . · ·, : .,**.** ·. : .. .t .·**.~** . .. . 

### Feedslream Anal ysis Plan

- October 2008 theJa These systems m ee t tbc requirements of40 CFR 63. 1 206 (c) (4), paragraphs (i), 

### (ii ) and (iii). 

### TI1 e systems and the rationa le that supports these systems are descri bed in 

### the fo ll owi ng paragraph. 7 . 1 ) .<'eed 

### Rate C o mpl ia n ce S)·s tems a nd M e th odo lo gy After the metals and ash concentrations fo r feedstreams are d . erermined, they will be 

### entered into the 

### facility's data management systems. 

### These fcedstream s 

### are i dentified in the system un der a site tracking n umber, bulk pit n u mber , or tank 

### num b er. On ce this 

### informat i on is in tho was te tracking system, tbe incinerator control systems are a b l" 

### to import and 

### store tbe data for use as the waste streams are processed at 

### the incinerators. All 

### waste i ntroduced into the incinerators has an associated site identification designation (receiver number, etc . ) so it can b e referenced to tb.e appropriate data from the was te trac k ing system. As 

### weights are recorded at 15 second intervals for each specific waste stream entering the incinerator, computations are being performed to calculate the qu a ntities ofmetals (as low v olatile metals, semi vo l ati l e 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 estab l ished operating parameter liroit s f or the m

e

tals categories a nd ash . One hour and 1 2 hour rolling totals are disp l ayed for the incin e

rator operators for monitoring of these 

### .feeds .

8 ! 

# I I

. i ' l ;j



## VES012290

# VES012291
. pdf

### APP ENDIXK TITLE V ITEMS TO BE REMOVED



### VE S0 12291**~c lia**  Snvironra9ntal Se rvi ces Per m

i: No .: v- rL

- l716300l03

- 08

- 01 Page: 7 of 176 2 . 1 H azardo us Waste Combustors, U nits 2, 3 and 4 (A) Emission Limi ta tions a n d Standards 1 4 0 C . F. R. § 7 1.6( ii ) (1 ) ] The P e rmittee shall c o m ply with the follo«ing requiren t ents for each in dividua l inci n erator u n less speci fied ot:1"• €!'' · " i se : 1 . Vis i ble em i ssion Limitation . (a l The**Perm~t tee**  shall nor; cause o r allo " t h e er.lission of smoke o.r oth e r pa rticula te matter, • .d th an cpacit y g reat e r than 30 pe.rce n t , i nto the a tmosp here 

### fro m any emissio n sour ce, except as allowed by 

### 3S IAC 21 2.223 ( b)**a~ d** **21 ~.**  (3 5 lAC 212.123(a) J (b) The Perm itt ee shall not ca use or allo" the emissio n of fugitive part i cu l ate mar;ter fr om any**p~ocess ,**  in cludi ng any mat er i a l**~~n li** **ng** o r**to ~age**  activity , th at is visibl e by an observer l oo king g enerall y overhea<i a " a p oint beyond t he pro p ert y line 

### of the scurce**~~ le** **ss** 

### th e wind speed is 9 r e a ter th an 40 . 2 kil ome ters per ho ur {2S miles per hour.) [ 3 ! , IAC 212 . 301 and 212.31'1 

### 2 . Sulfur Di ox i de Li mi tacio n. T

ota l su l fur di o xide emiss io ns fr om the faci l ity sha l l n ot ex c ee d 7 . 7 tons p er year fo r u ni•s 2 and 3 and 5 0 . 76 tons per year for unit 4 . { Cons tru c t ion pe r m i ts 87100024 and 88010001 1 3 . Carbon Non<>xide Lirr. i tat io n. {a) T he Per: mit t .::e sha l l not al low emiss io ns o f ca r bon 

### monoxide in excess o f 100 part s per mill ion by 

### vo : ume, over an h o ur ly ro lling average (mo nitored continuously \V i th a c or . tinuous emissions monitor i ng system: •, d r y b a s i s and correcced to 7 perce n t oxyqen . Th e Permi.tte e must als o document th at , dur ing the destruction and re mova l**effi~iency** (OR&) test runs or their equivalent as p ro v i d e d by §63 . ! 206(b) {7 ), hydroca r bons do not 

### ezceeti 10 par t s per million by 

### volume duri ng those**~ns,** ov er on ho u rly rolling aver age (monito ::: ed continuously tr;ith 

### a co ntinu o u s emissions monit.o rirH:! s y stem), dry basis, corrected to 7 percent ox yg en , 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

- 1 71 6 3 00 103 -08 -01 !?age: B of 176 (b) T he 

### F e r m i ttee shall not allol < emissions of carbon mo n oxide emissions from t he inc in e rator in e x cess o f 500 

### ppm corrected t o 50% 

### e xcess air. ! 3 5 lAC 216 . 1 4 1 , Construction pe r m i ts 83 12 0053, 8 7 10 002 4 , an d 88010001 ) (c) The Permi ttee s h all not allow emiss i ons of car b on 

### monox ide emissions from the facility in exceSs of 6.6 tons p er year f or 

### u n its 2 and 3 and 1 3.86 tons 

### per year for unit 4 . 

### !Const ru ctio n per mi ts 8 7 1 0002g and 88010001) 4 . Pa r tic ul ate Ha tte r Li mitation. (a) The Permittee shall no t c a u s e or allot" the emissio n of**particu.l~te** m a t ter into t h e atmosphere 

### from any incin e r a to r bur ni n g more t han 

### 0 .907 megag,am p er hou r (l1g/hr ; 2 , 000 pound p er ho ur (lb/ hr ) l b u t 

### less than 2 7. 2 

### Mg/hr (60, 000 lb/h r) of**n~fuse** 

### to 

### e xceed 183 mill i g rams**~r** 

### standard c u bic**te~** ( m

g/s c m; 0 . 08 grain per standard cubic foot (g r / scf) ) of 

### eff l uent gase s 

### correc t ed to 1 2 

### p e rcent carbon d i oxi d e (35 lhC 212 .1 8l( b) j . -( -!>-

) P ri9li te**Oete~er** 

## u, 2QGB , tJ:ie P e 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 aR** **da ..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 afte r October 1 4, 2 008 , t h e P e r m i t tee -shall n

ot allow emission s of pa rti culate matter from the fa cility i n excess of 0 . 013 grai n per sta n dard cubi c foot (gr/ scf) , correcce c l to 7 percent 

### o xy ge n. (40 C . f.R . § 63.1219(a) ('l) j (d) 'l' be Pe rmi ttee shall not 

### a ll o>J emissions of 

### total s u spen ded so l i d emissio:)S from t he fa ci lity i n e x cess of 15 .0 ton s pe r ye ar fot' units 2 cm d 3 and 1 6.92 tons per year for unit 4 . !Constr u c tion permi ts 87lOOOZ4 and 880 100 01 1 

### 5 . Vo latile Orq e n i c Compounds Li mitat i on . (a) 'l'he Permittee shall net cau se or al l O\\ ' th e discha"ge of more than 3 . 6 kg/h r ( 8 lbs/hr) of organic 

### materi al into the**a~rnosphere** 

### from any emission unit,



## VES012293Veo lia E n vil · cnroental Servic es 

### t' ermit No . : V-!L

- 1 7 163 00103

- 08-0 1 Pagt'l : 9 of 17£ -except that , if no ector n uisance ex i s t s, t his**lim i~atio** **n** 

### s h all apply only 1: 0 

### photoch e mi ca lly r ea c tive ma te rial. A l te rn atively, Pe rmittee may u se a 

### control devi c e to reduce such em i ss i ons eithe r to 10 p pm e quival en t m etha n e (mo le cu lar 'Ieight 1 6 i 

### or less, or to convert 85 pe r cent of the**hydroca~bons** to carbon 

### d ioxi d e and wa t er . [ 35 ! AC 21 9. 301, 21 9. 302) (bl Orgenic mate r ial e m issions from the fac ili ty sha ll O'lOt 

### exc eed 0. 9 t ons 9 er y ear for u nit s 2 and 3 a n d 3 . 1 t ons per**~rea r**  for unit. 4. ( C o ns t ru ct i on perm its 

### 87100024 and 88010001) 6 . Ni t:oge n 0:-;ide l .. imita ti on. Nitro 9en Ox i de e m i ssio ns f rom · t he facility sha l l not e ;; ce ad 

### 4 . 0 tons per year for unit s 2 and 3 and 61 .6**~e ns**  per yea r for unit 4. { Co ns t ruct io n permits 8 7 1 0 002 4 

### and 880 100 0 11 '· !-!azarclo us Ai r Pol l u ta nt Li mitat i 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 ·** **·-e****tal*la-"~****-c.., .b.,i.** **;; -m** **eter t>** **gids=~~ .....l:** **o --"'--** **pe rc** **e~ :..-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.siru 1 c: • c o r rec!:.e.cL_:.0-7_pe.r.c.e-n. t 

### oxygaR: -(h" ) ,.... ornJ> i nQd**e!;l "'s~** **lr:t$** Q f**~•;eAic, tO's¥yl~** **ffiT-~ cmi** **m~ -e..,.c** **o. ss**  of S?**;.;qJG!~-4;G.o·** ..,**fA "'C** **W-'1 -t-o** **~.Q..I:h..** 

### < b) On and a fter October 1 4, 2008 [ 4 0 C .f . R . S 63.1219\a) l : ( i} The Permi ttee shall not. allo \ -t emissions of d iox i n 

### and f u rans f r om the fac i lity in excess o f 0 .2 0 ng**~EQ /dscm,**  corr ecte d to 1 pe r ce n L c x ygen ;



## VES012294

### veo l ia En v ironmental Services P

ermit No.; V

- IL

- 1716300103

- 08

- 01 ?age: 10 of :7 6
(iilThe ?ermittee shall rJot**alloi<~** emiss i ons of mercury from the facility i n excess of 130 

### pg/d s cm , corrected to 7 

### percent oxygen; (iii)'!'he ? e rmi ttee shall not allo w em is s ions of 

### cadmium 

### and lead from the fa cility ir. 

### excess of 230 }Jg/dscm, combined emissions , C · ':lrrec t ed t o 7 p ercent o>:ygen; (i\t)**TfH~** P e r m i t t ee shall n ot allc\v emissions of a rse ni c , be ryllium , and chromi um from t he 

### facility i n e:<cess 

### of 

### 92 p g /dscm , combi n ed em is sion s , 

### correcte d to 7 

### percent oxygen; te l 

### The Permittee 

### sha: . l 

### design, in s t all. 

### operate, and maintain a t reatme nt pro c ess that destroys ben z ene in the**~;aste** stream by i n cinerating the waste in a 

### combustion unit that. achieves a**dest~uc t:i** **on** 

### effic ienc y of 99 percent or grea ter fo r ben z ene ( 40 C.P.R. S 61.348 t al t lJt iiiJ) . (d) P .ll 

### joints o < s eams 

### between t he pipe 

### sections of any t r ansfer system that c onsists of cont i n u ous ha r d pip i ng sha ll be permanently 

### o r semi

- permanently sealed (e . g . , a 

### welded joint bet,;een t H O**sec~ions** 

### of metal pipe 

### or a bo l t ed and gaske t e d f la nge) 

### (4 0 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..Q****x1g.** ao;: i d**~nd ~1** **11** or i**r. ~-** **~m i**  "'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'ao s., 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 , 20 08 !40 C.F.R. §**~3** 

### . 1219 (a) 

### l : '!'he P ermittee shall 

### not. allo" hydrogen chloride 

### and chlorine gas <to t a l chlo r ine ) e m issions from the facility i n exces s of 32 pa r ts per million by vcl urne,



### VE SOI2295

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### (t·;...{ Veolia En v ir onmenta l Services P

ermit No.: V

- IL

- 11!630 0103

- 08

- 01 I? age: 1 3 of 17 6 2. 

# the. Pe rm it t ee m u st operate Un its ? 3 , an d 4 under**t~ ~·** **9** operating pa r a meters limi ts (OPL ' s)**demonstrate** complian c e • ,; it h Subpar t EEE .

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## VES012296

### Veolia Env i ronmental Serv i ces Pe r m it No . : V

- l L

- 1 7 1 6300103

- 08- 0 1 I Ooerati na Parameto rs

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### V E S0 1 2297

### Veol ia EnYironmental Ser...-ices Permit No . : V-iL- 1716 300103

- 08

- 01 

### Page: 86 of**l?~** {c) 

### T he P e r m itt ee may petition t he Administrator to obtai n \Yt"itten approval to b U .( n hazardou s t<7aste prior 

### to submitting**~** 

### Notification of Compliance for**pu~poses** other than tes t ing o r p retestin g. Th e 

### Permittee must specify operating requirements, in c l ud i n g 

### limi t s on operating paramete rs, that th e**~ermittee** de te rmi nes 

### wi l l ensure complian c e t-.•ith the e m i ssion sta n dards of th i s subpart bused on available informatio n i ncl u ding data from the failed p erfo r mance test. The Admini s trator \-! i ll revie •.v, 

### mod i fy as necessary, a nd app r ove :. f warranted t he in te r.i. rr. 

### o p erat ing requirements. 

### .•.n appro val cf interim operating r e quir e ments ttlill incl ude c. s ched ul e fo r · 

### 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)) : Th e Pe rmitte e m u st retain t he**foll >~ing**  in 

### the ope rat ing reco.t"ds app lica ble to the Hazardous t-1aste 

### In ciner ators operated at this site: Reference Documen t, D a t a, or I :1 forma 

### tio n 40 C . t' . R . §§ 63. 1200 , 

### General. In fo rmation required 

### to 63 . 1C{b) and (c ) docu ment a nd m a in ta in compl ia nce totith 

### the re gul ations of Subpa rt EEE , i nclu din g data recorded b y CMSs , an d 

### copies 

### of all notifications, reports , p l ans, anci 

### other docu me n ts submitted to the**~.dministrator .**  4Q C,f.'_..; "".**·m~~-O-li opar~tion**  

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### c.r . R. If the P erm ittee elects 

### to comply § 63.1206 (b ) (1) 

### {ii) w ith all applicable re q ui**rerr ents**  

### and s t a n dards p romt;lgat ed under authority 

### of t he Clean 

### Air 1\c t , includin g Se ct io ns 11 2 ar. d 129 , in 

### lieu of the '



### V E S012298Veo lia Environmental SerJices**~ermit** tJo.: v-IL-17163001.03

- oe - Ol !?age : 1 04 of 17 6 hours of the initial survey, cond uct a t e st using EPA Refe r ence Method 9 <see 40 c . F.R . par t 6 0 , append i x A)
. (a) 

### If any of the visible em i ssions observations i ndicate visib l e em i ssions gr eater t h an 20t opacity, the 

### Permittee shall con d u ct 

### Hethod 9 vi s i ble emissio n s observations of the emission point in qu esti on for thirty 

### minutes each day, 

### until two consecutive daily 

### observations indicate v isib le emissions of 20% o p acity or less. (b )I f the M e t hod 9 v is ible emissions observation or if 

### -cwo consecut iv e daily observations i ndi cate visible emiss i ons of 20 % opacity or l ess , t h e Perm itt ee shall conduct >reek l y visib l e e mi ssions ohservations of t he e r: dssio n point for three add it . i onal v1eeks . (E) Recordkeep ing an d Reporting [40 C.F.R. § 71 . 6(a) (3 ) ) 

### 1. The Permittee shall ma i ntain r e co r ds of the total numb e r of d r um s crushed ( d rums / h o"r 

### a n d dru m s/ y ear) :or the drum cr us he r , pursuant to 40 C . F . R . § 7 1 . 6 (a) (i) (3) ( Bl : 2 . 

### The l?erroitt ee sha ll calculate 

### and keep r eco r ds 

### of VOM emi ssions fr om 

### the d r um c rusher based 

### on the 

### emiss ion factor eq u al to 9 

### 9 n4 lb VOM/1 drum c r ushed. This emissio n factor is based on the conse r vat i ve assumption that only meth anol res idue ( •,;it h the highest vapor pressure) is released from the 

### cru shed drums . 3 . 

### The Permittee s hall ma int ain the fo l low i ng r ecords of t he fugi t ive emission s : { 4 0 CFR § 7L6(a ) (3) (i) ( 8) 

### J (a)**:: ~etails**  of. each visua l su.r;rey o r visi ble emissi o ns**obse ~vati** **on,** including date , t i me,**obser~er** and 

### r es ult s for each em is sion unit a n d any other pollutant emitting activ i ty ; (b)Date, time a nd type of a ny invest i ga ti on conduct e d ; 

### u,ou< tt.S 

### descr ib<'tl 

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## V

ES01 2299