:.,. •• ··::··. '·" ~ ...... , . .... · . •• ;~ ·. ,:· . ...... .. • •• .. . ................ ; . ... . .... ·1 . . ...... .. .~.. •• (. • •• ... . . . .. . ·! •. -·~· ..... 

TAG: PD'.l' 

'l'WI INS'l'RlJMlmT CALl.BIU\TION RliCORD 

WIT t4 

OUARTBR.LY 

:t>''<\. • • • LOOP : 

1 :; ···1 OE~CRI """ • 4-40 

f , ' "''' IOVI'f ~ DP TP.AKS MANUl'ACT: 

.MODEL: 

FOXl30RO 

823 DPI . Srunr'! CB: : BAGHOOSB PRHS.Siln 

LOCATION: WAPC 

LI?-SRT.: 

P.UD: 

RXMAA.KS: 

I DISTL-IUIKS : 

SPEIC-Rri!XS: 

S/N: 

437 

l'Ol? 

1'1/GAS CLEANING TRAIN 

NORTR/CBNTRAL MGBOUSll 

SCAT..B: 

CALI!!• IN: 

OU.IB-OOT: 

PROCESS-SP: 

INST-SP: 

ACTlON: 

I /0 NUMBER: 

CAI.TBQT IQN NQTBS 

0-15" NC 

4-20 JoiAQC 

USE PmroMltTIC CALISAATION BENCH WITH li!1\HOMBTBR lillD LOOP 

ClU.nmATOR. INl'll'l' PliBUMATIC SIGNAL AND RBlU> OUTPUT liTrH 

LOOP ~IBRATOR. 

See !'<l<mufacturea literature for detailed instructions. 

Fill out and aflix a new cal i bration s t icker. 0 . 1 lb/hr 

CJ.f,IBAATION RRPORT 

.~~~-- .. ·~-·· .. -·---~- ·-.. --·-··-·-------·-·--··-···· .... ~--...... ,_,_ .... ---.... ·---·------·- ···· ...... -..... , ___ ,._,_, ___ ,~_ .. -................ ~. 

(:"'"·\. INP17I' V1lJ,lffl . INSTRIJMENT R_E1\DIN'G . 

. · 1'1 Bafore Cal.ibratio.o •? 9 9 /?!4 

Mt:er Ca.libratJon 

Comment s: 

f.~· . .. ... 

Performed by:---t,//a=..c..!.IC:c..L~4!:C:k......L,h::..:..;.;'J:Yf=---- Date: fi-/J.-oJ Tittle: fl." 10 {!;PM 

JB . 

CAl.S!mBT. WDB 

Place: ____ ~~~--~ ~---- (Field or Sbop) 

1;: 

r .. 

I. 

··+ 

VES012100 
..........• ... ... . .... ': : .... . ;···· " .. : :· ........ .. ....... ! l . . • - ·· 

'.l.'iU INS~' CALllllUl'l'ION RI!CORD 

UNlT #4. 

QUllk'.1'"'RL1C 

'tAG : l?D'l' 

?f. •. ,:_·. LOoP: 443. 

' ···. · ':' DBSCRIPON; DP 'l'lll\NS 

. . SERVICE: BAGHOU$B PRES SUER 

LOCATION: I'IAPC' 

LP·SIIT: 437 

P&ID: FO ? 

RJll.11\RKS: W/GAS CLBAN'ING TRAIN 

INSTL· RMKS : · NOR'I'H/IVES'I' BAGH0t1SE 

SPBC-I!MK'S: 

S( N: 

MA'NUBAC'l': FOXBORO 

MODliL: 823 DPI 

SCALE: 

C'..ALIB-IN: 0 - l.S" liC 

CALIB·Otrr: 4·20 ~!1\DC 

PROCSSSCSP: 

INST-SI?: 

ACTION; 

I/0 NllMBER: 

USB P.NIWMllTIC CAl.!BRAT I ON BENCH WITH MANOHE'l'BR AND LOOP 

CALIBRATOR. llfe>UT PNEUMATIC SIGNAL . AND READ OUT.PI1l' vii TB 

·LOOP CAL:CBR.A'l'OR. . 

See Manufactures literature f.or detailed instructions. Fill out and affik a new cal ibration Bti~~er. 

0.~ l b/hr 

CAIJBRATIDN !m!?ORT 

...... ...... 

I. 

., ........ ___________________ , ................. ______ .•..•..... \ I NPIJT V1\WB ------·--- .. ---U'iS:iiiJMENTREAi')iii'G·····---··---·····---· 

Before Cal ibration fl. tJ s/&.4 

!C'uc ,/9. 12 M/4 

M ter Cal:l.brat::!on 

CALIBRATXQR SOURCS PBfBRBNCB 

' t 

PerfoiUied by: ___,/la q.<2i&<~<:~~--"<"l~''---.k.f.6.,;· ..., ' ,._..____ Date :f/ ~ [ l - II r Time: 2 _? O(!j til liM 

~ 

:) JB 

CALSBI\BT. woa 

Place: ____ ~~~--~=-~---- (Field or Shop) 

l 

I 

! 

VES012101 
TAG: 

<!"~.- LOOP : 

:. ·· ·. ·1· DS:SCIU!'Oii: . . SB.RV!CE: 

LOCATION: 

X.P-SRT: 

PO:l O: 

REMA:RXS: Il~S'l'L- Rl1.KS: 

SJ?aC-RMJI:S : 

S/N: 

. ... h.: .. 

TWI INS"l'RI>MltNT CALr£SRATION RECORD 

UNI'X .lf:4 

QIJAR:rERLY 

PD'.l' 

442 

DP TRANS 

BAGBOUSB .I?RESSUER 

NAI?C 

437 

~'017 

Vl/GAS CLEANING TRAIN 

SOUTH/EAST BAG!fOUSB 

f.llUJUE'~C'l': FOXBORO 

loiOO!lf.: 823 Dl'l 

SCALE : CliLlB IN: o- 1s• we 

CALIB- OOT : 4··20 Ml\DC 

PROCJiSS - SI?' 

IN9T- SI?: 

ACTIOO: 

I/0 NUHBSR: 

Q I ,IJmATION NOTBS 

USE PMBUMATIC CALIBRATION BE!'ICS WITH MA.."l0MJ3Tti1R A1llD LOOP 

ClU.IBRATOJL INPUT PNEUMATIC SIGNAL AND RRAD Otl'l'PUT WITH 

LOOP CALIBRATOR. 

See ~factu es literat ure for detailed instructions. 

Fil l out and aff~ a new cal ibration sticker . 0.1 lb/hr 

Cr.TJ'BRA'J'ION R§QR'J: 

·-.,: •:;~,:,..-----~---- -- ..... --.... , ____ .... ____ ., _ .......... -·--··--·--·--·---·------·--- ---·--·--·-- -·-··- ;' · _., . INror VlWm INST.ltOMimT Rl!ADING 

. Before calibratiOIJ d. of .114 

If-· ?2. /v· J<j /?/A 

After CaLibration 

comments: 

II 

Performed by: ~lla~e~/~a"""-c_-'-...,k""'-'''-'t /?2 '-'-'--- Date.,{- U.- ~ 9 Time: ,'i: d 0 ~ PM. 

JB 

CALS.BBET. WOB 

l'lace: __ ~-=~~--~~~---­ {Field or Sb.op) 

... 

i: 

I 

-+ 

I ,. 

VES012102 
,. . ··- .... • ' 

't'I>..G: 

f. --0!. LOOP: 

.; ' :.: UBSCRIPON:' 

SI!RVICB: 

LOCATION: 

LP·SBT: 

P&ID: 

RE!11;RltS ; 

INS'I'L- l!MXS: 

SPEC· JU.IKS : 

S(N: 

. .. . ·-···· ..... . .. , . .. .. . . ·-·"' ..... · 

T'III INSTRU11I!l(l' C'1Llllrull'IOU izllrulil) 

UNIT ~~~ 

QOAR.'!'Hll..LY 

PDT 

443 

DP T.RAW 

BAG!iO'OSB PRESSUER 

WiU>C 

43 '/ 

P017 

14/ GII.S ~ 'J:RAIN 

SOUTH/Cl!N'l'RAL llAGBOOSB 

l4ANUFAC1': FOXB<mo 

l'IODln.: 823 DPI 

SCALl!: 

CALIB- IN: O-l.S• we 

CALlS-OUT: 4·20 11ADC 

Pll.ocBSS- SP: 

INST- SP: 

ACTION: 

I/0 NUMBB'R: 

Qllfo.:P3RATXON NOTBS 

USB PIIROMATlC CALIBRATION BBNCH i'IITH MANOMETJ!R AND LOOP 

CAL:D3RATOR. Illi?ll'l' PN13UMJ\TIC SlGWU. AND READ OUTPUT WIT!{ 

I.OOP CAL!llllATOR. 

! 

See Manufactures literature for detailed i nstructions. 

Fil l out and affix a ne'll calil>rat;i.on st:lcmr. 

0 .1 lb/h.1: 

After Calibration 

eo.tmente: 

... 

:, 

( .. 

l. 

:· 

' i 

I. 

Performed by:-f/lo;.LU;e~L,o.e:::C:.._....L f<:...,·,'-L m!!-_..:... Date : /1-(l~O? Time:.fl..• t7J ~PI~ 

Place: ____ ~~~--~~~---- (Field ar Shop) 

JB 

CALSRBET. WDB 

VES012103 
.. ·· ..... · ........... '.~· . .. .. . . . .. . . .. ..... .. . ' 

'.f.'WI INS'l'ROMEN'l' CAf,IBil.Al'IOlT ll.J«::RD 

UNI'1' ff4 

QUI'.R.TERLY 

TAG: G'"~~ , LOOP: 

t i 

PD'l' 

444 

' · OE!lCRIPON: 

· SBRVI CE: 

LOO.'l'l: ON: 

LI>-SHT: 

I>&lD: 

REMARKS : 

lNSTL-RMKS: 

SPEC-IU1lCS: 

S/N:· 

DP 'l,'RANS 

B~HOUSH PRESSOER 

WAPC 

437 

F0l 7 

W/GAS CLEAJI!N3 'l'AAIN 

SOUTB/HES'l' BAGBOUSB 

l\!liNUFIICI': 

NODRL: 

SCALE: 

CALJB-IN: 

CALIB· OU'l': 

PROCESS- SP: 

D!ST- SP: 

ACTION: 

I I 0 NIJMBER.: 

CAAIBR!IT;roN NQTBS 

FOXBORO 

823 DPl 

0- 1s• we 

4 - 20 ~IAOC 

US!i: PNEUMATIC CALIBRATION f!ENCll l'IITH MANOII'.aTBR AND LOOP 

CALIBRATOR . INPUT I.'NBOMATIC SIQNAf, AND READ OO'!'I?UT WI TH 

LOOP CALIBRATOR . 

See Manufactures literature .for detailed instructions . Fill out and affix a ne>r cali.bratioo sticker. · · 0.1 lb/hr 

f'AI.TBJ?)\'fTOB REPORT 

-r~---- --;.mro.r~mi·-·--- .. -- -·-----·---·------·------~ _____ ,,,_, ___ .. ____ ,.. ,, ..... .. ~ ... . 

---.J..£~- --Bef,_ore Calibrati012 ? J?,t~ ..1!A_ 

I .[fl t.J G /'l. .f? a iJ. 

After calibration 

? O,o I ,m,4 

eooments : 

Performed by: /lc:;u:tJ"e.~L='u"''.L-!::..--f.}1!..i.J lt2z?:L- Date: ll-/2 ·09 Time: £.'30 6j1 PM 

J13 . 

CALSlmBT. WDB 

Place: ____ ~~--~~~---- (Fie_ld or Stwp) 

I'' ,. 

:· .. 

VESOI2104 
0 0 0 4 0 OOooM • ·~ -! , ... 0 

. ' . OO·+OHo o• ... 0 00 0 0 0 o 00 • OOOo ... -.. .... : 

.. 

TAG: (4IT 

'I"'II I.lv<;TRI)M((II'f r::JU.:J:.uRAT.iON RBClOIID 

UNl:T i4 

(.ltJ.Il.R:l'.WU. y 

,a · .. .:·;. LOOP: 001 

~: •· :. 1 DBSCRIPON: WT 'l'RJINS 

SERVlClil : SHRlWDBD SOLIDS 

I.OCA'nON: Fl'RNSP 

LP-SYT: 1 PUD~ POll 

RE!'II\Rll'S: W/SOLIDS lmiiD S'!STBM 

lNSn.-RMKS: 

S.PBC- RM!tS: 

S/N: Bl2o65900A 

1-tANUFllCT: TOLEOO 

XODJU,: 8140 

SCALB: 0-3000# 

CALtB- IN: 0-3000# 

. CIU.IS· OUT: 4·20 I!:ADC 

PROCRSS-SP: 

INS'I'-SP: 

Ac:rrON: 

I/0 tiUMBRR: _m:S 

CALJ2RATJON N0Taa 

Cheak seale,.digital Calib~ation per. Tole~o instructions. 

Then dth no weig'ht on sca.le adjust analog zero. (NOTB: BIU 

>lill not display numbers lees than zero) . Next add weight .. to lOt are tnare of scales range, then adj ust ana.log span, 

to indicate weigbt on scale, as reed on BMI screeo. 

See ~ufactures literature for detailed instructions. 

Fill out and affix a new calibration sticker. 

' . .. 

,, ' 

j. 

CALD3RATIOH BEPORT i· \---- ·,· .. ·---·····--·-- ---·-----l:i Sii'tiMmtt-RiiiDll!IG- ·------·-.. -.......... _ ... __ _ 

0.1 lb/b~ 

· · O Before C!llibrat:i_on- - ---::=0=------ --

q~Q ____ ~9=~~--~

After Ca.libratjon 

COJllll\ent s : 

Per f ormed by:-~= 

.. rt, ~~ ( ">~ 

JB 

CALSHEBl'. WDB 

R 

Place•-- ~7.7.~~ ~-- ---- 5rShopl 

VESOI2105 
... .. .... ~· ···· --~! • •' •'•'' ' •• ' •• I • • ' • •....... _ ........ : .. ·· ... . 

Tl\G: WIT 

'J:!1Il INS'l"RUMEN:!' CALIBRAX.ION RECOlW 

1lbl !"l' #4. 

QOARnnu:;t 

M~ ' LOOP: 1A 

: ' '. DBSCR.ll'OJJ: WT TRANS ~~UF CT : TOLlllOO 

I SERVICB: DROM lr!!BD ~lODEl'· : 814 0 

LOCATIOll: P'l'RNSP 

LP-BBT: 

l?&ID: 

REMARKS~ W/OIUJM PBED NEMA'l'RDN 

INSTL- RMKS: 

SPEC- RMKS: 

S/N: 4~601574NS 

SeAL¥: 0-1,000 lb. 

CALIB-IM: 0-1,000 lb. CAI.lB- OUi: 4 -20 I<IAOC 

PROCBSS- SP: 

IliST- SP: 

ACTIO!l: 

I/O NUMSBil.: Nl:35 

CAI,IRRATIQKJ!TM.,W! 

Check scale, digit01l Calibr r>tion per. 'I'oledo innt:ructio na . Tl;len with no weight on scale adjust analog zero. (NOT8: H!ol! 

will noc display I!Ulllbers less t.ban :.:ero) . ~ext &dd weight - to lOt are 1110re of scales rauge, thaD adjust analog span, 

to indicate weight on s\Al1e. as read on B!o!l IIC:rOQJl. 

See Mwlufactures l iterature for detailed instructioniL 

.Pill out and affix a new calibration stiCker. 

0 .1 l _b/hr 

~I.IRBATION RBPORT 

"#""~·--- ----·---------

' : . ; IliPOT VJILUB ·----·---I NSTR'ONM · RiiADoo ·---·-·--........ 

.. 0 

5P 

Before Calibra~!an l) __ _..:::so:...___

Mu.r Cal.ibrat!on 

QLWztTlOH £Q1'1PCB BRlmRNC;B 

Comments: 

""~"" ( . Perfomed by: 6.1 :c f.u e 00 . : . JB 

CALSHBET. WI>B 

1 

-Place: __ -T~~~~--~~~---- 0§ or Sbop) 

j 

., 

;· 

i' 

I 

' • 

. • 

. • 

' 

'· 

VESOJ2106 
' .. . 'I . ... "'' "'· ··-~·:·· " .... 

'1'10 INS'J:I!D!IQDIT CALI!!!U>ttON RRCORD 

IJNlT #'1 

QUliRTBRLr 

l 'liG: 

.·· .,.;;·. LOOP: 

'. :,··. DSSC!UPON: 

Wtl' 

014B 

1'11' TRANS MA1!I1FAC'l' : TOLEDO 

MOD!!!.: 8140 

SCALJ!: 0~2001t 

CALIB-tN: 0-200# 

CJU.IB-011l': 4 - ~0 l4!UJC 

I?ROCBSS-SP: 

'I 

SBRVICE: JlOX • DROM FRED 

LOCATION: FTRNSI? 

LE'-Sii'r: 

PI<ID: 

REI-lARKS : NEI'I AIJX DRUI'I ll'BED 

XNSTL-RMXS: 'INST-SP: 

SI?BC-RMKS: ACTtOll': 

S/N: I/0 NOMBJ!Il.: 

CJ\loXBBUION NQl'IS 

Check scale, digital Calibration per. Toledo i.cstructions . Then with no weight on s:cale adjll!lt' aaalog zero. (NOTB: IU4I 

~ll not diEplay nurnl>ers l11ss tban :cero) .. Next ada weight = to 10t are mor e of scales ~ga , then adjust analog span, 

to indicate weight on scala, aa read on BMI screen. 

See Manufactures literature tor detailed inotructions. 

l'i.'l.l ouc and. at fix a new calibration sticker. 

O.J. lb/hr 

pr.xpp:aTIOlf )lBpoRT 

l&SlRUllBN't' llHADlNG 

l!ofore Cal.ibraeion 0 

Mt:er Ca.libr.:1.cian 

Commants: 

Performed by: 

JB 

CALBBE!rt' • WDB 

Place: ____ ,~~~~T--=~~---- ~rShop) 

~ 

,, 

(: 

I 

!-

I. 

'· 

,. 

I. 

r 

VES012107 
...... . • ,, ••. I • ' . • ' ' • ' . • ' " ·•• . , ., . .. ·. , _.' .. N .... ·.: .... ,,,.. . :-

•t•AG: 

t:! ~~ WOtJ : 

! .\ Ol!SCRIPON: 

,Sl!RVICB: 

LOCATION: 

LP- SH'l': 

l?&ID: 

. ~KS: 

INS'I'L-RM!CS: 

SPEC-.RMlS: 

S/N: 

55()A 

Tribe 

'1'lii Il'il:>"TRUMBrfT CliLl:lmhTIW R1!CORl:J 

tmtt f/4 

QUIUI.Tma.Y 

eaghoutle Leak Dcteccion 

F'LD 

wuroFAC"T: Aupurn 

MODBL: 't!H1!0 .dgd 

SCALI!: 0-lOOOpa 

CALIB-Il'T: 0-1000pa CALIB-OUT: 4-20ma 

PROClliSS-SP: 

INS'l'- SP: 

ACTIO'!!': 

1/0 lAA!BBR: 

l:,&;pw !1'!'TON NOTRS 

Disconnect the input cable a t the. BNC connector on the ioput 

card, and cheok. for zero. use Aubuzn, Triboflow, filed test 

unit, model 2902, to input a Pico-Amp slgna~ of 500pa CUUJ 

record these values . 

0.1 lb/hr 

CMJB!!ATION !l.Bl!OR.T 

. ·~· 

'~ 

' ' 

,. 

I 

I 

.. 

' ,, 

I , 

I 

r. 

~~.~------------------· ~~---------

• IHPilT VALOB Before Calibration 

0 · -T ------~~~ ------- 5"00 fA. 

Afcer Callbracion 

CALTBRJlTI()}( SOURCJl RRF"&!litJcB 

r" '!' ... ) .; . :' JB 

CALSHBET • WDB 

VES012108 
.. . . . . . .. . ··· ... ... .. . .... .. 

,, 

~- /~4 (IC4034) PAGE 1 OF 1 ~ 

. · ~tJAR'l'E.'a.Y CARBON INJECl'IO.~ .PREVEN'!'IVJ:: MAJliTENANCJi: CltF.CK SHEE"f • ::;;::: : t:.: :.: :.::.:: :::;::: :.:..--:·:;::.: :: ~ :: ;: : :-:::::: :::.: :.:.:: :;:: :::::;::: ::-: :-:::::-.: :~::.:: ; :-:;:::: :.:'::::s :-; :::: ;;: ~ :; ::: :;;..;;: :::: :r ::-:;:-::-:::: :: ::: ::: : 

1 Disconnect AC Power to the Digi Dri~re. 

2 Inspect AC & Motor drive screw terminal connections for 

signs of wear or corrosion and check that they. are tight. 

3 Replace the two Digi Drive fuses 

4 VerifY any external safety switches or lockouts are-b1:ill operation 

5 Remove Screw fccqer cover & blow out C1lt'l:5on & dust. 

6 Inspect Gears & Belts Cor wear or damage. 

7 check Operation of. Motor & <.!ears for abnormal noise or movement. 

rASS FAlL 

I 

, I 

/ 

I 

I 

I 

J 

' 

I 

co~~S~·~------------------------------------------------

.... -

. ' 

Name: J'Kc'l?.4 

QtlARTER.i 

11/1{06 KF 

Date :/!- lf-rl 7 Time: 3 ~ ~ (3 AM 

I· 

VES012109 
•

~· j •• •• , ; . : 

.. ~ I! .. ' 

'( · .. ... ·' 

TAI;f: FT 

TWI INSTRUMllNT CALIBRATION ltl«XmD 

UN!'!' t-4-

ANI!IUAL 

LOOP: 129 

O!!!SC.RXPOM: li'J.OW T.AA..'Ii!S MANU!?ACT: MIC.l{Q MO'riON 

to!Otll!L: OSlOOS :L2!l 

SCAJ.Jil: 

S!lRVIO: PCC LOW GRADEl I! OS X··1 0 

LOCATimf: 1?-.B/>IS 

LP SIIT~ 1:19 

I?&DJ: P013 

R~: W/BMS 

CA4IB-IN: 0-7,000 #/aR 

CALIB-ODT: 4 - 20 ~DC 

PROC&SS- SP: 

n.'STL-RJoiKS: INST-81?: 

l\CTION: 

1/0 NUMBE3t: 

SPBC- RMKS: 

S/N: 101499 

C!T.TBRATI~ 

FLush process piping, coonact water hose to upstream side of 

flow meter. set control aystem to <~ppropriate rate control, 

and read totali~er, flow water into a cont niner and ce«pare the toltalizez: reading to the measured amount in container. 

See Manufactures literature tor detail ed instructions. 

Fill out and affix a aew cal:i.bration sticker. 

e .1 1:9/b,; 10 ~ 

Cl\LIBllAT!ON I"I,EI?QRT 

INPift VALUI< -- - ·----.--.. --.~~-----.. ·-··--

l

r \b.. " IB~.~r_e calibrati on 1.,,_, lb~ .::> • s. (?eC min . ;or . ., " _-, ~ ~ 

A.teer Calibration 

Cotmlonts: 

Performed by: -'6~~~/b~~O~ -- Date:l2.-%'-09 Time: 2,.'00 AM@) 

JB 

CA.T.SHBET. WDB 

I 

Place: _____ ~~~~--~--~--- ao• Sllop) . 

! 

~ 

i 

li 

,, 

i; 

~ i 

.. 

I 

! : 

;: 

l 

!· 

! 

I! 1· 

VES012110 
..... ···· .,4··: .. . .. ," 

'rAG: Fl' 

................. ·...... . . ;• ... ..... ···-··. .·: . . . 

1.'91! IN.STIUJME!lT CAToiBRl\~'LON lll<CORP 

UNU f .4 

.ANNmiL 

.. . . .. . ... 

•.• :'\- . LOOl.': 1<\5 • OBSCRIPON: PLO'II TRANS 

Sli'RV.[CB: f/CC SLUPG!f .lC · 12 

LOCATION: P -BMS 

Ml\NOPll.cr: MICRO MO'!'IOll 

D~L: DLlOOS-SS 

SCI<LB: 

I.P-S!:!T: 1.45 

P&ID: 9013 

REMA!!.KS: W/llMS 

INSTI,-RMICS: 

Sl'SC-RMKS: 

S/N: 1.03056 

CALIB- IN: 0-8,000 #/!lk CALIB-~r: 4 · 20 ~~ 

PROCESS-SP: 

NST-~11?: 

ACTION: 

I/O Nm'.BBR: N1 : 28 

W ·T»BAUOl{ NQTRS 

Flush process p i ping, conr.tect wate .r hose to upstream s:ide oc 

flow meter. set control aystetn to appropriate rata control, 

and read totalizer, flo-~ water into a container and compare 

t1u! toltall.zer ;r~g to the meauured an:ou.ot in cont:ai oar. 

CMJBJ?WQN RBPORT 

.. -., ------==~ INPUT VliLUB -:-:~ ----·-. ----- INS~RXiUl:tBG =~--· 

, ll _ · f' ,.. Be Core Cal.ibr<~ tion 9 /i / lbs . IDes- pee m in 'n7r J n-ln, _ -

A~ter Calibration 

Ci!okrnRA.TIQH SO!ll!CR Jil!'f1llRRNCR 

... .. 

L 

r 

!: 

i 

r 

I 

Performed by:¥£. /DO 7 

Date: i 2,8..-0 't 'rime: '-/: 00 AM' 6J 

JB 

CALSHEBT . 'IDII 

Flace: ___ ~~~~----------- t§or Shop) 

VES012lll 
............ '::.:: ....... :..~ ·:·; , ....... ·. .... . ........ . ...... :: .. .. .. .. ... ..... . ... . , .... -... ~ ' · 

'lWI 

TAG : liT 

LOOP: 212 

Dl<SCR.TPON: l"WW 1'RANS 

SERVICE: IIDP TO X'-22 

LOCATION : S-BMS 

LP·SHT: 412 

P&ID: l!'Ol4 

REMARKS: ~1/.EIMS 

lNSTL-BMICS: 

SPEC-liNKS: 

S/N: 101 775 

INSTR~ 0\LIBRATION llllCORt>· 

UNI'l' #4 

A.NWAl. 

~.AtllJli'ACT: loiiCRO I•'IOI'ION 

~IODB[,: Dl.J)()O.S • 88 

SCAli&: 

CALIB- IN: 0- 7,000 #/Ra 

CALLB-OO'P: 4-20 M1IDC 

PROCllSS-SP: 

INS'l'-.SP: 

ACTioN: 

I/0 NUMBSR: 

QT.IBilATI()N NgfRS 

l!'lush procQ99 piping, connect water hose to upstraam side of 

flow meter. set control syst em to appl:'oprlate rate control, 

and read totalizer, flow waeer into n c:ontai.ner llt!d COlliJ>&r9 

the toltalizer re&ding to the meaeured amount in container. 

See r~uu.faotures literature for detailec1 in.structiOJW. Pill out and af~ix a new catibxation sticker. 4.-:L J,bfhr /090 

ALter ~libra ion 

ct\LIBRlJimt fiOTZRCE RBPIPB'NCE 

..... 

Perfol:l\led by:..,.b.J..J..~~b~b~O _ _ __ oate: ll,-C1-0j 'l'iroe: 4:0o AI@ 

JB 

CALSl!BBT. WDB 

7 

Place= ---- ~~~~----------­ (3orSbopJ 

I. 

., 

t 

' 

1-

I 

I 

I 

VESOI2112 
··~ ...... ... ......... · ••' 1 •• 

TAG : I.'T 

. ....... --· 

'IW:l INSTROMKN'£ Cl\J,UIRA'1"!0N RBOOIU> 

UN11' 11'4 

~ .·$ WOP: l.l8 : . ·:· · l>l!SCRIPON: ,FLOW 'l'lWi'S MA!iU£1'1\CT: MlCR.O MOTION 

~!ODEI.: Dl.OOS·IIY 

SCI\LB: 

. SeRVICll: PCC AQ LI.Q X·ll 

I.0CATION: 1?-lll'!S 

LP-SB'l': 138 

l?&ID: F013 

REMARKS: W/BMS 

INSTr.-R!IIXS: 

SPBC- RMP:S: 

9/}1: U.55343 

CALill- IN: 0·6,000 1#/IIR 

CJILIB- 001'; 4-20 MADC 

l'ROCBSS· SP: 

INS'l'- SP: 

ACTION: 

l/0 NtJMBi!R: 

C"lUJR)lA'fiQM AVfSS 

l!'lUSh proo'ess piping-, connect v.ater hose to upst.ream Bide Of 

flo•" met er. set cont rol system to appropriate rate control, 

and read tot alizer, flow ;qater into a container and compare 

the t.oltali z&· readi.og to t~ measured amount in container. 

Sea Manufactures literature for deta ~ed instructions. 

Fill out: and affi x a nev ealibratioil sticker. ·-Q...l . .li;/ b.::: !D'?o · 

CALTBRJ\XlOlf RBt>ORT 

.. 

I 

"T· IKPOT VJ~i:i:'ii-------- -- INS'tRt+ISN'r"lmADlNG-·-··-··-----... --·-

1 . r J Be{ore Calibration J" <:! J' _ S' lhs. p~~: r- C?o n ')Or m so . ___ . ...!.,..! ' .:.. ·· ~ 0.!>:::::..:. • _ _ _ _ 

After Calibration 

Perfox:m.ed :oy: ~ri) ~¥-;D-"·"'-v;;:.... _ _ _ __ Date :\H {)OJ Time: ..lE.Q.Q.@)M 

J8 

CAI.SHBBT. WDB 

Place: ____ ~~~--~--~-- 18 or SbopJ 

VES0121 13 
• ' •••• · · · -:.· •• J ..... ···-· .. . . 

TAG: ~~; . LOOP: r ::\ DKSCR!I?ON: 

SBRVICB : 

LOCA.TION: 

'1.'1:0: lNSl'RIJMI!N'l' CAJ,mRJ\:l'ION RMCORP 

wn· #4 

TT 

31'/A 

'rc .ASS!!.l1BLB 

sec OUTLET 

nn 

317 

1'0:1.5 

ANNUAL 

MAN!JFAC'r: 

MODBL: 

SCALR: 

CALXB-tN: 

CJ\LIB- 01)''1': 

CllBSSBu 

35:1.0 

type R TC 

0-300,0 1." . 

. . ... 

LP-SJlT; 

PUD > 

Rlll'IAlUr.S : 

!tiSTL- RMXS : 

PROCBSS- SP: 

4 - 2 0 MADC 

.?.4• INCONEL 601 l'fSLL 

SPEC- 1:<.\IKS: 

S/t'f: 

WS'J'- S P : 

ACTION: 

!/0 NUM!!Bll.: 

Qr:rnpl!TtQl!' NcrJ'BS 

N:l.; 51 

use cold junction compensated therroocouple calibrator to 

i nput a .caqpe.re.turo signal. o f 500 deg F. lllld 2, 000 deg. F. at 

input of transmi~cer; t:hen verify tll:l.s llingl.e in ¢ontrol 

room. . . . 

Sea Manufactures literatu.."'9 for detailed i nstructions. 

Pi l l out and affL"f ll new calibration st:icker. ~ .l: lb/ict 

Comments: 

Cl!Lil!BA,TIOO JW>OI!T 

After Calibration 

0\LTDRDT'IOK SOJJRCB HR}!RimNCB 

Plaoe' ---- ~~--~~~---­ lii'ield or Shop) 

'• 

' 

' ' 

r 

VES012114 
····i :. ~_._.,_....... ...... .. . . • .... ~.· "-·--·· ' ' . ' ................ ,., ... 

TAG: 

LOOP : 

JJESCRIPO!i : 

SlmVtCE: 

l:..OCATION: 

LI'- SHT·: 

l'&ll): 

REt.O\R..KS : 

INSTL- RMlC$ : 

SPRC- RM!CS: 

S/N: 

'1'W"l INS'In1l!l!llNT C/ILI'BRAl'ION RRCORD 

1J1\lrl' #4 

TT 

31./B • 

'l'C ASSEMllLB 

sec oUTT,lrl' 

l!W 

317 

FO:tS 

ANNolu. 

1'C l'IRLI. I NCONSL 601 2 4" 

t>lll.NWACT: CIIRGSRL 

t•lOOilL: 3510 

llC'..ALl'!": 'l'ype It TC 

CALIB- tN: 0-3000 F. 

CALIB- OO'l': 4-20 MADe 

PR.OCBSS-SP : 21" IliOJNEL 

I NST- 81' : 

ACT'!ON: • 

I /0 NllO'IBSR: .111:52 

CAI,IBBATIOK N£YrES 

601 WELL 

Use cold j unction compensated ·tbe=couple calibrator to 

i nput e. temperat:ux:e signal of 500 d.eg P.. and 2, 000 <ie<J. P. at 

i.nput of transndtter, th= ve rify t his singl e in cont r ol 

room. 

See rv-.anutactures l iterature for dAI:a.iled inst r uctiotls. 

Elill out and affix a ue"' c al:ibration s ticr..er. · . ...o.a l h/hr 

CALlJIRA-TION' RRPQRT 

I r: 

i· ! 

; 

-······-----1 

2 WD 

A£~ CalibratJ.o.n 

Coawents: 

w 0/JI~ , 

Perfotme!=l by: ____ ___ ___ Dat e : lt z-o?'Ti~re: /.'1'7 »t@ ! 

[. JB 

CALSRSST. HDB 

R 

Place '----;~[7.::-:-:-i~--:::---.--­ ~or Sbop) 

VES012115 
TAG: TT 

··· ····· .. ••••• • •• •• • \,. ....... ! ; 

'IWI :nll>'l'IWMBN'l' Cl\LIBI21\.'i'!ON Rt!OORD 

UN11' t!4 

l\NNUAL 

~:"_i. LOOP: ·lOSA 

~ :· '.: DBSCRIPON: · Pn£X·IE1'ER 

SERVICR: ltiLN OU'l'LB'r 

LOCllTION: B'l..O · 

LP-SHT: 305 

IA!IUFACT: J.2CO])( . 

·;o· \: :...; ·' · 

P&ID: POlS 

REMARKS : 44•99-F-1 - 0-l 

INSTL- RMXB: 55" Target. 'l'ulJa 

SI?EC-RMKS: 

S/N: 

l40DBr, , ~lODLINB4 44- 99- l'- l - 0-l 

SCALE : Type R TC 

CALIB-IN: 0•3,000 deg F ~IB OOT: 4- 20 MADC 

PNDCESS- SP: &~IS. BS~ 

INST-91?: 

AC'l'ION: 

I/0 1~: Nl:Sl 

Cl!J.J'l!RliTIOfl NOTES 

Install factory calibrated Py+ometer. 

see aoufaccures l!tera~ure for detailed instruccion8. 

Yill out and affix a ~ew calibration stiCker. 0 .1 lb/hr . 

INPU'l' VALIJB-·---.. -----·--- INSTRllMBNl' RBADING 

Betore Calibration 

CormleJltS : 

Performed by: ___________ Da.te : _ ___ Time: JIM PM 

JB . CALSHEET. WDB 

s 

Place: ___ ~~ -~~~~- (Fiel.d or Shop) · 

f; 

~.~ 

' i 

I 

:· 

I 

! 

' f 

VES012116 
··· ·:~-··:.:; ,., • .,.. • • •: • ,,,.,.,,. ' ''.• ........ ,. •• >~ ) ' "' ,,. ,• •'I ' ••••"- •• •. ' '... . ... .u .... •• 

"l'IU D ISn«JMUNT CAL.IBI!A'l'toN RllCORD . UNIT#~ 

TAG: '1"1' 

UlOP : · JO!!B 

DBSCRII?ON: PYROI'Ili'l'b"R. 

SERV'.!CB: l<!LN GU'rt.ET 

LOCII.'l'ION: J.I'LD 

LP-SHT: 305 

P&IO: POlS 

REMARKS : 44·99-P-l- 0-l 

INS'l'lo-RM:f{S: 55" 'l'a:cget Tuba 

SPBC-RMKS: 

9/N : 

J!N!IIJAL . 

MAlrot:ACl' : IRCON 

MODBL: !I!ODLI:NE4. d:'l•·9!H?-l -0-l 

SCJI.t..£1 : Type ~ TC 

CALIB-IN: 0- 3,000 deg P 

CALUI-001': 4 -20 MADC 

l'ROCBSS- SP: lllUS . 85't 

Il'IST·SP : 

ACTION: · I/0 NUMBBR: ~:52 

c;u.Il!M.T.ION NQllli 

Inscall faccoxy c~ibra ed pyrometer. 

See Manufactures l iterature t or detail ed inst ructions. 

Pill out and afftk a ne~ calibration st c~er. 

O.l lb/hr 

pr.WATIQH RBpORT 

I '•. 

~r--·- ·----,-o-·=-=----------· OIPOT Vl\Ltll! lNSIROIOiJI'l'"'READlliiT'---------· .. ; . 

"it;, 

~~:~l . .... 

Befor e C8libratian 

M t:er Ca.librati on 

Comments : bv JJI~ke .. j 

Performed by: ___________________ Date: ______ Time : _______ AM PM 

JQ Place: ____ ~~ ~~---- C1!LSlli!ET .WDB (Field or Sbop) 

s 

VESOI2117 
··-·· ... ·........ . . ' • ,, ... . .... ~.1'1.· •• 

'lWl !NSTROMBNT CALD!ll11:t<J:ON R.IJCD.RD 

UNrr #4 

·fAG~ 

'if· ~· LOOP: ~. DHSClUPON: 

SERVICE: 

LOCATION: 

L'P-SBT: 

P&.ID : 

Tl'· 

404A 

TC l'P.A.'l& • 

'l.'C GAS OIJTIJBT 

WAPC 

404 

!'016 

AlOOJAL . 

~!ANUFACT: MOORl! 

RBMliRl<S: 'il/ GAs CLEANING l"R,AA.N 

MO~: TIY/K2 0-L -~0MA 

SCALE : 0-1500 deg ~ 

CALm-Illl: :l'ype K TC 

CALIB-o!71': 4 - 20 MADe 

PROCBSS-SP: 

INSTL-RMKS: INS'l'-SP: 

SPBC-l!MXS: M!TI ON: 

S/N: I/O .tim!BBR : lil. : 11.4 

Use cold junction compensated thermocouple calibra tor to 

i upu t a temperature aignal of 200 Oeg F. and 1,000 deg.F. at .tu:eut of transl!li.t~er, then varify t h.t.s single i n conc:rol 

room. 

See Manufactures l iterature for detailed instructions. 

FilL out and a!fix a new calibration sticker. 

8.1 lb/ltt 

gLmRATION P'PORT 

-p \ ------:iJiiiiii'-v.u.w------.. ··--------·-.. ·--·-·---~~--

?ooe> Befor e Calibratio:~ ,

200 a. 

·(o00° ~t~o~o~o_0 ________ _ 

COillllents: 

JB 

. CALSl!l!i'T-WDB 

·I 

A£ter Clll.ibn.t.!on 

Place=---- ~~~--~------- r§§Jlr Shop) 

r l;: 

.. 

I 

L 

VES012118 
·. . . ' ................. :... . ~ .. ··'· 

'l'WI lNEr.!'RO!Ilmi'T CALIBRATIOU RBCORD 

UNIT #'1. 

M!Nmlo 

F . ' \ · .. 

'IIIG: 

, . ..;, LOOP: 

{· ·. :; DRSCRlPON: 

'£'T 

4.04B 

'I.'C TRANS MA!WFAC'!' : ~IOORll 

SERVT.CB: 

C.OCATION: 

LP-SBT: 

Po.IP: 

(;!J'IWIR.l(S : 

INSTL~ 'RMKS : 

SPEC-RM!CS: 

S/N: 

TC GAS OtrrLBT 

liAPC 

P016 

W/<IAS CXJ!l\.NUIG 'l'RAIN 

' MODRL: TIY/KJ- -1 -4-~0MA 

SCALE: 500 deg F 

CA!JIJ;-!N: Type K TC 

CALIB-orrr : 4.- 20 MADe 

PROCBSS-SP: 

Il<ST-SP: 

AC'flO.N: 

I/0 N!JMBim.: Nl.: 115 

Use c old junction cornvene ated tll.et1110Couple cal i brat ox: to 

input a temperature sJ.goo.l. of 2 00 des F . aud 1, ooo deg.F. at 

input of trant:m.itter, tll.en verify chis single in control 

X:OO!Il. 

See Maautactures literature for detailed in.structiona . Fill out: and ~fix a new calibration sticker. 

e . = lb/ lur 

•. 

1-

.. 

CiU.IBRATXQN RBPQ&T . ! 

r-· ------·~:--- . _j . ____ ;ror DO"'-o VAL _ _ m __ ,___B_e_·B_ort! .C81 ,: :~--·-------- - I 

1 po o~> \~ loo:?. o •·I:Jl. 

After Calibratioo 

CAf.IBRA_TlQN SQDBOJ RHDRVMCR 

,. 

Coa1nent~< : \\lo ~.At.\ o:v-Anol-..l Nro eQ 

wM.c.--

l?er rOXIlle1l by: ____ _ ____ Date: /[-/7·-o <7N.me:~ 

JB Pl ace=---,-...,-,...,...- ----- CALSHBBT. WDB (.F e1~ o.r Sh.op) 

I 

VES012119 
'lW".C n<Sl'R-lJI!ENT CllUf!RA'l'l:Ql( l!B<XllW 

llNI'l' #4 

TAG: liT 

,f':~: LOOI?: !l59A 

''' ' ' DESCRIPON: dp Tran~llt:ltter 

. SBRVlCE: SXACR FLOW 

LOCA:riON': VLD 

LP- SllT: 559 

P&ID: F019 

ANtiiUl\L 

RiNARKS: PSE averaging pitot tube 

INSTL- RM!'..S: Bast side of· Stack 

SPBC- RMKS: 

S/N: 1222931 

il. l: l b/h.7: . 

HANUFACT: Al.lt.OI!Illt ion Service 

MODB~: 11Sl DR2F2203 

SCALE: 0-1. 73 in c 

CALIB-!N: 0- 55,000 ACPM 

CAT,IB-OlJI': 4-20 I'IADC 

l?JlOCSSS-Sl?: 

INST- SP: 

AcriON: 

I / 0 NUMBSR: N0 0l: 0093 

CALlBJlATION JU!pg;RT 

.. 

I 

I 

[ 

I 

f 

I 

4.' "F ~ ...,-· .. -- --;r:ii'i1i'iTvn;ue---·---·---- - -·--:z:lliSbUJiii!:tiit RDDBG---- - -

< .' • 0 BcZore CaU.brac.ion · '-/. I ~ ,., A-

/.7 Y' w ... c , t:Z. 6~ 1"1.4 

After Callbrat.iot~ 4. 0 ~0 

J.73 zojJ 

CAl..I'SRl\l':r;!l1i SOQRCB RR!mBNrn 

Corom.ents: 

Performed by:,,6 · -,-: h,, pi 

Jll Place =----::~-::-: ~7"":~ ~..--­ OU.SH&ST. WDB (Fie.J.d o~ 

.· 

·. 

I 

\ 

( 

VES012120 
... 

T"AG: • .<o, T.OOP: 

~ · ·::) DBSCR.1J?ON: 

~RVICB : 

LOcJ\.TXON : 

LP•Sl!T: 

P&ID: 

RBMAR.KS: 

· INSTt-RMKS : 

SPtx:-RJ«S : 

S/N: 

TiU IN'S"TRUMBm OLD3RJ\TlON ~a>IUJ 

ORIT 4i4 · 

li'r 

S59B 

dp TranEI'IIicter 

STILCK PLOW 

ULD 

559 

POlS 

ANNtDIL 

PSS aver~ging pitot tube ~ortn side of StaCk 

12229H 

fii)U((1I'ACr: Automation Service MOD~: llSlD~2P22B3 

SCA~~ : 0 -1. 73 in we 

CALIB- !lr: 0-55,000 A.Cllt~ 

CALIB-OOT: 4-20 l·li>.DC 

PROCESS-SP: 

. INS'l'-SP: 

AC'.I'ION: 

I/0 NmlBIIR: li'OOl: 003 3 

c;&ulRRATIQJi NODS 

--6. I lb/ilt · 

CliLil!RATIQJi :UBPORT 

INPUT VALUE -·--·----lNSTJWIIWil RBWXbiG ~ 

------,,--0;;_--:----Be_f_ore Callbrat:ion · L{. I 3 tn J 

/."?<s ''w-e.. i<t. <tb,., A 

Ccamenta : 

JB 

CALSHBBT. 'i!DB 

0 After Calibratiao 

Place'-----~~~--~~~--­ ~rSbopJ 

., 

<. 

,', · 

I 

!. 

: 

I •' ·, 

1. 

j 

• ' 

VESOl2l21 
. · . . · ......... • .. .. ........ . 

l' 

'tAG: F'l' 

'niX Ili"S'!"I!li!I.K!IT cu..IBRATIO:N HBCilllD 

UN'l"T ·ff-4 

ANNUAL 

f., :, r.OOP: 42S 

> : : DESCRIPO.N: lo2!G ME1'l!R l>IAND11ACT: Fiscller. & l'or.l:or 

MODEL: 147SBN09PL29KOl1CAt~ 

SCALB: 0-20 Gl'fol 

' SBRVIO: X·18 D!L Sl'..lll!RY 

LOCATION: l'UL"C 

LP-SHT: 425 CALI B- IN: 0- 20 G?M 

PbiD: P016 

REI'IAAKS: W/GAS CU!ANDIG TRAIN 

INSl'L-RJIIItS : 

CALIB··Oll'r: 4-20 MADC 

PROCBSS- SI?: 

INST- SP: 

!lPRC-RMXS: ACTION: 

8/N: !/0 NUMBER: Nl: 112 

.t'.Al·'tBRATIQR NqrBS 

Plush process piping, connect water hose to upstream side of 

flow meter. Set concrol syscem to appropriate control rate, 

and r ead totali%er, f l ow water into a container· and compare 

the tol&alizar reading co the mea~ured amount in container. 

' . see HmU!xact:ures literature for detailed inatructio.ns. 

eill out and aftix a new calibration sticker . ..-e.1 i b/hz 

~~~ .-- -----1N~PU=t ~~--------- -------·---T:ra•s~DUJnmbes~t --------

(9 G, Q. . \ BIJ~o e Cal.ibrat_J.on _ __ __,<!J G~c...=.!!.,._ __ _ 

J Ga.\ ·2 Gc ..l 

.ll.f ;:er Ca2ibra c.ioa 

QfirppnTIQN' SO"RC8 ;gRFRRRNCJl 

Comments: 

JB 

CALBHEET. WOB 

Date :tJ-u-f:J:r= ,;; kX) .Nf@l 

Plaae: '· 

(Field or Shop) 

\ 

,, 

l 

• 

VES012122 
• • • • ·' • • •. -!', •• . ..... ...... _.•} 

... . -!";; 

~ :··· 

·' '• .. 

·.:.. 

' 

Tl\G : 

LOOP: 

Pl!SCIUPON: 

S8RvrCE: 

UCX:A"l'ION: 

LP-SHT: 

P.!<tl)' 

li.EMA.QJtS: 

INSTL- RMKC: 

Sl>BC- RMKS : 

S/N: 

IW.T. I lfS'.I.'RXIHllN£ (':JU.l.BAA.TI ON RE:CORD 

O.tllT ~ . 

liT 

426 

MAQ MB'l'BR 

ANNtli\L 

X-19 DIL SJ.UlUtY 

;uuoc 

4 26 

F016 . 

'1'1/G."'S CLB.AliiiNG TRAI!>I 

S;i.ze 1: or 25mm 

11\.'l!li'Ul' l\.CT : 

MODlilL: 

SOLI!: 

CALI B- IN• 

CALIB-001': 

PR.OCBSS-SP: 

IN&T- SP: 

ACTION: 

I/O l!UMBER: 

QI·TRBJl1'IOH RQ"'SS 

l!'i acb.er. & 

lODU'ISC 

o-ao GPM 

0-20 GPl'l 

4 ·20 111ADC 

Nl : 11-3 

Porter 

Plu.alt process piP,ing-, connect wa ter hose to upet ~:eam side o£ 

flow meter. set control system t o appro~riate control rete, aod read totali zer, flow wacer into a conta iner and compare 

the tolta.Uze:a: ~ng to t he me;seured amount in conta iner. 

See Joia.nufac:tures literat ure for detailed in.st :roctions. Fill out and a f fix a new coli.bration s ticker. 

8 .1 l b/ M 

'· 

.'. 

• 

., 

l· 

I. 

·. 

:s:NS'l':RIJKil RiWliNG -----------f ~~:~ 

DI.I?OT VALliE 

0 C..c .. \ Before Calibration 

J2 

CliLSHEE'l', WDB 

After Callbratjon 

CAI.I!!jAUON SOlJRC!! RJ!FgRJ!NCR 

Daee :l~ l\ -0 <4 ime~ 

Place: · ,JJ . (Field or Shop) 

···-·--... ..... ·.•nlr 

! 

VES01 2123 
........ " . ... . ... .. . ' 

>. 

(CMS Task IC403:>j PAGE I OF3 . 

·=----•-=-""=-=====-===="·"'- =~====~~AGS~ =~F~tji;,_ 

1 7SHI "'IlS KILN HIGIII UGII 

2 TSH~I7 SCC HIGH HIGH 

G TAli! 1-404 TaAPER!NG CHAMBER HIGI I l EM!' o 

7 \IIOI.A'OON OPAI:STY Ill Gil INSTANT A TEOIJS 

8 l'llOCESS MONITOR FAJLED 

9 WAS'fE F!:ED MOl./! fOR f).ll.B) 

12 v101J\'110tl STACIC FlOWIIIGH I MIN 

13 VIOI.ATIONZAC.3!6(1RV)OPHN 

14 VIOLATION ZAC-OZII EIJR<:l: VENT OPEN 

-

/ 

_.:....__ --·- / 

/ . 

'~--~.OS~!.':N.Il!:~~!:JCJ:__ ____ -· •0•- 0--00 ·· -- ---··· ----·-·· ·· ··---~· =-=-..,. .. -.. < • • ~ UMi5lJ ANAL. VZER r-Ail. CO . _,--

17 UJI.SSOANALY'.lER FAll. 02 "" 

11! VP..582 NW. VZI:!R FAIL HC / 

19 POAL-5!!3lc:N>I oaTil Po QO FNl FAR.UI1E) / 

2D WFO-off C/IRBON IWECTtON SYSTE!il FAJV'.O 'I"' 

21 PSt.tOIWSL-:100 SCC COI.t9o AIR fAN FAl.EO 

. }"' / 

2.3 I'Sk20il X.· 14 PRJMARY AJEL LOW PRI!SSo (ONLY APPLIC/li!).E RlR lR FUEL OIL) 0 ,--

25 ST,ACX. Fl.OW HIGH IHSTANTANEOUS / 

35 VIOI.ATION SCC TEMPollN/1 MIN Ava~AJ3C 0 /' 

Y.J VIOlATION toll~ 'ICM>o I.D.V I !oliN 1\\/ERAOE 

/ 

In WFO-OfFHCI..H~1 MtNAVERAGE / 

38 WR>-ni'F OPAalY HIOil I 1!11'1/\VFRAaE ___..-

39 WFO-OFF CO HIGH 1 MIN AVBVIOE /" 

l"'~: . t ' .. j) VJf'D.a=F.HC (lliC) .IIGH 1 MIN AVERAGE / Oo • 

41 Wl'O-OFF 8.1\GI.WUSE I:)B.TA P t1113H 1 t.lltl AVE.RIIGE . / 

'<· 

' 

I 

L 

I 

>o 

VESOJ2124 
. · 

• ........ ..... . .. . .. ·- -·~·· 

., .... 

42 Wf'f>-Ofr ~~ OlJI"LIITHIGHTEMP. I MltlAVI,I\1\0E 

.f:1 WI'D-OFF OX.'fGEf'H02} 1.1\W 1 Mill AVERAGIO · 

44 VIOlATION HCL HIGH 1 HOtr.'l. AIIF..Ili\GE 

~G Vl()l.AT!OI'/COHlGH I H~AVERAGI! 

-16 IIIOLATIONSCC'fe&>.!..OIV 1 HOURA~ 

47 

oUR. 

VIFD-OFF kOI'JEMP. LOW 1 - AVEI!NlE. 

48 VIOI.ATlCNOPACfTY H!GH-180Sr:cMOUR 

49 W~"f BAG!IOUSE DaTA P LDW I !>(N AVfRAGE 

. 52 Basi I.Aak De!EQion S)'$\em (fribo) 

GS P""""b161 Hour Roling Totol OP~ 

ao Non-P\Im41"'>lo ll'four Rolllna ToWI OPI. 

~-.IIllalltiJ:;tt.!.l:!2J!r.lli?llm!!J!o!l OPL,_,_ .. __ ...... _ ... _ ,_ ... __ ............. - --·-----··---·:. 

. . . J IITU 1 Hour Total OPL 

811 a. 12 ~""' Roi!Ilg Tolal a>\. 

70 Low V1ott.ti1o 12 Hour Rolh;l T olal OPL 

71 Semi \llclillt.,1;aHour-.gTollllOPL 

72 Mcot:UIY 12 Hoot Rl>!llng Tolal OPl 

73 A8f1 12 Ho·.r Roling Total OPL 

H PCC T-lu!O I HO<Jr Rolng AvetiQO Low 01'1. 

7S sec Temperob"" tr-li>urRl>llfng 1\"""''Jol.OW oPL 

76 SOl\ Oullet T"""""""'"' 1 1lour Rotlbl(J ~go HfgJ1 OPL 

79 StackHCI.Com>ctedii-IDII'Roli1G A'olllll9oHigiiOPL 

80 !bel< CO Corrected J} ~ RDMro Ave<OOO Hlgll ~ 

!~ : J Slack Acw 1 tiel! RoiiOia ... _. v~ OPI. 

82 llltCVttal..im<>Rol'l1 Mllllll<IA-~O L 

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PAGE30F3 

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50 WMTEFCED CUf-C.JFI'TiiSTBYOI'BlATOR 

UNn' ll\i OPERATOR TO CI.OSE MANIIALJ.IAND ~Yl! AT UQUID IJolJECTOR ~£FORE flEX LIME& Aln.IINt;"l\l 

SCRt;I'.NED ~XV.o13 ~1JOE CATE. 

VERIFY ATOMIZING AIR AJJIR/.1 IN" MANUALLY SHU"rTING AlR TO PRF..SSURE SWrri:H. 

(NOZZEJ. MUST ~PEN FOR ALARM TO FUNCTION) . 

;<,.10 / X-11 / X-12 /" X-22 / 

83 Ll""' SJurry Density low 1 Hour Rolling Average SllQutrlown . 

·~~ -----·-----------·----- { .. i LOG CHECKS IN OPERAT10t4S 8001< 

85 ROO OIJr l(JLJI PRESSURE UN!' (PT-300) 

COMMF.NTS : 

CHECI<l3> !IY : (\,eclstl)a.Vd<S. o.te :lo-5'-cP{ Thle: J:l/.s-~ 

APPROVED BY: 

BiWEEK\.Y_4 

911 om 1;1K 

1/aeJ..a{ lim ~ : Control Rootn 

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l"SHII.300 1<11.N HIGH HIGH 

z l'liHII-317 sec ~h6H HJOH 

3 1'/\liH.!O(J I(JLH H.'GH Pf<ESSUm; 

4 t>AHH-32.4 SCC HtOII PRESSURe 

6 TAflti-4~ TEMPERINa CIIAMBB'l HIGH TEMP 

7 V101.A110ti0PACIIYHIOH JNSfJINTATEllUS 

8 I'HOCESS MONrTOR ~AILED 

1 Z VIOlA 1100 STACK FWW IIIGI111AlN 

13 VIOLATION ZAi;.a18 (\RV) OPGN 

14 V10LA710N 7AC 0211 ~U ~GE VENT OPEN 

16 UA-55U AHM. VZ!!il FAIL CO 

17 lJA,.5(l() ANALYZER I' AIL. 02 

18 UA-582 ANAL. YZER FAll HC 

19 POAI.. 83 LOW 9ELTA P. (IP FAN FAILUru;) 

20 WfO.O~'f CARll ON IIIJECnON SV$'1Bo! PAllED 

21 PSL.IOM>SI.-200 SCC COMB. AIR F/IJ>I FAlUD 

. 

5·t 

23 PSL~ X-14PRIWIRY I'US.I.O'NP~"SS. (ONLY Al'f'UCABLE FORI'lf!T:L 0!1.) 

25 ~ACK~l.OW IIIGH IHSTmTANEO!Jll 

35 VIOI..AllOtiSCC'ItM'. LOW 1 I.QKAVERAGE 

38 ' V101.A'Tl011 Kll.N 'IB.IP. LO\V 1 lltW AVERN3E 

:>7 WFD-OI'F HCL HIGH 1 MlN AVERN3E 

.....-:-3~ WFO-OFFCOIIK".H 1 NA~ 

• ..0 WI'O.OFF HC (Jl-IC) IUGI11 lAIN AIIER#.GE 

41 Wfi}.Ofi'MeHOUseDB.TAP!IiGHf iAlN AIIERAGE . 

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CU -OFF=-·---··-~-----:-----==·~·- =-~-----!~~ FAll 

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4~ >,IJFD.OFF SDA OUTlET 111GH ·r EMP. 1 hUN A'll':l'liiGE 

49 WfD·OFF OXYGt'W (02) lOW 1 t~ N i\'\II;RAGE 

44 VIOI.I\TION HC\. H1Gil 1 HOUR AYEAAGI-. 

46 VIOCA110N OOHlGH OURAVER.~GE 

46 V10CA110N SCC 'l&'.P. I.C!N 1 HOUR A~ 

4'1 ~!)..QFFkJlN'fl:'I&' UJN ~ ~GE 

40 WFtXJF'f I!I'.GHOIJSE OO~'l\ r> LOW t t.CII'I f.VERAGE 

89 CL 12 Hour Rolling TOll>! OPt. 

70 """' ViOI8Iic f2 Hour R<l«<l9 T<>IZI ~Pt. 

71 Semi ~·o 1.2 Hoolr Ral!l1g Totol OPL 

Tel I~«<XA"Y 12 H<llll'Rvllns To!al 0?1. 

7:1 .._.h 121-iout Roling Tolllf OPL 

74 f'9C T""''"""IUre 1 HoU' RclfinaA~ LawOf'l. 

'16 SCC 'r""'potaiUJe 1 Hour RdiftlQ Aver9go Law OPl 

16 80A Ou1lol Temperalu!o 11io<.o' R<>fing """'age Hillh OPL 

77 e.sgl0009e Olfferentiol PreG$<.'1'8 1 t.C1niAa .A-o Law OP!.' 

78 BIIQ""'-Ollfer<n1!al 1'1=..-e 1 Mln~Ao Av6nl(lo lf1lh OPI. 

79 S!a k~lCL ~ 1 11cu Ro1llng A•-~ 01'\. 

80 ", .. ,... 

( ... J1 

Sl>od< CO COirecled 1 Hour~ A'fCn>go ~ OPL 

Block Aow 1 Hcllt Rolling A>it:1age H'9' OPL 

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'ADE~OFJ 

50 WASTJ: FEED CUT..QFf 1 CST BY OPERATOR 

m<JTIN llPERA fOR TO CfJlSE l.wllli\L HAIIIJ VALVF. ATUQUJD INJECTOI' BEI'oro! Rex UMI': & AIR IIN!i:TO 

$CR£E.NEO FE!'nER XV-1)13 SUD6 GATE. 

W~tf #4 Cll'tiRATOR TO VSW'( CUT-OC:f rN PReliSING EA~ Sl'ART BUTTON. 

(11 Ji:N INITllll & SIGN SHE£!) 

SHRI:OOED / SCREENt'P / MAIN ~OR 

X-10 .....;/~ X·11 / X-22 

AUX CON"" YO/~ 

VERIFY ATOM!ZING AIR ALARM ElY MANUAJJ:.Y SHtfl TING AIR m PRESSURF. SWITCH. 

(NOZZEL t..IUST l:lE OPEN FOR .AlARM TO !'UNCTION) / • . / 

X·10 ,/ X-11 / X-12 ~ / 

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~Ume S!wry Dan.s.:!!' LOw 1 Hoor Roilillg AVCI!IQO · Sl>ouldowrl 

--------···--·--·----- ;4 LOG Cl fECKS IN OPERA110NS OOOK. 

85 HOD OUT KILN PRESSURE LINE (PT-300) 

CHECKED BY : C\~e-\_ UWQ~t&= !crAm~= ~ 

APPI<OVED fN ; 

BlWEEI<l y-4 

9/10KJ7 HK 

_i/aeJ4.c. /..{lrvt Plooq : CQ!llrol Room 

; 

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VES0 12129 
..... ~( , ........... .:. ....... •:" < ' ..... ··· • I """ •" ... 

• :-:Rfo" V.""":' 

1~.:. 

2 TSHH-311 SC'.C HIGH HIGil 

3. PAKH-:100 KILN H1GH PRESSURt 

4 PAJ-ti.3Z4 SCC HIGH PRESSUII.!:: 

-6 "ll\IIIH041CMPEPW«>CHIII4JER HIGH lS.CP 

9 WASTE F!;ED ~R FAU.Sl 

17. 'ilol.'TJOU STACK FI.CJW HIGH 1 MIN 

18 VIOUITION ZAC·S16 (lRV) OP~ 

1e IJ(.,..$!AHAL.~RFAII.HC 

10" I'DAI.-663lCW OB.L' P. (lD FAH F~) 

:W '((RXJff CARBON !li.!ECIION SVS1UI fAII.Bl 

21 PSJ..100/PSI..·200 SCC COMB. N it fAH FAILED 

·---.. ~--~..,. 

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......... w-..s;:o.,:,~c:r~"..,..: r· ..... ~1'' """"; .. : f'·· . 

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23 PSI.-200 X-14 PRIMARY FUI;L LOW PRSSS. (ONLY APPLICABl.E F<lR 11:: FUEL Oil) 

:W S\ACK RJ.lW HUuH IHSTANTANEOI.I$ 

35 VIOifirt0/1 SCC -rEI*.LOW 1 ~N AVERAGE 

:lG VIOI.AliON KJIJ'j f<il'. LOW 1 MIN AVERAI3E 

trT WfO.Of'f Hct. HIGH l loi!N A'lffiAGE 

SO WFD-OFF CO 1-flGH 1MIH AVERAGE 0= WFI><lF'f.HC (TllC) Hl6l! 1 !.!IN Ali1!:RtoGE 

41 WFO.OFI' EIAGHOUSEPaTA p HIGH t"MIN .WERAGE . +-

YES012130 
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.· . -:....; ·,. 

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~ , ,; l't'£oCUf.OFF ·~--= ---- I'Al>"!> fAIL '· -.'\-- - -==---"'/l:•a==-----=-==-- ------......,~ . · ..... ~ 

43 WI'Tl-OfF OXYGEN (02) lOW 1 ~IN AVERAGE 

M VIOLJ'IION HCL HIGH 1 k'OUR AVERAGE 

46 VIOLATION CO HIGH 1 HOUH A.vtliAGii 

-46 · VIOI.ATION SCC TCMP. I.D'N 11101JR AVOlN3r: 

1\o~!l. 

11 VJFO.OFF KlLN TSti': UN: 1 - AVERAGE 

o!.H VIOlAT10NOPACm' HlCH430S£CIHOUR 

40 ~f I!AGHOIJl:o'f; DEL 'fA I' LOW 1 tAliMIIER/IGe 

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~ Nof>.Pumpablo 1 Hcurlln(Jing ToW ()~ / 7 

6U f>wnp<lb!c 1 Hour Roling Tol:il OPL 

?f.--.l~!!!L"!Y~..!!S.<"" R~J_'!!!J.l.Ql'L ___ ,~--- ···-···-: --·---- --·---·---· -"-~~......,, ---,.. 

·' B1U I HourTW.I OPL r / 

6S Cl12 Hour Roling Toial qt'L 

70 low Vlolalic.1ZHoorRQIIoglolol01'1 

'fl SIRI Vlola!ila 12 H- Roliqj TO!al oPL 

n ll.ercouy 12 HGox RoDng T""'l Of>L 

TS Ao~ 12 HCft#'Rol5r>g Toml OPL 

74 PCC Ten>C*ah.., 1 flourRolllrg AveraueLOWOf't 

'(15 SCC Tomp.,atute 1 Hour Roling Avetll!le L.cw OPt. 

90 Iliad< CO CQI\lded 1 HooJRoOng A-Hlgll 091. 

·~ ':• Slide flow HI.,.,..Rdtog ~ 1-0PL l 'lJ'I 

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l'MT f.i Of'E.~TOR TO CLOSE AlAHUALHA!ID VIIJ..VE AT LIQIJID fNJt:-ctOR~ A.EX l l\IF. &AIR'll~ TO 

SCRS:tla> FEEOB!xy·OI3 SUOEClf.TE. 

UNn-114 OPffiATOR ro Vc3liFYClff.Qf.l' I!V I'R.F..SSINll rACK START SIJTTON. 

(YHCN INffllll.&. SIGN NHJ,;I£1} 

· . SHHr.t.ll~fJl !h/t- SCRI~'J'It:'D ,V k MAIN CONIFEYOR ~ 

X--10 X-11 ~ X-12 ~ X-22 

1\UX CONVeYOR 

VERJI'Y ATOMJZliiG AIR M flY w.NUAI.L Y SlltrmNG AIR TO PRESSURE SWITCH. 

(NOZZEI..MUST BE OPEH FOR AlARM TO FUNCTION) • 

X'1D X-11 X-12 X-;!2 

ALSO CIIECK OI'C!RATlON OF RAM COOLING WATER LOW FLOW 1\LAR!A -~;>7.78) 

CHECY,EO BY: 

a3 . Ume Sfl.fl)' Oan~l(y Low 1 Hour RoUing Avar:l!IS ShouWown 

1-• 

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f .. : ' I.OG C!-l!iCKS IN OrERATIONS BOOK 

-------···-··- ' 

86 ROO OUT K!LN f>RI7SSUR.E UNE (PT -300} 

r.. . . ·::: 

COMMENTS : 

QiEC!CEDBY: 

BIWEEKl.Y_4 

9110107 HK 

Pw.:o: : Cailtol Roorn 

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PAa: 1 Of 3 ~m,;e<!_YUNtrt0-4 

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~ TSHli S0510LN HIGH HIOC I 

2 n>Htl-317 SCC HIGII HIOH 

4 f'AHH-321SCCH!GIIPilESSURE 

7 W.!IATION OPACI1YH1GH INSTAifli\TEOUS 

8 PROC"S.~ MONITOR ~NLB>. 

12 VIOLAllON STA<;K FLOW HIGH 1 MIN 

13 VIOlATION ZAC<I16 fffiV) OPEN 

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18 lll\.682 .o\NAI. YlER FAIL HC 

19 PDI\W63 LOW DeLTA P. OD FAN FAILURE;) 

20 IJI'Fl).()I-'F NJECTION SYS'rfl,l FI\ILED 

:Z1 PSL·IOOII'SIAOO SCC COla .AIR FAN FAIU:D 

35 'VXXATION SCC Teln'. LOW 1 MIN AVEW.ClE 

36 o\IIOLAllON KILN Tal'. lnti1MN A~GE 

'Sf WF'D-()!'F HCUtiGii 1 MIH AVERAGi! 

3S WfD.OR' OPACI'IY HIGH 11AlN -'\IERI'.GE 

39 WI'O-OFF CO HIGH 1 MIN AVB'IAGe . 

; ..... 

.. · ;, V'lfD-QFF.HC (THC) I!IGH 1 MIN AIIEJWlE 

-41 WFD-Of!' 8AGHOUSI! DElTA P HIGH f lAIN AVERAGE , ..:; • . ' . 

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4.2 WFD.OI'F SDA OU'fLEr liiGH TEMP. 1 MIN AVO<AGE 

43 WFD.Of'POXYGEN (02) LOW 1 MIN AVeRAGE 

¥ VIOt..\TIO!WCL H1GII1 HOUR A\IEAAGC: 

~ VJO!Al'KIN CO ttiGH I HOUR AV!'Jli\GS 

4G 'VIOLATION SCC lt:MP. LOW 1 HOUR 1\VERAGr:: 

. fW~I\. 

47 WFO-OFF KILN T9.4f'. LOW 1 Ill~ AVERAGE 

48 VIOLI\TIOtl OPACITY HIGH 480 SE.CIHOUR 

119 Wfl}.()FF BAGliOUSf Dcl.:fA P tOW 1 Mitt AVERAGE 

52 Bag Leak Det.ctfon Sy•tem (l'dbo) 

f.l5 Pumpable 1 Hour ROlling T~ Oi>L 

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00 Non-Purnpablrfl HoUrRoMing TolaiOPL 

-~%."~ ... :cowtw~.:rom.!.Qf!, •. _. ___ _ 

· . .£ rrru 1 Ho, •. ,oa.l OPI. 

e9 CI.12HourRo4fing TOisiOPL 

70 Low Violallle 12 Hour Rolling Total OPL 

71 S..nl Vloloffie f2 11our Rolfn9 'fobtl OPL 

72 Motr.ury 1211out Roling TQ!ai OPL 

13 Ash 1~ Hatx Rollln9 TOOJI OPL 

7 4 PCC Temponolure 1 Hour Roling A...,.!J' loW OPI.. 

75 SCCT~e 1 Hour Rolllng'Aveta(le l.<l\• OPt. 

77 . Beghouae D1!ferenllo1 Prcssu"' I Mil>.l1<> Alton>ge Low OPL' 

·78 lla!il>o<JS<> 0111\>ret.u..l Presau<e 1 Mlnule AV101>9e Hlg~ OPl 

711 Stadt HCL Coneued 1 Hour Roling A~ High OPL 

•. , ., 8D -CO Correc:lod 1 Hour Rolling, Ave,_ HIIJ!l OPl 

c · · .. :: ... :J1 Stadr f1C!w 1 HOur Roling A\'Ot8ge H'l!]ll OPL 

82' Hrl CI/H!a Lmo Flow 1 MitoJI<> A""fll90 01'1. .. 

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"IWEEKl.Y UNrT/14 CHECK $111'1-if PP.GF.~ 0>'3 

!' . ~Tr;fE~~~I=F - .. -=----~-----· · =="-·~~---·--~ .-·-=-= . . . ~ 

:: .. . . . 60 WASTE FEtnCUT-cJfF e&f8YOPI-:R.~'IO« 

UNfT 114 Of'ERA TOR TO Ct.OSE MAJ-•IAL i~I'ID VALVe Jcr UQUIU INJECTOR BEFOOl: REX LIME & .-,IR LINE TO 

SCRileNED Fe?; lfRXV.()1~ SU.DE GAT£. 

UNifl!4 Of>EAATOR TO V8l!FYCOT.o:F IIY I'RESSII-!G €ACI-l STAI<f 8\IITO t~. 

(lliEN IN01AL & SIGN SHEET) 

Sl·ntElXlED=. ___ (;CREENED W. N CONVr:VOR 

X·10 . if ) X·11 '9"L X-12 '\'Tf" X-22 

/1/JX COM'v"EY,9.R~--

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VERIFY ATOMC!Jt-.'GAlRAL.AilM SYIMNUAI.LY SIIU1TIN13AIR TOPRESSURF.IlWITCH. 

(NOZZE. MUST BE OPEN FOR Al.J\RM TO FUNC'nON) 

)(.tO --zt" X-11 'if' ~12 ----z;7' X-?.2 W.., 

ALSO ct-a:K OI'ERA'Il~ ~RAM <XlOUNG WillER u;r..v f lOW AI.AAIA (MS~ >71l5) 

cHEci(EO BY: ,Arr 1/pu<y 

83 !..lme SILIITY Oonsity Lew 1 Hour RoUing Average 

'5 LOG CliECKS IN. OPERATIONS BOOK. 

Sllouldown 

115 ROO OUT Klltl PRESSURE UNE (PT -300) 

. 

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_,.,, ::£~;;!: 

APPROVED rrf : 

BJWEEI(L Y _ 4 

9110107 HK 

jllo.a L~ /<J;.. 

Ploc:e : Coll!rlll Room 

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,_ ...... : ... ...-....... .. . •.• ··-=- •• •• 

1 TSI·III-305 KILN HIGH HIGH 

2 TSHH--317 8CC IIIGHHIGH 

4 f'JIIil'.324 SCC HIGH PRESSURE 

6 TNI!I-4G4l'EMPER!NG CIW.IIlERHIGll TELIP' 

1 IIIOlATIOHOPACIIYHIGH L1S'f!\llTATEOU6 

8 1-'ROCES$ MONITOR FAILED 

12 VIOlATlOt-1 STAf'.j( R..OW H1Gtl1 MIN 

13 VIOlATION ZAC-3 ~ (rR\1) OPEN 

1A VtolA1lOI( ZAC·026 SURGE VENT OPI.':N 

PACE 1 OF3 

PASS Fl\ll I -'::!o_~.~:::.:~=:o= 

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:- 16 UM>58ANAL~FAltCO . 

17 U~ANA!.VZERfAIL 02 

13 UMi&2 AWJ..Yl.ER FAIL HC 

Is' l'tW.r~ LOVI OB.TAP. ODFJ\H FA!LiJ!o.."J 

2.0 WflH)fFC,A.RaQN JliJEC'TlONSV'&'TSI FAl.EP 

21 PSI,.:100/PSI,200SCC COMB. AIR r-AN FAll.pD 

23 PSl-209 X· 14 PI<II&ARY Fllf't LOW PRESS. (ONLY PPPL~I..E FOR 112 I'\J13.. OIL) 

2.0 STACK fLOW HlGII INSTANTAN8)US 

36 VIOLAllON SCC 'IEI<P.l.OW 1 MIN AIIEAA!3E 

SB VIOIXIlOH KlLN TEiAP. I. OW 1 MIN AV!:RAGE 

~7 WRHlff HCL IIIGH 1 I.I!N A'A:RAGE 

38 wro-ofF OPliCITY fi!GH t ~oliN AVERAGE 

41 Wfi).OFF 81\GHOUSE oa TAP HIGH ,.MJH AvtWoGE . 

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'IWEO<\.VUNIT#4 (CilSTast iC4aJ2) PAG€20F3 

:, . ~·~ ... ~l.ca-''~FF -~--·----=-- -L-•~,q~-F;";~--~---·---- f.&-. FNI:_. .... . ::.;-- . . 

42. I'III'U-OFF SOA C)UT1.EI' HtGii 11$1.11'. 1 MI.N AVI:HI\GE 

~ wro-Orf OXYGCN (0 2) OW 1 MIN 1\\/ERAG!l 

44 VlbLATlON HCL t-IIGH 1 I toUR AVERA<>f. 

<IS IITOlATlON CO t i!GH 1 HO\JR AVERAG€ 

49 WI-U.QFF lli'IGHOIJSE DB.TA P ~OW 1 t/JN t.VS~E . 

67. ll<4!l ~ook Oele<:llon b)'slem (Tribo) 

65 Pumpa~lle 1 1iour Roli ng 'fohll OPL 

6U n-I'~Jmpabk> 1 Hour Rollin!J Toto! OPL 

~Z.J.I&t!i.Y.~ tii~IJ!I Tulal OPL, .:.,:: _ _ 

.!lJ l!fU 1 HO<r 'l'ot:J OPL 

7U U.·t v ..,'crljla12 Hou< f~<~Cnl~Total OPI. 

71 SetN Vlol;rtle 12HoorRollrlgTOiaiOPl 

72 Mo<w!Y 12 Hool Rolling Toto! OPL 

73 A'lh 12 He..-Rol'1rg Td al OPl 

7<4 PCC Tompert!hl!<t 1 Hour,Rolllhg A'B1ige t-OPI. 

75 $CCTOO>poroturo1 lour R\1llngAv.,_LDwOPL 

7G SOA o.rtlet To ~porotu;e1 H«A' !~I ling A~raoo ltg)l OPL 

'77 ~-Ollferenr .. t-..r&T Mlr1U10A1<01ago l.ow OPL' 

7U BaghollsaCII!cnaTJal Pr ... uro 1 I<IO>ut8 A..,_ High OPl 

'f9 SlaCt HCI. Coaectc<ll H<xl< ~ ,\-.go ~h OPL 

1., 110 Stood< CO Corroded 1 Houo Al>ilng AVW<CJOI11g)l OPL 

J ,,'/';. 

·' ')t Sloei<.flow I Hcu'Rol'n;; A;'Ofa9~ High OPL 

82. Hl1 CUHra Lime f1o.., 1 LIM!! A"""'9" OPL 

/ 

----· -- -

) / 

/ 

/ ---/ . 

/ 

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/ 

/ 

/ 

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/ 

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I 

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• • 

VES012137 
•• 0 • • . . . ... 0 '• 

.• 

HIWEEKI.Y UNIT:U ClifiGK SHEET 

~FEED CtJf.off' f ;::·~ - ---=-.. •-.. 11·-~·-~~--MM- -- ~-----~·--------~--=--

IJNIT#ol OPERA lOll TO ClOSI: I.WiUALHAND VAI.IIE ATUQIJIO IN-ECTOR IIEFORE FlEX Lr.'E & AIR liNE TO 

SCRt:I:'NED FEEllTH.XV-018 suoe GXTE. 

IJNif f:1 ~TOR TO Vl-lliFY CUT .()r;F flY PRESSING F..\CH Sf ART I'IVTTON. 

{ r HON INil ii\L & SIGN SI·IF£1) 

Sf lltEDDED /~ SCRt:l'llED ,/."" I-!>\ IN CONVEY911 / AtJX <:01'-IVG'i'OR / 

X-10 X-11 .X·12 __ .:_/ _ • X-:!Z 

v-t:rufY ATOMIZING AIR AlAA/11 BY MANUALLY SHUTTING AIR ·ro PRESSURE SWITCH. 

(NOZZEJ.. UUST BE 01-'EN FOR AIJIRIA TO FUNCTION) . 

X-10 . / . X,11 / . X-12 / X-22 / 

ALSOCHECKOI'~~OI' W~:::~WA1CRLOWf1 .0WALARM(MSGI!~8) 

CHEa<Eoav: \~4 5 a. vCLS 

.. B3 Urn~ Slursy ll~ Low 1 Hoor Rolling AvarBge !ihotJ!down 

-·~- v ..... ------· -~--- --·--------------·- 1. 'J LOG Cl IECKS IN OPERI\T!Ot-IS BOOK . ' 

65 ROO OUT KILN PRESSURE UNE (PT -300) 

COMMENTS : 

~BY: 

BJWeKLY_4 

9110107 HK 

.. 

u:~ lS~, 

~ 1<1rn 

:,. 

-~ . 

' . 

Time:· I : LJS ®~~ 

VES012 138 
, \ ' : . . .. ' 

·..--. ., 

. . 

ABSOLUTE CAUEW.ATION AUDIT (ACA) DATA SHEET 

Unff#_ ·_. 4 Serial # .. --.:.... cos~ ·-· 

- Parameter NIST Traceable Calibration Standards 

·c;' 02 25% Gas Concentration 

r CO-low range 200ppm Low (Zero) 0 ± 

r CO-high range 3000ppm · Mid B.a3 ± 

r HC! 1000ppm Hlg11 15 ± 

Run Number Concenlraoon Olfl'erence 

Reference Anatft.er Low Mid 

1-L.ow 0 0.1 -0.1 -

2-Mid 8.93 8.98 - .().05 

3-Hlgtl 15 15.3 - - .4-UJW - --i};1-- :...___~ v . 

S.Mid 8.93 9 - -0.(17 

~h 15 15.2 - - 7,Law - 0 .. " 0.1. .().1 -

8-Mid ~a 8.9 - 0.()3 

9-f!1gh 15 15.2 - -

Mean Oifie:ence = -0.10 -0.03 

Calibralioo Error= .0.40% .0.12% 

CsbaOOII Error" Mean Dilfarenc:e I Span Vakle •100 

·CE 

• SignBIJim 21412010 

Ell Tech 

Tile 

9122/2009 

I: 

! 

0.5 

0.5 

0.5 

High 

-

-

-0.3 

- .--r 

.().2 

- - .. 

-

..().2 

-0.23 

-0,93% 

VES012139 
.· .. . .............. .. ·-···· .. ABSOlUTE CALIBRA TrON AUDIT (ACA) DATA SHEET 

.~i~~~ · .. . ···: 

UnH# ~--

4 .. Serial#_. __ .:..~-

Parameter NIST Traoeable Callbration Slandards 

(' 02 25% Gas . Coocenlra1ion 

'r. CO-low range 200ppm Low (Zero) 0 ± 10 

r -h~h range 3000ppm M'td 66.9 ± 10 

r- HCI 1000ppm High 164. ± '10 

Run Number Concentmtion Dif.erence 

Reference lwl'(ll!l( low Wd High 

Hew 0 ..Q.2 0.2 - -

2:M'd 68.9 66.7 - 2.2. - ig h 154 152.6 - - 1.4 

... . #-..,... -~ - --4:tml-··- --·--1}------ ~. · M.-- r---·----· ~---

- 5.\!id 58.9 66.~ - 2.1 - !H-ligh 154 104.5 - - 5 

. 7-Lciw " " . 0 . . . " ·- • ..Q. I 0.1 - -

8-Mi:l 66.9 67 - 1.9 -

9-High 1&4 153.4 - - 0.6 

1.4eilll Otl191'811:e = 0.23 ~.07 0.50 

C8JU?rafun Emlr = 0.12% 1.03% 0.25% 

C!ilibrati:m 'Eirof: Moan Oiflerancel Span ¥ale • 100 

CE Ell Tect1 

2M010 . Dale 

,, 

; 

' · '· I • 

; 

!. 

i. 

'· 

; 

j 

'· 

VES012140 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHE:Er p 

' 

Unit#_ .... ~__ Serial# _ ··- -· .

132 :.. .. __ .. 

· .. 

Parameter NIST Tn.;eable CaUbration Standards 

roz 25% Gas Conceolrallon 

r- CO-low range 200ppm Low(Zoro) 0 . ± 150 

r. CO-h~h range 3000ppm ~td 1079.1 ± 100 

I"' HCI 1000ppm ligh 2289 ± 150 

Rlll1 Numtxw Coooen!ration Dilfcronro 

Reference Mayrer Low MMI Hgh 

1-lll'l'l .. 0 {).2 0.2 - - 2-Mld 1079.1 1006.5 - ·7.4 -

3-High 2289 2287 - - 2 I 

*l:xrrr--·- -----~ .. ·--·0.4--~ 

.. - --0.4.-- . ..: --. --~-··- · ------ ~ 1079.1 1077.6 - 1.5 - 6-Hgh 2281J· 2317.4 - - -26.4 

7-i.J:NI 0 {).t 0.1 - -

tuAid 1079.1 !077.7 - 1.4 - 9-H~h 2289 2301.9 "'" - ·12.9 r 

Meir1 Difference= 0.23 -1.50 ·13.10 ! 

catbratloo Enor = 0.01% .0.06% -0.44% 

Callllcalion Error= Mean Difference t Sp<r~ Value ' 100 

CE Ell Tech 

. nue 

912212009 

2/4rxl10 

DaiB 

VES012141 
...... . ... ,_ 

ABSOLUTE CAUBRATION AUDrr (ACA) DATA SttEET 

Unit# 4 Serial#_ 132 

Parameter NIST Traceable Calibratioo Standards 

r:· 02 25% Gas Concentration 

r CO-low range 200ppm . low (Zero) 0 ± !iO 

r CO-hgh range 3000ppm Md 315 ± &l 

I 

I 

(: HCI 1000ppm Hlgh if11 ± 60 !. 

Run Nutnller · Concentration Difletl!!lce 

Reft><ence Analyzer Low Mkf High 

1-low 0 .j).J 0.3 - - 2-Mi,d 318 284.9 - 33.1 -

3-Hlgh . 707 713.1 - - -6.1 

·f.i"' . '.; ! - ~l:olr- ·- __ _g__ -- . ~ . 

5-Mid 318 305.2 - 11.8 -

6-H'IJh 707 707.1 - - -0.1 

7-lhvt 0 0.6 ..().6 - -

8-Mid 316 314.2 - 3.8 -

9-High 707. 706:6 - - -1.8 

Mean OO!ei!II\Ce: .Q.10 16.23 -2.6() 

Caibra!bn Error"' · -Mfr. 1.62% -0.26% 

Caibmtlon E110(" Mean Cirereooe I Spa~ Value • 100 

CE Ell Tech 

llUe 

9fl.212009 

. 21ift.D10 Oats 

VES012142 
CEMS 

. Table! 

Summary of:R.cl.oll'vo 1\c:cumty T.,l Audit 'Res~ 

Veolla I".Jl Tcclwitol Solutions 

s .. ug:<·t, 'lllhlols 

.Tiu>~ :n, 23 and 211-, 200.? 

Cri~ u 

' P<.:t<:entof cmi•<iat> st'ludauior ab.olllle .. ~ dill't:!euce (ppnj or ':i). 

'PS 4B. 

' I'S 3. 

~MTOI\ L'ioWl UTA 

VEOU~Ps 5 JULY 71Z.:<S C1lC l'rojc<:~ 

' ' 

VES012143 
-, ,..~ 

. '·-'··"' 

·-·· NYX 

·. ·. .Incinerator 

D<l1a Poirt 

Carbon lnjoc:tion Flow 

um .. &llny DenSity 

Stack Op•dly 

Slock CO RCRA 

SPAOtiUeiTerop 

Basllcruso Dllf Pn>~ Low 

Ba~auoe 0111 F'rMl> High 

Slack T.HC 

X1 1 Wolgh1 

X2.2 W..lglrt 

Xl2 Welght 

X10 W<!ght 

Slad< KCL RCRA 

4 

IMiu 'l;\Gn 

AVll· 1\.VO 

Wara. m.:t 

l!li.OOOOO 

. 

3.000000 . ,OJ)I)(l(IQ 

~ GOOJ)()QO 

+IO.OOCO 500.0000 

3.!XIlOCO Z-Nao:IO 

0.1)00000 10.00000 

8J)OQO(lO 10.001)00 

.... 0000 OOOJlOilO 

''"'o '" ',a ........... • • • I" • •• 

I~ 

AVG 

01'1.. 

·-

. ·:i. 

__ .,. ·t:r 

I 

'foolie ,,..,.;t~t:tl Service.~ 

S"'.!if!Lr11inoi.s 

I 

1lir Rml 1 llr R<lh I Ht lilt l l!r R.oll I Hr Rnll ll{r.I<D!I 121ft 

W11m •11ot 01'1. Tot l"otS!m 1o\Of'L &cUl~ 

Wmn_ Warn 

I· s.o""""' e.=m IUilOOOO 

• .60GO>I BQ.4C!OCQ 1!040 

I 

I· 

I 

31>.00006 40JI01)00 100.00f0 

•u .INOO ~31..oo:l0 •:w..ooL I· 

I· 

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1: 

I· 

I '. 900~!10 ~..OOOD 1ooo..to\l 

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' 16.00000 !!:UOOOO 3o.&<IOj"' 

I ---. . · .. ···-1--

Crtolcd 

}'¢rio:1 Sta.-t 

"Puiad~ 

l >Rr Ulir 

nou Tot llloll1ot 

Sl::w_; OPJ, 

~ ( ~ .fl = . ..d 

li!/:0;.0 6:Q-3 AM 

lf~"Ul!O 6:00 /.M 

lllJlOlO G:OC AM 

· l'oe• son 

1 Hf TO-t 1 Hr '1m l lh Tu1 

wan. Shut or~ 

11J)!).OCC '\Gtl\l,Ot:a 1'MC-.OJO 

aso ooot llfiJ.oot~ tOOO >~ 

1cr.Kl.CCO 100Q.Wi) i ':CC-·)00 

10?0.00~. 1.9oeit.c31 t!U:.~ 

---....... . . "' . ~ .. : ;: '·=•:!•! 

VESOI2 144 
~­ .: .. ·~ 

·;<. ·· . ·NYX 

Slalll< 02 RCRA 4.000000 MOOOOO 

HCUoLtme 3l1.0000D 33.5QOOO 37.20000 

Stlred<lt~ Wejglll 

Tompemo CluunborTemp 800.0000 1200.000 

PCC Temp 1300.000 U'K'I.Cli.HI 

SCCTemp ~ tl:lG.CC)t 

Shock co CoiTOC!e6 ~.'1000 ~0 

Stack HCL Comcted 100.0000 110.0000 

StocK In CCITG<lled 4.tlOOOOU 

Sl.od< Flow ........ loW BTU Liqui<l Weight 

Hlah ElTU IJQul.d Well)hl 

Uquld Welgllt 

Contotnedzsd W"'9ht 

SoRds Weight 

wetght 

• 

9 v: .. Eo~~ Scniecs 

Sw Uliooio 

I 

t:mi.UOD 1815..003 

1901..000 189tl.OOO 

lJ<I.OCCOG nu.mo 

2G.IJOOCC 32.00000 

17ooo.tt S7«o.oo 3.8CtJ.~ 

I 

Z&OO.Q)) 5CSIVJOO ~JXII) 

1030JX).) 

1o<l<l0.00 

t:zooo.G-O 13\'XIO ~ 1nge.co 

Ctcato<! 

Pt.'iOll Stolt 

PtCodW 

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1!11201~ 5:0~ AM 

1/l/ 2010 6.'00 AM 

tn,"<-:ao 6:<:0 .\.\! 

?~e6C'!7 

Ul'JOO.'O 1~.~ .IOCJ.cA> 

\1!00.1100 16Ci:U.liC 1lC0,07,1 

1000.£100 '!:l!SO..tilO ~1 CO OO(l 

2jiO.CJOC D6Cl.CW ~J:C'C 

uooo.co 14000.00 ~tiCOO.OC 

-- ~·.:·'t. . -;-:--:-· 

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VES012148 
Certification Statement 

I certify under penalty ofi!Je law thai this document wos prtpared under my direclioo or 

supervision in accordance with a system designed to assure that qualified per>OMel properly 

gather onrl evaluate the infonnation submitted. Based on my inquiry ofthe person or persons 

who mallllgc the system, or those persons directly responsible for gathe<ing the informal ion, the 

informalion sublnlned is, to !he best of my knowledge and bdio( true, accurate, and complete. 

I am aware that thete are significant penalties f:or submitting false infonnation, including the 

possibility of line ond imprisonment for knowing violations. 

,...... ~ !l. Lj Doug Borris 

GenerAl Maa~ger 

Veolia BS Technical Solutions. l.l.C. 

Sauget, IL 

. ··'·. 

9jn I 12. I 

i 

. ' 

,, 

I 

,. 

! 

I. 

I I. 

VESOJ 2149 
· ... : . .; •,. • " . • , .. , .. . · .. :.. . . . " l <" • : . : • • • • • • '. : · 

Notification of Compliance (NOC) 

for Veolia ES Technical Solutions Units 2, 3, & 4 

40 CFR 63 Subpart EEE 

Hazardous Waste Combustor MACT Standard 

Compliance Date: June 18-25, 2012 

Owner/Operatorffitle: Vcolia ES Technical Solutions, L.L.C. 

Street· Address: 7 Mobile Avenue 

~~-- -------------------- City: Sauget State: IL Zip Code: 62201 

-------- ------------ Plant Name: Veolia ES Technical Services, L.L.C. 

;.: 

( 

[ 

I 

t 

l 

l 

Doug Harris I General Manager 

-=-- ....... --------·--========================---- Plant Con met I Title: 

I 

I. 

Pla.nt Address (if difftrent tban owner/operator's) i 

Street Address: 

City: State: Zip Code: 

Major or Are• Source This source is located at a facility that is a major source of Hazardous 

Air Pollutants. 

. ......... ____ _ 

2 

l 

' 

I 

VES012150 
I : .; __ ,_) -••• 

Introduction 

Veolia BS Tc:cbnical Solutions, L.L.C. in Sa.uget, Dlinois (Veolia-Saugtt) openr.es mroe (3) 

incinerators: two (2) fixed hearth units (Units 2 and 3) end one (1) rotlry kiln unit (Unit4). All 

tllree units opera~<: under Title V Penn it Number Y·IL-1716300103-03-0l i""''ed by U.S. EPA. 

Region 5. Each incinerator is subject to the Notional Emission Smndards for Hazardous Air 

Pollutants (NESHAPs) for Hazardous Waste Combustors (J'itle 40 of !he Code of federal 

Regulations, Part 63 (40 CF!t \'art 63), Subpart EBB), i.e., the HWC MAC I'. Per the 

requirements oftt1e HWC MACf at 40 CPR 63.1207(d)(2), a Confirmatory Performance Test 

for polychlorinated dibento·p-dioxlns and polychlorlnoted dibenz.ofumns (dioxinslfurans) must 

be conducted within the 31-month period following the oommeneement of the previous 

Comprellensivc Pufonnancc Test. 

The previoos Comprehensive PerfOCTnonce Test for the Unit 2 Incinerator began on December 8, 

2009, which required the Confirmatory Performance Test (CfP'T) to begin by July 8, 2012. 

Veolia-Snuger commenced the Unit 2 Ctl'T onlunc 18,2012. 

Tbe previous Comprehensive Performance Test for the Unit 31ncinerator be!Jlln on December I, 

2009, which required lhe Confirmatory Performance Test (Cfi>T) to begin 

Veoli3..Saugct commenced the Unit 3 Ctl'T on June 20, 2012. 

The previous Comprehensive Performance Test for the Unit 4 Rolm}' Kiln Incinerator began on 

December 16,2009, which required the Confirmatory Performance Test (CCP1) to begin by July 

16,2012. Veolia-Snuget oommenced theCfPT on June 25, 2012. 

The 40 CFR 63 Subpart EEE emission standards that are applicable to these units are specified in 

Table 1. 

Ta .blo 1. 40 CFR 63 Subpart EEE Emissions Standards 

P~rameter Limit 

0.20 ng TEQ!dscrn, corrected to 7% oxygen for incinerators 

with dry air pollution control system and inlet temperature to 

initial particul•te matter control device >400.F; 

·-··· .. Diox:ins-and-Furons ···- - -- ·-· .. -----or-,--·-... · ·· . ........ 

0.40 ng TEQ/dscrn, corrected to 7% oxygen for incinerators 

with dry air pollution control system ftn~ inlet temperature to 

initial particulate molter control device <400'F. .. 

3 

j: 

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.. 

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I 

- .. ·--·- l 

I 

i 

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VES012151 
.·.· . -~~- i . .: ..... · ... · ..... .. ~. . ..... ~ 

The applicable dioxjns/furans standard oft he liWC MACT for Units 2 and 3 is 0.20 ng 

TEQ/dsan, corrected to 7% oxygen, and the applicable dioxinslfurans stzndard of the H WC 

MACT fO< Unit 4 is 0.40 ng TEQ/dsan, correded 10 7% oxygen. These stand...ts were mel 

during the ConDrmatory Perfunnance Tests of Units 2, 3, 8lld 4. 

Results of Confirmatory Performance Tests 

The results of Ole Confirmatory Performance Test are provided in Attaclunent I, Floal Reports, 

Dloxlns/Furans Confirmaiory Performance Test Report for the Unit2 Fixed Hea1th Incinerator, 

Unit 3 Pixc<l Hearth Incinerator, and Unit4 RotAry Kiln daied June 2012. The Co11firmarory 

Performance Test reports Include: 

• The methods thl!t were used to dotermine compliance; 

• The results of the performMce tests, continuous monitoring system (CMS) 

performance evaluations, and other monitoring procedures that weno conducted; and 

• The ernissions of dioxins!furans, reported in units and averaging times, and In 

"ccordnnce with the test methods specified in Subpart BEE. 

Table 2 summarizes the results of the emissions Slmpling during the June 2012 Co ii mat~ry 

Performance Tests of Units 2, 3, and 4. 

Table 2.. Summary of HWC MACT Confirmatory Ptrformance Test Results 

Juno 2012 

IIWCMACT Test Method Unitt U•it 

Anr11gcTdt 

Stl.l•d•rd lte~utt 

Unh 2 0.20 0.00t78 

Unit 3 Dlox!ns/FuJall.$ EPA SW 8~6 ng TEQ/tlscm. 0.20 0.00068 Medtod 002lA oorrcctod co 1% 0; 

Unlt4 0.40 0.195 -

' r 

I 

I 

L 

... '------·----·---

4 

VES012152 
.. I . ··. 

•.) 

') 

. \ 

~ 

• •••. J ., .... . ... 

Operating Conditions 

In section 63.1207(b)(2), the HWC MACf states that "you must conduct oonfinnatory 

performance tests to: (i) Demonstrate complinnce with the dioxinlfuran emission standard when 

the source operates under normal operating conditions". "Normal operating conditions" are 

defined as: I) the average carbon monoxide emission level over the previous 12 months to the 

maximum allowed; 2) the operating limits established to maintain compliance with the 

dioxin/furan standard within the range of the nvernge vulue over the previous 12 months and the 

maximum, or minimum, allowed; and 3) chlorine feedrl\les at normal or greateo·. As such, no 

new or additlol\81 operating limits (OPLs) were established during this confim1a1ory perfonnw•cc 

lest. 

The approach for accomplishing the CfPT objectives was 1o operate the Units 2, 3, and 4 

incinerators at a single test condition represenmtive of typical operations. To accomplish this, a 

mix of waste streums that were representative of typical operntions were fe<l tO the incinerator, 

and the following parameters were operated between the previous 12-momh average and the 

maximum, or minimum, allowed, i.e., the OPI.s: primary combustion chamber temperature, 

secondary combustion chamber temperature, bagloouse inlet temperature, total hazardous waste 

r 

t 

I. 

I 

f 

I 

' I 

feedrate, total pumpable bazirdous waste fcedrate, staCk gas flowiile, carbOn ihJOCiiOnrate{'"'O"'n"•t ______ _ 

4, only) and the toc-1 chlorine feedrate. A variance was requested and apvrovcd for the 

eor.ceotralion or carbon monoxide (CO) In the stack gas to allow the operation of the incinerntor 

to maintain the CO concentration below the HWC MACf emission limit of 100 ppm corrected 

to 7% oxygen. Tables 3, 4, and S present the results of the key paramettl'3 monitored during the 

Cfl>Ts for Units 2, 3, and 4, respectively . 

s 

VESOI2153 
•; 

' ··.~ I , '' - . . - - TAble 3. Summary of U it 2 Operations 

' A vente Tarce~ Optndn~ 

OpuJtJng Parameter Ubi II Ru11 1 •• z R:nn l Durin: lbnc< f•tg<t 

• CIPT Achieved! 

lh&)\ouse [nld Te perature (HRA) •p •os.t 05.2 

.. 405.0 405.1 400 - 42U y.,. 

ftrlmary Ccunbuni 

(HR.Ai 

~ Clu\mbec Temperntu:e •F 1,750.5 I 4U 1,746.6 1,748.6 1.~ 1.~36 y.,. 

S.co~~ary Combu; ion Chamber Temperature •F 1.895.1 1 95.3 1,895.0 1,39H 1,917 - 1,S71 y,. IHRA -· - Stael Cazbon Mur.l.xJde (liRA) ppmv(7%0a 0.6 1.S 1.4 1.2 0- 100 Yes con'CC'.td) 

SiAcl< Qu Flowrue (HRA) •c.fm 14,063.1 t41 m.s 14,074.3 ,.,103.6 U,JI7 - 15,147 y.., 

St1c:k OX)'itn Cor.c"mtn.lioa % II.J 0.9 11..2 11.1 NIA NIA 

; 

Olorine Food (HII!AI lblhr 61.1 1.1 I 61.l 61.4 36.0-211 Yes 

I • I 

I Pumpable Wuo.: Feed (HRAl 

i 

lblhr 1,950.9 I ~67.2 1,972.7 1,963.6 1,371-3,107 Yes 

To<ai w .... Feed tR.Al lbllu 2,173.6 2 139.5 2,188.1 2,133.7 1,761-4,017 Yes 

" ! 

HRA - Hourly Rollina A """8• 

I 

I :• 

6 

'• 

··--· ·--1.--,-,_---· ---- ·-·---···· - ··· -:--· ... ·: 1' 

...... _______ ""·-;::;:--

VESOI2154 
' 

' 

Table 4. Summary of U~it 3 Operations 

Opttotfnc ' P"r•:tndeT Untu Ru•l I F. n2 Ru.JI.J 

8teJ\OU!t Inlet Tcf119c:rablrc (HRA) •p 406.3 5.3 404..5 

ri ry ComiJU!Itkm Chamber l emperan.ue 

IHRAl ' 

•f 1,78~6 I, SH 1, 93 -~ 

ScCOndory Combu)tlon O. ba~· Temperature 

JHI\Al ' 

•F ,90 · I OS.O 1,905.! 

SlACk CArbon Morioxide (HR.A) ppmv (7~ O, 0.0 M 0.0 co~) 

Sloclt Gu Flo..,..!O (KRA) ec!m IA.$03.1 ~~47.8 14.051.4 

Sto<t O•rJ<l' eo.;..ruruion % IU 2.9 ll.l 

CllloriM Fcod (HJ!Al 

- 55.1 6.0 61.0 P_.t>!e w .... P.ee<~ (1!1\A) '"' 1,902.1 I $1.0 1,913.6 

Tolal Wu;e Feed (HRA) IMu- 2,l0l.9 z •ao.t l.lll.J 

HI\A Hourly Rolling Average 

I 

7 

Annce Tfl.t'ftt Optntin& Durfn& 

Cfi'T Range 

405.4 39? -420 

1,787.9 1,&65 - 1,686 

1,905.1 1,9 13 - 1,8;1 

o.o 0- tOO 

14,234.1 U,-'99 - u.1•1 

12.9 NIA 

S1.A l?.S-211 

1~.5 l,S62 - l,l07 

2.161.• 1,76&- 4,017 

,..~ .. Addrved? 

Yes 

Yes 

v .. 

v .. 

v .. 

N/A 

Y:s 

v .. 

y.,. 

··' F-

> 

;-

· 

~ 

; 

!· 

• 

·---··~, "-~--· .. ~--· --• .--: · - .----··- ·~ .-- 1~~-

VESOI2 155 
·' ... : 

,, " 

I 

OpcndDJ: Panmettt 

8qhOUJe Jntet T (HilA) 

I = Comb..Con Cl>amlle< Tem-e 

s-nd..-y Comt..otlon Clwllb<rT....,.......,. 

) . Stocl<. Cori>oo Mo+-(KRA) 

St.ck Q., Flovo'nole (liRA) 

Catbc:m Fcccl. ~ 

Stact .~tygen eoqccntr•\ion 

Chlonne Feoc! QiAA) 

Pulllj)>ble WaJ1< feed (HI\Al 

Total Was~e Fe<d !HilA) 

Secondary CornbJstion Chambe: Liquid Fr.td 

(HRA) 

-

HRA- hourly rolllnr ftver~ne 

i 

Table 5. Summary of U~it 4 Operations 

U•tu R.a•) +l Ru:.3 

'F 3!9.1 *9.3 319.3 

"f 1.661.9 1~59 1 l.111.3 

•p I,I9U 1f0l.O 1,902.2 

ppnv (7%0, 0.1 I 0.1 (;Ocfet.ltd) 

.am 35,l90.i l ,m.a 35,602.9 

lblhr 6.7 !6.7 6.7 

% 13.2 2.9 I !3.0 

lblbr 118.6 !20.1 113.2 

lblhr 1,66;.5 I 741.0 1,73!.7 

lblbr S.lS9.l 5 800.1 5,953.0 

lblllr 540.0 42.9 510.3 

8 

--·-'-

Anra&f Tust.e Open tine ,..,, .. DuriDc IW>~· Ac:bltvtd? CIPT 

319.1 l iA -400 v .. 

l,6SS.I U6S - 1,499 v .. 

1,900.5 1,917- I,U6 v .. 

0.1 0-100 va 

35,329.1 3l,439- l7.432 y., 

6.7 7.26-6.2 v .. 

\ 3.0 NIA N/A 

119.0 !1.2-229 v .. 

1,7 14.4 !.336-3,291 y., 

5,704.1 •..Jl5- 12,897 Yeo 

. 

531.1 •oo- 1,176 Yes 

--· -- --- ·- ·- ·-- ·---

..... .; ' 

< 

VESOJ2156 
... .;;~ .) ... ~ :~:. ..... . . .:. ~---'····- .... ' . 

Hazardous Waste Residence Time 

Because of the f=d·hearth narure of the Units 2 and 3 lncinenttors, >Oiid waste ruidence time is 

based on the elapsed time between solids chl'l!CS or tho travel length of the ash ram feeder, 

which functions to clear the primary combust.ion chamber of solid waste residue. An elapsed 

time of one hour or an ash ram travel length of II 0 inches have been established as the criteria 

for determining when solid waste is no longer in the combustion zones. 

Since atomized liquid wilSie vaporizes almost instantaneously upon entering the combustion 

chambers, the residence time of these wames is much less th"" for solids. During the Units 2 and 

3 Cfi>Ts, the incinerators were operated at normal conditions. Liqllid and gaseoos wastes 

entering the Unit 2 incine~r demonstrated a residence time of approximately 5.4 seconds. 

Liqllid and gaseous W8$tCS entering the Unit 3 incinemor demonma!ed 8 residence time or 

approximately 5.4 seconds. 

The hazardous waste gas residence time for Unit 2 i& calculated as fullows using the throo-run 

average for the stack gas flowratc during the Unit 2 Cf'PT: 

-.-\-----:-. -.p..:,:r:,m=ary="'tom"' busl'ion CliamDe'fVi!lifri\'o·= ---·--------

\ I 

• Secondary Combustion Cbamber Volume - 635 It'; 

• Total Volume - 1,270 It'; 

• Average Flue Gas Flownore -I4,IO<Iacfm (235 ft'tsec); and 

• Total Combustion Zone RC$idenee Time • (1,270 ft'}/235 ft'l!l<c) ~ 5.4 sec. 

The hazardous waste gas residence time for Unit 3 is calculated as follows using the three-run 

average for the stllck gtL'i llowr&te during the Unit 3 Cf!YI': 

• Primary Combustion Chambeo· Volume - 635 It'; 

• Secondary Combustion ChambcrVolume-635 fl'; 

• Total Volume - 1,270 111

; 

• AvetUge flue Gas Flowrate- 14,234 acfm (2371\'/sec); and 

• Total Combustion Zone Residence Time .. (1,270 ft'}/237 tl1/sec) • 5.4 see. 

Solids residence lime in the Unit 4 !din i~ dependent upon the kiln rotation rate, solids bed depth, 

-;;r,; ~umbef of other parameters set by design .• The ni..Xi.;.\;m'solids hazlliXtous w.Stt' residence __ , .. 

time for Unit 4 incinerator, i.e., in the rotBry kiln, is 30 minutes based on calculations using an 

equation front Chemical Engineering Handbook, Perry's 5"' Edition. 

9 

f, 

.. 

f 

0 

,, 

'· i !: 

i 

l 

' 

VES012157 
. . 

' . 

~: .• :::::~y-~:·_···-e-.•. ;•· I • ·-·· ;_;_ .v:_ . . -...·.· 1 •• •• ' I • •·-· ··· 

Since etnmlztd liquid waste voporizcs almost inSiantaneously upon entering the combustion 

chambers, liquid and gaseous "'-aste entering the ineollCI1.tor has a resldenu time of 

epproximattly 7.5 seconds. 

The hazardous Wa>'le gas residence time for Unil4 is eolculated as follows using the three-run 

average for the stack gss flowrare during the Uni14 Cfl>T: 

• Primary Combustion Chamber Volume- 1,346ttl; 

• Sceondary Conobustion Chember Volume - 3,01!4 ft'; 

• TOlAI Volume - 4,430 ft3

; 

• A •cragc Flue Gas F~wrn!e 35,329 aclln (589 tt'lsec); and 

• Total Catnbustion Zone Residence Time • (~.430 ft') /589 ft'l'llce) •7.5 sec. 

10 

i 

I 

• I 

L 

I 

,. 

!: 

!. 

I· 

I 

I 

I 

I 

1 

• 

VESO I2158 
VES012159.pdf 
APPENDIXF 

CONSTRUCTION PERMITS 

VES012159 
' ' 

( i 

~ Illinois Environmental Protection ,Agency · 22M Churchill Road. Sprin,..r.eld, CL 62706 

217/782-2113 

CONSTRUCTION PERI4IT 

PERMITTEE 

'Trade Haste Incineration 

Attention: James L. Gary 7 Mobile Avenue 

Sauget, Illi noi~ 62201-1069 

Application.No. : 83120053 Ap~llcant's Designation: S~ject: lwo IWI-2000 Incinerators 

Date Issued: September 2, 1986 

location: II Mobile Avenue, Sauget 

1.0. No. : 163121AAP 

Date Received: June 9, 1986 

7 

. 

Permi t is hereby granted to t he above-designated Permittee to CONSTRUCT 

emission source(s) ana/or air pollution control equipment consisting of two 

TWI-2000 Series z·Hazardous Waste Incinerators one with a Joy Spray Dry Adsorber and fabric filter, and t he second unit wi-th .a Venturi Scrubber, 

Cyclonic Hater Gas Separator, Induced Draft fan, and Exhaust Expansion Tank as 

described in the above-referenced application. This Permit is subject to 

standard conditions attached hereto and the following special condition(s): 

1. The incinerator when constructed shall include a Haste Feed Interlock Sy~tem to insure that waste is not fe~ to the incinerator· unless all 

critical operating parameters are with acceptable limits. As part of this 

system stack monitors shall be installed on each incinerator for Oxygen, Carbon Monoxide, and Hydrocarbons. For the incinerator with the SOA. the 

following t\<10 additional emission monitors ·are required: Broken Bag Detector and hydrogen chlc.ride mon1tor. 

2. Particulate matter emissions from the incinerator shall not exceed 0.08 

grains per dry standard cubic foot of gas discharged to the atmosphere, 

pursuant to 35 !11. Adm. Code 121 .181(b). 

3. Carbon monoxide emissions from the incinerator shal l not exceed 500 parts 

per mill jon , corrected to SO percent ex~ess air, pursuant to 35 111. Adm. Code ?16.141. 

4. Hydrogen chloride emissions from incinerators 2 and 3 shall not exceed 4 

lbs/hr or the control devices shall demonstrate a minimum HCL removal ' efficiency of 99i . 

VES012160 
' ,. 

@ Illinois Envlronment!il Protection Agency ·; 2209 Churchill Roaa. Springfield. JL 62706 

Page 2 

5. The new incinera1;0rs shall be constructed and operatedyith a waste cutoff 

interlock syst€\11 which will prevent introduction of waste i nt o the 

illcinerator \4h en any of the follow!~ events have occurred. 

a. 

b. 

c. 

d. 

e. 

f, 

g. 

h. 

i. 

j. 

I.D . fan f ai lure. 

Atomi zing air' pressure el ~»r 10 psi g. 

Incinerat or chamber pressure 2" w.c. above atmosphoric for more than 

5 seconds. 

Emergency stacK opens. 

fail ure to sustain oper ating par ameters specified in special 

condition 3. 

. Bu rner failure in t he P.rimary or secondary cham.ber·. 

When primary c.hamber temperature ·fal ls below 15oo•r or secondary 

chamber exceeds 227s•r. 

Carbon monoxide concentration exceeds 500 ppm or exceed 50 ppm for 

POre than thr ee minutes, 

For The I nci nerator With fl Venturi Scrubber 

Quench >ta ter f1 ow be 1 ow 100 gpm. 

Venturi scrubber water below 37 gpm, pressure drop across Venturi 

scrubber less than ~ w.c. , scrubbe r pH ]ess than 6 and fl ue gas 

temperature ent ering the scrubber greater than 1so•r. 

For The lnc'inerator \lith fl .Spray Dr,Yer. Adsorber 

k. Loss of slurry flow to SOA. 

1. High hydrogen chlori de concentra tion. in the stack. 

m. High opacity as indi cated by the broken bag detector. 

n. High inl et temperature to the fabric filter . 

6. The incinerators and associated air pollution control equipment ~ll. be 

Constructed such that thl! values of the parameters· being monitored .are 

diSplayed· for operating pers<iMel . 

7. Operation of the incinerator utilizing auxiliary f uel will be limited as 

to composition and incinerator operati ng conditions whicb will meet .Jill 

applicable regul ations. Such a reque·st shou ld be incorporated in the ·-"-·' tria 1 bur.n p Jan. 

VES012 161 
@ Illinois. Environmental Protection Agency · 2200 Churchill .Road, Springfield, IL 62706 

Page 3 

8. Trade ~laste Incineration shall sub111it as-built plans and specifications to . < the Agency as part of their operating permit application. 

9. Prior to operation the new units, 2 and 3, shall be tested PVrsuant to an 

Agency approved trial burn plan. Trade Waste Incineration shall submit a 

detailed trial burn plan for Agency approval prior to startup. The trial 

burn plan shall provide for de1110nstration ·of the incinerators' destruction 

and removal efficiency, and particulate matter, carbon monoxide, organic material, and hydrogen chloride emissions throughout the range of waste 

characteristics and incinerator o~rating parameters for Wfiich an 

operattng permit •1111 be sought.uch trtal burn plan should also 

indicate period of operation of incinerators during shakedown and 

testing. Standard condition 9 which allows 3Q day~ for shakedown and 

testing, is hereby superceded by this condition. 

An operating permit will only ·be issued for these incinerators after a 

trial burn has demonstrated compliance 1'iith all applicable regulations. Based upon tri al burn operation and waste material burned, the operating permit may limit the incinerator.operating parameters and the composition 

of the incinerator's waste feed. 

10. As part of the trial burn plan, Trade Waste Inci neration shall propose 

pro.cedures for maintai ning operating records. Such procedures shall 

include appropriate noti fication to the Agency and action to be taken by 

operating personnel in the event of equip~nt malfunction or breakdown . 

11. Emissions of particulate matter (TSPl , sulfur oxides (502)., nit1'9gen 

oxides (NOxl, organic ma terial (0141 and carbon monoxide (CO) shall not 

exceed the amounts specified in the Table bel ow. 

Emission 

Source 

Existing Incinerator 

New Incinerators 

Storage Operations 

Annual Emissions (Tons/Year) 

TSP S02 NOX ~ CO 

15.0 

30.0 

7.7 

15.4 

4.0 

8.0 

0.9 

. 1.8 

6.9 

6.6 

13.2 

These limi ts are bas.ed on the potential emissions of the i ncinerators and 

storage as indicated ·in the permi t application. 

hur, P. E. 

Manager, Permit Section 

Division of Air Pol lution Control 

BM:JOC: jmm/1857F/25-27 

cc: Region 1 

VES012162 
~ Illinois Environmehtal Protection Agency · 2200 Churchill Road, Springfield, IL 62706 

' . \ . J 

217/782-2113 

CONSTRUCTION PERMIT 

PERMITTEE 

Trade Waste Inciner~tion, A Division of 

Chemical Waste Management 

Attention: James L. Gary 

7 Mobile Avenue 

SaUget, lllinois 62201-106!1 

~~~~~;: -~87100024 I .D. No. : 163121MP INCIR Date Received: May 24, 1988 

2, l ncinerator 

August 19, 1988 

Mobile Avenue, Sauget, Illinois 

Perm! t f s hereby granted to the above-designated Permi'ttee to CONSTRUCT 

emission source(s) and/or afr pollution control equipment consisting of 

Incinerator 13 Model TWI 2000 with associated Dry Scrubber as described in the 

r above-referenced. application. This Permit is subj~ct to standard conditions 

attached hereto and the following special condi tion(s): 

1. particulate matter emissions for the Incinerator shall not ·exceed 0. 08 

grains per dry standard cubic foot of the gas di stpar!{ed to the 

atmosphere, pursuant to 3o Ill. Adm. Code 121. 181(b). 

'2. Carbon JOOnoxide emissions from the Incinerator shall not exceed 500 parts 

per mi llion corrected to 50 percent excess air, pursuant to 35 111. Adm. Code 216.141. 

·J. The incinerator shall be equipped with sensors to monitor the fol101<tng parameter's: 

a. Upper and 1 ower combustion chamber ex l t gas tetllpeNture. b. Upper and lower combustion chamber pressure. c. Spray dryer ad.sorber inlet temperature. d. Spray dryer adsorber outlet temperature. 

e. Lime slurry head tank liquid level. 

f. Water pressure to slurry head tank makeup. 

g. 8aghouse tube sheet pressure drop. h. Combustion stack gas flow rate. 

l. Stack gas oxygen concentration. 

RECEIVED AUG l S 195& 

VESOI2163 
@ lll·inois Environmental ProlecLion Agency 

Page 2 

2200 Churchill Road, Springfield, IL 62706 

j. Stack gas carbon 00noxide concentration. 

k. Stack ga·s total hydrocarbon concentration. 

J. Stack gas HCL concentration. m. Stack gas opacity. 

n • . Liquid and/or ·sludge waste flow rate into the incinerator. 

o. Solid l>'aste charged .. p. Primary fuel pressure. 

q. Conbustion air pressure. r. Primary Bomer & Pilot flame. 

s. Secondary Burners & Pilots flames. 

t. Emergency stack latch. 

4. The incinerator shall be designed and constructed to orrate with an 

aut001atic waste feed cutoff interlock system which wil prevent the 

introduction of waste into the incinerator when operating outside the 

permitted range of parameters. 

a. Startup range of parameters are established based upon design specifications and perfonnance tests conducted on Incinerator Unit 2 

and can be changed after successful stack test demonstration on Unit 

3. 

(1) Primary chamber below l60QOF. (2) Secondary chamber bel ow 18000F. 

(3) Primary or secondary chamber above atmospheric pressure. (4) Spray dryer adsorber inlet greater than 22000F. 

(5) Spray dryer adsorber outlet greater t han 4000F or below 

3700F. 

(6) Low liquid level in lime slurry head tank. 

(7} low makeup water pressure into slurry heat tank. 

(8} Baghouse tube sh4!et pressure drop greater than 10 inches water 

col UlAn. 

(9) Combustion stack gas flow less than 5,000 acfm or greater than 

15,000 acfm. 

(10) Oxygen concentration less than 6$ by vol ume. (11 J Carbon monoxide concentration greater than 500 ppm. (12) Carbon monoxide concentration greater than 50 ppm for 3 rrtnutes. (13) Total hydrocarbon concentration greater than 100 ppm corrected 

to 7'{, oxygen. 

(14) HCl concentration greater than 100 ppm for 1 hour. (15) Opacity greater than 10$. 

(16) Primary fuel pressure below 30 psig. 

(17} Combustion air pressure below 10 inches W.C. (18} Primary burner failure. 

(19) Secondary burner failure. 

(20} Emergency .stack open. 

VES012164 
~ Illinois Environmental Protection Agency · 2200 Churchill 8ood, Springfield. IL 62706 

Page 3 

b. Operating parameters will be established based upoQ evaluation of 

actual operation and measured emissions during a trial burn. 

5. The inciner~tor and associated air pollut·ion control equip~~~ent shall 

be constructed such that the values of the p~ra~~~eters monitored 

and/or indicator of acceptable status are displayed for operating personnel with audible and visual ala~s. 

6. The Permittee shall su~it as built plans of the incinerator arid air 

pollution control equipment as part of the operating permit application. 

7. The Permittee shall not initiate the start-up of the incinerator withoot 

written approval from the Agency. This special condition supercedes standard condition 6(b). 

B. Stack emission tests shall be conducted on this Unit 3 Inci~erator to 

establish emission rates and compiiance with the applicable regulations. The required stack tests are to be conducted by an independent tester. 

a. Emission tests are required for the follm<ing pollutants: 

(1) Particulate Matter. (2) Hydrogen chloride. 

(3) Nitrogen oxides. 

(4) Carbon Monoxide. 

(5) Principal organic· hazardous components. 

b. The Permittee shall sub111it a stack test pl~n &t least 60 days in 

advance for Agency approval. The plan shall contain detailed plans 

and procedures. 

c. Written notice of· the scheduled dates for compliance stack ~e~tjng 

shall be given at l east 30 days in advance to the Agency. Final 

notice shall be given verbally not less than 7 days before e~isslon 

testing begins. The required notice shall be given to the follo'lling: 

Illinois Environmental Protection Agency Attn: Permit Section Manager 

Division of Air Pollution Control 

P.O. Box 19276 

Springfield, Illinois 62794-9276 

217/782-2113 

Illinois Environmental Protection Agency Attn: Source Emission Test Specialist Division of Air Pollution Contro.l 

The Intercontinental Center 

1701 First Avenue 

Maywood; n lfnois 60153 

VES012165 
\. . 

. ~ Illinois Envii·onmental Protection Agency · 2200 Chun:hill Road, Springfield, IL 62706 

Page 4 

Illinois Environmental Protection Agency Division of Air Ppllution Control - Regional Office 

2009 ~ 11 Street 

Collinsville, Illinois 62234 

618/345-0700 

9. Prior to startup, the Permittee shall submit instrumentation and 

monitorjng specifications. A proposal for the details of record keeping and report formats used to show compliance with the limitations of the 

operating parameters required to be monitored in special condition 3 of 

this construction permit shall be submitted to the Agency for approval. 

a. The instrumentation and· data logging equipment shall provide for 

storage of 100% of the incinerator parameters and stack monitored 

results in a computer readable fomat. Copies shall be made 

available to the Agency in a suitable computer readable format. 

b. The data logging equipment shall also provide for recording ~taste 

analysis parameter for as burned waste streams: 

c. The data logging ~quipme t shall provide real time access to the 

incinerator operating parameters through a telecommunication computer 

port. 

d. The proposal shall set forth the hardware and software sp~cifications 

for the information system along ~ith available options in report formats and data exchange media. 

e. The permittee shall install a computer l inkup system with !EPA 

Springfield, !EPA Col linsville and some location with public access. 

Such a system and location will require Agency approval. 

10. Prior to startup, the Permittee shall submit details of an operator training pragram for Agency approval . 

·11. Prior to startup, the Permittee shall submit for Agency approval, specifications for on-site security including video cameras, monitoring 

cabinet locks and seals and details of security fencing . 

12. Emissions of particulate 111atter (TSP), sulfur oxides CS02l, nitrogen 

oxides (IIOxl, organic material (OM), and carbon monoxide (CO) shall not 

exceed the amounts specified in the Table below. 

Annual Emissions (Tons/Year) Enii ssion Source TSP S02 NOx or~ co 

Incinera tor Unit 1 15.0 7.7 4.0 0.9 6.6 

Incinerator Unit 2 15.0 7.7 4.0 0.9 6.6 

Incinerator Unit 3 15.0 7.7 4.0 0.9 6.6 

Incinerator Unit 4* 16.92 50. 76 61.6 3.1 13.68 

Waste St orage 

VESOI2166 
~ Illinois Environmental Protection Agency • ~200 Churchill Road. Springfield. IL62706 

P.age 5 

*These 1 im.its are establis~ed !>a sell on 7205 hours of qperiltlon per year and average emission rates given in the applic~tion. These limits will be 

revised after the stack test results are reviewed. 

13. Prior to startup, the permittee shall provide details of the Quality ·Assurance/Quality Control programs for the monitoring systems specified in 

Special Condition 3 above for Agency approval. 

Please note that the start-up and trial burn plan as submitted with the 

application is not acceptabl e. Plan deficiencies will be identified at a 

later time. 

T11r A. Swelt r, .E. 

Manage , Permi tion 

Division of Air Pollution Control 

TAS:JDC:ds:5035H/32-36 

cc: Region 3 

VES012167 
[ 

j 

Julyl, 1985 

STATE OF.ILI.J!JOI.S. 

ENVIRONMENTAl PtlOTECTION AGeNcY 

OMSION OF AIR POU.tJllOH COHTROt 

2200 CHURCIII.l ROAD 

SPRINGREI.O, ILI,.IIIOIS 62706 

STANDARD CONDITIONS FOR CONSTRUCTION/DEVELOPMENT PERMITS 

ISSUED BY THE ILLINOIS ENVIRONMENTAL PROTECTION AGENCY 

The Illinois Environmental Protection Act (illinois Revised Statute.e, Chapter 111-1/2, s..,tion 1039) authorizes the 

Enviro-ental Protection Agency to impose ·conditlono on permits which it lsauea. 

The following conclitiona are applicable unl""' susperaeded by special condition <a). 

L Unlees this permit has been extended or it hno been voided by a newly iasued peTmit, this permit·willexpire one 

.Year from. the date of l_ssuance, unlesa a continuou.a program of construction or development on thJs project has 

otarte<i by such time. · ·, · 

< 

2. The c<inotruction or development .:Overed by this permit shall be aone in compliance with applicable provlaions of 

the Illinois Environmental Protection Act and Rerulatlons adopied by the llllnois Pollution Control Board. 

3. There shall be no dovlationo from the approved plano and opecificationa unleoe a written request for modillcation, 

along with plans and specUications aa required, shall have been submitted to the Agency and a supplemental 

written permit issued. 

4. The permiUee shall allow any duly authorized agent of the Agency upon the presentation of credentials, at 

reasonable times: 

a. to enter the permittee's property whore actual or potential effluent, emission or noise sources are located or 

where any activity is to be conducted pursuant to this permit, 

b. to have acceea ta and to copy any reeordo required to be'kept under the terms and conditions of tbi& permit... 

c. to IDSp""t, including during any houn of operation of eqa\pment con'structed or operated under this permit, 

ouch equipment and any equipment required to be kept., used, operated, calibrated and maintained under this 

permit., 

d. to obtain and remove eamples of any discharge or emi .. lono of pollutants, and 

e. to enter and utUite any photographjc, recording, testing, monitoring or other eqW~meot for the purpose of 

preserving, testing, monitoring, or recording aoy activity, discharge, or emiesion authorized by this permit. 

5. The issuance of this permit: 

a. shall not be considered aa in any manner affo<:ting the title of the premis .. upon which the permitted 

facilities are to be located, 

b. does not release thepermi<toe from any liability for damage to person or property caused by or resulting from 

the construction, maintenance, or operation of the proposed facilities. 

c. does not release the permittee from compliance with other applicable statute• and regulations of the United 

States, of the State of Illinois, or with applicable local laws, ordinances and regulations, 

d. does not take into consideration or attest to the structural stability of any units or parts or the project, and 

. 4k5n&0l.t!v. •ote5t ~»o.oM 

VES012168 
' 

DIRECTORY 

ENVIRONMENTAL PROTBICTION AGENCY 

DIVISION OF Affi POLLUTION CONTROL 

.__..)JulY I, 1985 

For aoql&ta.nce in prepariog a pertDil applie&Uon 

contact tho Pennlt SecUon, 

l!Uhoia Environmental !7otectioa Agoney 

Divia.ion of Air PoUutlo11 Coottol 

Pormit Soet!nn 

2200 ChurclUU Road 

Springfield, Illinois 62706 

C217J 782-2113 

or a regional omce of the Field 

Operations Section. The re.clonal 

omcea and their ue .. of reeponolbility 

e.re abown on tJLe map. The addrtuq 

and telephone numbers of the regional 

omcu are 88 follows: 

..-.. I 

llllnoia EPA 

ROI:ion 1 

JutorcpntlnenLfl]. Center 

1701 S. let Avenue 

MayY~ood, Ulinoia 60153 

(812) 346-9780 

Illinois EPA 

Roclon 2 

1>416 North Univ~mty 

Peoria, UIU.Olo 61614 

(309) 691-2200 

IUinoia EPA 

Re~on 3 

2009 Mall Stnat 

Collirurrille, Ulino!s 62234 

(618) 846-0700 

VES012169 
.i 

' 

~ Illinois Environmental Protection Agency 2200 Churchill Road, Sprin~field. JL 62706 

217/782-2113 

CONSTRUCTION PERMIT 

PERMITTEE 

Trade Waste Incineration 

A Division of Chemical Waste Ma nagement 

Attn: James L. Gary 7 Mobil Avenue · Sauget, Illinois 62201 

Appl~ation No.: 88010001 I.D. No.: 163l21AAP 

Apelicant's Designation: INCIN 14 

Su Ject: Transportable Rotary Kiln 

Date Issued: August 3, 1988 

Date Received: March 22, 1988 

Incinerator 

location: 7 Mobile Avenue, Sauget, IL 

Permit is hereby granted to the above-designated Pe~ittee to CONSTRUCT 

emission source(s) and/or air pollution control equipment consisting of a 

Transportable Rotary Kiln Incinerator Unit #4 equipped with a dry scrubber and 

a baghouse, as described i n the above-referenced application. This Permit is 

subject to standard conditions attached hereto and the fol lowing special cortdition(s): 

1. Particulate matter eini sslons from the incinerator shall not exceed 0.08 

grains per dry standard cubic foot of the gas discharged to the 

atmosphere, pursuant to 35 Ill . Adm. Code 121.181(b). 

2. Carbon monoxide enrisslons from t he incinerator shall not exceed 500 parts 

per million corrected to 50 percent excess air, pursuant to 35 Jll. Adm. Code 216,141. 

3. The incinerator shall be equipped wit~ sensors to continuously monitor the 

following parameters: 

a. Kiln and secondary combustion chamber exit gas temperature. b. Kiln and secondary canbustion chamber pre~sure. 

c. Spray dryer adsorber inlet· temperature. d. Spray dryer adsorber outlet temperature. 

e. Lime slurry feed tank liquid level low. 

f. Water pressure to slurry feed tank makeup. 

g. Baghouse tube sheet pressure drop. h. Combustion stack gas flow rate. 

i. Stack gas OXYgen concentration. 

j. Stack gas carbon monoxide concentration. 

k. Stack gas total h.ydrocarbon concentration. 

1. Stack gas HCL concentration. · m. Stack gas infrared absorption. n. Liquid and/or sludge waste flow rate into the incinerator. 

o. Solid ~1aste char~ed. 

VES012170 
~ lllfooj~ Ellvlronmenlal Protection Agency · 2200 Chu,chill Rood, Springfield. IL G2706 

Page 2 

p. Primary fuel pressure. 

q. C~ustion air pressure. 

r. Primary Burner & Pilot fl ame. 

s. Secondary Burners & Pilots f1 ame . t. Emergency stack latch. 

4. The Inc-inerator shall be de signed and constructed to operate with an 

automatic ~taste feed cutoff. Interlock system whi ch wi 11 prevent tile 

introduction of wast e into the incinerator when operating outsi_de the 

permitted range of parameters. 

a . Startu·p range of parameters are established based upon design 

specifications and perfonnance tests conducted on Inci.nerator Unit 2 

and can ~e changed after successful stack test demoostration on 

Unit 4. 

(1) Kiln chamber below 16oo•r. (2) Secondary chamber below 18oo•F. 

(3) Kiln or sec~ndary chamber above atmospheric ~ressure : 

(4) Spray dryer adsorber inlet greater than 2200 F. (5') Spray dryer adsorber outlet rea~ r thap 4oo•F or below 370°F. 

(6) lo~l li quid level in lime slurry feed tank. 

(7) low makeup 11ater pressure Into slurry feed tanlc. 

{8) Baghouse tube. sheet pressure drop greater than 10 inches water 

column. 

(9) Oxygen ~oncen ration less than 6% by voluue. (10) c·arbon mnoxide concentration greater th~n 500 ppm. (1 1.1 Carbon monoxide concentration grea~r than 50 ppm for 3 minutes. (12) Total hydrocarbon concentration greater 'than 100 ppm corrected 

to 7% oxygen for one hour running aver age. 

{13) HCl concentration greater than 100 ppm for 1 hour running 

average. (14) Opacity greater than 10%. 

(15) Primary fuel pressure below 30 pslg. 

(16) Combustjo~ air pressure below 10 inches W.C. 

(17) Kiln burner failure. 

{18) Secondary burner f ailure. 

(19) Emergency stack open. 

{20) Combustion stack gas floK parameters will be establi~hed at a 

1 ater stage: 

b. Operating parameters shall be established based upon evaluation of 

actual operation a.nd meqsured emissions during a trial burn. 

5. The incinerator and associated air poll ution control equipment shall be 

constructed such that the values of the parameters moni tored and/or 

Indicator of acceptable status are displayed for operating personnel with 

audible i!Od visual alal'"lllS. 

VESOI2171 
~ Illinoi.s Environmental Protection Agency 2200 Churchill Road. Springfield, I L 62706 

Page 3 

6. The Permittee shal l submit as built plans for the incinerator and air 

pollution control equipment as part of the operating permit appUcation. 

7. The Permittee sliall not Initiate the start-up of the incinerator without. written approval from the Agency, This special condition supersedes standard condition 6(b). 

8. Stack emission tests shal l be conducted on this Incinerator to establish 

emission rates and compliance with 'the applicable regulations. The 

requit·ed stack tests are to be conducted by an independent tester. 

a, Emission tests are required for the following pollutants: 

(1) Particulate matte.r . (2) Hydrogen chloride. 

(3) Nitrogen oxides. 

(4) Carbon monoxide. 

(5) Destruction of principal organic hazardous components. 

b. The Permittee shall submit a start-up plan and trial burn plans and 

procedures. Such a trial burn plan shall require the Agency's approval 30 days prior to any start-up pnd testing. 

c. Written notice of the scheduled dates for compliance stack ·testing shall be given at least 30 days in advance to the Agency. Final 

notice shall be given verbally not Jess than 7 days before emission 

testing begins. The required notice shall be given to the following: 

Il linois Eavironmental Protection Agency Attn: Permit Section Manager Division of .Air Pollution Control 

P.O. Box 19276 

Springfield, IL 62794-9276 

217 /782~2113 

Illinois Environmental Protection Agency Attn: Source Emission Test Specialist Division of Air Pollution Control 

Intercontinental Center 

1701 First Avenue 

Maywood, Il 60153 

312/345-9780 

Illinois Environmental Protection Agency Division of Air Pollution Control-Regional Office 

2009 Mall Street 

Collinsville, IL 62234 

618/345-0700 

VES012172 
~ Illinois Environmertal. Proteetion Agenty · 2200 Chu.-.:hill Road, Springfield. 11. 62706 

Page 4 

9, Prior to startup, the Permittee shall submit instrwnentation and 

monitoring specifications. A proposal For the details of record keeping 

and report formats used to show compliance with the limitations of the 

operating parameters required to be monitored in special condition 3 Qf 

this construction permit shall be submitted to tlie Agency for approval. 

a. The instrumentation a.nd data logging !lquipment shall provide ·for 

storage of 100$ of the incinerator parameters and stack m6n1tored 

results in a computer readable format. Copies shall be ~de 

available to the Ag_ency in a suitable computer readable format. 

b. The data logging ·equipment sha11 also provide for recording waste 

analysis parameter for as burned waste streams, 

c. The data loggl~g equipll\£!nt shall prollide real time access· to j;he 

incinerator operat ing parameters through a telecommunication computer 

p_or't. . 

d: The proposal shall set forth the hard\1are and software ·specifications 

for the information system along with available options in report 

formats and data exchange media. 

e. The permittee shall install a computer linkup system with !EPA 

Springfield, !EPA Collinsville and some location with public access. 

Such a system and location will requir e Agency approval . 

10. Prior to startup, the Per~ittee shall submit details of an operator training p.rogram for Agency approval . 

11. Prior t.o startup, the Permittee shall sub~it for Agency approval, 

specifications for on-site sec.urity including video cameras, l)lOnitoring 

cabinet locks and seals and details of security fencing. 

12. Emissions of particulate matter (TSP), sulfur oxides (SOz), nitrogen 

oxides (IIOxl, organic material (01~), and carbon lllOnoxide (CO) shall not 

exceed the amounts specified in the Table belo~'· 

Emf ssion 

Source 

Incinerator Unit 4 

Annual Emissfons (Tons/Year) 

TSP 502 NOx OM CO 

16.92 50.76 61.6 3.1 13. 68 

These 1 imits ·are establ !shed based on 7205 hours of operation per year and 

average emission rates given in the application. These limits will be 

revised after the stack test results are revie~ied. 

13. Prior to startup, the per'mittee shall provide details of the Quality 

Assurance/Qualizy Control programs for the monitoring systems specified in ... , Special Condition 3 above for Agency approval. 

VES012173 
~ lllinois Environmental Prol~c ion Agency · 2200 Churchill Rood, Springrield, IL 62706 

) Page 5 

TI1e Agency will review when amended the start- up plan and trial bum plans 

when they are received. 

TAS:JDC:jm/4932H/51-S5 

cc : Region 3 

VES012174 
July I, 1985 

STATe OF l.UNOJS 

E~AONMENT~ ptiO'{ECT'tON ~G£NCY 

btVISION ()F AIR POLLUllOH Caf4TROL 

2200 C+lJRCHLl ROAD 

SPRlNGFiil.D, U INOIS &1.71)5 

:Sl~N:9AR CONDITIGNS~R CONSTR:IlC'niON/DEVELOPMENT PERr.tlTS 

'IS&IJED 11Y THB ILL.INOIS ENViRONI\lENTAL PROTECTION AOENCY . 

The illinois Envll-onmental Protection Ac~ Ollinois Jtevised·Statutes, Chap~r U 1·112, Section 1039) authorJzes the. 

Envirt?nn1ental P.rotecijon Agency to impose conditions ~n permi\8 which it issues. 

The following .cqnditiona are .applicablc unless aUflpeneded by special condition(•). 

1. Unless this .permit has been extended or it has been voided by a·newly iasueil perm:it, this petr.nlt will'etpire 9ne 

yea:r from the date of issu8Jlce, unl~ a continuous program of construction or development on this project bas 

s~artea by su~lt time. 

2. The coostruction or devalopment covered by this permit shall be done In compliance with applicable proviaions of 

the llllnois En:Yironmental Protection Act and Regulations adopted by the Dlinois Pollution Control Board. 

S. Thera sha11 be·no deviations from the approved plans and spodfieati-ons unless a written requ.est for modification, 

along with plans and spe<:lfications as required, shall have been 6\lbmltted to the Agency and a supplemental 

writ teo parmi~ laaued. 

4. The permittee shall allow any duly authorized agent of the Agency upon tho presentation of credentials, at 

nasonab1e times: · 

a. to enter lhe permlttee'.s property where actual or potential ernuent, emission Qr noise sourcell are loca.ted or 

where any eelivi_ty i• to be conduc~ pursuant to this peTII)it, 

·b. to have access to and to copy any tecol'da l'equired to be kept under the terms a.nd conditions of tb.ia permit, 

c. .to inepect,.including during any hours of operation of equipment ton.structe<:l or operated under this permit, 

such equipment and any equipment required to be kept, used, operated, calibrated and maintained unaer tbls 

permit, 

d. .to obtain and remove samples of any dlschsl'fe or emissions of pollutants, and 

e. to enter and utilize any photograplric, recording, testing, monitoring or oiher equ!~ment for the pur pope. of 

preserving, t""ting, monitoring, or recording any activity, discharge, or emission authorhod by this permit. 

5. The issuan.cs of this permit: 

a. shall .not be considered aa i.n any Ql8nner affecting tbe title of the premises upon which the permitted 

facilities are to be located, 

b. doea:not releaso the permittee from any liability for damage to perSQn or property cauoed by or resulting from 

the constructi-on, maintenance, or -operation or tHe ~ropoe;ed facilities, 

c. does not release tbe permittee from compliance w'ith other applicable statutes and regulations of the United 

· - States, of the State of Dlinois, or with applicable local laws, ordinances and regulations, 

d. does not take int·o consideration or attest to the structural.stability of any units or: parts of the project, and 

!k~~~fi!v .. lil/05l 09~006 

·-· .... 

VESOI2175 
) 

Dm.EOTORY 

ENVIRONMENTAL PROTECTION AGENCY 

DIVISION OF AIR POLL'UTlON CONTROL 

••... July 1, 1985. 

For o,ssl.stance in praparlng a ~~ application 

contact tho Pon:nit Section, 

IUinols Environmental Protection Agency 

Diviaion of Air Pollution Control 

Peanlt Soct.lon 

2200 Churchill Road 

Springfield, illinois 62708 

!.217) 782·2118 

or· a regional office of the Field 

Operationt~ Section. The regional 

off"ICeS and their areaa or resp<>nsibility 

are shown ou the map. The addresses 

and telephone numbers of the regional 

offices are as follows: 

IUinois EPA 

Region 1 

Intercontinental Center 

1701 S .. 1st Avenue 

Maywood, Illinois 60153 

(312) 345-9780 

illinois EPA 

Region 2 

5415 Nort.b Univendty 

Peoria, lllinois 61614 

(309) 691-2200 

lllinois EPA 

Region 3 

2009 Mall Street 

Collinsville, Illinois 62284 

<618) 345.moo 

'''" 

VES012176 
\ 

'. 

~ fllil)ois ~nvironmental Protec tion Agency · 2200 Chu~chill Road, Springfield. 11.62706 

217/182-2113 

JOINT CONSTRUCTION AND OPERATING PERMIT 

PERMimE 

Trade Waste Incineration 

A Division of Chemical Waste ~~nagement, Inc. Attn: James L. Gary 

7 Mobile Avenue 

Sauget, Illinois 62201-1069 

Application No.: 88030101 A~lt cant's Designation: TANK FARM3 

S ject: Tank Farm Number 3 

Date Issued: June 27, 1988 

Location: 7· Mobile Avenue, S~uget, IL 

I. D. No .: 163121MP 

bate Received: March 29, 1988 

Operating Permit Expiration 

Date: June 30, 199o 

Permit is hereby granted to the above-designated Permittee to CONSTRUCT and 

OPERATE emission source{s) and/or ~ir pollution control equipment consisting of ten 12,000 gal. and sixteen 30,000 gal. 1~aste blending and storage tanks 

with carbon ·adsorption and associated truck and rail car unloading stations lith vapor bal ance as described in the above-referenced appl.ication. This 

Permit is subject to standard conditions attached hereto and the fol lowi ng special condition(s): 

1. Operation of the emission source(s) included i n this p,ermit shall not 

begin unti l all associated air pollution control equipment has been 

co.nstructed and is operational . 

2. lolithin 60 days from the issuance of this permit a carbon adsorber 

breaHh1·ough monitoring program shall be submitted for Agency approval •.. Operation of this tank farm shall not begin unti l the Agency has approved 

t he breakthrough monitor program. 

3. E11f ssions of organic material shall not exceed 2.5 tons/year .. This limit 

i s basi!d on Information provided in the applicatton. 

~ a Jwd:;;:--

Mana

Terryf 

get, Permit 

Sweftze~ Section 

Di vision of Air Pollution Control 

TAS:JD j~/4939 /54 

cc: Region 3 

VES012177 
-, 

July 1, 1986 

ST~TE OF U !NCMS 

fNWroNMENTAL PftOTECnoN AGENCY 

cifviSION OF ~ POLLUnON CONTROL 

2:.~00 CJflJftCfilll ROAD 

Sf'FitiiGFaO. IWNOIS 62706 

STANDARD .CONDITIONS FOR CONSTRUCTION/DEVELOPMENT PERMITS 

ISSUED BY THE ILLINOI$ ENVIRONMENTAL PROTECTION AGENCY 

The Dllno\s Environmental Protection Act Clllinoia Revised Statutes_, Chapter 111-112, Section 1039) authorizes the 

Environmental Protection Agency to impose conditions on permits which it issues. 

The following eoriditlons are applicable uuless susperoeded by apeclal conditloil(a). 

1. Unlcas this permil has ~n extended or It bile been vcided by a newly Issued permit, this permit w111 explro one 

year f~om tho dati of ia!uanee., unle.ss a d;tntlnuoua: program of construction or development on this project has 

started by such tim6. 

2. The construction or devel9pmen.t covered bj this permit &hliD be done in cora.pliance with applicable provisions of 

the Illinois Environmental Protection Act and Regulations adopted by tho Illinois Pollution Control Board. 

8. There shall be no deviations from the approved plans o.nd specit'icatioo..s unlesa a written requeat for modification. 

along with plans and specifications ao requizOO, shall have been aubmlttaa to tho Agency and a supplemental 

written permit iSBucd. 

4. The permitteo shall allow any duly authorized agent of the Agency upon the presentation or credentials, at 

rea&Onable tim&s: 

a.. to enter the permittee's property where actual or potential efnuent, emission or noise sources ar(lloca:ted or 

where any activity Is to be cooducled pursuant to Ibis permit, 

b. to have atce-ss to and to copy any records required to be kept under the terms and conditions of this permit, 

c. to inspect, including during any hours of operation of equipment constructed or operated under this permit, 

such equipment and any oquipment required tQ be kept, used, operated, calibrated and maintained under th.is 

permit, 

d. to obtain and remove &le; of any discharge or emis.sions of pollutants, and 

e. to enter and uUlize any photographic, recot:ding, testing, monitoring or other equhJment for the purpose of 

preservi.ng, testing. monitoring, or recording any activity, discharge, or emission authorized by this pern'lit. 

5. The issuanco of thle permit: 

a. shall not be considered as in e.ny manner affecting the title of the premises upon which tbc permitted 

facilities are to be located, 

b. does not rol&JlJle the permitt86 from any liabJUty for damage to person or property caused by or resulting from 

the construction, maintenance, or operation of the propoaed facilities, 

c. does not release the permittee £rom compliance with other applicable statutes and regulations of tbe United 

States, of tho State of lllinois, or with applicable local Jaws, or.Uoances and regulations, 

d. does not take into consideration or attest to the strudure1stahiHty of any units or parts of the project, tuld 

.lJsc5fi0°li:"'. ·• o1u ~ 1 09CHJos 

VES012178 
·: 

.•.. , •• ., . ·r. .. ~· ·. • • 

STANDMD I))NDITIONS 

t'QlL . . OPERA'l'ING PERMITS. 

July 1,1985 

Thelllinoie Environmental Protection .Act Ullinois Revised Statutes, Chapter 111·1/2, Section 1089) gl'!lDts the 

Environmental Protectlon A~ency aUthority to imp'os6 conditione on permits which it issaea. 

The ~oUo wblg couditiou are applicable unless superseded by special permit coildition(s). 

1. The ioananee of llm pet111U doeo not release the permit\ee from compliance with state and federal regula tiona 

which are part of the Dllnols State Implementation Plan, ae W.U as with othor applieoblo ototutee and regulations 

of the Unit..d Statee 0r the State of Dllnoio or with ·appUcabla local laws, ordlnonees and ·re.1ulationo. 

2. . . :t'l>~ ,il.g'!li,cy. has issued t!Uo permit basod upon the information oubmltted by the permittee IJ! the petlllit 

.. P,pll~~tjo.n. Auy misinformation, falao otatement or .miopraentatjon in the application shall be grounds for 

revocation under 35 IU. A!lm. Code 201.207. 

a .• a. The permittoe shall not authorize, cause, dlract or allow any' modification, as defined in 36 Dl. Adm. Code 

. •. 201.102,· of equlp,;,ent, operations o.r p.,;ctiees which are reflected In tbe permit application as submitted 

unleBS a new application or request for revision of the existing permit is filed with the Agency ~tnd unless a 

ne)V permit or reviaion of the existing permit(&) i& iuued ·for such modification. 

b. T!Us permit on!y covers emisoion sourc .. and control equip.meut wbile physically present at tho indicated 

plant location <a). UnleSs the permit specifically provid~a fot equipment relocation, this permit is void tot an 

item of equipment on the day it is removed from the permitted loeation(s) or if all equipment is removed, 

notwitbstanci!Df the expiration date specified on the pennit. 

4. The permittee shall aDow any duly outbor)%ed agent of the Agency, ppcn the presentation o,f credeotiolo, at 

reasonable times~ 

·e. to enter tha permit~e·a property where aetual or potenti~l effiue.nt, emission or noiae aourcea are located or 

where any activity is to be conducted pursuant to il permit, 

b. to have acceoo to and·to copy any records required to be kept under tbe terms and conditions of this porml!, 

c. to inepeCt., jocludiog during any hours of operation of equipment corurtru.cted or operated under thi~ patmit, 

such equipment and any equipment required to be kept, used, operated, calibratsd and malntsined under this 

permit, 

d. to obtaln ~d remove samples of any di-schatte or emission ·of pollutants, and 

&. to eoler .and uti!Ue any pbotographi<, recording, testing, monitoring or other equipment for the purpose of 

pree-errinf. testi.ng, monitorinj' or recording aoy activitY, diecb3.tg-e or emission authorized by this permit. 

5. Tbe is~Wu>ce of Ibis perm! t: 

.-,. 

' 

a. shall oot be eonaldered as in any manner affecting the title of the prentiseJt upon which the permitted 

facilities o,re located. 

b. does not releue the permittoe from any liability for damage to person or property caused by or resulting from 

the construction.. mainten~ce, or qpera.iion of the facilitiee-, 

~·fii'fa!v. ID/OA) 

VES012179 
.. 

fOR t«MCY US£ Olll.Y 

........_ I'JUSSUlli W01!T 

••• IWif OF O'llHER: 2<. iW£ Of CORPORATE DIYISIOII OR Pt.AiiT {IF DlrfEIIENT fllllH OllliER)' 

lb. lEL£911lWE MMIER: 21>. STREIT AOOR(SS OF EHJSSIOII SOORct' 

•• STREET liDORESS Of O'R11£R: 2< . mt Of EIIISSION SOIIA<t' 2\:f, TELEP~O!'!£ MIJMB£R: 

fld. CITY: 2e • .....,., , I ... LU<Al<O VllHI N till liMII>< 

Oru ooo 

h. STATE: r'· 21 p """'' z.. '""'""'" 2h. liP CODE: 

PmtiT JHF<lfij4AT101f NCO RtRROte£ 

' 3. ·. W!I:JJiC llllS R£PORTJWG PERJ(lO 

.I ts lME DAT'11 A1iO Ulf()CIAATIOII MAXlHI.tS "tj~lOIG FMH TillS PUC.£JITAGE BY WHICK 

PII£YJoosu SJJeHtnm Tllllt, OP£AA710tl ' ErtiSSIOMS HA\1£ Itt· . mt.ICAnOII IM!JEII IOOIIIFI<AfiOI< I<1IXI!r:l! CORA£CT, CUAS:EJIT llfD COJIILETI7 II£HAIJED CM'AS£0 OR DtCR£As.ED 

UICREASEO THE SAME DECI!£ASED 

0 m 011) ------ --- 0 YES o .. - 0 m 011) -- --- -

- - -- Om 0110 

P£1100 tOVER;m BY THIS Ra'OO': 

TO 

S. nef ADOV£ JNFORAAT!Otf IS SUBMITTED Of ACC:OJWMCE WITH PCB A£GS . , CNAPTER t, RUlE 107(b) AS AOOPJED Mill 14, 1972, Ali'O THE 

INFOAK\rtOH IS ll:tl£. COiftCT, COWLEJ't, .W0 CURRfJIT, niE SISKATUR.£ ttiST BE THAT OF ntE PERSON Atm()Rllf.D TO EXECUTE Art OP£1ATlrtG 

PfRHIT APPC.ICATIOH. 

AIITHOl.TUO SIGJIATIJII£ 

A COPY OF THIS fOI!If I<JST BE SUB!IImD fOIIlACH PEJOIIT AIOLICATIO!I USTED AIJ<WE • 

TtltS DOQJKSiT IS JIOT A IUrtrT ~LitATlOtl MD 1S S!UU FOR STATtSllCAL Alii lttFclaMATlOUAt.. f'IMPOS£5. 

IF Tilt UIFOAAATIOII CONTAurrD IN A USTtD PER:IIrT APPt.tCATTOff IS tiO LONGE:R CORitECT • MT£RJAl toR:RECTlliC TliE _ APPliCATIM. SQOOtb liE .SOO TO THE PERIUT SECTICif OF nt£ DIVISIOII OF AD PCUUTIOH CUITin.. If' TIE CORRECTlOft 

lS DUE 10 A tmtflCATI<ltl (IJtCIEASt IN OUSSfCftS) OR fiE:W E~IPMDIT. TJUS wtfER.lAL SRWLD 8£ SUBHmED AS A 

COttSTP.UCTIOH P'ERHJT AI'Pt.JtAflOit. DniERIUSE I. Lt'TT'D EXPl.Al«UIG 'T)( (XIflllEtTIOft Nlll IE SUFFICttrfT. 

JL 532 .. 0243 

APC l08 l t v. 6/15/ 78 

J 

' 

' 

' 

I 

VES012180 
J 

i>IRECOORY 

ENVDlONMENTAL PROTECTION AGENCY 

DIVISION OF AIR POLLUTION CONTROL 

, July 1, 1985 

For osoletanee In preJ)arlog a pennit applic•tlon 

contact tbe Permit ~ion, 

Dliool.o Environmental Protection Agency 

DIYloion of Air Pollulion Control 

Permit Section 

2200 Churchill Road 

Spring(ield, Dlinoia 62706 

<217> 78Z.211S 

or a "'gional office of the Field 

Opoutlo11o Section. The re~onal 

officao and their areas ofreapolllibDity 

are abown on the map. The addresse. 

and telephone numbers of the reiional 

offioea ""' ao follows: 

,......., 

Illinois BP A 

Region 1 

Intercontinental Conter 

1701 S. let AV1lllue 

Me,ywood, IDinoia 60163 

(312) 846-9780 

llU11oia EPA 

Regic>n 2 

6416 North Univereity 

Peoria. ll!lnoia 61614 

(3()9) 69J-2200 

Dllnolo BPA 

Rol!lon 8 

2009 Mall Street 

Collhlllvtllo. nnnol.e 62284 

(618) 346-0700 

VES012181 
t:i:::tt. State of lllinois 

~ .. ~ ENVIRONMENTAL PROTECTION AGENCY . ; . 

NOV 1 0 REC'O 

F 

I 

~ 

Mary A. Gade, Director 

217 -782-2113 

P. 0 . Box 19506, Springfield, IL 627'!4-9506 

r 

JOfN'!' COllS!.'RUC'l'ION AND OPERATING PER."!!T 

PER.'<I'l'TEl! 

~ade Was~a ncinera~ on 

Attn: General HauaQ"Q:r 

? t>fobi l e Avenue 

Sauget, IL 62201 

Application No. : 9SOS0025 

Applicant's Desi~tion: 250 Boiler 

Subject; clea~er rooks Boiler 

Date ssu~d: November 7, 1995 

~2~~: 7 ~obil e Avenue, Sauget, IL 

.D. No.' 163l2lAAP 

Date Recei ved: August 1!, 1995 

gperatinq Permit Expiration : November 7, 2000 

Permit is hereby r~ted to the above deaignat•d ~mittee to CO~STROCT and 

OPERATE emission source{s) and air pol ut on control equipment consisting of 

a Cleaver~Brooks natural gas f ired boiler model ca ?n0- 250-150 PSIC aa 

described in the above~~eferenced application. This Permit is subject to 

su.ndard conditions at.tached hereto and t.he following .special condition(&): 

1 a . Natural gas sha ll be e only fuel fired. , ' . 

. · / b . Sm.issions and operation of t.his boiler shall not exce-ed the following 

lirlits: 

l'uel 

NatUral Gas 

Ope rat ing How:s 

lbr iYrl 

S,760 

Ni t-rogen. 

{lb/hr) 

1.46 

OX-idee 

(to:l/xr) 

6.41 

carbon tconcxide 

!!2L!!!: ton/yr 

2.1 9.2 

'l'hes·e limits are based upon the maximum firi ng r ate for t he boi-ler, and 

standard emission factors. 

c . The Permittee shall notify the hgency prior to any change in the types 

of fuel used in the boi ler. 

d. ~li&:o.ee w-ith the an.."lual limit aha.ll be ,Petermined from a running 

total of 12 mont hs of dAta. ' 

2a. The er~ttee shall maintain records of the following itemat and such 

other items as may be appropriate to allow the J\genc~~ to review 

COli'/Pliance wi th the limits in Condition 1. 

i. Annual usage o!' natural gas tlO' acf/month at\d 10; scf/year). 

ii. Thase records shal l be r etained for thre~ years and shall be 

available for insp~ction by the Agency. 

I· 

l ,. 

! 

I 

I 

. 

!. 

I· 

I 

' 

VES012182 
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Pa ge 2 

If you hAve an ques tion on this. please call Jim Cobb at 217-782-~113. 

~ ~ t. {!:;/l;r-jr· .. _ Donald £ . sutton, P .E. t1anager, Perm.:L.t Sect.ion 

Oivif'ioo of 1\ir Poll·.J.tion CQntrol 

DES:JDC/S3112 .wpd 

ce: Region 3 

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YESOI2183 
FEB-06-2001 TUE 04:3t PK EPA AIR PERH IT FAX NO. 2176245023 

ILLINOIS ENVIRONMF.NTI\1. PRO-rEC:TION AGENCY 

---.. -··------··--·-·----·--· 

P.o. Box 19S<X>. s""""'"'"'· htiNOIS 62'9 ~sor, 

THOMAS v. SKINNER, D IRfCTC.)R 

Cl!R'l'!FIEU ~JAIL 

CONSTRO-~ION PL~IT GRANT - OPERATING PERMIT OENI~ 

PEJ)l1tTTEt 

onyx envirc-mtn•:mtal Sa.rvi.ces 

Attn: Oou<;r HarrS.s , Ge n . Mgr. 

-37 l<fobil.e Avenul\) 

Sauget, Illinoi s 62201 

licnt ~; 00110030 I .D. No.: 16312~P 

~1ioant•o Dooi qnation: CARBONINIG Date Roccived ; No c~er S, 2000 SUh1~ct 1 PAC Iojeation a nd Lime Recircul ation 

~~~~ Febru•~Y 6, 2001 l~ ~> on : ~7 Mobile Av~nue, Saugot 

Pc~t i~ horeby qranted t o the abovoMdesiqnat~d Permitteo to CONSTROCT ~mi~sion uoit(s} and/or a ir pollution control equi~ent ~isti q of an acllvated catbon i nject i on systom ~nd baghouso solids r ecirculation syst~ 

f.or t he Unit 4 ba~~ dous ~aste inciner ator ~s deecr ibed i n t ho 

et><.-.ve-.reterenood a.pp.U.eat ion. Thls Pe.rl'l'lit ia aubj~ot to :standard condi t ions 

attaebcd hereto and the following special c ondit ions : 

la . This conetrue~ion permit is ssu~d t or tmptovero~nti to the air 

pollution control :.yst<:lll to:t: the Onit 4 hazardou.e \\'aS: to i ncinerator to 

f acilitata cornpllanco \-lith the a}:)plic able ctt\isaion limitations of -10 

CF~ 63 SubpOllrt EEE, t'lation~l tm.i&~ion Standards for H-a-zardous Air 

Pollutants trom nz~ doua Waste oin~rators , which b~come effective on 

Sept cQbar 30, 2002 . 

b . 1'hi (f constructi on permit has not addressed t.he other applicable 

:rcqui rol!lents o! 40 CFR 63 Subpa t E&E, such •• operator tx~Wng and 

cert 1 fica. t ion. 

c, 

2 . 

3. 

1. 

Thi~ e~t does not authori ~ modification or r eoonstruction of th~ 

Onit 4 incinerator. 

Thi s ~.rnt t doca not 1;elax or re:vi$e. the x.:qui:r:caent!i' e st ablished in 

the exioti ng pe~1ts tor t hs Unit 4 i ncinerator, c .9. , Ai,r Pollution 

COnt rol Opcra ~ng Po~t 90020011. 

'tho i.mprovem,fJnta to t:he a i r pollution cont rol sy~tem ahall be ~igned, 

i~$tQlled, oqui ppod and ~perated to comply with npplic~hle cquir~ents 

of 40 CFR 63 Subpart EtE. I n p~ tioular, t he 3ystems must eo~ply wit,h 

4pplio~ble requi rements for ctiv~ted e~dbon inj eot lon syst~~ ond dry scrubbe~ syst eMo. 

T~e co~plianoc mil~•tonQs of tO CFR 63 Subpa~t E&E sha l l be c9~lished tor Unit 4 on o~ before t ha ~~quircd data, as Qpeo~£~~d 

below. 

~. Su~ittal ot a t~vision to the pending Title V ~ppli ~tion to 

i noorporete the requ1re Qnts of 40 CFR 63 Subpart &se, by 

Maroh 30, 2001. 

CeorJ.> ~ H. ~YAN, Govr~NOR 

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VES012184 
., : .. ........ ··-; ........ ' • ~; ... ::; f. .......... ·····;· >.~ ... :~~ .··· ~· .. , .. ~· •. ,, •.·.:. · ,•, .... . ... ':' .. ~. 

FEB-06-2001 TUE 04:31 PM EPA AIR PERtllT FAX NQ 2175245023 P. 03 

b. Submittfll of any request for extonde<l oomplianoc by September 30, 

2001. 

c. 

d. 

•• 

Submittal of Coftpl innco Proqr ess Report by OCtober l, 2001 . 

Submitte.l ot a ComprGh.cnaive fex£onnancc Test Plan by Marc:h 30, 

2002. 

Compliano~ ~ith tho epplioahle provieions of 40 CFR 63 8ubport 

&£&by September 30, 2002. 

!. !r.aitiat io.a. of init ial pox:formnnce testi ng on or bofore t-1a:t:'c h 30, 

2003. 

g. 

h. 

Cor11pletion of initial ~erformance t esting by May ?.9, 2003. 

Subuittal of Notification o£ Cornpl1ane6 or Non-Compliance by 

hugullt 27, 2003. 

S. The unit 4 ! ncinorat or m4Y be operated as generally thoriz d by oxi~ting poraits wi th the ~provementa to the control oyste~ addressed 

by t his construction perait~ Du~ing sueh operation, the Permittee 

Rhall ca ry out an orderly shakedown of e new syst~a, devolop limite 

for r e l evant oper at i ng parameters and oonduct r<lquir$d PQ~fonJiancc 

t esting . 

Thn OP~TING permit applicat iQn is DENIED bec~u•o t he Il ino~~ En~ir ~e tal 

PX'OtGoti on Ac t, Seotion 9, Allcl 35 Ill. l\<!ln. Code ~01. 60 might be violatod. 

PurGu&nt to Section 201 .160, an oporatinq pormit may not ba i~sued until the 

Qquipment h~a ~en oonstr uotod or moditie d in aecordanCQ with opplicable 

conditions in t h i D construct ion p~rmit . The Illin ois &PA ouqgests that you 

reappl.y 1or the opc.ratinq pormit atto,r the corwtJ:uct ion i s comp,l.~ted .in 

SJ,ccordance with the constructi on permit. This informstJ.on muS't; bo .:rubmi ttad 

in dupli cate and should refcrance the appl ication and I. D. nu'llbcrs assig'ncd 

abovG. 

If you h~vo any quostioD$ on t .hi8, plsaae call Christopher Romaino at 

2l'I/1S2• 2113. 

ocnatd E. Sutton, P.E. 

Manager, Permit Section 

DJ.vtsion o! A1.r. Pollution Co:1trol 

OF.:S :CRR: jar 

co: Region 3 

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VESOI2 85 
VES012186.pdf 
APPENDIXG 

STARTUP, SHUTDOWN, AND :MALFUNCTION PLAN 

VESOI2186 
STARTUP, SHUTDOWN AND MALFUNCTION PLAN 

Prepared for: 

Veolia ES Technical Solutions, LLC 

Sauget, illinois 

Prepared by: 

Franklin Engineering Group, Inc. 

Franklin, Tennessee 

October 2008 

VES012187 
TABLE OF CONTENTS 

1.0 INTRODUCTION ............................................. -.. -...... _,,,,_,,_,,, ....••..........•........ 1 

1.1 REGULA1'0RY REQUIREMENTS ..................................................................... 2 

1.2 REcORDK.IlEPING AND REPORTING PROCEDURES ......................................... 2 

1.2.1 Records ........................................................................................... 4 

1.2.2 Reports ............................................................................................ 4 

2.0 ENGINEERING DESCRIPTION ..... --............. -........ .,_ ................................... 6 

3.0 STARTUP AND SHUTDOWN PROCEDURES ................ - ... -............. --.... 13 

3.1 STARTUP .................................................................................................... 13 

3.2 NORMALSHlTTDOWN ................................................................................. 15 

4.0 MALFUNCTIONS ................................ -...................................................... _ .... 16 

4.1 1'-f:EASURES TO MINJMJZE THE FREQUENCY OF MALFUNCTIONS ................. 16 

4.2 MEASURES 1'0 MlNJMJZB THE SEVERITY OF MALFUNCTIONS ..................... 18 

4.3 CORRECTIVE MEASURES ............................................................................ 19 

i 

VES012188 
LIST OF TABLES 

TABLE 1-1 OVERVIEW OF REGULATIONS REGARDING STARTIJP, SHUTDOWN AND 

!v.IALFUNCT!ON ...........................•....•....•.....•........•....•.....•..........•........•......... 3 

TABl£ 4- 1 SUMMARY OF POTENTIAL MALFUNCTIONS AND CAUSES ............•........•..•.. 17 

TABLE 4-2 REDUNDANT EQUIPMENT AND SYSTEMS FOR MINIMIZING THE FREQUENCY 

OR SEVERITY OF MALFUNCTIONS .....................................•.......••••..........•.. 20 

LIST OF FIGURES 

FIGURE2-1 

FIOURE2-2 

FIGURE2-3 

FIXED HEARTH INCINERATOR, UNIT 2, BLOCK FlOW DIAGRAM ..•............... 7 

FixED HEARTH h'JCJNERATOR, UNIT 3, BLOCK fLOW DIAGRAM .................. 8 

ROTARY K!L."' INCINERATOR, UNIT 4, BLOCK FLOW DIAGRAM .................. II 

ATTACHMENT I 

A TT ACHt.IENT 2 

ATTACHMENT3 

ATTACHMENT4 

LIST OF ATTACHMENTS 

STARTUP RECORDKllEPING FORM 

SHUTDOWN RECORD KEEPING FORM 

MALFUNCTION R.ECORDICEEPINO FORM 

PROGRAM OF C0RREC11VE ACTIONS FOR MALFUNCTIONS 

ii 

VESOJ2189 
1.0 INTRODUCTION 

Veolia ES Technical Solutions, LLC (Veolia) owns and operates two fixed heru1h incinerators 

(Units 2 and 3) and a rotary kilo incinerator (Unit 4) at its facility located in Sauget, TIIinois. The 

incinerators are sul:(ject to the National Emissions Standards for Hazardous Air Pollutants 

(NESHAP) for Hazardous Waste Combustors (HWC), 40 CFR, Part 63, Subpart BEE(§ 63.1200 

to § 63.1221 ). Tite NESHAP specifies emissions standards which retlcct emissions performance 

of lvfa.xirnUJ!l Achievable Control Technologies (MACT), and is commonly referred to as the 

HWCMACf. 

The HWC MACT Standard defines the control of emissions during normal, day-to-day 

operations. In order to address the control of emissions during transient periods, the 

development of a Startup, Shutdown, and Malfunction Plan (SS!\fl') is required. Startup, 

shutdown, and malfunction (SSM) are defined in § 63.2 as follows: 

• Startup - the setting in operation of an affected source or portion of an affected source for 

any pwpose 

• Shutdown - the cessation of operation of au affected source or portion of an affected 

source for any purpose 

• Malfunction - any sudden, infrequent, and not reasonably preventable failure of air 

pollution control and monitoring equipment, process equipment, or a proc~s to operate 

in a normal or usual manner which causes, or has the potential to cause, the emission 

limitations in an applicable standard to be exceeded. Failures that are caused in part by 

poor maintenance or careless operation are not malfunctions 

During these transient periods of operations, a source must conform with its SSMP. Therefore, 

during periods of startup, shutdown, and malfunctions the operating and maintaining of the 

incinerator will be consistent with the procedures and corrective actions that are prescribed in 

this plan. This will ensure that emissions are minimized, to the exteut practical. 

TI1e purpose of this startup, shutdown, and malfunction plan is to: 

• Prescribe procedures for operating the incinerator systems during periods of startup, 

shutdown, and malfunction that are consistent with safety and good air pollution control 

practices 

• Describe measures for the prevention and minimization of excess emissions during 

periods of startup, shutdown, and malfunction 

• Reduce the reporting burden associated with periods of startup, shutdown, and 

malfunction 

• Satisfy the requirements of§ 63.1206(c) and§ 63.6(e)(3), as shown in Table 1-1 

VES012190 
Due to the similarity of the three incinerator systems, general references to an incinerator in this 

document will imply all three incinerator systems. Infonnation that is only applicable to one or 

two of the three units v.~ll be clearly identified either parenthetically or delineated by the section 

beading. 

As required by §§ 63.6(eXv) and 63.6(eXvi), this plan at\d other documents containing 

procedures or information referred to in this plan will be made available for inspection when 

requested by the Administrator. If Veolia is required to submit copies of this plan or portions of 

this plan (or related documents) confidential business information entitled to protection from 

disclosure will be clearly designated. 

The remainder of this section provides an overview of regulatory requirements and a pro gran\ for 

compliance with the recordkeeping and reporting requirements. Section 2.0 references an 

engineering description of the incinerator, air pollution control system, and continuous 

monitoring system. Section 3.0 addresses the startup and shutdown of the incinerator system. 

Section 4.0 addresses potential malfunctions of the incinerator system. 

1.1 Regulatory Requiremenll> 

One of the objectives for this document is to establish a progran\ that will ensure compliance 

wiili relevant sections of the loterim MACf Standards. Table 1-I includes the regulatory 

requirements and the location of each requirement addressed herein. 

1.2 Reeordkeeplng and Reporting Procedures 

This section addresses the recordkeeping and reporting requirements related to periods of SSM. 

The strutup, shutdown, and malfunction reports discussed in this plan ensure that V eolia is 

satisfying ilie general duty to minimize emissions and document that actions taken during those 

periods are consistent with this plan. These reports and records provide the necessary 

documentation to shield transient events from the HWC MACf emission standards imposed on 

steady-state operations. 

As long as actions taken during a transient event sufficiently maintain the incinerator system 

within limits, there is no justification in distinguishing iliat event trom steady-state operations. 

For example, problems may arise iliat meet the definition of a malfunction yet do not impact the 

ability to maintain ilic incinerator system within limits. lo these cases, maintaining ilie 

incinerator system within limits substantiates that the actions taken sufficiently met the 

objectives of this SSMP and minin1ized emissions to a greater degree ilian required by 

regulations. 

2 

VES012191 
Table 1-l 

Overview of Regulations Regarding Startup, Shutdown and Malfunction 

Regulatory Citation 

§ 63.6(e)(3)(i) 

§ 63.6(e)(3)(i) 

§ 63.1206(c}(2)(jj)(A) 

§ 63.1206(c)(2)(ii)(A) 

§ 63.1206(c)(2)(v)(A)(3)(i) 

§ 63.1206(c)(2)(v){A)(3)(ii) 

Description 

Description of potential causes of malfunctions 

Actions to minimize the frequency and severity of malfunctions 

startup 

3 

4.1, 4.2 

Table4-2 

3.0 

1.2.2 

1.2.2 

1.2.2 

1.2.2 . 

VES012192 
Accordingly, the recordkeeping and reporting requirements presented in this section are 

only applicable to periods of SSM in which there is a reasonable elq)CCtation that an OPL 

or emission standard can not be met This includes all startups, all shutdowns, and all 

malfunctions that result in an exceedance of an operating limit or emission standard. 

Malfunctions that prevent the ability to document on-going compliance are also subject to 

recordkeeping and reporting requirements. 

This plan, all revisions to this plan, and all records and reports described in this section 

will be retained in the operating record for at least five years. 

I. 2.1 Records 

SSM records will include the following: 

• Date and time of each SSM 

• The duration of each SSM 

• Documentation to demonstrate that actions taken during periods of SSM are 

consistent with this SSMP 

• Description of any actions taken during periods of SSM that are not consistent 

with procedures in this SSMP 

• Results of investigations and evaluations of excessive exceedances occurring 

during malfunctions 

Attachments I, 2, and 3 are blank recordkeeping forms for startups, shutdowns, and 

malfunctions, respectively. The information recorded on these forms will be utilized to 

document conformance with the SSM:P and to comply with the reporting requirements. 

The startup, shutdown, and malfunction reporting requirements are described in the next 

section. 

1.2.2 Reports 

Revisions to this SSMP may be made without prior agency approval to reflect changes in 

equipment and procedures and to meet the regulatory requirements. Any such revisions 

made during a semiaooual reporting period will be submitted with the periodic SSM 

report. Revisions to this plan- which alter the scope of activities during a startup, 

shutdown, or malfunction-will not take effect until a written notice, describing the 

revisions, is submitted to the permilling authority. Changes made to this plan that may 

significantly increase emissions arc subject to approval by the Administrator. A written 

request for approval of the changes aud the revised SSMP will be submitted to the 

4 

VES012193 
Administrator within 5 days after making such a change to this plan. Should an SSM 

event occur that is not addressed or inadequately addressed in this SSMP, Veolia will 

make the appropriate revisions to this plan within 45 days after the event. 

An investigation and evaluation will be perfonned on each set of I 0 exceedances of a 

specific emission standard or a specific operating parameter limit that occur during 

malfunctions within a 60 day period. Within 45 days of the lO'h exceedance, the 

investigation will determine plausible causes for each excessive exceedance. The 

evaluation will conclude how to minimize the frequency, duration, and severity of each 

excessive exceedance. The excessive emissions report required under§ 63.10(eX3) will 

include a summary of each investigation and evaluation required during the semiannual 

reporting period. In addition, the excessive emissions report will include any changes to 

this plan that may result from required investigations and evaluations of excessive 

exceedances occurring during malfunctions. 

Periodic SSM reports will be submitted to the Administrator semiannually, if a startup, 

shutdown, or malfunction occurred during that semiannual reporting period. This report 

will take the fonn of a letter to the Administrator and include the following infonnation: 

• A statement that actions taken during a.ll periods of startup, shutdown, or 

malfunction were consistent with the procedures given in this SSMP 

• TI1e number, duration, and a brief description of each malfunction 

• The name, title, and signature of the owner/operator (or other responsible official) 

certifying the accuracy of the report 

An immediate SSM report will be submitted if an action perfonned during a period of 

SSM is not consistent with this plan; and an OPL or emission standard is exceeded. 

Within two working days after such an action, the Administrator will be advised via 

telephone or fax. Within 7 working days after such an action, a letter to the 

Administrator will be delivered or postmarked. The letter will explain the event, reasons 

for not following this plan, and descriptions of the excess emissions and/or operating 

parameter monitoring exceedances believed to have occurred. The letter will also include 

the name, title, and signature of the owner/operator (or other responsible official) 

certifying the accuracy of the report. 

5 

VES012194 
2.0 ENGINEERING DESCRIPTION 

Brief descriptions of the fixed hearth incinerators and the rotary kiln incinerator are 

presented in this section. A detailed engineering description of the Unit 2 and 3 

incinerators is provided by Technical Description- Fixed Hearth, Incinerators Unir.s 

NOS. 2 & 3. A detailed engineering description of the Unit 4 incinerators is provided by 

Technical Description, 1)·ansportable Rotary Kiln h1cinerator Unit No. 4. Drawing 

numbers PFD-2000, PFD-3000, PFD-4000 are the process flow diagrams for these 

incinerators. These documents and drawings are incorporated here by reference. 

2.1 Fixed Hearth Incinerators 

Each of the fixed hearth incinerators includes the following components: 

• Feed equipment 

• PriO'lazy and secondazy combustion chambers 

• Lime injection system 

• Spray dryer absorber (SDA) 

• Fabric filter baghouse 

• Solids and ash removal systems 

• Induced draft (10) fan and stack 

• Instrumentation, controls, and data acquisition systems 

Figure 2-1 presents a block flow diagram of the Unit 2 incinerator system. The block 

flow diagram for Unit 3 is presented in Figure 2-2. 

A variety of solid, liquid, and gaseous wastes are thennally treated in the fixed hearth 

incine.rators. Solid waste is fed to the primary (lower) combustion chamber via a feed 

conveyor system and pnemnatic ram. Liquid waste from tanks and tanker trucks are fed 

to the primary combustion chamber through two atomized liquid injectors. 

Both Units 2 and 3 are equipped with a specialty waste feed systems. The Unit 2 primary 

waste from liquid containers and gas cylinders are fed to the Unit 2 primazy combustion 

chamber through a specialty feed port Waste from liquid containers is fed from a 

hooded feed system to the Unit 3 primary combustion chamber through a specialty feed 

injector. Off gases from the hooded feed emission control system ate fed directly to 

6 

VES012195 
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the Unit 3 secondary combustion chamber. Off gases from a waste handling glove box 

are also fed directly to the Unit 3 secondary combustion chamber. 

The primary combustion chamber main burner and the secondary combu;iion chamber 

main burner are used to maintain temperatures on natural gas. Combustion gases exit the 

primary combustion chamber and enter into the seccndary combustion chamber, which 

serves as an afterburner. Combustion gases exit the secondary combustion chamber and 

enter the SDA. Tite secondary combustion chamber is equipped with an emergency 

stack. 

Lime slurry and water are fed to the SDA atomizer. The atomizer bas a rapidly spinning 

wheel that atomizes the lime slurry and water into a cloud of fine droplets. Combustion 

gases are directed upward through a disperser in the SDA and into the cloud of fine 

droplet created by the atomizer. This provides acid gas removal and cooling of dte 

combustion gas. Dried spent chemicals and ash settle to the bottom of the SDA and are 

discharged to the ash removal system. 

Combustion gas exits the SDA and is distributed to dte fabric filter modules. Unit 2 has 

four fabric filter modules and Unit 3 bas three fabric filter modules. Combustion gas 

passes through Teflon-coated fiberglass cloth bags. Particles in the combustion gases are 

deposited on the outside of each bag in dte filter module. During the bag cleaning cycle, 

a burst of air in the direction opposite to the gas flow dislodges particulate matter from 

the bag. 

Tite induced draft fan is located downstream of the f•bric filter bagbouse. The induced 

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

main stack. 

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

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

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

integrated zirconium oxide-based analyzer detects oxygen concentrations. 

2.2 Rotary Kiln Incinerator 

The rotary kiln incinerator includes the following components: 

• Waste feed system 

9 

VES012198 
• Primary and secondary combustion chambers 

• T~peringchamb~ 

• Lime injection system 

• Spray dryer absorber 

• Carbon injection system 

• Fabric filter baghouse 

• Solids and ash removal systems 

• Induced draft (JD) fan and stack 

• Instrumentation, controls, and data acquisition systems 

Figure 2-3 presents a block flow diagram of the Unit 4 incinerator system. 

A variety of solid and liquid wastes are thermally treated in the rotary kiln incinerator. 

Solid wastes are fed to a ram feeder via a clamshell, a drum feed conveyor and an 

auxiliary feed conveyor. A hydraulic rant 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. 

The primary combustion chamber main burner and the secondary combustion chamber 

main burner are used to maintain temperatures on natural gas. Combustion gases exit the 

primary combustion chamber and enter into the secondary combustion chamber, which 

serves as an afterburner. A surge vent is located at the front of the kiln and the secondary 

combustion chamber is equipped with a !henna! relief vcot. 

Combustion gases exit the secondary combustion chamber and enter the tempering 

chamber. Process water is fed to tempering chamber through rur atomized spray nozzles. 

Combustion gas is cooled as it passes through the spray of water. The water is 

completely vaporized, cooling the combustion gas. The combustion gas exits the 

tempering chamber and is distributed between two identical SDAs. 

Lime slurry is fed to each SDA through air atomized spray nozzles. Combustion gases 

are directed downward through a duct in the SDA and then dispersed symmetrically into 

the cloud of atomized lime. Titis provides acid gas removal and cooling of the 

combustion gas. Dried spent chemicals and ash settle to the bottom of the SDA and are 

discharged to the ash removal system. 

10 

VES012199