### APPENDI X E MOS T RECEN T NO CNotificatio n o fComplianc e (NOC ) Repor t Veoli a E S Technica l Solutions , L.L.C . hereb ysubmit s th e Notificatio n o f

Complianc e (NOC ) Repor t i n complianc e wit h 4 0 CF R 63.1210(b ) an d 4 0 CF R 63.1207(j ) Applicabl e Rule : 4 0 CF R Par t63.1200 , Subpar tEE E —Nationa l Emissio n Standard s fo r Hazardou s Ai rPollutant s fo rHazardou s Wast e Combustors
. Thi s NO C i s b e i n g mad e i n acc o r d a ne e wit h § 6 3.9{h)
. SECTIO N I GENERA L I N FORMA TEO N A . I fyo u hav e bee n issue d a Titl e V permit , d o no tcomplet e thi s form
. Submi tyou rNO G i n accordanc e wit h you rTitl e Vpermit . [§63.9(h)(3) ] B . I fyo u hav e not bee n issue d a Titl e V permit , complet e th e remainin g portion s o fthi s sectio n an d afs o complet e Section s li-IX . [§63.9(h)( 2 C
. Prin to rtyp e th e followin g informatio n fo reac h facilit yfo rwhic h yo u ar e makin g notificatio n o f complianc e status : Operatin g Permi tNumbe r(OPTIONAL ) Facilit y|.D
. Numbe r(OPTIONAL ) 

## V- l L-1716300103-08-0 1 MLD093642424 . Responsibl e Official' s Name/Titl e 

## Dou g Harri s Stree tAddres s 

## #7 Mobil e Ave . Cit y Stat e 2| P Cod e 

## Sauge t I L 6220 1 -106 9 Facilit yNam e (i fdifferen tfrom Responsibl e Official' s Name ) 

## Veoli a E S Technica l Solutions , L.L.C
. 

# [ Facilit yStree tAddres s (I fdifferen ttha n Responsibl e Official' s Stree tAddress ) Facilit yLoca l Contac tNam e Titl e 

## Dou g Harri s Genera l Manage r Phon e (OPTIONAL ) 

## 618-271-280 4 City
. Stat e ZJ P Cod e 

## Sauge t 

# M l 6220 1 r-106 9 D . Indicat e th e relevan tstandar d o rothe rrequiremen ttha t i s th e basi s fo rthi s notificatio n an d th e source' s complianc e date : (§63,9(b)(2)(iii) } . Basi s fo rthi s notificatio n (relevan tstandar d o rothe rrequirement ) Complianc e Dat e (mm/dd/yy ) 

## 40 CF R 63,1200 Octobe r14 , 200 8

iSECTIO N II CERTIFICATIO N (Note: you may edit the text in (bin saclfon us

appropriate) Base d upo n informatio n an d belie fforme d afte ra'reasonabl e inquiry , I , a s a responsibl e officia l of th e above-mentione d facility , certif yth e informatio n containe d i n thi s repor ti s accurat e an d tru e t o th e bes to fm yknowledge . Th e above-mentione d facilit yha s complie d wit h th e relevan tstandar d o ran d othe rapplicabl e requirement s reference d i n th e relevan tstandard , [§53.9(h)(2)(i)(G) ] Nam e o fResponsibl e Officia l {Prin t o rType ) Titl e Date{rrinydd/yy ) 

## Dou g Harri s Genera l Manage r 03/16/201 0 Sicjnaturer-a fRe s pon s jtf e Offjcia l 

# 2 1 SECTIO N III Describ e th e method s yo u use d t o determin e compliance . [§G3,9(h)(2)(i)(A} ) RCR ATria E Bu m Dat a fro m EP Aapprove d testin g a s require d b yth e RCR APar tB permi tan d usin g al l approve d EP Amethod s wer e use d t o demonstrat e complianc e wit h al l applicabl e emissio n standard s define d i n 4 0 CF R 63.1219 . I n addition , Comprehensiv e Performanc e Testin g approve d b yUSEPA , Regio n 5 o n Augus tB , 200 8 an d conducte d i n Augus tan d Septembe ro f200 8 an d Comprehensiv e Performanc e Testin g approve d b yUSEPA , Regio n 6 o n Novembe r25 , 200 9 an d conducte d i n December , 2009 . Se e .th e ' attac h e d O pe rat i fig ' Parameters ' Table s an d 'HW C 'MAC TEmissio n 'St a rida fds ' tab ' ie ' T o rU rifts ' 2/3 ' a ri d Uni t%\ " tha t defin e th e operatin g parameter s establishe d durin g testin g tha t ensure s complianc e wit h th e performanc e standards . ' • SECTIO N I

V Describ e th e result s o fan yperformanc e tests , opacit yo rvisibl e emissio n observations , continuou s monitorin g syste m (CMS ) perfor m a ne e evaluations , and/o rothe rmonitorin g pracedure s o rmethod s tha t wer e conducted . [§63,9(h)(2)(i)(B) 3 | Se e attache d tes tresult s tha t wer e use d t o develo p th e limit s define d i n th e Operatin g Paramete rTables''" - •reference d i n Sectio n il l o fthi s report . Thes e result s als o includ e CM S Performanc e evaluation s an d monitorin g methods , SECTIO N V Describ e th e method s yo u wil l us e to determin e continuou s compliance , includin g a descriptio n o f mo n itor i n g an d rep o rti n g re q uir e m e n i s a n d tes tmethads , [§63,9(h)(2}(i)(C} J | Continuou s complianc e i s base d o n th e operatin g paramete rlimit s establishe d fro m complianc e testing,'', . ! define d i n th e attache d Operatin g Parameter s Tabl e reference d i n Sectio n II I o fthi s report . Thes e
i incinerato roperatin g parameter s ar e monitore d continuousl yt o verif ycomplianc e by . a proces s • monitorin g an d contro l system . Th e detail s o fthes e system s ar e define d i n detai l rn Sectio n 2.0 , Incinerato rProces s descriptio n reference d i n Sectio n VII I o fthi s reportan d attached .SECTIO N V I Describ e th e typ e an d quantit yo fhazardou s ai rpollutant s (HAP ) emitte d b yth e sourc e (o r surrogat e pollutant s i fspecifie d i n th e relevan tstandard) , reported i n unit s an d averagin g time s an d i n accordanc e wit h th e tes tmethod s specifie d i n th e relevan tstandard . [§S3.9(h){2)(i)(D) ] Se e attache d tes tresult s fro m complianc e testin g tha t wa s conducte d t o demonstrat e complianc e wit h th e HAP' s an d othe rpollutant s define d i n Subpar tEEE , SECTIO N VI I I fth e relevan tstandar d applie s t o bot h majo ran d are a sources , presen ta n analysi s demonstratin g whethe rth e affecte d sourc e i s a majo rsourc e {usin g th e emission s dat a generate d fo rthi s notification
. [5e3,9(h)(2)(i)(E} ] Thi s facilit yi s a majo rsourc e du e t o it s applicabilit yt o meTJESHA P regulations , specificall ySubpar tEEB' . an d Subpar tDD . Regardles s o fth e facility' s emissio n concentrations , thi s facilit yi s a majo rsourc e b y' definition
. SECTIO N VII I Describ e th e ai rpollutio n contro l equipmen t(o rmethod ) fo reac h emissio n point , includin g eac h .control , devic e .(or
. method } fo reac h hazardous , ai rpollutan tan d th e centre ! efficienc y.(percent ) fo r. . . eac h contro l devic e (o rmethod)
. [§e3.0(h)(2)(i}(F) 3 ! Se e attache d Sectio n 2,0 , Incinerato rProces s Descriptio n fro m 200 9 Performanc e Tes tPlan s fo r

.' Incinerator s 2 , 3 an d 4 tha t describe s th e ai rpollutio n contro l equipmen tfo reac h emissio n point , Also, , i se e attache d th e complianc e testin g dat a define d i n Sectio n I Vo fthi s repor ttha t detail s th e control . Iefficienc yfo reac h contro l device . SECTIO N I

X A , Di d yo u submi ta n applicatio n fo rconstructio n o rreconstructio n unde r§63,5(d ) tha t containe d preliminar yo restimate d data ? [§63.9{hJ(5) J Ye s I'I . , , N o j , , . No tapplicabl e J , (di d no tsubmi ta n applicatio n fo rconstructio n o r reconstruction)
. 8 , i fyo u answere d yes , provid e actua l emissio n dat a o rothe rcorrecte d infonnatio n below ,

EN D O F FORM . AResponsible Official

must sign this form - Se e Sectio n If

,

3

# #< \HW C MAC TEmissio nStandard s

••' i


### Paramete r

Unit s Sluniar d(_p,7%02) M.ethp do f Complianc e Dioxin/Fura n(D/F ) ltg/dscm'IE Q ' 0.2 0 (>40 0 de g F ) Operatin g Paramete r 0.40(<400degF ) Limit s "• • Mercur y (1-Ig

) ag/dae m13 0 Opiatin g Paramete r Limit s ' • Semivolatil eMetal s (SVM ) ug/dsc m23 0 Operatin g Paramete r Cadmium , Lea dLimit s Lo w Volatil eMetal s (LVM ) ug/dsc m9 2 Operatin g Paramete r Arsenic , Beryllium , Chromiu mLimit s Carbo nMonoxid e(CO ) PP^ v 10 0 Continuou s Emission s Monito r Hydroge nCMoride/Ciilorin eppm v 3 2 Operatin g Paramete r «:;,.(HC:/C12 ) \ . . . Limit s . - : 

### Particulat egr/dsc f 0.01 3 Operatin g Paramete r Limit s

### UNIT S 2/ 3 OPERATIN G PARAMETE RLIMIT S 1

Operatin g Paramete r Unit s Limiu i Tea l Dar e Performanc e Standard s Maximu m Tota l Pumpabl e T,b/l w Wast e (Hourl yRollin g Tote] ) Maximu m Tota l Fa/anlnij s Lb/h r Wast e (Hourl yK(tilin g Total ) Maximu m SLac k

Ga s Kio wAcf m Rat e (Hourl yRollin g Average } Minimu m Primar yCombustio n De g p Chambe rTemperatur e (Hourl y Rollin g Average ) Minimu m Secondar yCombustio n De g i ; Chambe rTcmpcrauir u (Hourl y Rollin g Average ) Maximu m Baghous u i n le i Temperatur e (Hourl yRollin g

- . Average )

Max . Tota l Lo wVolatil e Metal s Feedrat e (1 2 Hou rRollin g Total } Maximu m Sem i Volatil e Metal s Feedrat e {1 2 Hou rRn i Ji n g Total ) Maxhrnm i Mereur vFeedrat e {1 2 Hou rRollin g Total ) Maximu m Chlorin e i'eedrat e (1 2 Hou rRollin g Torn! ) Maximu m Ad a Feedrat e (1 2 Hou rRollin g Total ) Minimu m Sorben tFeedrat e {Hourl yRollin g Average ) De a P

M a xPump . Lo wVolatil e Metal s Lb/h r Feedrat e (1 2 flou rRollin g Total ) Lb/h r Lb/h r Lb/h r Lb/h r Lb/h r 31(1 7

15,14 7

1S7 7

42 0

4 6 4 7 fi3 0.001' J
21 8

UVlhCi , 1.5 7 Mmimuir i Carrie rFlui d Fto\vral o Cial/JbCt j 1.4 6 (Hourl yRollin g Average ) Jau , l')')3 Jan , 1993 Jan , 199 3

Dec , 2Q09 "

Dec , 200 9

Dec , 200 9

•5 1 Lp , 2 0 O

H Sap , 200 8 Sep , Aug , 200 8 Aug , 200 8 Oct; , 200 9 Dec , 200 9 Deo , 2 0 0 0 DRL , D/ F DRE , IV P DR.F , D/F , Part. , SVM , L V M DR1 LD/ F

DRE , D/ F

D/F , SVM , L V M L V M LV7 4 S V M

SVM , LV M IICIC1 2 Part , HCL/GI 2 HCI/C1 2

* Operatin g pavamctii rlimit s m Lubl e reflec tmor e conservativ e valu e betwee n Uni t2 au d Uni t3 tes tdata .

### iriSTT 4 OVFM ATTNG PARAMETE RLIMIT S

Operatin g Paramete r Unas liinit s TeatDat e Performanc e
Maximu m Tota l Pumpabl e Lb/h rPCC-329 1 Dec , 20( W Waste (Hourl yRollingTota l j SC C -117 6 Maximu m 'I'ota l I la^ar-dou s l,b/h rr( T, • 12.K97 I )ee , 200 9 WftS WCaourl yRollin g XofeiJJ SC C - 117( 5 Maximu m StaeUtrrwl-'ln wAcf m 37,43 2 nsc,2(K W Rat e (Hourl yRollin g Average- ) Minimu m PrimaryCOmbU-SCkiti De g p 1'19!J Beo . 200 9 Chambe rTemperatur e {Hourl y Rollin g Average ) Minimu m SecondaryCu-inbiiiiiio n Deg F 1B8 G Dec . 200 9 Chambe rTemperatur e (Hourl y Rrillin g Average ) Maximu m Baghous e J o let Dc g f> - 40 0 I )e t 200. 9 ' I 'esuperarure { [ ] ot i rl yKo I ) i n g

. AvcrHg? ) Max . J'ump . I^m

yVolatil e Mstal s 3,1>/ji r+ 7 Aug, , 200-5 •':Pee(tmeil- 2 Ho wRalling-Towl ) Max . •I 'ota l J jo wVolat i l a Merass I ,b/h r5 0 Aug., 200 8 FeerlnU e (1 2 Hou rRollin g Toltil ) Maximu m Hem i Vo l a>

i ] e V I esal s 1 .b/h r6 1 Aug, , 200 8 Fee d ral e (1 2 H o u rRollin g To(fil ) Ma xi mun i MereuryJ'eei trate J.roti f0,02 6 Aeg. . 20 0 S (1 2 Hou rRollin s Tolal ) Maximu m Chlorin e Pee d rate I,Mi r22 9 Dec , 20O!> (1 2 H im - Rollin g Total ) Maximu m A.sl i Pee d Ra w(1 2 I.Mi r64P 1 Deo . 200 9 1 lou tRulin g T o ml ) Carbo n fnjecrio n 1'eedrate J.b/b r6. 2 Deu , 200 3 (Hourl yRollin g Average ) DUK , IV K OKI! , D/ P DRf.v , D/ R Pail , SVM , L V M DRE , D/ F
DRK . D/ F
I VP , S"VM
. L V M L V M L V M S V M H g SVM , LVM , 1 1 CI/CI 2 Part , D/F , H s
M i draw n Sorben tFeetirale - Lb/l b Ct 22.2 5 {Hourl yRollin g Average ) Minimu m Carrie rFlui d Flowrat e Gal/l b Cl a3.1 0 (Hourl yRoilin g Average ) Dec , 200 9 Dec , 2-Q M HCI. ; CI! 2 JICl/f:i 2

# UNI T2 EMISSIO N RESULT S

i i

# ENS R Tii b) e 3- 3 RW I 2 G Samplin g Parameter s an d Emissio n Result s - Wee k o fAugus t11 , 200 6

I Sam p J-i Puramefe• - ;Haiwiie1nc . Hressu/ e VnlMit e Metere d Gsmplii _yijjum

e jkjoisturp j i02_atSlac k

_
, j if)yijt.5^?.^
. J®IPR,.-. i Star k .Fjowraj © j'teokirefe ; 

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. @
. 7 •S i O j [Stel e Dnsskir rRaff i QuflnStj fColjnclct j Stac k Coric
. @T % j Stoc k Emission - Kat e _ 

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in . H g

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# ENS R

Tabl e 3 - 4 Summar yo fItW C MAC TMetaT s - Augus t11 , ^QD 3
L o wVolatil e MetaE s Emission s - }'3 >m 3@ 7 % Metal s 

### Run

1 R U M ?
. ttun 3 A s 11.8 0 6.5 7 3.7F J B e a. u O. O U.1 3 O r 54, 7 4S. 3 47. 8 ffoFa l LV M 5B. D 51.f i 58. 1

LV M RegulatoryStandar d = 37 tig/m : t I Semi-Volatil e Meta l E m restarts

Ru n 1 Rni i 2 Ri m 3 Averag e 

# j P b 32 9 24 0 24 1 C d 1.3 B 1.34 1.2 1 - i kota ! SV M 23 0 24 2 24 2 r• S V M RegulatoryStandar d = 24 0 |jg/rr f 1 | Mercur yEmission s -ugfm 3 ^ 7%0 2 j R u n 2 | Ru n 3 Averag e 58. 0 5B. 2 

### UTA 5/. 9 Mercur yRegulatoryStandar d = 13D |jg/m 3

Cto(KUI^1^*fii^'!Vi l lU.OC»LS-tVTorrpV*la3D30SS a 3- 5 QSt£her2DD S

# KNS R Tabl e 3- 5 R M 2 9 Samplin g Parameter s an d Emissio n Result s - Wee k a fSeptembe r6 , 200 8
Ru n Ks . Dai n Star tTim o Sto p Tim e Uriils j 1

r14:3 5 " 16:4 6 '09-Stsp-U U
r12:2 0

r14:3 0 3

r 1Q-S3j:-[if i

r09:4 4

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Temp . Stac k Howral Q Isokinetic s in . H g ric f dsc f % v/ v % dr y T dsc; m % T29.6 0

r77.36 2 75,?S R 41. 4

r112 1

r38 5 4,69 8 10 7 " 29.7 5

" 79.26 9 78.40 7 41. 2 * •10.9 1

r38 1 5,09 9 10 3 r



### ?3T2 78.65 4 41. 8

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r38 4 •10 O _

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' 29.7 1 ' 77.05 9 77.45 2 41, 5 1 M 6

r3B 3 5,01 5 1U 4 TottlCltroiiiiuiitl'Cr l - - QuantityCalle d fid Stac k Cunc
. @7%.Q2 Slac k Emissio n Rat e LV M

|jg/m 3 lb/h r g/se c 12.1 S

B.1 G 1 .OOE-0 ^ 1.26E-0 5 2,7 9

1.74 2.4GE-05
. 3.02E-0 6 9,1 0

5.9 8 0.1OE-D 5 1.O2E-0 5 

### UM

5-2 9 '6.85E-0 5 '0.G3EO G Cadmiu m fCt l — Quantit yCollecte d Stac k Emissio n Rat e SV M



### m •ug/m 2• lb/h r pfse c 2.7 3

••1:B 3 ••- Z25E-0 5 2..i3E-0 6 2.7 4

•• •1:7 1 ••• 2.3GE-0 5 2.3 6 E-D S 2.2 0



### S-M-- 1.S4E-0 G 2.44E-0 6 " 25 5



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. @

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3Q. 6 3.7EE-U 4 4.74E-0 5 13. S

6. 7 1.20E-0 4

. 1.5 1 E-0 5 ay. o .

25. 4 3.45E-0 4 4.34E-0 5 ' 32,0 4

21. 6

r 2.8QE-0 4 ' 3.S3E-U S QuantityCollecte d Stac k Cone , @7%0 2 Stac k Emissio n Rat e N 3 ' ug/nrr

3 lb/hr ' g/se c •2.8 0

1.0 0 ' 2.31'E t C S

. 2.9JE-0 6 2.1 P

1.3 1 1.8 1 E-D 5

. 229J=-P e 2.1 0 "

1.3 7 1.05E-Q S •2.34E-C 6 ' * 2.3 3

1.5 2

r 1.99E-B G ""ZSIE-O B

- Bezslintt n EGjc

t« Q'aahfityCollecte d Stac k Cone , @ 7 % 0 2 Stac k Emissio n Rato jig/m 3 '

. !b/h r g/se c •0,2 0

0.1 3
•1 .B5E-Q b '

. 2.08E-0 7 0.2 0

•0.1 2 " ' 172E-0 S 2.17E*0 7 ' ••0.2 0

0.13 ' 1.77E-D & 2.22EA 7 0.2 0

0.1 3 '1,71'E-G B r2,16E-0 7 LVfi l Tota l = •ug/m B - 10. 2 3. 2 7. 5 G. S SV M Tota l = •ug/m B - 32, 4 . 10. 4 26. 9 G. S

WanS a Repor

t 'J i £1 2 tral.de e 3- 6 Cteuhc r2005.ENS R Tabl n 3-Q Summar yo fUW O MAC TMctat s - Septembe r8 , 200 6
Lo wVolatil e Metal s Emission s •u .g?rrr * @ 7% O z \ Ru n 1 ' Hu n 2 Ru n 3 . Averag e A s . 1.0 S 1.3 1 1.3 7 B e 0.1 3 0,1 2 0.1 3 C r 1. 7 6. 0 Tota l LV M 10. 2 3, 2 7. 5 S. 9

LV M Regulatnr ySianriar d = 9 2 |jg/m 3 Seimi-Volatil e Meta l Emission s Metal s Ru n 1 Ru n 2 Ru n 3 Averag e P b 3U. B 8. 7 25. 4 Cr t 1.8 3 1.7 1 1.4 3 Tota l SV M 32. 4 10. 4 26, 9 23. 2

SV M Regulator yStandar d = 23 0 |jg/m 3

' . .
CiVDOCllME-IWariokTWFJ-OCALSHVrcm^nDtouPaassD

Wcol b Repor

t Urf l 21i/v

^ Ace 3- 7 •deba r200 6

# A^COM

T a b I e 3 - 2 RMSttSASamplingPar a met e r s an d £mis 5 i o n Re s 1 1 It s - Tot a fC h J o r i c

fe/ P B Ru n Identificatio n Ru n 1 Ru n 2 Ru n 3 Averag e Ru n Dat e 12/08/0 9 12/09/0 9 12/10/0 9 Star tTime ' 10;O 5 . 9:4 5 11:0 0 Sto p Tim e 11:1 1 10:4 9 12:0 3 Exhaus tGa s Condition s Temperatur e (deg
. F ) 37 8 36 3 38 0 37 4 .Moistur e (volume% ) 44. 4 42, 9 43. 2 43. 5
' 'Oxyge n (dr yvolum e % ) 10. 3 10. 4 9. 3 10. 0 Carbo n Dioxid e (dr yvolum e % ) 8. 6 8. 2 8. 1 8. 3 Volumetri cFlo wRat e acf m 15,45 3 16,63 4 16,66 1 16,25 0 dscf m 5,35 2 5,96 3 5,92 1 5,74 5 Tota l Chlorin e ppmv , dr y_)

7 % 0 2 13. 4 16. 0 23. 5 17. 7 % o fStandar d 3 42.0 % 50.2 % 73.5 % 55.2 % Tota l Particulat e Matte r gr/dsc f©

7 % 0? 0.001 3 0.001 7 . 0,000 8 0.001 3 % o fStandar d b 9.7 % 13.2 % 6.2 % 9,7 %

" |-OCr 2Standar d - 3 2 pponv, dr y@ 7 % O a bParticulat e Matte rEmissls n Standard ^0.Q1 3 gi/dsc f© 7%O 3- 3Tabl e 3- 3 RU (J023 ASamplin g Parameter s an d Emissio n Result s ~ Djoxir t an d Fura n Ru n Nc . 

# j 1 Z _J i , Av e rag e Dat e Star tTim e _ — 09-lfec-n a Dat e Star tTim e 12:3 0 _ — 12:5 9 13:0 0 Sto p TTm

s 15:3 6 16:5 4 16:0 5 Unit s j |r i l | j | if! [ I Ur ? M i fi i n l? i l^ i uri^i ^ S^mpJ e Volum e dsc f 107.85 7 121.80 9 121,52 9 -117.06 5 Sampl e Volum e m 1 3 , O S 3' . 4 5 3.4 4 3.3 1 Mois tur a Conton t % W v 47. 3 - 43, 9 . 46. 1 45, 8 0 2C o rccen t ratio n %vtv (dry) 9.1 0 Ei.3 0 8.2 0 8.8 7 C 0 2Concentratio n % v, V(dry ) 6.4 3 5.1 4 7.9 0 8.1 6 .

. Isokinetic s % 9 8 9 5 9 7 9 7 Siac k Flowrat e 4,99 4 5,65 2 5,69 9 5,51 5 PCDD/PCD F Parameter s TET * (a ) p a ng/rrr 3 •TE Q p g ng/m 3 ,TE Q P 9 ng/nr f TE Q 1.0 0 675 0 7.0 1 2.3E-0 3 5.6 1 1.6E-0 3 7.1 7 2.1E-0 3 '*XOE-03" ~ 1.0 0 675 0 25, 2

"32. 2 4.1E-D 3

'"'I7VE"^03'" " 21. 9

"2976" " 3.2E-0 3 "&6E3 4 20. 6 2.1E-0 3

'*XOE-03" ~ f,2,3,4

= 7

= a-HxCD D 0.1 0 25, 2 "32. 2 4.1E-D 3

'"'I7VE"^03'" " 21. 9

"2976" " 3.2E-0 3 "&6E3 4 22. 7 6.6E-0 4 l,2,3,6,7,S-ir>s:jJl' j 0.1 0 53. 1 1.7E-0 3 49. 2 1.4E-Q 3 36. 1 1.0E-D 3 L2,3,7,B,9-HxCD D 0.1 0 35. 3 1.2E-0 3 6,9£-04" ~ 19 9 9.0E-0 4 27 . a .8.1E-0 4 OCD D 0.0 1

---- - 21 1

~m 1.2E-0 3

6,9£-04" ~ 19 9 9.0E-0 4 15 8 4.6E-0 4 ~3~8E4J 5 OCD D 0.0 1

---- - 21 1

~m 5.8E-0 5 20 0 .5.8E-0 S 13 1 4.6E-0 4 ~3~8E4J 5 2,3,7 4 S-TCD F 0.1 0 25, 1 8.2E-0 4 lTOE-04'" ' 1B. 8

• is, i' 5.5E-D 4 17. 1 5.0E-0 4

. . . n A S
. ••• . 4 . 8.2E-0 4 lTOE-04'" ' 1B. 8

• is, i' 5.5E-D 4 •20,1-• • •-2-.ee-0 4 •• ""77{iE-Q 3 •••""••'Q'S O 8.2E-0 4 lTOE-04'" ' •20,1-• • •-2-.ee-0 4 •• ""77{iE-Q 3 2,3,4,7 , S-FeCD f •••""••'Q'S O 10 8 1.8E-0 2 60. 9 8,SE^ 3 53. S •-2-.ee-0 4 •• ""77{iE-Q 3

. , 1 .AMiZi.S^CDF , 0,1 0 "o.'io " 59, 0

""SI B 1.9E-D 3 49. 2

"35. 3 1.4E-0 3

,,„,TM^.... , 2S. 5 8.3.E-0 4

"T3E-04" " 2,3,4,6,7,8- 1 (xCD F 0.1 0 97. 7 3.2E-0 3 5S. 1 "17.2 " 1.7E-0 3 ""s"0E4i4"'" ' 4.1E-0 4 46. 0

""1374"" ' 1.3E-0 3 ""3,9i'^4""" ' ""2761-0 4 L2,3,7,B,9-HxCD F • o.t o o76 T 26. 7

""ii??; * 8.7E-0 4 "s.SE^ M "'e".7E^"5" " 5S. 1

"17.2 " 1.7E-0 3 ""s"0E4i4"'" ' 4.1E-0 4 46. 0

""1374"" ' 1.3E-0 3 ""3,9i'^4""" ' ""2761-0 4 1,2,3,4,6,7,8-HpCD F o.t o o76 T 26. 7

""ii??; * 8.7E-0 4 "s.SE^ M "'e".7E^"5" " 14 2 1.7E-0 3

""s"0E4i4"'" ' 4.1E-0 4 46. 0

""1374"" ' 1.3E-0 3 ""3,9i'^4""" ' ""2761-0 4 1,2,3,4,7,8,9-HnCD F D.0 1 O.0Q 1 26. 6 8.7E-0 4

"s.SE^ M "'e".7E^"5" " 22, 8 6.6E-0 5 ' 13. 9 4.0E-0 5 OCD F D.0 1 O.0Q 1 48 . B i.ee-o s 78. 8 Z.3E-0 5 ! 23. 4 6.3E-Q 6 TOTA LTJKQ » (HS/'"* } Q.03 8 j.•!:.;!•-:•!,-;;: ! 0.02 4 0.02 0 0.02 7 TOTA LTEQ s (a B /in T7 % Oi ) 0.04 5 j.•!:.;!•-:•!,-;;: ! 0.02 8 0.02 2 0.03 2 TOTA LTEQ a fg/s ) - 9.1E-1 1 j.•!:.;!•-:•!,-;;: ! 6.5E-1 1 5.5E-1 1 7.0E-1 1 % o fStandar d " 23 % 14 % 11 % 1S %

* U.S
. EP A(1939 ) Toxi cEquivalenc yFa«o r FCDD.'PCD F Standfir d = D.2 D ng/dsc m © 7 % 0 ,

3- 4 FQtnjHryiUI D

# A3C0 M Tabl e 3- 4 R M 2 5 ASamplin g Parameter s an d Emissio n Result s Ru n Identificatio n 1 Averag e Ru n Dat e Star tTim e Sto p Tim e Exhaus tGa s Condition s Moistur e (volum e % ) Oxyge n (dr yvolum e %) OBDecO S 12:3 0 13:3 0
47. 3 9.1 0 09Dsc0 9

13:4 9 14:4 9
43. 9 9.3 0 1QDec0 9

14:0 0 15:0 0
46. 1 8.2 0 45 . 

# a

8.8 7 Tota l Hydrocarbon s ppm , dr y ppm , dr yadj . to 7 % 

### 0 2 0.6 6

0.7 8 0.2 9

0.3 4 0,1 7

0.1 8 0.3 7

0,4 4

3- 5 -tiliia v201 0I 

# UNIT3 EMISSIO N RESULT SENS R

Tabl e 3- 1 R M 2 9 Samplin g Parameter s an d Emissio n Result s Him N n 1 2 3 Dat e rU£-A-_o-0 3 Dti-Auj

-a a 07-Aug-D

8 Star tTim e , Unit ; " 12:5 6 Stu p Tiru o r15:1 4 r14:4 1 " 15:0 4 AVG S Sampljn E Parameters — flatomcfifcpressUf

A in . ti g ' 23.2 3 " 29.6 5 " 29.6 5 29.5 1 Vo;uui a Metere d dc f r00.53 9 r87.45 2 ' £)5,<M 3 r87.31 1 Sampf e Volum e dsc r 78.48 8 S4,3ii 8 83.5132 32.22 3 Moistur e % vfy 43. 0 40. 6 42. 2 0 2 atStac k %di y 11.9 9 to.j m 11.9 8 11.0 4 Ave . Stac k

Temp . T ' 37 2 ' 37 7 ' r37 4 37 4 Stac k Flowrat e dseffi t 5,66 5 ii rfS9 0 5,75 8 Isokinetic s • % 9 2 5)8 ' 9 5 9-, r i MercuryfHs! > Quantit yColtacte d p g 78. 5 30 5 ^ S0. 4 Stuc k (*'ortc
. @ 7 % 0 2 54. & 61. 1 57. 6 57 , J Stac k Emissio n Rat e 'iWb r 7 49E-0 1 R39E-C H G.19E-0 4 B.30E-CH r1.05E-C 4 ' &.44E--0 S 1-.10E-0 4 1.03E-O 4 B.30E-CH r1.05E-C 4 Tota l Cironrius i fCr t- LV M Quantit yColfeeter

f 37.5 0 21.7 6 

### ' fctack Cone
. @7%02 . •26.2 2 17.8 1 14.2 1 19,4 1 • ' 'SfackBrii-sirtiVRtfe' ' ' lb/hr ' ' ' ' 3.5>8E-tW ' •••2.02E-D4 ' r '2.7Gt-b4 ' g'ss c 4.S1E-0 5 3.45E-Q 5 2,55E-G! 3 r3.50E-O 5 Oa /aJiw i fc 'fl ) — SV M Quantit yCollects ^ 0,2 4 [><X ) 0.63 ' 0,5 9 Stac k ODFIC
. @7 & 0 - 0.1 7 0.5 3 !>.4 1 0.3 7 Stac k Emissio n Pat e JWtt f 8.D6E-0 6 5.35E-& 3 '5.40E-0 9 g/se c 2 .86E-D 7 1.02E-Q 3 7 .37 E O f rS.80E-D 7 SV M Quantit yCollecte d 83. 5 11 4 70. 1 ' 8M B Stac k Cpnis
. ©

7 % 0 2 ug/rn ? ' 5B. 4 ' . 66. 8 53. 9 Stac k Emission'Rat e M i r ' 1.O2E-0 3 S.50E-0 4 '8.24E-0 4 4.O0E-0 4 ' 1.29E-D 4 . iU ^ J S ' 1.G4E-0 4 Arseni c (Asi— Quantit yCollecte d 3,1 5 . ' 3.7 5 1.9 4 2.53 5

- Steel s ttorac. @ 7 % Q-, j •: .2-1 9 1,2 7 1.8 9 SiarJ ? grpessjorvRGt a tt^hr 3.O1E-05
. '2 .73&Q 5 Cffefi C
. ..3,79E-fl 3 4.24E-0B ' 2.27E-D 8 ' 3.43E-0 6

• Quan % ejecte d • M ••0.-2 0 . •' •0.2 0 0.20 ' a?. o •

. Sfec k Caw , @ 7 % 0 ^ 0 .1 4 0 ,1 2 0.1 3 0 .13 ' StBC k Emissio n Rai n lb/h r 1,0lK-« ?
. •1.80E-O S T.BSE^ B "1.85E-0 6 g/se c 2 .4tE-0 7 Z26E-0 7 •2 .34^-0 7 r2.34E-0 7 LV M Tota l - 28. 6 20. 1 15. 0 2 1 j » Tgia l = 'ng/rr f ''53.8"" ' 87. t 46. 2 67. 3

CSDOCyME-t'ilt!arith.'7V/I'LCICALS-1 , iTamiAnDlEst390SS

a Weolf a Repor t Uni t 3 draAdD

C 3- 2 Ootaber2tlO BTabl e 3- 2 Summar yo fHW C MAC TMetal s

. Lo wVolatil e MetaJ s Emission s - jjg/n f@ 7 % o 2 Metaf s R u n 1 R u n 2 R u n 3 Avera§ & A s 2.2 0 2M 1.27 " B e 0 J 4 0.1 2 0.1 3 G r 26. 2 17. 8 14. 2 Tota l LV M 28. Q 20. 1 15. 6 21. 4

L V M Regulator yStandar d = SejDi-Vo)a!H e Meta l Emission ©
- ra'in 3@ 7%Q s Me tate R i m 1 R u n 2 R u n 3 Averag e P b 58. 4 66. 6 . 45. S C d 0.1 7 0.5 3 0.4 1 TofaJSV M ss. e 1 07. 1 48. 2 57. 3

S V M RfisufattJr yStandar d = 23 0 \ig!nf

..... . Mercur yEmission s -pg/m 3@ 7 % 0 2

S i m 1 R u n £ R u n 3 Averag e 54. 3 61. 1 57, 8 57- 9 Mercur yHeguMor yStewar d = 130|jg/m 3

C:TOCUME-1 l

Waridi,TVVJLOWL&-1vremp^aiBsl5SDS[:Cl W e:(j II ? tepon Unit

s drafLdo s 3- 3Ta b r e 3^ 2 R M 5/2 6 ASam p [fri g Parameter s an d Emissio n Result s - Tota l Chloride/P M Ru n Identificatio n Ru n 

### 1 Ru n 2 T?u n 3 Averag e Ru n Dat e 12/01/0 9 •12/02/0 9 12/03/0 9 Star tTim e 11:1 6 .10:0 5 10:4 8 Sto p Tim e 12:2 1 1 1-0 9 11 :5 1 Exhaus tGa s 'Condition s Temperatur e (deg , F ) 37 7 37 7 37 8 37 7 Moistur e (voJum e % ) 43. 4 46. 9 42. 1 44 . 1 Oxyge n (dr yvolume% ) 9. 5 7. 8 10. 4 9. 2 Carbo n Dioxid e (dr yvolum e % ) B. 3 10. 0 8, 0 6. 8 Volumetri cFlo wRat e acf m 14, 1 G 7 1-4,81 7 15 ,34 0 14,75 1 dscf m 5,03 9 4,87 4 5,57 3 S.1G 2 Tota l Chlorin e ppmv , dr y@ 7 % 0 2 10 . 7 9. 8 21. 5 14. 0 % o fStandar d B 33.5 % 30.5 % . 67 .1 % 43.7 % Tofa ! Particulat e Matte r gr/dsc f@ 7 % 0 2 0.001 7 0.001 5 0.001 6 0.001 6 % o fStandar d * 13.0 % 11 ,9 % 12 .3 % 12.4 %

fl HCra ? SlafldsiEl=32ppfiriv i dry@7%O a bParticulat e Mat.sr-

Emissio n Standard = 0.0 1 3 gr.'csc f@ 7%O j

3^ 3 Hafuar y201 Q

# A..COM Tabl e 3- 3 R M 0023 ASamplin g Parameter s an d Emissio n Result s - Dioxrn s an d Furan s Ru n No . 1 2 3 Averaq e Dat e Sn-Dsc-O S 02-Doc-C S :;;:;: : :y:\;: : ;;;:i; : :;:;:;x;0;;:;:.:;:;.;:;:". ; 51a. 1 Tim e 13:4 1 12:3 0 13:1 8 : ::-: : ' : :-:-: : ' v :;;:;: : :y:\;: : ;;;:i; : :;:;:;x;0;;:;:.:;:;.;:;:". ; Ste p Tim e 16:4 9 15:3 5 16:5 3 !•:• . :• : v—'::::•::• : ::>:~:

: A' : •:•:-:•.• : Unit s '!-:;.;!v.;.;Xv-;";-Vv;- ; : : :v : : : : :o :':lv ': : :': : : : : : :o:':o: : Sampl e Vol'm e dsc f 106.67 9 112.72 9 120.26 3 113 .23 1 Sampl e Volum e m 1 3.0 2 . 3.19 3.4 1 3.2 1 Moistur e Conten t %vtv 48, 2 43. 1 42. 3 46. 2 0 2Concentratio n % v, V(dry ) 7.3 0 7.3 0 9.5 0 8 .0 3 C 0 2Concentratio n % v, V(dry } 9.9 3 . 9.7 8 8,1 5 9,2 9 Isokinetic s % 10 9 10 7 S 3 10 5 Stac k Flowrat e dscf m 4,45 2 4,81 0 5,57 3 4,94 S PCDD/PCD F Parameter s TEF(a ) P S TE Q p g nqlnf TE Q P 9 ng/m J

TE Q 2,3.7,8-TCD n 1,0 0 5.3 1 1.9E-Q 3 i 3.6 0 1.1E-D 3 4.6 0 . 1.3E-0 3 l,23,l,\i-?eCDD 0,5 0 25. 1 4.ZE-0 3 17. 0 17, 3 2.7E-0 3 21. 4 3.1E-0 3 [,2,3,4,7,8-HjiCD D . 0,1 0 27. 2 9.GE-0 4 17. 0 17, 3 B.4E-0 4 18. 1 5.3E-0 4 1,2,3,6,7,8-IijcCD D 0,1 0 59. 5 ZOE-0 3 40. 0 1.3E-0 3 41. 4 1.2E-0 3 d.i o 37. 7 1.2E-0 3 27. 3 8.6E-0 4 26, 7 7.8E-0 4 1,2,3,4,6,7.8-1- 1 pCD D 0,0 1 40 6 1.3E-0 3 25 3 7.SE-0 4 

# j 27 2 8.0E-0 4 ocn o o.oo t 54 0 1.SE-0 4 ! 33 0 1 .OE-0 4 34 8 1.CE-0 4
• • • 23;7^TCT>P G.-1 G •33.$- • •11E-03- - I -25, 8 •• '..&.1E-G 4 . . •30. 5 •• -9,1£-0 4 • 13,3,7,8-PeCn F 0,0 5 46 . 2 7.6E-0 4 ""1.6E-02." " 31,8-

"6 4 S " 5.DE-0 4 39. 2 5. 8 E-0 4 2,3,4,7,8-VeCD F 0.5 0 93, 3 7.6E-0 4 ""1.6E-02." " 31,8-

"6 4 S " 1.0E -Q 2 83. 0 1.3E-0 2 0.1 0 72, 0 2 ; 4E-Q 3 43 . 2 1.4E-0 3 51. 5 1.5E-0 3 0.1 0 61. 3 2.0E-O 3 39. 2 1.2E-0 3 49. 8 1.5E-0 3 0.1 0 88, 4 2.9E-0 3 53. 3 1.7E-0 3 71, 1 2.1E-0 3 1,2,3,7.8,9-HxCP F 0.1 0 20. 5 6.8E-0 4 13.2 - 4. 1 E-0 4 15. 8 4.6E-0 4 1,2,3,4,6,7,8-IfpCD F 0.0 1 23 3 7.7E-0 4 12 3 3.8E-0 4 "T9E-05 " 13 1

"15.7 " 3.&E-D 4 "4.6E"05 " 1,2,3,4.7,8,9-HpCDl - 0.0 1 [23. 5 7 .8E-0 5 12 3 3.8E-0 4 "T9E-05 " 13 1

"15.7 " 3.&E-D 4 "4.6E"05 " OCD F 0.00 1 85. 2 2.8E-0 5 45. 9 . 1.4E-0 5 40. 2 1.2E-0 5 TOTA LTE,Qs(ug/ni J ) = 0.03 9 .;:-:- . 0.02 4 :;>!;"- : 0.02 8 0.03 0 TOTA LTEQ s (ug /m 1 @ 7 % 0 3 ) 0.03 9 0.024 :;>!;"- : 0,03 5 0.O33 TOTA LTEQsfe r < 0 ^ B.1E-1 1 5.4E-1 1 :;>!;"- : 7.5E-1 1 7 ,0E -1 1 % o fStandar d 6. = 20% 12 % :•:-:• • 17 % 1S %

aU.S.EPA(19iU.S.EPA(1989 ) ToricEquwalenc yFacto r bPCDQ'PCD F Standar

d = -3.2 3 rig/dsc m @ 7%0 2

3^: .-BSni«?201 0

# AICOM Tabl e 3-4

R M 25 ASamplin g Parameter s an d Emissio n Result s Ru n identificatio n 1 Averag e Ru n pat e Star tTim e Sto o Tim e OlDecO Q 13:4 1 ' 14:4 1 02OSC0 9

•12:3 0 13:3 0 03Dec0 9

13:1 8 14:1 8 Exhaus tGa s Condition s Moistur e (volum e % ) Oxyge n (dr yvolum e % ) Tota l Hydrocarbon s ppm , dr y ppm , dr yadj . 7 % 0 2 46. 2 .7.3 0 0,9 1 0,9 3 43. 1

7.3 0

. 0.6 4 0.6 5 42. 3

fi.50
0.3 5 0,4 2 46, 2

8.0 3
0.6 3 0,6 7

3- 5 Siimd ' wi n

# UNI T4 EMISSIO N RESULT SENS R

Tabl e 3- 2 R M 2 9 Samplin g Parameter s ^nt l Emissio n Hate s Ru n No . Dat e t Startlim e S(u p Tim e Unit s 1

r -15:37 2 K 22-Aiii } (B

t " 1J):U 0

r13:0 1 3

'.23-Aug-O B

r08:5 5
r10:5 9 AVG S Barometri cPressur e Velu m e Msiersrt Sampl e Volum e Moistur e 0 2AStac k Aw#. Stac k

Temp . Stac k Flowrat e i isokinetic s in . H1 5 dc r dsc f & dr y * F dscf m % r

72.GA

rgo. TM 6!J.Q2 3 39. 0 ' 12.2 7

r39 0 17,26 0 10 1 "

2^m * 89.78 4 flU.43 3 33.5 . r12.1 3 ' 38 8 1725 5 im " 29.6 4

"31.42 0 89.26 4 4U.3

r'i1.G 3

r33 4 17,18 9 102 " 29.6 2

r90.71 4

r12,0 1 ' 39 1 17,24 1 j m . Quantit yCollecte d Stac k Cone
. @ 7%Oi Stst k Emissio n Rsfe.
. ug/nr3

Ih/hr
. g/se c 59. E

37. 9 1 .53E-fJ 3 1.93E-Q 4 387

24. 4 9.99F-D 4 T.26E-0 4 12. 3

25. 0 1.08E43 3 1 mv-.m r4E. 9

23. 1

r 1.2DE-0 3 Tntn l Chromiu m (C.r)

— Quantit yColinde d Stac k Coac.@7 % O j FUqc k Emissio n Kat e LV M

Hg • ut]/rn 3 Ih/h r g/sa c 3.1 ?

1.9 3

. aOIE-0 5 1.0 1 FD 5 S.2 0

3.9 6 1.62 E-0 4 ' 2.04(7 flfi •8.4 0

3.7ft T.B3S0 4 •2.05E-Q 5 r5.2 7 '

3.2 4

r 1.35E-Q 4 " 1.70E-O 5 Cadmiu m fC(T

> — Quantit yCollecte d Stac k Cnnc
. @7 % Q 2 Stan k Emissio n Rati * SV M

|IS7m 8 lb/h r •g/se c 0.8 0 •

0.5 1 2.05U-D 5 2.58E-0 6 1.2 7

- 0.8 0 3.2 7 R-t C 4M2E-fl 3 

### \:&

0.7 6 3.29E-0 5 4.14E-E 6 ' 1.1 2

0.6 9 '2.87E-D 5 " 3.6 1 E-D B Quaniit yCollected Stac k Cone
. @.7 % 6 2 , Stac k Emissio n Rat e SV M m lb/h r ' gfee c ' 34 3

21. 8 •8.8 1 E-m •1.1 1 £0 4 49. 1

30.9 - 1.27E4 B 1.B0E-D 4 •28, 3

. 1.13E-0 3 1.43E-0 4 ' 4ZB 3

26. 4

r1-.09E-03

r1.3BE-0 4
' -Aias<siiiefAsTr~ •-Quantity-.Collecte d .

. Stac k Cone'©7 % Oi • •Stac k Emissio n Rat e M 9 ug/m 3 lb/h r _g/$e c '4,5 2

3.0 7 1.24E-J H 1.5BE-D 5 9.B2 '

6.1 9 2.53E-B 4 •3.19E-0 5 " ' 16,2 2

9.S 9 ' 4.13B04 - 5.2 1 E-Q5 " . 10.2 9

" 6.2 8 '2.63&04 - " 3.32E-D 5 B e alliu m (Be i - . QuantityCollecte d Slac k Ctmc
. @7%0 2

.' Slac k Emissio n Rat e ug/m 3

Ih/h r g/se c 0,2 0

0.1 3 5.13E-D 6 B.47E-0 7 0.2 0

0.1 3 5.1GE-0 B B.5GE-Q 7 0.2 0

0.1 2 5.09E-Q 6 6.42E-G 7 r0,2 0

0.1 2 ^5.13E-0 B " 6.46E-0 7 LV M Tota l - ug/m 3 5.2 ' 10. 3 13. 5 SV M Tota l = jjg/m 3 22. 3 ' 31 7 271""" " 21 'jf - '" C-UJOCUME-f'Jsarteh.lWllLOCALS-liTeftiplnotesDstiSOtf 3- 3 Orf£/ber£DD EENS R Tabl e 3-3

Summar yo fHW C MAC TMr-taf a
L o wVolatil e Metal s Emissio n 5 7 % a , Melul s fturt 1 Ru n 2 R -Jii ! 3 Averag e A s 3.0 7 B.1- 3 9.5 9 B e 0 .1 3 0.1 3 0.1 2 C r ' 2. 0 4. 0 3. 8 Iota ! LV M 5. 2 1D. 3 13. 5

I .V M Regulatorystandar d = 9 2 ug/m.< * Ssmi-Volatif e Meta l Emission s

Ru n 1 Ru n 2 Ru n 3 P b 21. 8 30: 9 26. 3 C d 0.5 1 0.S D Q .7 B Tofa tSV M 22. 3 31. 7 27 , 1 27. 0

SV M RegulatoryStandar d - 23 C |jp f/rn 3 Mercur yEmission s -\i_tm z @ 7%0 2 Ru n 1 Ru n 2 Ru n 3 Averag e 37. 9 24. 4 25. 0 29. 1 MercuryRegulatoryStandar d = 13 0 pg/m 3

C:TOOTOr^-l\WaricKT\iVpLCCAL3-nTcnipVMt!sP305SI J VMOSff l B3.do c

# AZCOM Tabl s 3- 2 RW [ 5/2 6 A-Samplin g Para meter s a n d Emis s la n Result s - Tota E Chl o rscfe fP M R u n Identification - Ru n 1 Ru n 2 Ru n 3 Averag e Ru n Dat e 12/16/0 9 12/17/0 9 • 12/ 1 8/0 9 Star tTim e 11:3 8 9:4 6 9:5 0 Sto p Tim e 12:4 1 10:4 3 10:5 2 Exhaus tGa s Condition s Temperatur e (deg
. F ) 38 6 38 7 3B 7 38 7 Moistur e (volum e % ) 35. 7 35 . 2 35. 7 35, 9 Oxyge n (dr yvolum e % } 12. 7 12, 5 12. 6 12. 6 Carbo n Dioxid e (dr yvolum e % ) 5. 7 5. 9 '.5. 5 5. 7 Volumetri cFlo wRat e acf m 46,60 3 46,84 7 44,63 3 43,03 4 dscf m 18 : 84 5 18,64 5 1 7,70 4 18 .39 8 Tota l Chlorin e ppmv . dr y@ 7 % 0 2 - 29. 2 36. 4 3. 5 • 23 , 0 % o fStandar d * . 91.3 % 114 % 10,8 % 7 1 .& % Tota l Particulat e Matte r gr/dsc f@ 7 % D 2 % o fStandar d b 0.002 3 0.002 0 0,004 2 0.002 B 18.0 % •15.1 % 31.9 % 21,7 %

J HCICI j Starearr

J = 32ppnv . dr

y© 7%0 2 5ParSci,-'el &Mate rErnissb n Standard = 0.01 3 gr/dsc f© 7 % D z

3-3 ' Pabruar y2C1 0

# ACCO M Tabl e 3- 3 R M 0023 ASamplin g Parameter s an d Emissio n Result s - Dioxi n an d Fura n

Ku n No . 1 2 3 Averag e Date 16-Dac-0 9 1S-DQ^ 9 " SlsrtTim e 13:5 4 12:3 0 11:4 5 Step Tim e 16:5 9 15:3 5 14:5 0 ; ':-\ : ' : . " : . V:'! . Unit s Sampl e Vo'um e dsc f 137.45 5 131,66 7 131.71 7 133.65 3 Sampl e Volum e •rn 3 3.6 $ •3.7 3 3,7 3 3.7 8 Moistur e Conten t % v/v 35. S 36. 4 36. 0 36 . 0 0 2Concentratio n %Yf'v(dry ) 12.6 0 12.4 0 12.3 0 12.4 3 C 0 2Concentratio n % v,'v( d iy ) 5,6 6 4..B7 5.5 4 5 .3 S Isokinetic s % 10 0 10 1 9 9 10 0 Stac k Fbwrat e dscf m 18.60 1 17 S 65 5 18,00 2 18,08 9 PCDD / PCD F Parameter s TE F (a) p g rcg/rn 1 TE Q p g TE Q p g ng/rn 2 T E Q 2 ! 3,7,S-TCD D 1 .0 0 18. 8 4.8E-0 3 "3.7E-02 " 24. 6

""34 0 " S.01MJ3 : 20. 7 5.5E-0 3 1,2,3/7,8-PeCD D 0.5 0 28 3 4.8E-0 3 "3.7E-02 " 24. 6

""34 0 " 4.5E-0 2 31 1 4.2E-0 2 1,2,3,4,7,8-HxCD D 0.1 0 32 0 '924" " a ,2E^Q 3 ; •.Z4E-02" " 28 7 7.7E-0 3 28 6 7.7E-0 3 "'24E-02'" " '!,2,3,6,7,S-HxeD D 0.1 0 32 0 '924" " a ,2E^Q 3 ; •.Z4E-02" " 85 4 2.3E-0 2 90 1 7.7E-0 3 "'24E-02'" " 1,2,3,7,8,9-Hx.CD D 0.1 0 37 S 9.7E-0 3 28 5 7.6E-0 3 38 8 1.0E-0 2 l,2,3.4,fi,7,S-HpCO D 6.0 1 ' 2,94 4 7.8E-03 . 2j44 2 6-5E-0 3 2,69 5 7.8E-0 3 OCD D 0.00 1 1,24 5 3.2E-0 4 98 7 2.6E-0 4 1,18 9 3.2E-0 4 -2J,7,8~TCD F 0'.1 0 90, 2 2.3E-0 3 S7. 5 2.3E-0 3 90. 4 2.4E-0 3 ••-l^V^-PeCD F 0:0 5 •1-32 - • •1:7E-03 - • ••11 9 •• •1-.-6E--03 " . . 1 5 1 .. . •2:0E43 3 • 2,3,4,7^-PeCD F 0.5 0 60 8 7.8E-0 2 51 0 5.8E-Q 2 69 2 S.3E^0 2 [ ,2,3,4,7,S*HxCD F 0.1 0 28 2 7.2E-D 3 24 2 "292" " 3.5E-0 3 ''7.8E4T3" ' 29 1 1

'"379"" " 78E-0 3 L,2,3,6 , 7,8-HKCD F 0.1 0 fj'i' 6 36 7 : 7.2E-D 3 24 2 "292" " 3.5E-0 3 ''7.8E4T3" ' 29 1 1

'"379"" " 1.0E-0 2 2,3,4,6,7 t R-HxC!D F 0.1 0 fj'i' 6 86 0 ; 2.2E-0 2 TBE-OY " "Z"BI^03" " 61 5 1.6E-D 2 84 8 2.3E-0 2

_L2,3,7,8,9-HxCD F D.1 0 

### ao i 96. 5

"957"" ' 2.2E-0 2

TBE-OY " "Z"BI^03" " 55. 3

"730" " 1.5E-0 3 86. 6 2.3E-0 3 l.2,3,4A7,K-H_pCD F D.1 0 

### ao i 96. 5

"957"" ' 2.2E-0 2

TBE-OY " "Z"BI^03" " 55. 3

"730" " 2.0E-Q 3 1,00 7 2.7E-D 3 1 i2j3 1 4,7.8, 9 - I [p C D F 0.0 1 13 2 3.4E-0 4 • 78. 9 2.1E-C 4 13 0 3.5E-0 4 OCO F 0.00 1 21 0 5.4E-0 5 13 3 1 3.6E-0 5 20 1 5.4E-0 5 TOTA L TEQ s (nR/m 3 ) 0.21 8 -•" ' '•: 0:20 4 • • 0.24 1 0.22 1

. T(JTA L TEQ s (ag/m 1 @ 7 % On ) = 0.36 3 -•" ' '•: 0 .33 2 • • 0 .383 0,36 1 TOTA L TEQ s (gis)

= - 1.9E-0 9 • : .' : .'. . 1.7E-0 9 f . ; ;. ; _• • 2.0E-0 9 1.9E -0 9 % o fStandar d " = 91 % 33 % B7% 90 %

aU.S.EP A(1939)TDM s Equivalenc yFacto r 1 PCOD/PCD F Standar d = 0,4 0 ns'dsc m © 7% o .

3- *

# AZCOM Tabl e 3- 4 R M 25 ASamplin g Parameter s an d Emissio n Result s Ru n Identificatio n 1 Averag e Ru n Dat e Star tTim e Sto o Tim e 1SDecQ 9 14:0 7 15:0 7 17Dec0 9

12:5 1 , 13:5 1 18DecG 9

11:4 5 12:4 5 Exhaus tGa s Condition s Moratur e (volum e % ) Oxyge n (dr yvolum e % ) Tota l Hydrocarbon s •ppm , dr y ppm , dr yad}, 7

% 0 2 

### 35. 6

12,6 0
0.8 1 1,3 3 36, 4

12.4 0 

### 0,8 6 

### 141 36. 0

12.3 0
0.3 5 Q.6 1 36. 0

12,4 3 0,6 8 1.1 2•• - i



# SYSTE M REMOVA L EFFICIENC Y(SRE ) FO R UNIT S 2 , 3 AN D 4

i20Q S Wl&tal s an d 200 3 HC J Testin g Remova l Efficiencie s | , . I 1 | Uni t2 (LVM ) Remova l Uni t3 (LVM ) Remova l Uni t4 (LVM ) REmava i Em . Std. : 9 2 ug/dsc m Ru n Efficienc y(RE ) Em . Std,'
. B2 ug/dsc m Ru n Efficienc y(RE ) iEm . Std. : 9 2 ug/dsc m Ru n Efficienc y(RE ) (9/QB ) (% } (3/QB ) (% ) 1 (8/0B )

.. . f» )

.... . .. . f» ) 1 99.9997 3 89.899.1 9 1 S3.3995 S 2"" ' 89.9999 1 i 99- . 9 9 93 5 2 99.9391 6 3 59,9997 9 ' 3 93.9395 4 3 99.9388 2 Av g 99.5996 1 Ay g S9.&993 6 Av g 39.9991 9
Uni t2 (SVM ) Remova l Uni t3 (SVM ) Remova l Uni t4 (SVM ) Remova l Em . Std. : 23 0 uqJdsc m Ru n Efficienc y(RE ) Em . Std. : 23 0 uc|/dsc m Ru n Efficienc y(RE ) Em . Std. : 23 0 ug,'dsc m Ru n Efficienc y(RE )

(&/Q8) (B/OB ) (% > (8/08 ) • m 1 89.8993 6 ! l ' 98,9987 5 1 99.9963 3 2 99.8997 7 2 98.9884 2 2 99.9979 5 3 99.9994 2 " 3 " 98.0889 7 3 &9.&9S1 9 Ay g 99.9995 2 Ay g 99.9987 1 Av g 9S.93B2 4 j Unit2{Hg ) Remova l Uni t3 (Hg ) Re m ov a i Unit4(Hg ) Remova l Em . Std. : 130ug/dsc m Ru n Efficienc y(RE ) !Em . Std. : 13 0 uq/dsc m Ru n ' Efficienc y(RE ) Em : Std. : 130ug/dsc m Ru n Efficienc y(RE )

(8/08 ) C* > . (8/08 ) I m . . (S/OS ) {% ) I m . . 1 65.6 1 j i " 53.2 5 1 94.0 5 2 51.6 5 2 57.3 6 2 86 . T7 3 50.0 6 3 ! 54.5 6 ' 3 95-9 1 Av g 55.7 7 Av g ; 55.0 6 Av g 95-3 B
Unlt 2 (HCT/CI2 ) Remova l Unrt3(HCI/CJ2 ) Remova l Uni t4 (HCI/CI2 ) Removal : Em . Std. : 3 2 ppm v Ru n Efficienc y(RE ) Em . Std. : 3 2 ppm v RM n Efficienc y(RE ) Em - Std. ; 3 2 ppm v Ru n Efficienc y(RE ) (12/09 ) (%) (12/09 ) j

_(% > (1209 ) (% ) 1 90.8 6 : " "i " 99,9 9 1 99.1 8 2 . •09.6 3 ! 2 99.8 9 : 2 98.9 2

. 3 •99.7 1 i 3 99,7 7 ' 3 " 99.9 1 Av g '••89.8 0 ! Av g '9&.S 5 •Av g ' 99.3 4

# Incinerato rProces s Descriptio

n Uni t2

## 2. 0 incinerato rProces s Descriptio n 

# AECOM

2. 1 Proces s Overvie w VEoli a operate s 2

Fixe d Heart h Dua l Chambere d Incinerator s (Unit s 2 an d 5 ) an d on e rotar ykil n incinerato r (Uni t 4 ) atth e Sauget , I Lfacility. Th e too fixed heart h unit s ar e rate d a t 1 6 millio n Btu/h reach , incineratio n Uni tNo . 3 i s a mirro rimag e o fUni tNo . 2 . Bot h o fthes e unit s hav e thei row n wast e handlin g system s a s describe d i n th e section s that follow
. Th e oni ydifferenc e bein g Uni tNo , Z i s equippe d wit h four(4 ) baghous e moduies , whil e Uni tNo , 3- i s equippe d wit h thre e (3} baghous e modules . However , eac h incinerato ri s operate d identicall ywit h onl ythree-baghous e module s i n servic e durin g operation . U rit4 i s rate d atS O millio n Btu/h ran d i s equippe d wit h its ow n tan k far m system , dru m storage , bul k solid s storag e an d feed systems . 

### 2. 2 Wast e Feec F System s {4 0 CF R § 63,1207(f){1J(ii}(c) an d (f)(1){ifi)(0 ) an d (E)] 2.2. 1 Unc i 2 Liqui d Wast e Fee d Syste m an d Blendin g Operation s Th e fixe d heart h incinerato ri s designe d t o receive containers , aqueou s liqui d wastes , organi cliqui d wastes , specialt yFiqui d feeds , gase s an d direc tinject[[quid s fe d throug h th e aqueou s o rorgani cliqui d fee d systems . Thes e unit s ca n receiv e an ycombinatio n o fwaste s - liquid , semi-solid , solid-o rgase s - wit h a hea tvalu e o f u p to 1 6 millio n Btu/hr
. Uni t2 i s supporte d b ystorage/blen d tank s locate d i n Tan k Far m # 1 Rate s o ffee d ar e contnoffe d a t eac h incinerator , Segregate d liqui d waste s ar e store d unti i utilise d i n th e wast e blendin g facilities , A ttha i time , • •x&'&M<[[quids-ar e delivered-t o the-blendin g tank s wher e th e dail yliquid-fee d tothe'inoineratoris'TQrrriutatect r 'te'Ste'o!, V•' ] an d released to th e incinerator , Biendin g o fstore d Eiqul d waste s t o achiev e optimu m heatin g valu e an d

viscosit yfo rincineratio n take s plac e i n Tank s 2 , 4 , 6 & 8 , Si s additiona l tank s (10 , 20 , 30 , 40 , 5 0 & 60 ) ar e • use d t o segregat e differen twasf a strea m type s forblendin g o fliqui d fee d t o th e incinerator . Severa l criteri a ar e importan ti n designin g a blen d fro m availabl e waste s tha t hav e bee n segregate d principall yb yphysica l an d chemfca l properties , Thes e includ e compatibility , prope rrang e o fheatin g value , an d permi trestriction s

. regardin g elementa l compositio n (base d o n emissio n limitations)
. Th e materia l i s transferre d throug h abovegroun d pipeline s fro m th e tan k far m t o th e incinerator , Pipeline s use d t o transfe rliqui d organi cwast e an d aqueou s wast e ar e equippe d wit h strainers . I n -complianc e wit h th e Benzen e NESHAP , al l tank s ar e vente d t o individua l carbo n adsorptio n canister s fo r remova l o forganic s befor e vapo ri s discharge d t o th e atmosphere . Eac h carbo n adsorbe rcaniste ri s essentiall yequivalen tt o a 5 5 gallo n containe ro rgreater , i fnecessary , Al l tank s ar e equippe d wit h conservatio n vents , i n additio n t o th e carbo n caniste radsorber . Al l tank s ar e grounded , an d flam e arrester s ar e i n sta l le d betwee n t h e c a rb o n a d sorter s a n d th e 1 a nks , 2.2. 1.1 O rga n fcan d A q ueo u s Li q ui d Wast e Feed s Th e liqui d wast e injector s use d i n th e combustio n chamber s ar e air-atomizin g injectors ; Thes e ar e use d .fo r injectio n o fhig h Btu , lo wBt u liquid s an d specialt yfee d liquids . Dua l fiuiti injectio n nozzle s wil l b e use d fo r atomizatic n o fth e waste . Eac h o fth e injector s is.rate d a t0-30 0 gpt vTh e liqui d wast e fee d nozzle s ar e serve d b yparalle l redundan tpump s an d recirculatio n system s wit h bac k pressure'control ,•f2S Februar y»1 0

# AZCOM 2.2 .1 . 2 Packagec

fWaste Fee d Container s o fwaste s ar e sample d an d analyze d afte rreceip ti n accordanc e wit h th e facility' s Wast e Analysi s Pfan
. Thes e waste s ca n the n b e delivere d directl yto Uni t2 o rrepacke d int o smal l combustibl e container s a t th e facility
. Fiberboar d o rplasti ccontainer s (full yo rparti'atyful l o fwaste) , u p I D 4D-ga1o n size , ma yb e charge d directl yto th e primarychamber . Thes e wil i b e receive d a t th e doc k adjoinin g eac h fixe d heart h incinerator , an d charge d t o th e incinerato rwithi n 2 4 hour s o rreturne d t o permitte d storage . Solids , usuall ypackage d i n plasti cQ rf i b e rtoar d containers , ar e introduce d int o th e incinerato rthroug h a PL C controlle d airlock-ra m sysie m locate d a t th e lowe rfront o fth e primar ychambe ro fth e incinerator . Th e airloc k i s compose d o fa refractory-line d dcor , a doo rint o th e airloc k enclosure , an d tw o pneumati crams , Th e actio n o fth e feede ri s a s foriows :

* Wit h m e incinerato rdoo rclosed , th e airloc k doo ri s opened , < ? Th e firs t pneumati cra m (loa d ram ) pushe s weighe d charge s o fwast e int o th e airloc k chamber . » Th e airloc k

doo ri s closed . * Aswitc h i s activate d eithe rautomaticall yo rmanually , whic h open s th e doo rto th e incinerato ran d actuate s th e ra m (charg e ram ) tha t pushe s th e wast e int o th e incinerator . Th e ra m the n retract s an d th e Incinerato rdoo rcloses . 2.2.1. 3 S petlartyLl q ui d a n ifGaseou s Wast o Feed s Specialt yFee d System s associate d wit h Incinerato rNo . 2 ar e a s follow s

» Specialt yFeede r•
•Compresse d Ga s Cyiinde rFee d Syste m » Direc tInject Liqui d Fee d Syste m 

### 2. 3 Manufacturer , Mak e an d Moda l o fth e incinerato rJ4 0 CF R § 63.12Q7(f)(1Hiij)(A) I 2.3. 1 Combustio n Chambe rari d Burner s [40 CF R §63.12D7(f}(1 )(m )(B ) an d (C ) Incinerato rNo , 2 feature s a two-stag e combushor tprocess , ignitio n o fwast e materia l take s plac e i n th e primar y(lower ) combustio n chambe r(PCC)
. Asecondar y(upper ) combustio n chambe r(SCC ) serve s a s a n "after-burner' ' fo rproces s gases . Ignitio n o fth e wast e take s plac e a ttemperatures ' i n e>ccess o f170 0 degree s F , Th e secondar ycombustio n chambe rmaintain s a minimu m temperatur e o fapproximatel y1&00 degree s F . Th e fixe d heart h incinerato ri s fabricate d o fcarbo n steei . Th e primarychambe rha s a n externa l diamete rof9 feetan d i s 17, 5 fee tlong . Th e interio rwall s o fth e chambe rar e line d wit h approximatel y1 0 inche s ofbric k refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y7*2" . Th e cross sectiona E are a o fth e chambe ri s thu s 40. 3 squar e feet
. Tabl e 2-2 provide s a summar yo fth e incinerato r desig n specifications
. Liqui d an d soli d wast e feed s ente rth e lowe rchambe ro n th e front-fac e o fth e chamber . Th e primaryburne r an d th e specialt yfee d injecto rar e locate d nea rth e front-fac e o fth e chambe ran d ar e mounte d tangentially .
2- 7 Februar y201 3

# AZCOM Th e primar yburne ri s a Nort h America n burne rrate d a t 12, 3 millio n Btu/hr
. an d i s use d i n th e lowe rchambe r to maintai n permitte d temperatures , i t wil l bur n onl ynatura l ga s o rNo . 2 fue l oil . Th e burne rsyste m i s supplie d wis h combustio n gi rata stati cpressur e o f30 " wate rcolum n (WC) , Th e pSoi fo rth e primar yburne rwil l bur n natura l gas . Th e fue l syste m fo rth e lowe rchambe r(an d secondar ycombustio n chamber ) i s controlle d bya Factor yMutual . approve d burne rmanagemen tsyste m complet e wit h interlock s an d safet yvalves . 2.3. 2 Secondar yCombustio n Chambe r Th e secondar ycombustio n chambe r(SCC ) i s a horizontal , cylindrica l chambe rthat ha s a n externa l diamete r o f9 fee tan d i s 17. 5 fee tEong . Th e tnteriorwall s o fth e chambe rar e line d wit h approximatel y1 0 inche s rj fbric k refractoryan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y7'2" . Th e cross secti o n a tar e a ofth e cha m b e ri s t h u s 40. 3 s q u ar e feet , Followin g ignitio n o fth e wast e materia l unde rcontrolle d o rstarved-ai rcondition s i n th e lowe rchamber ; off- ' gase s trave l throug h a refractory-line d flu e ga s passag e int o th e upper-chamber , whic h act s a s a n afterburner, Turbulenc e i s achieve d byth e tangentia l introductio n o fai ran d additiona l fue l i n th e uppe rchamber . Th e SC C i s equippe d wit h on e burne rmounte d tangentiall yo n th e sid e o fth e chamber . Th e burne ri s a Nort h America n burne rrate d a t 6. 0 millio n Btu/h ran d i s fuele d wit h natura l ga s o rfue l oil , A s wit h th e primarychambe rburner ; th e SC C burne ri s supplie d wit h atomizin g ai ran d i s equippe d wit h a burne rmanagemen tsystem , Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof fwhe n ther e i s a Joss-o f-flame, , combustio n .air . supply , .fue l .pressure , atomizing , air.pressure , .or.pilo tburner . Leavin g th e uppe rchamber , th e ho tga s strea m travel s throug h 2 8 fee to frefractory-Sine d stac k section s befor e reachin g th e starto fth e ga s scrubbin g system . Th e combine d volum e o fth e uppe ran d lowe rchambers , th e flu e ga s passag e an d th e ho tcrossove rsectio n i s approximatel y156 7 cubi cfeet
. Th e tota l retentio n tim e o f combustio n gase s withi n th e syste m i s approximatel y5 seconds . 2.3. 3 Locatio n o fCombustio n Zon e Temperatur e Devic e [40 CF R § S3.1207{f){1)(xix) J Th e thermocoupl e tha t monitor s temperatur e i n th e primarycombustio n chambe ri s locate d o n to p o fth e chambe rabou tfiv e fee tfro m th e transition . Th e thermocoupl e tha t monitor s temperatur e i n th e SC C i s locate d o n tu p oft h e c h a m be ra bov e th e tr a n s ition , 2.3. 4 Hazardou s Wast e Residenc e Tim e \40 CF R § S3. J l207{f)(1)(ix) ] Th e Hazardou s wast e ga s residenc e tim e fo rth e Fixe d Heart h Incinerato ri s calculate d a s follows :

•PrimaryCombustio n Chambe rVolume-63 5 ff. 3

•Secondar yCombustio n C h a m b e rVol u m e - 63 5 ft 3

•Tota l Volume-127 0 fr. 3

•Maximu m Flu e Ga s Fiawrai e - 1 7,38 2 acf m (29 0 if/sec )

•Tota fCombustio n Zon e Residenc e Tim e = (127 0 ft 3 )/[29 0 Jf/sec ) = 4. 4 se c

2- 3 Hahmaryaul u

# AZCOM Since thes e incinerator s ar e fed heart h units , residenc e tim e i s base d o n th e elapse d tim e sinc e th e las : solid s charg e wa s pu t int o th e combustio n zon a o rbase d o n th e trave l lengt h o ftii s as h ra m that function s t o clea rth o primarycombustio n chambe ro fsoli d wast e residue , A n elapse d tim e o fon e hou ro ra trave l lengt h o f11 0 inche s fo rth e as h ra m hav e bee n establishe d a s th e criteri a fo rdeterminin g whe n soli d wast e i s n o longe ri n th e compustjo n zones , 1 2.3. 5 Combustio n Syste m Lea k Combustio n syste m leak s are prevente d throug h maintainin g a totallyseate d combustio n chamber , couple d wit h th e us e o fa n induce d draft fa n tha t maintain s a vacuu m ofnormall y- 4 t o •5 inche s o fwate rcolum n i n bot h combustio n chamber s whil e waste s ar e bein g fe d i o th e unit . 2.3. 6 Emergenc ySafet yVen t Th e incinerato ri s equippe d wit h a n emergenc ysafet yven t(ESV ) locate d a * th e to p o fth e secondar y combustio n chamber . Thi s ES Vi s a refractory-fine d emergenc ytherma l reife fven t(TRV ) whic h i s hel d i n th e dose d positio n b

ya pneumati ccylinder . Th e control.valv e i n th e lin e supplyin g ai rt o th e cylinde ran d th e cylinde rven tvalv e tha t open s th e TR Var e locate d i n th e contro l roo m fo reac h uni t Valv e lock s (wit h key s attached ) ar e utilize d to dete rindiscriminat e operatio n o fthes e valves . Openin g o fth e TR Vallow s ho t combustio n ga s to ven tfrom th e combustio n syste m durin g emergenc yshutdow n events . Th e purpos e o fth e TR Vi s t o protec tth e downstrea m APC S fro m excessiv e temperatur e situations , Alimi t switc h o n th e TK V shut s of fal l wast e feed s t o th e syste m a s i tsense s tha t .th e ca p i s opening . 

### 2. 4 Procedure s fo rRapidf yStoppin g Hazardou s Wast e Fee d Durin g Equipmen t Malfunction-£4 0 C^R§63,'l207<f)(1Kvi[i) } Equipmen tmalfunction s ar e identifie d byth e contro l syste m > observatio n o fproces s control variables , o rb y regula rfiei d inspections , i n th e even to fmino requipmen tmalfunction s (e.g
. Wast e fee d o rscrubbe Tleaks) , th e contro l roo m operato r wff fb e notified
. Th e contro l roo m operato rwil l the n clos e th e wast e fee d valve s an d disabl e th e wast e fee d pumps , I n th e even to fmajo requipmen tmalfunction s (e.g
. fire) , th e emergenc ysto p butto n locate d i n the . contr a I roo m wil l b e pushed . I fthi s butto n i s pushed , al l equipmen twil l switc h t o its fail-saf e position , 

### 2. 5 Ai rPollutio n Contro l Equipmen t [4 0 CF R §63.1207(f)( 1 >(lil)(G) ] 2.5. 1 Ai rPollutio n Contro l System s Description s Th e ai rpollutio n contro l syste m consist s o fa spra ydrye rabsorbe ran d fabri cfilte rbaghous e modules , Th e ai r pollutio n contro i syste m neutralize s acidi ccompound s an d remove s particulat e fro m th e exhaus tgas . Tw o subsystems , th e spra ydrye rabsorbe ran d th e fabri cfilter, carryou tth e chemica l neutralizatio n an d particulat e remova l functions , respectively . Athir d subsystem , th e lim e system , i s use d t o prepar e an d provid e lim e slurry t o th e spra yc'rye rabsorbe rfo rus e i n th e chemica l neutralizatio n process . Th e induce d draf t fa n an d stac k provid e th e mechanica l energ yrequire d t o transpor tth e flu e ga s throug h th e interconnectin g ductwork , to it s eventua l discharg e poin tbatmosph Ere .

2- 9 Ffhrta-ySCI Qjgki

2-5,1. 1 Lim e Syste m
• - Th e lim e syste m prepare s lim e slurryfo rus e i n th e chemica l neutralizatio n proces s i n sufficien tsuppl yan d

concentratio n t o maintai n continuou s flu e ga s treatmen ti n th e spra ydrye rabsorber . Th e syste m ha s bee n designe d fo rbatc h mixin g t o provid e thi s service , Veoli a utilize s hydrate d lim e a s it s neutralizin g agen ti n th e ai rpollutio n contro l systems . Th e ke yneutralizatio n paramete ro fth e hydrate d lim e i s th e "Ca O Equivalent. * Figur e 2- 1 i s th e specificatio n shee tfo rth e hydrate d lim e that Veoli a uses . Veoli a ha s use d thi s specifi c produc tfo rove r2 0 year s an d plan s to continu e wit h it s use , Althoug h ifVeoli a cfoe s chang e supplier s o rtyp e o flim e i n th e future , i twoul d hav e a :: Ca O Equivalent " specificatio n equa l t o o rgreate rtha n th e 72,6 % show n o n Figur e 2-1 . Hydrate d Jim e i s store d i n a storag e bi n abov e th e lim e preparatio n area . Th e storag e bi n i s size d t o hol d enoug h hydrate d lim e to maintai n severa l day s o fsyste m operatio n a tth e maximu m combustio n rat e o fth e incinerator . Lim e i s discharge d throug h th e conica l storag e bi n bottom . Th e flo wo fth e materia l fro m th e bi n i s aide d b ya vibratin g "liv e bottom, " o rbi n activator . Avariabl e spee d scre wfeede ri s use d to mete rth e hydrate d lim e i n th e proportion s require d fo rbatc h mixin g iim e slurry , Th e lim e i s mixe d wit h wate ri n a tan k beneat h th e lim e storag e bin . Th e scre wfeede rspee d an d 'th e rat e that wate ri s adde d to th e lim e slurrytan k ar e variabl e s o tha t th e desire d iim e solid s concentratio n ca n b e achieve d i n th e tank . Th e variabl e fee d adjustments - allo wwate ran d tim e t o b e adde d t o th e lim e slurrytan k a ta rat e tha t wil t allo wa batc h mod e o f' mixing . A n agitato ri s provide d i n th e slurrytan k to mi xth e wate ran d lim e an d to maintai n th e suspensio n of lim e solids . Th e mixe d lim e slurryi s pumpe d a ta continuou s rat e o fflo wthroug h a recirculatio n loo p E o th e atomizer . 2.5.1. 2 Sdfa yDryAbsorbe r
• : Uni t2 i s equippe d wit h a Spra yDrye rAbsorbe r(SDA ) locate d immediatel ydownsirea m o fth e secondar y

combustio n chamber . Th e SD Auni t i s fabricate d o f3/ B inc h carbo n steel , Th e functio n o fth e SD Ai s to : a Furthe rcoo l th e combustio n gase s from 1600- 2 000 ° F to 300-5C0"F , < •Neutraliz e an d remov e HC l an d othe racid s fro m th e combustio n gases , a Remcv e a pcrtio n o fth e particulat e (fl yash ) fra m thes e g ases , Slurr yflowto th e spra ydrye rabsorbe r(SDA ) i s metere d b ya flo wcontrol valv e to obtai n th e prope rfee d concentratio n to th e spra ydrye rabsorbe ratomizer . Automati c(o rmanual ) adjustmen tt o th e flo wi s mad e a s a functio n o fth e outpu t fro m a hydrochlori caci d (HCl ) analyze ri n th e ga s duc tdownstrea m o fth e fabri cfilter
. Th e amoun to fslurrymetere d i s proportiona l to th e amoun tofHC l monitored , Th e slurrypasse s throug h a stationaryswirl-typ e liqui d distributo rint o th e atomize rwhee l wher e induce d centrifuga l forc e fro m th e rapidfyspinnin g whee l discharge s th e slurrythroug h th e whee l nozzle s a thig h velocity . Th e desig n o fth e atomize rwheel , its rate o fspin , an d th e discharg e velocit yo fth e slurry , create s clou d o ffinel ydivide d droplet s aroun d th e peripher yo fth e atomize rwheel , Afeedbac k signa l fro m th e atomize rpowe rtransmitte rprovide s verificatio n tha t wate rflo wto the atomize rincrease s D rdecrease s ir t proportio n t o th e spra ydrye rabsorbe routle ttemperature . Flu e ga s enter s fro m th e botto m o fth e spra ydrye rabsorbe rthroug h a vertical , centrall ylocate d disperser , Th e disperse rdirect s th e flu e ga s throug h th e zon e fille d byth e atorrtze d slurryclou d wher e th e flu e gs s an d slurrymix- an d mos to fth e absorptio n occurs . Th e gase s the n flo wdownwar d throug h th e absorbe rchambe r
2-1 0 reSniai y2D1 5

# AzCOM
an d exi tthroug h a botto m sid e duc tA s th e gase s contac tan d pas s throug h th e clou d o fatomize d lim e slurry , th e wate ri n th e slurryevaporates , cooiin g th e gases . Simultaneously , th e lim e i n th e slurryreact s wit h th e hydroge n ch'orkf e i n tri e ga s u s to produc e calciu m salts . Som e o fth e resultin g drymaterial , consistin g o f calciu m salts , fl yas h an d exces s lime , fall s t o th e conica l botto m o fth e unit . Th e drymateria l fro m eac h uni t i s discharge d t o a conveyo rsyste m tha t transport s i t t o a dum p traile ro requivalen ttyp e system . 2.5.1. 3 Fabri cFilte r Ga s exhaustsr J fro m th e spra ydrye rabsorbe ri s distribute d b ymanifcl d duct s to fou rfabri cfilte rmodules , Th e uni t i s operate d wit h oni ythre e module s on-lin e wit h th e fourt h modul e off-lin e i n a standb ymode . Within eac h filte rmodule , th e ga s i s passe d throug h Teflon-coate d fiberglass clot h bags , Th e ga s passe s fro m th e outsid e t o th e insid e ofth e filte rbags . Particulat e entraine d i n th e ga s strea m i s mechanicall ydeposite d o n th e outsid e o fth e filte rbag s a s th e ga s passe s throug h th e cloth , Eac h modul e ha s a dea n ai rplenu m an d housin g sectio n t o contai n approximatel y9 6 bags . Eac h ba g i s approximatel y6 " i n diamete rb y20 ' long . Th e baghouse s ar e fabricate d fro m 3f16 * mil d stee l plate , o fwelde d construction , ga s tigh t an d stiffene d to withstan d th e maximu m operatin g negativ e pressure . Eac h compartmen tha s a tub e shee tthat support s th e bag s an d provide s fo rtop bag/cag e removal . Acces s to th e clea n ai rplenu m i s vi a a sid e acces s doo ri n th e clea n ai rplenum . Th e fabri cfilte rcleanin g mechanis m utilize s jet s o fai rto clea h th e filte rbags , Periodically , th e cleanin g sequenc e wil l b e initiated . Th e sequenc e i s starte d a tth e en d ofa 4 hou rtime d cycfe , whe n th e differentia l pressur e acros s th e filte rreache s a predetermine d setpoin to fapproximatel y7,0 " w.c , o rwhe n th e operato r initiate s a cycle . Th e controlle rthe n sequence s to eac h ro wo ffilte rbag s i n eac h module , releasin g a burs to f ai rapposit e txth e direcfjofro fga s flow, •Th e quickl yreleased 1 burs to fair-rirslodges-dus tcsk e o n th e exterio ro f eac h ba g a s ittravel s fro m th e to p t o th e botto m o fth e bags , Release d fro m th e bag , th e dus tcak e fall s b y gravit yint o th e hoppe ra tth e botto m o fth e module . Fro m ther e i ti s discharge d to a conveyo rsyste m tha t transport s i tt o a dum p trailer , o requivalen ttyp e system . Treate d b yth e spra ydrye rabsorbe ran d filtere d b yth e fabri cfilters , lii e cleane d flu e ga s exit s th e fabri cfilte r module s t o a n outle tmanifol d torexhaust . S.5.1. 4 Induce d Draf tFa n an d Stac k Th e induce d draft fa n an d stac k ar e locate d downstrea m o fth e fabri cfilter. Combustio n gase s ar e draw n throug h th e syste m b y. a 7 5 h p induce d draf t (ID ) fan , rate d at15,00 0 acf m a t 400 * F saturated , an d 22 " wate r colum n pressure . Th e induce d draft fa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s throug h th e spra ydrye rabsorber , fabri cfilter , an d al l interconnectin g ducts , Th e I D fa n include s a n inle t volum e contro l dampe rt o b e use d t o contro l th e velocit yo fth e ga s withi n th e ductin g an d treatmen tdevices . Treate d gase s ar e exhauste d from th e induce d draf t fa n to th e atmospher e throug h a 90-ft
. hig h stack , Th e stac k diamete rfo rUni t2 i s 3 9 inche s 3 , D , Th e stac k

i s equippe d wit h instrumen tsamplin g port s an d a samplin g platfor m fo remission s testing . Figur e 4- 1 provide s detail s o n th e desig n an d sampl e port location s an d configuration s fo rth e stack ,

2-1 1 Fahmar y20 1 •

### 2, 6 Stac k Emission s Monitorin g [40 CF R §63.1207(f)(1}<iii><H-) T Th e continuou s emission s monitorin g (CEM ) syste m consist s o fsampl e probes , sampl e deliver yan d conditionin g apparatus , an d ga s analyzers , Sample s ar e extracte d fro m th e samplin g port s o n th e stack , A CE M performanc e tes tan d qualit yassuranc e progra m ha s bee n imp'emsnte d i n accordanc e wit h Appendi x t o Subpar tEE E o fPar t63—Qualit yAssuranc e Procedure s fo rContinuou s Emission s Monitor s Used fa rHazardou s Wast e Combustors . Response s fro m eac h CEM S ar e fe d to th e Contro l Syste m (CS ) wher e th e C O hourl yrollin g averag e i s calculate d an d interlocke d to th e wast e fee d cutof fvalve s a s parto fth e Automati cWast e Fee d Cutof fSyste m (AWFCO ) discusse d i n Sectio n 2.8 , below , Th e followin g provide s a brie fdescriptio n o fth e CEM S instrument s includin g th e operatin g rang e an d measuremen l principal . 2.S. 1 CEM S Syste m Descriptio n Th e Continuou s Emission s Monitorin g Syste m (CEMS ) currentl ybein g utilize d a tIncinerato r2 analyze s far opacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , excep t opacity , ar e extractiv e device s mounte d i n samplin g port s D n th e stack . Th e tabl e belo wsummarize s ih e analyze rspecifications
. Th e opacit ymonito rcontinuousl ymeasure s th e stac k ga s opacit yan d report s th e measurement s to a n indicato ran d a recorder , A n opacit ytha t exceed s a prese tlimi t trigger s a n alar m an d interlock . Carbo n monoxid e an d hydroge n chlorid e ar e monitore d wit h extractiv e non-dispers e infrare d analyzers , Tota l hydrocarbon.i s monitored , wit h a n .extractiv e flam e ion.detector,analyzer. . .Oxygen.is.monitore d .wit h . a zirconiu m oxid e cell , Stac k ga s flowrat e i s continuousl ymonitore d usin g a n anuba rtha t send s a 4-2 0 m Asigna l to th e PL C tha t convert s th e signa l t o acfm
. Ta bl e 2- 1 U n it 2 C o nt i nu o u s Em i s s io n Mo n tt o r s Paramete r Curren t Mfg
. Rang e Principl e Oxyge n COS A 6-25 % Electrochemica l Carbo n Monoxid e Ecoche m MC 3 0-20 0 ppm v

. 0-30D Q ppm v Infrare d i Tota l hydrocarbon s Thermoeiectro n 0-10 0 ppm v FlD/lnfrare d Hydroge n chlorid e Ecoche m MG 3 0-1,00 0 ppm v Infrare d Opacit y Tefedyn e 0-100 % Whit e ligh t Stac k ga s flo w PSE/Rosemoun t 0-20,00 0 acf m Pressur e dro p 

### 21 Proces s Monitorin g an d Contro l Th e facilit yi s equippe d wit h a state-Df-the-artmonitorin g an d contro l system , whic h facilitate s complianc e wit h permi tconditions , an d otherwise , collect s proces s contro l information , facilitate s efficien toperatio n an d detect s an d prevent s damag e to th e facility , The.syste m consist s o fthre e majo rcomponents : 2-1 2» Ahuman-machin e interfac e (HMI ) system , * P r o g ra mm a bl e lo g i cco n tro t I er' s ( P LC's) , an d

* Ah i g h s pe e d etl i erne tca b I e co n nect s a 1 1 contr a I s yste m c cm p o n e n ts Th e desire d contro l function s ar e implemente d throug h th o HM ! system , Al i digita l contro l an d emergenc y interlock s ar e accomplishe d b yth e PLC , Th e contro l syste m i s capabl e o fmonitorin g th e 'operationa l envelope' 1 o fth e incinerato ran d i s capabl e o f performin g a-numbe ro factivitie s including :
» Contro ! roo m indicatio n o fprocesso rsensor s locate d withi n th e incinerato rsyste m (suc h a s pressure ' indicatio n o fa fiel d installe d pressur e transmitter) ; « Proces s controlle rfo rsingl e instrumen tloop s o ra n individua l sub-system , suc h a s a ternpenature contro l loo p involvin g a senso rreadin g fro m on e temperatur e transmitte raffectin g th e functio n o fon e temperatur e conEro i valve ; an d

* Alar m fo ra n exceedanc e o fa designate d setpoint , suc h a s a hig h pressur s o rlo wtemperature . Th e proces s contro l compute rwil l continuousl ycontro l an d monito rthe-operatio n o fth e incinerator . Whe n out of-rang e condition s exist , itwil l notifyth e operato ro fthos e conditions , Th e proces s contro l compute ri s programme d to shut-dow n equipmen t{i.e. , brin g th e syste m int o a saf e mode ) whe n designate d parameter s ar e exceeded , whic h i s a protectiv e mechanis m agains tpotentia l equipmen tdamage , operatio n outsid e o f permi tlimits , o rcondition s that migh tlea d t o a releas e t o th e environment . Continuou s monitorin g o fth e incinerato ran d scrubbe rsyste m i s a n importan taspec to fth e syste m design . A digita l readou to fal l monitorin g insfn j mentatio n i s displaye d o n th e mai n contro l screen . A n audibl e an d visua l alar m alert s th e incinerato roperato rS o significan tdeviation s from norma l operatin g conditions . Thi s syste m allow s a n immediat e respons e to advers e condition s b yth e operator , Automati cwast e fee d cut-of fan d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m ato rprio rto reachin g permi tlimi t levels . Monitorin g method s an d calibratio n frequencie s are . liste d i n Tabl e 2-3 , Th e Incinerato rha s a n independen tproces s contro l compute rthat interface s to th e Quantu m programmabl e controllers . Th e proces s compute ri s capabl e o fcontrollin g th e incinerato ri n cas e o i a failur e i n a HM J server . Thi s compute rrun s a RSVIE WHM I contro E softwar e tha t provide s operato rinterfac e to al l instrumentatio n an d controls . 

### 2, 8 Automati c Wast e Fee d Cut-of fSyste m [40 CF R §63.1207(f)(1)(iJi)(F) ] Th e Incinerato rha s a n Automati cWast e Fee d Cut-Of f(AWFCO ) Syste m tha t wil l shu twast e feed s offi n th e even tcertai n operatin g parameter s deviat e fro m allowabl e se tpoints . Th e PL C continuousl ymonitor s operatin g parameters , makin g adjustment s to th e proces s a s neede d fo rprope rcontrol , Alar m logi ci s incorporate d int o th e PL C syste m to automaticall yinitiat e a n AWFCO
. Tabl e 2- 3 summarize s th e curren t AWFC O se tpoints . AWFC O limit s hav e bee n establishe d base d o n severa l factor s tha t ar e summarize d below ,

* Regulatory/permi tlimit s - establishe d to compl ywit h existin g permits . A n exampl e o fthi s typ e oflimi t i s th e lo wtemperatur e limit , belo wwhic h wast e canno tb e fe d unti l th e prope rlimi t i s re-established . 2-1 3 Fabrasyail C

# AsCO M

s$piy I n addition , th e HW C MAC Tregulation s requir e tha tth e AWFC O syste m b e interlocke d wit h th e spa n f'-^J? o fea ch p roces s instru m e n tt h ati s p a r to fth e C o n t i n uou s M o n i j o rin g S yste m .(C M $} , A I i sti n g o fthes e ^ CM S instrument s an d thei rinterlocke d spa n setpoint s i s maintaine d a s par to fVeolia' s Operatin g Record , « Proces s safetylimit s - establishe d t o assur e proces s equipmen ti s protecte d an d unsaf e operatin g condition s d o notoccur . A n exampl e ofthi s i s inadequat e exces s ai ri n th e combustio n chambe rtha t ca n lea d t o fue l ric h conditions . * Utilit yo rFewe rfailur e - establishe d to facilitat e a controlle d shutdow n o fth e proces s durin g los s o f proces s air , steam , wate ro relectricity , A n exampl e o fthi s i s th e los s o finstrumen tai rtha ti s necessar yfo rcertai n type s o fproces s instrument s f o functio n properly . Waste s wil l no tb e re i n troduce d into th e incinerator s unti l prope roperatio n o fke yinstrument s i s re-established . I n additio n t o th e AWFC O system , operator s ca n manuall yshutdow n wast e reed s o rth e entir e proces s shoul d thi s b e needed , 2 .3. 1 AWFC O Syste m Testin g Veoli a test s th e AWFC O system s bi-weekly , a s weekl ytestin g woul d undul yinterfer e wit h operation s b y ceasin g an d restartin g wast e feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s durin g th e downtime , an d increasin g operatin g costs , Testin g o fth e AWFC O syste m i s a time-consumin g an d manpowe rintensiv e process . Th e curren ttestin g progra m ha s bee n i n plac e unde rth e • RCR Apermi tfo rove r2 0 year s an d ha s prove n to b e adequat e i n detectin g problems , Thi s rational e i s ^ % include d i n th e facility' s AWFC O Plan . I n som e case s thi s testin g occur s mor e frequentl ydependin g o n ha w [-y'^W often actual ' AWFCO' s bec' u rat ' th ' e ' Liti'It ' Per't h e req uiretfffe q uericy ; 'incinerato rperso n i i el ' cl i e'c'K' th e '• . ••• ' f u notio n a I ityo fAWFC O lo g i ct h a ti s par to fth e i nc i nerat o r"

&P L C syste m to mak e s u r e tha ts h c-ui d proces s condition s deviat e fro m allowabl e limits , th e compute rlogi cwil l initiat e wast e fee d shutdown s a s required . Thi s i s accomplishe d b ymanuall ysimulatin g proces s condition s tha tar e outsid e allowabl e limit s an d obseivin g an d documentin g whe n th e contro l o rbloc k vafv e softwar e logi co n th e wast e fee d lin e begin s to initiat e valv e closure . Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e ar e documente d b yoperatin g personne l t o safet yregulatoryrequirement s fo rsyste m testing . Result s ofthi s testin g ar e documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par to fth e unit' s Operatin g Record . 

### 2. 9 Ai rPollutio n Contro i Equipmen t Maintenanc e Practice s [4 0 CF R §63.1207Cf}(lHin>{G) ] 2.9. 1 Progra m Overvie w Onc e equipmen ti s installe d an d operational , Veoli a utilize s a n e>ctenstv e preventativ e maintenanc e (PM ) progra m t o kee p equipmen toperationa l an d preven tbreakdown s an d failures
. Base d upo n th e typ e o f equipmen ta ne

thistorica l operation s an d maintenanc e experience , schedule s fo rvariou s inspectio n an d P M activitie s ar e followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenanc e historie s o n equipment , routin e inspectio n an d lubricatio n program s fo rhig h wea requipmen tan d nan-destructiv e testin g o f pipin g an d vessel s usin g technique s like ultrasoun d t o asses s integrity . Th e frequenc yc fthes e activitie s varie s dependin g upo n th e equipmen tP M activit yan d th e incinerator' s shutdow n schedule , ^ J | p | Fo rexample , frequen t(i.e. , weekly ) instrumen tan d certai n mechanica l equipmen tcheck s ar e mad e fo rcritica i |'..' ' '': , proces s items , Lubrication , vibratio n analysi s an d othe rmechanica l integritycheck s ar e don e atlonge r 2-1 4 Felmiary.ZGI Ofrequencie s like monthl yo rquarterly . Finally , suc h item s a s inspectin g refractorybric k fo rwear , ar e typicall y performe d whe n th e entir e incinerato ri s shu tdow n fo rmsintenancE. 1 . 2,9, 2 Tes t Progra m Preparatio n Activitie s Prio rto testing , instrumentatio n associate d wit h ke yparameter s o fth e tes twer e checked , calibrated , o r replaced , a s appropriate , to ensur e prope roperatio n o fth e instrumentatio n durin g testin g (i.e. , wast e fee d flowmeters an d scales , CEMS , pressur e transmitters , thermocouples , stac k flowmeters , etc.)
.

••• vj
2-1 5 rstm^n ' 2CI D'?ffi.#>

. 

# AZCOM Tabl e 2- 2 Technica l fnformatio n S unwar yo n Incinerato rNo . 2 j Pvianuracture r Trad e Wast e Incineratio n

•Mode l No , . TWI-20C0, Serie s 2 Typ e Fixe d Hearth , Dua l Chambe r Dat e o fManufactur e 193 7 Dimension s Primar yChambe r Secondar yChambe r Externa l Lengt h 17.5 r 17.5 ' Externa l Diamete r 9 ' 9 '

1 interna l Diamete r 7*2 - TT Cross-sectiona l are a 40, 3 squar e fee t 40. 3 squar e fee t Burner s Primar yChambe rBurne r Secondar yChambe rBurne r Manufacture r Nort h America n Nort h America n Siz e 12. 0 Millio n Btu/h r 6. 0 Millio n Bfu/hr Fue l Natura l Ga s • Natura l Ga s Prime rMove r nduce d Draf tFa n 15,00 0 acf m @ 4C0 3 F saturated . 2 2 in . wate rcolum n

2-1 6 Fabruar ySC-1 0Tabl e 2- 3 Curren tAWFC O Parameter s an d Limit s fo rIncinerato rMo , 2. \ . '

Syste m Devic e Unit s Cutof fLimit s Calibratio n Frequenc y Tota l Pumpabl e Wast e Fee d rat e Mas s Flowmetere/Scale s Lb/h r • > 3f07(HRA ) Annuall y Tota l Wast e Feedrat e Mas s Flowmeters/Scaie s Lb/h r >40T 7 • Annually/quarterl y Hig h BT U Liqui d feedrate Mas s flowmete r lb/h r i>2 : 012 2 Annuall y •Lo wBT U Liqui d feedrat e •Mas s flowmete r lb/h r a 1,993 s Annuall y Specialt yfeede r Scal e lb/h r £724 2 Quarterl y Tota l LV M Feedrat e Mas s Flowmeters/Scaie s lb/h r >47(1 2 HRA f Annually/quarterl y

i Pumpabl e LV M Feedrat e Mas s Flowmeters/Scaie s lb/h r >43(-12HRA ) Annually/quarterl y

: SV M Feedrat e ' Mas s Flowmeters/Scaie s lb/h r > 6 3 {1 2 HRA ) Annually/quarterl y Mercur yFeedrat e Mas s Flowmeters/Scaie s lb/h r > 0.D03 4 (12HRA ) Annuatly/qtiarterfy Chiorin e Feedrat e Mas s Fsowmeters/Scale s lb/h r > 21 S (1 2 HRA ) Annually/quarterl y As h Feedrat e Mas s Fl&wmeters/Scale s lb/h r >67 3 (1 2 HRA ) Annually/quarterl y Primar yCombustio n Chambe rT e m perat u r

e Typ e KThermocoupl e ' F <1,59 0 {one-minut e average )
« 173 4 (HRA'' ) >2.40 0 (instantaneous) 2 Annuall y
Secondar yCombustio n Chambe rTemperatur e Typ e KThermocoupl e e F S1.7S 4 (one-minut e average ) <1S4 9 (HRA 1 )

.. . .S2,4D. Q .{instantaneous) 2 ... . Annuall y
PrimaryCombustio n Chambe rpressur e Pressur e transmitte r in . w.c . >-0. 1 { 5 secon d defey) Quarterl y• Secondar yCombustio n Chambe rpressur e Pressur e transmitte r in . w.c . ^ -0. 1 ( 5 secon d detay) Quarterl y Spra yDrye rAdsorbe r Outle tTemperatur e Typ e KThermocoupl e ' F >5DD (on e minut e average) 2 >42Q (HRA ) Annuall y ; Combustio n Ga s Flo wRat e Pito tTub e acf m >17,198 ? *15,14 7 (HRA ) Annuall y Stac KGa s Exces s Oxyge n Zirconiu m Oxid e fue l cel l % <. 3 (one-minut e avg. ) Quarteri y Stac k carbo n monoxid e Infrare d ppm v \ £10 0 ( H k

A) k5QQ (on e minut e average) 2 Quartert y Stac k Hydrocarbo n FI D j ppm v >1o'{on e minut e average ) Quartan " y Stac k ga s opacit y Whit e Ligh t % >1 0 (on e minut e average) 2\ Quarterl y Stac k hydroge n chloride 2 Infrare d ppm v >1D0(HRA) 3 £50 0 (on e minut e average) 2 Quarterl y : Fabri cfilte rpressur e dro p Delt a P transmitte r in . w.c . • 3 2 cr > 1 0 ( Tmin . average ) Quarterl y Min . Sorben tFeedrat e DensityTransduce r Ib/fb Cl 2 <1.7 6 Min . Carrie rFlui d Flowrat e Flowmete r gat/l b Cl 2 <1.70 " Annuall y 1 HR Amean s "hourl yrollin g average " a s calculate d b yaveragin g th e previou s 6 0 one-minut e averag e vafueg,
. 2 Thi s I s a RCR Apermi tlimi t only .

2-1 7

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2 -1 8

# IncineratorProces s Description Uni t3

# 2. 0 Incinerato rProces s Descriptio n 

# AZCOM

2. 1 Proces s Overvie w .Veoli a operate s tw

o Fixe d Heart h Dua l Chambere d Incinerator s (Unit s 2 an d 3 ) an d on e rotarykil n incinerato r (Uni t4 ) a tth e Sauget , I Lfacility , Th e tw o fixe d heart h unit s ar e rate d a t 1 6 millio n Btu/h reach . Incineratio n Uni tNo , 3 i s a mirro rimag e o fUni tNo , 2. Bot h o fthes e units hav e thei row n wast e handlin g system s a s describe d i n th e section s tha t follow
. Th e onl ydifferenc e bein g Uni tNo , 2 is equippe d wit h fou r(4 ) baghous e modules , whil e Uni tNo . 3 i s equippe d wit h thre e (3 ) ba g h e us e modules . However , eac h incinerator , i s operate d identicall ywit h onJ ythre e baghous e module s i n servic e durin g operation . Uni t4 i s rate d a t 5 0 mirlio n Btu/h ran d i s equippe d wit h it s ow n tan k far m system , dru m storage , bul k solid s storag e an d feed systems , 

### 2.2 Wast e Fee d System s [4 0 CF R § 63.1207(f)( 1 }{ir)(c ) an d (f)(1)(iiiJ(D ) an d (E} ] . 2,2, 1 Una

t 3 Liqui d Wast e Fee d Syste m an d Blendin g Operation s Th e fixe d heart h incinerato ri s designe d t o receiv e containers , aqueou s liqui d wastes , organi cliqui d wastes , specialt yliqui d feed s an d direc tinjectliquid s fe d throug h th e aqueou s o rorgani cliqui d fee d systems . Thes e unit s ca n receiv e an ycombinatio n o fwaste s - liquid , semi-soii d o rsoii d - wit h a heatvalue'o fu p t o 15 millio n Btu/hr , Uni t3 is.supporte d b ystorage/blen d tank s locate d i n Tan k Far m #1 . Rate s o ffee d ar e controlle d at eac h incinerator . Segregate d liqui d waste s ar e store d unti l utilize d i n th e wast e blendin g facilities
. A ttha t time , •liquids-ar e delivere d t o -th e -blending--tanks where - the - dail y-Pqui d fee d .to . the . incinerato r.is . formulated , .teste d an d release d t o th e incinerator . Blendin g o fstore d liqui d waste s t o achiev e optimu m heatin g valu e an d viscosit yfo rincineratio n take s plac e i n Tank s 2 , 4 , 6 S , 8 . Si xadditiona l tank s (10 , 20 . 30 , 40 , 5 0 & 60 ) ar e use d t o segregat e differen twast e strea m type s fo rblendin g o fliqui d fee d to th e incinerator ; Severa l criteri a ar e importan ti n designin g a bten d fro m availabl e waste s that hav e bee n segregate d principaEl yby-physica l an d chemica l properties , Thes e includ e compafibi|ity ; 

### .prope rrang e o fheatin g value , an d permi trestriction s regardin g elementa l compositio n (base d o n emissio n limitations)
. Th e materia l i s transferre d throug h abovegroun d pipeline s mo m th e tan k far m t o th e incinerator . Pipeline s use d t o transfe rliqui d organi cwast e an d aqueou s wast e ar e equippe d wit h strainers . i n complianc e wit h th e Benzen e NESHAP , al l tank s ar e vente d t o individua l carbo n adsorptio n canister s fo r remova l o forganic s befor e vapo ri s discharge d t o th e atmosphere . Eac h carbo n adsorbe rcaniste ri s essentiall yequivalen tt o a 5 5 gallo n containe ro rgreater , i fnecessary . Al l tank s ar e equippe d wit h conservatio n vents , i n additio n t o th e carbo n caniste radsorber, - Al l tank s ar e grounded , an d il.am e arrester s ar e installe d betwee n th e carbo n adsorber s an d th e tanks , 2.2.1. 1 Organi c an d Aq : u eou s Li q ui d Wast e Feed s Th e liqui d wast e injector s use d i n th e combustio n chamber s ar e air-atomizin g injectors , Thes e ar e use d fo r injectio n ofhig h Btu , lo wBt u liquid s an d specialt yfee d liquids , Dua l f- ; 

### ui d injectio n nozzle s wil l b e use d fo r atomrzatio n o fth e waste . Eac h o fth e injector s i s rated a t 0-30 0 gph . Th e liqui d wast e fee d nozzle s ar e serve d b yps

ra l I e I re d u n d a n t p u mp s a n d re d rc u lati o n syste m s wit h b a c k pres s u r e co n trol .



### 2 - 6 Fabrusr yK)l£ l2.2.1. 2 Package d Wast e Fee d

'•'Container s o fwaste s ar e sample d an d analyze d afte rreceip ti n accordant © wit h th e facility' s Wast e Analysi s Plan . Thes e waste s ca n the n b e delivere d directl yto Uni t3 o rrepacke d int o smal l combustibl e container s a t th e facility
. Fiberboar d o rplasti ccontainer s (full yo rpartiall yful l o fwaste) , u p t o 40-ga'llo n size , ma yb e charge d directl yto th e piimar ychamber , Thes e wil l b e receive d a t th e doc k adjoinin g eac h fixe d heart h incinerator , an d charge d to th e incinerato rwithi n 2 4 hour s o rreturne d t o permitte d storage , SoficJs , usuall ypackage d i n plasti co rfiberboar d containers , ar e introduce d ini o th e incinerato rthroug h a PL C controlle d airlock-ra m syste m locate d a t th e lowe rfron t o fth e primarychambe rofth e incinerstor . Th e airioc k i s compose d o fa refractory-line d door , a doo rint o th e airloc k enclosure , an d tw o pneumati crams . Th e actio n o fth e feede ri s a s follows:

* Wit h th e incinerato rdoo rclosed , tri e airloc k doo ri s opened , * •Th e firs t pneumati cra m (loa d ram ) pushe s weighe d charge s o fwast e int o th e airloc k chamber . * Th e airloc k

doe ri s closed , * Aswitc h i s activate d eithe rautomaticall yo r.manually , whic h open s th e doo rto th e incinerato ran d actuate s th e ra m (charg e ram ) that pushe s th e wast e int o th e incinerator , Th e ra m the n retract s an d th e incinerato rdoo rcloses , 2.2.1. 3 Specialt yLiqui d Wast e Feed s Specialt yFee d System s associate d wit h Incinerato rHo. 3 ar e a s follows

•\ ' Hoode d Specialt yContaine rFeede r

* Glov e Bo xEmissio n Contro l System s
* Direc tinjectLiqui d Fee d Syste m 

### 2. 3 Manufacturer , Mak e an d Mode l o fth e Incinerato r[4 0 CF R § 63.1207(f)(1){m}{A) I 2,3. 1 Combustio n Chambe ran d Burner s [4 0 CF R §63.1207(f)(1)(iii)(B ] an d (C ) Incinerato rNo . 3 feature s a two-stag e combustio n process . Ignitio n o fwast e materia ! ta'se s plac e i n th e primary(lower ) combustio n chambe r(PCC)
. Asecondar y(upper ) combustio n chambe r(SCC ) serve s a s a n "after-burner " fo rproces s gases, ' Ignitio n o fth e wast e take s plac e a t temperature s i n exces s o f170 0 degreesF . Th e secondar yco m b u stio n ch a m b e rm a i n t a i n s a m i n i m u m :erryp e rat u r e ofapprox i matel y1B0 0 degree s F , Th e fixe d heart h incinerato ri s fabricate d o fcarbo n steel . Th e primarychambe rha s a n externa l diamete ro f9 fee tan d i s 17, 5 fee tlong . Th e interio rw'atl s o fth e chambe rar e line d wit h approximatel y1 0 inche s o fbric k refractoryan d insulatio n backing > makin g th e interna l operatin g diamete rapproximatel y7'2-* . Th e cross sectiona l are a o fth e chambe ri s thu s 40, 3 squar e fee tTabl e 2-2 provide s a summar yo fth e incinerato r desig n specifications
. Liqui d an d soli d wast e feed s ente rth e lowe rchambe ra n th e front-fac e ofth e chamber . Th e primaryburne r an d th e s pe ci a It

yfee d i njecto ra r

e locate d nea rth e front-fac e o fth e o h a m be ra n d ar e mo u n te d ta n gent i a liy .

• •'1
2- 7 FetjrLrars ' 30' R

# AZCOM Th e primaryburne ri s a Nort h America n burne rrate d a * 12. 0 millio n Btu/hr
. an d i s use d f n th e lowe rchambe r

- to maintai n permitte d temperatures , i t wil l bur n onl ynatura l ga s c rNo , 2 fue l oil . Th e burne rsyste m i s supplie d wit h combustion-ai rat a stati cpressur e o f30 " wate rcolum n (WC) , The . pilo t fo rth e primaryburne rwil l bur n natura l gas , Th e fue l syste m fo rth e lowe rchambe r(an d secondar ycombustio n chamber ) i s controlle d b ya Factor yMutua l a p prove d b u rhe rm ana g e m en ts yst e m ccm p let s wit h i n ter l ock s a n d s a Fet yva!ves . 2.3. 2 Secondar yCombustio n Chambe r Th e secondar ycombustio n chambe r(SCC ) i s a horizontal , cylindrica l chambe rthat ha s a n externa l diamete ro f9

- fee tan d i s 17, 5 fee tlong . Th e interio rwall s o fth e chambe rar e line d wit h approximatel y1 0 inche s o fbric k

refractor yan d insulatio n backing , makin g th e interna l operatin g diamete rapproximatel y 7 : 2" . Th e cross-sectiona ! are a ofth e chambe ri s thu s 40. 3 squar e feet
. Foli cwin g ignitio n o fth e wast e materia l unde rcontrolle d o rstarved-ai rcondition s i n th e lowe rchamber , off gase s trave l throug h a refractory-line d flu e ga s passag e int o th e uppe rchamber , whic h act s a s a n afterburner
. Turbulenc e i s achieve d b yth e tangentia l Introductio n o fai ran d additiona l fue l i n th e uppe rchamber . Th e SC C i s equippe d wit h on e burne rmounte d tangentiall yo n th e sid e o fth e chamber . Th e burne ri s a Nort h America n burne rrate d a t5. 0 millio n Btu/h ran d i s fuele d wit h natura l ga s o rfue l oil , A s wit h th e prirnan ychambe rburner , th e SC C burne ri s supplie d wit h atomizin g ai ran d i s equippe d wit h a burne rmanagemen tsystem . Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof fwhe n ther e i s a-los s o fflarr^,-combustio n -air - supply, - -fue l -pressure- , -atomizing-ai r-pressure, - or - pilo tburner- , Leavin g th e uppe rchamber , th e hotga s strea m travel s throug h 2 8 fee to frefractory-line d stac k section s befor e reachin g th e star to fth e ga s scrubbin g system , Tn e combine d volum e o fth e uppe ran d lowe rchambers , th e flu e ga s passag e an d th e ho t crossove rsectio n i s approximatel y1,58 7 cubi cfeet
. Th e tota l retentio n tim e o f combustio n gase s withi n th e syste m i s approximatel y5 seconds . 2.3. 3 Locatio n o fCombustio n Zon e Temperatur e Devic e [4 0 CFR§S3.l207(f](1)(xix) J Th e thermocoupl e tha t monitor s temperatur e i n th e primarycombustio n chambe ri s locate d o n to p o fth e chambe ra bou t fiv e fee t fro m th e transition , Th e thermocoupl e tha t monitor s temperatur e i n th e SC C i s locate d o n top o fth e chambe rabov e th e transition , 2.3. 4 Hazardou s Wast e Residenc e Tim e [4 0 CF R §63.l207(f)(1)(ix) ] Th e Hazardou s wast e ga s residenc e tim e fo rth e Fixe d Heart h Incinerato ri s calculate d a s follows :

•P ri mar yCo m bustio n C h a m be rV o l u m e - 6 3 5 ff. 3 » Sec o n dar yCom b ustio n C hambe rV o l u m e - 63 5 ft 3
•Tota l Volume - 127 0 ft3
•Maximu m Flu e Ga s Flowrat e - 17,38 2 acf m (29 0 if/sec ) » Tota l Combustio n Zon e Residenc e Tim e - (127 0 ft 3 )/(29 Q ftVsec ) = 4. 4 se c

2- 8 Fsf3fHSr>'201 0

# AZCOM Sine s thes e incinerator s ar e fixed heart h unit s residenc e tim e i s bass d or-, th e eiapse d tim e sinc e th e las t so l id s charg e wa s pu t into th e combustio n zon e o rbase d o n th e trave l lengt h o fth e as h ra m tha t junction s to clea rih e primarycombustio n chambe ro fsoli d waste , residue . A n elapse d tim e o fon e hou ro ra trave l lengt h o f11 0 inche s fo rth e as h ra m hav e bee n establishe d a s th e criteri a fo rdeterminin g whe n soli d wast e i s no ionge ri n th e combustio n zones . 2.3. 5 Combustio n Syste m Lea k Combustio n syste m teak s ar e prevente d throug h maintainin g a totall yseale d combustio n chamber , couple d wit h th e us e o fa n induce d draft fa n tha t maintain s a vacuu m ofnormall y- 4 t o - 6 inche s o fwate rcolum n i n bot h combustio n chamber s whil e waste s ar e bein g fe d to th e unit . 2.3. 6 Emergenc ySafet yVen t Th e incinerato ri s equippe d wit h a n emergenc ysafet yven t(ESV ) locate d a tth e to p o fth e secondar y combustio n chamber . Thi s ES Vi s a refractory-line d emergenc ytherma l relie fven t(TRV ) whic h i s hel d i n th e dose d positio n b ya pneumati ccylinder . Th e contro l vaiv e i n th e lin e supplyin g ai rto th e cylinde ran d th e cylinde rven tvalv e that open s th e TR Var e locate d i n th e contro l roo m fo reac h uni t Valv e lock s (wit h key s attached ) ar e utilize d t o dete rindiscriminat e operatio n o fthes e valves . Openin g o fth e TR Vallow s hot combustio n ga s to

ven tfro m th e combustio n syste m durin g emergenc yshutdow n events . Th e purpos e o fth e TR Vi s t o protec tth e downstrea m APC S fro m excessiv e temperatur e situations . ASim i tswitc h o n th e TR V shut s of fal i wast e feed s to th e syste m a s itsense s tha t th e ca p i s opening . 

### 2. 4 Procedure s fo rRapidl yStoppin g Hazardou s Wast e Fee d Durin g Equipmen t Maffunctio n [40 CF R §63.12QT{f)(1)<viiif l Equipmen tmalfunction s ar e identifie d b yth e contro l system , observatio n o fproces s contro l variables , o rby regula rfiel d inspections . I n th e even to fmino requipmen tmalfunction s (e.g
. wast e fee d o rscrubbe rleaks) , th e contro l roo m operato r wil l b e notified
. Th e contro l roo m operato rwil l the n clos e th e wast e fee d valve s an d disabl e th e wast e fee d pumps . I n th e even to fmajo requipmen tmalfunction s (e.g
. fire) , th e emergenc ysto p butto n locate d i n th e contno ! roo m wil l b e pushe d I fthi s butto n i s pushed , al l equipmen twil l switc h t o ;ts fail-saf e position . 

### 2.5 Ai rPollutio n Contro l Equipmen t [4 0 CFR§63,12Q7(f){1)(iii)(G) ] 2.5. 1 Ai rPollutio n Contro l System s Description s Th e ai rpollutio n contro l syste m consist s o fa spra ydrye rabsorbe ran d fabri cfilte rbaghouse , Th e ai rpollutio n contro i syste m neutralize s acidi ccompound s an d remove s particulat e fro m th e exhaus tgas . Tw o subsystems , th e spra ydrye rabsorbe ran d th e fabri cfilter , carryou tth e chemica l neutralizatio n an d particulat e remova l functions , respectively . Athir d subsystem , th e lim e system , : s use d t o prepar e an d provid e lim e slurry t o th e spra ydrye rabsorbe rfo rus e i n th e chemica l neutralizatio n process . Th e induce d draf t fe n an d stac k provid e th e mechanica l energ yrequire d t o tran s port th e flu e ga s throug h th e interconnectin g ductwork , t o it s eventua l d isc h arg e p o int t o atmo s phere .

2- 9 ,-ehmar y0

# AZCOM 2.5,1. 1 Lim e Sy&tc m Th e lim e syste m prepare s lim e slurr yfo rus e i n th e chemica l neutralisatio n proces s i n sufficien tsuppl yan d concentratio n to maintai n continuou s flu e ga s treatmen ti n :h e spra ydrye rabsorber . Th e syste m ha s bee n designe d fo rbatc h mixin g t o provid e thi s service . Veoli a utilize s hydrate d iim e a s it s neutralizin g agen ti n th e ai rpollutio n contro l systems . Th e ke yneutralizatio n paramete ro fth e hydrate d lim e i s th e "Ca O Equivalent; . Figure 2- 1 i s th e specificatio n shee tfo rth e hydrate d lim e that Veoli a uses . Veoli a ha s use d thi s specifi c produc tfo rove r2 0 year s an d plan s to continu e wit h it s use . Although , i fVeoli a doe s chang e supplier s o rtyp e o fiim e i n th e future , i twoul d hav e a "Ca O Equivalent " specificatio n equa l to o rgreate rtha n th e 72.6 % show n o n Figure 2-1 . Hydrate d lim e i s stored ' i n a storag e bi n abov e th e lim e preparatio n area . Th e storag e bi n i s size d t o hol d enoug h hydrate d lim e to maintai n severa l day s o fsyste m operatio n a tth e maximu m combustio n rat e o fth e incinerator . Lim e i s discharge d throug h th e conica l storag e bi n bottom . Th e flo wo fth e materia l fro m th e bi n i s aide d b ya vibratin g "liv e bottom, " o rbi n activator , Avariabl e spee d scre wfeede ri s use d to mete rth e hydrate d lim e i n th e proportion s required fo rbatc h mixin g lim e slurry , Th e lim e i s mixe d wit h wate ri n a tan k beneat h th e lim e storag e bin . Th e scre wfeede rspee d an d th e rat e tha t wate ri s adde d to th e lim e slurrytan k • ar e variabl e s o tha t th e desire d lim e solid s concentratio n ca n b e achieve d i n th e tank . Th e variabl e fee d adjustment s allo wwate ran d lim e to b e adde d t o th e iim e slurrytan k a ta rat e that wil l allo wa batc h mod e o f rriExing . A n agitato ri s provide d i n th e slurrytan k to mi xth e wate ran d lim e an d to maintai n th e suspensio n o f lim e solids , Th e mixe d lim e slurr yi s pumpe d a ta continuou s rat e o fflowthrougl i a recirculatio n loo p t o th e atomize rats. rate o fu p t o 1 0 gpm . 2.5.1. 2 Spra yDr

yAbsorbe r Uni t3 i s equippe d wit h a Spra yDrye rAbsorbe r(SDA ) locate d immediatel ydownstrea m ofth e secondar y combustio n chamber . Th e SD Auni t i s fabricate d o f3/8 inc h carbo n stee LTh e functio n ofth e SD Ai s to :
» Furthe rcoo l th e combustio n gase s fro m 1600-2000 Ti o 300-5-a(} D F , •Neutraliz e an d remov e HC l an d othe racid s fro m th e combustio n gases , » Remov e a portio n o fth e particulat e (fl yash ) fro m thes e gases . Slurr yflo wt o th e spra ydrye rabsorbe r(SDA ) i s metere d b ya flo wcontro l valv e t o obtai n th e prope rfee d concentratio n to th e spra ydrye rabsorbe ratomizer . Automati c(o rmanual ) adjustmen tt o th e flo wi s mad e a s a functio n o fth e outpu t fro m a hydrochlori caci d (HCl ) analyze ri n th e ga s duc ttJownstrea m o fth e fabri cfilter , Th e amoun to fslurr

ymetere d i s proportiona l t o th e amoun to fHC l monitored . Th e slurr

ypasse s throug h a stationary'swirl-type.liqui d distributo rInto th e atomize rwhee l wher e induced ' centrifuga l forc e fro m th e rapidl yspinnin g whee l discharge s th e slurrythroug h th e whee l nozzle s a thig h velocity . Th e desig n o fth e atomize rwheel , it s rat e o fspin , an d th e discharg e velocit yo fth e slurry , creat e a clou d o ffinel ydivide d droplet s aroun d th e peripher yo fth e atomize rwheel . Afeedbac k signa l fro m th e atomize rpowe rtransmitte rprovide s verificatio n tha t wate rflo wto ih e atomize rincrease s o rdecrease s i n proportio n i o th e spra ydrye rabsorbe routle ttemperature . Flu e ga s enter s fro m th e botto m ofth e spra ydrye rabsorhe rthroug h a vertical , centrall yiocats d disperser . Th e disperse rdirect s th e flu e ga s throug h th e zon e fille d b yth e atomize d slurryclou d wher e th e flu e ga s an d slurrymi xan d mos to fth e absorptio n occurs , Th e gase s the n flo wdownwar d throug h th e absorbe rchambe r'
2-1 0

# AZCOM an d exi tt

t vouc h a botto m sid e duc tA s th e gase s contac tan d pas' s throug h th e clou d o fatomize d lim e slurry ,

. th e wate ri n th e slurryevaporates , coolin g th e gases . Simultaneously , th e lim e i n th e slurr yreact s wit h th e " ' hydroge n chlorid e j n th e gase s to produc e calciu m salts . Sem e o fth e resultin g drymaterial , consistin g o f calciu m salts , fl yas h an d exces s lime , fall s t o th e conica l botto m o fth e unit , Th e dr ymateria l fro m eac h uni t i s discharge d to a conveyo rsyste m tha t transport s i t to a dum p traile ro requivalen ttyp e system , 2.5.1. 3 Fabri c FNte r Ga s exhauste d fro m th e spra ydrye rabsorbe ri s distribute d by ' manifol d duct s t o thre e fabri cfilte rmodules , Withi n eac h filte rmoduie , th e ga s i s passe d throug h Teflon-coate d fiberglas s clot h bags . Th e ga s passe s fro m th e outsid e to th e insid e o fth e filte rbags . Particulate , entraine d i n th e ga s stream , i s mechanicall ydeposite d o n th e outsid e o fth e filte rbag s a s th e ga s passe s throug h th e cloth . Eac h modul e ha s a clea n ai rplenu m an d housin g sectio n t o contai n approximatel y9 5 bags . Eac h ba g i s approximatel y6 : i i n diamete rb y20 ' long . Th e baghouse s ar e fabricate d fro m 3/16 " mil d stee l plate , o fwelde d construction , ga s tigh t an d stiffene d to withstan d th e maximu m operatin g negativ e pressure , Eac h compartmen tha s a tub e shee ttha t support s th e bag s an d provide s fo rbo p bag/cag e removal . Acces s to th e clea n ai rplenu m i s vi a a sid e acces s doo ri n th e dea n ai rpienum , th e fabri cfilte rcleanin g mechanis m usi fees jet s o fai rt o clea n th e filte rbags , Periodically , th e cleanin g sequenc e wil l b e initiated . Th e sequenc e i s eithe rstarte d a tth e en d o fa time d cycle , o rwhe n th e differentia l pressur e acros s th e filte rreache s a predetermine d setpoin to fapproximatel y7.0 " w.c.. . o rwhe n th e operato r initiate s a cycle . Th e co n traile rthe n sequence s to eac h ro wo ffilterbag s i n eac h module , releasin g a burs tc f

... . .. . ' ai ropposit e t o th e directio n D fga s flow
. Th e quickl yrelease d burs to fai rdislodge s dus tcak e o n th e exterio rof '•=•;each'ba g 'a s i ttravetslrcn rthe-tap-fr o th e botto m o fth e -bags ; •-Release d fro m th e bag;-the-dust-cake - feKs-by • . ' } gravit yint o th e hoppe ra tth e botto m ofth e module . Fro m ther e i ti s discharge d to a conveyo rsyste m tha t transport s i tto a d ur n p tra i ler , o re q u iv a Ie n I typ e system . Treate d b yth e spra ydrye rabsorbe ran d filtere d b yth e fabri cfilter , th e cleane d flu e ga s exit s th e Fabri cfilte r module s t o a n outle tmanifol d fo rexhaus i 2 .5 .1. 4 Induced Draft Fa n an d Stac k Th e induce d draf t fa n an d stac k ar e locate d downstrea m o fth e fabri cfilter
. Combustio n gase s ar e draw n throug h th e syste m b ya 7 5 h p induce d draf t (ID ) fan , rate d a t15,00 0 acf m a t400 nF saturated , an d 22 " wate r colum n pressure . Th e induce d draf t fa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s throug h th e spra ydrye rabsorber , Fabri cfilter , an d al l interconnectin g ducts . Th e I D fa n include s a n infet volum e contro l dampe rto b e use d t o contro l th e velocit yo fth e ga s withi n th e ductin g an d treatmen tdevices , Treate d gasse s exhauste d fro m th e induce d draft fa n to th e atmospher e throug h a 90-ft
. hig h stack . Th e stac k diamete ri s 3 9 inche s I.D . Th e stac k i s equippe d wit h instrumen tsamplin g port s an d a samplin g platfor m fo remission s testing . Figur e 4- 1 provide s detail s o n th e desig n an d sampl e port location s an d configuration s fo rth e stack . 

### 2, 6 Stac k

Emission s Monitorin g [4 0 CF R §53,1207(f)(1)(iii}(H) ] Th e continiJousemissionsmonitoringsystem(CEMS)consistsofsamp' e probes , s a m pi e d e l iver ya n d conditionin g apparatus , an d ga s analyzers . Sample s ar e extracte d fro m th e samplin g port s o n th e stack , A
2-1 1 Febrjgr yC E M performanc e tes tan d qualit yassuranc e progra m ha s bee n implemente d i n accordanc e wit h th e Appendi xt o Subpar

t EE S o fPar t 63— QualityAssuranc e Procedure s fo rContinuou s Emission s Monitor s Use d fo rHazardou s Wast e Combustors . Response s fro m eac h CEM S wer e fe d to th e Contro l Syste m [CS ) wher e th e CO ' hourl yrollin g averag e wa s calculate d an d fnterfocke d t o th e wast e fee d cutof fvgtve s a s par to fti e Automati cWast e Fee d Cutof fSyste m (AWFCO ) discusse d i n Sectio n 2.8 , below . Th e followin g provide s a brie fdescriptio n o fth e CEM S instrument s includin g th e operatin g rang e an d measuremen tprincipal . 2.6. 1 CEM S Syste m Descriptio n Th e Continuou s Emission s Monitorin g System s (CEMS ) currentl yutilize d a tIncinerato r3 analyze s fo ropacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , excep topacity , ar e extractiv e device s mounte d i n samplin g port s o n ih e stack . Th e tabl e belo wsummarize s th e analyze r specifications
. Th e opacit ymonito rcontinuousl ymeasure s th e stac k ga s opacit yan d report s th e measurement s t o a n indicato ran d a recorder . A n opacit ytha t exceed s a prese tlimi t trigger s a n alar m an d interlock . Carbo n monoxid e an d hydroge n chi crid e ar e monitore d wit h extractiv e non- d i s pers e infrare d analyzers , Tota l hydrocarbo n i s monitore d wit h a n extractiv e flam e io n detecto ranalyzer . Oxyge n i s monitore d wit h a zirconiu m oxid e cell . ' Stac k ga s flo wrat e i s continuousl ymonitore d usin g a n anuba rtha t send s a 4-2 0 rr. Asigna l t o th e PL C that •Gorvvdrts the-signa l .t

o .acf m Ta bl e 2-1 Continuou s E m iss l o n M o n ito rs Paramete r Curren t Mfg . Rang e Principl e Oxyge n COS A D-25 % Electrochemica l Carbo n Monoxid e Ecoche m MC 3 0-20 G ppm v D-300 0 ppm v Infrare d Tota l hydrocarbon s Thermoelectro n 0-10 0 ppm v FiD /lnfrare d Hydroge n chlorid e Ecoche m MC 3 0-1,00 0 ppm v Infrare d Opacit y Teledyrt e 0-100 % Whit e ligh t Stac k ga s flo w PSE'Rosemoun t 0-20,00 0 acf m Pressur e dro p 

### 2. 7 Proces s Monitorin g an d Contro l Th e facilit yi s equippe d wit h a state-of-the-artmonitorin g an d contro l system , whic h facilitate s complianc e wit h permi tconditions. , an d otherwise , collect s proces s control information , facilitate s efficien toperatio n an d detect s an d prevent s damag e t o th e facility
. Th e syste m consist s o fthre e majo rcomponents :

* Ahuman^machtn e interfac e (HM ) system , •Pro g ra m m a bl e lo g i ccontroll e r' s ( P LC's} , a n d

2-1 2 FebruEF yK>l o

# A~€OM

* Ahig h spee d ethe m e tc a b l s c o n n ect s a 1 1 co n cro fsyste m co m p o h ent e Th e desire d contro l function s ar e implemente d throug h th e HM I system . Ai l digita l contro l an d emergenc y interlock s ar e accomplishe d b yth e PLC
. Th e contro l syste m i s capabl e o fmonitorin g th e "operationa l envelope " o fth e incinerato ran d i s capabl e o f performin g a numbe ro factivitie s including :
» Contro l roo m indicatio n o fprocesso rsensor s locate d withi n th e incinerato rsyste m {suc h a s pressur e indicatio n o

fa fiei d instaile d pressur e transmitter) :
* Proces s controlle rfo rsingl e instrumen tfoop s o ra n individua l sub-system , suc h a s a temperature contro l loop involvin g a senso rreadin g fro m on e temperatur e transmitte raffectin g th e functio n ofon e temperatur e contro l valve : an d

•Alar m fo ra n exceedanc e o fa designate d setpoint , suc h a s a hig h pressur e o rlo wtemperature. Th e proces s contro l compute rwil l continuousl ycontro l an d monito rth e operatio n o fth e incinerator . Whe n out-of-rang e conditfon s exist , i twi tnotifyth e operato ro fthos e conditions . Th e proces s contro l compute ri s programme d to shut-dow n equipmen t(i.e. , brin g th e syste m int o a saf e mode ) whe n designate d parameter s ar e exceede d whic h i s a protectiv e mechanis m agains tpotentia l equipmen tdamage , operatio n outsid e o f permi tlimits , o rcondition s that migh tlea d to a releas e to th e environment . Continuou s rr.onitorin g o fth e incinerato ran d scrubbe rsyste m i s a n importan taspec to fth e syste m design , A •digitorreaticc to fai fmonitorin g Instrumentation ' is displayed-o n th e 'mai n -control - screen : An-autfibl e an d visual alar m alert s th e incinerato roperato rt o significan tdeviation s fro m norma l operatin g conditions . Thi s syste m allow s a n immediat e respons e t o advers e condition s b yth e operator . Automati cwast e fee d cut-of fen d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m a to rprio rto reachin g permi tlimi t levels . Monitorin g method s an d calibratio n frequencie s ar e liste d i n Tabl e 2-3 , Th e incinerato rha s a n independen tproces s contro l compute rtha t Interface s t o th e Quantu m Progammabl e controllers , Th e proces s compute ri s capabl e o fcontrollin g th e incinerato ri n cas e o fa failur e i n a HM I server . Thi s compute rrun s a RSVIE WHM I contro l softwar e tha t provide s operato rrnterfac e to al l instrumentatio n an d controls , 

### 2. 8 Automati c Wast e Fee d Cut-of fSyste m [4 0 CF R §53.1207(f ) (1)(m)(F)] Th e incinerato rha s a n Automati cWast e Fee d Cut-Of f(AWFCO } Syste m tha t wil l shu twast e feed s of fi n th e even tcertai n operatin g parameter s deviat e from allowabl e se tpoints , Th e PL C continuousl ymonitor s operatin g parameters , makin g adjustment s to th e proces s a s neede d fo rprope rcontrol , Alar m logi ci s incorporate d int o th e PL C syste m to automaticall yinitiat e a n AWFCO
. Tabl e 2- 3 summarize s th e curren t AWFC O se tpoints , AWFC O limit s hav e bee n establishe d base d o n severa l factor s that ar e summarize d below ,

•R e g u lat a ry/per m i ti i m it s - e stab l i s h e d t o c o m pl ywit h existin g per m its . A n ex a m pi e o fthi s typ e ofI i m it i s th e le wtemperatur e limit , belo wwhic h wast e ca n no tb e fe d unti l th e prope rlimi t i s re-established . I n addition , Sh

e HW C MAC Tregulation s requir e tha t th e AWFC O syste m b e interlocke d wit h th e spa n ofeac h proces s instrumen ttha t i s parto fth e Continuou s Monitorin g Syste m (CMS) , Alistin g o fthes e 2-1 3

# AZCOM CM S instrument s an d thei rinterlocke d spa n setpoint s i s maintaine d a s par to fVeolia' s Operatin g Record . •
* Proces s safet yfimit s - establishe d t o assur e proces s equipmen ti s protecte d an d unsaf e operatin g condition s d o no toccur . A n exampl e o ftfvs i s inadequat e exces s ai ri n th e combustio n chambe rtha t ca n lea d to fue l ric h conditions . •Utilityo rPowe rfailur e - establishe d to facilitat e a controiie d shutdow n ofth e proces s durin g los s o f proces s air , steam , wate ro relectricity . A n exampl e o fthi s i s th e los s o finstrumen tai rtha t i s necessar yfo rcertai n type s proces s instrument s t o functio n properly . Waste s wil l no tb e re-introduce d •i n to t h e i n ciner a tors u n t i I proper ' o p e ra tio n o fke yinstr u m ent s i s re-ostab i ished . I n additio n t o th e AWFC O system , operator s ca n manuall yshutdow n wast e feed s o rth e entir e proces s shoul d thi s b e needed . 2.8. 1 AWFC O Syste m Testin g Veo;'i a test s th e AWFC O system s bi-weekly' , a s weekl ytestin g woul d undul yinterfer e wit h operation s b y 'ceasin g an d restartin g wast e feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s durin g th e downtime , an d increasin g operatin g costs . Testin g o fth e AWFC O syste m i s a time-consuirtih g an d manpowe rintensiv e process , Th e curren ttestin g progra m ha s bee n i n plac e unde rth e RCR Apermi tfo rove r2 0 year s an d ha s prove n to b e adequat e i n detectin g problems . Thi s rational e i s include d i n th e facility' s AWFC O Plan . I n som e case s thi s testin g occur s mor e frequentl ydependin g o n ho w ofte n actua l AWFCO s occu ra tth e uni t Pe rthe.require d frequency, incinerato rpersonne l chec k th e functionalit yc fAWFC O logi ctha t i s part'o fth e incinerator' s PL C syste m i o mak e sur e tha t shoul d proces s •csflditkms-deviat e from-allowable-limite i -the- compte rk^icwili-imtiato-waste-fee d shutdo\vns-as-required
. Thi s i s accomplishe d b ymanuall ysimulatin g proces s condition s tha t ar e outsid e allowabl e limit s an d observin g an d documentin g whe n th e contro l o rbloc k valv e softwar e logi co n th e wast e fee d lin e begin s to initiat e vaiv e closure . Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e ar e documente d b yoperatin g personne l to satisf yregulatoryrequirement s fo rsyste m testing . R e suit s o fthi s testin g ar e documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par to fth e unit' s Operatin g Record . 

### 2. 9 Ai rPollutio n Contro l Equipmen t Maintenanc e Practice s [4 0 CF R §63.l207(f)(1){iii)(G) ] 2.9. 1 Progra m Overvie w Onc e equipmen ti s installe d an d operational , Veoli a utilize s a n extensiv e preventativ e maintenanc e (PM ) progra m t o kee p equipmen toperationa l an d preven tbreakdown s an d failures , Base d upo n th e typ e o f equipmen tan d historica l operation s an d maintenanc e experience , schedule s fo rvariou s inspection-an d P M ' activitie s ar e followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenanc e historie s o n equipmen troutin e inspectio n an d lubricatio n program s fo rhig h wea requipmen tan d non-destructiv e testin g o f pipin g an d vessel s usin g technique s like ultrasoun d to asses s integrity . Th e frequenc yo fthes e activitie s varie s dependin g upo n th e equipment , P M activit yan d th e incinerator s shutdow n schedule , Fo rexample , frequen t(i.e. , weekly ] instrumen tan d certai n mechanica l equipmen tcheck s ar e mad e fo rcritica l proces s items . Lubrication , vibratio n analysi s an d othe rmechanica l integritycheck s ar e don e a tlonge r frequencie s lik e monthl yo rquarterly. Finally , suc h item s a s inspectin g refractorybric k fo rwear , ar e typicall y performe d whe n th e entir e incinerato ri s shu tdow n fo rmaintenance . 2-1 4 FefcfUETj J EC1 C2 .9. 2 Tes t P r o g ra m P re p a rat i o n Ac t fviti e s Prio rt o testing , instrumentatio n associate d wit h ke yparameter s o fth e tes twer e checked , calibrated , o r repla-ed , a s appropriate , C o ensur e prope roperatio n o fth e instrumentatio n durin g testin g (i.e. , wast e feed flowmeter s an d scales . CEMS , pressur e transmitters , thermocouples , stac k flowmeters , etc.)
.

2-1 5 Febrgf^ 1 PO'. cTabl e 2- 2 Technica l informatio n Summaryor t Incinerato rNo , 3 Manufacture r . . Trad e Wast e Incineratio n Mode l No , TWI-2000 : Serie s 2 Typ e Fixe d Hearth , Dua l Chambe r Dat e o fManufactur e 19S 7 Dimension s Primar yChambe r Secondar yChambe r Exter n a f

Lengt h 17,5 * 17.5 ' Externa l Diamete r 9 ' 9 ' interna l Diamete r TT • TT 

# i

•Cross-sectiona l are a 40. 3 squar e fee t 40. 3 squar e fee t

Burner s : Primar yChambe rBurne r Secondar yChambe rBurne r Manufacture r Mont h America n Mort h America n Siz e 12, 0 Millio n Btu/h r 6, 0 Millio n Bium r Fuel ' Natura l Ga s Natura l Ga s Prime rMove r induce d Draf tFa n 15,00 0 acf m © 400 ; > F saturated , 2 2 in . wate rcolum n

2-1 6 Fcirruori ) 201 0Tabl e 2- 3 Curren t AWFC O Parameters an d Limit s fo rIncinerato rNo , 3 Syste m Devic e Unit s CutoffLimit s Calibratio n Frequenc y Tota l Pumpa b l a Wast e Fee d rat e Mas s Fiowmeters/Scaie s Lb/h r > 310 7 (HRA ) Annuall y• Tota l Wast e Feedrat e Mas s Flowmeters/Scaie s . •Lb/hr ' >401 7 Annually/quarterl y High BT U Liqui d feedrat e Mas s flo wmete r ! •lb/h r > 2,012 2 Annuall y. Lo wBT U Liqu/

d feedrat e •Mas s flo wmete r Jb/h r > 1.993 2 Annuall y Specialt yfeede r Stal e lb/h r > 724 2 Quarterl y Tota l LV M Feedrat e Mas s Fiowmeters/Scale s lb/h r > 4 7 (1 2 HRA ) Annualty/quarterl y pumpabl e LV M Feedrat e Mas s Flowmeters/ S care s lb/h r > 4 6 (1 2 HRA ) Ann u airy/quarterl y iSV M Feedrat e Mas s Flowmeters/Scaie s lb/h r > 6 3 (1 2 HRA ) Annually/quarterl y MercuryFeedrat e Mas s Flcwrneters/Scale s lb/h r > 0.003 4 (12HRA ) Annuaily/quarterfy Chlorin e Feedrat e Mas s Flowmeters/Scaie s lb/h r > 218(1 2 HRA ) AnnuaHy/quarterfy •As h Feedrat e Mas s Flowmeters/Scaie s tb/h r > 67 3 (1 2 HRA } Annually/quarterl y PrimaryCombustio n Chambe rTemperatur e Typ o KThermocoupl e o p <1,59C (one-minut e average ) <1,71 2 (HRA' ) 5=2,4C- 0 (instantaneous) 3 Annuall y
iSecondar yCombustio n Chambe rTemperatur e Typ e KThermocoupl e ' F *1,79 4 (one-minut e average ) <1,84 5 (HRA 1 ) >2,40f l (instantaneous) 7 Annuall y PrimaryCombustio n Pressur e transmitte r in . w.c . > -0, 1 (5 secon d delay ) Quarterl y Secondar yCombustio n Chambe rpressur e Pressur e transmitte r in . w.c . ^ -0. 1 ( 6 secon d delay ) Quarterl y Spra yDrye rAdsorbe rOutle t Temperatur e Typ e KThermocoupl e T >5D Q (on e minut e average) 5 5 >42G(HRA )
. Annuall y Combustio n Ga s Flo wRat e Pito tTub e acf m >17.198 J H6.14 7 (HRA ) Annuall y Stac k Ga s Exces s Oxyge n 'Zirconiu m Oxid e fue l cel l % < 3 (one-minut e avg,) 2 Quarterl y Stac k carbo n monoxid e Infrare d ppm v £10 0 (HRA ) '^50 Q (on e minut e average) 2 Quarterl y Stac k Hydrocarbo n FI D ppm v > 1 0 (on e minut e average j ; Quarterl y Stac k ga s opacit y Whit e Ligh t % >1 0 (on e m i nute av e rage) 2 Quarterl y Stac k hydroge n chloride 2 Infrare d ppm v £10 0 (HRA) 2 2:500 (on e minute average) 5 Quarterl y Fabri cfilte rpressur e dro p Delt a P transmitte r in . w.c . £2 o r£1 0 ( 1 min . average ) QuarterlyMin . Sorben tFeadrat e DensityTransduce r lb/lbCI 2 ; ' <1.76 Min . Carrie rFlui d Flowrat e Flowmete r gal/l b Cla S <1.70 Annuall y 1 HR Amean s "hourl yrailing average * a s calculate d b yaveragin g th e previou s 6 0 one-minut e averag e values . j 2Thi s i s a RCR Apermi tlimi t only . i

2-1 7

# AXO M Figure 2 - 1 Hydrate d Lime Specification s

^r.n . 'ESTFfvn-C-*«t l 1..-iji-.f i

cuds xf fiJL
•i . . . , l n

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" C D-trrf—m-Jrx^i ^ upon , dLacr-a- o •* £

2-13 ' Februar y2D' 0

# IncineratorProces s Descriptio

n Unit4

## 2, 0 Incinerato rProces s Descriptio n 

# MCQM

2. 1 Proces s Overvie w

•Veoli a operate s two Fixed'Heart h Dua l Chambere d incinerator s (Unit s 2 an d 3 ) an d on e rotarykiE n -incinerato r (Uni t4 ) a tth e Sauget , I LFacility , Th e tw o fixe d heart h unit s ar e rate d a t 1 6 m i I iro n Btu/h reach , incineratio n Uni trVo , 3 i s a mirro rimag e o fUni tMo , 2 , Bot h o fthes e unit s hav e thei row n wast e handlin g system s a s describe d i n th e section s tha t follow
. Th o onl ydifferenc e bein g Uni tNo , 2 i s equippe d wit h fou r(4 ) baghous e modules , whil e Uni tNo . 3 i s equippe d wit h thre e (3 ) baghous e modu'es . However,'eac h incinerato ri s operate d identicall ywiti i onl ythre e baghous e module s i n servic e durin g operation , Uni t4 i s rated a t5 0 missio n Btu/h ran d Is

equippe d wit h it s ow n tan k far m system , dru m storage , bul k solid s storag e an d fee d systems , 

### 2. 2 Wast e Fee d System s [4 0 CF R § 63,1207{f)(1}(ii)(c) an d(f)(1)(!ii)(D) and (E) ] 2.2. 1 Uctit 4 Liqui d Waste Fee d Syste m an d Slendin g Operafion s Th e Uni t4 RotaryKil n ca n incinerat e any-o rth e wast e that Veoli a i s authorise d an d perrrrcte d t o receive . Al l physica l form s o fwaste s wil l b e handle d an d fe d b yth e system' s wast e fee d devices . Liquid s wil l b e fed to eithe rth e kil n o rth e Secondar yCombustio n Chambe r{SCC)
. Bul k soli d waste s wil l b e fe d t o th e kil n throug h th e ra m feeder
. Containerize d waste s wil l b e fe d t o th e kiln , thro ug h th e ra m feede ro rth e auxiliaryra m feeder
. Thi s uni t ca n receiv e an ycombinatio n o fwaste s - liquid , semi-solid , o rsoli d - wit h a hea tvalu e o fu p to 5 0 m ii i io n Btu/hr
. •' •

•'Unit- 4 'i s supporte d ty'Storage-tanks-locate d in-Tank-Farm-#3. - - These-tank s -ar e used-t o stor e the-Hquf d •organic wastes , aqueou s wastes , an d pumpabl e sludge s to b e fe d t o th e system ; Uniik e Tan k Far m #1 , al t o fth e tank s i n Tan k

Far m #3 ca n b e use d a s fee d tank s to th e incinerator . Severa l criteri a ar e importan ti n designin g a blen d fro m receive d wastes , Thes e includ e compatibility , prope rrang e o fheatin g value , an d permi t restriction s regardin g elementa l compositio n (hase d o n emissio n limitations)
. Pump s t o transfe rthes e waste s t o th e syste m ar e installe d i n th e tan k farm , Th e material.i s transferre d throug n abovegroun d pipeline s fro m th e tan k far m to th e incinerator , Pipeline s use d t o transfe rliqui d organi cwast e an d aqueou s wast e ar e equippe d wit h strainers . I n complianc e wit h th e Benzen e NESHAP , al l tank s ar e vente d t o individua l carbo n adsorptio n canister s fo r remova l o forganic s befor e vapo ri s discharge d t o th e atmosphere , Eac h carbo n adsorbe rcaniste ri s essentiall yequivalen tt o a 5 5 g ai l o n containe ro rgreater , i fnecessary . Ai l tank s ar e equippe d wit h conservatio n vents , i n additio n to th e carbo n caniste radsorber . Ai l tank s ar e grounded , and : flame arrester s . ar e installe d betwee n th e carbo n adsorber s an d th e tanks , 2.2.1. 1 Organi c an d Aqueou s Liqui d Wast e Feed s Th e liqui d wast e injector s use d i n th e combustio n chamber s ar e air-atomizin g injectors . Thss e ar e use d for injectio n o fpumpabl e sludges , aqueou s waste s an d organi cliqui d waste s to th e kil n an d fo rinjectio n o f organi cliqui d wast e fo th e SCC , Dua l flui d injectio n nozzle s wil l b e use d fo ratomizaiio n o fth e waste , Eac h o f th e injector s i s rate d a t 0-3O 0 gph , Th e liqui d wast e fee d nozzle s ar e sewe d b yparalle l redundan tpump s an d recirculatio n system s wit h bac k pressur e control .

2- 1 'Bm,ar y2C1 C

### 2.2.1 2 Package d an d B u Ik Soli d Wast e Feed s Container s cfwaste s ar e sample d an d analyze d afte rreceip ti n accordanc e wit h th e facility' s Wast e Analysi s Plan , These , waste s ca n the n b e delivere d directi ytp Uni t4 c rrepacked ' int o smal l combustibl e container s at th e facility
. Repackage d container s ar e delivere d to , an d staged , in ' th e Containe rStorag e L I n'tNo . 6 adjacen t t o th e Uni t4 incinerator . Whe n schedule d fo rfeedin g to th e system , th e container s o fwast e ar e transferre d by forkfift s t o th e fee d conveyor s servin g Uni t4 , Bul k solid s an d non-pumpabl e waste s ar e delivere d an d discharge d into wast e fee d bin s i n th e Byi k Solid s Storag e Buildin g afte rbein g received , sampled , an d analyzed . Aclamshel l operatin g fro m a n overhea d cran e i s use d t o transfe rthes e waste s fro m th e bin s t o th e fee d hoppers dischargin g t o th e system' s ra m feeder
. Th e weig h hoppe ri s equippe d wit h weig h cell s s o eac h charg e o fwast e ca n b e weighe d befor e i t i s discharge d int o th e ra m feeder
. Fugitiv e emission s ar e controlle d b ya baghouse . cyclone , an d carbo n adsorptio n syste m connecte d t o thi s system , Th e ra m feede ri s a 25-;nc h wid e by4 2 inc h hig h {insid e dimensions ) rectangula rtub e operate d b ya ' hydraulicall ydrive n ram . Th e ra m tub e i s equippe d wit h a vertical , hydraulicall yoperate d charg e doe rnea rth e Kii n end. . Thi s doo ri s opene d befor e th e ra m begin s advancin g to pus h a charg e int o th e kiln . Afte rth e ra m ha s Fuil yretracted , a Ji m i tswitc h trigger s th e doo rt o clos e s o a s t o protectth e ra m feede rfro m th e kiln' s radian thea tTh e ra m i s capabl e o foperatin g fro m 0-3 0 cydes/houx
. Th e to p fac e o fth e ra m feede rha s a X x2 ' openin g whic h receive s wast e charge s fro m th e hopper . Th e ra m feede risolatio n gate , th e charg e door , an d th e ra m operat e i n sequence . A cth e beginnin g o fa cycle , th e ra m i s full yretracted . O n a "start " comman d fro m -h e operato ro r%h e programmabl e controller , th e ra m feede r •fsojation-gate-opens-t o receiv e a -charge-o f-waste-from - -th e -h&pper.. . The.gat e .then , closes, , th e charge , doer..'... . opens , sn d th e ra m begin s it s advance . Onc o th e ra m reache s it s full ' extension , i t begin s to retract . Whe n th e rar n i s full yret-acted , th e charg e doo ri s close d an d th e cycl e ca n b e 'epeated . Thi s system' s sequence d operatio n combine d wit h th e negativ e pressur e i n th e kil n preven tfugitiv e emission s fro m escapin g th e kil n ra m feedersystem . Th e rar n feede rals o receive s container s o fwaste s delivere d b ya n auxiliaryfee d system . Th e auxiiiaryfee d conveyo ri s capabl e o fhandlin g charg e weight s o f1 t o 10 0 pounds . Th e syste m i s capabl e ofhandlin g charg e size s u p to 2 4 inche s i n diamete ran d 2 4 inche s tall . Th e auxiliaryfee d conveyo ri s capabl e o fmakin g 6 0 charge s a n hou ro ron e complet e cycl e ever yminute . • 2,2,1. 3 SpecialtyLiqui d Wast e Fee d Th e Speciait yFee d Syste m associate d wit h Incinerato rNo . 4 i s a Direc tinjec tLiqui d Fee d System
. 

### 2. 3 Manufacturer , Mak e an d Mode l o fth e Incinerato r[4 0 CF R § 63.1207{f)(1pi)(A} ] 2.3. 1 Combustio n Chambe ran d Burner s [4 0 CF R §53.1207(f)( 1 )(m)(B) an d (C ) Incinerato rNo . 4 feature s a two-stag e combustio n process . Ignitio n o fwast e materia l take s plac e i n th e kiln , o rprimar ycombustio n chambe r(PCC)
. Asecondar ycombustio n chambe r(SCC ) serve s a s a n "after-burner " fo rproces s gases-an d i s als o permitte d to incinerat e hig h Bt u liqui d waste . Ignitio n o fth e wast e take s plac e a t temperature s i n exces s o f160 0 degree s F . Th e secondar ycombustio n chambe rmaintain s a minimu m ter n p e rat u r e o

fapproxir rat e l y1B 7 5

d e g ree s F .

2- 2 rwriar y2Ci nTh e roar / kil n i s fabricate d ofcarbo n steei . Itha s approximat e dimension s c fB'S" O.D
. X35 ' -:ong . Iti s suppose d o n a one-degre e slop e b ytwo stee l tte s c- rridin g rings . Eac h ridin g rin g ride s o n tw o pair s o fstee l trunnion s an d hav e a n approximat e outsid e diamete ro f9 fee tS inches . Th e thicknes s an d fac e widt h o rth e trunnion s ar e approximatel y6 inche s an d 9 inches , respectively , Tabl e 2- 2 provide s a summar yo rth e ; n cin e rat o rde s i g n s pecificati o n s . Th e kil n i s -line d wit h approximatel y7 Vi inche s c fdens e abrasion-resistan thigh-alumin a firebric k refractory , Wit h thi s refractor ysystem , th e kil n ha s a n insid e diamete rofapproximatel y7 fee tan d a lengt h o f approximatel y3 5 feet , a n integra l cross-sectio n are a o fapproximatel y3 8 squar e fee tan d a n ircsrra l volum e o fapproximatel y1,34 6 cubi cfeet
. Al l kil n feed s wil l ente rthroug h th e uppe rkil n fac e plat e whic h i s locate d o n th e fee d en d ofth e kiln . Th e plat e contain s a primar yburner , thre e liqui d fee d nozzle s {fo rpumpabi e sludge , aqueou s waste , an d hig h 3t u liqui d waste) , a ra m feede ran d a surg e ven l Th e primar yburne ri s equivalen tto a Nort h America n 'Fue l Directed ' ournerc f2 5 MMBtu/hr
. an d burn s No . 2 fue l oi l o rnatura l gas . Th e burne rsyste m i s supplie d wit h approximate ^ 4,00 0 acfr n combustio n ai ra ta stati c pressur e o f20 " wate rcoium n (WC)
. Th e pilo tfo rth e primaryburne rwil l bur n natura l gas . Th e fue l syste m fo rth e kii n (an d secondar ycombustio n chamber ) i s controlle d b ya FactoryMutua l approve d burne rmanagemen tsyste m complet e wit h interlock s an d safet yvalves . 2.3. 2 Secondar yCombustio n Chambe r(SCC )

. Tne.SC C i s a . vertical , .cylindrical.chamber.hawng . .approxi.roa.t e dirnension s of
. 1 G' : 6* . O,p , x7 TbighI t i s fabricate d c fcarbo n stee l an d line d with , a n Inner cours e (ho tface ) o fapproximatel ysi xinche s o fhig h alumin a refractoryan d a n oute rcours e o fapproximatel ytw o inche s o finsulatin g refractory
. Wit h thi s installe d refractory , th e SC C ha s a n insid e diamete ro fapproximatel ynin e fee tTh e effectiv e lengt h (ga s retentio n length ) o fth e chambe ri s approximatel y48 ' - 6". Consequently , th e SC C ha s a cross-sectio n are a o fS 4 squar e fee tan d a n effectiv e volum e ofapproximatel y3,08 4 cubi cfeet, A tmaximu m combustio n ga s flows, th e combustio n ga s residenc e tim e i s greate rtha n tw o seconds . Combustio n gase s from th e kil n ente rth e botto m o fth e SC C throug h a refractory-line d sid e duc tan d exi tfro m th e to p o fth e SC C throug h a refractory-line d duc tt o th e temperin g chamber . Th e floo ro fth e chambe ri s slope d t o facilitat e th e remova l oi as h an d solid s throug h a sla g tap . Tli e SC C i s equippe d wit h on e burne rmounte d o n th e sidewal l o fth e chambe rnea rth e bottom . Th e burne ri s a Tran e Therma l Model , o requivalent , wit h a desig n hea tre'leas e o fapproximatel y3 0 millio n Btu/hr , Thi s burne ri s supplie d wit h No , 2 fue l oi l o rnatura l ga s an d combustio n air . A s wit h th e kii n burner , th e SC C burne ri s supplie d wit h ato m kin g ai ran d i s equippe d wit h a burne r managemen tsystem . Thi s syste m control s th e ignitio n an d initiate s a n automati cshutof fwhe n ther e i s a los s o fflame , corr.bustio n ai rsupply , fue l pressure , atomizin g ai rpressure , pilo tburne ro rI D fan
. Th e SC C burne ri s a high-intensity , vorte xtyp e uni t wit h a spi n van e assembly , Socate d withi n th e win d bo xto imparta n intens e rotar ymotio n to th e combustio n air . Thi s rotarymotio n an d th e burne rdesig n provide , complet e mixin g o fai ran d fuel , an d recirculatio n o fth e gase s withi n th e combustio n chambe rpromote s rapi d combustio n an d hig h hea tintensity , 2- 3 Februar y201 0

# A~COM 2.3. 3 Locatio n o fCombustio n Zon e Temperatur e Devic e [4 0 CF R §63 .1 207[f){1)(xis) ] Th e pyromete rtha t monitor s temperatur e i n th e rotar ykil n i s locate d lop-cente ri n th e transitio n sectio n betwee n th e rotarykil n an d th e SC C abou ttwo Feetdownstrea m from , th e exi - of.th e kiln . Th e thermocoupl e tha t monitor s temperature i n the'SC C i s locate d o n - h e wes tsid e o fth e chambe rnsa rth e $C C exi tduct . 2.3. 4 Hazardou s Wast e Residenc e Tim e [4 0 CF R §63.1207(fJ( 1 Th e hazardou s wast e ga s residenc e tim e fo rth e Uni t4 RotaryKil n Incinerato ri s calculate d a s follows :

•Rotar yKii n Volum e - 134 6 ft 3
« S econ d a ryCombusiionChamberVolums-3D5 4 ft 3

•Tota l Volume-443 0 ft 3

* Maximu m Flu e Ga s Flowrat e - 43,00 0 acf m {71 7 frVsec )

* Tota l Combustio n Zone Residenc e Tim e = (443 0 ft 3 )/(71 7 ft 5/sec ) = 6. 2 se c Base d o n th e equado n 0=[(0. 1 DL)/(NDSJ] ; where : 0 i s th e residenc e tim e i n minutes , Li s th e kil n lengt h i n fee t

•N i s th e ratationai spee d n revolution s pe rminute , • S -i s the-kil n -slop e .i n feet.per
. feet,.an d D i s th e interna l diamete ri n feet , an d Insertin g th e know n value s fo rL(35) , N (2) , S (a,0174) , an d D (6,5 ) resul ti n a residenc e tim e fo rth e rotary kii n o f3 G minutes . 2.3. 5 Combustio n Syste m Lea k Th e kii n itsel fi s equippe d wit h a doubl e sea tsyste m tha i i s comprise d o foverlapping , adjustable , stainles s stee l sprin g plate s o n bot h th e fee d an d discharg e end s o fth e kiln , Th e seein g edge s ofeac h plat e ar e fitte d wit h a sintered-meta l wea rsho e simila rt o a brak e sho e wit h th e inne rsea l restin g o n th e kil n sheli . Th e powdere d meta l formulatio n ibrth e sea i shoe s i n crud e graphit e granules , whic h mak e th e shoe s setf lubricating . Th e voi d betwee n th e seas s an d th e oute rshel l ofth e kil n pressurize d to furthe rpreven tfugitiv e emissions , I n additio n t o th e kil n sea l system , Uni t4 als o utilize s a n induce d draft fa n tha t maintain s a vacuu m o f- 0. 5 to - 1. 0 inches.wate rcolum n whil e wast e i s bein g fire d int o th e system . 2.3. 6 Emergenc ySafet yVen t Uni t4 i s equippe d wit h tw o emergenc yvents , on e locate d atth e kil n inle twhic h act s a s a n emergenc y pressur e relief , th e secon d i s locate d a t th e to p o f;h e SC C a s a therma l reiie fvent . Th e emergenc yven ta t th e kil n inle twoul d onl yb e require d fo ran-occurrenc e that overwhelm s th e abilityo f th e I D fa n t o contro l th e pressur e .ofth e kiln . Th e ven tan d chut e openin g i s designe d suc h tha t wast e fro m th e bul k soiid s chut e woul d no timped e th e escapin g ga s flow
. Adeflecto rseparate s th e fee d flo wfro m th e ven t opening , Th e entrai n meri tc fsolid s throug h th e surg e ven ti s minimal . A s a n extr a precaution , th e exhaus t 

### 2-4 F5:ruap/2D1 C

# MCOM openin g o fth e ven t>s angle d t o provid e a horizonta l exit , thereb yminimizin g solid s entrai n men * int o th e air , Th e vehO s kep tclose d b yweighte d louvers . Thes e louver s wil l ope n onf' yi fth e pressur e i n th e kil n suddenl y rise s beyond'th e compensatin g capacit yc fth e I D fan , Alimi t switc h o n th e louver s wii fautomaticall yshutoffal l wast e feed s t o th e kil n an d SC C whe n th e ven ti s opened . Th e incinerato ri s als o equippe d wit h a n emergenc ysafet yven t(ESV ) locate d atth e to p o fth e secondar y combustio n chamber . Thi s ES Vi s a refractory-line d emergenc ytherma l relie fven t(TRV ) whic h i s hei d i n th e dose d positio n b ya pneumati ccylinder . Th e contro l valv e i n th e lin e supplyin g ai rt o th e cylinde ran d th e cylinde rven tvalv e whic h open s th e TR Var e locate d i n th e contro l roo m fo reac h unit . Valv e lock s (with , -tey s attached ) are utilize d to dete rinrjischrrJnat e operatio n o fthes e valves . Openin g cfth e TR Vallow s ho t combustio n ga s t o ven tfro m th e combustio n syste m durin g emergenc yshutdow n events . Th e purpos e o fth e TR V:s to protec tth e downstrea m ARC S fro m excessiv e temperatur e situations , Alimi t switc h o n th e TR V shut s of fal l wast e feed s t o th e syste m a s i tsense s tha t th e ca p i s opening . 

### 2. 4 Procedure s fo rRapidl yStoppin g Hazardou s Wast e Fee d Durin g Equipmen t Malfunctio n [4 0 CFR§63,12Q7{f)(1)(viii) ] Equipmen tmalfunction s ar e identifie d b yth e contro l system , observatio n c fproces s contro l variables , o rb y regula rfiel d inspections . I n th e even tc fa mino requipmen tmalfunctio n (e .g . wast e fee d o rscrubbe rleaks) , th e control roo m operato r wil l b e notified
. Th e control roo m operato rwil l the n clos e the-wast e fee d valve s an d disabl e th e wast e fee d pumps .

' 'in ' ihe'a've'nt'bT'rhapr ' equipmehi'malfiiihctior i '[e.g. ' fire}, ' th e emergenc y'Stcp-butiorrfocate d in'th e •contro l roo m •• • wil l b e pushed . I fthi s butto n i s pushe d al l equipmen twil l switc h to its fail-saf e position , 

### 2. 5 Aa rPollutio n Contro l Equipmen t [4 0 CF R §63.1207(f)( 1 )(iii){G)] 2,5. 1 Ai rPollutio n Contro L System s Description s Th e ai rpollutio n contro l syste m consist s o fa temperin g chamber , two spra ydrye rabsorbers , an d fabri cfilte r baghous e modules . Th e ai rpollutio n contro l syste m neutralize s acidi ccompound s an d remove s particulat e from th e exhEus tgas . Tw o subsystems , th e spra ydrye rabsorbe ran d th e fabri cfilter , carryou tth e chemica l neutralizatio n an d particulat e remova l functions , respectively . Athird subsystem , th e lim e system , i s use d t o prepar e an d provid e lim e slurryt o th e spra ydrye rabsorbe rfo rus e I n th e chemica l neutralizatio n process . Th e induce d draft fa n an d stac k provid e th e mechanica l energ yrequire d to transpor tth e Flu e ga s thro-jgi i th e interconnectin g ductwork , t o its eventua l discharg e poin tt o atmosphere . 3?.3,1,1 Tamperin g Chambe r Th e tempering chambe ri s a vertrca? , cylindrica l uni t designe d to coo l th e combustio n gase s usin g a serie s o f interna l dual-flui d (wate ran d air) spra ynozzles , Th e combustio n gase s ente rth e to p o fth e chamber , flo w downwar d throug h th e spra ypatter n an d exi tfro m th e botto m o fth e chamber , Th e spra ypatter n i s designe d to eliminat e direc tcontac to fwate rwit h refractory , an d th e chambe ri s designe d t o maintai n a drybotto m unde r al l operatin g conditions , Tha tis , th e injectio n rat e o fspra ywate ri s controlle d s o that i tis'completel yvaporize d an d carrie d ou to fth e chambe ri n th e combustio n gases . Th e temperin g chambe ri s approximatel y49 ' hig h wit h 11 ' I.D . an d i s fabricate d o f3 4 inc h nomina l plat e thicknes s carbe n stee l (AST M A36 ) an d line d wit h refractory , Th e spra ynozzle s an d extension s ar e fabricate d o f30 4 S S material . 2- 5 Rsna.ar y?, 31 •

# AICOM Th e tempering chambe ri s size d s o that a comoustio n ga s retentio n tim e o fgreate rtha n on e secon d wil l be \ maintaine d a : al l ga s flows
. Becaus e sem e molten-particulate material s i n th e combustio n gase s ar e coole d < n thi s proces s u ritto belo wthei rfusio n poin tsom e solid s ar e generate d an d collecte d i n th e chamber . Therefore , th e chambe rha s a con s botto m an d a slid e gat e t o facilitat e th e remova l o fsolids . Thes e solid s ar e discharge d ont o a .conveyo rsystem , whic h Transport s the m to a hoppe r 2.5.1, 2 Lim e Syste m Th e lim e system-prepare s iim e slurryfo rus e i n th e chemica l neutralizatio n proces s i n sufficien tsuppl yan d concentratio n t o maintain - continuou s Hu e ga s treatmen ti n th e spra ydrye rabsorber . Th e syste m ha s bee n designe d fo rbatc h mixin g t o provid e thi s service . Veoli a utifee s hydrate d lim e a s it s neutralizin g agen ti rth e ai rpollutio n contro l systems . Th e ke yneutralizatio n paramete ro fth e hydrate d iim e i s th e 'Ca O Equivalent. " Figur e 2- 1 i s th e specificatio n shee tfo rth e hydrate d lim e tha t Veoli a uses . Veoli a ha s use d thi s specifi c produc tfo rove r2 D year s an d plan s to continu e wit h it s use , Althoug h i fVeoli a dee s chang e supplier s o rtyp e o flin e i n th e future , itwoul d hav e a "Ca O Equivalent ' specificatio n equa l to o rgreate rtha n th e 72,5 % shew n o n Figyr e 24 . Hydrate d lim e i s store d i n a storag e bi n abov e th e lim e preparatio n area . Th e storag e bi n i s size d t o hol d enoug h hydrate d iim e t o maintai n severa l day s a fsyste m operatio n a t th e maximu m combustio n rat e o fth e incinerator . Lim e i s discharge d throug h th e conica l storag e bi n bottom , Th e flo wo fth e materia l fro m th e bi n i s aide d b ya vibratin g "liv e bottom, " o rbi n activator . - Avariabl e spee d scre wfeede ri s use d t o mete rth e hydrate d lim e i n th e proportion s require d fo rbatc h mixin g lim e siurry . Th e iim s i s mixe d wit h wate ri n a tan k . beneat h th e lim e storag e bin . Th e scre wfeede rspee d an d th e rat e tha t wate ri s adde d t o th e iim e siurrySan k ar e variabl e s o tha t th e desire d lim e solid s concentratio n ca n b e achieve d i n th e tank . Th e variabl e fee d S . adji i strne'f i fs ' allo wwal e ra h d T l m e t o b e adde d t o th e ir m e -siurr y•tan k •a t -a - rat e tha t -wi n allo w•a- ba'o h mod e -o f mixing , A n agitato ri s provided ' i n th e slurr ytani < to mi xth e wate ranc ' lim e an d to maintai n th e suspensio n of lim e solids - Th e mixe d lim e slurryI s pumpe d a ta continuou s rat e o fflo wthroug h a recirculatio n loo p to th e SD Anozzles , 2.5.1,3 . Spra yDr

yAbsorbe r
•Uni t4 i s equippe d wit h tw o Spra yDrye rAbsorber s (SDA ) locate d immediatel ydownstrea m o fth e Temperin g Chamber
. Eac h SD Auni t i s fabricate d of3/8 inc h carbo n steel , Th e functio n o fth e SDA s i s to :
» Furthe rcoo l th e combustio n gase s fro m 600-800° F t o 3DO-500 r 'F , * Neutraliz e an d remov e HC l an d othe racid s fro m th e combustio n gases , •R e m ov e a p o rtio n ofth e p a di e u I at e ffl ya s h} fr o m th e s e g ases . Slurr yfio wt o eac h spra ydrye rabsorbe r(SDA ) i s metere d b ya flo wcontro l valv e to obtai n th e prope rfee d concentratio n to th e spra ydrye rabsorber . Manua l adjustmen tto th e flo wi s mad e a s a functio n o fth e SD A outle ttemperatur e an d a s a functio n o fth e outpu t fro m a hydrochlori caci d (HC! ) analyze ri n th e ga s duc t downstrea m o fth e fabri cfilter
. Th e combine d unit s ar e size d to remov e mor e tha n 82 0 lb/hr
. o fchtori.i e fro m tri e combustio n gases . Eac h SD Ai s approximately-72 ' hig h by10'7 " i n diameter . Eac h uni t include s a hea d section , an d a 50*conica l hopper . Each . SD Achambe rha s on e acces s doo ri n th e uppe rsection . Eac h hoppe rha s on e acces s door , a S flanged clean-ou tperl , an d a drai n connection . Th e SD Ahea d sectio n consist s o fa flange d inle tconnectio n -
2- 6

# AXOM
an d a ho ? ga s inls tplenum . Th o dual-flui d aicmizinrj nozzle s includ e stainles s stoo l housing, ? an d steiiiic d inserts . Th e nozzle s ar e assemble d to permi tfiei d remova l Fro m th e piping , Th e too lim e slurr ypipin g header s hav e automati cisolation'valves , Combustio n gase s ente rth e to p o feac h ofthes e units , flo wdownwar d throug h a centra l ductan d ar e disperse d symmetricall yfro m thi s duc tinto th e absorbe rchambe ra ta velocit yan d directio n that assure s optima l contacc-wit h th e clou d o fatomize d lim e slurrydroplet s introduce d into th e chambe rbydual-flui d (lirn e slurryan d air } rozzlcs . Th e gase s the n flo wdownwar d throug h eac h absorbe rchambe ran d exi tthroug h a botto m sid e duct , A s th e gase s contac tan d pas s throug h th e clou d o £atomize d iim e slurry , th e wate ri n th e slurryevaporates , coo'in g th e gases . Simultaneously , th e lim e i n th e slurryreact s wit h th e hydroge n chlorid e i n th e gase s to produc e calciu m safts
. Som e o fth e resultin g dr ymaterial , consistin g o fcalciu m salts , fl yas h en d exces s lime , fall s to th e conica l botto m o feac h unit , Th e drymateria ) fro m eac h uni t i s discharge d to a conveyo rsyste m whic h transport s i tto a dum p trafe ro requivalen ttyp e system . 2 .S.1. 4 Fabri cFilte r Ga s exhauste d fro m th e spra ydrye rabsorber s i s distribute d to tw o feoricFilte rmodule s connecte d i n parallel . Eac h modul e i s divide d int o thre e compartment s connecte d i n parallel , whic h contai n multipl e fabri cfilte rbag s throug h whic h th e combusto rgase s pas s t o .remov e particulates . Within eac h compartment , th e ga s i s passe d throug h Teflon-coate d fiberglas s clot h bags . Th e ga s passe s From th e outsid e to th e insid e ofth e filte r bags . Particulat e entraine d i n th e ga s strea m i s mechanicail ydeposite d o n th e outsid e o fth e filte rbag s a s th e ga s passe s throug h th e cloth . Eac h compartmen tha s a clea n ai rplenu m an d housin g sectio n to contai n approximatel y30 8 bags . Eac h ba g •is'HppTcximatery'5 :l 'fndiamet8rby-5 ! - long,-Tte-baghouses-^e-febrica ^ construction , ga s tigh t an d stiffene d to withstan d th e maximu m operatin g negativ e pressure . Eac h compartmen tha s a tub e shee ttha t support s th e baa s an d provide s for top bag/cag e removal . Acces s t o th e clea n ai rplenu m i s vi a a bolte d acces s door . Eac h traile rmounte d rnit contain s th e compresse d ai rheaders , ga s inle tan d outle tmanifolds , an d th e conveyor . Th e fabri cfilte rcleanin g mechanis m utilize s jet s o fai rto clea n th e filte rbags , Periodically , th e cleanin g sequenc e wil l b e initiated , Th e sequenc e i s starte d whe n th e differentia l pressur e acros s th e tite rreache s a predetermine d setpoin to fapproximatel y8-0 " w.c , o rwhe n th e operato rinitiate s a cycle . Th e controlle rthe n sequence s t o eac h rowo ffilte rbag s i n eac h module^ refeasin g a burs to fai ropposit e to th e directio n o fga s flew , Th e quickl yrelease d burs to fai rdislodge s dus tcak e o n th e exterio ro feac h ba g a s i ttravel s fro m th e to p to th e botto m c fth e bags . Release d fro m th e bag , th e dus tcak e fall s b ygravit yint o th e hoppe ra tth e botto m o fth e module , Fro m ther e i ti s discharge d to a conveyo rsyste m whic h transport s i tt o a dum p trailer , o r equivalen ttyp e system . Treate d b yth e spra ydrye rabsoroer s an d filtere d b yth e fabri cfibers, th e cleane d flu e ga s exit s th e fabri cfilte r compartment s t o a n outle tmanifol d fo rexhaust . 2.5.I S Carbo n Injectio n Th e carbo n injectio n syste m wil l ai rinjectactivate d carbo n int o Sh e plenu m immediatel yupstream o fth e baghouse s an d allo wfo ra mor e efficien tmean s o fcontrollin g Dioxin/Fura n an d mercuryemissions . Thi s syste m wil l b e controlle d bya n existin g PL C whic h wil l contro l th e inpu to factivate d carbo n t o th e baghous e inie tplenum . 2 to 2 0 pound s pe rhou ro fpowdere d activate d carbo n wil l b e ai rinjecte d int o thi s plenu m an d

2-7 ' Februar y231 C

# AZCOM allow fo rdirec ; contac twit h th e stac k gase s exitin g tli e *SDA's
. Tri o ke yadsorption , paramete rfo rth e carbo n i s

.. s tri e Iodin e IVunber . Figur e 2- 2 i s th o specificatio n shee tfo rth e powde r

### activate d carbo n thatVeoli a uses . Veoli a ha s use d th; s specifi cproduc tsinc e th e start-u p o fth e carbo n Injectio n syste m an d plan s to continu e wit h it s use . Although , i fVeoli a e'ee s chang e supplier s o rtyp e o fpowde ractivate d carbo n i n th e future , it woul d hav e a n Iodin e Numbe rspecificatio n equa l t o o rgreate rtha n th e 50 0 mc,' g show n i n Figur e 2-2 . Th e amoun to

fcarbo n : s dose d in a dust-fre e manne rint o a lo wpressur e ai rstrea m vi a pneumati ceduction , Th e eductc ruse s a blowe rfo rth e motiv e air . Hig h an d lo wai rpressur e switche s ensur e tha tth e blowe ri s ' operatin g correctl yan d tiia t th e carbo n deliverysyste m i s dea rfro m obstruction . Th e minimu m hig h pressur e setting , i s 4 psi g an d th e maximu m lo wpressur e settin g i s 1 inc h wate rcolumn . Th e carben/ai rstrea m wI I the n trave l throug h pipin g t o th e injectio n nozzl e int o th e ductwork . Th e carbo n wil l contac tth e ga s strea m exitin g th e SDA ' s an d allo wfo rth e adsorptio n o fan ydiosen/furan s an d mercurythatmigh tb e presen ti n thi s stream , Adsorptio n wf l continu e a s th e stac k gase s procee d throug h th e baghouses , Th e clea n stac k ga s wil l exi tth e finai'stac k

vi a th e induce d draf tfa n an d th e capture d solid s wil l b e discharge d fro m th e baghouse s vi a th e scre wconveyin g syste m int o a n enclose d dum p traile rfo rdisposa l a ta Subtitl e C landfill
. 2.5.1. 6 Induce d Draf tFa n an d Stac k

•Th e induce d craftfa n an d stac k ar e locate d downstrea m o fth e fabri cfilter , Combustio n gase s ar e draw n throug h th e syste m bya 40 0 h p induce d draf t(ID ) fan , rate d a t53,00 0 acf m a t400 c

### F saturated , an d 25 " wate r colum n pressure . Th e induce d draftfa n provide s th e mechanis m fo rtransportin g th e incinerato rflu e ga s throug h th e spra ydrye rabsorber , fabri cfilter , an d al l interconnectin g ducts . Th e ; D fa n include s a n inle t voium e contro l dampe rto b e use d t o contro l th e velocit yo fth e ga s withi n th e ductin g ar d treatmen tdevices . '"-Treate d gases'are ' exhausted'fro m 'the'induce d draft'fai t"to'th e atmb'spfrere ' throug h atCO-f thigh ' stack : The "

stac k diamete rfo rUni t4 i s 4 8 inche s I.D . Th e stac k i s equippe d wit h instrumen tsamplin g port s an d a samplin g platfor m fc remission s testing , Figur e 4 - 1 provide s detail s o n th e desig n an d sampl e per tlocation s an d co n Fi

g u ration s fo rth e stack , 

### 2. 6 Stac k

Emission s Monitorin g [40 CF R §63.1207(f)(1)(iH)(H) J Th e cont i r, u o u s s m issi o n s mo n fori n g syst e m fC E M 3 ) cons i st s o fsa m pi e probes , s a m pi e de l iveryan d conditionin g apparatus , an d ga s analyzers , Sample s ar e extracte d fro m th e transition ductin g locate d betwee n th e I D fa n an d th e stack . ACE M performanc e tes tan d qualit yassuranc e progra m ha s bee n implemente d i n accordanc e wit h th e Appendi xt o Subpar tEE £o fPar tS3—Qualit yAssuranc e Procedure s fo r Continuou s Emission s Monitor s Use d fo rHazardou s Wast e Cdmbustors . Response s fro m eac h CEM S ar e fe d t o th e Contro l Syste m (CS ) wher e th e C O hourl yrollin g averag e i s calculate d an d interlocke d to th e wast e fee d cutof fvalve s a s par to fth e Automati cWast e Fee d Cutof fSyste m {AWFCO ) discusse d i n Sectio n 2,5 , belaw . Tn e followin g provide s a brie fdescriptio n o fth e CErVi S instrument s includin g th e operatin g rang e an d measuremen tprincipal , 

### 2.S. 1 CE M Syste m Descriptio n Th e Continuou s Emission s Monitorin g System s (CEMS ) currentl ybein g utilize d a tIncinerato r4 analyze s fo r opacity , carbo n monoxide , hydroge n chloride , tota l hydrocarbon s an d oxygen . Thes e monitors , excep t opacity , ar e extractiv e device s mounte d i n th e ductwor k betwee n th e I D fa n an d th e stack . Th e tabl e belo w > summarize s th e analyze rspecifications
. 2- 8 Fsb-unr y£01 0Th o opacit ymonito rcor.tinuousl ymeasure s th e stac k ga s opacit yan d report s th e measurement s to a n indicato rana " a recorder . A n opacit ytha t excosd s a prese tlimi t tiggi^ s a n aiar m an d Interlock . Carbc n monoxid e an d hydroge n chlorid e ar e mastered - wit h extractiv e n o n-G:'s pers e Infrare d analyzers . Tota i hydrocarbo n i s monitore d wit h a n extractiv e flam e io n detecto ranalyser . Oxyge n i s monitore d wit h a zirconiu m 6x ; d a cell . Stac k ga s flo wrat e ; s continuousl ymonitore d usin g a n anuba rthat send s a 4-2 0 m Asigna l t o th e PL C that convert s th e signa ; to acfm
.

Tabl e 2- 1 Vsoli a E S Technica l Solution s - Continuou s Emission s Monitors Paramete r Curren t Mfg
. Rang e Principl e Oxyge n COS A ' 0-25 % Electrochemica l

. Carbo n Monoxid e Echoche m MC 3 •O-20 0 ppm v

•0-300 0 ppm v infrare d Tota l hydrocarbon s Thermoe-ectro n 0-10 0 ppm v F ID/Infra re d Hydroge n chioiid e Echochem , M C 3 0- 1 CCD ppm v infrare d Opacit y Teledyn e G-1G0 % Whit e ligh t

. . Stack , gas.flow
. PSE/Rcsemoun t 0-55,C0 0 acf m Pressur e dro p 

### 2. 7 Proces s Monitorin g an d Contro l Th e faciEityi s equippe d wit h a state-of-the-artmonitorin g an d contro l system , whic h facilitate s complianc e wit h permi tconditions , an d otherwise , collect s proces s contro l information ; facilitate s efficien toperatio n an d detect s an d prevent s damag e to th e facility
. Th e syste m consist s o fthre e majo rcomponents :

* Ahuman-machin e interfac e (Hivll ) system , » Programmabl e logi ccontroller s [PLC's h an d
» Ahig h spee d etheme i cabl e connect s al l contro l syste m component s Th e desire d ccntro i function s ar e implemente d throug h th e HM I system . Ai l digita l contro l an d emergenc y interlock s ar e accomplishe d b yth e PLC
. Th e contro l syste m i s capabl e ofmonitorin g th e "operationa l er.vefope : : o fth e incinerato ran d i s capabl e o f performin g a numbe ro factivitie s inoluciing :
» Contro l roo m indicatio n o fprocesso rsensor s locate d witht n ti e incinerato rsyste m (suc h a s pressur e indicatio n o fa fiel d .installe d pressur e transmitter) ;

2- 9 Februar y201 C» Proces s contr o I i e rfo rs in g I s i n str i J in s nt•oo p s o ra n i n d i vi d u a I s u b- s ysf cm , suc h a s a te m p e rature

s contro l loo p involvin g a senso rreadin g fro m on e temperatur e transmitte raffectin g th e functio n ofon e

temperatur e contrp i valve ; an d

* Alarm , fo ra n exceedanc e o fa designate d setpoint . suc h a s a h.:g h pressur e o rlo wtemperature . Th e proces s control compute rwii l continuousl ycontro l an d monito rth e operation , o fth e incinerator , W'n^ h out cf-rang e condition s exist , i twil l notifyth e operato ro fthos e conditions . Th e proces s contro l compute ri s programme d t o shut-dow n equipmen t{i.e. . brin g th e syste m int o a saf e mode ) whe n designate d parameter s ar e exceeded , whic h i s a protectiv e mechanis m agains tpotentia l equipmen tdamage , operatio n outsid e o f permi tlimits , o rcondition s tha t migh tlea d t o areleas e t o th e environment. . Continu e u s monitorin g o fth e incinerato ran d scrubbe rsyste m i s a n importan taspec to fth e syste m design , A digita l readou to fal l monitorin g instrumentatio n i s displaye d o n th e mai n contro l screen . A n audibl e an d visua l alar m aJert s th e incinerato roperato rt o significan tdeviation s fro m norma l operatin g conditions , Thi s syste m allow s a n immediat e respons e to advers e condition s byth e operator . Automati cwast e fee d cut-of fan d incineratio n shutdow n mechanism s ar e als o interlocke d wit h th e monitorin g syste m a to rprio rto reachin g

. permi tlimi t levels , Monitorin g method s an d calibratio n frequencie s ar e liste d i n Tabl e 2-3 . Th e Incinerato rha s a n independen tproces s contro l compute rthat interface s to th e A H en-Bra d le y programmabl e controllers . Th e proces s compute ri s capabl e o fcontrollin g th e incinerato ri n cas e ofa failur e i n aHM I serve: . Thi s compute rrun s aRSVIE WHM I centra l softwar e tha t provide s operato rinterfac e to ai i instrumentatio n an d controls . 

### 2: 3 Automati c Wast e Fee d - Cutof fSyste m {4 0 CF R fS3,42Q7{fK1 W»W)] Th e incinerato rha s a n Automati cWast e Fee d Cut-Of f{AWFCO ) Syste m tha t wil l shu twast e feed s ef fi n th e even tcertai n operatin g parameter s deviat e fro m allowabl e se tpoints . Th e PL C continuously - monitor s operatin g parameters, ' makin g adjustment s t o th e proces s a s neede d fo rprope rcontrol , Alar m logi ci s incorporate d '.hto th e PL C syste m to automaticall yinitiat e a n AWFCO
. Tabl e 2.- 3 summarize s th e current ' AWFC O se tpoints . AWFC O limit s hav e bee n establishe d base d o n severa l factor s tha t ar e summarize d below .
» Regulatory/permi tlimit s - establishe d to cornpl ywit h existin g permits . A n exarnpI e o fthi s typ e o fIimi t • i s th e lo wtemperatur e limit , belo wwhic h wast e canno tbe fe d unti l Lh e prope rlimi t i s reestablished . I n addition , th e HW C fVlAC Tregulation s requir e that th e AWFC O syste m b e interlocke d wit h th e spa n o feac h proces s instrumen ttha t i s par t o fth e Continuou s Monitorin g Syste m (CMS) , Alistin g o ftfiase C M S instrument s an d thei rinterlocke d spa n setpoint s i s maintaine d a s par to fVeolia' s Operatin g Record .
•Proces s safet ylimit s - est a b I i s h e d to ass u r e n reces s eq u i pmer ti s protecte d a n d u n saf e operat i n g condition s d o notoccur . A n exampl e o fthi s i s inadequat e exces s ai ri n th e combustio n chambe rtha i ca n lea d to fue l rich conditions , » Utilit yo rPowe rfailur e - establishe d to facilitat e a controlle d shutdow n o fth e proces s durin g tos s of proces s air , steam , wate ro relectricity . A n exampl e o fthi s i s th e los s o finstrumen tai rtha t i s necessar yfo rcertai n type s o fproces s instrument s t o functio n properly . Waste s wil l no tb e re introduce d int o th e 'incinerator s unti l prope roperatio n c fke yinstrument s i s re-estabtished .

2-1 0 Fstrjar y231 D

# A r-. i 

# COM I n additio n to th e AWFC O system , operator s ca n manuall yshutdow n wast e feed s o rth e entir e proces s shoul d thi s c e needed . 2,3, 1 AWFC O Syste m Testin g Veoii a tests th e AWFC O system s bi-weekiy , a s weekl ytestin g woul d undul yinterfer e wit h operation s b y ceasin g an d restartin g wast e feeds , potentiall yincreasin g emissions , incurrin g excessiv e downtime , burnin g additiona l natura l ga s durin g th e downtime , an d increasin g operatin g costs . Testin g c fth e AWFC O syste m i s a time-consumin g an d manpowe rintensiv e process . Th e curren ttestin g progra m ha s bee n i n plac e unde rth e RCFiA
. permi tfo rove r2 0 year s an d ha s prove n i o b e adequat e i n detectin g problems . Thi s rational e i s include d i n th e facility' s AWFC O Plan . I n som e case s thi s testin g occur s mor e frequentl ydependin g o n ho w ofte n actua l AWFCO s occu ra tth e unit . Pe rth e require d frequency , incinerato rpersonne l chec k th e functionalit yo fAWFC O logi ctha t i s par to fth e incinerator' s PL C syste m to mak e sur e tha t shoul d proces s condition s deviat e fro m allowabl e limits , th e compute rlogi cwil l initiat e wast e fee d shutdown s a s required . Thi s i s accomplishe d b ymanuall ysimulatin g proces s condition s tha t ar e outsid e allowabl e limit s an d observin g an d documentin g whe n th e contro l o rbloc k valv e softwar e logi co n th e wast e fee d iin e begin s to initiat e valv e closure. . Shoul d actua l AWFCO s occu rdurin g a give n testin g period , thes e ar e documente d b yoperatin g personne l t o satisf yregulatoryrequirement s fo rsyste m testing . Result s o rthi s testin g ar e documente d o n a separat e AWFC O Testin g Lo g an d maintaine d a s par to fth e unit' s Operatin g Record . 

### 2, 9 Ai rPollutio n Contro l Equipmen t Maintenanc e Piractics s [4 0 CF R

Onc e equipmen ti s installe d an d operational , Veoli a utilize s a n extensiv e preventativ e maintenanc e (PM ) progra m to kee p equipmen toperationa l an d preven tbreakdown s an d failures
. Base d upo n th e typ e o f equipmen tan d historica l operation s an d maintenanc e experience , schedule s fo rvariou s inspectio n an d P M activitie s ar e followed
. Thi s include s aspect s suc h a s documentin g detaile d maintenanc e historie s o n equipment , routin e inspectio n an d lubricatio n 'program s fo rhig h wea requipmen tan d non-destructiv e testin g o f pipin g an d vessel s usin g technique s lik e ultrasoun d to asses s integrity . Th e frequenc yo fthes e activitie s varie s dependin g upo n th e equipment , P M activit yan d th e incinerator' s shutdow n schedule . Fo rexample , Sequen t{i.e. , weekly } instrumen tan d certai n mechanica l equipmen tcheck s ar e mad e for critica l proces s items . Lubrication , vibratio n analysi s an d othe rmechanica l integrit ycheck s ar e don e a tlonge r frequencie s like.monthl yo rquarterly . Finally , suc h item s a s inspectin g refractorybric k fo rwear , ar e typicall y performe d whe n th e entir e incinerato ri s shu tdow n formaintenance . 2.9. 2 Tes t P rag ra r n P re parat i o n Acti vit i e s Prio rt o testing , instrumentatio n associate d wit h ke yparameter s c fth e tes twer e checked , calibrated , replaced, - a s appropriate , to ensur e prope roperatio n o fth e instrumentatio n durin g testin g (i.e. , wast e fee d flowmeter s an d scales , CEMS , pressur e transmitters , thermocouple s an d pyrometers , stac k flowmeters , etc.)
. 

### §63.12D7(f)(1Jp)(G) ] 2.3, 1 Progra m Overvie w

2-1 1 Fab-usry'201! ); Tabl e 2-2 Technica l Informatio n Summaryo n Incineratio n No . 4 [ Manufacture r Trad e Wast e Incineratio n • i ; i Mode l No , TWI-2000 , Serie s 2

Typ e ' Rotar yKil n Dat e o fManufactur e 138 9 Dimension s Primar yChambe r Secondar yChambe r Externa l Lengt h 35 ' Externa ? Diamete r B'8 " ID'S " interna l Diamete r 

### T 9 ' ! i " i Cross-sectiona l are a . 3 8 squar e fee t 6 4 squar e fee t 1

Burner s ! Primar yChambe rBurne r Secondar yChambe rBurne r Manufacture ri

j Nort h America n Tran e Therma l 3 iz e 12. 0 Millio n Btu/h r 3 0 Millio n Btu/h r Fue l Natura l Ga s Natura i Ga s Prime rMove r; nduce d Draf tFa n 4,00 0 acf m @ 400* F saturated , 2 0 in , wate rcolum n

2-1 2 .-abruar yiiO', 0Tabl e 2-3 Curren t AWFC O Parameter s an d Limits fo rIncinerato rMo . 4
Syste m (rJev(n e Unit s Cutof fLimit s | Calihratjo n | Fr4(|Utiic y
PrmaryCoT.bus[ : a n Chambe rTDnipuratur e • Pyrgrete r T ^ 1.2^ C (cre-minute av &-age)' . =3,4na [nsiamaneiius) 3 i | Ar.-,uall y i
LSscnndar

yOcrnhusiio i Chir rb=rTurnperaLr e ; lyp s K ;'hsrrn«5oupl & T S1.S2 E (i-.e-minute average ) * •=1 .BB H (HRA' ) su,« a fnitoi'laneons) 1 : .Am.'jsll y
Hr.mnr yCo-.busiio n Charnba rmeasure Freisur o transifiifee r i n w.c . £arrcsstierl c (lnst a nlaneous ; Ouan &'v ii'jcciiidu.ry' CombJsUo TChambe rpressure Pres s uroVansnite r in . w.c . = : atncsslierl : (Instorrteneous; . Oua -lfi' v SprayDiyu : Adsoibo i lillc ' I'eiiipfjrHli.ra Typ e KThermjrjOtlpl e 2l23J(aii u i-huteav[i , age?;>' ; Ar:;lu3ll / SprayDr/= rArisnrbs r0 JfelTe-npO'aty * T'/pp- KThe—occ\jp!-. i a £K > inn s rnhute average; 2
•M3 4 ( I iRA ) Anr.uall / Tota l Pi ;.T :;iabl e Watt e FBodra b Mas s He wmeter/scaJe S pcc->22S a (H?A i scc->iM 8 ;i -i7v

y Annuall y •Trjia l Wast e FEse'rar

e MaR= i rtrjwmeter/scalu y •Ibi'h - H-i.aa a ;H=IA. I Annjallvi ' Q jsfcry I .V M rgiwrat a flowmetEr/acale a lb.t r Pimpabl s •»4( ' Tula l - > 5 0 An n jallv ' Q-jHrtfiri y •SVM rssoral a Mass ' Ha wmeosr /acBle s Ib.'hr >fi^.;i^hPA ) Annialiy ' Q-jsrrerl y Mersjr yFeedrara Mas a tewmtiur.'scale s lb/h r *D.C2 3 (1 2 I IRA ) ArinuallVj ' Q jaiiar y : Ohbrln e '-''eeclrat

e : Mas s hsv / mewr/scaia s Ibft r >2£ 2 f' 2 HRA) AnmtalMQuarer V Aa: , Futfljfa'j ; Mas s Do wmecsr.'scale E Ib/r r Anruallyi'QuarSirljf 1 IWh r *S.2-fMSA > •uaitu.-. v •Csrbcc i Iniscfc n Svisici n Maximu m 1 ciivP-assart ; . PrassJi u awlti h in . v.x . * 1 •uaitu.-. Carbo n hiec"io* l SvH 'ernMir.irrjrr . .Hifl h Pressor s Prp.aa.Jr a Switc h psi g Ouarte-'y . COfiibL^llc-r i Sa s flo wRat e Aiuha r acf r Ar-nuall y Sloc KGa s F

MJOSB Oxyge n Zirconiu m (Mtf efua i sol i % 5 J (an a minute averaga) ' Quarter ^ j Stscl rcarto n monoxid e i j Infra i ie

d ppm v (HRA ;

s£t; o minut

e a'rtra^s.) 2 Qi ^arterli ' Slsck Hydrwarbn n . ; FI D ppm v a 1 D fcrra minut e average^ ' QL 'arteri y Slac < ga. 5 cwastv WKt e Ligh t % [cr.a minut e Ei ^rage) 3 O ^artfiri v £tsn < hyttroger : chlorida ? 1 pprr. v iai /MRA) 2

=:S» M (ori s n^'i-De average) 2 ••jarterty Licu d fegdratn Mas s He wmete r Annuall y Maa E Bo winous r fa'h r s 1.1 30 1 Annutli y Ufumme d snr l Bui * Salid s F=adr£l e Seal s lafh r C.:jarteri y Fabri c fife' pfotaur a dro p Delta P ira.-3tritte r• I n w.c . i. 2

cr> to fon e •ninijt

e average/ 2 Quart o rl v Min . Sorbin ; Fgedmt e DEr.3 % Transduce r \hl.b C! v <1.01 Min . Carrie. ' Flui d Flowfai a Flowmete r gsvl b Cl 2 •=1 .B 1 Annuallv'
1 HKA . mssn s 'hQur' yrolling avsrago ' a s calculat e byaveragin g Hi e prevfcu s S

O ane-mlri'jl a averag e values . 1 Thi s v s a RCR Apermi t :i,ml t Dnli '

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### TAG ;

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### TKPO T V&LFJ E 

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Comments .

Performe d by:* . Date : Time ; J B Place : ^"""^ ^ _ CM.SHEET.WT J B . AFieltpor Shop)

### LOOP :

DESCF.IPON : SERVICE : LOCATION : LP-SHT: ' P&ID : 303 1 REMARK S r INSTL-RMKS : SPEC-RMKS : S/J5T : TVi T mSTRUMEN T CALIBRATIO NRECOR D UNI T # 2 QUARTERL Y 21 0 WEIGH T TRANSMITTE R SOLI D CHAR GCORV . MMTOFACT : TOLED O MODT3L : 814 0 SCALE : 0-40 0 # CALIB-Itf:.0-40 0 # CALIB-OUT : 4-2 0 MAD C PROCESS-SP : 0#=81 9 et a lUST-SP : 2 0D#-24S 7 fits ACTION" : 1#-8.1 9 ctf j I/ O MJHBEE : 3007 0 CALIBRATIO NNOTE S Chec k scale , digita l Calibration , per . Toled o instructions . The n wit hn o weigh t o n scal e adjus t analo g zero . (MOTE : HM i wil l no t displa ynumber s les s than , zero ) r

### Kex t ad d weigh t = t o 10 % ar e mor e o f scale s range , then , adjus t analo g span ; t o indicat e weigh t onscale , a s rea d o n HM I screen . Se e Manufacture s literatur e £o r detaile dinstructions . Pil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T 

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Comments :
b y .^^ Tj^jj ^ Date =/d-/^0 ? Time : 7J)^ AM7 S Perforate d JB 

### CALSHBET.WD B Place : QFlelS^or Shop)

### TA G

LOO P DHSCRIPO M SERVIC E LOCATIO N LP-SH T P&I D REMARK S INSTL-RKK S SPEC-RMK S S/H . TW I rjtKSTJtUMEHT CALIBRATIO NRKCOK D OWI T # 2 QUAJiTEKL Y PD T 2 S 0 

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# IT
CALIBRATIO NSOUP.CZ REFERENC E

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### Performe d by : J B CSLSHSET.WD 3 Place : 'Held oj r Shop)

### TAG ;

LOOP ; ' DESCRIKM : SERVICS : LOCATION : LP-SHT : P&ID : REMARKS ; INSTL-EMK 3 t SPEC-RMKS :

S/UT ; 

### TH I INSTRUMEN T CALIBRATIO NRECOR D UH± T # 2 QUARTERL Y P T 20 0 PRESSUR E TRANSMITTE R LOWCHAMBE R FIEL D 203 2 MANTUFACT MODE L ' SCAL E CALIB-I N CALIB-OU T PROCESS-S P USST-S P ACTIQK f I/O.NUMBE R -7. 5 t o +2. 5 in . wc ,

4-2 0 M A

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Se e Manufacture s literatur e fo r detaile dinstruction s Pil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T J.fcifUT 'VALUEINSTRUMEN T READIN G -t f 

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### CALIBRATIO NSOURC E REFERENC E

Comments: '

Performe d by : J B CALSHEET.vTO B . Date •J0-22'0 C 

### j Time : 'Z-OO

AMfP M 

### Place : (Field os^Shopy

### ' TW 1 INSTRUMEN T (^ALTERATIO NRECCE D UNI T # 2 QUARTERL Y TAG: 

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Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READ1K G

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### CALIBRATIO NSOURC E REFERENC E

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### Performe d b y J H CALSHEET.TO B _Date : fo-ZZ'D^ Time : Z'fT

AMfpw L Place : fFiel doifSlxopf

### TpJ I INSTRTJMKNT CfiLTBEATIOI T RECOR D

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0-25 % 0-25 % 4-2 0 MAD C

CALIBRATIO NIK3TE S Flo wcalibratio nga s a t 2- 3 psi g an d 3 scf h

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### ^ q Afte r Calibration ^

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. CALIBRATIO NSOURC E REFERENC E ZER O GA S CY L #: ' CCilf.TS S 

### SPA NGA S CY L #: _
Comments :

Performe d b y J B CALSHEST.WD B 3Date:Mri^ l Time : /( I !op/$)

P M 

### Place : ^ — 

### or Shop}

### TW I ItfSTKDMEH T CALIQEBTTOK r RECOR D UNI T # 2 QTMRTERL X TAG : A T LOOP : 28S B • DESCRIPOW : H C MANOEACT : Therm o E.lec.co , SERVICE : STAC K GA S ANALYZE R MODEL : SI C LOCATION ; STAC K SCALE : 0-10 0 PP M LP-SHT : 55 6 CALIB-Ilf : PfilD : CALIB-OUT : 4-2 0 MSE C REMARKS : PROCil S S - S P : 12JSTL-KMKS : . INST-SP : SPEC-KMKS : 'ACTIOS : S/H : 63 0 O n MC S 10 0 I/ O UuMBER: ' CA L IBRATlOl f NOTE S 1 ) Ope n sampl e ga s bottl e valves . 2 } Pres s MENUButto n 3 ) Pres s CALIBRATIO N 4 } Pres s ZERO.ADJUS T 5 } Pres s SPA H ADJUS T a£te r 4)finishe d 6 ) Pres s RU Nafte r 5)finishe d 7 ) Clos e sampl e ga s bottles . Se e Manufacture s literatur e fo r detaile dinstructions . ' Fil l ou t an d affi xa ne wcalibratio nsticker . D. l lb/hr . CALIBRATIO NREPOR T INPU T • VALU E INSTRUMENT . • READIN G• • •

q Before Ca.libjrs.tion


### Afte r Calibratio n

CALIBRATIO NSOURC E REFERENC E GA S CY L # :

Cotnments: '

Performe d Date : Tim e : ° ' ^ f AM ) P M J B • Place: : CA L SHEET . WDB ((Field hr Shop)

### TW T INSTRUMEN T CALIBRATIO NRECOR D

um.T #2 - 

### QUARTERL Y TAG : A T LOOP : 2SB B • • DESCRIPOH : OPACIT Y SERVICE : STAC K GAS LOCATION : STAC K LP-SET : P&E D : REMARKS' : IBfSTL-RMKS : 'SPBC-RMKS : 2.QG t o 5 .70ma

S/H : MAMT F ACT : TELEDYN E INST . MODEL : -LightHaw k 5 6 OD I SCALE : 0-100 % CALEB-IN ; CALIB-OUT : 4-2 0 MAD C PROCESS-SP : INST-SP : ACTION : I/ O SOMBER : CALIBRATIO NNOTE S Clea nwindow s

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After Calibratio n

CALIBRATIO NSOURC E REFERENC E

Comment s

Performe d by : 

# C-Wc k J±dw&.(£$S



### Date : iCh^-O^ 

### Time : iTB CALSHEET.WD B Place: . fiel dTp r Shop)

### TN I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 2 ANNUA L TAG : T T LOOP : 20D A DESCRIPOJJ : PL C THERMOCOUPL E INPU T SERVICE : LOWE R CHAMBE R

FIEL D LOCATION ; LP-SHT : P&ID : REMARKS ; INSTL-RMKS : SPEC-RMKS : S/N : 203 2 

### MAM)E T 

### ACT ; MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-8P : ACTION : I/ O NUMBER : MODICO N

B883-20 0 0-250 0 deg . F , TYP E K

Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 5 0 0 de g F . an d 2,00 0 deg.F . a t inpu t o f PLC , the nverif ythi s singl e o n th e contro l pane l CRT .
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### CALIBRATIO NSOURC E REFERENC E

Commen t s : )U o Calibrato r neeta^of .

Performe d by ; I ^ V -T , f>*JX 0 Date : //-/fl-ff i Time : 2jZS ^,(g) , J B Place : CALSHEET.Wff i [Field hr Shoo}

### TH I INSTRTMKN T CALIBRATIO N RECOR D UNI T # 2 ANNUAL TAG : T T LOOP : 200 B • DESCRIPON : PL C THERMOCOUPL E INPU T MAITOFACT : MODICO N SERVICE : LOWE R CHAMBE R MOLEL : B883-200 . LOCATION : FIELl i SCALE : 0-250 0 deg . F . LP-SHT : CALIB-IN : TYP E K P&ID : 203 2 CALIB-OUT : REMARKS : PROCESS-SP : INSTL-EMKS : IHST-SP : SPEC-RMKS : • ACTION : S/N : I / O HOMSER : Cf l LIBERATIO NNOTE S Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 da g F . an d 2,00 0 deg.P . a t inpu t o f PLC , the n -verif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa newcalibratio nsticker . 0.1- lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READINO . r~y-\,-\& 

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CALIBRATIO NSOURC E REFERENC E

Comment s

Performe d by: . Date: . _A M /P MJ

. 

### J B Place : CALSHEET.WD B ( (Field) Or Shop)

### TAG :

LOOP ; ' DESCKJPOKf : SERVICE? : LOCATION : LP-SHT : P&I D : REMARKS : IttfSTL-RMK S : • SPEC-RMKS : 3/N : TW I INSXRUWEH T CALIBRATIO NRECOR D UNI T # 2 ANNUA L T T 219 A PL C THERMOCOUPL E INPU T UPPE R CHAMBE R FIEL D 203 3 

### MANUPACT : MODICO N MODEL : SCALE : 0-250 0 deg . CALIB-IN : TYP E K CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : P .

CALIBRATIO NNOTE S Us e cold , junctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g P . an d 2,00 0 deg.F . a t inpu t o f PLC , the nverif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALUEINSTRUMEN T READIN G•

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### CALIBRATIO NSOURC E REFERENC E

Comments : L i o coL\\htaAi9f\ needed,

Performe d by: . DateTims : J B Place : CALSHEET.HD B <(Field)or Shop)

### TAG :

LOOP : • ' DESCRIPON : SERVICE : LOCATION ; LP-SHT : P&I D : REMARKS : IBFHTL-RHKS : SPEC-RMKS : S/H : T B I INSTRUMEN T CALIBRATIO NRECOR D USU T # 2 ANNUA L T T 21S B PL C THERMOCOUPL E INPU T MANUFACT : MODICO N UPPE R CHAMBE R FIEL D 203 3 MANUFAC T MODE L SCAL E CALl'B
- II ? CALIB-OU T PROCESSES ? LNST-S P ACTlOlf ; I/ O NUMBER : 0-250 0 deg ,

TYP E K

CALIBRATTO NNOTE S Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a'typ e K

temperatur e signa l o f 50 0 <3e g F . an d 2,00 0 deg.F . a t inpu t o f PLC , the nverif ythi s singl e o n th e contro l pane l CRT ,
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READIN G

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CALIBRATIO NSOURC E REFERENC E

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### Performe d J B 

### CALSHEET.HD B Plac e r . fFieldSor Shop)n

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TYP E K

CALIBRATIO NNOTE S U s e col djunctiorj , compensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g P . an d 2,00 0 ' deg.F . a t inpu t o f PLC , the nverif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker , 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E 

# SOQ°f 

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CALIBRATIO NSOURC E REFERENC E

Comments : KinCo 11 i o Vo^to v\ needed,

yl/Jsis 

### Date : Time : Performed.b y J B CALSHEBT.WD B Place ;

### TAG :

LOOP ; DESCRIPOH : SERVICE : LOCATION ; LP-SH T P£I D REMARK S INSTL-RMK S SPEC-RMK S S/ N TW I IHSTRUMEN T CALIBRATIO NRECQP. U UNI T # 2 ANNUA L T T 27 0 PL C THERMOCOUPL E INPU T MANUFACT : MODICO N SD AOUTLE T FIEL D 203 4 MANUFAC T MODE L SCAL E CALIB-I K CALIB-OU T PROCESS-S P INST-S P ACTIO N I/ O NUMBE R 0-2S0 0 deg . F ,

TYP E K

Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g F . an d 2,00 0 deg.F , a t inpu t o f PLC , the n verif ythi s singl e o n th e contro l pane l CRT .
Se a Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affix- a ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO N REPOR T 

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# ^DO^

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### CALIBRATIO NSOURC E REFERENC E

Comment s

Performe d bv : 

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# ^^~-J ^9

Date : 

# ff-fd-O^j Time : 

# "2J

3S^fpM ^ J B Place : CALSBEET. WD B (fFieldjor Shop}

### TAG :

LOOP : ' DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID r REMARKS : INSTL-SMKS : SP2C-RMKS : S/N : TW. T n^TRl^EN T CALIBRATIO NRECOR D UNI T # 2 ANNUA L E T STAC K FLC WTRANSMITTE R STAC K FIEL D 203 5 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT: ' PROCESS-SP : INST-SP : ACTIOU ; I/ O NUMBER : Rosemoun t

Q-?.u,0O

D ACF M 4-2 0 MAL C S e t Damp/po t t o mi d poin t
CALIBRATIO NNOTE S US E PNEUMATI C CALIBRATIO NBENC H WIT H INCLIN E MANOMETE R MD LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/b r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T REABIN G 

# Q if . , .. . Before

Calibration

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### • r^tr Afte r Calibratio n, . „ , 

# D HO *A

CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : Data : Time : iTB Place : ^^^^"x . 

### CAL S HEET . VfDB /^ieldjs r Shop)

### TAG :

LOOP : DESCR.IPON ; SERVICE : LOCATION ; LP-SET : P&ID : REMARKS : INSTL-EMKS : SPEC-HMK S : S/N : TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 2 ANNUA L Jj' T 21 5 PLO W TRANSMITTE R HIG H BT U FL D 203 1 Change d Rang e 11/12/9 6 SENSITIVIT Y5.5 8 S W 1,2,3,4 , OF F 9715 3 • MANUFACT : MODEL : SCALE : CALIB-LM : CALIB-OUT : PROCESS-SP : INST-SP : .ACTION : I/ O NUMBER : MICR O MOTIO N

D 40S-S S 0-360 Q lb/h r 4-2 0 MAD C

CALIBRATIO NNOTE S Flus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter , se t contro l syste m t o appropriat e rat s control f 

### an d rea dtotalizer , flo wwate r int o a containe r an d compar e t h e toltalize r readin g t o th e measure d amoun t i n container .
Se e Manufacture s literatur e fo r detaile dinstructions , Fil l ou t an d affix : a ne wcalibratio nsticker . 0. 1 lb/h r • CALIBRATIO NREPOR T INDTJ T VALUEINSTRUMEN T READIN G i / \ .) , o Before Calibration

Q

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After Calibration



### CALIBRATIO NSOURC E RE-FBRSNCE Comments : 

# IV)f

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### Performe d b y JB 

### CALSHBET.WD B _pate : H-l^-O*} 

### Time:_^3 d mfw? 

### Plac e '{Fieldjor Shop)

### TAG ;

LOOP : •' BEISCRIPOW : SERVICE : LOCATION : LP-BST i ' P&IO : REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : TW I INSTRUMENT ' CALIBRATIO NRECOR D UNI T # 2 ANNUA L F T 21 6 FLOW TRANSMITTE R LO WBT U FL D 203 1 Change d Rang e 11/12/9 6 SENSITIVIT Y5.1( 5 S W 1,3,4 , OF F 3293 6 MANUFACT : MICR O MOTIO N MODEL ; D 40S-S S SCALE : 0-360 0 lb/h r CALIB-IN : 4-2 0 MAD C CALIB-OUT : PROCESS-SP : INST-SP : ACTION ; I/ O NUMBER ; CA L IBRATIO NNOTE S Plus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter , se t control
- syste mt o appropriat e rat e control , a n d rea dtotalizer , flo wttater int o a containe r an d compar e t h e tolcalipe r readin g t o th e measure d amoun t i n container ,
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa newcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALUEII^-TE ^3J (ffiNT----SEA0IN: G
, p

### Befor e Calibration 0\

a j i f H) Jfas , ^a r\nr f ^]n . I • / I \b s . 

### After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments : 

## hlo r/> l\Lr&i^ fivedecfPerforme d by : Date : IZ-I^-Q^ ? Time : ZGO AM J B Place : CALSHEET„WD B ({Field)or Shop)

### TB I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 2 ANNUAL TAG : F T LOOP : 28 8 • DESCRIPON : FLOW SERVICE : LIM E LOCATION : FIEL D LP-SET : P&.TJD : 203 4 REMARKS : INSTL-RMKS : SPEC-RM S : S/N : TRANSMITTE R

SLURR Y T O HEAD TAN K •MANDEAC T MODE L SCAL E CALIE-I N CALLS-OU T PROCESS-S P INST-S P ACTIO N I/ O NUMBE R E- H

0-2 0 GP M 4-2 0 MAD C

CALIBRATIO NNOTE S Flus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter . Se t contro l syste mt o appropriat e contro l rate , a n d rea dtotalizer , flo wwate r int o a containe r an d compar e t h e toltaliee r readin g t o th e measure d amoun t i n container .
Se e Manufacture s literatur e fo r detaile dinstructions , Fil l ou t an d affi xa ne wcalibratio nsticker . 0, 1 lb/h r > CALIBRATIO NREPOR T INPU T VALUEINSTRUMEN T READIN G i ^— r e ^ Before Calibration

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After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by: . 

# h^C.&j

Qj2)

Date; jHfi l TimeJ- ^ 

# TMf&) J " B Place:„ _ CALSHEET.WD B (Fiel dlo r Shop)MM J<?dm* d C t - S t Lncfe , M O S^T2 5 tiuiJiieas: {3

1 i) a 45-777 3 . Hax : {314 ) aiS-?/7 9 Seal s Inspectio n Repor t (JirstMBi - ONY XENVIRONMENTA L

# 7 MOBIL E AVENU E SAUGET , I L6220 1 Location : Direc tinjectio n MF03-/ Mfjaol ; WH3 0 ScaieTypc : VEHICi.F
. Capacity ; 6pnDU"LB ascription ; Glas s H I L Seria l No ; 01115 0 Seal s No : 2 Divisions : 5L 3 • Scal e Wa s torrid il l Tolerance : Xye s Shif tlost Slffe s / Comsr s / Weights

Apple d Scal u Readin g

(A s found) Ejro r(+/- ) Tcferanc

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s Uff) ' Amept, 1 Rejec t Sectipr - 1 21,00 0 li ) 4 0 l b 4 / - 4 5 l b ACCEP T

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### I D ACCEP T IB , 

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i b lfl,00 G lb +0 l b +/- 4a Oh ACCIsP ? ElEctioi i 4 IX, CQD l b 21 , OQ S l b 4 5 

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T€StPrL>cEdUTefollcnvsQ5POO9-O0l/0D Z NIST# ; MO : 235833/2532.5 0 3958 B OB5rj4-02SB/D34)45 0 2749S 9 Rfc e Lake : 622/266926^0 2 822/272331-0. 5 322/274031-0 6 _ „ /
.

CalDate : 11/09/200 3 NextOMdya : 9 0 Days Servic e Technicia n Registratio n # : 0524- M

. Calibrate d B yS&rvlc a TschnEcian : Ji m Koejkenmeie r Calibratio n Dates : JA N AP R JU LOc t Jo b Qjj&ueS : LT21765 1 Ropcr tID : SflB333S S

Uncertaint yo fMeasurcman tprovide d o n request FQ R CUSTOME R US E ONLY t

. Reviewe d By . . Dal e Reviewed , „



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1 WEEKL YUNIT# 2 COMPLIANC E CHEC KSHEE T (CMSTas k IC4D39) RAGt £1 O H 2
OPERATIN G PARAMETER S P L C COI L B WCOI L

' 1 OC L' TR VPOSITIO N (OPEN ) 0160 2 0040 1 2 OC L UPPE R CHAMBE R TEMP . 1 mi n avrj . 0040 2 3 OC L H I BT U lbs/h rMa x 0161) 4 0040 3 4 OC L LOWE R CHAMBE R TEMP . 1 itii n avg . 0160 5 0040 4 S OC L L O BT U lbs/h rMa x 01SD 6 0040 5 

## e OC L. FLU E GA S HCL , 1 hr . rollin g avg . 016D 7 0040 6 7 ' OCI
. FLU E GA S CO , 1 hr , rollin g avg . 0160 0 0040 7 a OC L FLU E GA S OPACITY , high."fo r4S D swc./hr
. avg . 0160 9 004O 6 9 OC L FLU E GA S OPACITY , hig h instantaneou s 01B1 0 0040 8 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min . av g 01B1 1 0041 0 1 1 OC L HEA TINPU Thig h mbiu/ri r 0 1 E l 3 0041 1 1 2 OC L CHLORIN E INPUT , hig h lbs/h r 0101 4 0041 2 1- 3 OC L SOLI O FEED , hig h lbs/h rMax . 0152 6 0041 3 1 4 OC L UPPE R CHAMBE R TEMP - lo w1 h rrollin g avg . 0153 8 0041 4 1 5 OC L SPECIALIT YFEEDE O hig h lbs/h rMax . 0151 S 0041 5 1 7 AWF C SDA-OUTLET'i'HMF
. high l min , avg . 0159 1 0041 7 1 8 AWF C B A G HOUS E DIFT.PR . DROP
. Lo w1 min . avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min . avg . 0159 4 0041 S 20 AWF C FLUE . GA S 02 , lo w1 min . avg . 0159 6 0042 0 21 AWF C FLUE . GA S HC , hig h 1 min . avg . 0159 7 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min . avg . 0159 S 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h tost. 0159 9 DD42 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min , avg . 0150 1 0042 4 % . i "AWFC " '' ' LO W'CHAJTOTSRTElVfP'. Vlow ' 1 ' t i r' / g vg , 01586'."' " •00425 '

. ) AWF C LOWE R CHANCE R P RESS , hig h fo r5 sees . 0158 3 0042 6 AWF C UPPE R CHAMBE R PRESS , hig h for 5 sees . 0156 9 0042 7 

## z e AWF C FASLE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min . 0162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h OfSO O 0043 0 3 2 MWF C A L LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 0 0043 2 3 5 MWF C . FLU E GA S HCL , hig h 1 mid , avg . 0159 2 0043 5 3 6 MWF C HEA TINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h lbs/h r 0162 3 0043 7 3 8 MWF C . E-STOP S o rT/ C MODUL E inactiv e 0161 5 0043 3 3 9 MWF C FLU E GA S CO , hig h 1 hr . avg . 0159 5 0043 9 4 0 MWF C ATOMIZE R hig h hig h vibratio n for 5 sec . 0162 4 0044 0 4 1 •SWF C SPEC
. FEE D lbs/h rhig h 0157 6 0044 1 PAS S y y 1ZL

y . y



### ZZ1

y ,

* y

y' BIWEEKL YUNIT# 2

COMPLIANC E C fIFC KSHEE T {CM S Tas k JC403G ) PAG E 2 O F 2
OPERATIN G PARAMETER S PL C COI LBWCG1 L PAS S FAI L 4 2 SWF C HJBT U Ibs/hrriigri
. 0157 8 0044 2 4 3 SWF C LOm u \b$!hr hig h 0158 0 0044 3 4 0 SWF C H I BT U los s o fsryna l 0301 9 OQ44 5 4 6 SWF C LOBT U los s o fsigna l 0302 0 0044 6 4 7 SWF C SPECIALIT YFEED/COMPRESSE D GA S FEE D Eos s o fsigna l 0302 1 0044 7 4 5 MWF C NORT H £SOUT H IP S ALARM S FAILE D 0570 3 0044 S 49 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 0302 2 0044 0 5 0 MWF C NORT H & SOUT H IP S SERVER5FAILE D C570 S OO45 0 5 1 SWF C DIREC TINJEC T(commo n alarm ) 0313 2 004S 1 5 2 OP L Ba g Lea k Detectio n Syste m (THbo ) '6 5 • P L Pumpabl e 1 Hou rRollin g Tota l OP L 0620 5 0411 3 e e OP L Non-Pumpabl e 1 Hou rRollin g Tota l OP L ceao s 0411 4 6 7 OPL
. Tota l wa.s£ e 1 Hou rRollin g Tote ! OP L 0820 8 0411 5 6 3 O P L CL1 2 Hou rRoKfn g Tota l OP L 0B21 1 0411 6 6 0 OP L Lo wVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 7 0 OP L Sem i Volatil e 1 2 Hou rRollin g Tota i OP L 0821 6 0411f t 7 1 OP L Mercur y1 2 Hou rRoilin g Tota i OP L 0321 6 0411 0 7 2 OP L A s h 1 2 Hou rRoilin g Tota i OP L OS22 0 0412 0 7 3 O P L P C C Temperatur e 1 Hou rRolling 1 Averag e Lo wOP L 0822 2 0412 1 7 4 OP L S C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0B22 4 0412 2 7 5 OP L SD AOutle tTemperatur e 1 Hou rRoilin g Averag e Hig h OP L 0922 6 0412 3 7 6 O P L Baghous e DrfFerenlia l Pressur e 1 Minut e Averag e Lo wOP L 0822 7 0412 4 7 7 O P L Baghous e DfffensriUa l Pressur e 1 Minut e Averag e Hig h OP L 0822 6 0412 5 •;-' f v " 'OP L S facR ' HCT
. Cofrecto'fl' T'Hou rRollin g 'Averag e 'Hig h OP L •-0823 2 0412 5 • O P L Stac k

C O Correcte d 1 Hou rRoilin g Averag e Hig h OP L 0S23 6 0412 7 s o OP L Stac k Flo w1 Hou rRollin g Averag e Hig h OP L 0824 4 0412 S S 1 O P L BT U 1 Hou rTota l OP L 0820 9 0412 9 8 2 O P L HrtCI/Hr a Lim e Flo w1 Minut e Averag e Hig h OP L 0825 1 0413 0 6 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0815 6 0413 2 6 4 WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTU/ChlARG E 8 5 Hi/D ! Atomtang ' flit Lo wpressur e alar m (Manua l Check ) B S Lo/D ! Atomizin g Af rLo wpressur e alar m (Manua l Check ) 8 7 Specialt yFeede rAtomizin g Ai rLo wPressur e alar m (Manua l check ) OC L -CONDFTiO N LIMI T AWF C ' -AUTOMATI C WAST E FEE D CUTOF F MWF C =MlS C WAST E FEE D CUTOF F SWF C ^SPECIFI C WAST E FEE D CUTOF F 

# 5 77 " 

## 7 ^

y .

^ 1

y y

Comment s

CHECKE D BY : ""TTj ^ .^PROVED : j/fajLor
. ££KLY_ 2 4/4/0 7 H K DATE : }0-1 y^- O 1 TIM E : PLACE : Contro l Roo m A M tP M' BIWEEKL YU N F T# 2 COMPLIANC E C J jfSC K5 ! 1EI= T •[CM S Tas k iMfflrj ) PAG E 1 O F 2
OPERATIN G PARAMETER S PL C COI LeWCOJ L i OC L T R VPOSITIO N (OPEN ) 0160 2 00 4 0 1 2 OC L UPPE R CHAMBE R TEMP . 1 mi n avg . 01K0 3 0040 2 3 OC L . H I BT U Ibs ffi rMa x 0160 4 0040 3 4 OC L LOWE R C i 1AMBERTEMP . 1 mi n avtj . 0160 5 0040 4 5 OC L L O BT U ibs/h rMa x 0160 6 0040 5 6 OC L , FLU E GA S HCL , 1 hr . rolling avg . 0160 7 0040 6 7 OC L FLU E GA S CO , 1 hr . rolling gvg . 0160 8 0040 7 8 OC L FLU E OA S OPACITY , hig h fcr4S0 sec./hr
. avg . 0160 9 D04D 8 •9- O C L FLU E GA S OPACITY , hig h instantaneou s 01G1 0 0040 9 1 0 O C L FLU E GA S FLO WRATE , hig h 1 min . av g 0161 1 0041 0 1 1 OC L HEA TINPU Thig h mbtu/h r 0161 3 0041 1 1 2 OC L CHLORIN H INPUT , hig h lbs/h r 0161 4 0041 2 1 3 O C L SOLt D FEED , hig h Ibs/h rMax , 0152 6 •0041 3 1 4 O C L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 6 0041 4 1 5 OC L SPECIALIT YFEEDE D hig h lbs/h rMax . 0151 6 0041 5 1 7 AWF C SDA-OUTLE TTEMP , high l min . gvg . 0159 1 0Q41 7 1 B AWF C B A G HOUS E DIFF.PR . DROP
. Lo w1 min . avg . 0159 3 0041 3 1 9 AWF C FLU E GA S CO rhig h 1 min , avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min . avg . G15S 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min . avg . D159 7 . 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min . airg . 0159 6 G042 2 2 3 AWF C FLU E GA S FLOWRATE , hig h irist . 0159 9 0D42 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min , aivg. 0160 1 0042 4 ..AWFC-. - 01-56 S 0042 5 • • ..AWFC-. - AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . •0153 8 0042 6 _7 - AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 0153 9 D042 7 2 5 AWF C FAfLE R O F PROCES S MONITO R 0152 7 0042 6 2 9 AWF C ( D FA N FAfLUR E a rhig h hig h vibratio n fo r6 min . D162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 0043 0 3 2 •MWF C A L LWAST E FTiF O OF F FRO M FI X{trtanuaH ysho toff ) O174 0 0043 2 3 5 MWF C FLU E GA S HCL , hig h 1 min . avg . 0159 2 0043 5 3 6 MWF C HEA TINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h lbs/h r 0162 3 0043 7 38 MWF C E-STOP S o rTIC MODUL E iracSv e 0161 5 •0043 8 3 9 MWF C FLU E GA S CO , hig h 1 hr.avg . 0159 5 0043 9 4 0 MWF C ATOMIZE R hig h hig h vibratio n for 5 se t 0162 4 0044 0 4 1 SWF C SPEC
. FEE D ibs/h rhig h 0157 6 0044 1 PAS S 

# y 

# i

/ /



# -± 1 T 

### z 

# J_ 

# iBIWEEKL YUNIT1K 2 (CM S Tas k !C4Q39 ) PAC E 2 O F 2 COMPLIANC E CHEC KS I iEF T y OPERATIN G PARAMETER S P L C COI L 0 WCOI L PAS S 4 2 SWF C HIBT J rbs/brhig h 0157 8 0044 2 4 3 SWF C LOBT U lbs/h rhig h 0158 0 0044 3 I - 4 5 SWF C H I BT U los s o fsigna l 0301 9 0044 5 

# J 4 6 SWF C LOBT U ios s o fsign a l 0302 0 0044 6 

## 7 . 4 7 SWF C SPECfALFT YFEED/COMPRESSE D GA S FEE D los s o fsigna l 0302 1 0O44 7 

# :/ 4 3 MWF C NORT H &SOUT H IP S ALARM S FAILE D 0570 3 0044 8 h 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 0302 2 0044 9 J5 0 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 5 1 SWF C DIREC TINJEC T(commo n alarm ) 0313 2 •0045 1 5 2 OP L Ba g Lea k Detectio n Syste m (Tribo ) 6 5 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3


## . / 6 6 OP L Non-Fumpabl a 1 Hou rRollin g Tota i OP L 0520 0 0411 4 j •6 7 OP L Tota i wast e 1 Hou rRollin g Tota l OP L 0B2O B 0411 5 

### / •G 8 OP L C L1 2 Hou rRoilin g Tota l OP L 0821 1 0411 6 G 9 OP L Lo wVolatil e 1 2 Hou rRollin g Tota i OP L 0821 4 0411 7 J 7 0 OP L Sem i Volatil e 1 2 Hou rRoilin g Tola i OP L 0821 6 0411 8 1 7 1 OP L Mercur y1 2 Hou rRollin g Tota i OP L 0B21 6 0411 9 

# J 7 2 OP L A s h 1 2 Hou rRollin g Tota l OP L 0622 0 0412 0 J 7 3 OP L P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0822 2 0412 1 

### / 7 4 OP L S C C Temperatur e 1 Hou rRoilin g Averag e Lo wOP L 0822 4 0412 2 

### ./ : 7 5 OP L S D AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L 0622 S ' 0412 3 j 7 6 OP L Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOP L 0622 7 0412 4 

## /
. . 7 7 OP L Baghous e Differsrrfia fPressur e 1 Minut e Averag e Hig h OP L •0622 8 0-112 5 O P L Stac k

HC LCorrecte d 1 Hou rRollin g Averag e Hig h OP L 0823 2 0412 6 

### ••: O P L Stac k C O Correcte d 1 Hou rRollin g Averag e Hig h OP L 03230 ' 0412 / 8 0 O P L Stac k Flo w1 Hou rRoilin g Averag e Hig h OP L 0824 4 0412 3 

# J 8 1 OP L BT U 1 Hou rTota l OP L 0320 9 D412 9 

# J. 8 2 OP L Hr tCI/Hr a Lim e Flo w1 Minut e Averag e Hig h OP L 0325 1 04f3 0 

# J 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0815 6 ' 0413 2 

# / 6 4 WiL LNO TACCEP TSOLI D CHARGE S >75 0 KBTU/CHARG E 

# J 8 5 Hi/D i Atomizin g Ai rLo wpressur e alar m (Manua l Check ) j . e e Lo/D I Atomizin g Ai rLo wpressur e afant i (Manua l Check ) 

## / 6 7 Specialt yFeede rAtomizin g Ai rLo wPressur e alar m (Manua fcheck ) 

### / OC L =CONDFT10 N LIMI T AWF C ^AUTOMATI C WAST E FEE D CUTOF F MWF C =M!S C WAST E FEE D CUTOF F SWF C ^SPECIFI C WAST E FEE D CUTOF F

Comment s

CHECKE D BY : j/ \ U

I$A APPROVED : /$b@hz & DATE ; /\9 - /O -0 ? TIM E ; /(P

: > , £> A M (fy ? PLACE : Contro ! Roo m ; cEKLY_ 2 4/4/0 7 H KRIVVFFKL YuNrn e

COMPLIANC E CHEC KSHEE T (CM S Tas k 104039 ) PAC E 1 O F 2
OPERATIN G PARAMETER S P L C COI L B WCOI L 1 OC L m

v POSITIO N (OPEN ) 0160 2 0040 1 2 CCI
. UPPLi R CHAMBERTtWP- 1 mi n avg . 0100 3 0040 2 3 . O C L H I UT U Ibs/h rMa x 01B0 4 0040 3 4 OC L LOWE R CHAMBE R TEMP , 1 mi n avg . 0160 5 0040 4

. 5 OC L L O BT U lbs/h rMa x 0160 8 OO40 5 6 OC L FLU E GA S HCL , 1 hr . rollin g avg . 0160 7 0040 6 7 O C L FLU E GA S CO , 1 hr . rollin g avg . 0160 3 0040 7 8 O C L FLU E GA S OPACITY , hig h fo r46 0 sec./hr
. avg . 0160 9 0040 8 0 O C L FLU E GA S OPACITY , hig h instantaneou s 01610 • 0040 8 1 0 O C L FLU E GA S FLO WHATE , hig h 1 min . av g •161 1 0041 0 1 1 O C L HEA TINPU Thig h mbfiVh r 0161 3 0041 1 1 2 O C L C H LO R IM E INPUT , hig h lbs/ 3 i r 0161 4 0041 2 1 3 O C L SOLI D FEED , hig h ibs/h rMax . 0152 6 0041 3 1 4 O C L UPPE R CHAMBE R Trr-Mp . tow 1 h rrollin g avg . 0153 5 0041 4 1 5 OC L SPECIALIT YFEEDE D hig h lbs/h rMax . 0151 6 0041 5 1 7 AWF C SDA-OUTLrHTTEMP , high l min , avg . 0159 1 0041 7 1 H AWF C BA G HOUSF J DIFF.PR . DROP
. Lo w1 min . avg . 0159 3 0041 8 i y , AWF C FLU E GA S CO , hig h 1 min . avfl
. 0159 4 00419 ' 2 0 AWF C FLU E GA S 02 , lo w1 min . avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , tiig n 1 min . av$
. 0150 7 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min . avg . 0159 8 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h irist . 0159 9 DQ42 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min . avg . 0160 1 •042 4 "\5 AWF C LO WCHAMBE R TEMP, , Lo w1 hr , avg . 015& S 0042 5 AWF C LOWE R CHAMBE R PRESS , high fo r5 sees. •0158 3 0042 6 2 7 AWF C UPPER . CHAMBE R PRESS , hig h fo r5 sees . 0156 3 0042 7 2 3 AWF C FAILE R O F PROCES S MONITO R 01.52 7 0042 8 2 S AWF C I D FA N FAILUR E o rhig h hig h vibratio n for 5 min . 0162 5 0042 9 3 D AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 0043 0 3 2 MWF C A L LWAST E FEE D OF F FRO M FI X(iiianuatl yshu toff) 0174 0 0043 2 3 5 MWF C FLU E GA S HCL , hig h 1 min , avg . 0159 2 0043 5 3 S MWF C HEA TINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h Ibs/h r 0162 3 0043 7 3 8 MWF C

_F,-STQP S orT/ C MODUL E inactiv e 0161 5 •0043 3 39 MWF C ' FLU E GA S CO , hig h 1 hr . avg . 0159 5 0043 9 AO MWF C ATOMIZE R hig h hig h vibratio n for 5 se a 0162 4 0044 0 4 1 SWF C SPEC
. FEE D lbs/h rhig h 0157 6 0044 1 PAS S

z i 

### Z . 

# ± zz 

# 5 Z
^ z 

# z z z ..\Zy»» 

# z" BJWLEKL YUNI T# 2 [CM S Tas k IC4039 ) PAG E 2 O F 2 COMPUANC^ ^

^ ; . _^

N

•"•""*' . OPERATIN G PARAMETER S P L C COI L B WCOI L PAS S "4 2 SWF C H I BT U Ibsfli rhig h 0157 S 0044 2 

## y 4 3 SWF C LOBT U lbs/h rhig h 0158 0 0044 3 

## y 4 5 SWF C HJBT U los s o fsigna l 0301 0 0D44 5 

## , y 4 6 SWF C LOBT U los s o fsigna l 030Z O 0044 6 

## y 4 7 SWF C SPECIALIT YFEED/COMPRESSE D GA S FEE D los s o fsigna i 0302 1 0044 7 4 8 MWF C NORT H & SOUT H IP S ALARM S FAILE D '0570 3 0044 8 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 0302 2 0044 9 5 0 MWF C NORT H & SOUT H IP S SEWERSFAfLE O 0570 5 0045 0 

## y 5 1 SWF C DtREC TINJEC T(commo n alarm ) 0313 2 0045 1 

## y 5 2 O P L Ba g Lea k Detectio n Syste m {Tribo } 

## ... 

## y, 0 5 O F L Ptrmnabf e 1 Hou rRaffin g Tota l OP L 0820 5 0411 3 

## / G O O P L Non-Pumpabl e 1 Hou rRailin g Tota l OP L 0820 6 0411 4 

## . y 6 7 O P L Tota l wast e 1 Hou rRollin g Tota l OP L 082O 3 0411 5 

## y 6 8 O P L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 S 

## y 6 9 O P L Lo wVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 

## y 7 0 O P L Sein i Volatil e 1 2 Hou rRailin g Tota l OP L 0B21 5 0411 8 

## ,y 7 1 OPl
. Mercur y1 2 Hou rRoilin g Tota l OP L 0&21 B 0411 9 7 2 O P L As h 1 2 Hou rRoiiin g Tota l OP L 0822 0 0412 0 7 3 O P L P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0822 2 0412 1 

## y 7 4 O P L S C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0822 4 0412 2 

## y 7 5 O P L SD AOutle t Temperatur e 1 Hou rRoilin g Averag e Hig h OP L 0322 6 0412 3 

### ^ 7 6 O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOP L 0822 7 0412 4 

## y .7 7 O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L 0822 8 0412 5 

## y % O P L Stac k

HC LCorrecte d 1 Hou rRollin g Averag e Hig h OP L 0623 2 0412 6 

## Z, I O P L Stac k

C O Correcte d 1 Hou rRoilin g Averag e Hig h OP L 0823 6 0412 7 

## y 8 0 O P L Stac k Ra w1 Hou rRollin g Averag e Hig h OPl , 0824 4 0412 3 

## y 8 1 O P L BT U 1 .HourTota l OP L 0820 9 0412 9 

## . ,y 8 2 O P L Hr

t Cl/Hra-Lim e Flo w1 Minut e Averag e Hig h OF L 0825 1 0413 0 8 3 AWF C • m e Sluir yPensif y1 Hou rRollin g Averag e LOW 0315 6 0413 2 

## y 3 4 WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTLL/CHARG E 

## y 8 5 Hi/D I Atomiiin g Ai rLo wpressur e alar m (Manua l Check ) 

## y 8 8 Lo/D I Atomizin g Ai rLo wpressur e afarr n (Manua l Check ) 8 7 Specialt yFeede rAtomizin g Ai rLo wPressur e alar m (Manua l check ) 

## y O C L ^CONDITIO N LIMF T AWF C ^AUTOMATI C WAST E FEE D CUTOF F MWF C =MIS C WAST E FEE D CUTOF F SWF C ^SPECIFI C WAST E FEE D CUTOF F

Comment s

CHECKE D BY :

# ^X^sJjPfl DCTEI /M/ H Q ? TIM E : 

# <jS > ^PROVED : j/a&/^ & PLACE : Contro l Roo m J ,cEKLY_ 2 4/4/0 7 H KBIWEEKL YUNIT* !

COMF 1 (ANC E CHEC KSH E IT T (CM S Tas k IC4039 ) J>AG E 1 OI - 2
OPERATIN G PARAMETER S P L C COI LB WCOI L 1 O C L •TR VPOSITIO N (OPFN ) 0160 2 0040 1 2 O C L UPPE R CHAMBE R T-MJP . 1 mi n avg . fj-tb'0 3 0040 2 3 O C L H tBT U lbs/h rMa x 0100 4 0040 3 4 O C L LOWE R CHAMBE R TFMP , 1 mi n avg . 0160 S G04O 4 5 O C L L O BTU lbs/h rMa x 0150 6 0U4D 5 6 O C L FLU E GA S HCL , 1 hr . rolling - avg . 0160 7 0040 6 7 O C L FLU E GA S CO , 1 hr . rollin g avg . 0160 8 O04O 7 3 O C L FLU E GA S OPACITY , hig h fo r48 0 sec./hr
. avg , 0160 9 0040 8 9 O C L FLU E GA S OPACITY , hig h instantaneou s 0161 0 004O 9 T O O C L FLU E GA S FLO WRATE , hig h 1 min . av g 0161 1 0041 0 1 1 O C L HEA TINPU Thig h mbrjj/h r 01G1 3 0041 1 1 2 O C L CHLORIN E INPUT , hig h Ibs/h r 0161 4 0041 2 .1- 3 O C L SOLI D FEED , hig h )bs/h rMax . 0152 6 0041 3 1 4 O C L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 8 0041 4 1 5 O C L SPECIAL ! F YFEE D E D hig h ibs/h rMax . 0151 6 0 W 5 1 7 AWF C SDA-OU' fLE TTEMP . iiigh Tmm . avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DiFF.PR . DROP
. Lo w1 min . avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min . avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 rle w1 min - avg . 01S9 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min . avg . 0159 7 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min . avg , •159 8 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h Ins t 0159 9 0042 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 inlrt . avg . 0160 1 0042 4 : 5 AWF C ••

•LOW'C'HAWERTOT:;'1b wTh ravg ; B15B6"'.'" " 00425 ' AWF C LOWE R CHAMBE R PRESS , hig h fo r6 sees . •0158 3 0042 6 Z 7 AWF C UPPE R CHAMBE R PRESS , hig h for 5 sees . 0158 9 0042 7 2 S AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E orhrg h hig h vibraUors fo r5 min . 0152 5 0042 9 3 0 AWF C Upps rat Lowe rChambe rTemp , hig h 0160 0 0043 0 '3 2 MWF C A L LWAST E FEE D OF F FRO M FI X(marjuafl yshu toff ] 0174 0 0043 2 3 5 MWF C FLU E GA S HCL , hig h 1 min . avg . 0159 2 0043 5 3G MWF C HEA TINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIME - IMPUT , hig h Ibs/h r 0162 3 0043 7 3 3 MWF C E-STOPSo rT/ C MODUL E inactiv e 0161 5 •0043 8 3f i MWF C FLU E GA S CO , hig h 1 hr . avg . 0159 5 0043 9 4 0 MWF C ATOMEE R hig h hig h vibratio n fo r5 se c 0162 4 0044 0 4 1 SWF C SPEC
. FEE D Ibs/h rhig h 0157 6 0044 1 PAS S FAI L



# y _y 

# 1ZL 

# 5 Z Z 1ZL 

## y y yL 

## y ,y y [r. ZZ1 

## ±y_ 

## y *y 

## y y^BJWEEKL YUNI T# 2

COMPLIANC E CHEC KS J 0:1 " (CM S TasklC4Q39 ) PAG E 2 O F 2

OPERATIN G PARAMETER S PL C COI LBWCOI L <\2 •> swr c HFBT U lbs/h rhig h 0157 3 0044 2 4 3 SWF C LOBT U lbs/h rhig h 0158 0 0044 3 4 3 SWF C h i I BT U los s o fsigna l 0301 9 0044 5 4 8 'SWF C LOBT U Jos s ofsigna l 0307, 0 0044 6 4 7 SWF C SPECIALIT YFEED/COMPRSSSE D GA S FEE D los s o fsigna l 0302 1 0044 7 4 8 MWF C NORT H & SOUT H tP S ALARM S FAILE D 0570 3 0044 8 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s D fsigna l 0302 2 0044 9 5 0 MWF C NORT H & SOUT H fP S SERVERSFAILE D 0570 5 0045 0 5 1 SWF C DIREC TINJEC T{commo n alarm ) 0313 2 0043 1 5 2 O P L Ba g Lea k Detectio n Syste m (Tribo ) 6 5 O R
. Pumpabl e 1 Hou rRollin g Tota l OP L 0320 5 0411 3 6 6 O F L Non-Puinpabl o THou rRollin g Tota i OP L 0320 Q 0411 4 6 7 O P L Tota l wast e 1 Hou rRollin g Tota l OP L 0S2Q S 0411 5 O P L CI
. 1 2 Hou rRoilin g Tota l OP L 0321 1 0411 6 6£ 5 OP L Lc wVolatil e 1 2 Hou rRollin g Tota l OP L 0621 4 0411 7 7 0 O P L Sem i Volatil e 1 2 Hou rRollin g Tota l OP L 0821 6 0411 3 7 1 OP L Mercur y1 2 Hou rRollin g Tota l OP L 0821 3 Q411 9 7 2 OP L Asi l 1 2 Hou rRollin g Tota l OP L 0822 0 11412 0 7 3 OP L P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0822 2 0412 1 7 4 OP L S C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0S22 4 0412 2 7 5 O P L SD AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L 0S22 6 0412 3 7 G O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOPt
. 0S22 7 0412 4 7 7 O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L 0622 8 0412 5 ...OP L Slac k

HC LCorrecte d 1 Hou rRollin g Avorag e Hig h OP L 0S23 2 0412 3 • : OF L Stac k

C O Correcte d 1 Hou rRollin g Averag e Hig h OP L 0823 6 0412 7 B O O P L Stac k Flo w1 Hou rRoilin g Averag e Hig h OP L 0824 4 0412 8 S 1 O P L BT U 1 Hou rTota l OP L 0320 9 0412 9 S 2 O P L HrtCI/Hr a Lim e Flo w1 Minut e Averag e Hig h OP L 0825 1 0413 0 3 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0S15 S 0413 2 8 4 WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTU/CHARG E 8 5 Hi/D i Ato m izin g Ai rLo wpressur e alar m (Ma. n ua ! Check: ) 8 6 Lo/D I Atomizin g Ai rLo wpressur e alar m (Manua i Check ) 8 7 Specialt yFeede rAtomizin g Ai rLa wPressur e alar m (Manua l check ) O C L =CONDmO N LIMI T AWF C -AUTOMATI C WAST E FEE D CUTOF F MWF C =MIS C WAST E FEE D CUTOF F

- SWF C ^SPECIFI C WAST E FEE D CUTOF F PAS S FAI L 

# y. > 7 

# yy y yL yL 

# y LZL yL yL 

# yy yl y: y^ yL 

# y yL

Comment s

CHECKE D BY : 

## I -^^L-jQ ^ DAT E 

## iO~Z

^"'Q^ TIME : 

### ^r3>( 9 

## fuFh* APPROVED : //^g -Z./*. ^

# /yChvy PUCE : CohlrolRoo m t , -:.EKLY_ 2 4/470 7 H K(31WEEKL YUNI T£ 2 (CM S Tas k iC4030 ) PAG E 1 O F 2 COMPLIANC E CHFC KSHEE T

OPERATIN G PARAMETER S P L C COI L BWCOI L PAS S

' 1 OC L T R VPOSITIO N (OPEN ) 0160 2 0041) 1 

# / 2 OC L UPPE R CHAMBE R TEMP . 1 mi n avg . 0160 3 0040 2 3 ' OC L H i BT U Ibs/h rMa x 0160 4 0040 3 4 OC L LOWE R CHAMBE R TEMP . 1 mi n avg . 0 1 SO S 0040 4 5 OC L' L O BT U Ibs/h rMa x 0160 S 0040 5 S OC L FLU E GA S HCL , 1 hr . rollin g avg . 0160 7 0040 6 

## y 7 OC L FLU E GA S CO , 1 hr . rollin g avg . 0160 3 0040 7 6 OC L FLU E GA S OPACITY , hig h for48 0 sec/fir
. avg . 0160 9 0040 6 S 3 OC L• FLU E GA S OPACITY , hig h instantaneou s 0161 D 0040 9 

## __^y_ 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min . av g •0161 1 0041 0 1 1 OC L HEA TINPU Thig h mbfu/fc r 0161 3 O041 1 

## y 1 2 OC L CHLORIN E INPUT , hig h lbs/h r O041 2 

## y 1 3 OC L SOU D FEED , hig h lbs/h rMax . 0152 8 0D41 3 

## y 1 4 O C L UPPE R CHAMBE R TEMP , lo w1 h rroilin g avg . 0153 a ' • 0D41 4 

## y 1 5 OC L SPECIALIT YFEEDE D hig h Ibs/h rMax . 0151 6 0FJ41 5 1 7 AWF C S D AOUTLE TTEMP , high l min . avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DJFF.PR . DROP , Lo w1 min . avg . D159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min , avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min , avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min . avg . 0159 7 0042 1 

## y 12 AWF C FLU E GA S HC Lhig h 1 min . avg . 0159 8 0042 2 

## y 2 3 AWF C FLU E GA S FLO WRATE , hig h irist . 0153 9 0042 3 

## ,y 2 4 AWF C FLU E GA S OPACITY , hig h 1 min . avg . 0160 1 0042 4 

## y. '•35 AWF C L O WCHAMBE R TEMP. , lo w1 hr . avg; . 0158 6 0042 5 

## . y : -6 AWF C LOWE R CHAMBE R PRESS , hig h for 5 sees . 015S B 0042 0 . 

## y 2 7 AWF C UPPE R CHAMBE R PRESS , hig h for 5 sees . 0153 9 0042 7 

# - y 2 8 AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 S 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratto n fo r5 min . 0162 5 0042 9 

## y 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 Q 0043 0 

## y 3 2 MWF C A L LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 O .0043 2 3 5 MWF C FL U E GA S HCL , hig h 1 min . avg . 0.159 2 0Q43 5 3 S MWF C HEA TINPU Thig h anticipate d D162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h Ibefli r 0162 3 0043 7 

## y 3 3 MWF C E-STOP S orT/ C MODUL E inactiv e 0161 5 O043. 3 3 8 MWF C FLU E GA S CO , hig h 1 hr . avg . 0159 5 O043 9 

## y 4 0 MWF C ATOMIZE R hig h hig h vibratio n fo r5 sec . 0162 4 O044 O 

## y 4 1 SWF C SPEC
. FEE D ibs/h rhig h 0157 S OD44 1 

## y[3

1 WEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039 ) PAG h 2 O P 2
OPERATIN G PARAMETER S P L C COI L H WCOI L PAS S FAI L 4 2 4 3 4 5 4 6 4 7 43 4 $ 5 0 5 1 5 2 6 5 6 B 6 7 6 8 6 9 7 0 7 1 7 2 7 3 7 4 ' 7 5 7 3 ,„..7X. . -v *.-.l 'T 6 7 9 s o B l 6 2 6 3 8 4 S S 8 6 S 7 SWF C SWF C SWF C SWF C SWF C MWF C SWF C MWF C SWF C OP L OP L OP L OP L O P L O F L O P L O P L OP L OP L OP L OP L OP L O P L O P L O P L OP L OP L OP L AWF C H1BT U lbs/h rhig h 0157 B

LOBT U ibs/n rhig h 0156 0 HlDTLItos s o fsigna l 0301 9 LOBT U los s o fsigna l - 0302 0 SPECIALIT YFEED/ C OMPRESSE D GA S FEE D los s o fsigna l 03D2 1 NORT H & SOUT H 3P S ALARM S FAILE D 0570 3 UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 03022 . NORT H & SOUT H IP S SERVERSFAILE D 0570 5 DIREC TINJEC T(commo n alarm ) 0313 2 Ba g Lea k

Detectio n Syste m (Tribo ) Pumpabl e 1 Hou rRollin g Tola ! OP L0620 5 Non-Pumpsbl e 1 Hou rRollin g Toia l OP L0820 6 Tota i wast e 1 Hou rRollin g Tota l OP L0320 3 CL1 2 Hou rRollin g Tota l OP L0821 1 Lo wVolatil e 1 2 Hou rRoilin g Tota l OP L0821 4 Sem i Volatil e 1 2 Hou rRollin g Tol a I OP L0821 6 Mercur y1 2 Hou rRoilin g Tota l OP L0821 8 As h 1 2 Hou rRollin g Tota l OP L0822 0 P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L0822 2 S C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L0822 4 SD AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L0822 6 Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOP L0822 7 .BaghQUse.
. Differentja[
. Pressure. . 1 Minut e Averag e Hig h 0 P L0822 5 Stac k HC LCorrecte d 1 Hou rRoilin g Averag e Hig h OP L0623 2 Stac k C O Correcte d 1 Hou rRollin g Averag e Hig h OP L0fi23 6 Stac k Flo wfHou rRollin g Averag e Hig h OP L0824 4 BT U 1 Hou rTota l OP LO820 0 Kr tCl/Hr a Lim e FID W1 Minut e Averag e Hig h OP L0325 1 Lim e Slurr yDensit y1 Hou rRoilin g Averag e Lo w0315 6 WiL LNO TACCEP TSOLI D CHARGE S >75 0 KBTU/CHARG E Hi/D fAtomizin g Ai rLo wpressur e alar m (Mqnua. F Check ) Lo/D I Atomizin g Ai rLo wpressur e alar m (Manua l Check ) Specialt yFeede rAtomizin g Ai rLo wPressur e alar m (Manua l check ) Q044 2 0044 3 0044 3 G044 S 0044 7 0044 B 0044 9 0045 0 0045 1 0411 3 0411 4 0411 5 0411 6 0411 7 D4T1 S 0411 9 0412 0 0412 1 0412 2 0412 3 0412 4 0412 5 '04126'. ' 0412 7 0412 3 0412 9 0413 0 041 3 2 

## ZL 

## y
y y 

# yy ~1y~ 

## y y

y„ y 

## y_ 

# y / O C L^CONDITIO N LIMI T AWF C =AUTOMATt C WAST E FEE D CUTOF F MWF C =M!S C WAST E FEE D CUTOF F SWF C ^SPECIFI C WAST E FEE D CUTOF F

Comment s

CHECKE D B Y: JSy^T T. i ^PROVED : DATE://-Z5'-Q < ? TME:*j?' » jS" ~ ^j ^ P M PLACE : Contro l Roo m ijfWEEKLY_ 2 4/4/0 7 H K

## ABSOLUT E CALIBRATIO N AUDI T(ACAJ DAT ASHEE T

Uni t# . Seria l # COS A 

## Paramete r > 0 2 25 % rCO-lo wrang e 200pp m rCO-hig h rang e '30GGpp m rHC l 1000pp m NIS TTraceabl e Calibratio n Standard s Paramete r > 0 2 25 % rCO-lo wrang e 200pp m rCO-hig h rang e '30GGpp m rHC l 1000pp m Ga s Concentratio n Paramete r > 0 2 25 % rCO-lo wrang e 200pp m rCO-hig h rang e '30GGpp m rHC l 1000pp m Lo w(Zero ) 0 

### " ± 0. 5 

## Paramete r > 0 2 25 % rCO-lo wrang e 200pp m rCO-hig h rang e '30GGpp m rHC l 1000pp m Mi d 8.9 3 

### ± 0. 5 

## Paramete r > 0 2 25 % rCO-lo wrang e 200pp m rCO-hig h rang e '30GGpp m rHC l 1000pp m Hig h 1 5 

# ± 0. 5 

### Ru n Numbe r Concentratio n 

### Difference '

Referenc e Analyze r Lov / • Mi d Hig h ' 1-Lc w 0 0 

## • o — 

### 2-Mi d 8,9 3 9. 1 -0.1 7 3-Hig h . 1 5 15. 1 4-M>w - 0 0 0 5-Mi d 6.8 3 9 — 

### -0.0 7 • — 

### 6-Hfg h 1 5 15, 3 — 

### -0, 3 7- 1 r> w 

### n n 0 .. . 

## e-Mid 3.9 3 9. 1

—_ 

### -0,1 7 — 

### 9-HEg h 1 5 •15, 2 — 

### -0. 2 Mea n Differenc e - Calibratio n Erro r- 0,0 0 -0.1 4 • -0.2 0 Mea n Differenc e - Calibratio n Erro r- 0.00 % -0.55 % -0.80 %
Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 10 0 

## Bria n Bunfil l H I Tec h Nam e Signature Titl e 

## 9/25/200 9 2/4/201 0 Dat e

## ABSOLUT E CALIBRATIO N AUDI T(ACA ) DATASHEE T

Unit # 2



## _

Seria l # Paramete r r 

## 0 2 25 %

' fCO-lo wrang e 20Dpp m r CO-hig h rang e 30QOpp m rHC ! lOOOpp m NIS TTraceabl e Calibratio n Standard s Paramete r r 

## 0 2 25 %

' fCO-lo wrang e 20Dpp m r CO-hig h rang e 30QOpp m rHC ! lOOOpp m Ga s Concentratio n Paramete r r 

## 0 2 25 %

' fCO-lo wrang e 20Dpp m r CO-hig h rang e 30QOpp m rHC ! lOOOpp m Lo w(Zero ) 0 

# ± 1 0 

## Paramete r r 

## 0 2 25 %

' fCO-lo wrang e 20Dpp m r CO-hig h rang e 30QOpp m rHC ! lOOOpp m Mi d 68, 9 

# ± t o 

## Paramete r r 

## 0 2 25 %

' fCO-lo wrang e 20Dpp m r CO-hig h rang e 30QOpp m rHC ! lOOOpp m High 15 3 

# ± 1 0 • 

### Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w Mi d Hig h t-Lo w 0 0. 1 -0. 1 — — 

### 2-Ml d 66. 9 71, 7 -2. 8 — 

### 3-Htg n • 153 152. 7 TM 

### 0. 3

a 0 4 M.i TU-SJYtt V 

### 5-Mid - 63. 9 7f. 8 ' — 

### - 3 — 

### 6-Hig h 15 3 152. 8 — TM 

### 0. 2 7-bM— - 0

_. . 0. 6 -flj3__
_ — — 

### B-MI d 68. 9 71. 6 — 

### -2. 7 — 

### 9-Hig h 15 3 ' 152. 5 . 0. 4 Mea n Differenc e - Calibratio n Erro r= -0.3 7 -2,6 3 0.3 0 Mea n Differenc e - Calibratio n Erro r= -0.18 % »1.42% 0.15 % Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 10 0 

## Brian Bunfll ! Nam e Signatur e 

## E/ l Tec h

' Titl e 9/25/200 9 Dat e 2V4/20tO

## ABSOLUT E CALIBRATIO N AUDI T(ACA ) DATASHEE T

Unit # Seria l if 34 6 

## Paramete r r0 2 

## 25 % f * CO-lo wrang e 200pp m COhlgFvrang e 3000pp m CHC 1 1000pp m NIS TTraceabl e Calibratio n Standard s Paramete r r0 2 

## 25 % f * CO-lo wrang e 200pp m COhlgFvrang e 3000pp m CHC 1 1000pp m Ga s Concentratio n Paramete r r0 2 

## 25 % f * CO-lo wrang e 200pp m COhlgFvrang e 3000pp m CHC 1 1000pp m Lo w(Zero ) 0 

# + 15 0 " 

## Paramete r r0 2 

## 25 % f * CO-lo wrang e 200pp m COhlgFvrang e 3000pp m CHC 1 1000pp m Mi d 1079. 1 

# + 15 0 

## Paramete r r0 2 

## 25 % f * CO-lo wrang e 200pp m COhlgFvrang e 3000pp m CHC 1 1000pp m . Hig h 222 0 

# ± 15 0 Ru n Numbe r 

### Concentratio n • Difference

Reference Analyze r Lo w Mi d Hig h 

### 1-Lo w . 0 0. 1 — 

### 2-Mir J ' 1079, 1 •1151. 9 — 

### -72. 3 — 

### 3-Hig h 222 0 2217. 4 — 

### 2. 6

:... 0 OA
. -QA, 5-Mi d 1079. 1 1D95. 3 -16. 2 — 

### 6-Hig h 222 0 2182. 5 — — 

### 37.5 / 7-L^ w n 

## . _._o, a - . JQ£...

——.. . . 

### JQ£... 8-Mic f 1079. 1 1091 2 -12. 1 — 

### 9-Hig h 222 0 2173. 4 — — 

### 41 6 Mea n Differenc e - Calibratio n Erro r= -0.3 7 -33.7 0 27,2 3 Mea n Differenc e - Calibratio n Erro r= -0.01 % -1.12 % 0.91 %

. Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 10 0 

## Bria n BunfilfE/ITec h Nam e Signature Titl e 

## 9/25/200 9 2/4/201 0 Dat e

## ABSOLUT E CALJBRATIO M AUDI T(ACA) DATASHEE T
Seria l 34 6 

## Paramete r r 

## 0 2 25 % tTM 1 

## CO-lo wrang e 200pp m CO-hig h 

## rang e 3000pp m . <* •HC l lOQOpp m NIS TTraceabl e CaObration Standard s 

## Paramete r r 

## 0 2 25 % tTM 1 

## CO-lo wrang e 200pp m CO-hig h 

## rang e 3000pp m . <* •HC l lOQOpp m Ga s Concentratio n Paramete r r 

## 0 2 25 % tTM 1 

## CO-lo wrang e 200pp m CO-hig h 

## rang e 3000pp m . <* •HC l lOQOpp m Lo w(Zero ) 0 

# + 5 0 

## Paramete r r 

## 0 2 25 % tTM 1 

## CO-lo wrang e 200pp m CO-hig h 

## rang e 3000pp m . <* •HC l lOQOpp m ' Mi d 31 6 

# + 5 0 

## Paramete r r 

## 0 2 25 % tTM 1 

## CO-lo wrang e 200pp m CO-hig h 

## rang e 3000pp m . <* •HC l lOQOpp m Hig h */4 3 

# ± 5 0 

### Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Low Mi d Hig h 1-Lo w 0 0 0 — — 

### Z-Ml d 31 8 276. 5 41. 5 — 

### 3-Hig h .74 3 741 1 •— — 

### 1. 9 4..LQV * 

### .0

. 0 5-Ml d 31 3 312, 4 — 

### 5. 6 — 

### 6-Hig h 743 738, 1 — 

### 4. 9 .:7-Low . .0 0 . . . .. . 0 . —. . —.. .



### 31 8 323. 1 — 

### -5.1 ' — 

### 9-Hig h 743 73 9 — 

### 4 Mea n Differenc e ~ Calibratio n Error = 0.00 ' 14.0 0 3.S D Mea n Differenc e ~ Calibratio n Error = 0,00 % 1.40% 0.36 % Calibratio n Erro r= Mea n Difference/Spa n Valu e * 100 

## Bria n Bunfil l E/ fTec h Nam e 

### Signature Titl e 

## 9/26/200 9 2/4/201 0 Dat eTable 1 Summar

yo fRelativ

e Accurac

yTes t Audi t Result

s Veoli a E S Tethlriea l Solution s Sanget . Illinoi s Jun e 22 , 2

3 an d 24,2009 CEM S Paramete r Unit s Measure d R A Criteri a Pass/Fai l Uni t2 C O pp m @ 7 $ O y 0,00 4 ppm 1 PffS S Uni t2 O2 , di y 

### i.o*- n Pas s Uni t2
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### %o 2 1. 0 3 ' c PSA- S Uni t4 C O pp m @ 7 % O,
. 1.14 6 ppm z Pas s Uni t4 Oa , dr y 0.15%' L 0 a ' c Pas s Uni t4 0 2 . we t ^ 0 2, 0,46% ' Pas s "Percen to femissio n standar d o rabsolut e averag e differenc e (pp m o r%)
. L 

### PS4B . C 

### PS3 ,

INCINERATO R C'fMS RAT A VEOUAE S JUL Y 7 , 200 9 t.:jif"Pj(>j«CD9&-5ei

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### TAG :

LOOP : • ; 

### DHSCSIPOK : SERVICE : LOCATION : LP-SBT : REMARKS : IJJST L - ELMKS : SPEC-HMKS : S/H : TW

X IHSTRUMKU T CaLIBEAriOM ' RECOR D

UNI T # 3 QUAli'l'ERIi Y W T 3 0 4 WEIGH T TRANSMITTE R SPECIALT Y FEEDE R (HOODED ) MA3STDPACT : MODEL : SCALE ; CALIB-IN" : CALIB-QUT : PKQCESS-SP :

. IHST-SP : ACTION : I/ O NUMBER. : TOLED O

814 0 EX P 0-2,00 0 # 0-2,00 0 # 4~2 Q MAD C 0#=ai 9 ct s 2 00#=114 7 et a 1#~1,£3 8 ct s 3001 2
Chec k scale , digita l Calibratio nper . Toled o instructions * The n wit hn o weigh t o n scale'adjus t analo g zero . {HOTS : HM I wil l not

displa ynumber s las s tha n zero} . fclext ad d weigh t = t o 10 % ar e mor e o f scale s range , the n adjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . Se e Manufacture s literatur e Fo r detaile dinstructions . Fil l ou t an d a££i xa ne wcalibratio nsticker . O . l lb/h r CALTERATIO HREPOR T i m m wlx b o . 

### INSTRUMEN T KEMJSWG •

Before Calibration

^r ^

After Calibration



### CALIBRATIO NSOtlKC E REFERENC E

Cohfftisiit s

Performe d by ; J B CALSH E ET • WD B I MO-tf 

### Dat&y^S^if^^ L Time : Z &£> _$M (p M 

### Place : ((FieldJor Shop}

### TW I INSTRUMEN T CALIBRATIO NRECOR D

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### 814 0 0-40 0 # 0-40 0 # 4-2 0 MAD C 0#=81 & CC S 2Q0#^245 7 ct s 1#=8.1 9 ct s I/ O NUMBER : 3002 2 CA L IBRAT T OK

F MOTE S Chec k scale , digita l Calibratio nper , Toled o instructions . Then , with'n o weigh t o n scal e adjus t analo g sero . (NOTE : HM I wil l no t displa ynumber s les s tha nzero ) . Nex t ad d weigh t = t o 1.0 % ar e raor e o f scale s range , the nadjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . Se e Manufacture s literature'fo r detaile dinstructions , Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T B&fore Calibration 

# o

Afte r Calibration

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Commen t s :
performe d by : fe^T ?sfe^ — Date :'feT%^



# Time:Z // 0 AM ( F M ) 

### J B . Plac e r . >s > 

### ~~~~2 K CALSHEET,WD B fField) or Shop)'TAG : LOOP : DESCRIPON : SERVICK : LOCATION : LP-SHT : P&ID : REMARKS : 

### IHSTk-RMKS : S2EC-RMKS :

S/N ; 

### TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 QUARTERL Y PD T 3 5 0 PRESSUR E DIFF . TRANSMITT E BAGHOUS E INLET/OUTLE T FIEL D 

### 303 5 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OOT : PROCESS-SP : INST-SP : •ACTION : I / O NUMBER : 

### YOKOQAW A 0-1 5 i n w

d 4-2 0 MAD C

U S E PNEUMATI C CAI J IBRATIO NBENC H WIT H INCLIN E MANOMETE R AN D LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D REA D 

### OUTPU T WIT H LOO P CALIBRATOR .



### Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 Xb/h r CALIBRATIO N REPOR T I^tT T VAT.UE ; INSTRUMEN T RSSASISG Befor e Calibratio n

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CALIBRATIO M

SOURC E REFERENC E

Comments :

Performe d by : $&&J-&c /<^ !

### ^ Date: 9 Time : Jh

y^/WF M 

# \ ::r J B Plac e - . CALSHEET.WD B {Field o r Shop)

### TAG :

LOOP : DESCRIP0N : SERVICE : LOCATION : LP-SET : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 QUARTERL Y P T PRESSUR E TRANSMITTE R LO W CHAMBE R PRESS . FIEL D 303 2 MANUFACT ; MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I/ O NUMBER ; Rosamoun t

115 1 D P -7. 5 t o +2 . 4-2 0 MAD C 5 

### in , wc .

CALIBRATIO NNOTE S Connec t transmitte r t o b e calibrate dt o pressur e sourc e an d calibrate dreferenc e {Manometer) , inpu t appropriat e pressur e an d verif ywit hcurren t meter . Complet e an d affi xa properl yfilled-ou t calibratio n sticker . Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T IKPU T VALU E IHST^WSJJ T RBaDlfl G• ^ &-tf Before

Calibration

„ ,
After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : /f£?e.£r&€- /(/fri Date : °7 Tima ^ / O ? 0 J B Place : CALSHEET.WD B (Field or Shop) 

### P M

### TH I INSTRUMEN T CALIBRATIOl * RECOR D KNI T # 3 QUARTERL Y TAG : P T LOOP : 31 9

: 

### DESCRIPON ; PRESSUR E TRANSMITTE R SERVICE : OPPE R CHAMBE R PRESSUR E LOCATION ; FIEL D LP--SHT : P£ID : 303 3 •REMARKS ; INSTL-RMKS : 8PEC-RMK S : S/titi MANUFAC T MODE L SCAL E •CALIB-I H CALIB-OU T PROCESS-S P INST-S P I ACTION ; I/ O NUMBER : -7. S t o +2. 5 in . wa .

4 - 2 0 MAD C

CALIBRATIO N

NOTE S Connec t transmitte r t o b e calibrate dt o pressur e sou.ro e a n d calibrate dreferenc e (Manometer} , inpu t appropriat e pressur e an d verif ywit bcurren t meter . Complet e an d affi xa properl yfilled-ou t calibratio n sticker . Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affil e a ne wcalibratio nsticker , 0. 1 lb/h r CALIBRATIO N REPOR T INFO ? "VALU

E Before

Calibration INSTRUMENT READING

After Calibration Z9> 9 8 TM A CALIBRATIO N

SOURC E REFERENC E

Comments :

Performe d bv : A/ss^Zaji A^^fyt

Date : ^/"M-^f

Time : &^S&/M P M J B Place : . 

### CAL SHEET . WDB (Field or Shop)

### TAG- :

LOOP : : ; DESCRLPON : • SERVICE : LOCATION : LP-SRT : P&ID ; REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : TW 1 INSTRUMEN T Cfi L JBRA'iTO NRECOR D

. UNI T # 3 QUARTERL Y Trib o Bag-hous e Lea k Detectio n FI D MAHOPACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS -SP : INST-SP : ACTION : I/O NUMBER : Aubur n

TRIBO.dg d 0-lOOOp a O-lGOOp a 4-20m a

CALIBRATIO NNOTE S Disconnec t th e inpu t cabl e a t th e BN C connecto r o n th e inpu t card , an d chec k 'fo r Hero , us e Auburn , Trib o flow , file dtes t unit , mode l 2902 , t o inpu t a Pico-Am p signa l o f 500p a an d recor dthes e values .

0, 1 lb / h r CALIBRATIO NREPOR T INPW''''VALtfEINSTRUMEN T REA&IN Q •

After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comment s : Ki n fafibr^vh W

# needed*

Performe d by; . Date: . 

# iMfrfl l Time : \l'ZO(w ) 

### P M J B Place : CALSHBET.WD B ((Field ) o r Shop)

### TAG :

i LOOP : ' ' DESCRIRON : SERVICE : LOCATION- : •LrP-EHT P&IIJ : REMARKS : INSTL-RMKS ; SFBC-RMKS r S/M : TW I MSTRUMEN T CALIBRATIO N RECOR D UNI T # 3 QUARTERL Y A T 3B 9 OXYGE NMANUFACT : CO S A STAC K GA S ANALY2E R FIEL D 303 5 MANUFACT : MODEL : SCALE : CALIB-IN' : CALIB-OOT : PROCESS-SP ; INST-SP : ACTION : I/ O NUMBER ; 0-25 %

0-25% 4-2 0 MAD C

CALIBRATIO N

NOTE S Flo wcalibratio nga s a t 2- 3 psi g an d 3 scf h

Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0.1 . lb/h r CALIBRATIO N REPOR T INPU T VALU E INSTRUMENT READING ^ y~i Before

Calibratio n„ „



# - ZA.?yf •a . d Afte r Calibratio n

CALIBRATIO NSOURC E REFERENC E ZER O GA S CY L ft; j j ^ 6 SPA NGA S CY L ft: ' £ flOl I 3 ^

Comments :

Performed , by ; _ Date : Time i 

## ^'S'Srmjpin JB Place : CA L SHEET . TOB gtfiel(S.J>r Shop)

### TAG :

. LOOP : DESCRIPOM ; SERVICE :
, LOCATION ; LF-SBT : P&ID : REMARKS : INSTL-RMKS : SeHC-BMKS : S/K : TW

X INSTRUMEN T CALIBRATIO NRECOR D

mxT 

### # 3 QUARTERL Y A T 3 6 S B H C STAC K GA S ANALYZE R STAC K 55 6 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP ; INST-SP : ACTION ; I/ O NUMBER : Therm o Elect .

SI C 0-10 0 PP M Co .
4-2 0 MAD C

CALIBRATIO N

MOTEL S 1) Ope n sampl e ga s bottl e valves . 2) Pres s MEN

UButto n 3 ) Pres s CALIBRATIO N' 4 } Pres s ZER O ADJUS T 5 } Pres s SPANADJUS T afte r 4) finishe d 6 } Pres s RU

Nafte r 5}finishe d 7 ) Clos e sampl e ga s bottles . Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T 

# memvmm O 

### Befor e Calibratio n 1NSTRBKEEO T REABINQ 

# -lie.2. Afte r Calibration

CALIBRATIO N

SOURC E REFERENC E GA S CY L # :

Comments ; fOo -fa C t\s£e

f>±t?



### Performe d b y J B • CALSHEET , WD

B Date : Time: . . 

# fQ&Sapm Place: . (Field

or Shop)

### TfT I INSTRUMEN T CALIBRATIO NRECOR D TAG ; LOOP : ' DESCRIPON ; SERVICE : LOCATION : LP-SHT ;

- P&ID : REMARKS : INSTL-RMKS : SPEC-RHKS :

S/K : 

### A T 3 

### S B E OPACIT Y STAC K GA S STAC K

2.0 0 t o E.72m a UNI T # 3 QUARTERL Y MANUFACT :

MODEL : SCALE : CALIB-IN : CALlB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : TELEDYNE ! INST .

LightHaw k 0-100 % 4-2 0 MAD C

CALIBRATIO NNOTE S Clea nwindows ,

Se a Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nstickier . 0- 1 lb/h r CALIBRATIO NREPOR T iNp W' VALCE.'INSTRUMEN T R S AfiJN S Before Calibration



### Afte r Calibration

CALIBRATIO NSODRC E REFERENC E

Comments : 

## Ccilihtodprf .^RT

YhQW^acj-u

Ce^S

C^ulddMfT

.

Performe d by ; J 2 

### , , . .T T

# y

J(0 Date :MzlM 3 Tims: . J B Place: . CALSHEET , VJDB 

### P M 'iel p or Shop}

### TW I INSTRUMENT CALIBRATIO NRECOR D UNI T # 3 ANNUAL TAG ; T T LOOP ; 30O A DESCRIPQN : PL C THERMOCOUPL E INPtJT " MANG'EACT : MODICO N

. SERVICE : LOEfE R CHAMBE R MODEL ; 883-20 0 LOCATION : FIEL D SCALE : 0-250 0 deg-
- F LP-SHT: ' CALIB-IN : TYP E K F&ID : 203 2 CALlB-OUT i REMARKS : PROCESS-SP : 1NSTL-RMKS : INST-SP : SPEC-RMKS : ACTION ; S/Cf : I/ O NUMBER : CALIBRATIO N

NOTE S Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g E . an d 2,00 0 deg.F . a t inpu t o f PLC , the n verif ythi s singl e o n th e contro l pane l CRT ,
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T TJipW' TMAIH INSTIltfM^N T READING ' -Z.QOO" 

# F • 

# .zat>o Q



### After Calibration

CALIBRATIO NSOURC E REFERSKC S

Comment s

Performe d by: , Date : Time ; je Place : CA L SHEET . HD B * tiwiel&pr Shop).

### TAG :

LOOP : DESCRIPON ; SERVICE : LOCATION ; LP -SHT : P&ID : REMARKS ; INSTL-RMKS ; SPEC-RMKS : S/N : TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUA L T T 3 00 B PL C THERMOCOUPL E INPU T LOWE R CHAMBE R FIEL D 303 2 MANDEACT : MODEL : SCAL E i CALIB-IN : CALIB-OUT : PROCESS-SP : INST-S P ACTIO N I/ O NUMBE R MODICO N

683-20 0 0-250 0 deg . TYP E K

CALIBRATION " NOTE S Us e col djunctio ncoirrpensate dthermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 5 0 0 de g F . an d 2,00 0 deg.F , a t inpu t o f PLC , the n verif ythi s singl e o n th e contro l pane l CRT ,
.Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker , 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READIN G SOO* 

# F Sstor e CsIltoatio n 

# 5PO0 ° Z.0OQ

0 

# h ZOOcf Afte r Calibration

CALIBRATIO N

SOURC E REFERENC E

consments :

Performe d

## hy-^j-^

\ . 

# '^JL J^JIP

Data : 

## )

I HO - Q°\ Time : 

## 2-'

m(Sj ) J B CALSHEET.WD B Place; , (Field b r Shop)

### TAG :

LOOP : " DfiSGHXPOU : SERVICE ; LOCATION ; LP-SET : P&ID : EEMARKS : INSTL-RMKS : SPEC-RMKS : S/N ; TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUA L T T 3 IS A PL C THERMOCOUPL E INPU T UPPE R CHAMBE R FIEL D 303 3 MANUFACT i MODEL : SCALE : CALIB-IN ; CALIB-OUT : PROCESS-SP : INST-SP ; ACTION : I/ O MJMBER t MODICO N

883-20 0 0-2S0 0 d * TYP E K >g . R



### CALIBRATIO N

NOTE S . Us e col djunctio ncontpensate d thermocoupl e calibrato r t o iapu t a typ e K teniperatur e signa l o f 50 0 de g ? , an d 2,00 0 deg-F . a t inpu t o f PLC , the n verif ythi s singl e o n th e contro l pane l CRT .

se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa newcalibratio nsticker . 0- 1 lb/h r CALIBRATIO N REPOR T INPUT V«IiUeINSTRUMEN T READUif S crv ^ P Befor e Calibratio n^ QUO 

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CALIBRATIO N

SOURC E REFERENC E

Comment s

Performe d by : ife^— ' t - Date : /^t > 0 l Time:£ ; 

### V^""_AM(^ ) J B Place : . ^-— ^ CALSHEET.WD B ' <(FieljJox- Shop)

### T K I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUA L TAG ; T T LOOP : 319 B " DESCRIPON : PL C THERMOCOUPL E INPU T ' MAHUFACT : MODICO N SERVICE : UPPE R CHAMBE R . MODEL: 

### 883-20 0 LOCATION : FIEL D SCALE : 0-250 0 deg . P . LP-SHT r CALIB-IN : TYP K K P&ID : 303 3 CALIB-OUT ; REMARKS : PROCESS-SP : mSTL-RMKS : INST-SP : SPEC-RKKS : ACTION : S/N : I/ O NUMBER : CALIBRATIO N

NOTE S Os e col djunctio ncompensate d tliermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g F . an d 2,00 0 • deg.F . a t inpu t o f PLC , the n verif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affis : a ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATION REPORT j ^ptf f GALOISTNSTRUMEN T READIN S 

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CALIBRATIO N

SOURC E REFERENC E

Comments: '

Performe d by; , Date : 

# l)~jQ-€ft Time : % J B Place : <^ =a 

### ^ > CALSHEET.WD B QField)or Shop)

### Tff l INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUA L TAG : T T LOOP : 32 3 : "DHSCRIPON : PL C THERMOCOUPL E INPU T MANUFACT : MODICO N SERVICE : SD AINLE T MODEL : 883-20 0 LOCATION : FIEL D SCALE ; 0-250 0 deg . F . LP-SHT : CALIB~IN : TYP E K PSID ; 303 3 CALlB-OUT : REMARKS : PROCESS-SP : INSTL-RMKS : INST-SP ; SPEC-RMKS i ACTION ; S/N : I/ O NUMBER :
Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 5 0 0 de g F . an d 2,00 0 deg . P . a t inpu t o f PLC , then , verif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literature s fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO N REPOR T INPU T VALTJEINSTRUMEN T READING•

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CALIBRATIO N

SOURC E REFERENC E

Comments :

erforme d by: . Date : Time : J B Place : . . , CALSHEET.KD B ^ QFiel^ orShop)

### TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUM * TAG : T T LOOP : 37 0 DESCR1PON : PL C THERMOCOUPL E INPU T SERVICE : SD AOUTLE T TEMP I

FIEL D LOCATION : LP-SHT : p&id : REMARKS : INSTL-RMK S : SPEC-RMKS : S/N : 303 4 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OOT: - PROCESS-SP : INST-SP ; ACTION : I/ O NUMBER : CALIBRATION

NOTE S MODICO N

883-20 0 0-250 0 deg . F . TYP E K

Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a typ e K temperatur e signa l o f 50 0 de g F , an d 2,00 0 deg.F . a t inpu t o f PLC , the nverif ythi s singl e o n th e contro l pane l CRT .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r
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Comment s

Performe d by : J^-^T" ^ Date: Ih]J>^

_Time^^ 5 

### AM^jj O JB ' Place : CALSHEET.TO B l(Fial&or Shop)

### TAG :

LOOP : ' DESCRIPON : SERVICE : LOCATION : LP-SHT : F&ID : REMARKS : INSTX.-BMKS : SPEC S RMKS ; S/N ; T W I INSTRUMEN T CALIBSATIO NRECOR D 

### UNI T # 3 ANNUA L 

### F T 3 8 3 

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0-20,00 0 ACF M 0-.5"WC 4-2 0 MAD C S e t Damp/po t t o mi d poin t
CALIBRATIO NNOTE S US E P3ffiUMATl C CALIBRATIO NBENC H WIT H INCLIN E MANOMETE R AND LOO P CALIBRATOR - INPU T .PNEUMATI C SIGNA L AN D REA D OUTPU T WIT H LOO P CALIBRATOR .

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### Se e Manufacture s literatur e fo r detaile dinstructions ,

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### CALIBRATIO NSOURC E REFERENC E

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### Date : A f y O f ^± m & . //Jp &



### <gj p P M J B Place : CALSHEHT.WDB (Field or Shop)

### TW I INSTRUMEN T CALIBRATIO NRECOR K UNI T # 3 ANNUA L TAG : F T LOOP : 31 5 : DRSCRIPON ; FLO W TRANSMITTE R MANUFACT : MICR O MOTIO N SERVICE : HIG H BT ULiqui dFee d MODEL : DS-040S119S U LOCATION : FL D SCALE : 0-360 0 lb/h r LP-SET : CA6IB-IN ; P&ID ; 303 1 CALIB-OOT : 4-2 0 MAD C REMARKS : PRQCESS-SP : INSTL-RMKS ; Flo wCal . *Il464128334. 2 $ INST-SP : SPEC-EMUS : ACTION : S/H : 23S61 5 I/ O NUMBER : 3000 1 CALIBRATIO NNOTE S Flus hproces s piping , connec t wate r hb& e t o upstrea mside
- o f flo wmeter , se t contro l syste m t o appropriat e rat e control , an d rea d totalizer , flo wwate r int o a containe r an d cottrpar e t h e toltalize r readin g t o th e measure d amoun t i n container .
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### CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : Date : Time: , AM(P^ ) J B CALSKEET.WD B Place : (Field hr Shop)

### TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 3 ANNUA L TAG : S T LOOP : 31 6 DESCRIFON : FLOW TRANSMITTE R SERVICE : LO

WBT U FL D LOCATIO N LP-fiH T PET D B3MAEK S XNSTL-BMK S SPBC-fiMK S S/N ; 303 1 MANUFACT : MODEL : SCALE : CALIB-IN : CALTB-OUT : PROCESS-SP : INST-SP : ACTION : I/O NUMBER : CALIBRATIO NNOTE S MICR O MOTIO N DS-04 0 0-360 0 lb/h r 4-2 0 MAD C
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Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T Tiji^''''VAWraIN^mJMEN T READIN G l ~ ,. < - n vSefor e Calibratio nqQ( V W f e e 1^;^ . i • f 0 /fc>S > 

### Afte r Calibration,

CALIBRATIO NSOURC E REFERENC E

Comments : iU ^ Ca L (jtwf- th* ^ rwed&d 1 .



### Performe d by; . Date : 

# li-i^Ol Time : _A

M(5?M ^ J B Place : * CA L SHEET . WD

B ({Field) or Shop) "

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CALIBRATIO NMOTE S ESTABLIS H UNIFOR MFLO WINT O CONTAINER , REA D TOTALIZER , FLO W FLUI D INT O GRADUATE D CONTAINE R AN D VERIF YWIT H TOTALIZER .

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Performe d hy : 

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: \ J B Place ; CALSHEET.WD B fffieldjor Shop)SiD*Jsdme d t t - iit . LOUJB , M O fStz g ttnilimuii (314

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Ca tDate : 11/12/200 9 NortCaldue : 9 0 day s Servic e TecJuilcta n RegTstratTortf c(H&2-IL ' Calibrate d leySarvk e Techrucian : Ala n Prim o C a l it o ratio n Dates : J A N AP S J Lr|

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### - y 7 OC L FLU E GA S C O >10 0 PP M 1H R Rollin g avg. 0087 2 0M0 7 

### - y a OC L FLU E GA S OPACIT Y ->3Q%fo r4a 0 SecJHr
. 0087 3 0040 B 9 OC L FLU E GA S OPACIT Y =>60 % instantaneou s 00B7 4 0040 9 y .1 0 OC L FLO E GA S FLO WRAT E >17,19 B ACF M for> 1 Mii. 0097 5 0041 0 y 11 . OCL ' MEA TINPU T ^>16MBTlMII ? 008S 5 0D41 1 y . 1 2 OC L CHLORIN E INPU T i-21 7 Ibs/H R 0086 6 0041 2 y 1 3 OC L SOU D FEfc'Qtf/H R MA X **104 1 «H R 0QS6 0 0041 3 y 1 4 OC L UPPE R CHAMBE R TF-MP - <134 5 DEGF I I R ROLLIN G AV G 0085 3 0041 4 y 1 5 OC L SPECIALIT YFEEDE D #/H R MA X =>fi0 8 #/H R 0095 2 0041 5 y 1 7 AWF C S D AOLFTLr : TTEMP , >50 0 deg . F1MI N avg . D0S8 7 0041 7 y 

### • X 1 8 AWF C B A G HOUS E DJFF.PR . PROP
. =<2"W C O R *10"W C 1M1 N avg . 0083 9 0041 6 y 

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### y 2 2 AWF C FLU E GA S HC L =*50 Q PP M 1M! N avg * 0089 4 0042 2 2 3 AWF C FLU E GA S FLO WRAT E 72 0 ACF M inst . 0D89 S DD42 3 y 7 4 - ••AWF C FLUE.GAS.QPAC1TY
. =>10 % 1MI N avg . 0069 7 0042 4 " V AWF C L O WCHAMBE R TEMP . <i 6.1 7 deg . F 1K R railin g svg . 0066 2 0042 5 AWF C LOWE R CHAMBE R PRES S ->-A" wefot 5 see s 0OSS 4 0042 6 y 2 7 AWF C UPPE R CHAMBE R PRES S =>-.V wefo r5 see s 00SS 5 0042 7 y 2 3 AWF C FAILE R O F PROCES S MONITO R LOS S O F SIGNA L D06B4 0042 6 2 9 AWF C I D FA N FAILUR E LO R I ? D F in FAN M CONTAC TO R VIH > 5 M M ooee a QQ42 9 y 3 0 AWF C UC/L C TEMPS , • TEMPERATUR E > 240 0 DEG , F 0160 0 0043 0 y 3 2 MWF C A L LWAST E FEE D OF F FRO M FI X W F SHUTDOW N MANUALL YFRO M FI X 0063 0 0043 2 y 3 5 MWF C FLU E GA S HC L =>5 Q PP M 1H R rollin g avg . 0087 8 O043 5 y 5 6 MWF C HEA TEN PU T =>15.5 MBTU/H R anticipate d 0088 0 D043 6 y 3 7 MWF C CHLORIN E INPU T =>23 3 Ibs/H R 0038 1 0043 7 y 3 8 \JWF C E-STOP S orT/ C MODUL E E-STO P & T/ C MODUL E inactiv e CQ8S 9 0043 3 y 3 9 MWF C FLU E GA S C O =>5 0 PP M iH R tollin g avg . 0089 1 0043 9 y 4 0 MWF C ATOMIZE R HI-H I Vibratio n sv/
. >Q rninute s 0085 2 0044 0 y / 4 1 SWF C SPEC
. FEE D ==>724#/H R EXCEEDE D 0DB6 3 0044 1



### • * iBIWEEKL YUNIT# 3

COMPLIANC E CHEC KSHEE T =dt * *•=== = OPERATIN G PARAMETER S {CM S Tas k [C I 033 )
PL C COI L13

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. B 6 B 7 8 8 HIRT U

LODT U HLBT U (se e not e 1 ) LOBT U (se e not e 1 ) SPECIALIT YFEE D =>2Q12*H R EXCEEDE D =>1993fflH R EXCEEDE D LOS S O F SIGNA L LOS S O F SIGNA L LOS S O F SIGNA L NORT H & SOUTH IP S ALAKM S FA5LE D C&MrfflJllKWTKW B 

### TIME D ou r

### FO R BOT H NORT H a SO U f H IP S SERVER S FAILE D COMMUNICATION'S TIME D OUrFOF L GOT H DIREC TINJEC TCOMMO N ALAR M Ba g Leaf cDetectio n Syste m (Tribe ) Pumpabl e 1 Hou rRollin g Tota l OP L Non-Pumpabl e fHou rRollin g Tota l OP L. Tota l wast e 1 I lou rRollin g Tota l OP L CL1 2 Hou rRollin g Tota l OP L Lavt Volatil e 1 2 Hou rRollin g Tota l OP L Semi
. Volatil e 1 2 Hou rRollin g Tota l OP L Mercur y1 2 Hou rRollin g Tota l OP L As h 1 2 Hou rRollin g Tota l OP L P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L S C C Temperatur e 1 Hou rRolling-Averag e Lo wOP L S D AOutle t Temperatur e 1 Hou rRollin g Averag e Hig h OP L Baghous e Differentia l Pressur e 1 Mfnut e Averag o Lo wOP L Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L ...fitadt.aCL.CD3lsctsd..i.H.BiJf..Rolling
. Averag e Hig h OP L Stac k C O Correcte d 1 Hou rRollin g Averag e Hlu h OP L Stac k Flo w1 Hou rRollin g Averag e Hig h OP L BT U 1 Hou rTota l OP L Hi t Cl/Hr a Lim e Fla w1 Minut e Averag e Hig h OP L Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTUflj J (D O NORT H TAN KFARM , BIWEEKL YCHECKS ) Hlro l Atomizin g Ai rLo wPressur e alar m (manua l check ) Lo/D I Atomizin g Ai rLo wPressur e alar m (manua l check ) Specialt yFeede rAtomizin g Ai rLo wPressur e alar m (manua l cheek ) 0096 5 0096 7 0301 0 0302 0 0302 1 0570 3 0570 5 0313 2 0S20 5 08Z0 6 0320 3 0821 1 0821 4 0821 6 0821 8 0822 0 0822 2 0622 4 0S22 6 0B2Z 7 0322 9 0823 2 '''0823 6 0824 4 0824 4 0825 1 0315 S 0044 2

0044 3 0044 5 0044 6 0044 7 0044 B 0045 0 0045 1 0411 3 0411 4 0411 5
' 0411 6 0411 7 0411 8 0411 0 0412 0 0412 1 0412 2 C412 3 0412 4 0412 $ 0412 6 ''04127' ' 0412 B D412 9 0413 0 0413 2 

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Comment s

CHECKE D BY : DATE : 

## A>-/V-B' ? TtME : / A M (P M P^WED : 

## J^g&L?^ far* PLACE : Contro l Roo m b,^-EEKLY_ 3 W 0 7 HK .BJWEEKL Yliff f# 3 (CM S Tas k EC4039 ) PAG F 1 O F
OPERATIN G PARAMETER S PL C COI L B WCOI L PAS S
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## V F 3 OC L FLU E GA S HC L >10T J PP M 1H R Rollin g avg . 0037 1 0040 6 is"
_ 

## 7 OC L FLU E GA S C O >10 0 PP M 1H R Rollin g avg . 0087 2 0040 7 8 OC L FLU E GA S OPACIT Y =>30 % fo r48 0 SecJHr
. 0087. 3 C04O B . 

## 5 O C L FLU E GA S OPACIT Y =>60 % Instantaneou s 0067 4 0040 9 . 

## s .1 0 OC L FLO E GA S FLO WRAT E >17,19 8 ACF M for> 1 MIN . 0Q&7 5 0041 0 1 1 O C L HEA T[NPU T =>1 G M BTU/H R 003G 5 0041 1 

### s 1 2 O C L CHLORIN E INPU T >21 7 Ibs/H R GOSB O 0041 2 1 3 O C L SOLI P FEE D #/H R MA X f=>l04 1 #/H R 00SB O 0041 3 / ' 1 4 OC L UPPE R CHAMBE R TEMP . < \ 84 5 DEGF 1 I R ROLLIN G AV G oafsa s 0041 4 1 5 OC L SPECIALIT YFEEDE D #/H R MA X ->50BWH R 0085 2 0041 5 

## r 1 7 AWF C SDAO U llfTTEMP
. >50 0 dog . F 1 MI N avg . 0068 7 0041 7 

### / 1 8 AWF C B A G HOUS E DiFF.Pft
. DROP
. =<2"WCOR=>10"W C 1 MI N avg . 0DBC S 0041 3 1 9 AWF C FLU E GA S C O =>50Q PP M 1MI N avg . 0QSB O 0041 9 2 0 AWF C FLU E GA S 0 2 -=<3 % 1M1 H avg . 0039 2 0042 0 2 1 AWF C FLU E GA S H C =>10PP M 1 MI N avg ; 0089 3 0042 1 

## s ' 2 2 AWF C FLU E GA S HC L =*500PPM1MINaV£ . • 0089 4 0042 2 

## / 2 3 AWF C FLU E GA S FLO WRAT E => , 72 0 ACF M mst . 0059 5 • 0042 3 

### C

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. 0042 4
- 4 AWF C LO WCHAMBE R TEMP . <1Sl7deg
. F VAR rollin g avg . 00S3 2 00425 ' 

## r •AWF C LOWE R CHAMBE R PRES S =;>-.1 " wefo f5 see s 0Q3B 4 0042 6 2 7 AWF C UPPE R CHAMBE R PRES S =>-.1"wcfo r5 see s 0089 5 0042 7 2 S AWF C FAILE R O F PROCES S MONITO R LOS S O F SIGNA L 0086 4 0O42 B 

## y 2 9 AWF C I D FA N FAILUR E LOS S O P I E FA N M CONTACT0RV|Q>5H W 0066 3 0042 9 

## •s 3 0 AWF C UC/L C TEMPS , TEMPERATUR E > 240 0 DEG
. F 0160 0 0043 0 

### / 3 2 MWF C A L LWAST E FEE D OF F FRO M FI X W F SHUTDOW N MANUALL YFRO M FI X 0068 0 0043 2 

## / 3 5 MWF C FLU E GA S HC L =^5 0 PP M 1H R rolling avg . oo&7 a 0043 5 3 e MWF C HEA TINPU T =»15. 5 MBTU/H R anticipate d QD8B 0 0043 6 

## •r 3 7 MWF C CHLORIN E INPU T =>23 3 Ibs^H R 0083 1 0043 7 

## s 3 8 MWF C E-STOP S orT/ C MODUL E E-STO F & TIC MODUL E Inactiv e 0089 0 0043 3 

## f 3 9 MWF C FLU E GA S C O ->50 PPM 1H R rollin g avg . 0089 1 0043 9 

## X. 4 0 MWF C ATOMIZE R HE-H i "Vibratio n sw . > 5 minute s 0066 2 0044 0 

# '* AA SWF C SPEC , FEE D 

## *>724#fHR EXCEEDE D 0096 3 0044 1 

## /BIWr-EKLYUNlr# 3 [CM S Tas k PACtd 2 0F 2
OPERATIN G PARAMETER S PL C COI L BWCOI L• PAS S 4 2 SWF C HIBT U =>2012#H R EXCEEDE D 0006 5 0044 2 

### X, 4 3 SWF C LOBT U =>1$93*H R IrXCEEDE D 0096 7 0044 3 

### / 4 5 SWF C HiBTL f(se e not e 1 ) LOS S O F SIGNA L 0301 9 O044! 5 

## X 4 0 SWF C LOBT U {se e not e 1 ) LOS S O F SIGNA L 0302 0 0044 6 

### / 4 7 SWF C SPECIALIT YFEE D LOS S O F SIGNA L 0302 1 0044 7 

## X 4 6 MWF C WORT H 6 . SOUT H IP S ALARM S FASLE D CQumWbTi^'STir/zfrwrFaRncmt 0570 3 0044 8 / 5 0 MWF C WORT H a som H ir s SERVER S PAH-E D COMMUUICATIDHSTIM C L I ciurFD R BOT H 0570 5 0045 0 

## x 5 1 SWF C DIREC TINJEC TCOMMO N ALAR M 0313 2 0045 1 

## x 5 2 O P L Ba g Lea k Detectio n Syste m (Tribo ) 

## X 6 5 O P L Pumpabl e 1 Hou rRollin g Tota l OP L D82Q 5 0411 3 • 6 6 O P L Non-Pumpabl e 1 Hou rRollin g Tota l OP L 0411 4 "6 7 O P L Tola ! wast e 1 Hou rRollin g Tota l OP L 0620 8 0411 5 s~ 6 3 O P L CL1 2 ffourRcllfn g Tota l OP L 0821 1 0411 8 s6 0 O P L Lo wVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 .X 7 0 O P L Semi
. Voiatil o 1 2 Hou rRcKIn g Tota l OP L 0821 6 0411 8 

## X 7 1 O P L Mercur y1 2 Hou rRollin g Tota l OP L 0821 6 0411 9 

## X 7 2 O P L As h 1 2 Hou rRoilin g Tota l OP L 0822 0 0412 0 

## X 7 3 O P L P C C Temperatur e 1 Hou rRollin g Averag e Le wOP L 0822 2 0412 1 

## X 7 4 O P L S C C Temperatur e 1 Hou rRoIETng Averag e Lo wOP L 0822 4 0412 2 

## X 7 5 O P L SD AOutle t Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 

### / 7 G O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOP L 0622 7 0412 4 

## X 7 7 O P L Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L 0322 3 0412 3 

### /

. ...DE L .Stac k

HC LCorrecte d 1 Hou rRollin g Averag e Hig h OP L 0323 2 0412 6 

## X y ' ' " \OP L Stac k C O Correcte d 1 Hou rRoilin g Averag e Hig h OP L 0923 5 0412 7 

## x "v . O P L Stac k Ro w1 Hou rRollin g Averag e Hig h OPl
. 0324 4 0412 8 

## X G 1 O P L BT U 1 Hou rTota l OP L 0824 4 0412 9 

## X 8 2 OPL
. Hr tCVtfra Lim a Flo w1 Minut e Averag e Hig h OP L 0825 1 ' 0413 0 

## X 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0815 S 0413 2 

## X 8 4 WIL LNO TACCEP TSOLI D CHARGE S ^75 0 KBTU/L B 

## X 8 5 (O O NORT H TAN KFARM , BIWEEKL YCHECKS ) -S 6 HifD l Atomizin g Ai rLo wPressur e alar m (manua l chock ) 

## y 8 7 LoflU l Atomizin g Ai rLo wPressur e aJar m (manua l check ) 

## y 8 8 SpeciaK yFeede rAtomizin g Ai rL wPressur e alar m (manua l cheek ) 

## X* O C L ^CONDITIO N UMI T AWF C -AUTOMATI C WAST E FEE D CUTOF F MWF C =M1S C WAST E FEE D CUTOF F SWF C ^SPECIFI C WAST E FEE O CUTOF F

Comment s

CHECKE D BY ; APT-WED : r '• u •••. i E L ' ^-EKLY^ a 4/4/0 7 l-i K 

### DATE : tQ-ZOr-Df
. mB 

### . g}<f y PLACE : Contro l Roo mB I WEEKL YUNI T# 3

^MPLIANCt i CHEC KSHEE T (CM S Tas k | C4039 ) PA G E 1 O F 2
OPERATIN G PARAMETER S PL C COt LB WCOI L 

### FAIL 1 O C L T R VPOSITIO N Ca p Ope n • 0079 1 0040 1 2 C3C L UPPE R C I EAMBERTfrMP
. <179 4 fori MI N AV G 00B6 7 0O40 2 3 O C L I \

\ #/H R MA X =i*82 S *H R 0006 4 0040 3 4 O C L LOWE R CHAMBE R TF.MP . <l590for1M1NAV( 5 00B6 0 0040 4 5 O C L L O BT U #/H R MA X kW22#/HR 0096 6 D040 5 e O C L FLU E GA S HC L >10 0 PP M 1H R Rollin g avg . 00&7 1 G040 B 7 O C L FLU E CA S C O MO O PPM.1H R Rollin g avg . 0087 2 0040 7 8 O C L FLU E GA S OPACIT Y =>30%for4SOSecJHr
. 0037 3 0040 6 9 O C L FLU E GA S OPACIT Y =>6Q % instantaneou s D087 4 0040 9 .1 0 O C L FLO E CA S FLO WRAT E >17, 1 S 3 ACF M for> 1 MIN , 0087 5 0041 0 11 . O C L HEA TINPU T =s>1 6 MBTU/HR
. 0036 5 0041 1 1 2 O C L CHLORIN E INPU T >21 7 Ibs/I-I R •00B6 0 0041 2 1 3 O C L SOLI D FEE D MI R MA X =*>104 1 S/H R OOOfi O 0041 3 1 4 O C L UPPE R CHAMBE R TEMP . <1H45-DEG F H R ROLLIN G AV G 00B3 3 D041 4 1 5 O C L SPECIALIT YFEEDE D &H R MA X ->60SS/H R C09B 2 0041 5 1 7 AWF C SD AOUTLA YTEMP . >5Dflceg
. F 1 MI N avg . 0088 7 0041 7 1 8 AWF C B A G HOUS E DIFF.PR . DROP
. *<2"W C O R =>10"W C 1MI N avg . 0068 9 0041 8 1 9 AWF C FLUEGASC O ^>500 PP M 1 MI N avg . 0089 0 0041 9 2 0 AWF C FLU E GA S 07 . -<3 % 1MI N &<sg. 0089 2 0042 0 2 1 AWF C FLU E GA S H C =M0PPM1MINavg . 0089 3 0042 1 2 2 AWF C FLU E GA S HC L =^50 0 PP M 1 MI N avg . 0080 4 0042 2 AWF C FLU E GA S FLO WRAT E => , 72 0 ACF M Tnat . 0080 5 0042 3 XT " ...AWF C ELUEGAS.DPACtrY
. =H0 % IMlNavg . 0080 7 0042 4 AWF C L O WCHAMBE R TEMP . . <1.61 7 deg . F1H R rolling avg . 0039 2 0042 5 AWF C LOWE R CHAMBE R PRES S ->-.1"wcfo f5 see s 0088 4 0042 6 2 7 AWF C UPPE R CHAMBE R PRES S =s>-1"wcfo r5 see s 0088 5 0042 7 2 3 AWF C FAILE R O F PROCES S MONITO R LOS S O F SIGNA L O0BG 4 0042 8 2 9 AWF C I D FA N FAILUR E 

### LPS S C F I D 

### FM J M coimc f

### O H va => E 

### MI N 0D8G 3 0042 0 3 0 AWF C UC/L C TEMPS
. TEMPERATUR E > 240 0 DEG , F 0160 0 D043 0 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X W F SHUTDOW N MANUALL YFRO M FI X 00650 ' 0043 2 3 5 MWF C ' FLU E GA S HC L s=>5 0 PP M 1H R rollin g avg . 0087 0 0043 5 3 6 MWF C HEA TINPU T• =*>1$. $ MBTU/H R anticipate d 0083 0 0043 5 3 7 MWF C CHLORIN E INPU T ~>23 3 Ibs/H R • 0088 1 0043 7 3 B IWVF C E-STOP S o rT7 C MODUL E &STO P & T/ C MODUL E inactiv e 0089 9 0043 8 3 9 MWF C FLU E GA S C O =>5 0 PP M 1H R roilin g avg . 0069 1 0043 3 4 0 MWF C ATOMIZE R HI-H I Vibratio n sw . >5 minute s 0066 2 0044 0 4 1 SWF C SPEC
. FEE D ==>724*i4 R EXCEEDE D 0095 3 0044 1 

### zzr 

## y 

# y

y L 

## yL\

~y~ 

# 5n I WEEKL YUNI T# 3 COMP J .IANC E CHEC K3HE E f (.CM S Tas k 1C4039 ) PAC E 2 C F 2

4 2 4 3 4 5 4 6 4 7 4 8 5 0 5 1 5 2 6 5 G O D 7 e a 7 0 7 1 7 2 7 3 7 4 7 5 7 6 7 7

6 1 6 2 6 3 S 4 B 5

-. S 6 87 =>2012iWU KEXCEEDE D =>1993/HH R EXCEEDE D LOS S O F SIGNA L LOS S O F SIGNA L LOS S O F SIGNA L OPERATIN G PARAMETER S SWF C HIBT U SWF C LOBT U SWF C HIBT U (se e not e 1 ) SWF C LOBT U {se e not e 1 } SWF C SPECIALIT YFEE D MWF C NORT H i-SOUT H fF 5 ALARM S FAILE D C0MMUMWTiQN , a 'iMKiJ0 , J rFO R Ber n i MWF C MONT H & SOUT H IP S SERVER S FAILE D COMMtJNlDVnON' 5 TMt0 OUrFORLDT K SWF C DIREC TINJEC TCOMMO N ALAR M OP LHa g Leak , Detectio n Syste m (Tribe ) OP LPumpabl e 1 Hou rRollin g Tota i OP L OP LNon-Pumpabf e 1 Hou rRollin g Tota l OP L OP LTota l wasst o 1 Hou rRollin g Tota l OP L OP LCL1 2 Hou rRollin g Tota l OP L OP LLo wVolatil e 1 2 Hou rRolfin g Tota l OP L OP LSemi
. Volatil e 1 2 Hou rRollin g Tota l O P L OP LMercur y1 2 Hou rRollin g Tota l OP L OP LAs h 1 2 Hou rRollin g Tota l OP L OP LPC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L OP LSC C Temperatur e 1 Hou rRollin g Averag e Lo« rOP L OP LSD AOutle tTemperatur e - 1 Hou rRollin g Averag e Hig h OP L OP LBagboits e Differentia l Pressur e 1 Minut e Averag e Lo wOP L O P LBaghous e Dffferentia l Pressur e t Minut e Averag e Hig h OP L

. . OP LStackJICL.Cone ^ Averag e Hig h OP L OP LStac k

C O Correcte d 1 Hou rRollin g Averag e Hiu h OP L OP LStac k

Flo w1 Hou rRollin g Averag e Hig h OP L OP LBT U 1 Hou rTota l OP L OP LKr tCE/Hr a Lim e Flo w1 Minut e Averag e Hig h OP L AWF C Lim e Slurr yDensit y1 Hou rRoRino . Averag e Lo w

WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTUAJ B (D O NORT H TAN KFARM ; BIWEEKL YCHECKS ) Hi/D 3 Atomizin g Ai rLo wPressur e alar m .(manua l check ) Lo/D I Atomizin g Ai rLo wPressur e alar m (manua l check ) Speciall yFeede rAtomizin g Ai rLo wPressur e alar m (manua l cheek) ' PL C COI LDWCOI L 0096 5 D096 7 0301 9 0302 0 0302 1 0570 3 0570 5 0313 2 0B2D 5 0320 6 0820 5 0821 1 0821 4 0621 6 0821 8 0B22 Q 0322 2 0322 4 0322 © 0322 7 0322 8 0823 2 '0823 6 0824 4 0824 4 DS25 1 0044 2

0044 3 0044 5 0044 6 0044 7 0044 3 004S Q 0045 1 PAS S FAI L

OC L=CONDmO N UMF T AWF C ^AUTOMATI C WAST E FEfc D CUTOF F MWF C -MIS C WAST E FEE D CUTOF F SWF C =SPEClH C WAST E FEE D CUTOF F

Comment s

CHECKE D BY : ftfihVL- DATE : 

### W^ZS^H TIME' : 

### $? )2*\ Cg > M | p ;^OVED : ^//aA /^ZC J(^fr*

PLACE : Contro l Roo m b . :dEKLY_ 3 4/4/071-I KB i WEEKL YU N I Tm

^OMPLIANC R CHECKSHTn T
•.. . '.' > OPERATING ' PARAMETER S (CM S Tas k 1C4030 ) PA R t l \ O F
P L C COI LBWCOi L 1 OC L TR VPOSITIO N Ca p Ope n 0079 1 0040 1 2 OC L UPPE R CHAMBTi R TEMP . <l734fD /1MINAV G 00BS 7 004O 2 3 OC L M l BT U S/HRMA X =>82BffiflH R 0D96 4 0040 3 4 OC L LOWE R CHAMBE R TEMP , <l590for1ML N AV G 0086 3 0040 4 5 OC L L O BT U #JH R MA X -1B22#/H R 0096 6 0040 5 C OC L FLU E GA S HC L H00PPM1H R Rollin s avg . 0087 1 0040 6 7 OC L ' FLU E GA S C O >-100FFM1H R Roilinnavg . 0087 2 0040 7 8 OC L FLU E GA S OPACIT Y *>30 % for 43 0 SecJJlr
. 0087 3 0040 8 9 OCI
. FLU E GA S OPACIT Y ^>60 % instantaneou s 0087 4 0040 9 1 0 OC L FLU E GA S FLO WRAT H >\7, 1& 3 ACF M fo r> 1 MIN . 0037 5 0041 O 1 1 O C L HEA TINPU T ^ 1 6 MBTU/H R 0036 5 0041 1 1 2 O C L CHLORIN E IMPU T >217lbs/ll K 0030 0 0041 2 1 3 OC L SOLI D FEE D WH R MA X =>104 1 Ml R .0006 0 0041 3 1 4 OC L UPPE R C1-IAME3E R TEMP . <1B4 5 DEG F H R ROLLIN G AV G 0038 3 (1041 4 1 5 O C L SPFXIALIT YFEEDE D #/H R MA X =:>S0B#/H R 0096 2 0041 5 1 7 AWF C SD AOUTLE TTEMP . ^50 0 rfeg. F 1MI N avg . 0088 7 0041 7 1 6 AWF C BA G HOUS E DIFF.FR . DROP
. =<2"W C O R =>10"W C 1MI N avg . 0088 9 0041 8 1 9 AWF C FLU E GA S C O *=>50 0 PP M 1 MI N avg . 0089 0 0D41 9 2 0 AWF C FLUE : GA S 0 2 -<3 % 1MI N ai/g
. 0089 2 0042 0 2 1 AWF C FLU E GA S H C *s>1 0 PP M 1MI N avg . 0069 3 •0042 1 2 2 AWF C FLU E GA S HC L =>50 0 PP M 1M1 N fevg. 0OB9 4 . 0042 2 2 3 AWF C FLU E GA S FLO WRAT E 72 0 ACF M ins L 0039 5 0042 3 ...AWF C FLUE.QAS..QPAC.ITY
. =>10 % 1 MI N avg . 0039 7 0042 4 AWF C LO WCHAMBE R TEMP , <161 7 deg . F1H R rollin g avg . 0033 2 0042 5

. y AWF C LOWE R CHAMBE R PRES S =>-.! " w c for 5 see s 0088 4 0042 6 2 7 AWF C UPPE R CHAMBE R PRES S =>-.1''wefo r5 see s 0088 6 0042 7 23 AWF C FAILE R O F PROCES S MONITO R LOS S O F SIGNA L 0086 4 0042 8 2 9 AWF C I D FA N FAILUR E LOS S 0t 1 0 FA N M CONTACt ' O R WE S > S MIN 0086 3 0Q42 9 3 D AWF C UC/L C TEMPS
. TEMPERATUR E > 24D 0 DEG
. F 0160 0 0043 0 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X W F SHUTCOW N MA N LfALL YFRO M FJ X ooea o 0043 2 3 5 • •MWF C FLU E GA S HC L =>5 0 PP M 1 H R rnlling avg . Q087 B 0043 5 3 6 MWF C HEA TINPU T =>15. S MBTU/H R anticipate d 0033 0 0043 6 3 7 MWF C CHLORIN E INPU T =>23 3 Ibs/H R 00B8 1 0043 7 3 8 MWF C E-STOP S orT/ C MODUL E E-STO P a T/ C MODUL E Inactiv e 0089 9 0G43 B 3 9 MWF C FLU E GA S C O P P M 1H R collin g avg . 0089 1 0043 9 4 0 MWF C ATOMIZE R Hl-H i VibTaHio h aw . >5 rninute s 0086 2 0044 0 4 1 SWF C SPEC
. FEE D =>724#/H R EXCEEDE D 0096 3 0044 1 PAS S



# - y 

# 1 I I IkBIWEEKL YUNI Tm

I COJWPLJANC E CHEC KSJIB ^ (CM S Tas k 104038 ) PAC E 2 O F 2
P L C COI LB WCOI LPAS S AZ SWF C 4 3 SWF C 4 5 SWF C 4 6 SWF C 4 7 SWF C 4 3 MWF C 5 0 MWF C 5 1 SWF C 5 2 OP L 6 5 . OP L S S OP L 6 7 OP L 6 8OP L 6 9 OP L 7 0 OPI 7 1 OP L 7 2 OP L 7 3 OP L 7 4 OP L 7 5 OP L 7 6 OP L 7 7 OP L O P L
; T ' \ OP L i OP L 5 1 DE L 8 2 OP L 8 3 AWF C 8 4 . B 5

. 3 6 3 7

O C L AWF C MWF C SWF C =>2012J!yi-t R EXCEEDE D =-1&93ff/H R EXCEEDE D LOS S O F SIGNA L LOS S O F SIGNA L LOS S O F SIGNA L O0SG 5 0UH6 7 0301 9 0302 0 0302 1 0570 3 0570 5 0313 2 0020 5 0820 6 0820 8 0821 1 0321 4 0621 6 DS21 S 0322 0 0322 2 0822 4 0822 6 0B22 7 0B22 B 0S23 2 "03238 " 0324 4 0824 4 0825 1 0615 6 0044 2

0044 3 0044 5 0044 6 0044 7 QQ44 8 0045 0 0045 1 0411 3 0411 4 0411 5 0411 6 0411 7 0411 5 0411 9 0412 0 0412 1 0412 2 0412 3 0412 4 0412 5 0412 6 ''04127* ' 0412 8 0412 9 0413 0 0413 2 

### e x



## "77" 

# \y T7~ ±XL OPERATIN G PARAMETER S HEUT U LOBT U H I BT U (se e not e 1 ) LOtfi' U (se e not e 1 } SPECIALIT YFEE D NORT H &

. SOUT H IP S ALARM S FAILE D cohaiUNlCATioN'siiMiji^ DirrnoRBorr

t NORT H &SOUT H Wt. SERVER S FAILE D COMMUNICATION' S 11MB ! niJTFORBOrc H DIREC TINJEC TCOMMO N ALAR M Ba g Lea k

Detectio n Syste m (Tribo ) Pctuipablt s 1 Hou rRollin g Tota l OP L Non-Pumpabf e | Hou rRollin g Tota l OP L T'ofa l wast e 1 Hou rRollin g Tota l OP L CL1 2 Hou rRollin g Tota l OP L Le wVolatil e 1 2 Hou rRollin g Tota l OP L Semi
. Volatil e 1 2 Hou rRollin g Tota l OP L Mercur y1 2 Hou rRollin g Tota l OP L As h 1 2 Hou rRollin g Tota l OP L P C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L S C C Temperatur e 1 Hou rRollin g Averag e Lo wOP L SD AOutle t Temperatur e 1 HOE FRollin g Averag e Hig h OP L Baghous e Differentia l Pressur e 1 Minut e Averag e Lo wOP L Baghous e Differenlia ! Pressur e 1 Minut e Averag e Hig h OP L 

### JSaaiLti^Csest^^Xii^^Mm Averag e Hig h OP L Stac k C O Correcte d 1 Hou rRollin g Averag e Hig h OP L Stac k Rov/ 1 Hou rRollin g Averag e Hig h OP L BT U 1 Hou rTota l OP L Hr tCl/Hr a Lim e FID W1 Minut e Averag e Hig h OP L Llrn e Slurr yDensft y1 Hou rRollin g Averag e Lo w WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTUA. B (D O NORT H TAN KFARM , BIWEEKL YCHECKS ) HiVD I Atomran g Ai rLo wPressur e alar m (manua l check ) Lo/D I Atomran g Ai rLo wPressur e alar m (manua l check ) Specialt yFeede rAtomizin g ATrLa wPressur e alar m (manua l cheek ) CONDITIO N LIMI T =ALTrOMATl C WAST E FEE D CUTOF F =MIS C WAST E FEE D CUTOF F =SPEC1FI C WAST E FEE D CUTOF F
Cement s 

### 'SCfr Ul^f[0SJ£ \

DOm r&tl 

# Jji

ftJ O
. 

### IOT A FAI L



### 17



# ~7> 

# i f

• 1 £
CHECKE D B Y AC-^PVED ; $ • ' Y-.,EEKLY_3 ' 4/4/0 7 H K 

### \y

DATE ; 

### //"//H P



# 9TIME : 

### <g ! 

### 3S^

M J M PLACE : Contro l Roo m

## ABSOLUT E CALIBRATIO N AUDI T{ACA J UAI A SHfcf c \


## Uni t# Seria l # . COS A 

## Paramete r > 0 2 25 % 

## r CO-lo wrang e 200pp m 

## rCO-hig h rang e 3000pp m r HC l IGOOpp m 

## NIS TTraceabl e Calibratio n Standard s Paramete r > 0 2 25 % 

## r CO-lo wrang e 200pp m 

## rCO-hig h rang e 3000pp m r HC l IGOOpp m 

## Ga s Concentratio n 

## Paramete r > 0 2 25 % 

## r CO-lo wrang e 200pp m 

## rCO-hig h rang e 3000pp m r HC l IGOOpp m Low[Zero ) 

## 0 

# + 0. 5 Paramete r > 0 2 25 % 

## r CO-lo wrang e 200pp m 

## rCO-hig h rang e 3000pp m r HC l IGOOpp m Mi d 

## 8.9 3 

# ± 0,

5 Paramete r > 0 2 25 % 

## r CO-lo wrang e 200pp m 

## rCO-hig h rang e 3000pp m r HC l IGOOpp m 

## High • 1 5 

# ± 0. 5
Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w •Mi d • Hig h 1-Lo w 0 0. 2 

## -0.2 — — 

## 2-Mi d • 8.9 3 6,S B 0.0 5 15 15, 1 — 

### -0. 1 4-Lo w 0 D. 2 -0. 2 — — 

### 5 M d . 8.9 3 3.3 3 — 

### 0. 1 — 

## 6-Hig h t s • 15. 1 — 

### -0. 1 7-Lo w 0 0. 2 -0, 2 — 

### 8-Ml d 3.9 3 8,8 3 — 

### 0. 1 9-Hig h 1 5 1 5 — 

### 0 Mea n Differenc e - Calibratio n Erro r= -0.2 0 

## o.o a -0,0 7 Mea n Differenc e - Calibratio n Erro r= -0.80 % 0,33 % •-0.27 % .Calibratio n Erro r= Mea n Differenc e / Spa n Valu e * 10 0 

## Bil l Adam s Nam e 

# Has atfa Signature 

## E/fTec h Titl e 

## 9/23/200 9 2/4/2Q1 0 Date

## ABSOLUT E CALIBRATION AUDI T(ACA ) DATASHEE T

Uni t# 

## Seria l # 15 4 

## Paramete r r 0 2 25 %

'** CCMo wrang e 200pp m 

## r CO-hig h range 3000pp m r HC E 1000pp m MS TTraceabl e Calibratio n Standard s Paramete r r 0 2 25 %

'** CCMo wrang e 200pp m 

## r CO-hig h range 3000pp m r HC E 1000pp m Ga s Concentratio n Paramete r r 0 2 25 %

'** CCMo wrang e 200pp m 

## r CO-hig h range 3000pp m r HC E 1000pp m Low[Zero] 0 

# ± 1 0 

## Paramete r r 0 2 25 %

'** CCMo wrang e 200pp m 

## r CO-hig h range 3000pp m r HC E 1000pp m Mi d 68. 9 

# ± 10 ' 

## Paramete r r 0 2 25 %

'** CCMo wrang e 200pp m 

## r CO-hig h range 3000pp m r HC E 1000pp m Hig h 15 2 1 0 

### Ru n Numbe r Concentratio n Differenc e



## Referenc e Analyze r Low Mi d 

## High . 1-Lo w 0 0, 8 • ^O. B — 

### 2-Mi d 69. 9 73. 3 — 

### 4. 4 — 

### 3-Hig h 15 2 152. 9 — — 

### 4-Lo w 0 

## 1 - 1 — 

### 5-Mi d . 6B. 9 

### 72. 1 — 

### -3. 2 — 

### 6-Hig h 152 

### 148, 3 — 

### 3. 7 7-Lo w 0 -0. 3 0. 3 — 

### 8-Ml d 68. 3 71, 6 -2. 7 — 

## 9-Hsg h 15

2 

### 148, 1 — — 

### 3. 9 Mea n Differenc e = 

## Calibration Erro r- -0,5 0 -3.4 3 2.2 3 Mea n Differenc e = 

## Calibration Erro r- -0,25 % -1.72 % 

## 1.12 % Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 100 

## Bil l Adam s E/ l Tec h Nam e 

# •R/ AJ a Aart Signatur e Titl e 

## 9/23/200 9 2/4/201 0 Dat e

### ABSOL U t h UALIBK AJIU KAUU U (AUA J 

### ut\ i A

### onp c t


## Unit # Seria l # 15 4 

## Paramete r NIS T

## Traceabl e Calibratio n Standard s r 

## 0 2 25 % Ga s Concentratio n rCO-lo wrang e 

## 2D0pp m Lo w(Zero) 

## D 

# ± 15 0 i*' 

## CO-hig h rang e 

## 30Q0ppr n Mi d 

## 1079.1 

# ± 15 0 rHC I IDOOpp m Hig h 

## 228 3 

# ± IS

O

• 

### Run Numbe r Concentratio n Difference

Referenc e 

## Analyze r Low Mi d Hig h 

## 1-Lo w 0 

## 0.8 — — 

### 2-Mi d 1079. 1 1127. 1 •-4 8

— . 

### 3-Hig h 228 5 2237.5 . — 

### -2. 5 4-Lo w 0 0. 9 -0. 9 

## 5-M3 d . ' 1079. 1 1081, 6

—' 

### -2. 5

22S 5 2265. 1 — — 

### 19. 9 7-Lcw 0 -0. 3 0, 3 — 

### 8-Mi d ' 1079. 1 107S. 1 3 — 

## 9-Hig h 228 5 2252.4 - — — 

### 32, 6 Mea n Difference = -0.4 7 -15.8 3 16,6 7



### . Calibratio n Error- -0,02 % -0.53 % •0.56 % Calibratio n Erro r= Mea n Difference / Span Valu e * 10 0 

## Bil l Adam s E/ l TEC H .Nam e Titl e 

## 9/23/200 9 Signature 

### 2/4/201 0 Date

### AB5UL UI £ LAUBKA I iU NAUU ! I (AL-A J Urtlftoncc i


## Unit * J L . Seria l # Paramete r r 0 2 25 % f * CO-lo wrang e 200ppr n f CO-hig h rang e 3000pp m ^ HC l 10G0pp m NIS TTraceabl e Calibratio n Standard s Paramete r r 0 2 25 % f * CO-lo wrang e 200ppr n f CO-hig h rang e 3000pp m ^ HC l 10G0pp m Ga s Concentratio n Paramete r r 0 2 25 % f * CO-lo wrang e 200ppr n f CO-hig h rang e 3000pp m ^ HC l 10G0pp m Lo w(Zero ) 0 

# ± 5 0 

## Paramete r r 0 2 25 % f * CO-lo wrang e 200ppr n f CO-hig h rang e 3000pp m ^ HC l 10G0pp m Mid 31 B 

# ± 50 

## Paramete r r 0 2 25 % f * CO-lo wrang e 200ppr n f CO-hig h rang e 3000pp m ^ HC l 10G0pp m Hig h 730 

# ± 50 

### Ru n Numbe r .Concentratio n Difference

Referenc e Analyze r Low Mi d Hig h f-Lo w 0 0. 8 -0. 8 — — 

### 2-Ml d 31 8 326, 8 — — 

### 3-Hig h 73 0 742. 9 — 

## _ -12. 9 . 44.o w 0 0. 9 —



### 31 3 345. 2 — 

### -27. 2 • — 

### 6-Hig h 73 0 737. 9 — 

### -7. 9 7-Lo w 0 -0, 3 0. 3 — 

### 8-Mi d 31 8 353. 1 -35. 1 —



### 73 0 737, 1 — 

### -7. 1

Mea n Differenc e - -0.4 7 -23.7 0 -9,3 0 Caitbratio n Error = -0.05 % -2.37 % -0.93 % Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 10 0 

## Bil l Adam s Mam a 

## &JAJ Signatur e E/ITec h Title 9/23/200 9 Dat e 2/4/201 0Tahiti 1 

### Summar yo fRelativ e AccuracyTea

t Audi t Result

s Veoli a K S Teclinica l Solution s Saa^ct , Illinoi s Jnne 22, 2

3 an d 24,200

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### Pas s TJni t 2
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t 0.13%> a 

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### 1.

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### TW I INSTRUMEN T CALIBRATIO NRECOR D TAG : LOOP :

. DESCRIPON ; SERVICE : LOCATION ; LP-SST : P&ID : REMARKS ; IFTST L - RMKS : SPRC-EMKS : £/N : UlStt T # 4 QOARTERIx t P T 30 0 PRES S TRANS M Kim HOOD PTRNS P 30 0 F01 5 Rarange d 1/19/9 6 MODEL : SCALE : CALIB-BT : CALIB-OUT : PROCESS-SP : ROSEMOWT

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# T^mWSO ^Ws^^' ^ f f 

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./

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### After Calibration



### Comments : CA L IBRATj^Q NSOTTTfC E REFHRBMC E

Performe d hy : 

# lac k?foi

Data : 

# ff^P

-0 ? Time ; 

# S

*oV A M J B ' Place : , ^ _ CALSHEET.WEX B (Field or Shop)

### Tlf l INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y TAG : P T LOOP : 32 4 DESCRIPON : PRES S TRANS M SERVICE : SC C OUTLE T LOCATION : £T, D LP-SHT i 32 4 P&I D .REMARK S IHSTL-RMK S SPEC-RlflE S S/ N MAHUFAC T MODE L SCAL E CALIB-I N CALIB-OO T PROCESS-S B IMST-S P ACTIO N I/ O NUMBE R ROSEMONT

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CALIBRATIO NNOTE S US E PNEUMATI C CALIBRATIO NBENC H WIT H MANOMETE R AND LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AND REA D OUTPU T WIT H LOO P CALIBRATOR .

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### Comment s CALIBRATIO NSQURC B RKFEREKC B

Performe d b y J B CALSHEET.WD B Place: . (Field or Shop)

### TAG :

LOOP : DESCRIEQKT : SERVICE : LOCATION: - X.P-SHT : P&ID : REMARKS : INSTD-RMKS : SPEC-RMKS : S/N ; TU T INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y PD T 43 9 D P TRAN S BAGHOUS E PRESSTJE R WAP C 43 7 FO I 7 W/GA S CLEANIN GTRAI N NORTH/EAS T BAGHOUS E MAMUFACT : POXBOR O MODEL : 82 3 DP I SCALE : CALIB-IN : CALIB-OUT : PROCRSS-SP : INST-SP : ACTION : I/ O NUMBER : 0-15 " W C 4-2 0 MAD C

CALIBRATIO NNOTE S TJS E PNEUMATI C CALIBRATIO NBENC H WIT H MANOMETE R AN D LOO P CALIBRATOR , INPU T PNEUMATI C SIGNA L AM D REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READIN G

. Before Calibration

,
After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : 

## J/^/ M KJ^ Vatai£Lz£?-Qf Time:Q^- i _.£M)P M J B Place : . CALSHEET . WDB (Field or Shop)

### TAG : 1 

### LOOP : DEGCRIPOW : SERVICE : LOCATION : LP-SHT : P&ID ; REMARKS : INSTL-RMKS : SPEC-RMK S : S/N : TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y PD T 44 0 D P TRAN S BAGHOUS E PRESSDE R WAP C 43 7 P01 7 W/GAS CLEANIN GTRAI N 1TORTH / CENTRA L BAGHOUS E MANUFACT ; FOXBOR O MODEL : 02 3 DP I SCALE : CALIE-IN : 0-1S " W C CALIB-OUT : 4-2 0 MAD C PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : CALIBRATIO NNOTE S US S PWETJMATI C CALIBRATIO NBENC H WIT H MANOMETE R AN D LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e fo r detailed , instructions . Fil l cu t an d affi xa ne wcalibratio nsticker , 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T READIN G Before Calibration

«, ~_ a . _<l?9/* 4 , _ After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments : $ L

# Ch^/s bm,A ' CT

A



### Performe d by : 

# £/ft.eL&€ fan*

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# /^fa-Of

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Se e ManufacLure s literatur e fo r detaile dinstructions . Fil l ou t an d affii c a ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREPOR T INPU T -VALU

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CALIBRATIO NSOURC E REFERENC E

Comments :

=erforme d by : /f&>&/ J?/'**-. Date -Jf^/l-^ J Time* : 

### /*^gg L J B CALSHEET.WD B Place: . (Field or Shop) Pi "

### Tff I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y TAG : PD T

. LOOP : 44 2 • . ; i 

### ' DESCRIPOH : D P TRAS S MANUFACT : FOXBOR O SERVICE : BAGHOUS E PRSSSUE R MODEL : S2 3 DP I LOCATION : WAP-

C SCALE : LP-SHT : 4 3 7 , CALIB-IN : 0-15 " W C PS-ID : F01 7 CALIB-OOT : 4-2 0 MAD C REMARKS : W/GAS CLEANIN GTRAI NPROCESS-SP ? IHSTL-RMKS : SOUTH/EAS T BAGHOUS E INST-SP : SPEC-RMXS r ACTION : S/N : I/ O DUMBER :

. CADIBRRTIO NNOTE S US E PNEUMATI C CALIBRATIO NBENC H WIT H MANOMETE R AN D LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AND REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e fo r detaile dinstructions ! Fil l ou t an d affil e a ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO NREEOR T INPU T VALU E INSTRUMEN T READIN G Before Calibration

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### CALIBRATIO NSOURC E REFERENC E

Comments J

Performe d by ; jffa / nr. • Date:^/!- ^ Time : (t&k PM . J B Place : . CALSHEET,WD B (Field or Shop)

### TAG :

LOOP : '• • DESCEIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMRS : 

### SPEC-RMKS : S/N : TH I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y PD T 44 3 D P TRAN S BAGHOUS E PRESSUE R WAP C 4 3 7 

### F01 7 W/GAS CLEANIN GTRAI N SOUTH/CENTRA L BAGHOUS E MANUFACT : MODEL : SCALE ; CALIB-IN : CALIB-OTJT : FROCKSS-SP : INST-SP : ACTION" : I/ O NUMBER : EOXBOR O

82 3 DP I 0-15 " W

C 4-2 0 MAD C

US E PNEUMATI C CALIBRATIO NBENC H WIT H MANOMETE R AM ) LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r

INPU T VALU E INSTRUMEN T READIN G
A

### Before Calibration

^

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CALIBRATIO NSOURC E REFERENC E

Comments" : • 'A/n •cL&J. 

# (2 &yfi

forme d by : fhh*>

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82 3 DP I 0-15 " W

C 4-2 0 MAD C

CALIBRATIO NNOTE S US S PNEUMATI C CALIBRATIO NBENC H WIT H MANOMETE R AND LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D REA D OUTPU T WIT H LOO P CALIBRATOR .

Se e Manufacture s literatur e .fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . • O . l lb/h r CALIBRATIO NREPOR T INPU T VALU E i^STBOOnW^""^^^ ^ 

### Before Calibration n 

### X



### Afte r Calibration A 

## O <* /nA

CALIBRATIO NSOURC E REFERENC E

Performe d by : J?afcL&^. 

## Pftrj Date:/A/2-<?9



### Time : $>~3& 

### J B . " Place ; CALSHEET.WD B (Field or Shop) 

### P M

### TAG : LOO Pr ! 

### DESCRIPON ; SERVICE : LOCATION : LP-SHT : P&I D i REMARKS : INSTL-RMKS : SPBC-RMJC S : 

### TW I INSTRUMEN T r^ALIBRATtO NRECOR D UNI T # 4 QUARTERL Y WI T oo a 

### W T TRAN S SHREDDE D SOLID S FTRNS P I FO I 2 W/SOLID S FEE D SYSTE M S/N : E12S65900 A MANUFACT : MODEL : SCALE : CALIB-IN :

. CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : Nl: 5

TOLED O 814 0 0-3GQ0 # O-3QO0 # 4-2 0 MAD C

Chec k scale,.digita l Calibratio nper . Toled o instructions . The n wit hn o weigh t o n scal e adjus t analo g zero . {NOTE : HM I wil l no t displa ynumber s les s tha nzero ) . Nex t ad d weigh t = t o 10 & ar e mor e o f scale s range r

### the nadjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker , 0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E INSTRUMEN T

rf-. Before CaJ.jMra.tion 

### O . <~ > , After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments ;

Performe d by' : &UJTC"<JK/U^J$
. .. Pate : i(-£-Q ? Time : *V ; 

### 0 0 j&Mfp i J B CALSHEET « WDB R Place i fiel dhr Bhop)

### TH I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 QUARTERL Y TAG : WI T LOOP : 014 A ' DESCRIPOlf ; W

T TRAN S SERVICE : DRU

M EEE D LOCATION : FTRNS P LP-SET : P&ID : REMARKS' : W/DRU

M FEE D NEMATRO N INSTL-RMKS : SPEC-RMKS ; S/N : 42S01574N S MANUFACT : TOLED O MODEL : 814 0 SCALE : 0-1,00 0 lb . CALIB-IN : 0-1,00 0 lb . CALIB-OUT : 4-2 0 MAD C PROCESS-SP : INST-SP : ACTIOS : I/ O NUMBER : HI:3 5 CALIBRATION ; jgsre g Chec k scale , digita l Calibratio nper . Toled o instructions . Then , wit hn o weigh t o n scal e adjus t analo g zero . (NOTE : HM I wil l no t displa ynumber s les s tha nzero ) . Nex t ad d weigh t * t o 10 % ar e mor e o f scales
- range , the n adjus t analog
- span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r CALIBRATIO N REPOR T INPU T VALU E D. INSTRUMENT READIN G

Befor e Calibration. 

## SO Afte r Calibration

CALIBRATIO NSOURC E REFERENC E

Comments :
hxST , ^ 0 Date : /A (^Cf l Time : 

### 3\£ >

A M 6? ) Performe d by : J B CA L SHEET . WD

B 1 Place: . (Fieljd or Shop)

### TW I JIT S TRUMEH T CALIBRATIO NRECOR D TAG : " ' LOOP : • DESCRIPOW : SERVICE : LOCATION : LF-SET : P&TD : REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : UNI T # 4 QUARTERL Y WI T 014 B W T TRAN S AUX . DRU

M FTRNS P FEE D

HE WAUX DRU M FEE D MANUFACT : MODEL ; SCALE : CALIB-IN : CALEB-OUT : PROCESS-SP : TNST-SP : ACTIOS ; I/ O NUMBER : CALIBRATIO NNOTE S TOLEDO B14 0 O-200 # 0-200 # 4 - 3 0 MAD C

Chec k scale , digita l Calibratio nper , Toled o instructions . Ths n wit hn o weigh t o n scale
- adjust'analo g aero . (NOTE : HM I wil l no t displa ynumber s les s tha n 2 ;ero ) , . Nex t ad d weigh t = t o 10 % ar e mor e o f scale s range , the n adjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . Se e Manufacture s literatur e fo r detaile dinstruction s Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r

INPU T VALU E 

# O CALIBRATIO NREPOR T INSTRUMEN T READIE S

before Calibration

After Calibration 

# D s o

CALIBRATIO NSOURC E REFERENC E

Cotftmfint s

Performe d by: . CALSHEET.WD B Date: , Tim e : m 

### (p^ Place : . ({Field

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### TAG ;

v -LOOP : DESCRXPON : SERVICE : LOCATION ; LP-SET : p£TD ; REMARKS : JNETL-RMKS : SPEC-RMK S : S/KT r Tff I INSTRUMEN T C&LIBRATTO NRECOR D UNI T # 4 Q UARTERL Y S5UA 

### Trib o Baghous e Leak : Detection . FL D MANUFACT ; MODEL : SCALE : CALIB-IN : CALIB-OUT i PROCESS-SP : INST-SP : ACTION : I/ O NUMBER r CALIBRATIO NNOTE S Aubur n TRIBO.dg d 0-l00Op a 0-lDOOp a 4-20m a

Disconnect : th e inpu t cabl e a t th e BN C connecto r o n th e inpu t card , an d chec k fo r zero . Us e Auburn F

### Triboflow , file dtes t unit , mode l 2902 , t o inpu t a Pico-Am p signa l o f 500p a an d recor dthes e values .

0. 1 lb/h r . CftLlftKATIO NREPOR T INPU T VALU E INSTRUMEN T HEADIN G Befor e Calibration
After Calibration

CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : fitU 0(j ~ Date :it ^?Time : 9 J B Place : ^ ^ CALSHEET,WD E {iFiei§/6r Shop} P M

### „f£U 4 (1C4034 )

' • ^UAKFEJRL Y CARBO NINJECTIO NPREVENTIV E MAINTENANC E CHEC K SHEE T

1 Disconnec t A C Powe r t o th e Dig i Drive . 2 Inspec t A C & Moto r driv e scre wtermina l connection s fo r sign s o f wea r o r corrosio nan d chec k tha t the yar e tight . 3 Replac e th e tw o Dig l Driv e fuse s 4 Verif yan yexterna l safet yswitche s o r lockout s ar c stil l operatio n 5 Remov e Scre wfeede r cove r & blo wou t carbo n8 s dust . 6 Inspec t G ear s Ss Belt s fo r wea r o r damage . 7 Chec k Operatio no f Moto r & Gear s fo r abnorma l nois e o r movement . •& • Repiaee..aiiy...needed.p.&xl ^

COMMENT S ;

Name : Date://
- 6-t?1 Time : 3 » ? 3 A M0S.

QUARTER . 4 11/1/0 6 K F PAG EIO FI



### PAS S FAI L

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### TAG' :

•r% . LOOP : •'.• J DESCRIPON : SERVICE : LOCATION : LP-SHI : P&ID : REMARKS : INSTL-RMES : SPEC-RMKS ; S/N : TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 ANNUA L F T 12 9 FLOW TRM S PC C LO WGRAD E WDJ? X-1 0 P-BM S 12 9 E01 3 W/BMS 10149 9 MANUFACT : MODEL : SCALE : CALTB-IN : CALIB-OOT : PROCESS-SP : INST-SP ; ACTION : I/ O NUMBER : MICR O MOTIO N

DS100 S 12 0 0-7,00 0 #/H

R 4-2 0 MAD C

CALIBRATIO NNOTE S Flus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter , se t contro l syste mt o appropriat e rat e control , an d rea dtotalizer , flo wwate r int o a containe r an d compar e t h e toltalize r reading " t o th e meaauxe d amoun t i n container .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affix : a ne wcalibratio nsticker . CALIBRATIO NREPOR T TfJPTJ T VALUEINSTRUMEN T REftDIN G \r~w . o (.Befor e Calibration
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### After Calibration


### CATiTRRATljQ K SOURC E REFERENC E

Comment s

Performe d toy: J

### Date : Time : J B P i ace : CA L SHEET . WD B (Field)or Shop} 

### I

### TW I INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 ANNUA L TAG : .LOOP :

. DESCRIPOW ; SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : W/BMS INSTL-RMKS : SPEC-RMKS : S/N : F T 14 5 PLO W TRAN S PC C SLUDG E P-BM S 14 5 J?01 3
10305 6 X-1 2 MANUFACT : MICR O MOTIO N MODEL : DL100S-S S SCALE : CALIB-IN ; CALIB-OUT i PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : NT;2 8

0-8,00 0 #/H

R 4-2 0 MAD C

CALIBRATIO NNOTE S Flus hproces s piping, , connec t wate r hos e t o upstrea ma±d&o f flo wmeter , se t contro l syste mt o appropriat e r-at e control , an d rea dtotalizer , flo wwate r int o s containe r an d compar e t h e toltalize r readin g t o th a measure d atnonn t i n container .

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### CA L I E RATIO NSOURC E REFERENC E

Comments :

Performe d hy : 

# IsibXCLE^/^b p Date : il-H^O' t Time : 

# ^"-OO m 

### J B Place ; CALSHEET.WD B (field]or Shop)

### TW I INSTRUMEN T CALIBRATIO NRECORD TAG : LQOP : DESCRIPOOtf ; SERVIC2 : LOCATION : LP-SHT ; PfiTD : REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : UNI T # 4 ANNUA L F T 21 2 FLO W TRAN S WDF T O X-2 2 S-BM S 21 2 F01 4 W/BK S 10177 5 MANDFAC T MODE L SCAL E CALIB-I N CALIB-OO T PROCESS-S P INST-.S P ACTIO N I/ O NUMBE R CALIBRATIO NNOTE S MICR O MOTIO N D1D0QS-S S 0-7,00 0 #/H

R 4-2 0 MAD C

Flus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter , se t contro l syste mt o appropriat e rat e control , an d rea d totalizer , flo wwate r int o a containe r an d compar e t h e toltalize r readin g t o th e measure d amoun t i n container .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker , lb/fee
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### Afte r Calibration

CALIBRATIO NSOURC E REFERENC E

Comments :

s



# hh/^O

Date : 

# )l^D°i Time : 

# H'OO

AM ( g h performe d b y J B Place : CALSHEET . WDB {Field} or Shop) l

### TV7 I INSTRUMEN T CALIBRATION " RECOR D UNI T # 4 AKNUA L TAG : LOOP : • DESCRIPON : SERVICE : LOCATION : LP-SET : P&ID : REMARKS : *?/BMS INSTL-RMK S ; SPEC-RMKS : S/N : 115534 3 F T 13 8 FLO W TRAN S PC C A Q L1 Q X-l l P-BM S 13 3 F01 3 MANUFACT : MICR O MOTIO N MODEL : D100S-H Y SCALE : CALIB-IN : 0-6,00 0 #/H R CALlB-OUT t 4-2 0 MAD C PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : CALIBRATIO NNOTE S Flus hproces s piping- , connec t wate r hose t o upstrea msid e o f flo wmeter , se t contro l syste mt o appropriat e rat e control , an d rea dtotalizer , flo wwate r int o a containe r an d compar e t h e toltalize r readin g t o th e measure d amoun t i n container .
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### CALIBRATIO NSOURC E REFERENC E

Coroments :

Performe d by : 

# .ftfi /t) ^ 

# Date :\^^0 ^ Time : 

# )V OOl 

### J B Place : CALSHEET.TO B fjfreljjo r Shop):b:V-r-'h 

### TAG :

LOO P : DESCRIPOJtf : SERVICE : LOCATION : LP-SHT : P&ID ; REMARKS ; INSTL-RMKS : SPEC-RMKS : S/ET : Ttf l INSTRUMEN T CALIBRATIO NRECOR D UNI T # 4 ANNUA L T T 317 A T C ASSEMBL E SC C OUTLE T FD D 31 7 F01 5 T C PfEL L INCONE L 60 1 24 " MANUFACT ; CHESSE L MODEL : 351 0 SCALE : Typ e R T C CALIB-IN : 0-300, 0 F • CALIB-OUT : 4-2 0 MAD C PROCESS-SP ; 24 " INCONE L 60 1 WEL L INST-SP : ACTION ; I/ O NUMBER : N1;S 1 CALIBRATIO NNOTE S U s e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a .teitjperatur e signa l o f 50 0 de g F . an d 2,00 0 deg.F . a t inpu t o f transmitter , the nverif ythi s singl e i n contro l room , •
S e e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa newcalibratio nsticker . CALIBRATIO NREPOR T INPU T VALU E Before Calibration 

### INSTRUMEN T READING?
20OD After calibration



### CALIBRATIO NSOURC E REFERENC E

Comments : ^ 0 CMJ fcrATl. ^

• Performe d by : 

## §zUj CkJjtAWr\^_Date : 

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## i Tima : AM^PM^ ) J B Place : CALSHEET.WD B (Field or Shop) R

### TAG- '

LOOP : ' DESCRIPOE r SERVICE : LOCATION : LP-SHT ; P&ID : REMARKS : IWSTL-RMKS r SPEC-RMKS S/N : TW I INSTRUMEN T CALIBRATION " RECOR D UNI T # 4 ANNUA L T T 3I7 B T C ASSEMBL E SC C OUTL5J T EL D 31 7 pgi s T C WEL L INCONE L £0 1 24 " MAJJUFACT : CHRSSE L MODEL : 351 0 SCALE' : Typ e R T C CALIB-IH : 0-300 0 F CALIB-O'OT: . 4-2 0 MAD C PROCESS-SP : 24 " INCONE L 60 1 WEL L INST-SP : ACT!OH : I/ O NUMBER : 1*1:5 2

. CALIBRATION ' NOTE S Us e col djunctio ncompensate d 'thermocoupl e calibrato r t o inpu t a temperatur e signa l o f 50 0 da g F . an d 2,00 0 detj.F , a t inpu t o f transmitter , the nverif ythi s singl e i n contro l room .
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### INSTRU ^

After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comment s : . „ . „ _
Performe d by : Date : / f^ f T-^ffirime : A 7 9 A M J B Place : . s— CALSHEET.WD B \^ield)or Shop) 

### R

### TW I INBTROMEN T CALIBRATIO NRECOR D UNI T # 4 AKNUA L TAG : T T LOOP : -305 A DESCRIPON : -PYROMETE R SERVICE ; KIL NOUTLE T LOCATION : EL D • LP-SHT : 30 5 P&ID : F01 5 REMARKS : 44-99-F-1-0- 1 INSTL-RMKS : 55 " Targe t Tub e SPEC-RMKS : S/N ; MANUFACT : IRCO N' MODEL : M0DLIHE 4 44-99-F-l-0- 1 SCALE ; Typ e R T C CALIB-IN : 0-3,00 0 de g F CALIB-OOT : 4-2 0 MAD C PROCESS-SP : EMIS . 85S r INST-SP : ACTION : I/ O NUMBER ; Nl:5 1 CALIBRATIO NMOTE S Instal l factor ycalibrate dPyrometer .

Se e Manufactures.literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r

INPUT 1 

### VALU E CALIBRATIO NREPOR T Befor e Calibration. READIN G

After Calibration



### CALIBRATIO NSOURC E REFERENC E

Comments : ^/^m/ W

# Fluke

Performe d by: . J B •CA L SHEET . TOB 3 

### Date: . Place : Time :

(Field or Shop) 

### AMP H

### TW I msraOMEK T CALIBRATIO NRECOR D UNI T # 4 ANNUA L . TAG TI T 

### LOOP: - 3D3 B DESCRIPON ; P^RQr *ETE R 

### SERVICE : KIL NOUTLE T LOCATION : FL D LP-SHT ; 30 5 P&ID : F01 5

. REMARKS : 44-99-F-l-0- 1 INSTL-RMKS ; 55 1 1 

### Targe t Tub a SPEC-RMKS : S/N : MANUFACT : IRCO N MODEL : MODLINE 4 SCALE : Typ e R T C CALIB-IN : 0-3,00 0 de g F CALIB-OUT : 4-2 0 MADC PROCESS-SP : EMIS . 85 ^ INST-SP ; ACTION ; • I/ O NUMBER : HI;5 2 44-99-P-1-0
-

CALIBRAT1Q NNOTE S Instal l factor ycalibrate dPyrometer .

Se e Manufacture s literatur e fo r detaile dinstructions , Fil l ou t an d affi xa ne wcalibratio nsticker . 0. 1 lb/h r

INPU T VALU E CALIBRATIO NREPOR T INSTRUMEN T HEADIN G Befor e Ca.libra.txon

After Calibration

CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by: . J B CA L SHEET . WD E S „ Date: . Place : Time : JW P M (Field or Shop)

### TB I INSTRUMEN T CALIBRATIO NRECOR D TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS ; UNI T # 4 ANNUA L T T 404 A T C TRAN S T C GA S OUTLE T WAP C 40 4 F01 S W/GA S CLEANIN GTRAI N MANUFACT ; MODEL : SCALE : CALIB-IN : CALIB-GUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : Nl:ll 4

MOOR E TIY/K2-0-1-4-20M A 0--150 0 de g F Typ e K T C 4-2 D MAD C

CALIBRATIO NNOTE S Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a temperatur e signa l o f 20 0 de g F . an d 1,00 0 deg.F . a t inpu t o f transmitter , the nverif ytbl s singl e i n contro l room .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . -0. 1 lb/ha?
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### CALIBRATIO NSOURC E REFERENC E

Comments :

Performe d by : Date : i { f 

### 1 Time: . //.3^fiMjb M J B Place : , , CA L SHEET . TOB • (Fd^ldjir Shop)

### TH I INSTRUMEN T CALIBRATIO NRECOR D DNI T #4 . ANNUA L TAG : T T

; 

### LOOP : 404 B ! • DRSCRIPON ; T C TRAN S SERVICE : T C GA S OUTLE T LOCATION : KAP C LP-SHT : PSblD : P01 6 REMARKS : W/GA

S CLEANIN GTRAI N INSTL-SMKS : 3PHC-RMKE : S/N : MANUFACT : MOOR E ' MODEL : T1Y/K2-0-1-4-20M A SCALE : 0 7 

### 150 0 de g F CAL'IR-IN : Typ e K T C CALIB-QUT ; 4-2 0 MAD C PROCESS-SP : INST-SP : ACTION ; I/ O NUMBER : HI:11 5 CALIBRATIO NNOTE S Us e col djunctio ncompensate d thermocoupl e calibrato r t o inpu t a temperatur e signa l o f 20 0 de g F . an d 1,00 0 deg.F . a t inpu t o f transmitter , the nverif ythi s singl e i n contro l room ,
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticlter .

INPU T VALU E D CALIBRATIO NREPOR T

Before Cs.li~bra.tion 

### INSTRUMEN T READIN G ?.qo°
Afte r Calibratio n

CALIBRATIO NSOURC E REFERENC E

Conments : t^ O C a U QJrATlOl O NttOtzQ

Performe d by : Date : (f~l"7~Q ?lime : / / ' ^ IfrffiJp M J B P i ac e : CALSHEET.MD B (Field or Shop) 

### I

### TAG :

LOOP : DESCRIPON :

. SERVICE : LOCATION" : LP-SHT : P&ID : REMARKS : INSTL-RMK S t SPEC-RMKS : S/N : W I INSTRUMEN T CALIBRATIO NRECOR D OMI T # 4 ANNUA L F T 5 3 9 A d p Transmitte r STAC K FLO W FL D 55 9 F01 S FS E averagin g pito t tub e Eas t sid e of'Stac k 122293 1 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-S-P : ACTION : I/ O NUMBER : N00l;009 3

Automatio nServic e 11S1DR2F22B 3 OKI . 7 3 i n w c 0-£5 r 

### 00 Q ACF M 4-2 0 MAD C

CALIBRATIO NNOTE S

lb/fog
CALIBRATIO NREPOR T jf s Before Calibration

/ J , vJ

~After Calibration

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## 17-3 2J OJ> CALIBRATIO NSOURC E REFERENC E

Comments' :

Performe d hy: , fe*--^T7^/ Data : 

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# ? ^ 1 Time : 

## f 'foaOjQ j P M J B Place : , _ CAXiSHEET.WD B {Fiel dosf Bhopf 1

### TAG:



### LOO P : ) DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPBC-RMKS : S/N : TW I INSTRUMEN T fCALIBRATIO NRECOR D UNI T # 4 ANNUA L F T 559 B d p Transmitte r STAC K FLOW FL D F01 8 PS E averagin g pito t tub e Nort hsid e o f Stac k 122293 1 MANUFACT : MODEL ; SCALE : CALIB-IN" : CALIB-OUT : PROCESS-SP ; . ' INST-SP : ACTION : I/ O N0MBBR : NODI:009 3

Automatio n Servic e 11S1DR2F22B 3 0-1.7 3 i n w c 0-55,00 0 ACF M 4-2 0 MAD C

CALIBRATION " NOTE S

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WRODRC E REFERENC E

Commen t $ •

Performe d by ; • Date : Time: , woo J B Place : ^T^. CALSHEET.WD B (Fleld\>r Shop)

### Ttf l INSTRUMEN T CALIBRATIO NRECOR D TAG : LOOP : .' • DESCRIPOST ! SERVICE : LOCATION" : LP-SHT ; P&ID : REMARKS : INSTL-RMKS : E3&EC-RMKS : S/N : UNI T # 4 ANNUM . F T 42 5 MAC METE R X-1 8 DI L SLURR Y WAP C 42 5 F01 6 W/GAS CLEANIN GTRAI N MANUFACT : MODEL ; SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : Nl:11 2

Fische r & Forto r 1 4 7 5EN 0 9 PL 2 9KDHCAC L Q-2 0 GP M 0-2 0 GP M 4-2 0 MAD C

Flus hproces s piping , connec t wate r hos e t o upstrea m sid e o f flo wmeter . Se t contro l syste mt o appropriat e contro l rate , an d rea dtotalizer , flo wwate r int o a container ' an d compar e t h e toltalise r readin g t o th e measure d amoun t in ' container .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker . -0. 1 lb/h r CALIBRATIO NREPOR T INPU T VALU E "•1T3ETRIJMEN T READTJI G

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### Afte r Calibratio n

CALIBRATIO NSOURC E REFERENC E

Performe d > j A,

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## J B Place : V ',-eJg ^ CALSHEET.WD E (Field o r Shop)

### TW T INSTRUMEN T CALIBRATIO NRECOR D TAG : LOOP : 1 

### PESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS : S/N : UNI T # 4 ANNUA L F T 42 6 MA G METE R D I L SLURR Y WAP C 42 6 F0I 6 W/GAS CLEANIN GTRAI N Siz e 1 : o r 25m

m MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OOT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : N i : 11- 3

Fische r & Porte r 10D1475 C 0-2 0 GP M 0-2 0 GP M 4-2 0 MAD C

CALIBRATIO NNOTE S Flus hproces s piping , connec t wate r hos e t o upstrea msid e o f flo wmeter . Se t contro l syste mt o appropriat e contro l rate , a n d rea dtotalizer , flo wwate r int o a containe r an d compar e t h e toltali^e r readin g t o th e measure d amoun t i n container .
Se e Manufacture s literatur e fo r detaile dinstructions . Fil l ou t an d affi xa ne wcalibratio nsticker * 0, 1 lb/h r

INPU T VALU E Before Calibrat e ox ; INSTRUMEN T READIN G O 

### G
After Calibration



### CALIBRATIO NSOTIRC E REFERENC E

### mWEHMX UNIT# 4 [CMSTas k IC4Q32 ) PAG E 1 1 O F 3 • ^$SJJ|fJ>E B C.yX-?--- - • FAf L

1 TSU I [-3H 5 KIL N HIG H IUG I f 2 T3HH-3T 7 SC C HIG H HIG H 3 PAHH-30 0 KIF. N HIG H PRESSUR E 4 PAHH-32 4 EC- C HIG H PRESSUR E ^ B TAMM0 4 TEMPERIN G CHAMBE R HIG H 'lEMP . 7 VIOLATIO N OPACITY ! IIG U INSTANTATEOU S i 8 PROCES S MONITO R FAILE D 3 WAST E FEE D MONITO R FAILE D 1 2 VIOLATIO N STAC KFLO WHIG H 1 MI N ^ ~ 1 3 VIOLATIO N y£AC~3t 6 (TRV ) OPH N ' ~- - 14 ' VIOLATIO N ZAG-DZ S SURG E VEN TOPE N ^
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isrr i r-EK D CUT-OF F (CMSTssf cIC4032 ) PAG t2 O F 3 PAS S FAI L

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' J BT U 1 Hou rTota l OP L 5 3 CL1 2 Hour

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HC LCorrecte d 1 Hou rRoilin g Averag e Hig h OF L 6 0 Stac k

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### 7BIWhEKL YU N I TiPi

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### SHREDDE D X-1 0 

### SCREENED ^ X-1 1 MAI N CONVEYO R AU XCONVEYO R



### . X-1 2 X-22 " VERF YATOMIZIN G AI R ALAR M B YMANUALL YSHUTTIN G AJ R T O PRESSUR E SWITCH
. (NOZZE LMUS TBfjOPE N FO R ALAR M T O FUNCTION } X-1 1 

### X-1 2 X-2 2 A ! S O CHEC KOPERATIO N O F RA M COOLIN G WATE R LO WFLO WA l AR M (MSG#>27G ) CHECKE D BY : ^ 3 QL I 

### 8 3 Lim e Slurr yDensff yLo w1 Hou rRollin g Averag e Shpufdow n

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. 85 ROD OU TKIL N PRESSUR E LjN E (PT^QD ) COMMENT S ;

CHECKE D BY :
APPROVE D BY : \ t \



### R rltlQxU "SO. t /ds • Date : iO'^~CP( 

### Time : 3'^~ > 

### ^T<gM > H e A^/H ^

Place : Contro l Roo m BIWEEKLY

_ 4 9/10/0 7 H KWEEKL YUWET# 4 (CM S Tos k IC4Cf32 ) PAG E 10 F 3 '^IET^E P 

### 9yt9f f ^ -^- ^

- . _PASS
_

1 TSH I 1-30 5 KIL N HIG H HIG H ^ _ 2 TSHH-31 7 SC C HIG H HIG H ^

•3. PAHH-30 0 KIL N HIG H PRESSUR E

1 3 VI O LATIO N ZA0 3 1 6 (TRV ) OPE N 4 PAHH-32 4 SC C HJGI J PRESSUR E ^ 6 TAHH^}D4TEMPER1M G CHAMBE R HIG H TEM P ^ 7 VIOLATIO N OPACFfYHIG H INSTAhFTATEDU S , •f 8 PROCES S MONFTO H FAILE D 7 9 WAST E FEE D MONITO R FAILE D 1 2 VIOLATIO N STAC KFLO WI UG H 1 MI N

1 4 VIOLATIO N 7A C 02 6 SURG E VEN TOVE N /*_
_ 4 5 4JA^ 7 ANALYSE R RAIL44CI.
. ( 6 UA-55 E ANALYZE R FAI LC O ' •, 1 7 UA-5G D ANALYZE R FAILG 2 . f" 1f i UA-56 2 ANALYZE R FAI LH C ' 7 1 9 PDAL-5S 3 LO WDELT AP . (I P FA N FAILURE ) 7 2 0 WFD-OF F CARBO N INJECTIO N SYSTE M FAILE D / £ 1 PSMGQ/PSL-20 D SC C COMB
. AI R FA N FAILE D • 2 3 PSL-Z0 9 X-t 4 PRIMAR YFUE LLO WPRltSS , (ONL YAPPLICABL E FO R # 2 FUE LOIL ) STAC KFLO WHIG H INSTANTANEOU S _.Xf , 3 5 VIOLATIO N SC C TEMP , LO W1 MI N AVERAG E . 7 3 5 -'VIOLATIO N KIL N TEMP . LO W1 MI N AVERAG E ^ ' 3 7 WFD-OF F HC LHIG H 1 MI N AVERAG E 3 3 WFD-OF F OPACIT YHIG H 1 ML N AVERAG E i ,.3 9 WFD-OF F C O HIG H 1 MI N AVERAG E

' -f O WFD-OF F H C (THC ) HIG H 1 MI N AVERAG E " S\_ 4 1 WFD-OF F BAGHOUS E DELT AP HIG H 1 M) N AVERAG E . CBlWtEKL YUNF T# 4 [CM S Tas k SC4032 ) PA G H 2 O F 3 ^^£FE^qjr-QFF

__ r.-==— w . i ,-= ^ ^===== = = ^£^L^- =

4 2 WFD-0F F SD A0UTLE THIG H " E EMP . 1 MI N AVF : RAG E ^ 4 3 WFD-OF F OXYGb' N (Q2 ) LO W1 MI N AVERAG E ^ 4 4 VIOLATIO N HC LHIG H 1 HOU R AVERAG F - 7 4 5 VIOLATIO N C O HIG H 1 I [OU R AVERAG E ^ 4 E VIOLATIO N SC C TEMP . LO W1 HOU R AVERAGE" ! ^ 4 / WrD-OF F KIL N TL'MP . LO W ; 1 ISOTAVfcKAG E f 4 H VIO LA'liO N OPACIT YHIG H 48 0 SEC/HO!J R 7 4 0 WFD-OF F BAGHOUS E DELT AP LO WtMI N AVERAG E X 5 2 Ra g Lea k

•electio n Syste m (Tribe ) / $ 5 Pumpabl e 1 Hou rRollin g Tota l OP L/ jv. ; - - 

## y 5 6 Non-Pumpable l Hou rRollin g Tota l OPL-- " ^ ' ^ - '- , • *$7- T^.Wa^..l.Hni^.J3£iaitJ.TjQtai..QP LI J 8 BT U 1 Hou rTota l OP L•7 6 9 CL1 2 Hou rRailin g Tote ! OP L, f 70 Lo wVolatil e 1 2 Hou rRollin g Tota l OP L 7 1 Sem i Vtolatii o 1 2 Hou rRollin g Tota l OP L7 7 2 Mercur y1 2 Hou rR o Itin g Tota l OP L' ^ 7 3 As h 1 2 Hou rRollin g Tota l OP L^ 7 4 PC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L' ^ 7 5 SC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 7f J SD AOutle t Ternperaturc i 1 Hou rRollin g Averag e Hig h OP L" 7 7 Baghous e DEfferentus I Pressur e 1 Minut e Averag e Low OPL 7 3 Baghous e DifferontjR l Pressur e 1 Minut e Averag e Hig h OP L• 7$ Stat k

HC LCorrecte d 1 I lou rRollin g Averag e Hig h OP L^ '

. . S O Stac k

C O Correcte d 1 Hou rRollin g Averag e Hig h OP L^ j' 1 Stac k

Fle w1 Hou rRollin g Averag e HTg h OP L fl 2 Hi t Cl/Hr a Um e Flo w1 Minut e Averag e O P LS
.WEEKL YU N I T#4 - CHEC KSHF.E T" l-'AG E 3 O F 3

. '^T E Fl-liU

CUT-OF F _: ;
5 0 WAST E FEE D CUT-OF F 1 ES TB Y0 PERATO R UNJT# 4 OPER A1 O R T O CLOS E MANUA LHAN D VALW ? A TLIQUI D INJECTO R BEFOR KFLE XLIM E & AI R I .IN E T O SCREENE D FEEDE R XV-DT 3 SLID E GATE
. UNff* 4 OPERATO R T O VERIF YCUT-OF F B YPRESSIN G EAC H STAR TBUTTON
. fT i I E N INITIA L& SIG N SHEET ) SHRfcDDE D S

SCREENE D MAI N CONVEYO R ^ AU XCONVEYO R X -1 0 X -1 1 

### X-1 2 

# y X -2 2 VEERIFYATOMiZlN G AI R ALAR M B YMANUALLYSHU 1 TIN G AI R T O PRESSUR E SWITCH
. (NOZZE LMUS TB E OPE N FO R ALAR M T O FUNCTION ) X-1 0 

### ^

X -1 1 

### ^ X -1 2 

### ^



### . X -2 2 ^ ALS O CHEC KQPEROTK3 N O F RA M CODUJjIGfWATE R LO WFLfi WALAR M [MSG S >278 > CHECKE D BY : V

# Vwj -dX^ . 

# T 0 ^ KL\ 5 S 3 LimeSlurryDensit yLe w1 Hou rRollin g Avonagf i •Shoubdcw n ;ALO G C i IEGK S I N OPERATION S BOOK
. 8 5 RO D OU TKJL N PRESSUR E LIN E (PT-300 )
COMMENTS : •

CHECKE D BY : APPROVE D J3Y : Place : Contro l Roo m BtWEEKLY_ 4 9/10/0 7 H KSi' - . (UNI T# 4 (CM S Tas k 104032 ) PAG E 1 O F 3

1 TSJIH-3DliJ<n. M NIG H HIG H 2 TSHH-31 7 SC C HJG H HfG H 3 . PAHH-30 0 KIL N HIG H PRESSUR E 4 PAHH-32 4 SC C HIG H PRESSUR E

•6 ' 7A1-II-M0 4 TEMPERIN G CHAMBE R HIG H TEM P

' 7 VIOLATIO N OPACIT YH1GIIJNSTANTATEOU S B PROCES S MONFTO KFAILE D 9 WAST E FEE D MONITO R FAILE D 12 VIOLATIO N STAC KFLO W\ UG H 1 MI N 

### 7

1 3 VIOLATIO N ZAC-31 6 (TRV ) OPE N ' ( y 1 4 V|O I AT I O N ZAC-D2 6 SURG E VEN TOPE N 1 5 UA-55 7 ANALYZE R FAi LHCL

_.. _

_. : UA-5S B ANALYZE R FAI LC O ' - i 1 7 UA-SS O ANALYZE R FAI L0 2 1 8 UAH56 2 ANALYZE R FAI LH C ; y 1 & ' PDAL-5G 3 LO WDELT AP

_(I D FA N FAILURE ) '7, 0 WFD-OF F CARBO N INJECTIO N SYSTE M FAILE D r. i 2 1 PSL-1D0/PSL-2D Q SC C COMB , Ai R FA N FAILE D ' '" S £ 3 PSL-20 9 X-1 4 PRIMAR YFLIE LLO WPRESS
. (ONL YAPPLICABL E FO R # 2 FUE LOJL ) 2 5 STAC KFiJU WHIG H INSTANTANEOU S 3 5 VIOLA ' RO N SC C TEMP . LO W1 MI N AVERAG E 3( 3 VIOLATIO N KIL N TEMP . LO W1 MI N AVERAG E 3 7 WFD-OF F HC LHIG H 1 MI N AVERAG E 3 8 WFD-OF F OPACIT YHIG H 1 MJ N AVERAG E 3 9 WFD-OF F C O HIG H 1 Mf N AVERAG E 

# 7 7 /

\.
. ••• •WFD-OFF-H C (THC ) HIG H 1 MI N AVERAG E 4 1 WFD-OF F BAGHOUS E DELT AP HIG H 1MI N AVERAG E 

### Z .» ^FtE^UT-OF F ^ _^

42 Wr-D-OF F SD AOUTLF1 ' HIG H 17' : MP - i MI N AVERAG E 4 3 WFD-OF F OXYGE N [02 ) LO W1 Mi N AVERAG E A4 VIOLATIO N HC LHIG H 1 HOU R AVERAG E 4 5 VIOLATIO N C O HIGI1 1 HOUJ ? AVHliAC ^ 4 6 •VIOLATIO N SC C TEMP . LO W1 1IOU R AVERAG E 4 7 WFD-OF F KIL N TEMP'. ' LO W1 IWfffAVERAG E 4 H VIOLATIO N OPACFI THiC H 43 0 SEC/HOU R 4 9 WFD-OF F BACHOU^ E DELT AP LO W1 MI N AVERAG E 3 2 Ba g Lea k

Detectio n Syste m (Fr i bo ) 55 Pumpabl e 1 Hou rRollin g Tota l OP L 5 6 Non-PurapabS e 1 Hou rKollin g Tota l OP L f} 7 Tota l Wast e 1 I lou rRoilin g Tota l OP L (i'M 5 Tac k 1040:52 ) PAG E 2 O F 3 PAS S

7 4 PC C Temperatur e 1 Hou rRoilin g Averag e Lnvt OP L 7 5 SC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 7 6 SD AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L 7 7 Baghous e Differentia l FTOSKIP G 1 Minut e Averag e Lo wOPL ' 7 8 Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L 70fStac k

HC LCorrecte d 1 Ho wRollin g Averag e Hig h OP L S O Sfacf cC O Coirecte d 1 Hou rRollin g Ave?t*y e Hig h OP L

' ' i vStac k

Flo w1 Hou rRollin g Avefag o I llrj h OP L B2 HrtCl/Hr a Lim e Flo w1 Minut e Averag e OP L 

# / ••BT U 1 Hou rTota l OP L- r ^ m C L1 2 Hou rRollin g Tnfa i OP L 7 0 Lov/Vlolatiic.12 ; Hou rRollin g Tota l op l 7 1 Sem i Violatil e 1 2 Hou rRollin g Tota l OP L_

' ' '

# / 7 2 Mercur y1 2 Hou rRollin g Tota l OP L. X 

### Z " 7 3 As h VZ

Hou rRollin g Tota l OP L 

### -7^ 

## r 

# 7,. ( !JW!'# 4

, \ P i 1 -i D CUT-OF F CHECKSHEE T PAG E 3 O F 3

5 0 WAbT F FEE D CUT-QF F TES TB YOPERATO R UNI T1t4 OPERATO R T O CLOS E MANUA LHAN D VALV E A TLIQUI D INJECTO R BEFOR E FLE XLM~. & AI R LIN E T O SCREENE D FEEDE R XV-O t3 SLID E GATE
. U N I T# 4 OPERATO R T O VEI N F YCUT-OF F B YPRES S I N O EAC H STAR TBUTTON
. O 'HE N INITIAL S SIG N KHEEl )

•'SHREI3DF. D 

## ffafa^ SCRTENF- D S^/

V MAI N CONVEYO R AU XCONVEYO R !^V?X
_ X-1 0 ^J^-^W- - x-1 1 

### ^h^f^-^ X-1 2 H*^'— - x-2 2 

## '?i--^r i 

## ^2^ _ VERJF YATOMIZJK G Af R ALAR M B YMANUALLYS J JUTTIN G AI R T O PRESSUR E SWJTCH
. (NOZZE LMUS TB E OPE N FO R ALAR M T O FUNCTION )

ALS O C I lEC KOPERATIO N O F RA M COOLIN G WATE R LO WFLO WALAR M (MSG S >?J$) CHECKE D BY : 5 3 Lim e Slurr yDensit yLo w1 Hou rRollin g Averag e Shoutdcw n L O G CHECK S I N OPERATION S BOOK
. 8 5 RO D OU TKIL N PRESSUR E LIN E (PT-300 ) COMMENTS :

CHECKE D BY : 

### Date : / /
APPROVE D PY : Place : Contro l Roa m BfWEEKLY_ 4 9/1070 7 H K^

I WEEKLYU N I T# 4 (CM S Tas k K>W32 ) PAO E 1 O F 3 \&TE FEE D O U T-OF F PAS S

1 - TSFiH - 30 5 KIL N HIG H HIGI I 2 TSHH-3-17SC C HIG H HIG H 3 PAHIk^O G KIL N HIG H PRESSUR E ./ ^ 4 PAHH-32 4 SC C HFG I fPRESSUR E 6 TAHH - 40 4 TEMPERIN G C I I AMBE R HIG H TEM P 7 VIO LATPO N ORAC H YHIG H INSTANIWTEQU S H PROCES S MONITO R FAILE D 9 WAST E FEE D MONITO R FAILE D 1 2 VIOLATIO N STAC KFLO WHIG H 1 Mi N 1 3 VIOLATIO N ZAC-31 6 (TRV ) OPE N 1 4 VIOLATIO N 7AC-Q2 6 SURG E VEN TOPE N .1 5 UA-GS 7 ANALYZE R FAI LHCL
_

' J UA-5S R ANALYZE R FAI LCO
. • , 1 7 UA-5B 0 ANALYZE R FAI LO Z 1 8 UA-5S 2 ANALY^ R FAI LH C 1 9 PDAL-56 3 LO WDfcLT AP . (I D FA N FAILURE ) ' 2 0 WFD-OF F CARBO N INJECTIO N SYSTE M FAILE D 2 1 PSL-^100VPSL-20 D SC C COMB , AI R FA N FAILE D ; r 2 3 FSL-20 9 X-1 4 PRIfMR YFUE LLO WPRESS
. (ONL YAPPLICABL E FO R # 2 FUE LOIL^ 2 5 STAC KFLO WHIG H INSTANTANEOU S 3 5 VIOLATIO N SC C TEMP . LO W1 MI N AVERAG E . 3 5 -VIOLATLO N KIL N TEMP . LO W1 Ml N AVERAG E 3 7 WFD-OF F HC LHIG H 1 MI N AVERAG E ^ 3 3 WFD-OF F OPACIT YHIG H 1 M l WAVERAG E ' x / f 3 9 WFD-OF F C O HIG H 1 MI N AVERAGE : •

•WFD-OFF-H C (THC ) HtG H 1 MI N AVERAG E ' 4 1 WFD-OF F BAGHOUS E DELT AP HIG H iMI N AVERAG E .3 •BIWEEKL YUNI TM (CM S Tas k IC4032) PAG E 2 O F 3 ^fEn'Fi^LJT^Pr ^ _ =^ = _ _.. c = =„ = . c....^

= _ = .„._„_ PAS S

•1 2 WFD-OF F SD AOUTLE THIG H TEMP , 1 MI N AVERAG E ./ ^ i 4 3 WFD-OF F OXYGE N (02 ) LO W1 MI N AVERAG E ^/ ^ 4 4 VIOLATIO N IJCLH3GI1 1 HOU R AVERAG E 4 5 VIOLATIO N C O HIG H 1 HOU R AVERAG E 4 6 "V I OtAHO N SC C ' 1 E M P . LO W1 H OU R AVERA G E 4 7 WFD-OF F KIL N TEMP - LO WTfJlfl S AVERAG E y 4 3 VIOLATIO N OPACIT YHIG H 48 0 SEC/HOU R m WFD-OF F BAGHOUS E DELT AP LO W1 MJ N AVERAG E 5 2 Ba g Lea k

Detectio n Syste m (Tribo ) 6 5 Pumpabl e 1 Hou rRollin g Tota l OP L 6 5 Non-Pompabl e 1 Hou rRollin g Tota l OP L ^.....Xofc^Wa^.! ^

. AD'i' U 1 Hotir-Tofa l OF L 6 9 CL1 2 Hou rRollin g Tota l OP L- . ^ 7 0 Lo wViokfll e 1 2 Hou rRollin g Tota l OP L 7 1 Sem l Violstfl e 1 2 Hou rRollin g Tota l OP L 7 2 Mercur y12

i lou rRollin g Tota l OP L 7 3 As h 1 2 Hou rRollin g Tota l OP L 7 4 PC C Temperatur e 1 Hou rRollin g Averag e L3 wOP L, 7 5 SC C Temperatur e 1 Hou rRolling'Averag e Ltn vOP L 7 5 SD AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L 7 7 •Baghous e Differentia l Pressur e 1 Minut e Averag e Low fOPL " 7 B Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L. 73 ' Stac k

HC LConrect-e d 1 Hou rRoilin g Averag e Hig h OP L

. . BO Stac k

C O Correcte d 1 Hou rRollin g Averag e Hig h OP L

V J 1 Stac k

Flo w1 Hou rRollin g Averag e Hig h OP L £2 ' Hr l Ci/Hr a Lim o Ro w1 Minut e Averag e OP L_"

* WEEKL YUNFT# 4 CHEC KS I <r-[- TPAG E 3 O F 3 AST E FEE D CUT-OFF ^ ^ _ t^ „ ;,_„__^_ =


### s o WAST E FEE D 

### cur-orF rTES TB YOPERATO R UMF T# 4 OPERATO R T O CLOS E MANUA LHAN D VALV E A TUGUJ D INJECTO R BEFOR E FLE XI.IM E & AI R LIN E T O SCREWE D FEEDE R XV-O- H SLID E GATE UNI T# 4 OPERATO R T O VERIFY " CUT-OF F E YPRESSIN G EAC H STAR TBUTTON
. (THE N INITIA L&SIG N SHEET ) SHREDDE D SCREENE D MAI N CQNVI=YO R AUXCOtfv/EYQ R 

### X -1 0 

# \Ff

•

### X

-1 1 \Py^ 

### X

-12 CT^ T

### X

-22 V/ ^

~r VEPJFY " ATOMIZIM G AI R ALAR M B YMANUALL YS I JUTTIN G AI R T O 

### PRESSUR E SWITCH
. (NOZZE LMUS T

### B E OPE NFO R ALAR M T O FUNCTION ) 

### x -10 v 

### 7 ? r

### x

-1 1 VA ' x-1 2 x-2 2 VT^. . ALS O CHEC KOPERAT J O N O FRA M COOLIN G WATE R LO WF LO WALAR M (MSG * >27B) CHECKE D B Y: B 3 Lim e Sfun yDensit yLo w1 Hou rRollin g Averag e Sriouldow n V LO G CHECK S I N OPERATION S BOOK ! 8 5 RO D OU TKiL N PRESSUR E UN E (PT-300 ) COMMENTS :

CHECKE D BY : f ^ t ^jf i

' P a te://:/?-Q l Time : 7.' S O A M <PM ^ APPROVE D 0Y : /J^r^^ O Place : Corrtro l Roo m BIWEEKLYj l 9/10/0 7 H K"~R i WEEK ! , YU NI T# 4 (CM S Tas k lt>1032 ) ' PAG E 1 O F 3 

### "-•xmSTF. FEE D CUTOF F PAS S

1 TSI-f] L-3D S KIL N HIG H HfG H ?
. TSHH-31 TSC C 1IIG H HIG H 3 PAHH-30 0 KIL N HJG H PRESSUR E S 4 PAHH-32 4 SC C HIG H PRESSUR E / 6 TAHM- WTEMPERIN G C I (AMBE R HIGI I TEMP ' X 7 V30LATIO N OPACIIYHI6 H I^^STA^F^ATEOU S 8 PROCES S MONJTO R FAILED ' ^ 9 WAST E FEE D MONITO R FAILE D ^ XI VIOLATIO N STAC KFLO WHIG H 1 M! M 1 3 VIOLATIO N ZACXJlt i (FRV ) OPE N X 1 4 VtOI-ATtO N ZAC - 02 5 SURG E VEN TOPE N ' S~ , 4 5 UA-6S7.AWALYZEREAiLl.LC LX . •1 6 UA-55 S ANALYZE R FAI LC O ; _f 1 7 UA-S8 0 ANALYZE R FAI L0 2 1 & UA-5B 2 ANALYZE R FAI LH C 19 ' PDAL-5S 3 LO WDELT AP . (I D FA N FAILURE ) / 2 0 WFD-OF F CARBO N INJECTIO N SYSTE M FAILE D 2 1 PSL-10D/PSI--2D Q SC C COMB
. AI R FA N FAILE D 2 3 PSL-20 9 X-1 4 PRIMAR YFJF LLO WPRESS
. (ONL YAPPLICABL E FO R # 2 FUE LOIL ) 2 5 STAC KFLO WHIG H INSTANTANEOU S 3 5 VIOLATIO N SC C TEMP , LO W1 M I N AVERAG E 3 3 VIOLATIO N KIL N TEMP , LO W1 MI N AVERAG E .3 7 WFD-OF F HC LIIIGH 1 Mi N AVERAG E 3 B WFD-OF F OPACIT YHIG H 1 MI N AVERAG E 3 9 WFD-OF F CO " HIG H 1 MI N AVERAG E ; WFD-OFF-H C rJHC ) HIG H 1 MI N AVERAG E 4 1 WFD-OF F BAGHOUS E DELT AP HIG H 1 MI N AVERAG E . X' I WEEKL YUNI T# 4

,:*STT ; FEE D CUT-UF F (CM S Tas k IC4032 ) PAG E 2 O F 3 PAS S FAJ L

4 2 WFD-OF F SD AOUTLE THIG H TEMP . 1 Mt N AvHiAG E 4 3 WrD-OF F OXYGE N (02 ) LO W1 MI N AVERAG E 4 4 VIOLATIO N HO LHIG H 1 HOU R AVERAG E 4 5 VIOLATIO N C O HIG H 1 HOU R AVERAG E 4 6 VIOLATIO N SC C TEMP . LO W1 HOU R AVERAG E 4 7 WFD-OF F K l L N TEMP . LO W1 Km AVERAG E 4&VIOLATIO N OPACIT YHIG H 4fl D SEC J TIOU R 4 9 WhD-OF F BAGHOUS E DELT AP LO W1 Mt N AVERAG E " 57 , Ba g Lea k

Detectio n Syste m (Tribo ) 6 5 Pumpabl e 1 Hour Rollin g Tota l OP L 6t i iNon-Pumpabt e 7 Hou rRollin g Tota l OP L 

### '.•§7. Tota l Wast e 

### i

Hou rKotlin g Tota l OP L j o BT U 1 Hou rTota l OF L G 9 CL1 2 Hou rRollin g Tota l OP L 7 U Lo wVIolatit e 1 2 Hou rRollin g Tota l OP L 7 1 Sern i Violat e 1 2 Hou rRollin g Tota l OP L 7 2 Mercur y1 2 Hou rRoilin g Tota l OP L 7 3 As h 1 2 Hou rRollin g Tota l OP L 7 4 PC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 7 5 SC C Temperatur e 1 Hou rRollin g Averag e La wOP L 7 G SD AOutle tTemperatur e 1 Hou rRollin g Averag e Hig h OP L 7 7 Baghous e Differentia } Pressur e 1 Minut e Averag e Lo wOPL ' 7 8 Baghous e Differentia l Pressur e 1 Minut e Averag e Hig h OP L 7 9 Stac k

HC L

### Corrected

\ Hou rRollin g Averag e Hig h OP L 8 0 Stac k

C O Can-Grte d 1 Hou rRollin g Averag e Hig h OP L

: Slac k

.Flo w\ Hou rRollin g Averag e Hig h OP L 6 2 ' HrtCWr a Lam e Flo w1 Minut e Averag e OP L 

# /

rBIWEEKL YU N F TSf 4 .g^STF : FEED_CUl'.OFF
_ CHF-C KSHEE T PA« E 3 O F 3

Ei D WAST E FEE D OU TOF F TES TB YOPERATO R UNI T# 4 OPERATO R T O CLOSF
. MANUA LHAN D VA I ,V E A TLIQUI D INJECTO R BEFOR E FLE XLIM E & AI R LiNET O SCREENE D FEEDJ'KXV--D1 3 51JD E GATE
. UNI TiP\ OPERATO R T O VERIF YCUT-OF F B YPRESSIN G EAC H STAR TBOTTOM
. (THE N INHIA L& SIG N SNFET ) S tIKEDDE D X-1 0 _SCRhENED
_ X-1 1 _MAI N CONVETYOl i X-1 2 A U XCONVEYO R



### X-2 2 VERIF YATOMIZIN G AI R ALAR M B YMANUALL YSHUTTIN G AI R T O PRESSUR E SWITCH
. (NOZZE LMUS TB E OPE N FO R ALAR M T O FUNCTION ) X-1 0 f

XA 1 S x.-1 2 y X-2 2 S ALS O CHEC KOPERATIO N O F RA M COOUN G WA'lE R LOWiF l .O WALAR M (MSG # ^-278 ) CHECKE D BY : V . Vu rV . I QU. 3 &^XTl S 8 3 Lim e Slurr yDensit yLo w1 Hou rRoilin g Averag e

' } LO G C I [ECK S I N OPERATION S BOOK
. B 5 RO D OU TKIL N PRESSUR E LIN E (PT^300 ) 

### Shouidowj i

COMMENTS :

CHECKE D B Y APPROVE D B Y: Oate:l3.—1 J '6 C 3 l Time: - 1 

### - US (A^PW - Place : Contro!Roo m B!WEEKLY

_ 4 9/10/0 7 H K

## ABSOLUT E CALIBRATIO N AUDI T(ACA) DATASHEE T

Uni t# ' 4

## Sedaf# Paramete r 0 2 25 % rCO-lo wrang e 2QQpp m r CO-hfg h range 3000pp m rH Q lOOQpp m 

## NIS TTraceabl e Cafibratio n Standard s Paramete r 0 2 25 % rCO-lo wrang e 2QQpp m r CO-hfg h range 3000pp m rH Q lOOQpp m 

## Ga s Concentratio n Paramete r 0 2 25 % rCO-lo wrang e 2QQpp m r CO-hfg h range 3000pp m rH Q lOOQpp m Lo w[Zero ) D 0. 5 

## Paramete r 0 2 25 % rCO-lo wrang e 2QQpp m r CO-hfg h range 3000pp m rH Q lOOQpp m 

## •Mid S.S 3 

# ± Paramete r 0 2 25 % rCO-lo wrang e 2QQpp m r CO-hfg h range 3000pp m rH Q lOOQpp m 

## High 1 5 

# ± D.E Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Low Hig h

•1-Low 0 0. 1 -0. 1 — — 

### 2~Mi d 8.9 3 8.9 8 • — 

### -0,0 5 3-Hig h 1 5 15. 3 — 

### -0. 3 4-L6 w 

# o 0: 1

_; 

### 5-Mi d 6.9 3 9

— . 

### -0.0 7 — 

### 6-Hig h 1 5 15, 2 — 

### -0. 2

. 7rLo w . 0 ... . . . D.1 . . . -O J

. . —. .. . —. . 

### B-Mi d 0.9 3 8. 9 0.0 3 9-Hrg h 1 5 15. 2 — . — 

### -0. 2
• 

### Vlea n Differenc e = -0.1 0 -0.0 3 -0.2 3 Calibratio n Erro r= -0.40 % -0.12 % -0,93 % Calibratio n Erro r- Mea n Differenc e / Spa n Valn e * 10 0



## E/ l Tec h Title 9/22/200 9

## ABSOLUT E CALIBRATIO N AUDI TfACA ) DATASHEE T

Unit#

_. L. . Seria l # Paramete r 0 2 25 % i CO-lo wrang e 200pp m ; r CO-hig h rang e 3000pp m r HC 3 lOOOpp m MS TTraceabl e Cafibratio n Standard s Paramete r 0 2 25 % i CO-lo wrang e 200pp m ; r CO-hig h rang e 3000pp m r HC 3 lOOOpp m Ga s •Concentratio n Paramete r 0 2 25 % i CO-lo wrang e 200pp m ; r CO-hig h rang e 3000pp m r HC 3 lOOOpp m Lo w(Zero) Q 

# + 1 0 

## Paramete r 0 2 25 % i CO-lo wrang e 200pp m ; r CO-hig h rang e 3000pp m r HC 3 lOOOpp m Mi d 68,

9 

# ± 1 0 

## Paramete r 0 2 25 % i CO-lo wrang e 200pp m ; r CO-hig h rang e 3000pp m r HC 3 lOOOpp m Hig h 15

4 

# ± 1 0 Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w Mi d High 1-Lo w 0 -0. 2 6. 2 2-Mi d •68. 9 66 7 — 

### 2, 2 — 

### 3-Hig h 154 152, 6 — — 

### 1. 4 A • _n

### A {1. 4 u 

### 5-Mi d 68. 9 66. 8 2. 1 6-Hig h 154 154. 5 — — 

### -0. 5

. . 7-Low. . . ." . 0 .. . .... . .-0. 1 0. 1 — 

### Mfi d S3, 9 6 7 — 

### 1. 9 — 

### 9-Hig h 154 153, 4 — 

### 0. 6 Mea n Difference = Calibratio n Error 0.2 3 2.0 7 0.5 0 Mea n Difference = Calibratio n Error - 0,12 % 1.03% 0.25 % Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 10 0



## E/ l Tec h Titl e 9/22/200 9

## ABSOLUT E CALIBRATIO N AUDI T(ACA ) DATASHEE T

: 

## VUnJtf

f• 4

## ' •Seria l # '

_13 2 

## Paramete r <~02 25 % c CO-lo wrang e 200pp m f CO-hig h rang e 3000ppr n rHC ! 1000pp m NIS TTraceabl e Calibratio n Standard s Paramete r <~02 25 % c CO-lo wrang e 200pp m f CO-hig h rang e 3000ppr n rHC ! 1000pp m Gas Concentratio n Paramete r <~02 25 % c CO-lo wrang e 200pp m f CO-hig h rang e 3000ppr n rHC ! 1000pp m Lo w{Zero } •o • 

# ± 15 0 

## Paramete r <~02 25 % c CO-lo wrang e 200pp m f CO-hig h rang e 3000ppr n rHC ! 1000pp m Mi d 1075, 1 

# ± 1.5 0 

## Paramete r <~02 25 % c CO-lo wrang e 200pp m f CO-hig h rang e 3000ppr n rHC ! 1000pp m Hig h 223 9 

# ± 15 Q Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Low Mi d Hig h 1-Low . . 0 •-0. 2 0, 2 — — 

### Z4M • 1079. 1 1086, 5 -7. 4 — 

### 3-Hfg h 228 9 22B7 — 

### 2 n .rj i 

### O d 5-Mi d 1079. 1 1077. 6 — 

### 1.5

2289 - 2317. 4 — — 

### -28. 4 7-Lo w 0 -0. 1 0, 1 — — 

### 8-Ml d 1073, 1 1077. 7 • — 

### 1.4 — 

### 9-Hig h 228 9 2301. 9 -12. 9 Mea n Differenc e - Calibratio n Erro r= 0.2 3 -1.50 ' -13.1 0 Mea n Differenc e - Calibratio n Erro r= 0,01 % -0,05 % -0.44 % Calibratio n Erro r- Mea n Differenc e / Spa n Valu e * 1 0 0 j i 

## E/ITec h

. Titl e 9/22/200 9 ; Dat e : I

## ABSOLUT E CALIBRATION AUDI T(ACA ) DATASHEE T

UnEt # 4Seria l #



## ' Paramete r C 0 2 25 % 

## rCO-lo wrang e 200ppr n r CO-hig h rang e 3000pp m
* HC l 1000pp m NIS TTraceabl e Calibratio n Standard s ' Paramete r C 0 2 25 % 

## rCO-lo wrang e 200ppr n r CO-hig h rang e 3000pp m
* HC l 1000pp m Gas Concentratio n ' Paramete r C 0 2 25 % 

## rCO-lo wrang e 200ppr n r CO-hig h rang e 3000pp m
* HC l 1000pp m Low(Zero ) D 

# ± 5 0 

## ' Paramete r C 0 2 25 % 

## rCO-lo wrang e 200ppr n r CO-hig h rang e 3000pp m
* HC l 1000pp m Mi d 31 8 

# ± 5 0 

## ' Paramete r C 0 2 25 % 

## rCO-lo wrang e 200ppr n r CO-hig h rang e 3000pp m
* HC l 1000pp m High 70 7 

# ± Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w Mi • Hig h 1-Low 0 -0, 3 0, 3 — 

### 2-Mir J 31 8 264. 9 — 

### '33. 1 — 

### 3-Hig h ' •70 7 713. 1 -6. 1 4-tu w 

### 0 o 

### 0 : 5-Mi d 31 6 306, 2 — 

### 11. 8 6-Hig h 70 7 ' 707. 1 -0. 1 7-Lo w 0 0, 6 -0. 6 —



### . 8-Mi d 31 8 314. 2 3. 8 — 

### 9-Hig h 707 . 708: 6 — — 

### -1, 6 Mea n Difference ~ -0.1 0 16.2 3 -2.6 0 Calibratio n Erro r- •-0,01 % 1.62% -0,26 % Calibratio n Erro r= Mea n Difference / Spa n Valu e * 10 0 

## C E E/ l Tec h

### Tabl e1 -Summar y o£ Relativ eAccurac y Tes t Audi t Hcsult e Veoli aE S Technica l Solution s Siiuget , Illinoi s Jun e 22, 2 3 an d24,200 5 CEM S Paramete r unit s Measure dR A Criteri a
' Uni t % C O pp m@ 7 $ 0,004 ppm 1 

### Pas s ' Uni t % Oj , dr

y 1.0" " Pas s ' Uni t % Oj , W5

t %0-z 

### 0.l3% a t-f)" " Pltff t 

### Uni t 3 C O ppm© • 7 % O 2 

### 0.06 3 ppra 3 

### 5 s 

### * Pass ; Uni t 3 0 2 , diy %0 » 

### 0 .02% a 

### .1 . 0 • 

### Pas s Uni t 3 Oj , wet. % O a 

### •0 .31% * 1 . 0 w 

### Pas s Uni t 4 C O pp m@ 7 % 0 2 

### 1,146 ppm £ 5" * 

### Pas s Uni t 4 Oi , dry %'O i 0 .15ft " 1.0' * 

### Pas s Uni t 4 0 2 s

### wot %0 2. 

### 0.46% a 1.0 * 

### Psts s

" Percen t

o f emissio nstandar

dor absolut e averag e differenc e (pp mor %) . h 

### Pfl4B . c

### P S 3 .

INCINERATOR . mj £RAT A VEOU A 5 JUL Y 7,20CS CS C Projec

t093-56 7

## Incinerato r Dat a Poin t "Veofi a KtiVitunrricntR l Service s SausStitrilinoi s Created Perio dSt m Perio dE n 1/I/201 0 6;0 0 A M 1/1/201 0 6:0

0 A M 1/i/ZOl O 6:0

0 A M Page 5 o f7
1 Mi nJ

. M nI Mi n1 Hi
- Rai l1 H r Rol lLH r

RiA : LH r

RDI I 11-I

r Rol l1 Hr.RoI l1 2 H r J. 2 H r llH i11-I

r Tot i H r To t t H r Tut AYG
- AV GAV GWarnShut OFI-

j To t To t Shu t Tu t OP LRol lTo t

Rol lTut

Rol lTo t

\ V?JT . Shu

t OP L War nStm

t OPL , WarnWarnShu ; OP T Carbo n injectio n Flo w Lim e SlurryDensit y Stac k Opacit y Stac k C O RCR A SD AOufle tTem p Baghous e DiffPres s Lo w Baghous e Dif fPres s Hig h Stac k TK C X1 1 Weigh t X2 2 Weigh t X1 2 Weigh t X1 Q Weigh t Stac k HC LRCR A 6.6UOCO D G.2DC-000 65 .0000 0 S.DtJMa O . 10.0DM Q 450.0MK ] 5Q0.O00 D 440.000 Q 5DCI.U0U O

a.naooo o Z.IJQQOO O 9.0Q00Q 0 10,0000 0
s.onnoo o 10 .D &00 0 as .5ona a 115,400 m sri^ooii }

30.QDOOO 40.tlDa0

0 10P.Q3Q O 429.D00 0 431.000

0 434.00 ^

AQQ.UUQQ

500.000 0 . 900.CDO O 950.00 0 0 IClOQ .&Di l 1550.0C C 1CSQ ,OC a 1700 .0 'J O asQ.oofjcL'S-D.OOC D 1005.00 0 lmo,OD D 1-550X0

0 1'C-C.00C

1590.DO D ' 16S0.CU

0 17C-C.00C15,0000 0 32.tinaa o 35 .PGCI1I OYdotia . Em'h'utiraepial Service s Sauge t TJlinnif s
4 ,00000 0 3 .00000 0 3P.Q0D[! n 33,5000r> 37.2000 0 Stac k 0 2 RCR A HGLtopm e Shredde d Weigh t Temperin g Chambe rTem p 8OO.000 0 1200.00 0 P C C Tem p S C C Tem p Stac k C O Correcte d Stac k HC LCorrecte d Stac k O Z Correcte d Stac k Fio w Lo wBT U Liqui d Weigh t Hig h BT U Liqui d Weigh t Liqui d Weigh t Containerize d Weigh t Soirtf s Weigh t Weigh t 130Q.PD 3 1S40.0U D 1850.001 } 1825.00 0 450.000 0 500.000 0 "100 .0000 150.000 0 4.OO0UU U
asoaa.o n 1570.00 0 151S.00 3 1507.00 Q 1905.00 0 1B90.00 0 13BS,Oo d 30.0000 0 7 E .0000 0 100.000( 1 SC O 000 0 32.0000 0

37000.0 0 37300.0 0 M O 6-3.01 ?

2300.00 0 305D.00 0 325S.0D 0 1500.00 0 IDtiOQ.Q D 12soo.u a iaaoo.u a I3796.c n Created Perio dStar

t Perio dEi i 1/1/20T.0 6:0 0 A M V1/2CU G6:0 0 A M VV20L0 6;C 0 AlVl '

13-MO.C D 14500,3

0 ';i"C-CD.0C

1600.M 0 IB S 3. OD D 1700.1 ] D O

1 n no.oc- o 105O. C a o ; 1 c n,oo c

2500,00 0 £750.00 0 30CO.OCO 1 a aoo.e e 14000.0

0 15000.0

cST U

Chlorin e Mercury Asl i Lo wVolatil e Sem i Volatil e F.uvjrnjmiejnia . 1 Service s Saugui Tlliruri s Create* : Perio dStar

t Perio dE n

2S5.000 0 £62,030 0 ojiama a o,02ftOO- 3 BOOD.G0Q 0777.00 0 43.0000 0 47 . a 000 0 U1/20I 0 6:0GA M L 'l/201 0 G ; 0 G A M b';/20l u 6:00A M Pag e 7 o f 7

. 45D30QC B 4330005 3 530CC30 0 2&CU.-30 0 2503.00 0 3D24.QQ G 4OC.0O0 O 46C-.D0O O 5C0.OCC 0 g,S5t00 O O.K7530 O 0.31230 Q 90000.0 3 1000G B . 0 10£324.- 3 50C.OOQ O 540.00D U 5B4.00D C 60. 0 D00 0 64.0000 0 700,000 0 740.D00 0 768.030 0

### Certificatio n Statemen t

1 certif y unde r penalt y o f th elaw tha t thi s document

was preparedunde

r m y directio no r supervisio ni naccordanc e wit hasystemdesigne dt

o assur e tha t qualifie dpersonnel properl y gather an devaluate theinformatio nsubmitted . Base do nmy inquir y o f thepersonor

person s wh o manag e th

esystem , o

r thos e person s directl y responsibl efo r gatherin g theinformation , th e informatio nsubmitte dis , t o th ebes t o f m y knowledg eandbelief , true , accurate , andcomplete . Ia mawar e tha t ther e ar esignifican t

penaltie s fo r

submittin g fals einformation , includin g th e possibilit y o f

finean dimprisonment

fo r knowin g violations .

Dou g Harri s Genera l Manage r Veoli aE S Technica l Solutions , L.L.C . Sauget , I L Signature :

1

# Notificatio n ofComplianc e (NOC )

fo rVeoli a E S Technica l Solution s Unit s 2 , 3 , & 4

4 0 CF R 63 Subpar t EE E Hazardou s Wast e Combusto rMAC TStandar d 

# Complianc e Date : Jun e 18-25 , 201 2
Owner/Operator/Title : Veoli aE S Technica l Solutions , L.L.C . Stree t Address : 7 Mobil eAvenu e City : Sauget State : I LZi p Code : 6220 1 Plan t Name : Veoli aE S Technica l Services , L.L.C . Plan t Contac t / Title : Dou g Harri s / Genera l Manager Plan t Addres s (i f

differen t

tha nowner/operator's ) Stree t Address : City : State : Zi p Code : Majo r o r Are aSourc eThi s sourc ei s locate da t afacilit y tha

t i s amajo r

sourc eo f

Hazardou s Ai r Pollutants .

### Introductio n

Veoli aE S Technica l Solutions , L.L.C , i nSauget , Illinoi s (Veolia-Sauget ) operate s thre e (3 ) incinerators : tw o (2) fixe dheart hunit s (Unit s 2 and3 ) andone(1 ) rotary kil nuni t (Uni t 4) , Al l thre e unit s operat

e unde r Titl eV Permi t

Numbe r V-IL-1716300103-08-0 1 issue dby U.S . EPA , Regio n5 . Eac hincinerato r i s subjec t

t o theNationa lEmissio nStandard s fo r Hazardou s Ai r Pollutant s (NESHAPs ) fo r Hazardou s WasteCombustor s (Titl e4 0 o f th eCod eo f

Federal Regulations , Par

t 63 [40 CF RPar

t 63] , Subpar

t EEE) , i.e. , th

eHW C MACT . Pe

r the requirement s o f

theHW C MAC Ta

t 4 0 CF R63.1207(d)(2) , aConfirmator y Performanc eTes t fo r polychlorinate ddibenzo-p-dioxin s andpolychlorinate ddibenzofuran s (dioxins/furans ) mus t beconducte dwithi nthe31-mont hperio dfollowin g th

ecommencement

o f thepreviou s Comprehensiv ePerformanc eTest . Th epreviou s Comprehensiv ePerformanc eTes t fo r theUni t 2 Incinerator

bega no nDecember

8 , 2009 , whic hrequire dtheConfirmator y Performanc eTes t (CfPT ) t o begi nb y Jul y 8 , 2012 , Veolia-Sauge t

commence dtheUni t

2 CfP TonJune 18 , 2012 , Th epreviou s Comprehensiv ePerformanc eTes t fo r th eUni t 3 Incinerato r

bega nonDecembe r

1 , 2009 , whic hrequire dtheConfirmator y Performanc e Tes t (CJPT ) to begi nb y Jul y \ . 2012 . Veolia-Sauge t

commence dtheUni t

3 CfP TonJune 20 , 2012 . Th epreviou s Comprehensiv ePerformanc eTes t fo r th eUni t 4 Rotary Kil nIncinerato r bega no n Decembe r

16,2009 , whic hrequire dth eConfirmator y Performanc eTes t (CfPT ) to begi nb y Jul y 16 , 2012 . Veolia-Sauge t commence dtheCfP To nJune 25 , 2012 . Th e4 0 CF R63 Subpar

t EE Eemissio nstandard s tha t ar eapplicabl et

o thes e unit s ar

especifie din Tabl e1 . T a bl e 1 . 4 0 CF R 6 3 Subpar t EE E Emission s Standard s



### Paramete r Limi t

Dioxin s an

dFuran s 0.2 0 ng TEQ/dscm , correcte dt o 7 % oxyge nfo r

incinerator s withdr y ai r pollutio ncontro l syste mandinle t temperatur

e t o initia lparticulatematte

r contro l devic e>400°F ; 0,4 0 n g TEQ/dscm , correcte dt o 7 % oxyge nfo r

incinerator s withdr y ai r pollutio ncontro l syste mandinlet temperatur

e t o initia lparticulatematte

r contro l devic e<400°F .
3

### Th eapplicabl edioxins/furan s standar do f th eHW C MAC Tfo r

Unit s 2 and3 i s 0.20 n g TEQ/dscm , correcte dto 7 % oxygen , andtheapplicabl edioxins/furan s standar do f theHW C MAC Tfo r

Uni t 4 i s 0.4 0 n g TEQ/dscm , correcte dt o 7 % oxygen . Thes estandard s wereme t durin g theConfirmator y Performanc eTest s o f Unit s 2 , 3 , and4 . Result s o fConfirmator yPerformanc e Test s Th eresult s o f

theConfirmator y Performanc eTes t ar eprovide di nAttachmen t 1 , Fina lReports , Dioxins/Furan s Confirmator y Performanc eTes t Report fo r theUni t 2 Fixe dHeart

hIncinerator , Uni t 3 Fixe dHeart

hIncinerator , andUni t

4 Rotary Kil ndatedJune2012 . Th eConfirmator y Performanc eTes t

report s include :

• Th emethod s tha

t wer eusedto determinecompliance ;
• Th eresult s o f

theperformanc etests , continuou s monitorin g system(CMS ) performanc eevaluations , andothe r monitorin g procedure s tha t wereconducted ; and

• Th eemission s o f

dioxins/furans , reportedi nunit s andaveragin g times , andi n accordanc ewit hth

etes t method s specifie di nSubpar t EEE , Tabl e2 summarize s theresult s o f th eemission s samplin g durin g theJune201 2 Confirmator y Performanc eTest s o f

Unit s 2 , 3 , an

d4 . Tabl e 2 . Summar yo fHW C MAC TConfirmator yPerformanc e Tes t Result s Jun e 201 2 HW C MAC T Standar d Test

Metho d Unit s Limi t Averag eTes t Resul t Uni t 2 Dioxins/Furan s EP ASW-84 6 Method0023 A ng TEQ/dscm ,

correctedt

o 7 % O z 0.20 0.0017 8 Uni t 3 Dioxins/Furan s EP ASW-84 6 Method0023 A ng TEQ/dscm ,

correctedt

o 7 % O z 0.2

0 0.0006 8 Uni t 4 Dioxins/Furan s EP ASW-84 6 Method0023 A ng TEQ/dscm ,

correctedt

o 7 % O z 0.4

0 0.19 5



### 4

### Operatin g Condition s

Insectio n63.1207(b)(2) , theHW C MAC Tstate s tha t "yo umus t

conduc t confirmatory performanc etests to : (i ) Demonstratecomplianc ewithth edioxin/fura nemissio nstandar dwhe n th esourc eoperate s unde

r normal operatin g conditions" . "Norma ! operatin g conditions " ar e definedas : 1 ) th eaveragecarbo nmonoxid eemissio nleve lover th epreviou s 1 2 month s to the maximu mallowed ; 2) th eoperatin g limit s establishe dto maintai ncomplianc ewit hthe dioxin/fura nstandar

dwithi nth

erange o f

theaverag evalu eove r

th epreviou s 1 2 month s andth e maximum , o r

minimum , allowed ; an

d3 ) chlorin efeedrate s a t normal o

r greater . A s such , no new or additiona l operatin g limit s (OPLs ) wereestablishe ddurin g thi s confirmatory performanc e test . Theapproac hfo r

accomplishin g theCfP Tobjective s wa s to operate theUnit s 2 , 3 , and4 incinerator s a

t asingl etes t

conditio nrepresentativ eo f typica loperations . T o accomplis hthis , a mi xo f wastestreams tha

t wererepresentativ eo f

typica loperation s werefe dto th eincinerator , an dthefollowin g parameters wereoperatedbetweenthepreviou s 12-mont haverageandth e maximum , or

minimum , allowed , i.e. , theOPLs : primary combustio nchambe r temperature , secondar y combustio nchambe

r temperature , baghous einlet temperature , total hazardou s wast e feedrate , total pumpabl ehazardou s wast efeedrate , .stac

k gas flowrate , carbo ninjectio nrat e (Uni t 4 , only ) andth

etotal chlorin efeedrate . Avarianc ewa s requeste dandapprove dfo r the concentratio no f

carbo nmonoxid e(CO ) i nthestack gas to allo w theoperatio no f theincinerato r t o maintai nth

eC O concentratio nbelo w th eHW C MAC Temissio nlimi t o f 10 0 ppmcorrecte d to 7 % oxygen . Table s 3 , 4 , and5 presen t theresult s o f

th eke y parameters monitore ddurin g th e CfPT s fo r

Unit s 2 , 3 , and4 , respectively .

5Tabl e 3 . Summar yo fUtjiit 2 Operation s Operatin gParameter i Unit s Ru n 1 F ti n 2 Ru n 3 Averag e Durin g CfP T Targe tOperatin g

Rang e Targe t

Achieved ? Baghous e Inle

t Ter iperatur

e (HRA ) ° F 405. 1 A 05. 2 405. 0 405. 1 400-42 0 Ye s Primar y Combust s (HRA ) nChambe r Temperatur

e o p 1,750. 5 1 , 748. 8 1,746. 6 1,748. 6 1,845-1,68 6 Ye s Secondar y CombustionChambe

r Temperatur

e (HRA ) | ° F 1 ,895. 1 1 , 895. 3 1,895. 0 1,895. 1 1,917-1,87 7 Ye s Stac k CarbonMonoxide(HRA ) ppm v (7 % 0 2 corrected ) 0. 6 1. 5 1 .4 1. 2 0-10 0 Ye s Stac k Ga s Flowrat e(HRA ) acf m 14,063. 1 14 ,173. 5 14,074. 3 14,103. 6 13,317-15,14 7 Ye s Stack OxygenConcentration % 11. 3 10. 9 11. 2 11. 1 N/ A N/ A Chlorin eFeed(HRiA) lb/h r 61. 2 51. 7 61. 2 61. 4 36.0-21 8 Ye s PumpableWast

e Feed(HRA ) i lb/h r 1,950. 9 1 967. 2 1,972. 7 1,963. 6 1,571-3,10 7 Ye s Total Wast

e Feed(jHRA) lb/h r 2,173. 6 2 189. 5 2,188. 1 2,183. 7 1,761-4,01 7 Ye s ! HR A- Hourly Rollin g Averag e

### Tabl e 4 . Summar yo f Uni t 3 Operation s Operatin g Paramete r Unit s Ru n1 B .un2 Ru n3 Averag e Durin g CfP T Targe t

Operatin g Rang e Targe t

Achieved ? Baghous e Inle

t Temperatur

e (HRA ) o p 406. 3 4 05. 3 404. 5 405. 4 399-42 0 Ye s Primar y CombustionChambe

r Temperatur

e (HRA ) ! ° F 1 ,784. 6 1 , 785. 8 1,793. 2 1,787. 9 1,865-1,68 6 Ye s Secondar y CombustionChambe

r Temperatur

e (HRA ) 

### I a F 1,905. 1 1 , 305. 0 1,905. 1 1,905. 1 1,913-1,87 7 Ye s Stac k CarbonMonoxide(HRA ) ppm v (7 % 0 2 corrected ) 0. 0 0.0 0. 0 0. 0 0-10 0 Ye s Stac k Gas Flowrat

e(HRA ) acf m 14,303. 1 1 4 ,347. 8 14,051. 4 14,234. 1 13,499-15,14 7 Ye s Stac k OxygenConcentration % 12. 8 12. 9 13. 1 12. 9 N/ A N/ A ChlorineFeed(Hl|A ) lb/h r 55. 1 56.0 61. 0 57. 4 37.5-21 8 Ye s Pumpable Wast

eFeed(HRA ) lb/h r 1,962. 8 1 , 957. 0 1,913. 6 1,944. 5 1,562-3,10 7 Ye s Tota l Wast e Feed(HRA ) lb/h r 2,202. 9 2 . 180. 1 2,1.22. 3 2,168. 4 1,768-4,01 7 Ye s HR A- Hourly Rollin g Averag e

7Tabl e 5 . Summar yo fUrii t 4 Operation s Operatin g Paramete r Unit s Ru n1 P<u n2 Ru n3 Averag e

Durin g CfP T Targe t

Operatin g Rang e Targe t

Achieved ? Baghouse Inlet

Temperatur

e(HRA ) = F 389. 8 3 89. 8 389. 8 389. 8 384-40 0 Ye s Primar y CombustionChambe

r Temperatur

e (HRA ) o p 1,668. 9 1 , 569. 2 1,717. 3 1,685. 1 1,86 5 - 1,49 9 Ye s Secondar y CombustionChambe

r Temperatur

e (HRA ) i o p 1,898.4 I , 901. 0 1,902. 2 1,900. 5 1,917-1,88 6 Ye s Stac k CarbonMotjoxid e(HRA ) ppm v (7 % 0 2 corrected ) 0. 1 0. 1 0. 1 0. 1 0-10 0 Ye s Stac k Gas Flowrat

e(HRA ) acf m 35,290. 7 3 5 ,093. 8 35,602. 9 35,329. 1 33,439-37,43 2 Ye s CarbonFeed(HRA ) ib/h r 6. 7 6. 7 1 6. 7 6. 7 7.26-6. 2 Ye s Stack OxygenConcentration % 13. 2 12. 9 13. 0 13. 0 N/ A N/ A Chlorin eFeed(HRA ) lb/h r 118. 6 20. 1 118. 2 119. 0 88.2-22 9 Ye s PumpableWast

eFeed(HRA ) lb/h r 1,663. 5 1 741. 0 1,738. 7 1,714.4 1,336-3,29 1 Ye s TotalWast

eFeedjriRA ) lb/h r 5,359. 1 5 800. 1 5,953. 0 5,704. 1 4,335-12,89 7 Ye s Secondar y CombdstionChambe

r Liqui dFeed (HRA ) lb/h r 540. 0 \ 42. 9 510. 3 531. 1 400-1,17 6 Ye s HR A - hourly rollin g average

i



### 8Hazardou s Wast e Residenc e Tim e



### Becaus eo f

th efixed-hearthnatur

e o f theUnit s 2 and3 Incinerators , soli dwast eresidenc etim ei s basedonth eelapse dtim ebetweensolid s charge s o r thetrave l lengt

ho f theashra

mfeeder , whic hfunction s t o clea r theprimary combustio nchamber o f soli dwast

eresidue . A nelapsed tim eo f onehou r

or a nashra mtrave l lengt

ho f 11 0 inche s hav ebeenestablishe da s thecriteri a fo r determinin g whensoli dwast ei s no longer

i nthecombustio nzones . Sinc eatomize dliqui dwast evaporize s almos t

instantaneousl y upo nenterin g th ecombustio n chambers , th eresidenc etimeo f thes e waste s i s muc hles s tha nfo r solids . Durin g theUnit s 2 and 3 CfPTs , th eincinerator s wer eoperate da

t normal conditions . Liqui dandgaseou s waste s enterin g theUni t

2 incinerator

demonstrate daresidenc etim eo f approximatel y 5.4 seconds , Liqui dan

dgaseou s waste s enterin g theUni t 3 incinerato r

demonstratedaresidenc etim eo f approximatel y 5. 4 seconds . Thehazardou s wast

ega s residenc etim efo r

Uni t 2 i s calculate da

s follow s usin g th

ethree-ru n averag efo r

th estac k

gas flowratedurin g th

eUnit 2 CfPT :

• FnmaryCO T"~""~~'~~~ " o Secondary Combustio nChamber Volum e- 63 5 ft 3 

### ;
• Tota l Volume-1,27 0 ft 3 

### ; • Averag eFlu eGa s Flowrate-14,10 4 acf m(23 5 frVsec) ; an

d
• Tota l Combustio nZon eResidenc eTim e= (1,27 0 ft 3 

### ) / 23 5 frVsec ) = 5. 4 sec . Thehazardou s wast

ega s residenc etimefo r

Uni t 3 i s calculate da

s follow s usin g th

ethree-run averag efo r

th estack ga s flowratedurin g th

eUnit 3 CfPT :

• Primar y Combustio nChamber Volum e- 63 5 ft 3 

### ; aSecondary Combustio nChamber Volum e- 63 5 ft 3 

### ;
• Tota l Volum e-1,27 0 ft 3 

### ; » Averag eFlu eGa s Flowrate- 14,23 4 acf m(23 7 ftVsec) ; an

d
• Tota l Combustio nZon eResidenc eTim e= (1,27 0 ft 3 

### ) / 23 7 frVsec ) = 5.4 sec . Solid s residenc etim ei ntheUni t 4 kil ni s dependen

t upo nthekil nrotatio nrate , solid s be ddepth , an danumbe r

o f othe r parameters se

t b y design . Th emaximu msolid s hazardou s wast eresidenc e tim efo r Uni t 4 incinerator , i.e. , i ntherotar y kiln , i s 3 0 minute s basedo ncalculation s usin g a n equatio nfro mChemica lEngineerin g Handbook , Perry' s 5 t h

### Edition .

9

### Sinc eatomize dliqui dwast e vaporize s almos t

instantaneously upo nenterin g thecombustio n chambers , liqui dan dgaseou s wast e enterin g th eincinerator has aresidenc etimeo f approximatel y 7. 5 seconds . Th ehazardou s wast

e ga s residenc etimefo r

Uni t 4 i s calculate das follow s usin g th ethree-ru n averag e fo r

thestac k ga s flowratedurin g theUni t 4 CfPT :

« Primary Combustio nChamber Volum e- 1,34

6 ft 3 

### ;
• Secondar

y Combustio nChamber Volum e- 3,084 ft 3 

### ;
• Tota l Volume-4,43 0 ft 3 

### ; « Averag eFlu eGa s Flowrate- 35,32 9 acf m(58 9 frVsec)

; and « Tota l Combustio nZon eResidenc eTim e= (4,43 0 ft 3 

### ) / 58 9 frVsec

) = 7. 5 sec .

1 0