APPENDIX E 

MOST RECENT NOC 
Notification of Compliance (NOC) Report 

Veolia ES Technical Solutions, L.L.C. hereby submits the Notification of 

Compliance (NOC) Report in compliance with 

40 CFR 63.1210(b) and 40 CFR 63.1207(j) 

Applicable Rule: 40 CFR Part 63.1200, Subpart EEE — National Emission Standards for 

Hazardous Air Pollutants for Hazardous Waste Combustors. This NOC 

is be i ng made i n acco rd a nee with §6 3.9{h). 

SECTION I 

GENERAL IN FORMAT EON 

A. If you have been issued a Title V permit, do not complete this form. Submit your NOG in 

accordance with your Title V permit. [§63.9(h)(3)] 

B. If you have not been issued a Title V permit, complete the remaining portions of this section 

and afso complete Sections li-IX. [§63.9(h)(2 

C. Print or type the following information for each facility for which you are making notification of 

compliance status: 

Operating Permit Number (OPTIONAL) Facility |.D. Number (OPTIONAL) 

V-l L-1716300103-08-01 MLD093642424. 

Responsible Official's Name/Title 

Doug Harris 

Street Address 

#7 Mobile Ave. 

City State 2|P Code 

Sauget IL 62201 -1069 

Facility Name (if different from Responsible Official's Name) 

Veolia ES Technical Solutions, L.L.C. 

[ 

Facility Street Address (If different than Responsible Official's Street Address) 

Facility Local Contact Name Title 

Doug Harris General Manager 

Phone (OPTIONAL) 

618-271-2804 

City. State ZJP Code 

Sauget M l 62201 r-1069 

D. Indicate the relevant standard or other requirement that is the basis for this notification and 

the source's compliance date: (§63,9(b)(2)(iii)} . 

Basis for this notification (relevant standard or other requirement) Compliance Date (mm/dd/yy) 

40 CFR 63,1200 October 14, 2008 

i 
SECTION II 

CERTIFICATION (Note: you may edit the text in (bin saclfon us appropriate) 

Based upon information and belief formed after a'reasonable inquiry, I, as a responsible official of 

the above-mentioned facility, certify the information contained in this report is accurate and true to 

the best of my knowledge. The above-mentioned facility has complied with the relevant standard 

or and other applicable requirements referenced in the relevant standard, [§53.9(h)(2)(i)(G)] 

Name of Responsible Official {Print or Type) Title Date{rrinydd/yy) 

Doug Harris General Manager 03/16/2010 

Sicjnaturer-af Res pons jtfe Offjcial 

2 1 

SECTION III 

Describe the methods you used to determine compliance. [§G3,9(h)(2)(i)(A}) 

RCRA TriaE Bum Data from EPA approved testing as required by the RCR A Part B permit and using all 

approved EPA methods were used to demonstrate compliance with all applicable emission standards 

defined in 40 CFR 63.1219. In addition, Comprehensive Performance Testing approved by USEPA, Region 

5 on August B, 2008 and conducted in August and September of 2008 and Comprehensive Performance 

Testing approved by USEPA, Region 6 on November 25, 2009 and conducted in December, 2009. See .the 

' attach ed O per ati fig' Parameters' Tables and 'HWC 'MACT Emission 'Sta rida fds' tab' ie' To r U rifts' 2/3' a rid Unit %\" 

that define the operating parameters established during testing that ensures compliance with the 

performance standards. ' • 

SECTION IV 

Describe the results of any performance tests, opacity or visible emission observations, 

continuous monitoring system (CMS) perform a nee evaluations, and/or other monitoring 

pracedures or methods that were conducted. [§63,9(h)(2)(i)(B)3 

| See attached test results that were used to develop the limits defined in the Operating Parameter Tables''"-

• referenced in Section ill of this report. These results also include CMS Performance evaluations and 

monitoring methods, 

SECTION V 

Describe the methods you will use to determine continuous compliance, including a description of 

mon itori ng and repo rtin g req uire m e n is a nd test methads, [§63,9(h)(2}(i)(C}J 

| Continuous compliance is based on the operating parameter limits established from compliance testing,'',. 

! defined in the attached Operating Parameters Table referenced in Section III of this report. These 

i incinerator operating parameters are monitored continuously to verify compliance by. a process • 

monitoring and control system. The details of these systems are defined in detail rn Section 2.0, 

Incinerator Process description referenced in Section VIII of this report and attached. 
SECTION VI 

Describe the type and quantity of hazardous air pollutants (HAP) emitted by the source (or 

surrogate pollutants if specified in the relevant standard), reported in units and averaging times 

and in accordance with the test methods specified in the relevant standard. [§S3.9(h){2)(i)(D)] 

See attached test results from compliance testing that was conducted to demonstrate compliance with 

the HAP's and other pollutants defined in Subpart EEE, 

SECTION VII 

If the relevant standard applies to both major and area sources, present an analysis 

demonstrating whether the affected source is a major source {using the emissions data 

generated for this notification. [5e3,9(h)(2)(i)(E}] 

This facility is a major source due to its applicability to meTJESHAP regulations, specifically Subpart EEB'. 

and Subpart DD. Regardless of the facility's emission concentrations, this facility is a major source by ' 

definition. 

SECTION VIII 

Describe the air pollution control equipment (or method) for each emission point, including each 

.control, device .(or. method} for each hazardous, air pollutant and the centre! efficiency .(percent) for . . . 

each control device (or method). [§e3.0(h)(2)(i}(F)3 

! See attached Section 2,0, Incinerator Process Description from 2009 Performance Test Plans for 

.' Incinerators 2, 3 and 4 that describes the air pollution control equipment for each emission point, Also,, 

i see attached the compliance testing data defined in Section IV of this report that details the control. 

I efficiency for each control device. 

SECTION IX 

A, Did you submit an application for construction or reconstruction under §63,5(d) that contained 

preliminary or estimated data? [§63.9{hJ(5)J 

Yes I'I. , , No j , , . Not applicable J , (did not submit an application for construction or 

reconstruction). 

8, if you answered yes, provide actual emission data or other corrected infonnation below, 

END OF FORM. A Responsible Official must sign this form - See Section If, 

3 
#<\ HWC MACT Emission Standards 

• • 'i 

Parameter Units Sluniard (_p,7% 02) M.ethpd of Compliance 

Dioxin/Furan (D/F) ltg/dscm'IEQ ' 0.20 (>400 deg F) Operating Parameter 

0.40(<400degF) Limits "•• 

Mercury (1-Ig) ag/daem 130 Opiating Parameter 

Limits '• 

Semivolatile Metals (SVM) ug/dscm 230 Operating Parameter 

Cadmium, Lead Limits 

Low Volatile Metals (LVM) ug/dscm 92 Operating Parameter 

Arsenic, Beryllium, Chromium Limits 

Carbon Monoxide (CO) PP^ v 100 Continuous Emissions 

Monitor 

Hydrogen CMoride/Ciilorine ppmv 32 Operating Parameter 

«:;,.(HC:/C12) \ . .. Limits . -

: 

Particulate gr/dscf 0.013 Operating Parameter 

Limits 
UNITS 2/3 OPERATING PARAMETER LIMITS

 1 

Operating Parameter Units Limiui Teal Dare 

Performance 

Standards 

Maximum Total Pumpable T ,b/lw 

Waste (Hourly Rolling Tote]) 

Maximum Total Fa/anlnijs Lb/hr 

Waste (Hourly K(tiling Total) 

Maximum SLack Gas Kiow Acfm 

Rate (Hourly Rolling Average} 

Minimum Primary Combustion Deg p 

Chamber Temperature (Hourly 

Rolling Average) 

Minimum Secondary Combustion Deg i ; 

Chamber Tcmpcrauiru (Hourly 

Rolling Average) 

Maximum Baghousu in lei 

Temperature (Hourly Rolling 

-. Average) 

Max. Total Lo w Volatile Metals 

Feedrate (12 Hour Rolling Total} 

Maximum Semi Volatile Metals 

Feedrate {12 Hour Rni Jin g Total) 

Maxhrnmi Mereurv Feedrate 

{12 Hour Rolling Total) 

Maximum Chlorine i'eedrate 

(12 Hour Rolling Torn!) 

Maximum Ad a Feedrate (12 

Hour Rolling Total) 

Minimum Sorbent Feedrate 

{Hourly Rolling Average) 

Dea P 

M a x Pump. Lo w Volatile Metals Lb/hr 

Feedrate (12 flour Rolling Total) 

Lb/hr 

Lb/hr 

Lb/hr 

Lb/hr 

Lb/hr 

31(17 

15,147 

1S77 

420 

46 

47 

fi3 

0.001'J 

218 

UVlhCi , 1.57 

Mmimuiri Carrier Fluid Fto\vralo Cial/JbCtj 1.46 

(Hourly Rolling Average) 

Jau, l')')3 

Jan, 1993 

Jan, 1993 

Dec, 2Q09" 

Dec , 2009 

Dec, 2009 

•51 Lp, 20 OH 

Sap, 2008 

Sep, 

Aug, 2008 

Aug, 2008 

Oct;, 2009 

Dec, 2009 

Deo, 20 00 

DRL , D/F 

DRE, IVP 

DR.F, D/F, 

Part., SVM , 

L V M 

DR1L D/F 

DRE , D/F 

D/F, SVM , 

L V M 

L V M 

LV74 

S V M 

SVM , LV M 

IICIC12 

Part, 

HCL/GI2 

HCI/C12 

* Operating pavamctiir limits m Luble reflect more conservative value between Unit 2 aud Unit 3 test data. 
iriSTT 4 OVFMATTNG PARAMETER LIMITS 

Operating Parameter Unas liinits Teat Date 

Performance 

Maximum Total Pumpable Lb/hr PCC-3291 Dec, 20(W 

Waste (Hourly RollingTotal j SCC -1176 

Maximum 'I'otal I la^ar-dous l,b/hr r(T,• 12.K97 I )ee, 2009 

WftSW Caourly Rolling XofeiJJ SCC - 117(5 

Maximum StaeUtrrw l-'lnw Acfm 37,432 nsc,2(KW 

Rate (Hourly Rolling Average-) 

Minimum Primary COmbU-SCkiti Deg p 1'19!J Beo. 2009 

Chamber Temperature {Hourly 

Rolling Average) 

Minimum Secondary Cu-inbiiiiiion DegF 1B8G Dec. 2009 

Chamber Temperature (Hourly 

Rrilling Average) 

Maximum Baghouse Jo let Dcg f>- 400 I )et 200.9 

' I 'esuperarure {[ ] oti rly K o I) i ng 

.A vcrHg?) 

Max. J'ump. I^my Volatile Mstals 3,1>/jir +7 Aug,, 200-5 

•':Pee(tmeil-2 How Ralling-Towl) 

Max. • I 'otal J jow Volati la Merass I ,b/h r 50 Aug., 2008 

FeerlnUe (12 Hour Rolling Toltil) 

Maximum Hem i Vol a>i ] e VI esals 1 .b/h r 61 Aug,, 2008 

Feed rale (12 Ho ur Rolling To(fil) 

Max i muni Mereury J'eeit rate J.rotif 0,026 Aeg.. 200 S 

(12 Hour Rollins Tolal) 

Maximum Chlorine Peed rate I,Mir 229 Dec, 20O!> 

(12 Him- Rolling Total) 

Maximum A.sli Peed Raw (12 I.Mir 64P1 Deo. 2009 

1 lout Ruling To ml) 

Carbon fnjecrion 1'eedrate J.b/br 6.2 Deu, 2003 

(Hourly Rolling Average) 

DUK, IVK 

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 

Hg 

SVM, LVM , 

11 CI/CI2 

Part, 

D/F, Hs 

Mi drawn Sorbent Feetirale- Lb/lb Ct2 2.25 

{Hourly Rolling Average) 

Minimum Carrier Fluid Flowrate Gal/lb Cl a 3.10 

(Hourly Roiling Average) 

Dec, 2009 

Dec, 2-QM 

HCI.;CI!2 

JICl/f:i2 
UNIT 2 

EMISSION RESULTS 

i i 
ENSR 

Tiib)e 3-3 RWI 2G Samplin g Parameters an d Emissio n Result s - Wee k of Augus t 11, 2006 

I Samp J-i Puramefe•-

;Haiwiie1nc. Hressu/e 

VnlMite Metered 

Gsmplii_yijjume 

jkjoisturpj 

i02_at Slack _ 

, j if)yijt.5^?.^. J®IPR,.-. 

i Stark .Fjowraj© 

j'teokirefe; 

r* * r 

•Quantify__CtiiectefJ 

[Stack CoJie. @. 7 •Si Oj 

[Stele Dnsskirr Raffi 

QuflnStjf Coljnclctj 

Stack Coric. @T % 

j Stock Emission- Kate _ 

i "..r::r:'::]': r..: 

units 

in. Hg 

_cfscfm 

'St""' 

.„JH<L-

_ 1 

"i-iMtr' 

1§':5<T' 

ea 

2 

"73:16 ~ 

LVM 

m.5_ 

5S.0 

tT.St);:04 

TiseE-iii-j 

j 29.55 

Too^ T 

j—4g3'"'" 

"r^'ayo"" 

! 96 

""j" 54.&S _ 

•Qutanllty Conu.Eted _ ^ 

1 Stock Gone. @ fti.__2 

.l^okCmission^'t o 

:

Leat1_jTPM • 

Quantify ^Coljectnd^ 

Stock ^£n^@J%; Oa _ 

Stec-k irrrfesfow Rate-

; Stack Cone. 

; Bfi^Uiam jBe> -

j lQna>i% Coltectsd _ 

j Stack Cent. @7 % 0 2 

! Slack Emission Rote 

iLVM; Totals* 

jSVMTotaJ-

..m_. 

po/jvf 

g/sec 

...j... 

I 

SVM 

fjg/mf4 

gfeee 

Ijg/m* 

I'M**'.. 

g/sec 

1.9!! 

l'.3S " ' 

\Z37E-Vr3 

.L_2??- 5. 

j_ _ 22&T_ 

[Y.61E-04 

Mir" 

__;__0.Z0 

230.1 

j 5B.2 ^ 

13-Aug-OB 

12:47" 

4 1130'' 

""97 

29.61 

_81.9&6 

msji" 

''"4b.1T" 

'"5/175"" 

9 5 " 

i____37.S 

y7:P!iF:o+ 'JSiE-04 ' 

l . Z.!K3 

74J27E- M 

1'p5E: fl5' 

I 

__o.gp...... 

tmI-0 6 

2413 

.,j„. V3-T5__, 

T" 47.76 

f __75J5 ___ 

T"t.2t' ' 

"JTesE^os 

'241.3 

-i v 

[3.3eE-03.. 

1'4~23E4il4" 

...API.:.... 

1.31 ' 

'lji2E-SI" 

'2.29Ei's 

I 

4 -> 

I a.6?___ 

i 3J 0 

355.06 

23B' i 

4.i'4E-04" 

J.3STOte-^os-" f ''•tJBE-^js' 

,_CC.Z0_ 

J 0.13 

51.6 

242.5 

1_.ft5E:0a 

'2J3E-67' 

233.1" 

i-Veolla Ruport UnHiflnal.dcc 

3-4 GclolBr200S 
ENSR 

Table 3-4 Summary of ItWC MACT MetaTs - August 11, ^QD3 

L o w Volatile MetaEs Emissions - }'3>m3

 @ 7% 

Metals Run 1 R U M ?. ttun 3 

As 11.80 6.57 3.7FJ 

Be a.u O.O U.13 

Or 54,7 4S.3 47.8 

ffoFal LVM 5B.D 51.fi 58.1 

LVM Regulatory Standard = 37 tig/m:t 

I Semi-Volatile Metal Em restarts 

Run 1 Rnii 2 Rim 3 Average 

j Pb 329 240 241 

Cd 1.3B 1.34 1.21 -i 

kota! SVM 230 242 242 

r • S VM Regulatory Standard = 240 |jg/rrf 

1 

| Mercury Emissions -ugfm 3^ 7% 02 j 

R u n 2 | Ru n 3 Average 

58.0 5B.2 UTA 5/.9 

Mercury Regulatory Standard = 13D |jg/m3 

Cto(KUI^1^*fii^'!VillU.OC»LS-tVTorrpV*la3D30SSa 3-5 QSt£her2DDS 
KNSR 

Table 3-5 R M 29 Sampling Parameter s an d Emissio n Result s - Week af Septembe r 6, 2008 

Run Ks. 

Dain 

Start Timo 

Stop Time 

Uriilsj 

1 

r

 14:35 

" 16:46 

'09-Stsp-UU 

r

 12:20 

r

 14:30 

3 

r

1Q-S3j:-[ifi 

r

 09:44 

r

 11:G3 __ AV£5 

' 29.71 

' 77.059 

77.452 

41,5 

1 M 6 

r

 3B3 

5,015 

1U4 

SawpEotf Paitutieters — 

Barometric Pro a sure 

Volume Metered 

L3 simple Volume 

Moisliire 

O2 at Stack 

Avf), Stack Temp. 

Stack HowralQ 

Isokinetics 

in. Hg 

ricf 

dscf 

% v/v 

% dry 

T 

dsc;m 

% 

T

 29.60 

r

 77.362 

75,?SR 

41.4 

r

 1121 

r

 385 

4,698 

107 

" 29.75 

" 79.269 

78.407 

41.2 

*• 10.91 

r

 381 

5,099 

103 

r

 ?3T2 

78.654 

41.8 

r

 1TH5 

r

 384 

•10O 

__ AV£5 

' 29.71 

' 77.059 

77.452 

41,5 

1 M 6 

r

 3B3 

5,015 

1U4 

TottlCltroiiiiuiitl'Crl --

Quantity Called fid 

Stack Cunc. @7%.Q2 

Slack Emission Rate 

LVM 

|jg/m3 

lb/hr 

g/sec 

12.1S 

B.1G 

1 .OOE-0^ 

1.26E-05 

2,79 

1.74 

2.4GE-05. 

3.02E-06 

9,10 

5.98 

0.1OE-D5 

1.O2E-05 

UM 

5-29 

'6.85E-05 

'0.G3EOG 

Cadmium fCtl — 

Quantity Collected 

Stack Emission Rate 

SVM 

m 

• ug/m2 • 

lb/hr 

pfsec 

2.73 

• • 1:B3 • • -

Z25E-05 

2..i3E-06 

2.74 

• •• 1:71 • • • 

2.3GE-05 

2.36 E-DS 

2.20 

S-M--

1.S4E-0G 

2.44E-06 

" 255 

'•••i.aB-- • • 

'2.1BE-05 

" 2.75E-06 

LeadfPtOQuantfty Coliected 

Slack Cone. @ 7% 0 2 

Stack Emission Rule 

SVM 

Mg 

ug/nrf 

Lb/hr 

g/sec 

45.6 

3Q.6 

3.7EE-U4 

4.74E-05 

13.S 

6.7 

1.20E-04 

. 1.51 E-05 

ay.o . 

25.4 

3.45E-04 

4.34E-05 

' 32,04 

21.6 

r

2.8QE-04 

' 3.S3E-US 

Quantity Collected 

Stack Cone, @7%02 

Stack Emission Rate 

N3 

' ug/nrr3 

lb/hr' 

g/sec 

• 2.80 

1.00 

' 2.31'EtCS 

. 2.9JE-06 

2.1P 

1.31 

1.81 E-D5 

. 229J=-Pe 

2.10 " 

1.37 

1.05E-QS 

• 2.34E-C6 

'* 2.33 

1.52 

r

1.99E-BG 

""ZSIE-OB 

-

Bezslinttn EGjct « 

Q'aahfity Collected 

Stack Cone, @ 7% 0 2 

Stack Emission Ratojig/m3

' 

. !b/hr 

g/sec 

• 0,20 

0.13 

• 1 .B5E-Qb' 

. 2.08E-07 

0.20 

•0.12 " 

' 172E-0S 

2.17E*07 

'• • 0.20 

0.13' 

1.77E-D& 

2.22EA7 

0.20 

0.13 

'1,71'E-GB 

r2,16E-07 

LVfil Total = 

• ug/mB-

10.2 3.2 7.5 G.S 

SVM Total = • ug/mB

- 32,4 . 10.4 26.9 

G.S 

WanSa Report 'Ji £12 tral.dee 

3-6 Cteuhcr 2005. 
ENS R 

Tabln 3-Q Summary of UWO MACT Mctats - September 8, 2006 

Low Volatile Metals Emissions • u.g?rrr* @ 7% Oz \ 

Run 1 ' Hun 2 Run 3 . Average 

As . 1.0S 1.31 1.37 

Be 0.13 0,12 0.13 

Cr 1.7 6.0 

Total LVM 10.2 3,2 7.5 S.9 

LVM Regulatnry Sianriard = 92 |jg/m3 

Seimi-Volatile Metal Emissions 

Metals Run 1 Run 2 Run 3 Average 

Pb 3U.B 8.7 25.4 

Crt 1.83 1.71 1.43 

Total SVM 32.4 10.4 26,9 23.2 

SVM Regulatory Standard = 230 |jg/m3 

' .. 

CiVDOCllME-IWariokTWFJ-OCALSHVrcm^nDtouPaassD 

Wcolb Report Urfl 21i/v^ Ace 

3-7 •debar 2006 
A^COM 

Ta b Ie 3 -2 RMSttSASamplingPara mete rs and £mis5 io n Res 11 Its - Tota f Ch Jo ri cf e/P B 

Run Identification Run 1 Run 2 Run 3 Average 

Run Date 12/08/09 12/09/09 12/10/09 

Start Time ' 10;O5 . 9:45 11:00 

Stop Time 11:11 10:49 12:03 

Exhaust Gas Conditions 

Temperature (deg. F) 378 363 380 374 

.Moisture (volume%) 44.4 42,9 43.2 43.5 

' 'Oxygen (dry volume %) 10.3 10.4 9.3 10.0 

Carbon Dioxide (dry volume %) 8.6 8.2 8.1 8.3 

Volumetric Flow Rate 

acfm 15,453 16,634 16,661 16,250 

dscfm 5,352 5,963 5,921 5,745 

Total Chlorine 

ppmv, dry _) 7% 0 2 13.4 16.0 23.5 17.7 

% of Standard

 3 42.0% 50.2% 73.5% 55.2% 

Total Particulate Matter 

gr/dscf © 7% 0? 0.0013 0.0017 . 0,0008 0.0013 

% of Standard

 b 9.7% 13.2% 6.2% 9,7% 

" |-OCr 2 Standard - 32 pponv, dry @ 7% Oa 

b

 Particulate Matter Emisslsn Standard ^0.Q13 gi/dscf © 7% O3-3 
Table 3-3 RU (J023A Sampling Parameters and Emission Results ~ Djoxirt and Furan 

Run Nc. j 1 Z _Ji , Ave rage 

Date 

Start Time 

_ — 

Date 09-lfec-na 

Start Time 12:30 

_ — 

12:59 13:00 

Stop TTms 15:36 16:54 16:05 

Units j |ri l| j| if! [I Ur? M if i in l?i l^i uri^i^ 

S^mpJe Volume dscf 107.857 121.809 121,529 -117.065 

Sample Volume m

1 3, OS 3'. 45 3.44 3.31 

Moist ura Contont % Wv 47.3 - 43,9 . 46.1 45,8 

0 2 Co rcc ent ration % vtv (dry) 9.10 Ei.30 8.20 8.87 

C 0 2 Concentration % v,V (dry) 6.43 5.14 7.90 8.16 . 

. Isokinetics % 98 95 97 97 

Siac k Flowrate 4,994 5,652 5,699 5,515 

PCDD/PCD F 

Parameters TET* (a) 

pa ng/rrr3 

• TEQ 

pg ng/m3 

,TEQ 

P9 ng/nrf 

TEQ 

1.00 

675 0 

7.01 2.3E-03 5.61 1.6E-03 7.17 2.1E-03 

'*XOE-03"~ 

1.00 

675 0 25,2 

"32.2 

4.1E-D3 

'"'I7VE"^03'"" 

21.9 

"2976"" 

3.2E-03 

"&6E3 4 

20.6 

2.1E-03 

'*XOE-03"~ 

f,2,3,4=7=a-HxCDD 0.10 

25,2 

"32.2 

4.1E-D3 

'"'I7VE"^03'"" 

21.9 

"2976"" 

3.2E-03 

"&6E3 4 22.7 6.6E-04 

l,2,3,6,7,S-ir>s:jJl'j 0.10 53.1 1.7E-03 49.2 1.4E-Q3 36.1 1.0E-D3 

L2,3,7,B,9-HxCDD 0.10 35.3 1.2E-03 

6,9£-04"~ 199 

9.0E-04 27. a .8.1E-04 

OCDD 

0.01 

---- -

211 

~m 

1.2E-03 

6,9£-04"~ 199 

9.0E-04 

158 4.6E-04 

OCDD ~3~8E4J5 

0.01 

---- -

211 

~m 5.8E-05 200 .5.8E-0S 131 

4.6E-04 

~3~8E4J5 

2,3,74S-TCDF 0.10 25,1 8.2E-04 

lTOE-04'"' 

1B.8 

• is,i' 

5.5E-D4 17.1 5.0E-04 

.. . n A S . • • • . 4 . 

8.2E-04 

lTOE-04'"' 

1B.8 

• is,i' 

5.5E-D4 

•20,1-•• • -2-.ee-04 • • 

""77{iE-Q3 •••""••'Q'SO 

8.2E-04 

lTOE-04'"' •20,1-•• • -2-.ee-04 • • 

2,3,4,7, S-FeCDf ""77{iE-Q3 •••""••'Q'SO 108 1.8E-02 60.9 8,SE^ 3 53.S 

• -2-.ee-04 • • 

""77{iE-Q3 

., 1 .AMiZi.S^CDF , 0,10 

"o.'io" 

59,0 

""SIB 

1.9E-D3 49.2 

"35.3 

1.4E-03 ,,„,TM^.... , 

2S.5 8.3.E-04 

"T3E-04"" 

2,3,4,6,7,8-1 (xCDF 0.10 97.7 3.2E-03 5S.1 

"17.2 " 

1.7E-03 

""s"0E4i4"'"' 

4.1E-04 

46.0 

""1374""' 

1.3E-03 

""3,9i'^4"""' 

""2761-04 

L2,3,7,B,9-HxCDF • o.to 

o76T 

26.7 

""ii??;* 

8.7E-04 

"s.SE^ M 

"'e".7E^"5"" 

5S.1 

"17.2 " 

1.7E-03 

""s"0E4i4"'"' 

4.1E-04 

46.0 

""1374""' 

1.3E-03 

""3,9i'^4"""' 

1,2,3,4,6,7,8-HpCDF ""2761-04 

o.to 

o76T 

26.7 

""ii??;* 

8.7E-04 

"s.SE^ M 

"'e".7E^"5"" 

142 

1.7E-03 

""s"0E4i4"'"' 

4.1E-04 

46.0 

""1374""' 

1.3E-03 

""3,9i'^4"""' 

""2761-04 

1,2,3,4,7,8,9-HnCDF D.01 

O.0Q1 

26.6 

8.7E-04 

"s.SE^ M 

"'e".7E^"5"" 22,8 6.6E-05 ' 13.9 4.0E-05 

OCD F 

D.01 

O.0Q1 48. B i.ee-os 78.8 Z.3E-05 ! 23.4 6.3E-Q6 

TOTAL TJKQ» (HS/'"*} Q.038 j.•!:.;!•-:•!,-;;:! 0.024 0.020 0.027 

TOTAL TEQs (a B /in T 7 % Oi) 0.045 

j.•!:.;!•-:•!,-;;:! 

0.028 0.022 0.032 

TOTAL TEQa fg/s) - 9.1E-11 

j.•!:.;!•-:•!,-;;:! 

6.5E-11 5.5E-11 7.0E-11 

% o f Standard " 23% 14% 11% 1S% 

* U.S. EPA (1939) Toxic Equivalency Fa«or 

FCDD.'PCDF Standfird = D.2D ng/dscm © 7% 0 , 

3-4 FQtnjHryiUID 
A3C0M 

Table 3-4 RM 25 A Sampling Parameters and Emission Results 

Run Identification 1 Average 

Run Date 

Start Time 

Stop Time 

Exhaust Gas Conditions 

Moisture (volume %) 

Oxygen (dry volume %) 

OBDecOS 

12:30 

13:30 

47.3 

9.10 

09Dsc09 

13:49 

14:49 

43.9 

9.30 

1QDec09 

14:00 

15:00 

46.1 

8.20 

45. a 

8.87 

Total Hydrocarbons 

ppm, dry 

ppm, dry adj. to 7% 02 

0.66 

0.78 

0.29 

0.34 

0,17 

0.18 

0.37 

0,44 

3-5 -tiliiav 2010 
I 

UNIT 3 

EMISSION RESULTS 
ENS R 

Table 3-1 R M 29 Samplin g Parameters an d Emissio n Result s 

Him Nn 1 2 3 

Date r

 U£-A-_o-03 Dti-Auj-aa 07-Aug-D8 

Start Time , Unit; " 12:56 

Stup Tiruo r 15:14 r

 14:41 " 15:04 AVGS 

SampljnE Parameters — 

flatomcfifc pressUfA in. tig ' 23.23 " 29.65 " 29.65 29.51 

Vo;uuia Metered dcf r

 00.539 r 87.452 ' £)5,<M3 r

 87.311 

Sampfe Volume dscr 78.488 S4,3ii8 83.5132 32.223 

Moisture % vfy 43.0 40.6 42.2 

02 at Stack %di y 11.99 to.jm 11.98 11.04 

Ave. Stack Temp. T ' 372 ' 377 ' r

 374 374 

Stack Flowrate dseffit 5,665 iirfS90 5,758 

Isokinetics •% 92 5)8 ' 95 9-,r

i 

MercuryfHs!> 

Quantity Coltacted pg 78.5 305 ^ S0.4 

Stuck (*'ortc. @ 7% 02 54.& 61.1 57.6 57, J 

Stack Emission Rate 'iWbr 7 49E-01 R39E-CH G.19E-04 B.30E-CHr

' &.44E--0S 1-.10E-04 1.03E-O4 1.05E-C4 

B.30E-CHr

 1.05E-C4 

Total Cironriusi fCrt - LVM 

Quantity Colfeeterf 37.50 21.76 ' 

fctack Cone. @7%02. • 26.22 17.81 14.21 19,41 • 

' 'SfackBrii-sirtiVRtfe'' ' lb/hr' ' ' ' 3.5>8E-tW' • • • 2.02E-D4' r'2.7Gt-b4' 

g'ssc 4.S1E-05 3.45E-Q5 2,55E-G!3 r 3.50E-O5 

Oa/aJiwi fc'fl) — SVM 

Quantity Collects^ 0,24 [><X) 0.63' 0,59 

Stack ODFIC. @7 & 0- 0.17 0.53 !>.41 0.37 

Stack Emission Pate JWttf 8.D6E-06 5.35E-&3 '5.40E-09 

g/sec 2.86E-D7 1.02E-Q3 7.37E Of r S.80E-D7 

SVM 

Quantity Collected 83.5 114 70.1 ' 8M B 

Stack Cpnis. © 7% 0 2 ug/rn? ' 5B.4 ' . 66.8 53.9 

Stack Emission'Rate M i r ' 1.O2E-03 S.50E-04 '8.24E-04 

4.O0E-04 ' 1.29E-D4 . iU ^ J S ' 1.G4E-04 

Arsenic (Asi— 

Quantity Collected 3,15 .' 3.75 1.94 2.535 

- Steels ttorac.@ 7% Q-,j • : .2-19 1,27 1.89 

SiarJ? grpessjorvRGta tt^hr 3.O1E-05. '2.73&Q5 

CffefiC . ..3,79E-fl3 4.24E-0B' 2.27E-D8 ' 3.43E-06 

• 

Quan % ejecte d • M • • 0.-20 .• ' • 0.20 0.20 ' a?.o • 

. Sfeck Caw , @ 7% 0^ 0.14 0,12 0.13 0.13' 

StBCk Emission Rain lb/hr 1,0lK-«? .• 1.80E-OS T.BSE^B "1.85E-06 

g/sec 2.4tE-07 Z26E-07 •2.34^-07 r

 2.34E-07 

LVM Total - 28.6 20.1 15.0 21 j» 

Tgial = 'ng/rrf ''53.8""' 87.t 46.2 67.3 

CSDOCyME-t'ilt!arith.'7V/I'LCICALS-1,iTamiAnDlEst390SSa 

Weolfa Report Unit 3 draAdDC 

3-2 Ootaber2tlOB 
Table 3-2 Summary of HWC MACT Metals 

. Lo w Volatil e MetaJ s Emission s - jjg/n f @ 7 % o 2 

Metafs R u n 1 R u n 2 R u n 3 Avera§& 

A s 2.20 2M 1.27" 

Be 0 J 4 0.12 0.13 

Gr 26. 2 17.8 14.2 

Total LV M 28.Q 20.1 15.6 21.4 

L V M Regulatory Standard = 

SejDi-Vo)a!H e Meta l Emission © - ra'in3

 @ 7%Q s 

Met ate R i m 1 R u n 2 R u n 3 Averag e 

Pb 58.4 66.6 . 45.S 

C d 0.17 0.53 0.41 

TofaJSV M ss. e 

1

 07.1 48.2 57.3 

S V M RfisufattJry Standard = 230 \ig!nf 

..... . 

Mercur y Emission s -pg/m 3 @ 7 % 0 2 

S i m 1 R u n £ R u n 3 Average 

54. 3 61.1 57,8 57-9 

Mercur y HeguMor y Stewar d = 130|jg/m 3 

C:TOCUME-1lWaridi,TVVJLOWL&-1vremp^aiBsl5SDS[:Cl 

We:(jII? tepon Units drafLdos 

3-3 
Tab re 3^2 RM 5/26 A Samp [frig Parameters and Emission Results - Total Chloride/PM 

Run Identification Run 1 Run 2 T?un 3 Average 

Run Date 12/01/09 • 12/02/09 12/03/09 

Start Time 11:16 .10:05 10:48 

Stop Time 12:21 11-09 11:51 

Exhaust Gas 'Conditions 

Temperature (deg, F) 377 377 378 377 

Moisture (voJume %) 43.4 46.9 42.1 44.1 

Oxygen (dry volume%) 9.5 7.8 10.4 9.2 

Carbon Dioxide (dry volume %) B.3 10.0 8,0 6.8 

Volumetric Flow Rate 

acfm 14,1 G7 1-4,817 15,340 14,751 

dscfm 5,039 4,874 5,573 S.1G2 

Total Chlorine 

ppmv, dry @ 7% 02 10.7 9.8 21.5 14.0 

% of Standard

 B 33.5% 30.5% . 67.1% 43.7% 

Tofa! Particulate Matter 

gr/dscf @ 7% 0 2 0.0017 0.0015 0.0016 0.0016 

% of Standard * 13.0% 11,9% 12.3% 12.4% 

flHCra?SlafldsiEl=32ppfirivi dry@7%Oa 

b

 Particulate Mat.sr- Emission Standard = 0.01 3 gr.'cscf @ 7%Oj 

3^3 Hafuary 201Q 
A..COM 

Table 3-3 RM 0023A Sampling Parameters and Emission Results - Dioxrns and Furans 

Run No. 1 2 3 Averaqe 

Date Sn-Dsc-OS 02-Doc-CS 

:;;:;:::y:\;::;;;:i;::;:;:;x;0;;:;:.:;:;.;:;:".; 51a.1 Time 13:41 12:30 13:18 :::-::'

:

:-:-:::;;:;: 'v ::y:\;::;;;:i;::;:;:;x;0;;:;:.:;:;.;:;:".; 

Step Time 16:49 15:35 16:53 

!•:•. :•: v—'::::•::•: ::>:~::A': •:•:-:•.•: Units '!-:;.;!v.;.;Xv-;";-Vv;-; :

:

:v:

:

:

:

:o:':lv':::':::

:

:

:

:o:':o:: 

Sample Vol'me dscf 106.679 112.729 120.263 113.231 

Sample Volume m

1 3.02 . 3.19 3.41 3.21 

Moisture Content %vtv 48,2 43.1 42.3 46.2 

0 2 Concentration % v,V (dry) 7.30 7.30 9.50 8.03 

C 0 2 Concentration % v,V (dry} 9.93 . 9.78 8,15 9,29 

Isokinetics % 109 107 S3 105 

Stack Flowrate dscfm 4,452 4,810 5,573 4,94S 

PCDD/PCD F 

Parameters TEF(a) 

PS 

TEQ 

pg nqlnf 

TEQ 

P9 ng/mJ 

TEQ 

2,3.7,8-TCDn 1,00 5.31 1.9E-Q3 i 3.60 1.1E-D3 4.60 . 1.3E-03 

l,23,l,\i-?eCDD 0,50 25.1 4.ZE-03 17.0 

17,3 

2.7E-03 21.4 3.1E-03 

[,2,3,4,7,8-HjiCDD . 0,10 27.2 9.GE-04 

17.0 

17,3 B.4E-04 18.1 5.3E-04 

1,2,3,6,7,8-IijcCDD 0,10 59.5 ZOE-03 40.0 1.3E-03 41.4 1.2E-03 

d.io 37.7 1.2E-03 27.3 8.6E-04 26,7 7.8E-04 

1,2,3,4,6,7.8-1-1 pCDD 0,01 406 1.3E-03 253 7.SE-04 j 272 

8.0E-04 

ocn o o.oot 540 1.SE-04 ! 330 1 .OE-04 348 1.CE-04 

• • • 23;7^TCT>P G.-1G •33.$-• •11E-03-- I -25,8 •'..&.1E-G • 4 .. • 30.5 • • -9,1£-04 • 

13,3,7,8-PeCnF 0,05 46.2 7.6E-04 

""1.6E-02."" 

31,8-

"64 S " 

5.DE-04 39.2 5.8 E-04 

2,3,4,7,8-VeCDF 0.50 93,3 

7.6E-04 

""1.6E-02."" 

31,8-

"64 S " 1.0E-Q2 83.0 1.3E-02 

0.10 72,0 2;4E-Q3 43.2 1.4E-03 51.5 1.5E-03 

0.10 61.3 2.0E-O3 39.2 1.2E-03 49.8 1.5E-03 

0.10 88,4 2.9E-03 53.3 1.7E-03 71,1 2.1E-03 

1,2,3,7.8,9-HxCPF 0.10 20.5 6.8E-04 13.2- 4.1 E-04 15.8 4.6E-04 

1,2,3,4,6,7,8-IfpCDF 0.01 233 7.7E-04 123 3.8E-04 

"T9E-05 " 

131 

"15.7 " 

3.&E-D4 

1,2,3,4.7,8,9-HpCDl- 0.01 [23.5 7.8E-05 "4.6E"05" 

123 3.8E-04 

"T9E-05 " 

131 

"15.7 " 

3.&E-D4 

"4.6E"05" 

OCDF 0.001 85.2 2.8E-05 45.9 . 1.4E-05 40.2 1.2E-05 

TOTA L TE,Qs(ug/niJ) = 0.039 .;:-:-. 0.024 

:;>!;"-: 

0.028 0.030 

TOTA L TEQs (ug/m1 @ 7 % 03) 0.039 0.024 :;>!;"-: 0,035 0.O33 

TOTA L TEQsfer<0 ^ B.1E-11 5.4E-11 

:;>!;"-: 

7.5E-11 7,0E-11 

% of Standard

 6

 .= 20% 12% :•:-:•• 17% 1S% 

a

 U.S.EPA(19iU.S.EPA(1989) ToricEquwalency Factor 

b

 PCDQ'PCDF Standard = -3.23 rig/dscm @ 7%02 

3^: .-BSni«?2010 
AICOM 

Table 3-4 RM 25A Sampling Parameters and Emission Results 

Run identification 1 Average 

Run pate 

Start Time 

Stoo Time 

OlDecOQ 

13:41 ' 

14:41 

02OSC09 

• 12:30 

13:30 

03Dec09 

13:18 

14:18 

Exhaust Ga s Conditions 

Moisture (volume %) 

Oxygen (dry volume %) 

Total Hydrocarbons 

ppm, dry 

ppm, dry adj. 7% 0 2 

46.2 

.7.30 

0,91 

0,93 

43.1 

7.30 

. 0.64 

0.65 

42.3 

fi.50 

0.35 

0,42 

46,2 

8.03 

0.63 

0,67 

3-5 Siimd' win 
UNIT 4 

EMISSION RESULTS 
ENS R 

Table 3-2 RM 29 Sampling Parameters ^ntl Emission Hates 

Run No. 

Date t 

Start lime 

S(up Time 

Units 

1 

r

 -15:37 

2 

K

22-Aiii} (Bt 

" 1J):U0 

r

 13:01 

3 

'.23-Aug-OB 

r

 08:55 

r

 10:59 AVGS 

Barometric Pressure 

Velum e Msiersrt 

Sample Volume 

Moisture 

0 2 A Stack 

Aw#. Stack Temp. 

Stack Flowrate 

i isokinetics 

in. H15 

dcr 

dscf 

& dry 

*F 

dscfm 

% 

r

 72.GA 

r

 go. TM 

6!J.Q23 

39.0 

' 12.27 

r

 390 

17,260 

101 

" 2^m 

* 89.784 

flU.433 

33.5. 

r

 12.13 

' 388 

17255 

im 

" 29.64 

"31.420 

89.264 

4U.3 

r

 'i1.G3 

r

 334 

17,189 

102 

" 29.62 

r

 90.714 

r

 12,01 

' 391 

17,241 

j m . 

Quantity Collected 

Stack Cone. @ 7% Oi 

Ststk Emission Rsfe.. 

ug/nr3 

Ih/hr. 

g/sec 

59.E 

37.9 

1.53E-fJ3 

1.93E-Q4 

387 

24.4 

9.99F-D4 

T.26E-04 

12.3 

25.0 

1.08E433 

1 mv-.m 

r

 4E.9 

23.1 

r

1.2DE-03 

Tntnl Chromium (C.r) — 

Quantity Colinded 

Stack Coac.@7% Oj 

FUqck Emission Kate 

LVM 

Hg • 

ut]/rn3 

Ih/hr 

g/sac 

3.1? 

1.93 

. aOIE-05 

1.01 FD5 

S.20 

3.96 

1.62 E-04 

' 2.04(7 flfi 

• 8.40 

3.7ft 

T.B3S04 

• 2.05E-Q5 

r

 5.27 ' 

3.24 

r

1.35E-Q4 

" 1.70E-O5 

Cadmium fC(T> — 

Quantity Collected 

Stack Cnnc. @7 % Q2 

Stank Emission Rati* 

SVM 

|IS7m8 

lb/hr 

• g/sec 

0.80 • 

0.51 

2.05U-D5 

2.58E-06 

1.27 

- 0.80 

3.27 R-tC 

4M2E-fl3 

\:& 

0.76 

3.29E-05 

4.14E-E6 

' 1.12 

0.69 

'2.87E-D5 

" 3.61 E-DB 

Quaniity CollectedStack Cone. @.7% 6 2 , 

Stack Emission Rate 

SVM 

m 

lb/hr 

' gfeec 

' 343 

21.8 

• 8.81 E-m 

• 1.11 £04 

49.1 

30.9-

1.27E4B 

1.B0E-D4 

• 28,3 

. 1.13E-03 

1.43E-04 

' 4ZB3 

26.4 

r

 1-.09E-03 

r

 1.3BE-04 

' -Aias<siiiefAsTr~ 

• -Quantity-.Collected . 

. Stack Cone'©7% Oi 

•• Stack Emission Rate 

M9 

ug/m3 

lb/hr 

_g/$ec 

'4,52 

3.07 

1.24E-JH 

1.5BE-D5 

9.B2 ' 

6.19 

2.53E-B4 

•3.19E-05 

" ' 16,22 

9.S9 

' 4.13B04-

5.21 E-Q5 

". 10.29 

" 6.28 

'2.63&04-

" 3.32E-D5 

Be allium (Bei - . 

Quantity Collected 

Slack Ctmc. @7%0 2 

.' Slack Emission Rate 

ug/m3 

Ih/hr 

g/sec 

0,20 

0.13 

5.13E-D6 

B.47E-07 

0.20 

0.13 

5.1GE-0B 

B.5GE-Q7 

0.20 

0.12 

5.09E-Q6 

6.42E-G7 

r

 0,20 

0.12 

^5.13E-0B 

" 6.46E-07 

LVM Total - ug/m3 5.2' 10.3 13.5 

SVM Total = jjg/m3 22.3 ' 317 271"""" 21'jf-

'" 

C-UJOCUME-f'Jsarteh.lWllLOCALS-liTeftiplnotesDstiSOtf 3-3 Orf£/ber£DDE 
ENS R 

Table 3-3 Summary of HWC MACT Mr-tafa 

L o w Volatile Metal s Emission 5 7% a , 

Meluls fturt 1 Run 2 R-Jii! 3 Average 

As 3.07 B.1-3 9.59 

Be 0.13 0.13 0.12 

Cr ' 2.0 4.0 3.8 

Iota! LVM 5.2 1D.3 13.5 

I.VM Regulatory standard = 92 ug/m.<* 

Ssmi-Volatife Metal Emissions 

Run 1 Run 2 Run 3 

Pb 21.8 30:9 26.3 

Cd 0.51 0.SD Q.7B 

Tofat SV M 22.3 31.7 27,1 27.0 

SVM Regulatory Standard - 23C |jpf/rn3 

Mercury Emissions -\i_tmz @ 7% 0 2 

Run 1 Run 2 Run 3 Average 

37.9 24.4 25.0 29.1 

Mercury Regulatory Standard = 130 pg/m3 

C:TOOTOr^-l\WaricKT\iVpLCCAL3-nTcnipVMt!sP305SIJ 

VMOSffl B3.doc 
AZCOM 

Tabls 3-2 RW[ 5/26 A-Sampling Para meters an d Emiss la n Results - TotaE Chlo rscfef P M 

R u n Identification- Run 1 Run 2 Run 3 Average 

Run Date 12/16/09 12/17/09 • 12/1 8/09 

Start Time 11:38 9:46 9:50 

Stop Time 12:41 10:43 10:52 

Exhaust Gas Conditions 

Temperature (deg. F) 386 387 3B7 387 

Moisture (volume %) 35.7 35.2 35.7 35,9 

Oxygen (dry volume %} 12.7 12,5 12.6 12.6 

Carbon Dioxide (dry volume %) 5.7 5.9 '.5.5 5.7 

Volumetric Flow Rate 

acfm 46,603 46,847 44,633 43,034 

dscfm 18:845 18,645 1 7,704 18.398 

Total Chlorine 

ppmv. dry @ 7% 02 - 29.2 36.4 3.5 • 23,0 

% of Standard * . 91.3% 114% 10,8% 71 .&% 

Total Particulate Matter 

gr/dscf @ 7% D 2 

% of Standard

 b 

0.0023 0.0020 0,0042 0.002B 

18.0% • 15.1% 31.9% 21,7% 

J

 HCICIj StarearrJ = 32ppnv. dry © 7% 02 

5

 ParSci,-'el& Mater Ernissbn Standard = 0.013 gr/dscf © 7% Dz 

3-3' Pabruary 2C10 
ACCOM 

Table 3-3 RM 0023A Sampling Parameters and Emission Results - Dioxin and Furan 

Kun No. 1 2 3 Average 

Date 16-Dac-09 1S-DQ^9 

" SlsrtTime 13:54 12:30 11:45 

Step Time 16:59 15:35 14:50 

;

':-\:' : ." : . V:'!. Units 

Sample Vo'ume dscf 137.455 131,667 131.717 133.653 

Sample Volume • rn3 3.6$ • 3.73 3,73 3.78 

Moisture Content % v/v 35.S 36.4 36.0 36.0 

0 2 Concentration %Yf'v(dry) 12.60 12.40 12.30 12.43 

C 0 2 Concentration % v,'v (d iy) 5,66 4..B7 5.54 5.3S 

Isokinetics % 100 101 99 100 

Stack Fbwrate dscfm 18.601 17S655 18,002 18,089 

PCDD / PCDF 

Parameters TEF (a) 

pg rcg/rn1 

TEQ 

pg 

TEQ 

pg ng/rn2 

T EQ 

2!3,7,S-TCDD 1.00 18.8 4.8E-03 

"3.7E-02" 

24.6 

""340 " 

S.01MJ3: 20.7 5.5E-03 

1,2,3/7,8-PeCDD 0.50 283 

4.8E-03 

"3.7E-02" 

24.6 

""340 " 4.5E-02 311 4.2E-02 

1,2,3,4,7,8-HxCDD 0.10 320 

'924"" 

a,2E^Q3 ; 

•.Z4E-02"" 

287 7.7E-03 286 7.7E-03 

'!,2,3,6,7,S-HxeDD 0.10 "'24E-02'"" 

320 

'924"" 

a,2E^Q3 ; 

•.Z4E-02"" 854 2.3E-02 901 

7.7E-03 

"'24E-02'"" 

1,2,3,7,8,9-Hx.CDD 0.10 37S 9.7E-03 285 7.6E-03 388 1.0E-02 

l,2,3.4,fi,7,S-HpCOD 6.01 ' 2,944 7.8E-03. 2j442 6-5E-03 2,695 7.8E-03 

OCDD 0.001 1,245 3.2E-04 987 2.6E-04 1,189 3.2E-04 

-2J,7,8~TCDF 0'.10 90,2 2.3E-03 S7.5 2.3E-03 90.4 2.4E-03 

• • -l^V^-PeCD F 0:05 • 1-32- • •1:7E-03- • ••119 • • •1-.-6E--03" . . 1 5 1 .. . •2:0E433 • 

2,3,4,7^-PeCDF 0.50 608 7.8E-02 510 5.8E-Q2 692 S.3E^02 

[ ,2,3,4,7,S*HxCDF 0.10 282 7.2E-D3 242 

"292"" 

3.5E-03 

''7.8E4T3"' 

291 1 

'"379"" " 

78E-03 

L ,2,3,6, 7,8-HKCD F 0.10 

fj'i'6 

367 : 

7.2E-D3 242 

"292"" 

3.5E-03 

''7.8E4T3"' 

291 1 

'"379"" " 1.0E-02 

2,3,4,6,7tR-HxC!DF 

0.10 

fj'i'6 860 ; 2.2E-02 

TBE-OY " 

"Z"BI^03"" 

615 1.6E-D2 848 2.3E-02 

_ L2,3,7,8,9-HxCDF D.10 

aoi 

96.5 

"957""' 

2.2E-02 

TBE-OY " 

"Z"BI^03"" 

55.3 

"730"" 

1.5E-03 86.6 2.3E-03 

l.2,3,4A7,K-H_pCDF 

D.10 

aoi 

96.5 

"957""' 

2.2E-02 

TBE-OY " 

"Z"BI^03"" 

55.3 

"730"" 2.0E-Q3 1,007 2.7E-D3 

1 i2j314,7.8,9 -I [pC DF 0.01 132 3.4E-04 • 78.9 2.1E-C4 130 3.5E-04 

OCOF 0.001 210 5.4E-05 133

 1 3.6E-05 201 5.4E-05 

TOTAL TEQs (nR/m3) 0.218 

-•" ' '•: 

0:204 

•• 

0.241 0.221 

. T(JTAL TEQs (ag/m1 @ 7 % On) = 0.363 -•" ' '•: 0.332 

•• 

0.383 0,361 

TOTAL TEQs (gis) = - 1.9E-09 • : .': .'. . 1.7E-09 f .; ;.; _ • • 2.0E-09 1.9E-09 

% of Standard " = 91% 33% B7% 90% 

a

 U.S.EPA (1939)TDMsEquivalency Factor 

1

 PCOD/PCDF Standard = 0,40 ns'dscm © 7% o . 

3-* 
AZCOM 

Table 3-4 RM 25A Sampling Parameters and Emission Results 

Run Identification 1 Average 

Run Date 

Start Time 

Stoo Time 

1SDecQ9 

14:07 

15:07 

17Dec09 

12:51 , 

13:51 

18DecG9 

11:45 

12:45 

Exhaust Gas Conditions 

Morature (volume %) 

Oxygen (dry volume %) 

Total Hydrocarbons 

•ppm, dry 

ppm, dry ad},7% 02 

35.6 

12,60 

0.81 

1,33 

36,4 

12.40 

0,86 

141 

36.0 

12.30 

0.35 

Q.61 

36.0 

12,43 

0,68 

1.12 
• • -i 

SYSTEM REMOVAL EFFICIENCY (SRE) 

FOR 

UNITS 2, 3 AND 4 

i 
20QS Wl&tals and 2003 HCJ Testing Removal Efficiencies | , . I 

1 | 

Unit 2 (LVM) Removal Unit 3 (LVM) Removal Unit 4 (LVM) REmavai 

Em. Std.: 92 ug/dscm Run Efficiency (RE) Em. Std,'. B2 ug/dscm Run Efficiency (RE) iEm. Std.: 92 ug/dscm Run Efficiency (RE) 

(9/QB) (%} (3/QB) (%) 1 (8/0B) 

... f») 

..... 

... f») 

1 99.99973 89.899.19 1 S3.3995S 

2""' 89.99991 i 99-. 99 935 2 99.93916 

3 59,99979 ' 3 93.93954 3 99.93882 

Avg 99.59961 Ayg S9.&9936 Avg 39.99919 

Unit 2 (SVM) Removal Unit 3 (SVM) Removal Unit 4 (SVM) Removal 

Em. Std.: 230 uqJdscm Run Efficiency (RE) Em. Std.: 230 uc|/dscm Run Efficiency (RE) Em. Std.: 230 ug,'dscm Run Efficiency (RE) 

(&/Q8) (B/OB) (%> (8/08) • m 

1 89.89936 !l ' 98,99875 1 99.99633 

2 99.89977 2 98.98842 2 99.99795 

3 99.99942 " 3 " 98.08897 3 &9.&9S19 

Ayg 99.99952 Ayg 99.99871 Avg 9S.93B24 

j 

Unit2{Hg) Removal Unit 3 (Hg) Rem ova i Unit4(Hg) Removal 

Em. Std.: 130ug/dscm Run Efficiency (RE) !Em. Std.: 130 uq/dscm Run ' Efficiency (RE) Em:Std.: 130ug/dscm Run Efficiency (RE) 

(8/08) C*> . (8/08) I m . . (S/OS) {%) I m . . 

1 65.61 j i " 53.25 1 94.05 

2 51.65 2 57.36 2 86. T 7 

3 50.06 3 ! 54.56 '3 95-91 

Avg 55.77 Avg ;

 55.06 Avg 95-3B 

Unlt2 (HCT/CI2) Removal Unrt3(HCI/CJ2) Removal Unit 4 (HCI/CI2) Removal: 

Em. Std.: 32 ppmv Run Efficiency (RE) Em. Std.: 32 ppmv RMn Efficiency (RE) Em- Std.; 32 ppmv Run Efficiency (RE) 

(12/09) (%) (12/09) j _ (%> (1209) (%) 

1 90.86 : " "i " 99,99 1 99.18 

2 . • 09.63 ! 2 99.89 : 2 98.92 

. 3 •99.71 i 3 99,77 ' 3 " 99.91 

Avg '••89.80 ! Avg '9&.S5 •Avg ' 99.34 
Incinerator Process Description 

Unit 2 
2.0 incinerator Process Description 

AECOM 

2.1 Process Overview 

VEolia operates 2 Fixed Hearth Dual Chambered Incinerators (Units 2 and 5) and one rotary kiln incinerator 

(Unit 4) at the Sauget, IL facility. The too fixed hearth units are rated at 16 million Btu/hr each, incineration 

Unit No. 3 is a mirror image of Unit No. 2. Both of these units have their own waste handling systems as 

described in the sections that follow. The oniy difference being Unit No, Z is equipped with four (4) baghouse 

moduies, while Unit No, 3- is equipped with three (3} baghouse modules. However, each incinerator is 

operated identically with only three-baghouse modules in service during operation. Ur it 4 i s rated at SO million 

Btu/hr and is equipped with its own tank farm system, drum storage, bulk solids storage and feed systems. 

2.2 Waste FeecF Systems {40 CF R § 63,1207(f){1J(ii}(c) and (f)(1){ifi)(0) and (E)] 

2.2.1 Unci 2 Liquid Waste Feed System and Blending Operations 

The fixed hearth incinerator is designed to receive containers, aqueous liquid wastes, organic liquid wastes, 

specialty Fiquid feeds, gases and direct inject [[quids fed through the aqueous or organic liquid feed systems. 

These units can receive any combination of wastes - liquid, semi-solid, solid-or gases - with a heat value of 

up to 16 million Btu/hr. 

Unit 2 is supported by storage/blend tanks located in Tank Farm #1 Rates of feed are contnoffed at each 

incinerator, Segregated liquid wastes are stored untii utilised in the waste blending facilities, At thai time, • 

•x&'&M< [[quids-are delivered-to the-blending tanks where the daily liquid-feed tothe'inoineratoris'TQrrriutatectr'te'Ste'o!, 

V •' ] and released to the incinerator, Biending of stored Eiquld wastes to achieve optimum heating value and 

viscosity for incineration takes place in Tanks 2, 4, 6 & 8, Sis additional tanks (10, 20, 30, 40, 50 & 60) are • 

used to segregate different wasfa stream types for blending of liquid feed to the incinerator. Several criteria 

are important in designing a blend from available wastes that have been segregated principally by physical 

and chemfcal properties, These include compatibility, proper range of heating value, and permit restrictions 

. regarding elemental composition (based on emission limitations). The material is transferred through 

aboveground pipelines from the tank farm to the incinerator, Pipelines used to transfer liquid organic waste 

and aqueous waste are equipped with strainers. 

In -compliance with the Benzene NESHAP, all tanks are vented to individual carbon adsorption canisters for 

removal of organics before vapor is discharged to the atmosphere. Each carbon adsorber canister is 

essentially equivalent to a 55 gallon container or greater, if necessary, All tanks are equipped with 

conservation vents, in addition to the carbon canister adsorber. All tanks are grounded, and flame arresters 

are in stal led between th e ca rbo n ad sorters a nd the 1a nks, 

2.2.1.1 O rgan fc and Aq ueo us Liq uid Waste Feeds 

The liquid waste injectors used in the combustion chambers are air-atomizing injectors; These are used .for 

injection of high Btu, low Btu liquids and specialty feed liquids. Dual fiuiti injection nozzles will be used for 

atomizaticn of the waste. Each of the injectors is.rated at 0-300 gptv The liquid waste feed nozzles are 

served by parallel redundant pumps and recirculation systems with back pressure'control, 

•f2S February »1 0 
AZCOM 

2.2.1.2 Packagecf Waste Feed 

Containers of wastes are sampled and analyzed after receipt in accordance with the facility's Waste Analysis 

Pfan. These wastes can then be delivered directly to Unit 2 or repacked into small combustible containers at 

the facility. Fiberboard or plastic containers (fully or parti'aty full of waste), up ID 4D-ga1on size, may be 

charged directly to the primary chamber. These wili be received at the dock adjoining each fixed hearth 

incinerator, and charged to the incinerator within 24 hours or returned to permitted storage. 

Solids, usually packaged in plastic Q rfi be rtoard containers, are introduced into the incinerator through a PLC 

controlled airlock-ram sysiem located at the lower front of the primary chamber of the incinerator. The airlock 

is composed of a refractory-lined dcor, a door into the airlock enclosure, and two pneumatic rams, The action 

of the feeder is as foriows: 

* With me incinerator door closed, the airlock door is opened, 

<? The first pneumatic ram (load ram) pushes weighed charges of waste into the airlock chamber. 

» The airlock door is closed. 

* A switch is activated either automatically or manually, which opens the door to the incinerator and 

actuates the ram (charge ram) that pushes the waste into the incinerator. The ram then retracts and 

the Incinerator door closes. 

2.2.1.3 S petlarty Llq uid an if Gaseous Wasto Feeds 

Specialty Feed Systems associated with Incinerator No. 2 are as follows 

» Specialty Feeder • 

• Compressed Gas Cyiinder Feed System 

» Direct Inject Liquid Feed System 

2.3 Manufacturer, Make and Modal of the incinerator J40 CFR § 63.12Q7(f)(1Hiij)(A)I 

2.3.1 Combustion Chamber arid Burners [40 CF R §63.12D7(f}(1)(m)(B) and (C) 

Incinerator No, 2 features a two-stage combushort process, ignition of waste material takes place in the 

primary (lower) combustion chamber (PCC). A secondary (upper) combustion chamber (SCC) serves as an 

"after-burner'' for process gases. Ignition of the waste takes place at temperatures' in e>ccess of 1700 

degrees F, The secondary combustion chamber maintains a minimum temperature of approximately 1&00 

degrees F. 

The fixed hearth incinerator is fabricated of carbon steei. The primary chamber has an external diameter of 9 

feet and is 17,5 feet long. The interior walls of the chamber are lined with approximately 10 inches of brick 

refractory and insulation backing, making the internal operating diameter approximately 7*2". The crosssectionaE area of the chamber is thus 40.3 square feet. Table 2-2 provides a summary of the incinerator 

design specifications. 

Liquid and solid waste feeds enter the lower chamber on the front-face of the chamber. The primary burner 

and the specialty feed injector are located near the front-face of the chamber and are mounted tangentially. 

2-7 February 2013 
AZCOM 

The primary burner is a North American burner rated at 12,3 million Btu/hr. and is used in the lower chamber 

to maintain permitted temperatures, it will burn only natural gas or No. 2 fuel oil. The burner system is 

supplied wish combustion gir at a static pressure of 30" water column (WC), The pSoi for the primary burner will 

burn natural gas. 

The fuel system for the lower chamber (and secondary combustion chamber) is controlled by a Factory Mutual. 

approved burner management system complete with interlocks and safety valves. 

2.3.2 Secondary Combustion Chamber 

The secondary combustion chamber (SCC) is a horizontal, cylindrical chamber that has an external diameter 

of 9 feet and is 17.5 feet Eong. The tnteriorwalls of the chamber are lined with approximately 10 inches rjf brick 

refractory and insulation backing, making the internal operating diameter approximately 7'2". The crosssectio n at are a of the cham be r is th us 40.3 sq u are feet, 

Following ignition of the waste material under controlled or starved-air conditions in the lower chamber; off-' 

gases travel through a refractory-lined flue gas passage into the upper-chamber, which acts as an afterburner, 

Turbulence is achieved by the tangential introduction of air and additional fuel in the upper chamber. 

The SC C is equipped with one burner mounted tangentially on the side of the chamber. The burner is a North 

American burner rated at 6.0 million Btu/hr and is fueled with natural gas or fuel oil, 

As with the primary chamber burner; the SCC burner is supplied with atomizing air and is equipped with a 

burner management system, This system controls the ignition and initiates an automatic shutoff when there is 

a Joss-of -flame,, combustion .air. supply, .fuel .pressure, atomizing, air.pressure, .or.pilot burner. 

Leaving the upper chamber, the hot gas stream travels through 28 feet of refractory-Sined stack sections before 

reaching the start of the gas scrubbing system. The combined volume of the upper and lower chambers, the 

flue gas passage and the hot crossover section is approximately 1567 cubic feet. The total retention time of 

combustion gases within the system is approximately 5 seconds. 

2.3.3 Location of Combustion Zone Temperature Device [40 CFR § S3.1207{f){1)(xix)J 

The thermocouple that monitors temperature in the primary combustion chamber is located on top of the 

chamber about five feet from the transition. The thermocouple that monitors temperature in the SC C is located 

on tup of th e ch am ber a bove the tra n s ition, 

2.3.4 Hazardous Waste Residence Time \40 CFR § S3.Jl207{f)(1)(ix)] 

The Hazardous waste gas residence time for the Fixed Hearth Incinerator is calculated as follows: 

• Primary Combustion Chamber Volume-635 ff.3 

• Secondary Combustion C h a m be r Volu me - 635 ft3 

• Total Volume-1270 fr.3 

• Maximum Flue Gas Fiawraie -17,382 acfm (290 if/sec) 

• Totaf Combustion Zone Residence Time = (1270 ft3)/[290 Jf/sec) = 4.4 sec 

2-3 Hahmaryaulu 
AZCOM 

Since these incinerators are fed hearth units, residence time is based on the elapsed time since the las: 

solids charge was put into the combustion zona or based on the travel length of tiis ash ram that functions to 

clear tho primary combustion chamber of solid waste residue, An elapsed time of one hour or a travel length 

of 110 inches for the ash ram have been established as the criteria for determining when solid waste is no 

longer in the compustjon zones,

 1 

2.3.5 Combustion System Leak 

Combustion system leaks are prevented through maintaining a totally seated combustion chamber, coupled 

with the use of an induced draft fan that maintains a vacuum of normally - 4 to • 5 inches of water column in 

both combustion chambers while wastes are being fed io the unit. 

2.3.6 Emergenc y Safety Vent 

The incinerator is equipped with an emergency safety vent (ESV) located a* the top of the secondary 

combustion chamber. This ESV is a refractory-fined emergency thermal reifef vent (TRV) which is held in the 

dosed position by a pneumatic cylinder. The control.valve in the line supplying air to the cylinder and the 

cylinder vent valve that opens the TRV are located in the control room for each unit Valve locks (with keys 

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

combustion gas to vent from the combustion system during emergency shutdown events. The purpose of the 

TRV is to protect the downstream APCS from excessive temperature situations, A limit switch on the TKV 

shuts off all waste feeds to the system as it senses that .the cap is opening. 

2.4 Procedures for Rapidfy Stopping Hazardous Waste Feed During Equipment 

Malfunction-£40 C^R§63,'l207<f)(1Kvi[i)} 

Equipment malfunctions are identified by the control system > observation of process control variables, or by 

regular fieid inspections, 

in the event of minor equipment malfunctions (e.g. Waste feed or scrubbeT leaks), the control room operator 

wfff be notified. The control room operator will then close the waste feed valves and disable the waste feed 

pumps, 

In the event of major equipment malfunctions (e.g. fire), the emergency stop button located in the. contra I room 

will be pushed. If this button is pushed, all equipment will switch to its fail-safe position, 

2.5 Air Pollution Control Equipment [40 CFR §63.1207(f)(1 >(lil)(G)] 

2.5.1 Air Pollution Control Systems Descriptions 

The air pollution control system consists of a spray dryer absorber and fabric filter baghouse modules, The air 

pollution controi system neutralizes acidic compounds and removes particulate from the exhaust gas. Two 

subsystems, the spray dryer absorber and the fabric filter, carry out the chemical neutralization and particulate 

removal functions, respectively. A third subsystem, the lime system, is used to prepare and provide lime slurry 

to the spray c'ryer absorber for use in the chemical neutralization process. The induced draft fan and stack 

provide the mechanical energy required to transport the flue gas through the interconnecting ductwork, to its 

eventual discharge point batmosphEre. 

2-9 Ffhrta-ySCIQ 
jgki 2-5,1.1 Lime System 

• - The lime system prepares lime slurry for use in the chemical neutralization process in sufficient supply and 

concentration to maintain continuous flue gas treatment in the spray dryer absorber. The system has been 

designed for batch mixing to provide this service, Veolia utilizes hydrated lime as its neutralizing agent in the 

air pollution control systems. The key neutralization parameter of the hydrated lime is the "CaO Equivalent.* 

Figure 2-1 is the specification sheet for the hydrated lime that Veolia uses. Veolia has used this specific 

product for over 20 years and plans to continue with its use, Although if Veolia cfoes change suppliers or type 

of lime in the future, it would have a ::CaO Equivalent" specification equal to or greater than the 72,6% shown 

on Figure 2-1. 

Hydrated Jime is stored in a storage bin above the lime preparation area. The storage bin is sized to hold 

enough hydrated lime to maintain several days of system operation at the maximum combustion rate of the 

incinerator. Lime is discharged through the conical storage bin bottom. The flow of the material from the bin is 

aided by a vibrating "live bottom," or bin activator. A variable speed screw feeder is used to meter the 

hydrated lime in the proportions required for batch mixing iime slurry, The lime is mixed with water in a tank 

beneath the lime storage bin. The screw feeder speed and 'the rate that water is added to the lime slurry tank 

are variable so that the desired iime solids concentration can be achieved in the tank. The variable feed 

adjustments- allow water and time to be added to the lime slurry tank at a rate that wilt allow a batch mode of ' 

mixing. An agitator is provided in the slurry tank to mix the water and lime and to maintain the suspension of 

lime solids. The mixed lime slurry is pumped at a continuous rate of flow through a recirculation loop Eo the 

atomizer. 

2.5.1.2 Sdfay Dry Absorber 

•: Unit 2 is equipped with a Spray Dryer Absorber (SDA) located immediately downsiream of the secondary 

combustion chamber. The SDA unit is fabricated of 3/B inch carbon steel, The function of the SDA is to: 

a Further cool the combustion gases from 1600-2 000°F to 300-5C0"F, 

<• Neutralize and remove HCl and other acids from the combustion gases, 

a Remcve a pcrtion of the particulate (fly ash) fram these g ases, 

Slurry flow to the spray dryer absorber (SDA) is metered by a flow control valve to obtain the proper feed 

concentration to the spray dryer absorber atomizer. Automatic (or manual) adjustment to the flow is made as 

a function of the output from a hydrochloric acid (HCl) analyzer in the gas duct downstream of the fabric filter. 

The amount of slurry metered is proportional to the amount of HCl monitored, 

The slurry passes through a stationary swirl-type liquid distributor into the atomizer wheel where induced 

centrifugal force from the rapidfy spinning wheel discharges the slurry through the wheel nozzles at high 

velocity. The design of the atomizer wheel, its rate of spin, and the discharge velocity of the slurry, creates 

cloud of finely divided droplets around the periphery of the atomizer wheel, A feedback signal from the 

atomizer power transmitter provides verification that water flow to the atomizer increases Dr decreases irt 

proportion to the spray dryer absorber outlet temperature. 

Flue gas enters from the bottom of the spray dryer absorber through a vertical, centrally located disperser, 

The disperser directs the flue gas through the zone filled by the atorrtzed slurry cloud where the flue gss and 

slurry mix- and most of the absorption occurs. The gases then flow downward through the absorber chamber 

2-10 reSniaiy 2D15 
AzCOM 

and exit through a bottom side duct As the gases contact and pass through the cloud of atomized lime slurry, 

the water in the slurry evaporates, cooiing the gases. Simultaneously, the lime in the slurry reacts with the 

hydrogen ch'orkfe in trie gas us to produce calcium salts. Some of the resulting dry material, consisting of 

calcium salts, fly ash and excess lime, falls to the conical bottom of the unit. The dry material from each unit is 

discharged to a conveyor system that transports it to a dump trailer or equivalent type system. 

2.5.1.3 Fabric Filter 

Gas exhaustsrJ from the spray dryer absorber is distributed by manifcld ducts to four fabric filter modules, The 

unit is operated with oniy three modules on-line with the fourth module off-line in a standby mode. Within each 

filter module, the gas is passed through Teflon-coated fiberglass cloth bags, The gas passes from the outside 

to the inside of the filter bags. Particulate entrained in the gas stream is mechanically deposited on the outside 

of the filter bags as the gas passes through the cloth, 

Each module has a dean air plenum and housing section to contain approximately 96 bags. Each bag is 

approximately 6" in diameter by 20' long. The baghouses are fabricated from 3f16* mild steel plate, of welded 

construction, gas tight and stiffened to withstand the maximum operating negative pressure. Each 

compartment has a tube sheet that supports the bags and provides for top bag/cage removal. Access to the 

clean air plenum is via a side access door in the clean air plenum. 

The fabric filter cleaning mechanism utilizes jets of air to cleah the filter bags, Periodically, the cleaning 

sequence will be initiated. The sequence is started at the end of a 4 hour timed cycfe, when the differential 

pressure across the filter reaches a predetermined setpoint of approximately 7,0" w.c, or when the operator 

initiates a cycle. The controller then sequences to each row of filter bags in each module, releasing a burst of 

air apposite txthe direcfjofrof gas flow, • The quickly released1 burst of air-rirslodges-dust cske on the exterior of 

each bag as it travels from the top to the bottom of the bags, Released from the bag, the dust cake falls by 

gravity into the hopper at the bottom of the module. From there it is discharged to a conveyor system that 

transports it to a dump trailer, or equivalent type system. 

Treated by the spray dryer absorber and filtered by the fabric filters, liie cleaned flue gas exits the fabric filter 

modules to an outlet manifold tor exhaust. 

S.5.1.4 Induced Draft Fan and Stack 

The induced draft fan and stack are located downstream of the fabric filter. Combustion gases are drawn 

through the system by .a 75 hp induced draft (ID) fan, rated at 15,000 acfm at 400* F saturated, and 22" water 

column pressure. The induced draft fan provides the mechanism for transporting the incinerator flue gas 

through the spray dryer absorber, fabric filter, and all interconnecting ducts, The ID fan includes an inlet 

volume control damper to be used to control the velocity of the gas within the ducting and treatment devices. 

Treated gases are exhausted from the induced draft fan to the atmosphere through a 90-ft. high stack, The 

stack diameter for Unit 2 is 39 inches 3, D, The stack is equipped with instrument sampling ports and a 

sampling platform for emissions testing. Figure 4-1 provides details on the design and sample port locations 

and configurations for the stack, 

2-11 Fahmary 201 • 
2,6 Stack Emissions Monitoring [40 CFR §63.1207(f)(1}<iii><H-)T 

The continuous emissions monitoring (CEM) system consists of sample probes, sample delivery and 

conditioning apparatus, and gas analyzers, Samples are extracted from the sampling ports on the stack, A 

CEM performance test and quality assurance program has been imp'emsnted in accordance with Appendix 

to Subpart EEE of Part 63—Quality Assurance Procedures for Continuous Emissions Monitors Used 

far Hazardous Waste Combustors. 

Responses from each CEMS are fed to the Control System (CS) where the CO hourly rolling average is 

calculated and interlocked to the waste feed cutoff valves as part of the Automatic Waste Feed Cutoff System 

(AWFCO) discussed in Section 2.8, below, The following provides a brief description of the CEMS 

instruments including the operating range and measuremenl principal. 

2.S.1 CEMS System Description 

The Continuous Emissions Monitoring System (CEMS) currently being utilized at Incinerator 2 analyzes far 

opacity, carbon monoxide, hydrogen chloride, total hydrocarbons and oxygen. These monitors, except 

opacity, are extractive devices mounted in sampling ports Dn the stack. The table below summarizes ihe 

analyzer specifications. 

The opacity monitor continuously measures the stack gas opacity and reports the measurements to an 

indicator and a recorder, An opacity that exceeds a preset limit triggers an alarm and interlock. 

Carbon monoxide and hydrogen chloride are monitored with extractive non-disperse infrared analyzers, Total 

hydrocarbon.is monitored, with an .extractive flame ion.detector,analyzer.. .Oxygen.is.monitored .with .a 

zirconium oxide cell, 

Stack gas flow rate is continuously monitored using an anubar that sends a 4-20 mA signal to the PLC that 

converts the signal to acfm. 

Ta ble 2-1 U n it 2 Co nti nuo us Emi ss ion Mo n tto rs 

Parameter Current Mfg. Range Principle 

Oxygen COSA 6-25% Electrochemical 

Carbon Monoxide Ecochem MC3 0-200 ppmv 

. 0-30DQ ppmv 

Infrared 

i Total hydrocarbons Thermoeiectron 0-100 ppmv FlD/lnfrared 

Hydrogen chloride Ecochem MG3 0-1,000 ppmv Infrared 

Opacity Tefedyne 0-100% White light 

Stack gas flow PSE/Rosemount 0-20,000 acfm Pressure drop 

21 Process Monitoring and Control 

The facility is equipped with a state-Df-the-art monitoring and control system, which facilitates compliance with 

permit conditions, and otherwise, collects process control information, facilitates efficient operation and detects 

and prevents damage to the facility, The.system consists of three major components: 

2-12 
» A human-machine interface (HMI) system, 

* P ro g ra mma ble log ic con trot I er's (P LC's), and 

* A h ig h s pee d etli ernet cab Ie con nects a 11 contra I s ystem cc m po n e n ts 

The desired control functions are implemented through tho HM! system, Ali digital control and emergency 

interlocks are accomplished by the PLC, 

The control system is capable of monitoring the 'operational envelope'1 of the incinerator and is capable of 

performing a-number of activities including: 

» Contro! room indication of processor sensors located within the incinerator system (such as pressure' 

indication of a field installed pressure transmitter); 

« Process controller for single instrument loops or an individual sub-system, such as a ternpenature 

control loop involving a sensor reading from one temperature transmitter affecting the function of one 

temperature conEroi valve; and 

* Alarm for an exceedance of a designated setpoint, such as a high pressurs or low temperature. 

The process control computer will continuously control and monitor the-operation of the incinerator. When outof-range conditions exist, it will notify the operator of those conditions, The process control computer is 

programmed to shut-down equipment {i.e., bring the system into a safe mode) when designated parameters 

are exceeded, which is a protective mechanism against potential equipment damage, operation outside of 

permit limits, or conditions that might lead to a release to the environment. 

Continuous monitoring of the incinerator and scrubber system is an important aspect of the system design. A 

digital readout of all monitoring insfnj mentation is displayed on the main control screen. An audible and visual 

alarm alerts the incinerator operator So significant deviations from normal operating conditions. This system 

allows an immediate response to adverse conditions by the operator, Automatic waste feed cut-off and 

incineration shutdown mechanisms are also interlocked with the monitoring system at or prior to reaching 

permit limit levels. Monitoring methods and calibration frequencies are. listed in Table 2-3, 

The Incinerator has an independent process control computer that interfaces to the Quantum programmable 

controllers. The process computer is capable of controlling the incinerator in case oi a failure in a HMJ server. 

This computer runs a RSVIEW HMI controE software that provides operator interface to all instrumentation and 

controls. 

2,8 Automatic Waste Feed Cut-off System [40 CFR §63.1207(f)(1)(iJi)(F)] 

The Incinerator has an Automatic Waste Feed Cut-Off (AWFCO) System that will shut waste feeds off in the 

event certain operating parameters deviate from allowable set points. The PLC continuously monitors 

operating parameters, making adjustments to the process as needed for proper control, Alarm logic is 

incorporated into the PLC system to automatically initiate an AWFCO. Table 2-3 summarizes the current 

AWFCO set points. AWFCO limits have been established based on several factors that are summarized 

below, 

* Regulatory/permit limits - established to comply with existing permits. An example of this type of limit 

is the low temperature limit, below which waste cannot be fed until the proper limit is re-established. 

2-13 FabrasyailC 
AsCOM 

s$piy In addition, the HWC MACT regulations require that the AWFCO system be interlocked with the span 

f'-^J? of eac h p rocess instrum e n t th at is pa rt of the Co n ti n uous Mo n i jo ring Sy stem .(CM $}, AI i stin g of these 

^ CMS instruments and their interlocked span setpoints is maintained as part of Veolia's Operating 

Record, 

« Process safety limits - established to assure process equipment is protected and unsafe operating 

conditions do not occur. An example of this is inadequate excess air in the combustion chamber that 

can lead to fuel rich conditions. 

* Utility or Fewer failure - established to facilitate a controlled shutdown of the process during loss of 

process air, steam, water or electricity, An example of this is the loss of instrument air that is 

necessary for certain types of process instruments fo function properly. Wastes will not be rein troduced into the incinerators until proper operation of key instruments is re-established. 

In addition to the AWFCO system, operators can manually shutdown waste reeds or the entire process should 

this be needed, 

2.3.1 AWFCO System Testing 

Veolia tests the AWFCO systems bi-weekly, as weekly testing would unduly interfere with operations by 

ceasing and restarting waste feeds, potentially increasing emissions, incurring excessive downtime, burning 

additional natural gas during the downtime, and increasing operating costs, Testing of the AWFCO system is 

a time-consuming and manpower intensive process. The current testing program has been in place under the • 

RCR A permit for over 20 years and has proven to be adequate in detecting problems, This rationale is 

^ % included in the facility's AWFCO Plan. In some cases this testing occurs more frequently depending on haw 

[-y'^Woften actual' AWFCO's bec'u r at' th' e' Liti'It' Per'th e req uiretf ffeq uericy; 'incinerator person ii el' cli e'c'K' the 

'•. • • •' fu notion a I ity of AWFCO log ic th at is part of the i nci nerato r"& P LC system to make su re that sh c-uid process 

conditions deviate from allowable limits, the computer logic will initiate waste feed shutdowns as required. 

This is accomplished by manually simulating process conditions that are outside allowable limits and obseiving 

and documenting when the control or block vafve software logic on the waste feed line begins to initiate valve 

closure. Should actual AWFCOs occur during a given testing period, these are documented by operating 

personnel to safety regulatory requirements for system testing. Results of this testing are documented on a 

separate AWFCO Testing Log and maintained as part of the unit's Operating Record. 

2.9 Air Pollution Controi Equipment Maintenance Practices [40 CFR 

§63.1207Cf}(lHin>{G)] 

2.9.1 Program Overview 

Once equipment is installed and operational, Veolia utilizes an e>ctenstve preventative maintenance (PM) 

program to keep equipment operational and prevent breakdowns and failures. Based upon the type of 

equipment a net historical operations and maintenance experience, schedules for various inspection and PM 

activities are followed. This includes aspects such as documenting detailed maintenance histories on 

equipment, routine inspection and lubrication programs for high wear equipment and nan-destructive testing of 

piping and vessels using techniques like ultrasound to assess integrity. The frequency cf these activities 

varies depending upon the equipment PM activity and the incinerator's shutdown schedule, 

^ J | p | For example, frequent (i.e., weekly) instrument and certain mechanical equipment checks are made for criticai 

|'..'' '':, process items, Lubrication, vibration analysis and other mechanical integrity checks are done at longer 

2-14 Felmiary.ZGIO 
frequencies like monthly or quarterly. Finally, such items as inspecting refractory brick for wear, are typically 

performed when the entire incinerator is shut down for msintenancE.1. 

2,9,2 Test Program Preparation Activities 

Prior to testing, instrumentation associated with key parameters of the test were checked, calibrated, or 

replaced, as appropriate, to ensure proper operation of the instrumentation during testing (i.e., waste feed 

flowmeters and scales, CEMS, pressure transmitters, thermocouples, stack flowmeters, etc.). 

••• vj 

2-15 rstm^n' 2CID 
'?ffi.#>. 

AZCOM 

Table 2-2 Technical fnformation S unwary on Incinerator No. 2 

j Pvianuracturer 

Trade Waste Incineration 

• Model No, . TWI-20C0, Series 2 

Type Fixed Hearth, Dual Chamber 

Date of Manufacture 1937 

Dimensions Primary Chamber Secondary Chamber 

External Length 17.5r 17.5' 

External Diameter 9' 9' 

1

 internal Diameter 7*2- TT 

Cross-sectional area 40,3 square feet 40.3 square feet 

Burners Primary Chamber Burner Secondary Chamber Burner 

Manufacturer North American North American 

Size 12.0 Million Btu/hr 6.0 Million Bfu/hrFuel Natural Gas • Natural Gas 

Primer Mover nduced Draft Fan 15,000 acfm @ 4C03F saturated. 22 in. water column 

2-16 Fabruary SC-10 
Table 2-3 Current AWFCO Parameters and Limits for Incinerator Mo, 2. 

\ . ' 

System Device Units Cutoff Limits 

Calibration 

Frequency 

Total Pumpable Waste Feed 

rate 

Mass Flowmetere/Scales Lb/hr •> 3f07(HRA) Annually 

Total Waste Feedrate Mass Flowmeters/Scaies Lb/hr >40T7 • Annually/quarterly 

High BTU Liquid feedrate Mass flow meter lb/hr i>2:0122 Annually 

• Low BTU Liquid feedrate • Mass flow meter lb/hr a 1,993s Annually 

Specialty feeder Scale lb/hr £ 7242 Quarterly 

Total LVM Feedrate Mass Flowmeters/Scaies lb/hr >47(12 HRAf Annually/quarterly 

i Pumpable LVM Feedrate Mass Flowmeters/Scaies lb/hr >43(-12HRA) Annually/quarterly 

:SVM Feedrate ' Mass Flowmeters/Scaies lb/hr > 63 {12 HRA) Annually/quarterly 

Mercury Feedrate Mass Flowmeters/Scaies lb/hr > 0.D034 (12HRA) Annuatly/qtiarterfy 

Chiorine Feedrate Mass Fsowmeters/Scales lb/hr > 21S (12 HRA) Annually/quarterly 

Ash Feedrate Mass Fl&wmeters/Scales lb/hr >673 (12 HRA) Annually/quarterly 

Primary Combustion 

Chamber Te m peratu re 

Type K Thermocouple 'F <1,590 {one-minute average) 

« 1734 (HRA'') 

>2.400 (instantaneous)2 

Annually 

Secondary Combustion 

Chamber Temperature 

Type K Thermocouple eF S1.7S4 (one-minute average) 

<1S49 (HRA1) 

... .S2,4D.Q .{instantaneous)2.... 

Annually 

Primary Combustion 

Chamber pressure 

Pressure transmitter in. w.c. >-0.1 {5 second defey) Quarterly • 

Secondary Combustion 

Chamber pressure 

Pressure transmitter in. w.c. ^ -0.1 (5 second detay) Quarterly 

Spray Dryer Adsorber 

Outlet Temperature 

Type K Thermocouple 'F >5DD (one minute average)2 

>42Q (HRA) 

Annually ; 

Combustion Gas Flow Rate Pitot Tube acfm >17,198? 

*15,147 (HRA) 

Annually 

StacK Gas Excess Oxygen Zirconium Oxide fuel cell % <.3 (one-minute avg.) Quarteriy 

Stack carbon monoxide Infrared ppmv \ £100 (H kA) 

k5QQ (one minute average)2 

Quarterty 

Stack Hydrocarbon FID j ppmv >1o'{one minute average) Quartan" y 

Stack gas opacity White Light % >10 (one minute average)2

 \ Quarterly 

Stack hydrogen chloride2 Infrared ppmv >1D0(HRA)3 

£500 (one minute average)2 

Quarterly

 : 

Fabric filter pressure drop Delta P transmitter in. w.c. •3 2 cr> 10 (T min. average) Quarterly 

Min. Sorbent Feedrate Density Transducer Ib/fb Cl 2 <1.76 

Min. Carrier Fluid Flowrate Flowmeter gat/lb Cl 2 <1.70" Annually 

1

 HRA means "hourly rolling average" as calculated by averaging the previous 60 one-minute average vafueg,. 

2

This Is a RCRA permit limit only. 

2-17 

r 
Figure 2-1 Hyctrated Lime Specifications 

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2-18 
Incinerator Process Description 

Unit 3 
2.0 Incinerator Process Description 

AZCOM 

2.1 Process Overview 

.Veolia operates two Fixed Hearth Dual Chambered Incinerators (Units 2 and 3) and one rotary kiln incinerator 

(Unit 4) at the Sauget, IL facility, The two fixed hearth units are rated at 16 million Btu/hr each. Incineration 

Unit No, 3 is a mirror image of Unit No, 2. Both of these units have their own waste handling systems as 

described in the sections that follow. The only difference being Unit No, 2 is equipped with four (4) baghouse 

modules, while Unit No. 3 is equipped with three (3) bag he use modules. However, each incinerator, is 

operated identically with onJy three baghouse modules in service during operation. Unit 4 is rated at 50 mirlion 

Btu/hr and is equipped with its own tank farm system, drum storage, bulk solids storage and feed systems, 

2.2 Waste Feed Systems [40 CFR § 63.1207(f)(1 }{ir)(c) and (f)(1)(iiiJ(D) and (E}] . 

2,2,1 Unat 3 Liquid Waste Feed System and Blending Operations 

The fixed hearth incinerator is designed to receive containers, aqueous liquid wastes, organic liquid wastes, 

specialty liquid feeds and direct inject liquids fed through the aqueous or organic liquid feed systems. These 

units can receive any combination of wastes - liquid, semi-soiid or soiid - with a heat value'of up to 15 million 

Btu/hr, 

Unit 3 is.supported by storage/blend tanks located in Tank Farm #1. Rates of feed are controlled at each 

incinerator. Segregated liquid wastes are stored until utilized in the waste blending facilities. At that time, 

•liquids-are delivered to -the -blending--tanks where- the- daily -Pquid feed .to. the. incinerator .is. formulated, .tested 

and released to the incinerator. Blending of stored liquid wastes to achieve optimum heating value and 

viscosity for incineration takes place in Tanks 2, 4, 6 S, 8. Six additional tanks (10, 20. 30, 40, 50 & 60) are 

used to segregate different waste stream types for blending of liquid feed to the incinerator; Several criteria 

are important in designing a btend from available wastes that have been segregated principaEly by -physical 

and chemical properties, These include compafibi|ity;.proper range of heating value, and permit restrictions 

regarding elemental composition (based on emission limitations). The material is transferred through 

aboveground pipelines mom the tank farm to the incinerator. Pipelines used to transfer liquid organic waste 

and aqueous waste are equipped with strainers. 

in compliance with the Benzene NESHAP, all tanks are vented to individual carbon adsorption canisters for 

removal of organics before vapor is discharged to the atmosphere. Each carbon adsorber canister is 

essentially equivalent to a 55 gallon container or greater, if necessary. All tanks are equipped with 

conservation vents, in addition to the carbon canister adsorber,- All tanks are grounded, and il.ame arresters 

are installed between the carbon adsorbers and the tanks, 

2.2.1.1 Organic and Aq: u eous Liq uid Waste Feeds 

The liquid waste injectors used in the combustion chambers are air-atomizing injectors, These are used for 

injection of high Btu, low Btu liquids and specialty feed liquids, Dual f-;uid injection nozzles will be used for 

atomrzation of the waste. Each of the injectors is rated at 0-300 gph. The liquid waste feed nozzles are 

served by ps ral I e I red un d a n t pu mps a nd red rcu latio n system s with ba ck press u re con trol. 

2-6 Fabrusry K)l£l 
2.2.1.2 Packaged Waste Feed 

'•'Container s of wastes are sampled and analyzed after receipt in accordant© with the facility's Waste Analysis 

Plan. These wastes can then be delivered directly to Unit 3 or repacked into small combustible containers at 

the facility. Fiberboard or plastic containers (fully or partially full of waste), up to 40-ga'llon size, may be 

charged directly to the piimary chamber, These will be received at the dock adjoining each fixed hearth 

incinerator, and charged to the incinerator within 24 hours or returned to permitted storage, 

SoficJs, usually packaged in plastic or fiberboard containers, are introduced inio the incinerator through a PLC 

controlled airlock-ram system located at the lower front of the primary chamber of the incinerstor. The airiock 

is composed of a refractory-lined door, a door into the airlock enclosure, and two pneumatic rams. The action 

of the feeder is as follows: 

* With the incinerator door closed, trie airlock door is opened, 

*• The first pneumatic ram (load ram) pushes weighed charges of waste into the airlock chamber. 

* The airlock doer is closed, 

* A switch is activated either automatically or .manually, which opens the door to the incinerator and 

actuates the ram (charge ram) that pushes the waste into the incinerator, The ram then retracts and 

the incinerator door closes, 

2.2.1.3 Specialty Liquid Waste Feeds 

Specialty Feed Systems associated with Incinerator Ho. 3 are as follows 

• \ ' Hooded Specialty Container Feeder 

* Glove Box Emission Control Systems 

* Direct inject Liquid Feed System 

2.3 Manufacturer, Make and Model of the Incinerator [40 CFR § 63.1207(f)(1){m}{A)I 

2,3.1 Combustion Chamber and Burners [40 CFR §63.1207(f)(1)(iii)(B] and (C) 

Incinerator No. 3 features a two-stage combustion process. Ignition of waste materia! ta'ses place in the 

primary (lower) combustion chamber (PCC). A secondary (upper) combustion chamber (SCC) serves as an 

"after-burner" for process gases,' Ignition of the waste takes place at temperatures in excess of 1700 

degreesF. The secondary com bu stion cha m be r m a in ta i n s a m i n i m u m :errype ratu re of approxi mately 1B00 

degrees F, 

The fixed hearth incinerator is fabricated of carbon steel. The primary chamber has an external diameter of 9 

feet and is 17,5 feet long. The interior w'atls of the chamber are lined with approximately 10 inches of brick 

refractory and insulation backing> making the internal operating diameter approximately 7'2-*. The crosssectional area of the chamber is thus 40,3 square feet Table 2-2 provides a summary of the incinerator 

design specifications. 

Liquid and solid waste feeds enter the lower chamber an the front-face of the chamber. The primary burner 

and the s pec ia Ity feed i njector a re located near the front-face of the oh a m ber an d are mo u n ted tan genti a liy. 

• •'1 

2-7 FetjrLrars' 30'R 
AZCOM 

The primary burner is a North American burner rated a* 12.0 million Btu/hr. and is used fn the lower chamber 

- to maintain permitted temperatures, it will burn only natural gas cr No, 2 fuel oil. The burner system is 

supplied with combustion-air at a static pressure of 30" water column (WC), The. pilot for the primary burner will 

burn natural gas, 

The fuel system for the lower chamber (and secondary combustion chamber) is controlled by a Factory Mutual 

ap proved bu rher m anag e m ent s yste m ccmp lets with in terl ocks a nd s a Fety va!ves. 

2.3.2 Secondary Combustion Chamber 

The secondary combustion chamber (SCC) is a horizontal, cylindrical chamber that has an external 

diameter of 9- feet and is 17,5 feet long. The interior walls of the chamber are lined with approximately 10 

inches of brick refractory and insulation backing, making the internal operating diameter approximately 

7

:

2". The cross-sectiona! area of the chamber is thus 40.3 square feet. 

Folic wing ignition of the waste material under controlled or starved-air conditions in the lower chamber, offgases travel through a refractory-lined flue gas passage into the upper chamber, which acts as an afterburner. 

Turbulence is achieved by the tangential Introduction of air and additional fuel in the upper chamber. 

The SCC is equipped with one burner mounted tangentially on the side of the chamber. The burner is a North 

American burner rated at 5.0 million Btu/hr and is fueled with natural gas or fuel oil, 

As with the prirnany chamber burner, the SC C burner is supplied with atomizing air and is equipped with a 

burner management system. This system controls the ignition and initiates an automatic shutoff when there is 

a-loss of flarr^,-combustion -air- supply,- -fuel -pressure-, -atomizing-air -pressure,- or- pilot burner-, 

Leaving the upper chamber, the hot gas stream travels through 28 feet of refractory-lined stack sections before 

reaching the start of the gas scrubbing system, Tne combined volume of the upper and lower chambers, the 

flue gas passage and the hot crossover section is approximately 1,587 cubic feet. The total retention time of 

combustion gases within the system is approximately 5 seconds. 

2.3.3 Location of Combustion Zone Temperature Device [40 CFR§S3.l207(f](1)(xix)J 

The thermocouple that monitors temperature in the primary combustion chamber is located on top of the 

chamber a bout five feet from the transition, The thermocouple that monitors temperature in the SC C is located 

on top of the chamber above the transition, 

2.3.4 Hazardous Waste Residence Time [40 CFR §63.l207(f)(1)(ix)] 

The Hazardous waste gas residence time for the Fixed Hearth Incinerator is calculated as follows: 

• P ri mary Com bustion C h am ber Vo lu me - 63 5 ff.3 

» Seco n dary Comb ustion C hamber Vo lu me - 635 ft3 

• Total Volume- 1270 ft3 

• Maximum Flue Gas Flowrate - 17,382 acfm (290 if/sec) 

» Total Combustion Zone Residence Time - (1270 ft3)/(29Q ftVsec) = 4.4 sec 

2-8 Fsf3fHSr>'2010 
AZCOM 

Sines these incinerators are fixed hearth units residence time is bassd or-, the eiapsed time since the last 

sol ids charge was put into the combustion zone or based on the travel length of the ash ram that junctions to 

clear ihe primary combustion chamber of solid waste, residue. An elapsed time of one hour or a travel length 

of 110 inches for the ash ram have been established as the criteria for determining when solid waste is no 

ionger in the combustion zones. 

2.3.5 Combustion System Leak 

Combustion system teaks are prevented through maintaining a totally sealed combustion chamber, coupled 

with the use of an induced draft fan that maintains a vacuum of normally - 4 to - 6 inches of water column in 

both combustion chambers while wastes are being fed to the unit. 

2.3.6 Emergency Safety Vent 

The incinerator is equipped with an emergency safety vent (ESV) located at the top of the secondary 

combustion chamber. This ESV is a refractory-lined emergency thermal relief vent (TRV) which is held in the 

dosed position by a pneumatic cylinder. The control vaive in the line supplying air to the cylinder and the 

cylinder vent valve that opens the TRV are located in the control room for each unit Valve locks (with keys 

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

combustion gas to vent from the combustion system during emergency shutdown events. The purpose of the 

TRV is to protect the downstream APC S from excessive temperature situations. A Sim it switch on the TRV 

shuts off ali waste feeds to the system as it senses that the cap is opening. 

2.4 Procedures for Rapidly Stopping Hazardous Waste Feed During Equipment 

Maffunction [40 CFR §63.12QT{f)(1)<viiifl 

Equipment malfunctions are identified by the control system, observation of process control variables, or by 

regular field inspections. 

In the event of minor equipment malfunctions (e.g. waste feed or scrubber leaks), the control room operator 

will be notified. The control room operator will then close the waste feed valves and disable the waste feed 

pumps. 

In the event of major equipment malfunctions (e.g. fire), the emergency stop button located in the contno! room 

will be pushed If this button is pushed, all equipment will switch to ;ts fail-safe position. 

2.5 Air Pollution Control Equipment [40 CFR§63,12Q7(f){1)(iii)(G)] 

2.5.1 Air Pollution Control Systems Descriptions 

The air pollution control system consists of a spray dryer absorber and fabric filter baghouse, The air pollution 

controi system neutralizes acidic compounds and removes particulate from the exhaust gas. Two 

subsystems, the spray dryer absorber and the fabric filter, carry out the chemical neutralization and particulate 

removal functions, respectively. A third subsystem, the lime system, :s used to prepare and provide lime slurry 

to the spray dryer absorber for use in the chemical neutralization process. The induced draft fen and stack 

provide the mechanical energy required to trans port the flue gas through the interconnecting ductwork, to its 

eventual d isch arge po int to atmos phere. 

2-9 ,-ehmary 0 
AZCOM 

2.5,1.1 Lime Sy&tcm 

The lime system prepares lime slurry for use in the chemical neutralisation process in sufficient supply and 

concentration to maintain continuous flue gas treatment in :he spray dryer absorber. The system has been 

designed for batch mixing to provide this service. Veolia utilizes hydrated iime as its neutralizing agent in the 

air pollution control systems. The key neutralization parameter of the hydrated lime is the "CaO Equivalent;. 

Figure 2-1 is the specification sheet for the hydrated lime that Veolia uses. Veolia has used this specific 

product for over 20 years and plans to continue with its use. Although, if Veolia does change suppliers or type 

of iime in the future, it would have a "CaO Equivalent" specification equal to or greater than the 72.6% shown 

on Figure 2-1. 

Hydrated lime is stored' in a storage bin above the lime preparation area. The storage bin is sized to hold 

enough hydrated lime to maintain several days of system operation at the maximum combustion rate of the 

incinerator. Lime is discharged through the conical storage bin bottom. The flow of the material from the bin is 

aided by a vibrating "live bottom," or bin activator, A variable speed screw feeder is used to meter the 

hydrated lime in the proportions required for batch mixing lime slurry, The lime is mixed with water in a tank 

beneath the lime storage bin. The screw feeder speed and the rate that water is added to the lime slurry tank • 

are variable so that the desired lime solids concentration can be achieved in the tank. The variable feed 

adjustments allow water and lime to be added to the iime slurry tank at a rate that will allow a batch mode of 

rriExing. An agitator is provided in the slurry tank to mix the water and lime and to maintain the suspension of 

lime solids, The mixed lime slurry is pumped at a continuous rate of flow througli a recirculation loop to the 

atomizer at s. rate of up to 10 gpm. 

2.5.1.2 Spray Dry Absorber 

Unit 3 is equipped with a Spray Dryer Absorber (SDA) located immediately downstream of the secondary 

combustion chamber. The SDA unit is fabricated of 3/8 inch carbon steeL The function of the SDA is to: 

» Further cool the combustion gases from 1600-2000T io 300-5-a(}DF, 

• Neutralize and remove HCl and other acids from the combustion gases, 

» Remove a portion of the particulate (fly ash) from these gases. 

Slurry flow to the spray dryer absorber (SDA) is metered by a flow control valve to obtain the proper feed 

concentration to the spray dryer absorber atomizer. Automatic (or manual) adjustment to the flow is made as 

a function of the output from a hydrochloric acid (HCl) analyzer in the gas duct tJownstream of the fabric filter, 

The amount of slurry metered is proportional to the amount of HCl monitored. 

The slurry passes through a stationary 'swirl-type.liquid distributor Into the atomizer wheel where induced' 

centrifugal force from the rapidly spinning wheel discharges the slurry through the wheel nozzles at high 

velocity. The design of the atomizer wheel, its rate of spin, and the discharge velocity of the slurry, create a 

cloud of finely divided droplets around the periphery of the atomizer wheel. A feedback signal from the 

atomizer power transmitter provides verification that water flow to ihe atomizer increases or decreases in 

proportion io the spray dryer absorber outlet temperature. 

Flue gas enters from the bottom of the spray dryer absorher through a vertical, centrally iocatsd disperser. 

The disperser directs the flue gas through the zone filled by the atomized slurry cloud where the flue gas and 

slurry mix and most of the absorption occurs, The gases then flow downward through the absorber chamber ' 

2-10 
AZCOM 

and exit tt vouch a bottom side duct As the gases contact and pas's through the cloud of atomized lime slurry, 

. the water in the slurry evaporates, cooling the gases. Simultaneously, the lime in the slurry reacts with the 

"' hydrogen chloride jn the gases to produce calcium salts. Seme of the resulting dry material, consisting of 

calcium salts, fly ash and excess lime, falls to the conical bottom of the unit, The dry material from each unit is 

discharged to a conveyor system that transports it to a dump trailer or equivalent type system, 

2.5.1.3 Fabric FNter 

Gas exhausted from the spray dryer absorber is distributed by' manifold ducts to three fabric filter modules, 

Within each filter moduie, the gas is passed through Teflon-coated fiberglass cloth bags. The gas passes from 

the outside to the inside of the filter bags. Particulate, entrained in the gas stream, is mechanically deposited 

on the outside of the filter bags as the gas passes through the cloth. 

Each module has a clean air plenum and housing section to contain approximately 95 bags. Each bag is 

approximately 6:i in diameter by 20' long. The baghouses are fabricated from 3/16" mild steel plate, of welded 

construction, gas tight and stiffened to withstand the maximum operating negative pressure, Each 

compartment has a tube sheet that supports the bags and provides for bop bag/cage removal. Access to the 

clean air plenum is via a side access door in the dean air pienum, 

the fabric filter cleaning mechanism usi fees jets of air to clean the filter bags, Periodically, the cleaning 

sequence will be initiated. The sequence is either started at the end of a timed cycle, or when the differential 

pressure across the filter reaches a predetermined setpoint of approximately 7.0" w.c... or when the operator 

initiates a cycle. The con trailer then sequences to each row of filter bags in each module, releasing a burst cf 

.... ... ' air opposite to the direction Df gas flow. The quickly released burst of air dislodges dust cake on the exterior of 

'•=•;each'ba g 'as it travetslrcnr the-tap-fro the bottom of the -bags; • -Released from the bag;-the-dust-cake- feKs-by 

•. '} gravity into the hopper at the bottom of the module. From there it is discharged to a conveyor system that 

transports it to a d urn p trai ler, o r eq u iva Ie n I type system. 

Treated by the spray dryer absorber and filtered by the fabric filter, the cleaned flue gas exits the Fabric filter 

modules to an outlet manifold for exhausi 

2.5.1.4 Induced Draft Fan and Stack 

The induced draft fan and stack are located downstream of the fabric filter. Combustion gases are drawn 

through the system by a 75 hp induced draft (ID) fan, rated at 15,000 acfm at 400n F saturated, and 22" water 

column pressure. The induced draft fan provides the mechanism for transporting the incinerator flue gas 

through the spray dryer absorber, Fabric filter, and all interconnecting ducts. The ID fan includes an infet 

volume control damper to be used to control the velocity of the gas within the ducting and treatment devices, 

Treated gasses exhausted from the induced draft fan to the atmosphere through a 90-ft. high stack. The 

stack diameter is 39 inches I.D. The stack is equipped with instrument sampling ports and a sampling platform 

for emissions testing. Figure 4-1 provides details on the design and sample port locations and configurations 

for the stack. 

2,6 Stack Emissions Monitoring [40 CFR §53,1207(f)(1)(iii}(H)] 

The continiJousemissionsmonitoringsystem(CEMS)consistsofsamp'e probes, sa m pie d el ivery a nd 

conditioning apparatus, and gas analyzers. Samples are extracted from the sampling ports on the stack, A 

2-11 Febrjgry 
C E M performance test and quality assurance program has been implemented in accordance with the 

Appendix to Subpart EES of Part 63—Quality Assurance Procedures for Continuous Emissions 

Monitors Used for Hazardous Waste Combustors. 

Responses from each CEM S were fed to the Control System [CS) where the CO' hourly rolling average was 

calculated and fnterfocked to the waste feed cutoff vgtves as part of tie Automatic Waste Feed Cutoff System 

(AWFCO) discussed in Section 2.8, below. The following provides a brief description of the CEMS 

instruments including the operating range and measurement principal. 

2.6.1 CEMS System Description 

The Continuous Emissions Monitoring Systems (CEMS) currently utilized at Incinerator 3 analyzes for opacity, 

carbon monoxide, hydrogen chloride, total hydrocarbons and oxygen. These monitors, except opacity, are 

extractive devices mounted in sampling ports on ihe stack. The table below summarizes the analyzer 

specifications. 

The opacity monitor continuously measures the stack gas opacity and reports the measurements to an 

indicator and a recorder. An opacity that exceeds a preset limit triggers an alarm and interlock. 

Carbon monoxide and hydrogen chic ride are monitored with extractive non-d is perse infrared analyzers, Total 

hydrocarbon is monitored with an extractive flame ion detector analyzer. Oxygen is monitored with a 

zirconium oxide cell. ' 

Stack gas flow rate is continuously monitored using an anubar that sends a 4-20 rr.A signal to the PLC that 

•Gorvvdrts the-signal .to .acfm 

Ta ble 2-1 Continuous Em issl on Mo n ito rs 

Parameter Current Mfg. Range Principle 

Oxygen COSA D-25% Electrochemical 

Carbon Monoxide Ecochem MC3 0-20G ppmv 

D-3000 ppmv 

Infrared 

Total hydrocarbons Thermoelectron 0-100 ppmv FiD/lnfrared 

Hydrogen chloride Ecochem MC3 0-1,000 ppmv Infrared 

Opacity Teledyrte 0-100% White light 

Stack gas flow PSE'Rosemount 0-20,000 acfm Pressure drop 

2.7 Process Monitoring and Control 

The facility is equipped with a state-of-the-art monitoring and control system, which facilitates compliance with 

permit conditions., and otherwise, collects process control information, facilitates efficient operation and detects 

and prevents damage to the facility. The system consists of three major components: 

* A human^machtne interface (HM) system, 

• Prog ram ma ble log ic controlle r's (P LC's}, a n d 

2-12 FebruEFy K>lo 
A~€OM 

* A high speed ethem et ca bl s co n n ects a 11 co n crof system com po h ente 

The desired control functions are implemented through the HMI system. Ail digital control and emergency 

interlocks are accomplished by the PLC. 

The control system is capable of monitoring the "operational envelope" of the incinerator and is capable of 

performing a number of activities including: 

» Control room indication of processor sensors located within the incinerator system {such as pressure 

indication of a fieid instailed pressure transmitter): 

* Process controller for single instrument foops or an individual sub-system, such as a temperature 

control loop involving a sensor reading from one temperature transmitter affecting the function of one 

temperature control valve: and 

• Alarm for an exceedance of a designated setpoint, such as a high pressure or low temperature. 

The process control computer will continuously control and monitor the operation of the incinerator. When 

out-of-range conditfons exist, it wit notify the operator of those conditions. The process control computer is 

programmed to shut-down equipment (i.e., bring the system into a safe mode) when designated parameters 

are exceeded which is a protective mechanism against potential equipment damage, operation outside of 

permit limits, or conditions that might lead to a release to the environment. 

Continuous rr.onitoring of the incinerator and scrubber system is an important aspect of the system design, A 

• digitorreaticct of aif monitoring Instrumentation' is displayed-on the 'main -control- screen: An-autfible and visualalarm alerts the incinerator operator to significant deviations from normal operating conditions. This system 

allows an immediate response to adverse conditions by the operator. Automatic waste feed cut-off end 

incineration shutdown mechanisms are also interlocked with the monitoring system at or prior to reaching 

permit limit levels. Monitoring methods and calibration frequencies are listed in Table 2-3, 

The incinerator has an independent process control computer that Interfaces to the Quantum Progammable 

controllers, The process computer is capable of controlling the incinerator in case of a failure in a HMI server. 

This computer runs a RSVIEW HMI control software that provides operator rnterface to all instrumentation and 

controls, 

2.8 Automatic Waste Feed Cut-off System [40 CFR §53.1207(f) (1)(m)(F)] 

The incinerator has an Automatic Waste Feed Cut-Off (AWFCO} System that will shut waste feeds off in the 

event certain operating parameters deviate from allowable set points, The PLC continuously monitors 

operating parameters, making adjustments to the process as needed for proper control, Alarm logic is 

incorporated into the PLC system to automatically initiate an AWFCO. Table 2-3 summarizes the current 

AWFCO set points, AWFCO limits have been established based on several factors that are summarized 

below, 

• R eg u lata ry/perm it ii m its - e stabl i s h ed to co m ply with existing perm its. An exa m pie of this type of I i m it 

is the lew temperature limit, below which waste can not be fed until the proper limit is re-established. 

In addition, She HWC MACT regulations require that the AWFCO system be interlocked with the span 

of each process instrument that is part of the Continuous Monitoring System (CMS), A listing of these 

2-13 
AZCOM 

CMS instruments and their interlocked span setpoints is maintained as part of Veolia's Operating 

Record. • 

* Process safety fimits - established to assure process equipment is protected and unsafe operating 

conditions do not occur. An example of tfvs is inadequate excess air in the combustion chamber that 

can lead to fuel rich conditions. 

• Utility or Power failure - established to facilitate a controiied shutdown of the process during loss of 

process air, steam, water or electricity. An example of this is the loss of instrument air that is 

necessary for certain types process instruments to function properly. Wastes will not be re-introduced 

• i n to th e i n cinera tors u n ti I proper' o pe ra tion of key instru m ents is re-ostabi ished. 

In addition to the AWFCO system, operators can manually shutdown waste feeds or the entire process should 

this be needed. 

2.8.1 AWFCO System Testing 

Veo;'ia tests the AWFCO systems bi-weekly', as weekly testing would unduly interfere with operations by 

'ceasing and restarting waste feeds, potentially increasing emissions, incurring excessive downtime, burning 

additional natural gas during the downtime, and increasing operating costs. Testing of the AWFCO system is 

a time-consuirtihg and manpower intensive process, The current testing program has been in place under the 

RCRA permit for over 20 years and has proven to be adequate in detecting problems. This rationale is 

included in the facility's AWFCO Plan. In some cases this testing occurs more frequently depending on how 

often actual AWFCOs occur at the unit Per the.required frequency, incinerator personnel check the 

functionality c f AWFCO logic that is part'of the incinerator's PLC system io make sure that should process 

•csflditkms-deviate from-allowable-limitei -the- compter k^icwili-imtiato-waste-feed shutdo\vns-as-required. 

This is accomplished by manually simulating process conditions that are outside allowable limits and observing 

and documenting when the control or block valve software logic on the waste feed line begins to initiate vaive 

closure. Should actual AWFCOs occur during a given testing period, these are documented by operating 

personnel to satisfy regulatory requirements for system testing. Re suits of this testing are documented on a 

separate AWFCO Testing Log and maintained as part of the unit's Operating Record. 

2.9 Air Pollution Control Equipment Maintenance Practices [40 CFR 

§63.l207(f)(1){iii)(G)] 

2.9.1 Program Overview 

Once equipment is installed and operational, Veolia utilizes an extensive preventative maintenance (PM) 

program to keep equipment operational and prevent breakdowns and failures, Based upon the type of 

equipment and historical operations and maintenance experience, schedules for various inspection-and P M ' 

activities are followed. This includes aspects such as documenting detailed maintenance histories on 

equipment routine inspection and lubrication programs for high wear equipment and non-destructive testing of 

piping and vessels using techniques like ultrasound to assess integrity. The frequency of these activities 

varies depending upon the equipment, PM activity and the incinerators shutdown schedule, 

For example, frequent (i.e., weekly] instrument and certain mechanical equipment checks are made for critical 

process items. Lubrication, vibration analysis and other mechanical integrity checks are done at longer 

frequencies like monthly or quarterly. Finally, such items as inspecting refractory brick for wear, are typically 

performed when the entire incinerator is shut down for maintenance. 

2-14 FefcfUETjJ EC1C 
2.9.2 Test P ro g ra m P re pa rati on A c tf vitie s 

Prior to testing, instrumentation associated with key parameters of the test were checked, calibrated, or 

repla-ed, as appropriate, Co ensure proper operation of the instrumentation during testing (i.e., waste feed 

flowmeters and scales. CEMS, pressure transmitters, thermocouples, stack flowmeters, etc.). 

2-15 Febrgf^1

 PO'.c 
Table 2-2 Technical information Summary ort Incinerator No, 3 

Manufacturer .. Trade Waste Incineration 

Model No, TWI-2000: Series 2 

Type Fixed Hearth, Dual Chamber 

Date of Manufacture 19S7 

Dimensions Primary Chamber Secondary Chamber 

Extern a f Length 17,5* 17.5' 

External Diameter 9' 9' 

internal Diameter TT • TT i 

• Cross-sectional area 40.3 square feet 40.3 square feet 

Burners : Primary Chamber Burner Secondary Chamber Burner 

Manufacturer Month American Morth American 

Size 12,0 Million Btu/hr 6,0 Million Biumr 

Fuel' Natural Gas Natural Gas 

Primer Mover induced Draft Fan 15,000 acfm © 400; >F saturated, 22 in. water column 

2-16 Fcirruori) 2010 
Table 2-3 Current AWFCO Parameters and Limits for Incinerator No, 3 

System Device Units Cutoff Limits 

Calibration 

Frequency 

Total Pumpab la Waste Feed 

rate 

Mass Fiowmeters/Scaies Lb/hr > 3107 (HRA) Annually • 

Total Waste Feedrate Mass Flowmeters/Scaies . • Lb/hr' >4017 Annually/quarterly 

High BTU Liquid feedrate Mass flow meter ! • lb/hr > 2,0122 Annually . 

Low BTU Liqu/d feedrate • Mass flow meter Jb/hr > 1.9932 Annually 

Specialty feeder Stale lb/hr > 7242 Quarterly 

Total LVM Feedrate Mass Fiowmeters/Scales lb/hr > 47 (12 HRA) Annualty/quarterly 

pumpable LVM Feedrate Mass Flowmeters/S cares lb/hr > 46 (12 HRA) Annu airy/quarterly 

iSVM Feedrate Mass Flowmeters/Scaies lb/hr > 63 (12 HRA) Annually/quarterly 

Mercury Feedrate Mass Flcwrneters/Scales lb/hr > 0.0034 (12HRA) Annuaily/quarterfy 

Chlorine Feedrate Mass Flowmeters/Scaies lb/hr > 218(12 HRA) AnnuaHy/quarterfy 

•Ash Feedrate Mass Flowmeters/Scaies tb/hr > 673 (12 HRA} Annually/quarterly 

Primary Combustion 

Chamber Temperature 

Typo K Thermocouple op <1,59C (one-minute average) 

<1,712 (HRA') 

5=2,4C-0 (instantaneous)3 

Annually 

iSecondary Combustion 

Chamber Temperature 

Type K Thermocouple 'F *1,794 (one-minute average) 

<1,845 (HRA1) 

>2,40fl (instantaneous)7 

Annually 

Primary Combustion Pressure transmitter in. w.c. > -0,1 (5 second delay) Quarterly 

Secondary Combustion 

Chamber pressure 

Pressure transmitter in. w.c. ^ -0.1 (6 second delay) Quarterly 

Spray Dryer Adsorber Outlet 

Temperature 

Type K Thermocouple T >5DQ (one minute average)55 

>42G(HRA) . 

Annually 

Combustion Gas Flow Rate Pitot Tube acfm >17.198J 

H6.147 (HRA) 

Annually 

Stack Gas Excess Oxygen 'Zirconium Oxide fuel cell % < 3 (one-minute avg,) 2 Quarterly 

Stack carbon monoxide Infrared ppmv £100 (HRA) 

'^50Q (one minute average)2 

Quarterly 

Stack Hydrocarbon FID ppmv > 10 (one minute averagej ; Quarterly 

Stack gas opacity White Light % >10 (one mi nute ave rage)2 Quarterly 

Stack hydrogen chloride2 Infrared ppmv £100 (HRA)2 

2:500 (one minute average)5 

Quarterly 

Fabric filter pressure drop Delta P transmitter in. w.c. £ 2 or £ 10 (1 min. average) QuarterlyMin. Sorbent Feadrate Density Transducer lb/lbCI 2 ;' <1.76 

Min. Carrier Fluid Flowrate Flowmeter gal/lb ClaS <1.70 Annually 

1

 HRA means "hourly railing average* as calculated by averaging the previous 60 one-minute average values. j 

2

 This is a RCRA permit limit only. i 

2-17 
AXO M 

Figure 2-1 Hydrated Lime Specifications 

^r.n. 'ESTFfvn-C-*«tl 1..-iji-.fi 

cuds x f 

fiJL 

• i . . . , l n 

. . . - . - , ns. . A La 

-LSi.O I\iibS.J. ( v:i . 5 T-i . E 

^Wj , - - • .-

a . a s Cu >, ,T^i 

Cdi2a 4 , , , . 0 . 05 z « it. 1^ 

3 Viqu.i'va.l.oat . 0 . CU2 T-O 

3J.0 S . , . . - - i T 1 1 o 1-13 O .05 . 

A L P O 8 ; - - - - _ . _ . . _ tr.-sor i £ ci, j - - . . f.1 o r O, 3.17 

CO O ,J>I5 

.... . , 1 c- . I.LI 0 - 9 S 

o Lo • -Olf J 

MaO- .... . a . DOM.-; 

. .6E L U JA . .1 , JSlf.MI tl.. . .. . jJ-JV.U# S-. 

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

2-13' February 2D'0 
Incinerator Process Description 

Unit 4 
2,0 Incinerator Process Description 

MCQM 

2.1 Process Overview 

• Veolia operates two Fixed'Hearth Dual Chambered incinerators (Units 2 and 3) and one rotary kiEn -incinerator 

(Unit 4) at the Sauget, IL Facility, The two fixed hearth units are rated at 16 mi I iron Btu/hr each, incineration 

Unit rVo, 3 is a mirror image of Unit Mo, 2, Both of these units have their own waste handling systems as 

described in the sections that follow. Tho only difference being Unit No, 2 is equipped with four (4) baghouse 

modules, while Unit No. 3 is equipped with three (3) baghouse modu'es. However,'each incinerator is 

operated identically witii only three baghouse modules in service during operation, Unit 4 is rated at 50 mission 

Btu/hr and Is equipped with its own tank farm system, drum storage, bulk solids storage and feed systems, 

2.2 Waste Feed Systems [40 CFR § 63,1207{f)(1}(ii)(c) and (f)(1)(!ii)(D) and (E)] 

2.2.1 Uctit 4 Liquid Waste Feed System and Slending Operafions 

The Unit 4 Rotary Kiln can incinerate any-or the waste that Veolia is authorised and perrrrcted to receive. All 

physical forms of wastes will be handled and fed by the system's waste feed devices. Liquids will be fed to 

either the kiln or the Secondary Combustion Chamber {SCC). Bulk solid wastes will be fed to the kiln through 

the ram feeder. Containerized wastes will be fed to the kiln, thro ugh the ram feeder or the auxiliary ram feeder. 

This unit can receive any combination of wastes - liquid, semi-solid, or solid - with a heat value of up to 50 

m iii ion Btu/hr. • ' • 

• 'Unit-4 'is supported ty'Storage-tanks-located in-Tank-Farm-#3.- - These-tanks -are used-to store the-Hqufd •organicwastes, aqueous wastes, and pumpable sludges to be fed to the system; Uniike Tank Farm #1, alt of the 

tanks in Tank Farm #3 can be used as feed tanks to the incinerator. Several criteria are important in designing 

a blend from received wastes, These include compatibility, proper range of heating value, and permit 

restrictions regarding elemental composition (hased on emission limitations). Pumps to transfer these wastes 

to the system are installed in the tank farm, The material.is transferred througn aboveground pipelines from 

the tank farm to the incinerator, Pipelines used to transfer liquid organic waste and aqueous waste are 

equipped with strainers. 

In compliance with the Benzene NESHAP, all tanks are vented to individual carbon adsorption canisters for 

removal of organics before vapor is discharged to the atmosphere, Each carbon adsorber canister is 

essentially equivalent to a 55 g ail on container or greater, if necessary. Ail tanks are equipped with 

conservation vents, in addition to the carbon canister adsorber. Ail tanks are grounded, and: flame arresters . 

are installed between the carbon adsorbers and the tanks, 

2.2.1.1 Organic and Aqueous Liquid Waste Feeds 

The liquid waste injectors used in the combustion chambers are air-atomizing injectors. Thsse are used for 

injection of pumpable sludges, aqueous wastes and organic liquid wastes to the kiln and for injection of 

organic liquid waste fo the SCC, Dual fluid injection nozzles will be used for atomizaiion of the waste, Each of 

the injectors is rated at 0-3O0 gph, The liquid waste feed nozzles are sewed by parallel redundant pumps and 

recirculation systems with back pressure control. 

2-1 'Bm,ary 2C1C 
2.2.12 Packaged and Bu Ik Solid Waste Feeds 

Containers cf wastes are sampled and analyzed after receipt in accordance with the facility's Waste Analysis 

Plan, These, wastes can then be delivered directiy tp Unit 4 cr repacked' into small combustible containers at 

the facility. Repackaged containers are delivered to, and staged, in' the Container Storage LI n't No. 6 adjacent 

to the Unit 4 incinerator. When scheduled for feeding to the system, the containers of waste are transferred by 

forkfifts to the feed conveyors serving Unit 4, 

Bulk solids and non-pumpable wastes are delivered and discharged into waste feed bins in the Byik Solids 

Storage Building after being received, sampled, and analyzed. A clamshell operating from an overhead crane 

is used to transfer these wastes from the bins to the feed hoppers discharging to the system's ram feeder. 

The weigh hopper is equipped with weigh cells so each charge of waste can be weighed before it is 

discharged into the ram feeder. Fugitive emissions are controlled by a baghouse. cyclone, and carbon 

adsorption system connected to this system, 

The ram feeder is a 25-;nch wide by 42 inch high {inside dimensions) rectangular tube operated by a ' 

hydraulically driven ram. The ram tube is equipped with a vertical, hydraulically operated charge doer near the 

Kiin end.. This door is opened before the ram begins advancing to push a charge into the kiln. After the ram 

has Fuily retracted, a Jim it switch triggers the door to close so as to protect the ram feeder from the kiln's 

radiant heat The ram is capable of operating from 0-30 cydes/houx. 

The top face of the ram feeder has a X x 2' opening which receives waste charges from the hopper. The ram 

feeder isolation gate, the charge door, and the ram operate in sequence. Ac the beginning of a cycle, the ram 

is fully retracted. On a "start" command from -he operator or %he programmable controller, the ram feeder 

• fsojation-gate-opens-to receive a -charge-of -waste-from- -the -h&pper... The.gate .then, closes,, the charge, doer..'.... 

opens, snd the ram begins its advance. Onco the ram reaches its full' extension, it begins to retract. When the 

rarn is fully ret-acted, the charge door is closed and the cycle can be 'epeated. This system's sequenced 

operation combined with the negative pressure in the kiln prevent fugitive emissions from escaping the kiln 

ram feeder system. 

The rarn feeder also receives containers of wastes delivered by an auxiliary feed system. The auxiiiary feed 

conveyor is capable of handling charge weights of 1 to 100 pounds. The system is capable of handling charge 

sizes up to 24 inches in diameter and 24 inches tall. The auxiliary feed conveyor is capable of making 60 

charges an hour or one complete cycle every minute. • 

2,2,1.3 Specialty Liquid Waste Feed 

The Speciaity Feed System associated with Incinerator No. 4 is a Direct inject Liquid Feed System. 

2.3 Manufacturer, Make and Model of the Incinerator [40 CFR § 63.1207{f)(1pi)(A}] 

2.3.1 Combustion Chamber and Burners [40 CFR §53.1207(f)(1 )(m)(B) and (C) 

Incinerator No. 4 features a two-stage combustion process. Ignition of waste material takes place in the kiln, 

or primary combustion chamber (PCC). A secondary combustion chamber (SCC) serves as an "after-burner" 

for process gases-and is also permitted to incinerate high Btu liquid waste. Ignition of the waste takes place at 

temperatures in excess of 1600 degrees F. The secondary combustion chamber maintains a minimum 

tern pe ratu re of approxirr ate ly 1B7 5 d eg rees F. 

2-2 rwriary 2Cin 
The roar/ kiln is fabricated of carbon steei. It has approximate dimensions cf B'S" O.D. X 35' -:ong. It is 

supposed on a one-degree slope by two steel ttes c-r riding rings. Each riding ring rides on two pairs of steel 

trunnions and have an approximate outside diameter of 9 feet S inches. The thickness and face width or the 

trunnions are approximately 6 inches and 9 inches, respectively, Table 2-2 provides a summary or the 

;n cine rato r des ig n s pecificatio n s. 

The kiln is -lined with approximately 7 Vi inches cf dense abrasion-resistant high-alumina firebrick refractory, 

With this refractory system, the kiln has an inside diameter of approximately 7 feet and a length of 

approximately 35 feet, an integral cross-section area of approximately 38 square feet and an ircsrral volume 

of approximately 1,346 cubic feet. 

All kiln feeds will enter through the upper kiln face plate which is located on the feed end of the kiln. The plate 

contains a primary burner, three liquid feed nozzles {for pumpabie sludge, aqueous waste, and high 3tu liquid 

waste), a ram feeder and a surge venl 

The primary burner is equivalent to a North American 'Fuel Directed' ournercf 25 MMBtu/hr. and burns No. 2 

fuel oil or natural gas. The burner system is supplied with approximate^ 4,000 acfrn combustion air at a static 

pressure of 20" water coiumn (WC). The pilot for the primary burner will burn natural gas. 

The fuel system for the kiin (and secondary combustion chamber) is controlled by a Factory Mutual approved 

burner management system complete with interlocks and safety valves. 

2.3.2 Secondary Combustion Chamber (SCC) 

. Tne.SCC is a. vertical, .cylindrical.chamber.hawng. .approxi.roa.te dirnensions of. 1 G':6*. O,p, x 7T bighIt is 

fabricated cf carbon steel and lined with, an Inner course (hot face) of approximately six inches of high alumina 

refractory and an outer course of approximately two inches of insulating refractory. With this installed 

refractory, the SC C has an inside diameter of approximately nine feet The effective length (gas retention 

length) of the chamber is approximately 48' - 6". Consequently, the SCC has a cross-section area of S4 

square feet and an effective volume of approximately 3,084 cubic feet, At maximum combustion gas flows, 

the combustion gas residence time is greater than two seconds. 

Combustion gases from the kiln enter the bottom of the SC C through a refractory-lined side duct and exit from 

the top of the SCC through a refractory-lined duct to the tempering chamber. The floor of the chamber is 

sloped to facilitate the removal oi ash and solids through a slag tap. 

Tlie SC C is equipped with one burner mounted on the sidewall of the chamber near the bottom. The burner is 

a Trane Thermal Model, or equivalent, with a design heat re'lease of approximately 30 million Btu/hr, This 

burner is supplied with No, 2 fuel oil or natural gas and combustion air. 

As with the kiin burner, the SCC burner is supplied with atom king air and is equipped with a burner 

management system. This system controls the ignition and initiates an automatic shutoff when there is a loss 

of flame, corr.bustion air supply, fuel pressure, atomizing air pressure, pilot burner or ID fan. 

The SC C burner is a high-intensity, vortex type unit with a spin vane assembly, Socated within the wind box to 

impart an intense rotary motion to the combustion air. This rotary motion and the burner design provide, 

complete mixing of air and fuel, and recirculation of the gases within the combustion chamber promotes rapid 

combustion and high heat intensity, 

2-3 February 2010 
A~COM 

2.3.3 Location of Combustion Zone Temperature Device [40 CFR §63.1207[f){1)(xis)] 

The pyrometer that monitors temperature in the rotary kiln is located lop-center in the transition section 

between the rotary kiln and the SCC about two Feet downstream from, the exi- of.the kiln. The thermocouple 

that monitors temperature in the'SCC is located on - he west side of the chamber nsar the $C C exit duct. 

2.3.4 Hazardous Waste Residence Time [40 CFR §63.1207(fJ(1 

The hazardous waste gas residence time for the Unit 4 Rotary Kiln Incinerator is calculated as follows: 

• Rotary Kiin Volume - 1346 ft3 

« S econd a ryCombusiionChamberVolums-3D54 ft3 

• Total Volume-4430 ft3 

* Maximum Flue Gas Flowrate - 43,000 acfm {717 frVsec) 

* Total Combustion Zone Residence Time = (4430 ft3)/(717 ft5/sec) = 6.2 sec 

Based on the equadon 0=[(0.1 DL)/(NDSJ]; where: 

0 is the residence time in minutes, 

L is the kiln length in feet 

• N is the ratationai speed n revolutions per minute, • 

S -is the-kiln -slope .in feet.per. feet,.and 

D is the internal diameter in feet, 

and Inserting the known values for L (35), N (2), S (a,0174), and D (6,5) result in a residence time for the rotary 

kiin of 3G minutes. 

2.3.5 Combustion System Leak 

The kiin itself is equipped with a double seat system thai is comprised of overlapping, adjustable, stainless 

steel spring plates on both the feed and discharge ends of the kiln, The seeing edges of each plate are fitted 

with a sintered-metal wear shoe similar to a brake shoe with the inner seal resting on the kiln sheli. The 

powdered metal formulation ibrthe seai shoes in crude graphite granules, which make the shoes setflubricating. The void between the seass and the outer shell of the kiln pressurized to further prevent fugitive 

emissions, In addition to the kiln seal system, Unit 4 also utilizes an induced draft fan that maintains a vacuum 

of - 0.5 to - 1.0 inches.water column while waste is being fired into the system. 

2.3.6 Emergency Safety Vent 

Unit 4 is equipped with two emergency vents, one located at the kiln inlet which acts as an emergency 

pressure relief, the second is located at the top of ;he SCC as a thermal reiief vent. 

The emergency vent at the kiln inlet would only be required for an-occurrence that overwhelms the ability of 

the ID fan to control the pressure .of the kiln. The vent and chute opening is designed such that waste from the 

bulk soiids chute would not impede the escaping gas flow. A deflector separates the feed flow from the vent 

opening, The entrain merit cf solids through the surge vent is minimal. As an extra precaution, the exhaust 

2-4 F5:ruap/2D1C 
MCOM 

opening of the vent >s angled to provide a horizontal exit, thereby minimizing solids entrain men* into the air, 

The vehOs kept closed by weighted louvers. These louvers will open onf'y if the pressure in the kiln suddenly 

rises beyond'the compensating capacity cf the ID fan, A limit switch on the louvers wiif automatically shutoff all 

waste feeds to the kiln and SCC when the vent is opened. 

The incinerator is also equipped with an emergency safety vent (ESV) located at the top of the secondary 

combustion chamber. This ESV is a refractory-lined emergency thermal relief vent (TRV) which is heid in the 

dosed position by a pneumatic cylinder. The control valve in the line supplying air to the cylinder and the 

cylinder vent valve which opens the TRV are located in the control room for each unit. Valve locks (with, -teys 

attached) are utilized to deter inrjischrrJnate operation of these valves. Opening cf the TRV allows hot 

combustion gas to vent from the combustion system during emergency shutdown events. The purpose of the 

TRV :s to protect the downstream ARCS from excessive temperature situations, A limit switch on the TRV 

shuts off all waste feeds to the system as it senses that the cap is opening. 

2.4 Procedures for Rapidly Stopping Hazardous Waste Feed During Equipment 

Malfunction [40 CFR§63,12Q7{f)(1)(viii)] 

Equipment malfunctions are identified by the control system, observation cf process control variables, or by 

regular field inspections. 

In the event cf a minor equipment malfunction (e.g. waste feed or scrubber leaks), the control room operator 

will be notified. The control room operator will then close the-waste feed valves and disable the waste feed 

pumps. 

' 'in' ihe'a've'nt'bT'rhapr' equipmehi'malfiiihctiori '[e.g.' fire},' the emergency 'Stcp-butiorrfocated in'the •control room • • • 

will be pushed. If this button is pushed all equipment will switch to its fail-safe position, 

2.5 Aar Pollution Control Equipment [40 CFR §63.1207(f)(1 )(iii){G)] 

2,5.1 Air Pollution ControL Systems Descriptions 

The air pollution control system consists of a tempering chamber, two spray dryer absorbers, and fabric filter 

baghouse modules. The air pollution control system neutralizes acidic compounds and removes particulate 

from the exhEust gas. Two subsystems, the spray dryer absorber and the fabric filter, carry out the chemical 

neutralization and particulate removal functions, respectively. A third subsystem, the lime system, is used to 

prepare and provide lime slurry to the spray dryer absorber for use In the chemical neutralization process. The 

induced draft fan and stack provide the mechanical energy required to transport the Flue gas thro-jgii the 

interconnecting ductwork, to its eventual discharge point to atmosphere. 

3?.3,1,1 Tampering Chamber 

The tempering chamber is a vertrca?, cylindrical unit designed to cool the combustion gases using a series of 

internal dual-fluid (water and air) spray nozzles, The combustion gases enter the top of the chamber, flow 

downward through the spray pattern and exit from the bottom of the chamber, The spray pattern is designed 

to eliminate direct contact of water with refractory, and the chamber is designed to maintain a dry bottom under 

all operating conditions, That is, the injection rate of spray water is controlled so that it is'completely vaporized 

and carried out of the chamber in the combustion gases. The tempering chamber is approximately 49' high 

with 11' I.D. and is fabricated of 34 inch nominal plate thickness carben steel (ASTM A36) and lined with 

refractory, The spray nozzles and extensions are fabricated of 304 SS material. 

2-5 Rsna.ary ?,31 • 
AICOM 

The tempering chamber is sized so that a comoustion gas retention time of greater than one second will be 

\ maintained a: all gas flows. Because seme molten-particulate materials in the combustion gases are cooled <n 

this process ur it to below their fusion point some solids are generated and collected in the chamber. 

Therefore, the chamber has a cons bottom and a slide gate to facilitate the removal of solids. These solids are 

discharged onto a .conveyor system, which Transports them to a hopper 

2.5.1,2 Lime System 

The lime system-prepares iime slurry for use in the chemical neutralization process in sufficient supply and 

concentration to maintain- continuous Hue gas treatment in the spray dryer absorber. The system has been 

designed for batch mixing to provide this service. Veolia utifees hydrated lime as its neutralizing agent ir the 

air pollution control systems. The key neutralization parameter of the hydrated iime is the 'CaO Equivalent." 

Figure 2-1 is the specification sheet for the hydrated lime that Veolia uses. Veolia has used this specific 

product for over 2D years and plans to continue with its use, Although if Veolia dees change suppliers or type 

of line in the future, it would have a "CaO Equivalent' specification equal to or greater than the 72,5% shewn 

on Figyre 24. 

Hydrated lime is stored in a storage bin above the lime preparation area. The storage bin is sized to hold 

enough hydrated iime to maintain several days af system operation at the maximum combustion rate of the 

incinerator. Lime is discharged through the conical storage bin bottom, The flow of the material from the bin is 

aided by a vibrating "live bottom," or bin activator. - A variable speed screw feeder is used to meter the 

hydrated lime in the proportions required for batch mixing lime siurry. The iims is mixed with water in a tank . 

beneath the lime storage bin. The screw feeder speed and the rate that water is added to the iime siurry Sank 

are variable so that the desired lime solids concentration can be achieved in the tank. The variable feed 

S . adji i strne'fi fs' allow wale r a hd Tl me to be added to the irm e -siurry • tank • at -a- rate that -win allow • a- ba'oh mode -of 

mixing, An agitator is provided' in the slurry tani< to mix the water anc' lime and to maintain the suspension oflime solids- The mixed lime slurry Is pumped at a continuous rate of flow through a recirculation loop to the 

SDA nozzles, 

2.5.1,3. Spray Dry Absorber 

• Unit 4 is equipped with two Spray Dryer Absorbers (SDA) located immediately downstream of the Tempering 

Chamber. Each SDA unit is fabricated of 3/8 inch carbon steel, The function of the SDAs is to: 

» Further cool the combustion gases from 600-800°F to 3DO-500r'F, 

* Neutralize and remove HCl and other acids from the combustion gases, 

• Re m ove a po rtion of the pa die u I ate f f ly as h} f ro m the se g ases. 

Slurry fiow to each spray dryer absorber (SDA) is metered by a flow control valve to obtain the proper feed 

concentration to the spray dryer absorber. Manual adjustment to the flow is made as a function of the SDA 

outlet temperature and as a function of the output from a hydrochloric acid (HC!) analyzer in the gas duct 

downstream of the fabric filter. 

The combined units are sized to remove more than 820 lb/hr. of chtori.ie from trie combustion gases. Each 

SDA is approximately-72' high by 10'7" in diameter. Each unit includes a head section, and a 50*conical 

hopper. Each. SDA chamber has one access door in the upper section. Each hopper has one access door, a 

S flanged clean-out perl, and a drain connection. The SDA head section consists of a flanged inlet connection -

2-6 
AXOM 

and a ho? gas inlst plenum. Tho dual-fluid aicmizinrj nozzles include stainless stool housing,? and steiiiicd 

inserts. The nozzles are assembled to permit fieid removal From the piping, The too lime slurry piping 

headers have automatic isolation'valves, 

Combustion gases enter the top of each of these units, flow downward through a central duct and are 

dispersed symmetrically from this duct into the absorber chamber at a velocity and direction that assures 

optimal contacc-with the cloud of atomized lime slurry droplets introduced into the chamber by dual-fluid (lirne 

slurry and air} rozzlcs. The gases then flow downward through each absorber chamber and exit through a 

bottom side duct, As the gases contact and pass through the cloud o£ atomized iime slurry, the water in the 

slurry evaporates, coo'ing the gases. Simultaneously, the lime in the slurry reacts with the hydrogen chloride 

in the gases to produce calcium safts. Some of the resulting dry material, consisting of calcium salts, fly ash 

end excess lime, falls to the conical bottom of each unit, The dry materia) from each unit is discharged to a 

conveyor system which transports it to a dump trafer or equivalent type system. 

2.S.1.4 Fabric Filter 

Gas exhausted from the spray dryer absorbers is distributed to two feoric Filter modules connected in parallel. 

Each module is divided into three compartments connected in parallel, which contain multiple fabric filter bags 

through which the combustor gases pass to .remove particulates. Within each compartment, the gas is 

passed through Teflon-coated fiberglass cloth bags. The gas passes From the outside to the inside of the filter 

bags. Particulate entrained in the gas stream is mechanicaily deposited on the outside of the filter bags as the 

gas passes through the cloth. 

Each compartment has a clean air plenum and housing section to contain approximately 308 bags. Each bag 

•is'HppTcximatery'5:l'fndiamet8rby-5!- long,-Tte-baghouses-^e-febrica^ 

construction, gas tight and stiffened to withstand the maximum operating negative pressure. Each 

compartment has a tube sheet that supports the baas and provides for top bag/cage removal. Access to the 

clean air plenum is via a bolted access door. Each trailer mounted rnit contains the compressed air headers, 

gas inlet and outlet manifolds, and the conveyor. 

The fabric filter cleaning mechanism utilizes jets of air to clean the filter bags, Periodically, the cleaning 

sequence will be initiated, The sequence is started when the differential pressure across the titer reaches a 

predetermined setpoint of approximately 8-0" w.c, or when the operator initiates a cycle. The controller then 

sequences to each row of filter bags in each module^ refeasing a burst of air opposite to the direction of gas 

flew, The quickly released burst of air dislodges dust cake on the exterior of each bag as it travels from the top 

to the bottom cf the bags. Released from the bag, the dust cake falls by gravity into the hopper at the bottom 

of the module, From there it is discharged to a conveyor system which transports it to a dump trailer, or 

equivalent type system. 

Treated by the spray dryer absoroers and filtered by the fabric fibers, the cleaned flue gas exits the fabric filter 

compartments to an outlet manifold for exhaust. 

2.5.IS Carbon Injection 

The carbon injection system will air inject activated carbon into She plenum immediately upstream of the 

baghouses and allow for a more efficient means of controlling Dioxin/Furan and mercury emissions. This 

system will be controlled by an existing PLC which will control the input of activated carbon to the baghouse 

iniet plenum. 2 to 20 pounds per hour of powdered activated carbon will be air injected into this plenum and 

2-7' February 231C 
AZCOM 

allow for direc; contact with the stack gases exiting tlie *SDA's. Trio key adsorption, parameter for the carbon is 

..s trie Iodine IVunber. Figure 2-2 is tho specification sheet for the powder activated carbon that Veolia uses. 

Veolia has used th;s specific product since the start-up of the carbon Injection system and plans to continue 

with its use. Although, if Veolia e'ees change suppliers or type of powder activated carbon in the future, it 

would have an Iodine Number specification equal to or greater than the 500 mc,'g shown in Figure 2-2. 

The amount of carbon :s dosed ina dust-free manner into a low pressure air stream via pneumatic eduction, 

The eductcr uses a blower for the motive air. High and low air pressure switches ensure that the blower is ' 

operating correctly and tiiat the carbon delivery system is dear from obstruction. The minimum high pressure 

setting, is 4 psig and the maximum low pressure setting is 1 inch water column. The carben/air stream w II then 

travel through piping to the injection nozzle into the ductwork. The carbon will contact the gas stream exiting 

the SDA's and allow for the adsorption of any diosen/furans and mercury that might be present in this stream, 

Adsorption wfl continue as the stack gases proceed through the baghouses, The clean stack gas will exit the 

finai'stack via the induced draft fan and the captured solids will be discharged from the baghouses via the 

screw conveying system into an enclosed dump trailer for disposal at a Subtitle C landfill. 

2.5.1.6 Induced Draft Fan and Stack 

• The induced craft fan and stack are located downstream of the fabric filter, Combustion gases are drawn 

through the system by a 400 hp induced draft (ID) fan, rated at 53,000 acfm at 400c F saturated, and 25" water 

column pressure. The induced draft fan provides the mechanism for transporting the incinerator flue gas 

through the spray dryer absorber, fabric filter, and all interconnecting ducts. The ;D fan includes an inlet 

voiume control damper to be used to control the velocity of the gas within the ducting ard treatment devices. 

'"-Treate d gases'are' exhausted'from 'the'induced draft'fait "to'the atmb'spfrere' through atCO-ft high' stack: The " 

stack diameter for Unit 4 is 48 inches I.D. The stack is equipped with instrument sampling ports and a 

sampling platform fcr emissions testing, Figure 4-1 provides details on the design and sample pert locations 

and con Fig u rations for the stack, 

2.6 Stack Emissions Monitoring [40 CFR §63.1207(f)(1)(iH)(H)J 

The conti r, u o us sm issio n s mon fori n g syste m f C EM 3) consi sts of sam pie probes, sa m pie del ivery and 

conditioning apparatus, and gas analyzers, Samples are extracted from the transition ducting located between 

the ID fan and the stack. A CE M performance test and quality assurance program has been implemented in 

accordance with the Appendix to Subpart EE£ of Part S3—Quality Assurance Procedures for 

Continuous Emissions Monitors Used for Hazardous Waste Cdmbustors. 

Responses from each CEM S are fed to the Control System (CS) where the CO hourly rolling average is 

calculated and interlocked to the waste feed cutoff valves as part of the Automatic Waste Feed Cutoff System 

{AWFCO) discussed in Section 2,5, belaw. Tne following provides a brief description of the CErViS 

instruments including the operating range and measurement principal, 

2.S.1 CEM System Description 

The Continuous Emissions Monitoring Systems (CEMS) currently being utilized at Incinerator 4 analyzes for 

opacity, carbon monoxide, hydrogen chloride, total hydrocarbons and oxygen. These monitors, except 

opacity, are extractive devices mounted in the ductwork between the ID fan and the stack. The table below 

> summarizes the analyzer specifications. 

2-8 Fsb-unry £010 
Tho opacity monitor cor.tinuously measures the stack gas opacity and reports the measurements to an 

indicator ana" a recorder. An opacity that excosds a preset limit tiggi^s an aiarm and Interlock. 

Carbcn monoxide and hydrogen chloride are mastered-with extractive no n-G:'s perse Infrared analyzers. Totai 

hydrocarbon is monitored with an extractive flame ion detector analyser. Oxygen is monitored with a 

zirconium 6x;da cell. 

Stack gas flow rate

 ;s continuously monitored using an anubar that sends a 4-20 mA signal to the PLC that 

converts the signa; to acfm. 

Table 2-1 Vsolia ES Technical Solutions - Continuous Emissions Monitors 

Parameter Current Mfg. Range Principle 

Oxygen COSA ' 0-25% Electrochemical 

. Carbon Monoxide Echochem MC 3 • O-200 ppmv 

• 0-3000 ppmv 

infrared 

Total hydrocarbons Thermoe-ectron 0-100 ppmv F ID/Infra red 

Hydrogen chioiide Echochem, MC 3 0-1 CCD ppmv infrared 

Opacity Teledyne G-1G0% White light 

.. Stack, gas.flow. PSE/Rcsemount 0-55,C00 acfm Pressure drop 

2.7 Process Monitoring and Control 

The faciEity is equipped with a state-of-the-art monitoring and control system, which facilitates compliance with 

permit conditions, and otherwise, collects process control information; facilitates efficient operation and detects 

and prevents damage to the facility. The system consists of three major components: 

* A human-machine interface (Hivll) system, 

» Programmable logic controllers [PLC'sh and 

» A high speed ethemei cable connects all control system components 

The desired ccntroi functions are implemented through the HMI system. Ail digital control and emergency 

interlocks are accomplished by the PLC. 

The control system is capable of monitoring the "operational er.vefope:: of the incinerator and is capable of 

performing a number of activities inoluciing: 

» Control room indication of processor sensors located withtn tie incinerator system (such as pressure 

indication of a field .installed pressure transmitter); 

2-9 February 201C 
» Process contro Ii er for s ing I s in stri J ins nt • oop s or a n i n d i vid u a I s u b-s y sfc m, such a s a tem pe rature 

s control loop involving a sensor reading from one temperature transmitter affecting the function of one 

temperature contrpi valve; and 

* Alarm, for an exceedance of a designated setpoint. such as a h.:gh pressure or low temperature. 

The process control computer wiil continuously control and monitor the operation, of the incinerator, W'n^h outcf-range conditions exist, it will notify the operator of those conditions. The process control computer is 

programmed to shut-down equipment {i.e.. bring the system into a safe mode) when designated parameters 

are exceeded, which is a protective mechanism against potential equipment damage, operation outside of 

permit limits, or conditions that might lead to a release to the environment.. 

Continue us monitoring of the incinerator and scrubber system is an important aspect of the system design, A 

digital readout of all monitoring instrumentation is displayed on the main control screen. An audible and visual 

alarm aJerts the incinerator operator to significant deviations from normal operating conditions, This system 

allows an immediate response to adverse conditions by the operator. Automatic waste feed cut-off and 

incineration shutdown mechanisms are also interlocked with the monitoring system at or prior to reaching 

. permit limit levels, Monitoring methods and calibration frequencies are listed in Table 2-3. 

The Incinerator has an independent process control computer that interfaces to the AH en-Brad ley 

programmable controllers. The process computer is capable of controlling the incinerator in case of a failure in 

a HMI serve:. This computer runs a RSVIEW HMI central software that provides operator interface to aii 

instrumentation and controls. 

2:3 Automatic Waste Feed - Cutoff System {40 CFR f S3,42Q7{fK1 W»W)] 

The incinerator has an Automatic Waste Feed Cut-Off {AWFCO) System that will shut waste feeds eff in the 

event certain operating parameters deviate from allowable set points. The PLC continuously- monitors 

operating parameters,' making adjustments to the process as needed for proper control, Alarm logic is 

incorporated '.hto the PLC system to automatically initiate an AWFCO. Table 2.-3 summarizes the current' 

AWFCO set points. AWFCO limits have been established based on several factors that are summarized 

below. 

» Regulatory/permit limits - established to cornply with existing permits. An exarnpIe of this type of Iimit • 

is the low temperature limit, below which waste cannot be fed until Lhe proper limit is reestablished. 

In addition, the HWC fVlACT regulations require that the AWFCO system be interlocked with the span 

of each process instrument that is part of the Continuous Monitoring System (CMS), A listing of tfiase 

C M S instruments and their interlocked span setpoints is maintained as part of Veolia's Operating 

Record. 

• Process safety limits - esta b I i s h ed to assu re n recess equ i pmert is protected a nd u n safe operati ng 

conditions do not occur. An example of this is inadequate excess air in the combustion chamber thai 

can lead to fuel rich conditions, 

» Utility or Power failure - established to facilitate a controlled shutdown of the process during toss of 

process air, steam, water or electricity. An example of this is the loss of instrument air that is 

necessary for certain types of process instruments to function properly. Wastes will not be reintroduced into the 'incinerators until proper operation cf key instruments is re-estabtished. 

2-10 Fstrjary 231D 
A r-. i COM 

In addition to the AWFCO system, operators can manually shutdown waste feeds or the entire process should 

this ce needed. 

2,3,1 AWFCO System Testing 

Veoiia tests the AWFCO systems bi-weekiy, as weekly testing would unduly interfere with operations by 

ceasing and restarting waste feeds, potentially increasing emissions, incurring excessive downtime, burning 

additional natural gas during the downtime, and increasing operating costs. Testing cf the AWFCO system is 

a time-consuming and manpower intensive process. The current testing program has been in place under the 

RCFiA. permit for over 20 years and has proven io be adequate in detecting problems. This rationale is 

included in the facility's AWFCO Plan. In some cases this testing occurs more frequently depending on how 

often actual AWFCOs occur at the unit. Per the required frequency, incinerator personnel check the 

functionality of AWFCO logic that is part of the incinerator's PLC system to make sure that should process 

conditions deviate from allowable limits, the computer logic will initiate waste feed shutdowns as required. 

This is accomplished by manually simulating process conditions that are outside allowable limits and observing 

and documenting when the control or block valve software logic on the waste feed iine begins to initiate valve 

closure.. Should actual AWFCOs occur during a given testing period, these are documented by operating 

personnel to satisfy regulatory requirements for system testing. Results or this testing are documented on a 

separate AWFCO Testing Log and maintained as part of the unit's Operating Record. 

2,9 Air Pollution Control Equipment Maintenance Piracticss [40 CFR 

Once equipment is installed and operational, Veolia utilizes an extensive preventative maintenance (PM) 

program to keep equipment operational and prevent breakdowns and failures. Based upon the type of 

equipment and historical operations and maintenance experience, schedules for various inspection and PM 

activities are followed. This includes aspects such as documenting detailed maintenance histories on 

equipment, routine inspection and lubrication 'programs for high wear equipment and non-destructive testing of 

piping and vessels using techniques like ultrasound to assess integrity. The frequency of these activities 

varies depending upon the equipment, PM activity and the incinerator's shutdown schedule. 

For example, Sequent {i.e., weekly} instrument and certain mechanical equipment checks are made for critical 

process items. Lubrication, vibration analysis and other mechanical integrity checks are done at longer 

frequencies like.monthly or quarterly. Finally, such items as inspecting refractory brick for wear, are typically 

performed when the entire incinerator is shut down for maintenance. 

2.9.2 Test P rag ra rn P re parati on Activ iti es 

Prior to testing, instrumentation associated with key parameters cf the test were checked, calibrated, replaced,-

as appropriate, to ensure proper operation of the instrumentation during testing (i.e., waste feed flowmeters 

and scales, CEMS, pressure transmitters, thermocouples and pyrometers, stack flowmeters, etc.). 

§63.12D7(f)(1Jp)(G)] 

2.3,1 Program Overview 

2-11 Fab-usry'201!) 
; Table 2-2 Technical Information Summary on Incineration No. 4 

[ Manufacturer Trade Waste Incineration 

•i 

;i Model No, 

TWI-2000, Series 2 

Type ' Rotary Kiln 

Date of Manufacture 1389 

Dimensions Primary Chamber Secondary Chamber 

External Length 35' 

Externa? Diameter B'8" ID'S" 

internal Diameter T 9' ! 

i " 

i Cross-sectional area . 

38 square feet 64 square feet

 1 

Burners ! Primary Chamber Burner Secondary Chamber Burner 

Manufacturer i 

j 

North American Trane Thermal 

3 ize 12.0 Million Btu/hr 30 Million Btu/hr 

Fuel Natural Gas Naturai Gas 

Primer Mover ; nduced Draft Fan 4,000 acfm @ 400*F saturated, 20 in, water column 

2-12 .-abruary iiO',0 
Table 2-3 Current AWFCO Parameters and Limits for Incinerator Mo. 4 

System ( rJev(ne Units Cutoff Limits 

| Calihratjon 

| Fr4(|Utiicy 

Prmary CoT.bus[:an Chamber TDnipurature • Pyrgreter T 

^ 1.2^C (cre-minute av&-age)'. 

=3,4na [nsiamaneiius)3 

i 

| Ar.-,ually 

i 

LSscnndary Ocrnhusiioi Chirr b=r TurnperaLre ; lyps K ;'hsrrn«5oupl& T 

S1.S2E (i-.e-minute average) * 

•=1.BBH (HRA') 

su,«a f nitoi'laneons)1 

: .Am.'jslly 

Hr.mnry Co-.busiion Charnbar measure Freisuro transifiifeer in w.c. £ arrcsstierlc (lnsta nlaneous; Ouan&'v 

ii'jcciiidu.ry' CombJsUoT Chamber pressure Press uroVansniter in. w.c. =: atncsslierl: (Instorrteneous;. Oua-lfi'v 

Spray Diyu: Adsoiboi lillc' I'eiiipfjrHli.ra Type K ThermjrjOtlple 2l23J(aiiu i-huteav[i,

age?;>'; Ar:;lu3ll/ 

Spray Dr/=r Arisnrbsr 0 JfelTe-npO'aty* T'/pp- K The—occ\jp!-.i 

a £K> inns rnhute average;2 

• M34 (I iRA) 

Anr.uall/ 

Total Pi;.T:;iable Watte FBodrab Mass Hew meter/scaJeS 

pcc->22Sa (H?Ai 

scc->iM 8 ;i-i7vy 

Annually 

•Trjial Waste FEse'rare MaR=i rtrjwmeter/scaluy •Ibi'h- H-i.aaa ;H=IA.I Annjallvi' Q jsfcry 

I.VM rgiwrata flow metEr/acalea lb.tr 

Pimpabls •»4(' 

Tulal - > 50 

Ann jallv' Q-jHrtfiriy 

•SVM rssorala Mass' Haw meosr/acBles Ib.'hr >fi^.;i^hPA) Annialiy' Q-jsrrerly 

Mersjry Feedrara Masa tew mtiur.'scales lb/hr *D.C23 (12 I IRA) ArinuallVj' Q jaiiary 

: Ohbrlne '-''eeclrate : Mass hsv/ mewr/scaias Ibftr >2£2 f'2 HRA) AnmtalMQuarerV 

Aa:, Futfljfa'j; Mass Dow mecsr.'scaleE Ib/rr Anruallyi'QuarSirljf 

1 IWhr *S.2-fMSA> 

•Csrbcci Iniscfcn Svisicin Maximum 1 ciiv P-assart; . PrassJiu awltih in. v.x. *1 •uaitu.-. •uaitu.-.v 

Carbon hiec"io*l SvH'ernMir.irrjrr. .Hiflh Pressors Prp.aa.Jra Switch psig Ouarte-'y. 

COfiibL^llc-ri Sas flow Rate Aiuhar acfr Ar-nually 

SlocK Gas FMJOSB Oxygen Zirconium (Mtfe fuai soli % 5 J (ana minute averaga)' Quarter^ 

j 

Stsclr carton monoxide i 

j 

Infrai ied ppmv 

(HRA; 

s£t;o minute a'rtra^s.)2 Qi^arterli' 

Slsck Hydrwarbnn . ; FID ppmv a 1D fcrra minute average^' QL'arteriy 

Slac< ga.5 cwastv WKte Light % [cr.a minute Ei^rage)3 O^artfiriv 

£tsn< hyttroger: chlorida? 

1 

pprr.v 

iai/MRA) 2 

=:S»M (oris n^'i-De average)2 ••jarterty 

Licud fegdratn Mass Hew meter Annually 

MaaE Bow inousr fa'hr s 1.1301 Annutliy 

Ufummed snrl Bui* Salids F=adr£le Seals lafhr C.:jarteriy 

Fabric fife' pfotaura drop Delta P ira.-3tritter • In w.c. i. 2 cr> to fone •ninijte average/2 Quarto rlv 

Min. Sorbin; Fgedmte DEr.3% Transducer \hl.b C!v <1.01 

Min. Carrie.' Fluid Flowfaia Flowmeter gsvlb Cl 2 •=1.B1 Annuallv' 

1

 HKA. mssns 'hQur'y rolling avsrago' as calculate by averaging Hie prevfcus SO ane-mlri'jla average values. 

1

 This vs a RCRA permit :i,mlt Dnli' 

Z-13 Fabrja"/2D1D 
Figure 2A Hydrated Lime Specifications 

Ff/I r"& f. <J ri f..i >•- => 

Cod e r^-Sao 

i . U 

[QRljj , , , , , s.E.ri* 1.5 •S»7 .sr.* 

22. a t-B 7 3 . © 

~d V-a 

C.ra ^ .... . . t'n 5. 75 

CiL204 ' c , ft'. I'ii o .13 

- . ' . . . . ' . . -D. 03.3 n 

e/.O, ..... . 

...... . 

La 0 ,tS3 . 

A^' J S ; . . . . . , . , , - 0.2.0 to a ma 

^.LV o 

Ma.^ - . . .. . . 0. 10 il> 0 r.r, 

" vl.l ti S3 

F. rO ^CJ a O iZ 

MtG u - , - . . 0-OO1 5 C O o , 

K i n MM .tt>S 1.CU. 0% 

95 . 

i«lce o Sa.l 92 , & 

=i friis.pjp.a £ JL'Jhi> 

j x-i.' u-u K 

2 - U 
MCOM 

Mi, 

Figure 2-2 Carbon Specification Sheet 

ESO 

WORJ T America s Inc . 

Most Chcaoss + Ftease Rt=3ESI Pcrformanco. 

DATASHEE T 

Ha. 110.1 

Nov 2Ctl3 

D^RCCT FGL 

POWDERED ACTIVATE) CARtKJf* 

DARCO FGt |2 4 lignite ccai-based acwajed oarbon rnanufactufmi spcdficaai' JOF tie removal Cf heavy rhelal* 

awJ atler emvKsmlnarne- iyptcejly jbunrf in incinerator flue gas emissidn alrcsros. Its n|:«n pate ssti\Ktt*'5 ami fins 

particle- SEE psrrrrtthe rspid adsorption bfgaacoUs mercury, «tfoXins ;PCCD) *nd fc^ns fprjOF), vyhJah is CEitirjtfT 

fbrgona" adscrp*/e pBrfonrnarres.la H-Jiirjasaliefama Yi'trarr; toi itw'it tsnfti are eh.art 

DARCO FS L is a Ffac IVAviCiJf pr,uwter>*t isarfiflh yHt[l fflinfrri^l caking tendanoaa, which maiHB if kfea' for 

aubrcnafra ttosfcig systems Mlft Ctflf Dr Vi*J ftiJeHlortdireglY Ina the llue gas stream. It va maraJFscttirad 'Mtn a VEry 

h^h Igrfliost tBttipcrslurs in punut? safas dpfirstlw at the: elevated tejnpara'jjraa inh<tfcnl in incinerator Boa £jas 

streams. 

Product Sap^rfjcaTKMistiSafcissES itecaWijizring afnciency 

rjfopfejrE, 'A as patted 

Mesh sk a CU.B. Start Sctiss) 

LESS than 325 m^St* (4i5 p.-n)v & 

Tyaicai Prpjjgf lie?* 

Iodine pOmfcst; rfifHa 

Total liiifSir, % 

BttBc'iteiifflIK 'farftpKI, ff'rh'L 

IbtfC 

Siutfeca area, rnVg 

tgtlltlim temperature,, °C 

40 min. 

SDmSn. 

•DO 

0.6 

'K63' 

3 ° 

SSiD 

4S0 

'far geiiersl ipiorcnatkin; only, not to ba itscd as pit chase sije^lfcalls ns, 

P'acAaaiitnrrrBiTs.^PriaKsn. 

etancferd package fs. 900 S) WWSn pofyofapryteTe amn begs vMh a, glued pfesfe Jrar. Alternate package |ne|ijtfaa. 

pnsunwnfe tK*; Eaifef. 

AsttolSd WKbOft fMOt REGULATED} 

©osmpt Fcurif DOT, iATA, and, MD G regulations 

[onpQrrJEsport das^iScaliari: 3E02.10.DtXia(HS Tariff Classirisalior.) 

DnmestfcF'fi^rjIllGlassi&iefiori; N fJ F C LMOGBff 

SatW 

Wst WJliifiristi tafboft deptetaa oxygen torn air -arid, iticrefafs, dangerously low levels oF OKygan may he 

irtcorjntenssl. Whenever vjorie^s enEa-r a Veaael norilaSning activated carbon, Bhc VrsScPa oiCygan content 

Shmtd ctefenvplcied and yrartc pro-neduraa for pcrtantialCy low cKygcn areas shoufci ba TcJIoVrad. Appropriate 

pno-sictfve; equtpn-i^n* should ba worn. Avoid bhalafioc of {MfiSas&'e 6i»rtX5in tiust. N5 pi'OMejns ars knuvm io 

sa- easaclsfedj In hiswlSing thfe maisrML HCWOYor. tho jjruriutt tmy flpntain U? tg 1^% s3|i:^ ^quaitz). Lor{jterm sottaiariiin of high duat concontraiion? ^art Jsai ts respiratory loipfllfnient. Usa forescf Ventlfatlon cf a. 

Cfttst masKWtieii nsossaaqy for protection agajnat afrbcrno aijst ojtpcsurs (s » Cyjij 01 F-SUiaat HogalnliDna -

TtUe.29, sutapiini;, par, 1910.1000. Tablo Z^3). 

Fl*r*: An^ spacirealkn glmi iralfd flt lime pF tou^iies* af <h(f pLimrcttrgci, Ha^tvir, wa q-ilrmun j] pollsy iir 

"320S iYestUftliteteitr AVfincre, Marshal, TX TSSrij" 

Tz!*phono (Q03) B2&-iC0Q* 1-30OJ4-t-$Z45 • PAX (303? H23-1Q03 

ft'my.riCVTf.aiYiafJhaa.rjoni »mr&grjorjt-amcrfoa^.CCifn 

2-15 
CMS Performance Evaluation 

Unit 2 
TAG; 

LOOP: 

DESCRIPQN: 

LOCATIOLI 

LP-SHT 

REMARKS 

INSTL-EMKS 

SPEC-RMKS 

S/N: 

TSfJ mSTRDWENT CAT,lBRa.TIO^ RECORD 

nun' #2 

WT 

2D4 

WEIGHT Tsmsmrx-ER 

SPECIALTY FEEDER MODEL,; 

SCALE; 

CALIB-BI: 

CALIB-OUT: 

PROCESS-SP: 

ACTION : 

TOLEDO 

3140 EXP 

0-4f 000 # 

D-4,0QG # 

4-20 MADC 

0#*819 et a 

2QQ#=*9B3 CtS 

1#=.S1S chs 

I/O MDMBBSL: 30052 

CALIBRATION NOTES 

Check scal e j. digita l Calibratio n per , Toledo instructions . 

Then with, no weigh t on scal e adjus t analo g Hero.. {NOTE: HMI 

wil l not displa y numbers les s than zero) . Nex± add weight 

>* t o 10% are more o f scale s range, tha n adjus t analo g span/ 

t o ind.ica.te weight on scale , as read, on HMI screen . 

See Manufactures-literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

C&LIBRATlON REPORT* 

INSTRUMENT EEftDlMS 

Before Calibration 

After Calibration 

TKPOT V&LFJE 

0 

/sx ) 

CALIBRATtOM SOtJKCK EggBftENCE 

Comments. 

Performed by:*. Date: Time; 

JB Place : ^"""^^ _ 

CM.SHEET.WTJB . AFieltpor Shop) 
LOOP: 

DESCF.IPON: 

SERVICE: 

LOCATION: 

LP-SHT:' 

P&ID: 3031 

REMARKS r 

INSTL-RMKS: 

SPEC-RMKS: 

S/J5T: 

TViT mSTRUMENT CALIBRATION RECORD 

UNIT #2 

QUARTERLY 

210 

WEIGHT TRANSMITTER 

SOLID CHARG CORV. 

MMTOFACT: TOLEDO 

MODT3L: 8140 

SCALE: 0-400 # 

CALIB-Itf:.0-400 # 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 0#=819 et a 

lUST-SP: 2 0D#-24S7 fits 

ACTION": 1#-8.19 ctf j 

I/O MJHBEE: 30070 

CALIBRATION NOTES 

Check scale , digita l Calibration , per . Toledo instructions . 

Then wit h no weight on scal e adjus t analo g zero . (MOTE: HMi 

wil l not displa y numbers les s than, zero ) r Kext add weight 

= t o 10% are more o f scale s range, then, adjus t analo g span; 

t o indicat e weight on scale , as rea d on HMI screen . 

See Manufactures literatur e £or detaile d instructions . 

Pil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

o 

so 

INSTRUMENT READING 

Before Calibration £*j 

Afte r Calibration 

CALIBRATION SOORCE REFERENCE 

Comments: 

Perforated b y .^^ T j^jj ^ Date =/d-/^0 ? Time: 7J)^ AM7S 

JB 

CALSHBET.WDB 

Place : 

QFlelS^or Shop) 
TAG 

LOOP 

DHSCRIPOM 

SERVICE 

LOCATION 

LP-SHT 

P&ID 

REMARKS 

INSTL-RKKS 

SPEC-RMKS 

S/H. 

TWI rjtKSTJtUMEHT CALIBRATION RKCOKD 

OWIT #2 

QUAJiTEKLY 

PDT 

2 S0 

PERSfJiTRE! rUFP . TRANSMITTE 

B-^HOUSE INLET/OUTLET 

FIELD 

203 5 

MANumCT; YOKOGAWA • 

MODEL: 

SCALE: 0-15 i n wc 

CALIB-IH: 

CALIB-OX3T: 4-20 'MLA 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

CALIBRATION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETHR AHD LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e fo r detaile d instructions . 

Pil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPtfT TZALUE 

if 

ITISTKDKESTT READING 

0 w x 

Before Calibration 

)<r " W.C . 

O After Calibration 

IT 

CALIBRATION SOUP.CZ REFERENCE 

ComErients: 

Performed by: 

JB 

CSLSHSET.WD3 

Place : 

'Held ojr Shop) 
TAG; 

LOOP; 

' DESCRIKM: 

SERVICS: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS; 

INSTL-EMK3 t 

SPEC-RMKS: 

S/UT; 

THI INSTRUMENT CALIBRATION RECORD 

UH±T #2 

QUARTERLY 

PT 

200 

PRESSURE TRANSMITTER 

LOW CHAMBER 

FIELD 

2032 

MANTUFACT 

MODEL 

' SCALE 

CALIB-IN 

CALIB-OUT 

PROCESS-SP 

USST-SP 

ACTIQKf 

I/O.NUMBER 

-7.5 t o +2.5 in . wc, 

4-20 MA 

CALIBRATION NOTES 

Coruiact transmitte r to' bs calibrate d t o pressur e sourc e and 

calibrate d referenc e (Manometer), inpu t appropriat e pressur e 

and verif y wit h curren t meter ^ 

See Manufactures literatur e fo r detaile d instruction s 

Pil l ou t and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

J.fcifUT 'VALUEINSTRUMEN T READING 

-tf Before Calibration , r _ , 

After Calibration 

2 . S 

ft 

2 0 . Q y» A 

CALIBRATION SOURCE REFERENCE 

Comments:' 

Performed by: 

JB 

CALSHEET.vTOB 

. Date •J0-22'0Cj Time: 'Z-OO AM fPM 

Place : 

(Field os^Shopy 
' TW1 INSTRUMENT (^ALTERATION RECCED 

UNIT #2 

QUARTERLY 

TAG: PT 

,#><*,. • LOOP: 219 

r • ' HESCRIPONr" PRESSURE TRANSMITTER 

SERVICE; UPPER CHAMBER 

LOCATION: FIELD 

LP-SHT: 

PSID: 3033 

REMARKS: 

INSTL-RMKS: 

' SPEC-RMS: 

S/N: 

MANUFACT: 

MODEL: 

SCALE; 

CALIB-1N: 

CALIB-OUT: 

PROCESS-SP: 

1NST-SP: 

ACTION: 

I/O NUMBER; 

-7.5 t o +2,5 in . wc. 

4-20 MA 

CALXBRATTON NOTES 

Connect transmitte r t o be calibrate d t o pressur e sourc e and 

calibrate d referenc e (Manometer), inpu t appropriat e pressur e 

and verif y with, curren t meter. 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READ1KG 

I S " 

Afte r Calibration 

Z,S " zo. o 

CALIBRATION SOURCE REFERENCE 

Comments: 

if • i 

Performed by 

JH 

CALSHEET.TOB 

_ Date: fo-ZZ'D^ Time: Z'fT AMfpwL 

Place : 

fFiel d oifSlxopf 
TpJI INSTRTJMKNT CfiLTBEATIOIT RECORD 

TAG; 

LOOP: 

DESCRIPON; 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-EMtCS; 

SPEC-RMKS: 

S/E: 

UNIT #2 

QUARTERLY 

AT 

2 89 

OXYGEN 

STACK GAS 

STACK 

203 5 

ANALYSER 

MANUFACT: 

MODEL: 

• SCALE: 

CALEB-IN: 

CAHB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

COSA 

0-25% 

0-25% 

4-20 MADC 

CALIBRATION IK3TES 

Flow calibratio n gas a t 2-3 psi g and 3 scf h 

See Manufactures literatur e fo r detaile d instructions . 

Fil l ou t and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPOT VAL0EIHSTROMSN T READING 

•rj ^ Before Calibration ^ <~\ 

6< O £• a 

2Us " 20- H 

^ q Afte r Calibration ^ ^ 

. CALIBRATION SOURCE REFERENCE 

ZERO GAS CYL #:' CCilf.TS S 

SPAN GAS CYL #:_ 

Comments: 

Performed by 

JB 

CALSHEST.WDB 

3Date:Mri^ l Time: /( I !op/$) P M 

Place : ^ — 

or Shop} 
TWI ItfSTKDMEHT CALIQEBTTOKr RECORD 

UNIT #2 

QTMRTERLX 

TAG: AT 

LOOP: 28SB 

• DESCRIPOW: HC MANOEACT: Thermo E.lec.co, 

SERVICE: STACK GAS ANALYZER MODEL: SIC 

LOCATION; STACK SCALE: 0-100 PPM 

LP-SHT: 556 CALIB-Ilf: 

PfilD: CALIB-OUT: 4-20 MSEC 

REMARKS: PROCilS S - S P: 

12JSTL-KMKS: . INST-SP: 

SPEC-KMKS: 'ACTIOS: 

S/H: 630 On MCS 100 I/O UuMBER:' 

CAL IBRATlOlf NOTES 

1) Open sample gas bottl e valves . 

2} Pres s MENU Butto n 

3) Pres s CALIBRATION 

4} Pres s ZERO.ADJUST 

5} Pres s SPAH ADJUST a£ter 4)finishe d 

6) Pres s RUN afte r 5)finishe d 

7) Clos e sample gas bottles . 

See Manufactures literatur e fo r detaile d instructions . 

' Fil l out and affi x a new calibratio n sticker . 

D.l lb/hr . 

CALIBRATION REPORT 

INPUT • VALUE INSTRUMENT. • READING • • • 

q Before Ca.libjrs.tion 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

GAS CYL #: 

Cotnments:' 

Performed Date : Time : °' ^ f AM) PM 

JB • Place: : 

CAL SHEET. WDB ((Field hr Shop) 
TWT INSTRUMENT CALIBRATION RECORD 

um.T #2-

QUARTERLY 

TAG: AT 

LOOP: 2SBB 

•• DESCRIPOH: OPACITY 

SERVICE: STACK GAS 

LOCATION: STACK 

LP-SET: 

P&ED : 

REMARKS': 

IBfSTL-RMKS: 

'SPBC-RMKS: 2.QG t o 5.70ma 

S/H: 

MAMTF ACT: TELEDYNE INST. 

MODEL: -LightHawk 5 6 ODI 

SCALE: 0-100% 

CALEB-IN; 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O SOMBER: 

CALIBRATION NOTES 

Clea n windows 

See Manufacture s literatur e fo r detaile d instructions . 

Pil l ou t and affi x a new calibratio n sticker , 

o . l lb/h r 

CALIBRATION REPORT 

USrpUT VALUE 

Sefar e Calibratio n 

INSTRUMENT READIKTG' 

After Calibratio n 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed by: C-Wck J±dw&.(£$S Date: iCh^-O^ Time: 

iTB 

CALSHEET.WDB 

Place: . 

fiel d Tpr Shop) 
TNI INSTRUMENT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

TAG: TT 

LOOP: 20DA 

DESCRIPOJJ: PLC THERMOCOUPLE INPUT 

SERVICE: LOWER CHAMBER 

LOCATION; FIELD 

LP-SHT: 

P&ID: 

REMARKS; 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

203 2 

MAM)ETACT; 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP: 

INST-8P: 

ACTION: 

I/O NUMBER: 

MODICON 

B883-200 

0-2500 deg. F, 

TYPE K 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a typ e K temperature signa l of 50 0 deg F. and 2,000 

deg.F. a t inpu t of PLC, the n verif y thi s singl e on th e 

contro l pane l CRT. 

Ses Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker , 

0.1 Lb/hr 

CALIBRATION RKPQRT 

INPUT VALUE'INSTRUMEN T READ IMS 

C—j^^o Before Ca.libra.tion ^ .c 500 H 60I 

ZOoO a F • . 2s)oQ& 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comment s: )U o Calibrato r neeta^of . 

Performe d by; I^V -T , f>*JX 0 Date: //-/fl-ff i Time: 2jZS ^,(g) , 

JB Place : 

CALSHEET.Wffi [Field hr Shoo} 
THI INSTRTMKNT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

TAG: TT 

LOOP: 200B 

• DESCRIPON: PLC THERMOCOUPLE INPUT MAITOFACT: MODICON 

SERVICE: LOWER CHAMBER MOLEL: B883-200. 

LOCATION: FIELl i SCALE: 0-2500 deg. F. 

LP-SHT: CALIB-IN: TYPE K 

P&ID: 2032 CALIB-OUT: 

REMARKS: PROCESS-SP: 

INSTL-EMKS: IHST-SP: 

SPEC-RMKS: • ACTION: 

S/N: I/O HOMSER: 

Cfl LIBERATION NOTES 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l of 500 dag F. and 2,000 

deg.P. a t inpu t o f PLC, the n -verif y thi s singl e on the 

contro l pane l CRT. 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1- lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READINO. 

r~y-\,-\& r ~ Before Calibratio n <r~>\^.0 

6 O O H 5OO 

7^00O° F • ZtiQQ* 

After Ca.libra.tiou 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed by:. Date:. _AM /PM J 

. 

JB Place : 

CALSHEET.WDB ( (Field) Or Shop) 
TAG: 

LOOP; 

' DESCKJPOKf: 

SERVICE?: 

LOCATION: 

LP-SHT: 

P&ID : 

REMARKS: 

IttfSTL-RMKS :• 

SPEC-RMKS: 

3/N: 

TWI INSXRUWEHT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

TT 

219A 

PLC THERMOCOUPLE INPUT 

UPPER CHAMBER 

FIELD 

203 3 

MANUPACT: MODICON 

MODEL: 

SCALE: 0-2500 deg. 

CALIB-IN: TYPE K 

CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

P. 

CALIBRATION NOTES 

Use cold, junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l o f 500 deg P. and 2,000 

deg.F. a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUEINSTRUMEN T READING • 

r~ Before Calibration f ^ v . f ) 

O DO }- .SC O 

2,iOc)0Q F Zooo° 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: Li o coL\\htaAi9f\ needed, 

Performe d by:. DateTims : 

JB Place : 

CALSHEET.HDB <(Field)or Shop) 
TAG: 

LOOP: 

•' DESCRIPON: 

SERVICE: 

LOCATION; 

LP-SHT: 

P&ID : 

REMARKS: 

IBFHTL-RHKS: 

SPEC-RMKS: 

S/H: 

T BI INSTRUMENT CALIBRATION RECORD 

USUT #2 

ANNUAL 

TT 

21SB 

PLC THERMOCOUPLE INPUT MANUFACT: MODICON 

UPPER CHAMBER 

FIELD 

2033 

MANUFACT 

MODEL 

SCALE 

CALl'B- II? 

CALIB-OUT 

PROCESSES? 

LNST-SP 

ACTlOlf; 

I/O NUMBER: 

0-2500 deg, 

TYPE K 

CALIBRATTON NOTES 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a'type K temperature signa l o f 500 <3eg F. and 2,000 

deg.F. a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT, 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

o j — Before Calibration ^.o 

•SQQ F S~oo 

ZOC6 ° 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Comments: 

ov, g>^jT T p a t e : Performe d ll-IQ-m^,2^n_^(Q \ 

J B 

CALSHEET.HDB 

Plac e r. 

fFieldSor Shop) 
n • 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

TAG; TT . 

LOOP: 7,21 

DfiSCRIPON: PLC THERMOCOUPLE INPUT 

SERVICE: SPA IMLET 

LOCATION: FIELD 

LP-SHT: 

2 033 

MANUFACT: MODICON 

MODEL 

P&1D: 

REMARKS: 

IJffSTL-EMKS : 

SPEC-RMKS: 

S/N: 

SCALE 

CAL1B-IN 

CALIB-OUT 

PROCESS-SP 

INST-SP 

ACTION 

I/O NUMBER 

0-2500 deg. 

TYPE K 

CALIBRATION NOTES 

U se col d junctiorj , compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l o f 500 deg P. and 2,000 

' deg.F. a t inpu t o f PLC, then verif y thi s singl e on the 

contro l pane l CRT. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker , 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE 

SOQ°f 

Zooo0 fINSTRUMENT • -READINGBefore Calibration . a 

.. _ S Oi 

ZPO 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: Kin Co 11 io Vo^to v\ needed, 

Performed.by y l/Jsis Date: Time: 

JB 

CALSHEBT.WDB 

Place ; 
TAG: 

LOOP; 

DESCRIPOH: 

SERVICE: 

LOCATION; 

LP-SHT 

P£ID 

REMARKS 

INSTL-RMKS 

SPEC-RMKS 

S/N 

TWI IHSTRUMENT CALIBRATION RECQP.U 

UNIT #2 

ANNUAL 

TT 

270 

PLC THERMOCOUPLE INPUT MANUFACT: MODICON 

SDA OUTLET 

FIELD 

2034 

MANUFACT 

MODEL 

SCALE 

CALIB-IK 

CALIB-OUT 

PROCESS-SP 

INST-SP 

ACTION 

I/O NUMBER 

0-2S00 deg. F, 

TYPE K 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l of 500 deg F. and 2,000 

deg.F, a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT. 

Sea Manufacture s literatur e fo r detaile d instructions . 

Fil l ou t and affix- a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUEINST&U&EN T READING 

C^QQ° p i Before Calibration ^DO^ 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed bv: -f?^—^T^ ^^~-J^9 Date: ff-fd-O^j Time: "2J 3S^fpM ^ 

JB Place : 

CALSBEET.WDB (fFieldjor Shop} 
TAG: 

LOOP: 

' DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&IDr 

REMARKS: 

INSTL-SMKS: 

SP2C-RMKS: 

S/N: 

TW.T n^TRl^ENT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

ET 

STACK FLCW TRANSMITTER 

STACK 

FIELD 

2035 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUT:' 

PROCESS-SP: 

INST-SP: 

ACTIOU; 

I/O NUMBER: 

Rosemount 

Q-?.u,0OD ACFM 

4-20 MALC 

S et Damp/pot t o mid poin t 

CALIBRATION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH INCLINE MANOMETER MD 

LOOP CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT 

WITH LOOP CALIBRATOR. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/b r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT REABING 

Q

if . , ... Before Calibration "j> <r^ ^ a 

• r^tr Afte r Calibratio n , . „ , D HO *A 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: Data : Time: 

iTB Place : ^^^^"x . 

CALS HEET. VfDB /^ieldjs r Shop) 
TAG: 

LOOP: 

DESCR.IPON; 

SERVICE: 

LOCATION; 

LP-SET: 

P&ID: 

REMARKS: 

INSTL-EMKS: 

SPEC-HMKS : 

S/N: 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #2 

ANNUAL 

Jj'T 

215 

PLOW TRANSMITTER 

HIGH BTU 

FLD 

2031 

Changed Range 11/12/96 

SENSITIVITY 5.58 

SW 1,2,3,4, OFF 

97153 

• MANUFACT: 

MODEL: 

SCALE: 

CALIB-LM: 

CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

.ACTION: 

I/O NUMBER: 

MICRO MOTION 

D 40S-SS 

0-360Q lb/h r 

4-20 MADC 

CALIBRATION NOTES 

Flus h process piping , connect water hose t o upstream sid e o f 

flo w meter, se t contro l system t o appropriat e rat s control f 

and rea d totalizer , flo w wate r int o a containe r and compare 

t he toltalize r readin g t o th e measured amount i n container . 

See Manufacture s literatur e fo r detaile d instructions , 

Fil l out and affix : a new calibratio n sticker . 

0.1 lb/h r • 

CALIBRATION REPORT 

INDTJT VALUEINSTRUMEN T READING 

i / \ .) , o Before Calibration Q Q cr ii * IO rnirx. Vor . /,7-b lbs, 

After Calibration 

CALIBRATION SOURCE RE-FBRSNCEComments: IV)ft ii b x&how nP&rJeat 

Performe d by 

JB 

CALSHBET.WDB 

_ pate : H-l^-O*} Time:_^3 d mfw? 

Plac e 

'{Fieldjor Shop) 
TAG; 

LOOP: 

•' BEISCRIPOW: 

SERVICE: 

LOCATION: 

LP-BSTi 

' P&IO: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

TWI INSTRUMENT' CALIBRATION RECORD 

UNIT #2 

ANNUAL 

FT 

216 

FLOW TRANSMITTER 

LOW BTU 

FLD 

2031 

Changed Range 11/12/96 

SENSITIVITY 5.1(5 

SW 1,3,4, OFF 

32936 

MANUFACT: MICRO MOTION 

MODEL; D 40S-SS 

SCALE: 0-3600 lb/h r 

CALIB-IN: 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION; 

I/O NUMBER; 

CAL IBRATION NOTES 

Plus h proces s piping , connect water hose t o upstream sid e of 

flo w meter, se t control - system t o appropriat e rat e control , 

a nd rea d totalizer , flo w ttater int o a containe r and compare 

t h e tolcalipe r readin g t o th e measured amount i n container , 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT 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 

CALIBRATION SOURCE REFERENCE 

Comments: hlo r/> l\Lr&i^ fivedecfPerforme d by: Date: IZ-I^-Q^? Time: ZGO AM 

JB Place : 

CALSHEET„WDB ({Field)or Shop) 
TBI INSTRUMENT CALIBRATION RECORD 

UNIT #2 

ANNUALTAG: FT 

LOOP: 288 

• DESCRIPON: FLOW 

SERVICE: LIME 

LOCATION: FIELD 

LP-SET: 

P&.TJD: 2034 

REMARKS: 

INSTL-RMKS: 

SPEC-RMS : 

S/N: 

TRANSMITTER 

SLURRY TO HEAD TANK 

•MANDEACT 

MODEL 

SCALE 

CALIE-IN 

CALLS-OUT 

PROCESS-SP 

INST-SP 

ACTION 

I/O NUMBER 

E-H 

0-20 GPM 

4-20 MADC 

CALIBRATION NOTES 

Flus h proces s piping , connect wate r hose to upstream sid e o f 

flo w meter. Set contro l syste m t o appropriat e contro l rate , 

a nd rea d totalizer , flo w wate r int o a containe r and compare 

t h e toltaliee r readin g t o th e measured amount i n container . 

See Manufactures literatur e fo r detaile d instructions , 

Fil l out and affi x a new calibratio n sticker . 

0,1 lb/h r > 

CALIBRATION REPORT 

INPUT VALUEINSTRUMEN T READING 

i ^— re ^ Before Calibration ( c— \i 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performe d by:. h^C.&j Qj2) Date; jHfi l TimeJ- ^ TMf&) 

J"B Place:„_ 

CALSHEET.WDB (Fiel d lo r Shop) 
MM J<?dm*d Ct - St Lncfe, MO S^T25 

tiuiJiieas: {31 i) a 45-7773 . Hax: {314) aiS-?/79 

Seal s Inspection Report 

(JirstMBi- ONYX ENVIRONMENTAL 

#7 MOBILE AVENUE 

SAUGET, IL 62201 

Location: Direct injection 

MF03-/ Mfjaol; WH30 

ScaieTypc: VEHICi.F. 

Capacity; 6pnDU"LB 

ascription; Glass HI L 

Serial No; 011150 

Seals No: 2 

Divisions: 5L3 • 

Scale Was torrid ill Tolerance: X yes 

Shift lost 

Slffes / Comsrs / Weights 

Appled 

Scalu Reading 

(As found) 

Ejror (+/-) Tcferance 

Jdali ilunanqe 

Hcala Read inJj After 

AdiuEimant (As Uff) ' 

Amept,1 

Reject 

Sectipr- 1 21,000 li) 40 lb 4 / - 45 l b ACCEPT 

21,000 lis 51,000 J.b 40 l b 45 l b ACCEPT 

^szticn J 21,iK;o l b 31,D00 Lb 40 16" 4 / - 45 l b ACCEPT 

flection 4 31,00 0 l b 21,0D0 l b t o ' l b 4 / - 45 Lb 

Settim i Is 31,DOC l b 21,ODD l b 4U IP 4 / - 45 113 . AC03Fr""' 

Sectio n f> 21j000 U i 21,005 l b 45 l b 4/- . 45 .ih 7iCCEPT 

BuSdup Ws&jht Wsirjnls Applied Seals R&adjiig 

(A3 found) 

Tolersnu? 

M-jInttrwnos 

Scab Reaiing Aftsr 

Adjustment {A* Left} 

3,0GD l b 3,000 l b + D l b 10 l b ACCSPT 

e,ooo l b e,ooo l b +0 l b 47- l ^ l b A'JCUP'l 

SjOoo l b i>p0CD l b + 0 l b 4 / - 20 ,Lb A'JCBPI 

12rO0O l b L3rQCD Is 4-0 l b f/- 5.5 ]b SCCEF'f " 

15,000 l b - • l5,oo o l b •[•o l b 

4 / - 3 0 ID 

ACCEPT 

IB, ODD i b lfl,00G lb +0 l b +/- 4a Oh ACCIsP? 

ElEctioii 4 IX,CQD l b 21, OQS l b 45 lh *•(*• 4S l b 

T€StPrL>cEdUTefollcnvsQ5POO9-O0l/0DZ NIST#; MO: 235833/2532.50 3958B OB5rj4-02SB/D34)450 2749S9 

Rfce Lake: 622/266926^02 822/272331-0.5 322/274031-06 _ „ / . 

CalDate: 11/09/2003 NextOMdya: 90 Days 

Service Technician Registration #: 0524-M 

. Calibrated By S&rvlca TschnEcian: Jim Koejkenmeier 

Calibration Dates: JAN APR JUL Oc t 

Job Qjj&ueS: LT217651 Ropcrt ID: SflB333SS 

Uncertainty of Measurcmant provided on request 

FQR CUSTOMER USE ONLY t 

. Reviewed By. . Dale Reviewed ,„ 

This flQ3unlcni *h=JI nal be rrpraijccd, ratspl ill Tall WEtt&Ul lilB Sppsovpl cf flczuralz SLjpcrin-Srfc Cntfpsnf.. 

PSjelCfl RmOJE , Hun 1F, DBMeMS 
B-1 WEEKLY UNIT#2 

COMPLIANCE CHEC K SHEET 

(CMSTask IC4D39) RAGt£ 1 OH 2 

OPERATING PARAMETERS P LC COIL BW COIL 

'1 OCL ' TRV POSITION (OPEN) 01602 00401 

2 OCL UPPE R CHAMBER TEMP. 1 min avrj. 00402 

3 OCL HI BTU lbs/hr Max 0161)4 00403 

4 OCL LOWE R CHAMBER TEMP. 1 itiin avg. 01605 00404 

S OCL LO BTU lbs/hr Max 01SD6 00405 

e OCL . FLUE GAS HCL, 1 hr. rolling avg. 016D7 00406 

7 ' OCI. FLUE GAS CO , 1 hr, rolling avg. 01600 00407 

a OCL FLUE GAS OPACITY, high."for 4SD swc./hr. avg. 01609 004O6 

9 OCL FLUE GAS OPACITY, high instantaneous 01B10 00408 

10 OCL FLUE GAS FLOW RATE, high 1 min. avg 01B11 00410 

11 OCL HEAT INPUT high mbiu/rir 01 El 3 00411 

12 OCL CHLORINE INPUT, high lbs/hr 01014 00412 

1-3 OCL SOLIO FEED , high lbs/hr Max. 01526 00413 

14 OCL UPPE R CHAMBER TEMP- low 1 hr rolling avg. 01538 00414 

15 OCL SPECIALITY FEEDEO high lbs/hr Max. 0151S 00415 

17 AWFC SDA-OUTLET'i'HMF. highl min, avg. 01591 00417 

18 AWFC B AG HOUSE DIFT.PR. DROP. Low 1 min. avg. 01593 00418 

19 AWFC FLUE GAS CO , high 1 min. avg. 01594 0041S 

20 AWF C FLUE. GAS 02 , low 1 min. avg. 01596 00420 

21 AWFC FLUE. GAS HC, high 1 min. avg. 01597 00421 

2 2 AWF C FLU E GAS HCL, high 1 min. avg. 0159S 00422 

23 AWF C FLU E GAS FLOW RATE, high tost. 01599 DD423 

24 AWFC FLU E GAS OPACITY, high 1 min, avg. 01501 00424 

%. i "AWFC " ''' LO W 'CHAJTOTSRTElVfP'.V low' 1' ti r'/ g vg, 01586'."'" • 00425' 

.) AWFC LOWER CHANCER P RESS, high for 5 sees. 01583 00426 

AWFC UPPE R CHAMBER PRESS , high for 5 sees. 01569 00427 

ze AWFC FASLER OF PROCES S MONITOR 01527 00428 

29 AWF C ID FAN FAILURE or high high vibration for 5 min. 01625 00429 

30 AWFC Upper or Lower Chamber Temp, high OfSOO 00430 

32 MWFC A L L WASTE FEED OF F FRO M FIX (manually shut off) 01740 00432 

35 MWFC . FLUE GAS HCL, high 1 mid, avg. 01592 00435 

36 MWFC HEAT INPUT high anticipated 01622 00436 

37 MWFC CHLORINE INPUT, high lbs/hr 01623 00437 

38 MWF C . E-STOPS or T/C MODULE inactive 01615 00433 

39 MWFC FLU E GAS CO , high 1 hr. avg. 01595 00439 

40 MWFC ATOMIZER high high vibration for 5 sec. 01624 00440 

41 •SWFC SPEC . FEED lbs/hr high 01576 00441 

PASS 

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' BIWEEKLY UNIT#2 

COMPLIANCE Cf IFCK SHEET 

{CMS Task JC403G) PAGE 2 O F 2 

OPERATING PARAMETERS PLC COIL BWCG1L PASS FAIL 

42 SWFC HJBTU Ibs/hrriigri. 01578 00442 

4 3 SWFC LOm u \b$!hr high 01580 00443 

40 SWFC HI BTU loss of srynal 03019 OQ445 

46 SWF C LOBTU loss of signal 03020 00446 

47 SWFC SPECIALITY FEED/COMPRESSED GAS FEED Eoss of signal 03021 00447 

4 5 MWFC NORTH £ SOUTH IPS ALARMS FAILED 05703 0044S 

49 SWF C UPPE R CHAMBER SECONDAR Y FUEL loss of signal 03022 00440 

50 MWFC NORTH & SOUTH IPS SERVER5FAILED C570S OO450 

51 SWF C DIRECT INJECT (common alarm) 03132 004S1 

52 OPL Bag Leak Detection System (THbo) 

'65 • P L Pumpable 1 Hour Rolling Total OPL 06205 04113 

ee OPL Non-Pumpable 1 Hour Rolling Total OP L ceaos 04114 

67 OPL . Total wa.s£e 1 Hour Rolling Tote! OPL 08208 04115 

6 3 O PL CL1 2 Hour RoKfng Total OPL 0B211 04116 

6 0 OPL Low Volatile 12 Hour Rolling Total OP L 08214 04117 

70 OPL Semi Volatile 12 Hour Rolling Totai OPL 08216 0411ft 

71 OPL Mercury 12 Hour Roiling Totai OPL 03216 04110 

72 OPL A sh 12 Hour Roiling Totai OPL OS220 04120 

7 3 O PL P C C Temperature 1 Hour Rolling1 Average Low OPL 08222 04121 

7 4 OPL S C C Temperature 1 Hour Rolling Average Low OPL 0B224 04122 

7 5 OPL SDA Outlet Temperature 1 Hour Roiling Average High OPL 09226 04123 

7 6 O PL Baghouse DrfFerenlial Pressure 1 Minute Average Low OPL 08227 04124 

77 O PL Baghouse DfffensriUal Pressure 1 Minute Average High OPL 08226 04125 

•;-'fv" 'OPL Sf acR' HCT. Cofrecto'fl'T 'Hour Rolling 'Average 'High OP L •-08232 04125 • 

O P L Stack C O Corrected 1 Hour Roiling Average High OP L 0S236 04127 

s o OPL Stack Flow 1 Hour Rolling Average High OPL 08244 0412S 

S1 O PL BTU 1 Hour Total OPL 08209 04129 

82 O PL HrtCI/Hra Lime Flow 1 Minute Average High OPL 08251 04130 

63 AWF C Lime Slurry Density 1 Hour Rolling Average Low 08156 04132 

64 WILL NOT ACCEPT SOLID CHARGES >750 KBTU/ChlARGE 

85 Hi/D! Atomtang' flit Low pressure alarm (Manual Check) 

BS Lo/D! Atomizing Afr Low pressure alarm (Manual Check) 

87 Specialty Feeder Atomizing Air Low Pressure alarm (Manual check) 

OCL -CONDFTiON LIMIT 

AWF C ' -AUTOMATIC WASTE FEED CUTOFF 

MWFC =MlSC WASTE FEED CUTOFF 

SWFC ^SPECIFIC WASTE FEE D CUTOFF 

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Comments 

CHECKE D BY : ""TTj ^ 

.^PROVED : j/fajLor . 

££KLY_2 

4/4/07 HK 

DATE: }0-1 y^- O 1 TIME : 

PLACE : Control Room 

A M tP M 
' BIWEEKLY UN FT #2 

COMPLIANCE CJ jfSCK 5! 1EI=T 

•[CMS Task iMfflrj) PAGE 1 OF 2 

OPERATING PARAMETERS PLC COIL eWCOJL 

i OCL T RV POSITION (OPEN) 01602 004 01 

2 OCL UPPER CHAMBER TEMP. 1 min avg. 01K03 00402 

3 OCL . HI BTU Ibsf fir Max 01604 00403 

4 OCL LOWER Ci 1AMBERTEMP. 1 min avtj. 01605 00404 

5 OCL LO BTU ibs/hr Max 01606 00405 

6 OCL , FLUE GA S HCL, 1 hr. rolling avg. 01607 00406 

7 OCL FLUE GAS CO, 1 hr. rolling gvg. 01608 00407 

8 OCL FLUE OAS OPACITY, high fcr4S0 sec./hr. avg. 01609 D04D8 

•9- O CL FLUE GA S OPACITY, high instantaneous 01G10 00409 

10 O C L FLUE GA S FLOW RATE, high 1 min. avg 01611 00410 

11 OCL HEAT INPUT high mbtu/hr 01613 00411 

12 OCL CHLORINH INPUT, high lbs/hr 01614 00412 

13 O CL SOLtD FEED , high Ibs/hr Max, 01526 • 00413 

14 O CL UPPER CHAMBER TEMP, low 1 hr rolling avg. 01536 00414 

15 OCL SPECIALITY FEEDED high lbs/hr Max. 01516 00415 

17 AWF C SDA-OUTLET TEMP, highl min. gvg. 01591 0Q417 

1B AWF C B AG HOUS E DIFF.PR. DROP. Low 1 min. avg. 01593 00413 

19 AWF C FLUE GAS CO r high 1 min, avg. 01594 00419 

20 AWF C FLUE GA S 02 , low 1 min. avg. G15S6 00420 

21 AWF C FLU E GAS HC, high 1 min. avg. D1597 . 00421 

22 AWF C FLU E GAS HCL, high 1 min. airg. 01596 G0422 

23 AWF C FLUE GAS FLOWRATE, high irist. 01599 0D423 

24 AWF C FLUE GAS OPACITY, high 1 min, aivg. 01601 00424 

..AWFC-.- ..AWFC-.- 01-56S 00425 •• 

AWF C LOWER CHAMBER PRESS, high for 5 sees. • 01538 00426 

_7- AWF C UPPE R CHAMBER PRESS, high for 5 sees. 01539 D0427 

25 AWF C FAfLER OF PROCES S MONITOR 01527 00426 

29 AWF C (D FAN FAfLURE ar high high vibration for 6 min. D1625 00429 

30 AWF C Upper or Lower Chamber Temp, high 01600 00430 

32 •MWFC A LL WASTE FTiFO OF F FROM FIX {trtanuaHy shot off) O1740 00432 

35 MWFC FLUE GAS HCL, high 1 min. avg. 01592 00435 

36 MWFC HEAT INPUT high anticipated 01622 00436 

37 MWF C CHLORINE INPUT, high lbs/hr 01623 00437 

38 MWF C E-STOPS or TIC MODULE iracSve 01615 • 00438 

39 MWF C FLUE GAS CO , high 1 hr.avg. 01595 00439 

40 MWFC ATOMIZER high high vibration for 5 se t 01624 00440 

41 SWF C SPEC . FEED ibs/hr high 01576 00441 

PASS 

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BIWEEKLY UNIT1K2 (CMS Task !C4Q39) PACE 2 O F 2 

COMPLIANCE CHEC K SI iEFT 

y OPERATING PARAMETERS P LC COIL 0W COIL PASS 

42 SWFC HIBTJ rbs/brhigh 01578 00442 

43 SWFC LOBTU lbs/hr high 01580 00443 I -

45 SWFC HI BTU loss of signal 03019 00445 

46 SWFC LOBTU ioss of signa l 03020 00446 J 7. 

47 SWFC SPECfALFTY FEED/COMPRESSED GAS FEED loss of signal 03021 0O447 :/ 43 MWFC NORTH & SOUTH IPS ALARMS FAILED 05703 00448 h 

49 SWFC UPPE R CHAMBER SECONDARY FUEL loss of signal 03022 00449 J50 MWFC NORT H & SOUTH IPS SERVERSFAILED 05705 00450 

51 SWF C DIRECT INJECT (common alarm) 03132 • 00451 

52 OPL Bag Leak Detection System (Tribo) 

65 OPL Pumpable 1 Hour Rolling Total OPL 08205 04113 

./ 

66 OPL Non-Fumpabla 1 Hour Rolling Totai OPL 05200 04114 j 

• 67 OPL Totai waste 1 Hour Rolling Total OPL 0B2OB 04115 / 

• G8 OPL C L 12 Hour Roiling Total OPL 08211 04116 

G9 OPL Low Volatile 12 Hour Rolling Totai OPL 08214 04117 J 

70 OPL Sem i Volatile 12 Hour Roiling Tolai OPL 08216 04118 1 

71 OPL Mercury 12 Hour Rolling Totai OPL 0B216 04119 

72 OPL A s h 12 Hour Rolling Total OPL 06220 04120 J J 

73 OPL P C C Temperature 1 Hour Rolling Average Low OPL 08222 04121 / 

74 OPL S C C Temperature 1 Hour Roiling Average Low OPL 08224 04122 ./: 

75 OPL S D A Outlet Temperature 1 Hour Rolling Average High OPL 0622S ' 04123 j 

76 OPL Baghouse Differential Pressure 1 Minute Average Low OPL 06227 04124 /. . 

77 OPL Baghouse Differsrrfiaf Pressure 1 Minute Average High OPL • 06228 0-1125 

O PL Stack HC L Corrected 1 Hour Rolling Average High OPL 08232 04126 

• • : O PL Stack C O Corrected 1 Hour Rolling Average High OPL 03230' 0412/ 

80 O PL Stack Flow 1 Hour Roiling Average High OPL 08244 04123 

81 OPL BTU 1 Hour Total OPL 03209 D4129 J 

82 OPL Hrt CI/Hra Lime Flow 1 Minute Average High OPL 03251 04f30 J. 

83 AWF C Lime Slurry Density 1 Hour Rolling Average Low 08156 ' 04132 J / 64 WiL L NOT ACCEPT SOLID CHARGES >750 KBTU/CHARGE 

85 Hi/Di Atomizing Air Low pressure alarm (Manual Check) J j . 

ee Lo/DI Atomizing Air Low pressure afanti (Manual Check) / 

67 Specialty Feeder Atomizing Air Low Pressure alarm (Manuaf check) / 

OCL =CONDFT10N LIMIT 

AWFC ^AUTOMATIC WASTE FEED CUTOFF 

MWFC =M!SC WASTE FEED CUTOFF 

SWFC ^SPECIFI C WASTE FEED CUTOFF 

Comments 

CHECKED BY : j/ \ U I$A 

APPROVED : /$b@hz & 

DATE ; /\9 - /O -0? TIME ; /(P : > , £> A M (fy ? 

PLACE : Contro! Room 

; cEKLY_ 2 

4/4/07 HK 
RIVVFFKLY uNrne 

COMPLIANCE CHECK SHEET 

(CMS Task 104039) PAC E 1 OF 2 

OPERATING PARAMETERS P L C COIL B W COIL 

1 OCL mv POSITION (OPEN) 01602 00401 

2 CCI . UPPLiR CHAMBERTtWP- 1 min avg. 01003 00402 

3 . O CL HI UTU Ibs/hr Max 01B04 00403 

4 OCL LOWE R CHAMBER TEMP , 1 min avg. 01605 00404 

. 5 OCL LO BT U lbs/hr Max 0160 8 OO405 

6 OCL FLUE GAS HCL , 1 hr. rolling avg. 01607 0040 6 

7 O CL FLUE GA S CO, 1 hr. rolling avg. 01603 00407 

8 O CL FLUE GA S OPACITY, high for 460 sec./hr. avg. 01609 0040 8 

0 O C L FLUE GAS OPACITY, high instantaneous 01610• 00408 

10 O C L FLU E GAS FLOW HATE, high 1 min. avg •1611 00410 

11 O C L HEA T INPUT high mbfiVhr 01613 00411 

12 O CL CH LOR IME INPUT, high lbs/3 ir 01614 00412 

13 O CL SOLID FEED, high ibs/hr Max. 01526 0041 3 

14 O C L UPPE R CHAMBER Trr-Mp. tow 1 hr rolling avg. 01535 00414 

15 OCL SPECIALITY FEEDED high lbs/hr Max. 01516 00415 

17 AWF C SDA-OUTLrHTTEMP, highl min, avg. 0159 1 00417 

1H AWF C BAG HOUSF J DIFF.PR. DROP. Low 1 min. avg. 01593 00418 

i y , AWF C FLUE GA S CO, high 1 min. avfl. 01594 00419' 

2 0 AWF C FLUE GA S 02, low 1 min. avg. 01596 00420 

21 AWF C FLUE GA S HC, tiign 1 min. av$. 01507 00421 

2 2 AWF C FLUE GA S HCL, high 1 min. avg. 01598 00422 

2 3 AWF C FLUE GA S FLOW RATE, high irist. 01599 DQ42 3 

2 4 AWF C FLUE GA S OPACITY, high 1 min. avg. 01601 •0424 

"\5 AWF C LOW CHAMBER TEMP, , Low 1 hr, avg. 015&S 00425 

AWF C LOWER CHAMBER PRESS, high for 5 sees. • 01583 00426 

2 7 AWF C UPPER. CHAMBER PRESS , high for 5 sees. 01563 00427 

2 3 AWF C FAILER OF PROCESS MONITOR 01.527 00428 

2 S AWF C ID FAN FAILURE or high high vibration for 5 min. 01625 00429 

3D AWF C Upper or Lower Chamber Temp, high 01600 00430 

3 2 MWFC A L L WASTE FEED OF F FROM FIX (iiianuatly shut off) 01740 00432 

3 5 MWFC FLUE GAS HCL, high 1 min, avg. 01592 00435 

3 S MWFC HEAT INPUT high anticipated 0162 2 00436 

3 7 MWFC CHLORINE INPUT, high Ibs/hr 0162 3 00437 

3 8 MWF C _ F,-STQPS orT/C MODULE inactive 01615 • 00433 

39 MWFC ' FLUE GAS CO, high 1 hr. avg. 01595 00439 

AO MWFC ATOMIZER high high vibration for 5 se a 01624 00440 

41 SWF C SPEC . FEED lbs/hr high 01576 00441 

PASS 

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" BJWLEKL Y UNIT #2 [CM S Task IC4039) PAG E 2 O F 2 

COMPUANC^ ^ ^ ; ._ ^ N 

• "•""*'. OPERATING PARAMETERS P LC COIL BW COIL PASS 

"42 SWF C HI BTU Ibsflir high 0157S 00442 y 

43 SWF C LOBTU lbs/hr high 01580 00443 y 

45 SWF C HJBTU loss of signal 03010 0D445 

, y 

46 SWF C LOBTU loss of signal 030ZO 00446 y 

47 SWF C SPECIALITY FEED/COMPRESSED GAS FEED loss of signai 03021 00447 

48 MWF C NORTH & SOUTH IPS ALARMS FAILED '05703 00448 

49 SWF C UPPE R CHAMBER SECONDARY FUEL loss of signal 03022 00449 

50 MWF C NORTH & SOUTH IPS SEWERSFAfLE O 05705 00450 y 

51 SWF C DtRECT INJECT (common alarm) 03132 00451 y 

52 O P L Bag Leak Detection System {Tribo} 

... y, 

05 O F L Ptrmnabfe 1 Hour Raffing Total OPL 08205 04113 / 

GO O P L Non-Pumpable 1 Hour Railing Total OPL 08206 04114 

. y 

67 O P L Total waste 1 Hour Rolling Total OPL 082O3 04115 y 

68 O P L CL 12 Hour Rolling Total OPL 08211 0411S y 

69 O P L Low Volatile 12 Hour Rolling Total OPL 08214 04117 y 

70 O P L Seini Volatile 12 Hour Railing Total OPL 0B215 04118 ,y 

71 OPl . Mercury 12 Hour Roiling Total OPL 0&21B 04119 

72 O P L Ash 12 Hour Roiiing Total OPL 08220 04120 

73 O P L P C C Temperature 1 Hour Rolling Average Low OPL 08222 04121 y 

74 O P L S C C Temperature 1 Hour Rolling Average Low OPL 08224 04122 y 

75 O P L SDA Outlet Temperature 1 Hour Roiling Average High OPL 03226 04123 ^ 

76 O P L Baghouse Differential Pressure 1 Minute Average Low OPL 08227 04124 y 

.77 O P L Baghouse Differential Pressure 1 Minute Average High OPL 08228 04125 y 

% O P L Stack HCL Corrected 1 Hour Rolling Average High OPL 06232 04126 Z, 

I O P L Stack C O Corrected 1 Hour Roiling Average High OPL 08236 04127 y 

80 O P L Stack Raw 1 Hour Rolling Average High OPl, 08244 04123 y 

81 O P L BTU 1 .HourTotal OPL 08209 04129 

. ,y 

82 O P L Hrt Cl/Hra-Lime Flow 1 Minute Average High OFL 08251 04130 

83 AWF C • m e Sluiry Pensify 1 Hour Rolling Average LOW 03156 04132 y 

34 WILL NOT ACCEP T SOLID CHARGES >750 KBTLL/CHARGE y 

85 Hi/DI Atomiiing Air Low pressure alarm (Manual Check) y 

88 Lo/DI Atomizing Air Low pressure afarrn (Manual Check) 

87 Specialty Feeder Atomizing Air Low Pressure alarm (Manual check) y 

O C L ^CONDITION LIMFT 

AWF C ^AUTOMATIC WASTE FEED CUTOFF 

MWF C =MISC WASTE FEE D CUTOFF 

SWF C ^SPECIFIC WASTE FEED CUTOFF 

Comments 

CHECKE D BY : ^X^sJjPfl DCTEI /M/ H Q ? TIME : <jS> 

^PROVED : j/a&/^ & PLACE : Control Room 

J ,cEKLY_2 

4/4/07 H K 
BIWEEKLY UNIT*! 

COMF1 (ANCE CHEC K SHE ITT 

(CMS Task IC4039) J>AGE 1 OI- 2 

OPERATING PARAMETERS P L C COIL BW COIL 

1 O C L • TRV POSITION (OPFN) 01602 00401 

2 O C L UPPE R CHAMBER T-MJP. 1 min avg. fj-tb'03 00402 

3 O C L Ht BTU lbs/hr Max 01004 00403 

4 O C L LOWER CHAMBER TFMP, 1 min avg. 0160S G04O4 

5 O C L LO BTU lbs/hr Max 01506 0U4D5 

6 O C L FLUE GAS HCL, 1 hr. rolling- avg. 01607 00406 

7 O C L FLUE GAS CO, 1 hr. rolling avg. 01608 O04O7 

3 O C L FLU E GAS OPACITY, high for 480 sec./hr. avg, 01609 00408 

9 O C L FLU E GAS OPACITY, high instantaneous 01610 004O9 

TO O C L FLU E GAS FLOW RATE, high 1 min. avg 01611 00410 

11 O C L HEAT INPUT high mbrjj/hr 01G13 00411 

12 O C L CHLORINE INPUT, high Ibs/hr 01614 00412 

.1-3 O C L SOLID FEED, high )bs/hr Max. 01526 00413 

14 O C L UPPE R CHAMBER TEMP, low 1 hr rolling avg. 01538 00414 

15 O C L SPECIAL! FY FEED ED high ibs/hr Max. 01516 0 W 5 

17 AWF C SDA-OU'f LET TEMP. iiighT mm. avg. 01591 00417 

18 AWF C BAG HOUSE DiFF.PR. DROP. Low 1 min. avg. 01593 00418 

19 AWF C FLUE GAS CO, high 1 min. avg. 01594 00419 

20 AWF C FLUE GAS 02 r lew 1 min- avg. 01S96 00420 

21 AWF C FLUE GAS HC , high 1 min. avg. 01597 00421 

22 AWF C FLUE GAS HCL, high 1 min. avg, •1598 00422 

23 AWF C FLUE GAS FLOW RATE, high Inst 01599 00423 

24 AWF C FLUE GAS OPACITY, high 1 inlrt. avg. 01601 00424 

:5 AWF C • •• LOW'C'HAWERTOT:;'1b w Th r avg; B15B6"'.'"" 00425' 

AWF C LOWER CHAMBER PRESS , high for 6 sees. • 01583 00426 

Z7 AWF C UPPE R CHAMBER PRESS, high for 5 sees. 01589 00427 

2S AWF C FAILER OF PROCES S MONITOR 01527 00428 

29 AWF C ID FAN FAILURE orhrgh high vibraUors for 5 min. 01525 00429 

30 AWF C Uppsr at Lower Chamber Temp, high 01600 00430 

'32 MWF C A L L WAST E FEED OFF FROM FIX (marjuafly shut off] 01740 00432 

35 MWF C FLUE GAS HCL, high 1 min. avg. 01592 00435 

3G MWF C HEAT INPUT high anticipated 01622 00436 

37 MWF C CHLORIME- IMPUT, high Ibs/hr 01623 00437 

33 MWF C E-STOPSor T/C MODULE inactive 01615 • 00438 

3fi MWF C FLUE GAS CO , high 1 hr. avg. 01595 00439 

40 MWF C ATOMEE R high high vibration for 5 se c 01624 00440 

41 SWF C SPEC . FEE D Ibs/hr high 01576 00441 

PASS FAIL 

y 

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BJWEEKLY UNIT #2 

COMPLIANCE CHEC K SJ 0:1 " 

(CM S TasklC4Q39) PAGE 2 OF 2 

OPERATING PARAMETERS PLC COIL BWCOIL 

<\2 

• > 

swrc HFBTU lbs/hr high 01573 00442 

43 SWF C LOBTU lbs/hr high 01580 00443 

43 SWFC hi I BTU loss of signal 03019 00445 

48 'SWF C LOBTU Joss of signal 0307,0 00446 

47 SWF C SPECIALITY FEED/COMPRSSSED GAS FEED loss of signal 03021 00447 

48 MWFC NORTH & SOUTH tPS ALARMS FAILED 05703 00448 

49 SWFC UPPER CHAMBER SECONDARY FUEL loss D f signal 03022 00449 

50 MWFC NORTH & SOUTH fPS SERVERSFAILED 05705 00450 

51 SWF C DIRECT INJECT {common alarm) 03132 00431 

52 O PL Bag Leak Detection System (Tribo) 

65 O R . Pumpable 1 Hour Rolling Total OPL 03205 04113 

66 O F L Non-Puinpablo T Hour Rolling Totai OPL 0320Q 04114 

67 O PL Total waste 1 Hour Rolling Total OP L 0S2QS 04115 

O PL CI. 12 Hour Roiling Total OPL 03211 04116 

6£5 OPL Lcw Volatile 12 Hour Rolling Total OPL 06214 04117 

70 O PL Semi Volatile 12 Hour Rolling Total OPL 08216 04113 

71 OPL Mercury 12 Hour Rolling Total OPL 08213 Q4119 

72 OPL Asil 12 Hour Rolling Total OPL 08220 114120 

73 OPL P C C Temperature 1 Hour Rolling Average Low OPL 08222 04121 

74 OPL S C C Temperature 1 Hour Rolling Average Low OPL 0S224 04122 

75 O PL SDA Outlet Temperature 1 Hour Rolling Average High OPL 0S226 04123 

7G O PL Baghouse Differential Pressure 1 Minute Average Low OPt. 0S227 04124 

77 O PL Baghouse Differential Pressure 1 Minute Average High OPL 06228 04125 

...OPL Slack HC L Corrected 1 Hour Rolling Avorage High OPL 0S232 04123 

•

:OFL Stack C O Corrected 1 Hour Rolling Average High OPL 08236 04127 

BO O PL Stack Flow 1 Hour Roiling Average High OPL 08244 04128 

S1 O PL BTU 1 Hour Total OPL 03209 04129 

S2 O PL HrtCI/Hra Lime Flow 1 Minute Average High OPL 08251 04130 

33 AWF C Lime Slurry Density 1 Hour Rolling Average Low 0S15S 04132 

84 WILL NOT ACCEPT SOLID CHARGES >750 KBTU/CHARGE 

85 Hi/Di Atom izing Air Low pressure alarm (Ma.n ua! Check:) 

86 Lo/DI Atomizing Air Low pressure alarm (Manuai Check) 

87 Specialty Feeder Atomizing Air Law Pressure alarm (Manual check) 

O C L =CONDmON LIMIT 

AWF C -AUTOMATIC WASTE FEED CUTOFF 

MWFC =MISC WASTE FEED CUTOFF 

- SWF C ^SPECIFIC WASTE FEED CUTOFF 

PASS FAIL 

y. 

> 7 

yy 

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Comments 

CHECKE D BY : I -^^L-jQ ^ DATE iO~Z^"'Q^ TIME: ^r3>( 9 fuFh* 

APPROVED : //^g -Z./*. ^ /yChvy PUCE : CohlrolRoom 

t , -:.EKLY_ 2 

4/4707 HK 
(31WEEKLY UNIT £2 (CMS Task iC4030) PAG E 1 OF 2 

COMPLIANCE CHFC K SHEET 

OPERATING PARAMETERS P L C COIL BWCOIL PAS S 

' 1 OCL T R V POSITION (OPEN) 01602 0041)1 / 

2 OCL UPPE R CHAMBER TEMP. 1 min avg. 01603 00402 

3 ' OCL Hi BTU Ibs/hr Max 01604 00403 

4 OCL LOWER CHAMBER TEMP. 1 min avg. 01 SOS 00404 

5 OCL ' LO BTU Ibs/hr Max 0160S 00405 

S OCL FLU E GAS HCL, 1 hr. rolling avg. 01607 00406 y 

7 OCL FLU E GAS CO, 1 hr. rolling avg. 01603 00407 

6 OCL FLU E GAS OPACITY, high for480 sec/fir. avg. 01609 00406 

S3 OCL • FLUE GAS OPACITY, high instantaneous 0161D 00409 __^y_ 

10 OCL FLUE GAS FLOW RATE, high 1 min. avg • 01611 00410 

11 OCL HEAT INPUT high mbfu/fcr 01613 O0411 y 

12 OCL CHLORINE INPUT, high lbs/hr O0412 y 

13 OCL SOU D FEED, high lbs/hr Max. 01528 0D413 y 

14 O CL UPPE R CHAMBER TEMP, low 1 hr roiling avg. 0153a ' • 0D414 y 

15 OCL SPECIALITY FEEDED high Ibs/hr Max. 01516 0FJ415 

17 AWF C S DA OUTLET TEMP, highl min. avg. 01591 00417 

18 AWF C BAG HOUSE DJFF.PR. DROP, Low 1 min. avg. D1593 00418 

19 AWF C FLU E GAS CO, high 1 min, avg. 01594 00419 

20 AWF C FLU E GAS 02 , low 1 min, avg. 01596 00420 

21 AWF C FLU E GAS HC, high 1 min. avg. 01597 00421 y 

12 AWF C FLU E GAS HC L high 1 min. avg. 01598 00422 y 

23 AWF C FLU E GAS FLOW RATE, high irist. 01539 00423 ,y 

24 AWFC FLU E GAS OPACITY, high 1 min. avg. 01601 00424 y. 

'•35 AWF C L OW CHAMBER TEMP., low 1 hr. avg;. 01586 00425 . y 

: -6 AWF C LOWER CHAMBER PRESS, high for 5 sees. 015SB 00420 . 

y 

27 AWF C UPPE R CHAMBER PRESS, high for 5 sees. 01539 00427 

28 AWF C FAILER OF PROCESS MONITOR 01527 0042S - y 

29 AWF C ID FAN FAILURE or high high vibratton for 5 min. 01625 00429 y 

30 AWF C Upper or Lower Chamber Temp, high 0160Q 00430 y 

32 MWFC A L L WASTE FEED OFF FROM FIX (manually shut off) 0174O .00432 

35 MWFC FLU E GAS HCL, high 1 min. avg. 0.1592 0Q435 

3S MWFC HEAT INPUT high anticipated D1622 00436 

37 MWF C CHLORINE INPUT, high Ibeflir 01623 00437 y 

33 MWFC E-STOPS orT/C MODULE inactive 01615 O043.3 

38 MWFC FLUE GAS CO, high 1 hr. avg. 01595 O0439 y 

40 MWFC ATOMIZER high high vibration for 5 sec. 01624 O044O 

y 

41 SWF C SPEC . FEED ibs/hr high 0157S OD441 y 
[31 WEEKLY UNIT #2 

COMPLIANCE CHEC K SHEET 

(CMS Task IC4039) PAG h 2 OP 2 

OPERATING PARAMETERS P LC COIL HW COIL PASS FAIL 

42 

43 

45 

46 

47 

43 

4$ 

50 

51 

52 

65 

6B 

67 

68 

69 

70 

71 

72 

73 

74 

' 75 

73 

,„..7X.. 

-v*.-.l 

'T6 

79 

so 

Bl 

62 

63 

84 

SS 

86 

S7 

SWF C 

SWF C 

SWF C 

SWF C 

SWF C 

MWFC 

SWF C 

MWFC 

SWF C 

OPL 

OPL 

OPL 

OPL 

O PL 

O FL 

O P L 

O PL 

OPL 

OPL 

OPL 

OPL 

OPL 

O P L 

O PL 

O PL 

OPL 

OPL 

OPL 

AWF C 

H1BTU lbs/hr high 0157B 

LOBTU ibs/nr high 01560 

HlDTLItoss of signal 03019 

LOBTU loss of signal - 03020 

SPECIALITY FEED/C OMPRESSED GAS FEED loss of signal 03D21 

NORTH & SOUTH 3PS ALARMS FAILED 05703 

UPPE R CHAMBER SECONDARY FUEL loss of signal 03022. 

NORTH & SOUTH IPS SERVERSFAILED 05705 

DIRECT INJECT (common alarm) 03132 

Bag Leak Detection System (Tribo) 

Pumpable 1 Hour Rolling Tola! OPL 06205 

Non-Pumpsble 1 Hour Rolling Toial OPL 08206 

Totai waste 1 Hour Rolling Total OPL 03203 

CL1 2 Hour Rolling Total OPL 08211 

Low Volatile 12 Hour Roiling Total OPL 08214 

Semi Volatile 12 Hour Rolling Tola I OPL 08216 

Mercury 12 Hour Roiling Total OPL 08218 

Ash 12 Hour Rolling Total OPL 08220 

P C C Temperature 1 Hour Rolling Average Low OPL 08222 

S C C Temperature 1 Hour Rolling Average Low OPL 08224 

SDA Outlet Temperature 1 Hour Rolling Average High OPL 08226 

Baghouse Differential Pressure 1 Minute Average Low OPL 08227 

.BaghQUse.. Differentja[. Pressure.. 1 Minute Average High 0 P L 08225 

Stack HCL Corrected 1 Hour Roiling Average High OPL 06232 

Stack CO Corrected 1 Hour Rolling Average High OPL 0fi236 

Stack Flow f Hour Rolling Average High OPL 08244 

BTU 1 Hour Total OPL O8200 

Krt Cl/Hra Lime FIDW 1 Minute Average High OPL 03251 

Lime Slurry Density 1 Hour Roiling Average Low 03156 

WiL L NOT ACCEPT SOLID CHARGES >750 KBTU/CHARGE 

Hi/Df Atomizing Air Low pressure alarm (Mqnua.F Check) 

Lo/DI Atomizing Air Low pressure alarm (Manual Check) 

Specialty Feeder Atomizing Air Low Pressure alarm (Manual check) 

Q0442 

00443 

00443 

G044S 

00447 

0044B 

00449 

00450 

00451 

04113 

04114 

04115 

04116 

04117 

D4T1S 

04119 

04120 

04121 

04122 

04123 

04124 

04125 

'04126'.' 

04127 

04123 

04129 

04130 

04132 

ZL 

y 

y 

y 

yy 

~1y~ 

y 

y 

y„ 

y 

y_ 

y 

/ 

O CL ^CONDITION LIMIT 

AWFC =AUTOMATtC WASTE FEED CUTOFF 

MWFC =M!SC WASTE FEED CUTOFF 

SWF C ^SPECIFIC WASTE FEED CUTOFF 

Comments 

CHECKED BY : JSy^T T . 

i ^PROVED : 

DATE://-Z5'-Q <? TME:*j?' » jS" ~ ^j ^ P M 

PLACE : Control Room 

ijfWEEKLY_ 2 

4/4/07 HK 
ABSOLUTE CALIBRATION AUDIT (ACAJ DATA SHEET 

Unit #. Serial # COS A 

Parameter 

> 02 25% 

r CO-low range 200ppm 

r CO-high range '30GGppm 

r HCl 1000ppm 

Parameter NIST Traceable Calibration Standards 

> 02 25% 

r CO-low range 200ppm 

r CO-high range '30GGppm 

r HCl 1000ppm 

Gas Concentration 

Parameter 

> 02 25% 

r CO-low range 200ppm 

r CO-high range '30GGppm 

r HCl 1000ppm 

Low (Zero) 0 "± 0.5 

Parameter 

> 02 25% 

r CO-low range 200ppm 

r CO-high range '30GGppm 

r HCl 1000ppm 

Mid 8.93 ± 0.5 

Parameter 

> 02 25% 

r CO-low range 200ppm 

r CO-high range '30GGppm 

r HCl 1000ppm High 15 ± 0.5 

Run Number Concentration Difference ' 

Reference Analyzer Lov/ • Mid High ' 

1-Lcw 0 0 •o — 

2-Mid 8,93 9.1 -0.17 

3-High . 15 15.1 

4-M>w- 0 0 0 

5-Mid 6.83 9 — -0.07 • — 

6-Hfgh 15 15,3 — -0,3 

7-1 r>w n n 0 ... 

e-Mid 3.93 9.1 — _ -0,17 — 

9-HEgh 15 • 15,2 — -0.2 

Mean Difference -

Calibration Error -

Mean Difference - 0,00 -0.14 • -0.20 

Calibration Error - 0.00% -0.55% -0.80% 

Calibration Error - Mean Difference / Span Value * 100 

Brian Bunfill HI Tech 

Name 

Signature 

Title 

9/25/2009 

2/4/2010 

Date 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

Unit#

 2_ Serial # 

Parameter 

r 02 25% 

'f CO-low range 20Dppm 

r CO-high range 30QOppm 

rHC ! lOOOppm 

Parameter NIST Traceable Calibration Standards 

r 02 25% 

'f CO-low range 20Dppm 

r CO-high range 30QOppm 

rHC ! lOOOppm 

Gas Concentration 

Parameter 

r 02 25% 

'f CO-low range 20Dppm 

r CO-high range 30QOppm 

rHC ! lOOOppm 

Low (Zero) 0 ± 10 

Parameter 

r 02 25% 

'f CO-low range 20Dppm 

r CO-high range 30QOppm 

rHC ! lOOOppm 

Mid 68,9 ± to 

Parameter 

r 02 25% 

'f CO-low range 20Dppm 

r CO-high range 30QOppm 

rHC ! lOOOppm High 153 ± 10 • 

Run Number Concentration Difference 

Reference Analyzer Low Mid High 

t-Low 0 0.1 -0.1 — — 

2-Mld 66.9 71,7 -2.8 — 

3-Htgn • 153 152.7 TM 0.3 

a 04 M.i 

T U-SJYtt V 

5-Mid- 63.9 7f.8 ' — -3 — 

6-High 153 152.8 — TM 0.2 

7-bM— - 0_ .. 0.6 -flj3___ — — 

B-MId 68.9 71.6 — -2.7 — 

9-High 153 ' 152.5 . 0.4 

Mean Difference -

Calibration Error = 

Mean Difference - -0.37 -2,63 0.30 

Calibration Error = -0.18% »1.42% 0.15% 

Calibration Error - Mean Difference / Span Value * 100 

Brian Bunfll! 

Name 

Signature 

E/l Tech 

' Title 

9/25/2009 

Date 

2V4/20tO 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

Unit# Serial if 346 

Parameter 

r 0 2 25% 

f* CO-low range 200ppm 

COhlgFvrange 3000ppm 

CHC1 1000ppm 

Parameter NIST Traceable Calibration Standards 

r 0 2 25% 

f* CO-low range 200ppm 

COhlgFvrange 3000ppm 

CHC1 1000ppm 

Gas Concentration 

Parameter 

r 0 2 25% 

f* CO-low range 200ppm 

COhlgFvrange 3000ppm 

CHC1 1000ppm 

Low (Zero) 0 + 150 " 

Parameter 

r 0 2 25% 

f* CO-low range 200ppm 

COhlgFvrange 3000ppm 

CHC1 1000ppm 

Mid 1079.1 + 150 

Parameter 

r 0 2 25% 

f* CO-low range 200ppm 

COhlgFvrange 3000ppm 

CHC1 1000ppm . High 2220 ± 150 

Run Number Concentration • Difference 

Reference Analyzer Low Mid High 

1-Low . 0 0.1 — 

2-MirJ ' 1079,1 • 1151.9 — -72.3 — 

3-High 2220 2217.4 — 2.6 

:...0 OA. -QA , 

5-Mid 1079.1 1D95.3 -16.2 — 

6-High 2220 2182.5 — — 37.5/ 

7-L^w n . _._o,a - . JQ£... JQ£... — —.. . . 

8-Micf 1079.1 10912 -12.1 — 

9-High 2220 2173.4 — — 416 

Mean Difference -

Calibration Error = 

Mean -0.37 -33.70 27,23 Difference -

Calibration Error = -0.01% -1.12% 0.91% 

. Calibration Error - Mean Difference / Span Value * 100 

Brian Bunfilf E/ITech 

Name 

Signature 

Title 

9/25/2009 

2/4/2010 

Date 
ABSOLUTE CALJBRATIOM AUDIT (ACA) DATA SHEET 

Serial 346 

Parameter 

r 02 25% 

tTM1 CO-low range 200ppm 

CO-high range 3000ppm . 

<*• HCl lOQOppm 

Parameter NIST Traceable CaObration Standards 

r 02 25% 

tTM1 CO-low range 200ppm 

CO-high range 3000ppm . 

<*• HCl lOQOppm 

Gas Concentration 

Parameter 

r 02 25% 

tTM1 CO-low range 200ppm 

CO-high range 3000ppm . 

<*• HCl lOQOppm 

Low (Zero) 0 + 50 

Parameter 

r 02 25% 

tTM1 CO-low range 200ppm 

CO-high range 3000ppm . 

<*• HCl lOQOppm 

' Mid 316 + 50 

Parameter 

r 02 25% 

tTM1 CO-low range 200ppm 

CO-high range 3000ppm . 

<*• HCl lOQOppm High */43 ± 50 

Run Number Concentration Difference 

Reference Analyzer Low Mid High 

1-Low 0 0 0 — — 

Z-Mld 318 276.5 41.5 — 

3-High .743 7411 • — — 1.9 

4..LQV* .0. 0 

5-Mld 313 312,4 — 5.6 — 

6-High 743 738,1 — 4.9 

.:7-Low. .0 0 . . . ... 0 . — . . —.. . 

318 323.1 — -5.1' — 

9-High 743 739 — 4 

Mean Difference ~ 

Calibration Error= 

Mean Difference ~ 0.00' 14.00 3.SD 

Calibration Error= 0,00% 1.40% 0.36% 

Calibration Error = Mean Difference/Span Value * 100 

Brian Bunfill E/f Tech 

Name 

Signature 

Title 

9/26/2009 

2/4/2010 

Date 
Table 1 

Summary of Relative Accuracy Test Audit Results 

Veolia ES Tethlrieal Solutions 

Sanget. Illinois 

June 22, 23 and 24,2009 

CEM S Parameter Units Measured R A Criteria Pass/Fail 

Unit 2 CO ppm @ 7 $ Oy 0,004 ppm 1 Uni PffSS t 2 

O2, diy i.o*-n Pass 

Unit 2 

0 ; , wet 1,0 "'B Pass 

Unit 3 CO ppm @ 7% 0 2 0.063 ppm" Pass t 3 

om%6 1.0

 v Psiss 

Unit 3 

0 2 . wet %o2 1.0

 3 'c PSA-S 

Unit 4 CO ppm @ 7% O,. 1.146 ppmz Uni Pass t 4 

Oa, dry 0.15%' L 0 a

'

c Pass 

Unit 4 

0 2 . wet ^ 0 2 , 0,46%' Pass 

"Percent of emission standard or absolute average difference (ppm or %). 

L PS4B. 

C PS3, 

INCINERATOR C'fMS RAT A 

VEOUAE S 

JULY 7, 2009 

t.:jif"Pj(>j«CD9&-5ei 
Incinerator 

Date Point 

Thermodynamic BTU 

HCLtoLIme 

Slack CO Corrected 

LimeSEurry Density 

Stack HCL Corrected 

Stack HCL RCRA 

Stack 02 Corrected 

Stack 02 Raw 

Stack Opacity 

Stack Row 

SDA OutfetTemp 

Baghouse Diff Press Low 

Baghouse Dfff Press High 

'P.nviromiipital Services 

Saiigk Illinois period En 

1/1/2(310 <T:(iOAM 

VVZOLZ 6:MA\i 

1/1.'J01D <J:OrjAV: 

Page i oi 7 

3 Min IMin 1 Mm 1 Hrllali L Hr Roll 1 Hr Roil I. Hr Roll 1 HrRoL 1 HrK^U 12 Bfc 12 Hr 12 lit lHrTor Ki r To: 1 Ilr Tc-L 

A V G 

Warn 

A V G 

Shut 

A VG 

OPL 

Warn She. OPL 

25.00000 i. 8.00000 33.50000 

4S0.00DD 5D3.00DQ , SO.IfDOOO 75.00000 • 100.000C1 

Tot TotSliut TuiOPL Roll Tot Roll Tot RoUTW Warn 

Warn Warn Sfc'Jl: OPL 

Shut OPL 

67.50000 O.DOOOOD 

45D.O0Q0 5po,ooua 

450.0000 5QQ.OOO0. 

4,000000 

4.00000 D 3.OOOO0D 

tf.auoooa laooooo 

15QQD.DD 

430.0000 500,0030 

3.DDa000 2.000000 

9.000000 to,00000 

67.50000 67.30000 67.00000 

2S.OODD0 32.00000 

20,00000. 25.D0OOO 100.0a3a 

15.00000 1S.S00Ca 13.CBM0 

14SC0.OQ 14950.00 1S147.W 

417.0000 413-D D DO 420,0015(1 
Stack THC 

Low BTU Weight 

Special Feed WefyM 

High BTU Weight 

Solids Weight 

PCC Temp 

S C C Temp 

Stack CO RCRA 

Liquid Weight 

Wfllght 

Chloiine 

Mercury 

Ash 

Law Volatile 

Sernf Volatile 

Vbolia 

Efivxro'jinftntai Services 

S£iUg«tnl3iKjis' 

s-mwrao laootrao 

1750.00(1 1590,000 

1BSQ.0DD 1734,000 

450.0000 500.0000 

looo.ona 1320.000 insg.ooo 

Created • 1/1/2010 &0CAM 

Period Start 1/1/2.010 fcOClAM 

Period Ha 1/1/2010 (?;0C A M 

l-wil of 7 

. 1900.000 1 £33.000 1B93.0DO 

. QtiC-.DOOO QQ^.aOOO 724,00c 3 

. 190Cv030 1952.000 i0'l2.r.cn 

, iooo.ono . 1020.030 :os'i.ooG 

1 Vttj.OUO i 742,000 1714.0 DO 

•t 580,300 1854.KJ0 1B49.0CP 

so.ooo'oa ao.ooooo 100.0000 

2SS0.003 29S0.0CD ^ 137-ODD 

3750.000 3353.000 4017.000 

2.DO.0000 sm.aooo 

0.CD3000 0.0C-3400 

625.0000 673.0000 

40.U3000 4G.0DQD0 

.00000 63,00300 

24CD.000 2500,000 2616.00-3 200,0003 2'7.00-30 233.00CG 

o,oanooo 0.034000 o.C43SQC 

7500,000 SOOO.000 5076,300 

500.CDD0 530,11000 552.000c 

700.0000 730.3000 7iTfi.OO0C . • 
CMS Performance Evaluation 

Uni t 3 
TAG: 

LOOP: 

•

; DHSCSIPOK: 

SERVICE: 

LOCATION: 

LP-SBT: 

REMARKS: 

IJJSTL - ELMKS: 

SPEC-HMKS: 

S/H: 

TWX IHSTRUMKUT CaLIBEAriOM' RECORD 

UNIT #3 

QUAli'l'ERIiY 

WT 

3 04 

WEIGHT TRANSMITTER 

SPECIALTY FEEDER (HOODED) 

MA3STDPACT: 

MODEL: 

SCALE; 

CALIB-IN": 

CALIB-QUT: 

PKQCESS-SP: 

. IHST-SP: 

ACTION: 

I/O NUMBER.: 

TOLEDO 

8140 EXP 

0-2,000 # 

0-2,000 # 

4~2Q MADC 

0#=ai9 ct s 

2 00#=1147 et a 

1#~1,£38 ct s 

30012 

Check scale , digita l Calibratio n per . Toledo instructions * 

Then wit h no weight on scale'adjus t analo g zero . {HOTS: HMI 

wil l not displa y numbers las s tha n zero} . fclext add weight 

= t o 10% ar e more of scale s range, the n adjus t analo g span, 

t o indicat e weight on scale , as rea d on HMI screen . 

See Manufacture s literatur e For detaile d instructions . 

Fil l ou t and a££ix a new calibratio n sticker . 

O .l lb/h r 

CALTERATIOH REPORT 

i m m wlx b 

o . 

INSTRUMENT KEMJSWG• 

Before Calibration ^r ^ 

After Calibration 

CALIBRATION SOtlKCE REFERENCE 

Cohfftisiits 

Performed by; 

JB 

CALSHE ET• WDB 

I MO-tf 

Dat&y^S^if^^ L Time: Z &£> _$M (pM 

Place : 

((FieldJor Shop} 
TWI INSTRUMENT CALIBRATION RECORD 

TAG: 

LOOP: 

DESCRIPON; 

SERVICE: 

LOCATION: 

. LP-SHT: 

P&ID: 

REMARK'S: 

INSTL-RMKS: 

SPEC-RMES: 

S/N; 

1MIT #3 

QUARTERLY 

310 

WEIGHT TRANSMITTER 

SOLID CHARG COSVFIELD 

3031 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OOT: 

PROCESS~SP: 

INST-SP: 

ACTION: 

TOLEDO 

8140 

0-400 # 

0-400 # 

4-20 MADC 

0#=81& CC S 

2Q0#^2457 ct s 

1#=8.19 ct s 

I/O NUMBER: 30022 

CAL IBRATT OKF MOTES 

Check scale , digita l Calibratio n per , Toled o instructions . 

Then, with'no weight on scal e adjus t analog sero . (NOTE: HMI 

wil l no t displa y numbers les s tha n zero) . Next add weight 

= t o 1.0% ar e raore o f scale s range, then adjus t analo g span, 

t o indicat e weight on scale , as rea d on HMI screen . 

See Manufactures literature'fo r detaile d instructions , 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

B&fore Calibration o 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE: 

Comment s: 

performed by: fe^T?sfe^—Date:'feT%^ Time:Z//0 AM ( F M ) 

J B . Plac e r . >s>~~~~2K 

CALSHEET,WDB fField) or Shop)' 
TAG : 

LOOP : 

DESCRIPON : 

SERVICK : 

LOCATION : 

LP-SHT : 

P&ID : 

REMARKS : 

IHSTk-RMKS: 

S2EC-RMKS: 

S/N; 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

QUARTERLY 

PDT 

3 5 0 

PRESSURE DIFF . TRANSMITT E 

BAGHOUSE INLET/OUTLE T 

FIEL D 

3035 

MANUFACT: 

MODEL: 

SCALE : 

CALIB-IN : 

CALIB-OOT : 

PROCESS-SP : 

INST-SP : 

•ACTION: 

I / O NUMBER: 

YOKOQAWA 

0-15 i n wd 

4-20 MADC 

U S E PNEUMATI C CAI J IBRATIO N BENC H WITH INCLIN E MANOMETER AN D 

LOO P CALIBRATOR . INPU T PNEUMATI C SIGNA L AN D READ OUTPUT 

WIT H LOOP CALIBRATOR . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 Xb/hr 

CALIBRATION REPORT 

I^tT T VAT.UE ; INSTRUMENT RSSASISGBefor e Calibratio n 

^ Afte r Calibration ,, 

CALIBRATIOM SOURCE REFERENCE 

Comments: 

Performed by: $&&J-&c /<^!^ Date: 9 Time: Jh y^/WF M 

\ 

::r JB Plac e -. CALSHEET.WDB {Field o r Shop) 
TAG: 

LOOP: 

DESCRIP0N: 

SERVICE: 

LOCATION: 

LP-SET: 

P&ID: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

QUARTERLY 

PT 

PRESSURE TRANSMITTER 

LOW CHAMBER PRESS. 

FIELD 

3032 

MANUFACT; 

MODEL 

SCALE 

CALIB-IN 

CALIB-OUT 

PROCESS-SP 

INST-SP 

ACTION 

I/O NUMBER; 

Rosamount 

1151 DP 

-7.5 t o +2. 

4-20 MADC 

5 in , wc. 

CALIBRATION NOTES 

Connect transmitte r t o be calibrate d t o pressur e source 

and calibrate d referenc e {Manometer), inpu t appropriat e 

pressur e and verif y wit h curren t meter. 

Complete and affi x a properl y filled-ou t calibratio n 

sticker . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

IKPUT VALUE IHST^WSJJT RBaDlflG • 

^ &-tf Before Calibration „ , 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: /f£?e.£r&€- /(/fri Date: °7 Tima ^ / O ?0 

JB Place : 

CALSHEET.WDB (Field or Shop) 

PM 
THI INSTRUMENT CALIBRATIOl* RECORD 

KNIT #3 

QUARTERLY 

TAG: PT 

LOOP: 319 

: DESCRIPON; PRESSURE TRANSMITTER 

SERVICE: OPPER CHAMBER PRESSURE 

LOCATION; FIELD 

LP--SHT: 

P£ID: 3033 

•REMARKS; 

INSTL-RMKS: 

8PEC-RMKS : 

S/titi 

MANUFACT 

MODEL 

SCALE 

•CALIB-IH 

CALIB-OUT 

PROCESS-SP 

INST-SP I 

ACTION; 

I/O NUMBER: 

-7.S t o +2.5 in . wa. 

4 - 2 0 MADC 

CALIBRATION NOTES 

Connect transmitte r t o be calibrate d t o pressur e sou.roe 

a nd calibrate d referenc e (Manometer}, inpu t appropriat e 

pressur e and verif y wit b curren t meter. 

Complete and affi x a properl y filled-ou t calibratio n 

sticker . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affil e a new calibratio n sticker , 

0.1 lb/h r 

CALIBRATION REPORT 

INFO? "VALUE 

Before Calibration 

INSTRUMENT READING 

After Calibration 

Z9> 9 8 TM A 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed bv: A/ss^Zaji A^^fyt Date: ^/"M-^f Time: &^S&/M PM 

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: 

TW1 INSTRUMENT CfiL JBRA'iTON RECORD 

. UNIT #3 

QUARTERLY 

Trib o 

Bag-house Leak Detectio n 

FID 

MAHOPACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

Auburn 

TRIBO.dgd 

0-lOOOpa 

O-lGOOpa 

4-20ma 

CALIBRATION NOTES 

Disconnec t the inpu t cabl e a t the BNC connector on th e inpu t 

card , and check 'for Hero, use Auburn, Trib o flow , file d tes t 

unit , model 2902, t o inpu t a Pico-Amp signa l o f 500pa and 

recor d thes e values . 

0,1 lb / h r 

CALIBRATION REPORT 

INPW''''VALtfEINSTRUMEN T REA&INQ • 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments : Ki n fafibr^vh W needed* 

Performed by;. Date:. iMfrfll Time: \l'ZO(w ) PM 

JB Place : 

CALSHBET.WDB ((Field ) o r Shop) 
TAG: 

i LOOP: 

'' DESCRIRON: 

SERVICE: 

LOCATION-: 

•LrP-EHT 

P&IIJ: 

REMARKS: 

INSTL-RMKS; 

SFBC-RMKSr 

S/M: 

TWI MSTRUMENT CALIBRATION RECORD 

UNIT #3 

QUARTERLY 

AT 

3B9 

OXYGEN MANUFACT: COS A 

STACK GAS ANALY2ER 

FIELD 

3035 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN': 

CALIB-OOT: 

PROCESS-SP; 

INST-SP: 

ACTION: 

I/O NUMBER; 

0-25% 

0-25% 

4-20 MADC 

CALIBRATION NOTES 

Flow calibratio n gas a t 2-3 psi g and 3 scf h 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1. lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

^ y~i Before Calibratio n „ „ 

- ZA.?yf • a . d 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

ZERO GAS CYL ft; j j ^ 6 

SPAN GAS CYL ft: '£ flOl I 3 ^ 

Comments: 

Performed, by; _ Date: Timei ^'S'Srmjpin 

JB Place : 

CAL SHEET. TOB gtfiel(S.J>r Shop) 
TAG: 

. LOOP: 

DESCRIPOM; 

SERVICE: 

, LOCATION; 

LF-SBT: 

P&ID: 

REMARKS: 

INSTL-RMKS: 

SeHC-BMKS: 

S/K: 

TWX INSTRUMENT CALIBRATION RECORD 

mxT #3 

QUARTERLY 

AT 

3 6 SB 

HC 

STACK GAS ANALYZER 

STACK 

556 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP; 

INST-SP: 

ACTION; 

I/O NUMBER: 

Thermo Elect . 

SIC 

0-100 PPM 

Co. 

4-20 MADC 

CALIBRATION MOTELS 

1) Open sample gas bottl e valves . 

2) Pres s MENU Butto n 

3) Pres s CALIBRATION ' 

4} Pres s ZERO ADJUST 

5} Pres s SPAN ADJUST afte r 4) finishe d 

6} Pres s RUN afte r 5}finishe d 

7) Clos e sample gas bottles . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

mem vmm 

O 

Befor e Calibratio n 

1NSTRBKEEOT REABINQ 

-lie.2. 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE 

GAS CYL #: 

Comments; fOo -faC t\s£e f>±t? 

Performed by 

J B • 

CALSHEET, WDB 

Date: Time:. . fQ&Sapm 

Place:. 

(Field or Shop) 
TfTI INSTRUMENT CALIBRATION RECORD 

TAG; 

LOOP: 

' DESCRIPON; 

SERVICE: 

LOCATION: 

LP-SHT; 

- P&ID: 

REMARKS: 

INSTL-RMKS: 

SPEC-RHKS: 

S/K : 

AT 

3 S BE 

OPACITY 

STACK GAS 

STACK 

2.00 to E.72ma 

UNIT #3 

QUARTERLY 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALlB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

TELEDYNE! INST. 

LightHawk 

0-100% 

4-2 0 MADC 

CALIBRATION NOTES 

Clea n windows, 

Sea Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n stickier . 

0-1 lb/h r 

CALIBRATION REPORT 

iNp W ' VALCE.'INSTRUMEN T RS AfiJNS 

Before Calibration 

Afte r Calibration 

CALIBRATION SODRCE REFERENCE 

Comments: Ccilihtodprf .^RT YhQW^acj-u Ce^S C^ulddMfT . 

Performed by; J 2 , , . .T T y J(0 Date:MzlM3 Tims:. 

J B Place:. 

CALSHEET, VJDB 

PM 

'iel p or Shop} 
TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TAG; TT 

LOOP; 30OA 

DESCRIPQN: PLC THERMOCOUPLE INPtJT" MANG'EACT: MODICON 

. SERVICE: LOEfER CHAMBER MODEL; 883-200 

LOCATION: FIELD SCALE: 0-2500 deg-- F 

LP-SHT:' CALIB-IN: TYPE K 

F&ID: 2032 CALlB-OUTi 

REMARKS: PROCESS-SP: 

1NSTL-RMKS: INST-SP: 

SPEC-RMKS: ACTION; 

S/Cf: I/O NUMBER: 

CALIBRATION NOTES 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l of 500 deg E. and 2,000 

deg.F. a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT, 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

TJipW' TMAIH INSTIltfM^N T READING' 

-Z.QOO" F • .zat>oQ 

After Calibration 

CALIBRATION SOURCE REFERSKCS 

Comments 

Performed by:, Date: Time; 

je Place : 

CAL SHEET. HDB * tiwiel&pr Shop). 
TAG: 

LOOP: 

DESCRIPON; 

SERVICE: 

LOCATION; 

LP-SHT: 

P&ID: 

REMARKS; 

INSTL-RMKS; 

SPEC-RMKS: 

S/N: 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TT 

3 00B 

PLC THERMOCOUPLE INPUT 

LOWER CHAMBER 

FIELD 

3032 

MANDEACT: 

MODEL: 

SCALE i 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP: 

INST-SP 

ACTION 

I/O NUMBER 

MODICON 

683-200 

0-2500 deg. 

TYPE K 

CALIBRATION" NOTES 

Use col d junctio n coirrpensated thermocouple calibrato r t o 

inpu t a type K temperature signa l o f 50 0 deg F. and 2,000 

deg.F, a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT, 

.See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker , 

0.1 lb/hr 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

SOO* F Sstor e

 CsIltoatio n

 5PO0° 

Z.0OQ 0 h ZOOcf 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE 

consments: 

Performe d hy-^j-^ \ . '^JLJ^JIP Data: ) I HO - Q°\ Time: 2-' m(Sj ) 

JB 

CALSHEET.WDB 

Place; , 

(Field b r Shop) 
TAG: 

LOOP: 

" DfiSGHXPOU: 

SERVICE; 

LOCATION; 

LP-SET: 

P&ID: 

EEMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N; 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TT 

3 ISA 

PLC THERMOCOUPLE INPUT 

UPPER CHAMBER 

FIELD 

3033 

MANUFACTi 

MODEL: 

SCALE: 

CALIB-IN; 

CALIB-OUT: 

PROCESS-SP: 

INST-SP; 

ACTION: 

I/O MJMBERt 

MODICON 

883-200 

0-2S00 d* 

TYPE K 

>g. R 

CALIBRATION NOTES . 

Use col d junctio n contpensated thermocouple calibrato r t o 

iapu t a typ e K teniperature signa l o f 500 deg ?, and 2,000 

deg-F. a t inpu t of PLC, the n verif y thi s singl e on th e 

contro l pane l CRT. 

see Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0-1 lb/h r 

CALIBRATION REPORT 

INPUT V«IiUeINSTRUMEN T READUifS 

crv ^ P Befor e Calibratio n ^ 

QUO f- • ' QQ f 

2000 ° F 2,c3oo °-

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed by: ife^— ' t - Date: /^t > 0 l Time:£; V^""_AM(^ ) 

JB Place : . ^-— ^ 

CALSHEET.WDB ' <(FieljJox- Shop) 
T KI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TAG; TT 

LOOP: 319B 

" DESCRIPON: PLC THERMOCOUPLE INPUT ' MAHUFACT: MODICON 

SERVICE: UPPER CHAMBER . MODEL: 883-200 

LOCATION: FIELD SCALE: 0-2500 deg. P. 

LP-SHTr CALIB-IN: TYPK K 

P&ID: 3033 CALIB-OUT; 

REMARKS: PROCESS-SP: 

mSTL-RMKS: INST-SP: 

SPEC-RKKS: ACTION: 

S/N: I/O NUMBER: 

CALIBRATION NOTES 

Ose col d junctio n compensated tliermocouple calibrato r t o 

inpu t a typ e K temperature signa l o f 500 deg F. and 2,000 

• deg.F. a t inpu t o f PLC, then verif y thi s singl e on the 

contro l pane l CRT. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affis : a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

j^ptff GALOISTNSTRUMEN T READINS 

^5T)Qa f - Before Calibration ZQO° 

£ > / \ .~ \ /- v <3 Zoc o P 2^oo < 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments:' 

Performed by;, Date: l)~jQ-€ft Time: 

% 

JB Place : <^=a^> 

CALSHEET.WDB QField)or Shop) 
Tff l INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TAG: TT 

LOOP: 323 

: "DHSCRIPON: PLC THERMOCOUPLE INPUT MANUFACT: MODICON 

SERVICE: SDA INLET MODEL: 883-200 

LOCATION: FIELD SCALE; 0-2500 deg. F. 

LP-SHT: CALIB~IN: TYPE K 

PSID; 3033 CALlB-OUT: 

REMARKS: PROCESS-SP: 

INSTL-RMKS: INST-SP; 

SPEC-RMKSi ACTION; 

S/N: I/O NUMBER: 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l o f 50 0 deg F. and 2,000 

deg. P. a t inpu t o f PLC, then, verif y thi s singl e on the 

contro l pane l CRT. 

See Manufactures literature s fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALTJEINSTRUMEN T READING • 

/—,^A O f— Befor e Calibratio n r—^o 

•ZGQQDF Zooo° 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

erforme d by:. Date: Time: 

JB Place : .. , 

CALSHEET.KDB ^ QFiel^ or Shop) 
TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUM* 

TAG: TT 

LOOP: 370 

DESCR1PON: PLC THERMOCOUPLE INPUT 

SERVICE: SDA OUTLET TEMPI 

LOCATION: FIELD 

LP-SHT: 

p&id : 

REMARKS: 

INSTL-RMKS : 

SPEC-RMKS: 

S/N: 

3034 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OOT:-

PROCESS-SP: 

INST-SP; 

ACTION: 

I/O NUMBER: 

CALIBRATION NOTES 

MODICON 

883-200 

0-2500 deg. F. 

TYPE K 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a type K temperature signa l o f 500 deg F , and 2,000 

deg.F. a t inpu t o f PLC, the n verif y thi s singl e on the 

contro l pane l CRT. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

INS1SBMKNT REAi>lNg 

befor e Calibratio n _ A ,o 

_ SOI 

ZQQQ°£ ZOQZ 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed by: J^-^T" ^ Date: Ih]J>^ _ Time^^ 5 AM^jj O 

JB' Place : 

CALSHEET.TOB l(Fial& or Shop) 
TAG: 

LOOP: 

' DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

F&ID: 

REMARKS: 

INSTX.-BMKS: 

SPECS RMKS; 

S/N; 

T WI INSTRUMEN T CALIBSATIO N RECORD 

UNIT #3 

ANNUA L 

FT 

3 8 3 

STACK FLOW TRANSMITTER 

STACK 

FIELD 

303 5 

MANUFACT: 

MODJSL: 

SCALE: 

CALIB-IH: 

CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTIOH: 

I/O NUMBER: 

Rosemount 

0-20,000 ACFM 

0-.5"WC 

4-20 MADC 

S et Damp/pot t o mid poin t 

CALIBRATION NOTES 

USE P3ffiUMATlC CALIBRATION BENCH WITH INCLINE MANOMETER AND 

LOOP CALIBRATOR- INPUT .PNEUMATIC SIGNAL AND READ OUTPUT 

WITH LOOP CALIBRATOR. 

i • 

See Manufactures literatur e fo r detaile d instructions , 

Fil l cu t and affi x a new calibratio n sticker , 

o . i lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

Befor e Calibration 

After Calibration ,/ f 

fat" t/? c / ?. 9fr* » A 

CALIBRATION SOURCE REFERENCE 

Comments: . AJri /tended dtJ.\%r&//ort 

Performed by: ^4$&/s***. JZi'm , Date: A f y O f ^± m & . //Jp & <gjp PM 

JB Place : 

CALSHEHT.WDB (Field or Shop) 
TWI INSTRUMENT CALIBRATION RECORK 

UNIT #3 

ANNUAL 

TAG: FT 

LOOP: 315 

: DRSCRIPON; FLOW TRANSMITTER MANUFACT: MICRO MOTION 

SERVICE: HIGH BTU Liqui d Feed MODEL: DS-040S119SU 

LOCATION: FLD SCALE: 0-3600 lb/h r 

LP-SET: CA6IB-IN; 

P&ID; 3031 CALIB-OOT: 4-20 MADC 

REMARKS: PRQCESS-SP: 

INSTL-RMKS; Flo w Cal . *Il464128334.2$ INST-SP: 

SPEC-EMUS: ACTION: 

S/H: 23S615 I/O NUMBER: 30001 

CALIBRATION NOTES 

Flus h proces s piping , connect water hb&e t o upstream side- of 

flo w meter, se t contro l system t o appropriat e rat e control , 

and rea d totalizer , flo w water int o a containe r and cottrpare 

t h e toltalize r readin g t o the measured amount i n container . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0,1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT SEADIRS 

i t i /% i Before Calibratio n j » i 

After Calibratio n 

/ a os- j u 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: Date: Time:, AM(P^ ) 

JB 

CALSKEET.WDB 

Place : 

(Field hr Shop) 
TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TAG: ST 

LOOP: 316 

DESCRIFON: FLOW TRANSMITTER 

SERVICE: LOW BTU 

LOCATION FLD 

LP-fiHT 

PETD 

B3MAEKS 

XNSTL-BMKS 

SPBC-fiMKS 

S/N; 

3031 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALTB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

CALIBRATION NOTES 

MICRO MOTION 

DS-040 

0-3600 lb/h r 

4-20 MADC 

30002 

Flus h proces s piping , connect water hose t o upstream sid e o f 

flo w meter, se t contro l system to_appropriat e rat e control , 

and rea d totalizer , flow wate r int o a containe r and compare 

t h e toltalize r readin g t o th e measured amount i n container , 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

Tiji^''''VAWraIN^mJMEN T READING 

l ~ ,.< - n vSefore Calibratio n q Q( V W 

f e e 1^;^ . i • f 0 /fc>S> 

Afte r Calibration, 

CALIBRATION SOURCE REFERENCE 

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

Performe d by;. Date: li-i^Ol Time: _AM (5?M^ 

JB Place : * 

CAL SHEET. WDB ({Field) or Shop) " 
TWI INSTRUMENT CALIBRATION RECORD 

UNIT #3 

ANNUAL 

TAG: FT 

LOOP; 363 

•" DESCRIPON: FLOW TRANSMITTER 

SERVICE: LIME SLURRY TO HEAD TANK 

LOCATION: FIELD 

LP-SHT: 

P&LD; 3034 

REMARKS ; 

INSTL-RMXS : 

SPEC-RMKS: 

MANUFACT 

MODEL 

SCALE 

CALIB-IN 

CBXIB-OOT 

PROCESS-SP 

INST-SP 

ACTION 

I/O NUMBER 

B-H 

0-20 GPM 

4-20 MADC 

CALIBRATION MOTES 

ESTABLISH UNIFORM FLOW INTO CONTAINER, READ TOTALIZER, FLOW 

FLUID INTO GRADUATED CONTAINER AND VERIFY WITH TOTALIZER. 

See Manufactures; literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CflLIRRATlOK REPORT 

INPUT VALUEmsT&BMEN T READING 

*7 <r~ 17 •• Befor e Ca.Hbra.tion cn if 

HL _________ _ 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Comments 

Performed hy : \ J^ P Date: U'lS^ l Time: fyQ& AM $wT} 

:\ J B Place ; 

CALSHEET.WDB fffieldjor Shop) 
SiD*Jsdmed t t - iit. LOUJB, MO fStzg 

ttnilimuii (314) &i5-7T?E - Fix; {31^ Ms-! 779 

Scale Inspectio/t Report 

rjustanen ONYX F NVI ROM MENTAL 

#7 MOBILE AVENU E 

SAUGET , IL S22D1 

Location: tffrect Injection 

IWFG/ft/lode!: WI130 

Scale Typo; VEHICLE 

Capacity: BQCODLB 

csKffpflon: Class I El L 

Serial No: 1)13121 

•Scale No: 3 

Divisions: 5LB 

Seals was found in To'erarioffi [~] yea X no 

ahiilTfiftt 

SldeafCorjiyrs/ 

Applied 

Spate Readinr; 

(Astound) 

Error (*f-J T-L-rarjce 

Accept 

Scale Reading Aft=r 

Arijusfoiunl (As Lefij 

ACG3Dt / 

Ea^tinr. 1 21,00D l b aurs4!s l „ -55 .i.b 4-/- 20 l b 21,005 l h Acow r 

Sectio n 2 2i,oo o In 30,SS<J l b -20 l b +/- 20 l h 21,U00 l b ACCIFT 

21,DUO l b 21.0C-D l b 4-0 l b +/- 20 l b 21,OCA IB" ACCEPT 

Sec:LiOll 4 31,COD l b 21,0CD l b + IJ .lb + /*• 2D _3 2 1 , DO0 l b ' '" J&CCBFf ~~' 

EsOtinn £ 21, 00b 1_ 2 1 , tjyij l h +0 l h W - „ ,f.b 21,00 0 i i 

Sectle a 5 21,000 lb 21,005 l h +5 l h -1-/- 20 l b 21,00.5 15' ACCE?? 

) 

1 

Bu1lnup> Weight Scale Reading 

(As fcund) 

Error (+f) Tbv2rar.ee 

Accept 

Stale- Roadlng Aftsr 

Adjuslmsnf (As Left) 

Acnept/ 

Sectio n 17 3, D 3D l b 3,DOS l b -i-5 l h +/- b l b 

6,00 0 l b ti.,005 l h +5 l b +/- 5 J.b ACER?!- """ 

9,00 0 l b 3,0C5 l b H-ii l b 4 / - 10 l b ACCEPT 

3,3,000 lh 12,DDb lb +.5 Ijl 4 7 - 10 l b ACCEPT 

15,DEC l b 15,00 5 l b +5 l b •t f - IS l b ACCEPT 

16,000 l b IBr0Q5 l b •i-5 l b 4-/- 2d li) J-CCEPT 

iectlo n J 31,ooa i t 22,005 l b +-5 Jb 4-/- 2C l b ACCEPT 

Test Procedura follows QSPD09-OG1/OQ2 NlST#: MO: 250883/253250 3S59S OBS04-02Mra3-04K) PJ43M 

RiceLako: fl22/266S26-fJ2 1322/272301-06B22/2740B1-0S 

f Coramerits/Enviroprnsnfal Conditions :FoUn<I broken foot insertion 1, on closer [nspedfari found the sca b had S bad faeE / \J_ 

\ in scale. Installed 5 new cell and feet. ^^fi^^C—? Z^"*^"*- / 

Cat Date: 11/12/2009 NortCaldue: 90 days 

Service TecJuilctan RegTstratTortfc (H&2-IL' 

Calibrated ley Sarvke Techrucian: Alan Primo 

C al ito ration Dates: J AN APS J Lr|_ OCT 

Job Queue*: LT217651 Report ID; 68(101637 

Uncertainty of Moasyremerit provided on rcqu asf. 

FOR CUSTOMS USE ONLY t 

RevIawadByl^ _ _ Date RsvisWfed 

ThbdacinncsTleaall OA. b! ffcpfiKSjMd, WBSpllntiilli'lvllhnsrtthEapprava- rfAtSU/BlftSLjiniioi 3S3I8 CompFTf-
1 

BIWEEKLY UNIT t& (CMS Task IC4Q3H) PAGE 1 OF 2 

-'WPLIANC 5 CriECKSjjEET___ ____ „_„__„__ _ ____;.„.„.„,.. _ 

OPERATING PARAMETERS PLC COIL BWCOI L PASS 

1 OCL *TRV POSITION Cap Open 00791 U04Q1 

2 OCL UPPER y CT CAMBER TI-'MP. <1794 for 1MIN AV G 0D8S7 0D4O2 • y 

3 OCL HI BTU SJHR MAX =>828f?/HR O0Q64 00403 

4 OCL LOWER CHAMBER Tf^MP- <1590 fori MIN AVG 0036S 004D4 

S OCL LOBTUWHRMA X F.1S22SHR • 009G6 00405 . : y 

e OCL FLUE GA S HCL >10C PPM 1HR Rolling awj. 00871 0CHG6 

7 OCL FLUE GA S CO - y >100 PP M 1HR Rolling avg. 00872 0M0 7 - y 

a OCL FLUE GAS OPACITY ->3Q% for 4a0 SecJHr. 00873 0040B 

9 OCL FLUE GAS OPACITY =>60% instantaneous 00B74 00409 y 

.10 OCL FLOE GAS FLOW RATE >17,19B ACF M for >1 Mii. 00975 00410 y 

11. OCL ' MEAT INPUT ^>16MBTlMII? 008S5 0D411 y . 

12 OCL CHLORINE INPUT i-217 Ibs/HR 00866 00412 y 

13 OCL SOU D FEfc'Qtf/HR MAX **1041 «H R 0QS60 00413 y 

14 OCL UPPE R CHAMBER TF-MP- <1345 DEGF I IR ROLLING AVG 00853 00414 y 

15 OCL SPECIALITY FEEDED #/HR MAX =>fi08 #/HR 00952 00415 y 

17 AWFC S DA OLFTLr: T TEMP, >500 deg. F1MIN avg. D0S87 00417 y 

18 AWFC B AG HOUSE DJFF.PR. PROP. =<2"WC OR *10"W C 1M1N avg. 00839 00416 • X 

y 

• X 

19 AWF C FLUE GAS CO =>S00 PP M 1 MIN avg. 00690 00419 

2P AWF C FLUE GA S 02 =<3% 1MIN Bvg. 00392 00420 y 

21 AWF C FLUE GA S KG =>10 PPM 1 MIN avg. 0DS93 00421 

22 AWF C FLUE GA S HCL =*50Q PP M 1M!N avg* 00894 00422 y 

23 AWFC FLUE GAS FLOW RATE 720 ACF M inst. 0D89S DD423 y 

7 4 - ••AWFC FLUE.GAS.QPAC1TY. =>10% 1MIN avg. 00697 00424 

"V AWFC L OW CHAMBER TEMP. <i 6.17 deg. F 1KR railing svg. 00662 00425 

AWF C LOWER CHAMBER PRES S ->-A" wefot 5 sees 0OSS4 00426 

y 27 AWFC UPPE R CHAMBER PRES S =>-.V wefor 5 sees 00SS5 00427 y 

23 AWFC FAILER O F PROCESS MONITOR LOSS OF SIGNAL D06B4 00426 

29 AWFC ID FAN FAILURE LOR I? DF in FAN M CONTACT OR VIH >5 MM ooeea QQ429 y 

30 AWFC UC/LC TEMPS, • TEMPERATURE > 2400 DEG, F 01600 00430 y 

32 MWFC A L L WASTE FEED OFF FROM FIX WF SHUTDOWN MANUALLY FROM FIX 00630 00432 y 

35 MWFC FLUE GAS HCL =>5Q PP M 1HR rolling avg. 00878 O0435 y 

56 MWFC HEAT EN PUT =>15.5 MBTU/HR anticipated 00880 D0436 y 

37 MWFC CHLORINE INPUT =>233 Ibs/HR 00381 00437 y 

38 \JWFC E-STOPS orT/C MODULE E-STOP & T/C MODULE inactive CQ8S9 00433 y 

39 MWFC FLUE GAS C O =>50 PPM iH R tolling avg. 00891 00439 y 

40 MWFC ATOMIZER HI-HI Vibration sv/. >Q rninutes 00852 00440 y / 

41 SWFC SPEC . FEE D ==>724#/HR EXCEEDE D 0DB63 00441 

• * i 
BIWEEKLY UNIT#3 

COMPLIANCE CHEC K SHEET 

=dt* *•==== 

OPERATING PARAMETERS 

{CMS Task [CI 033) 

PLC COIL 13W COII. 

PAGE 3 OF 2 

PAS S FAI L 

42 SWF C 

43 SWF C 

45 SWF C 

48 SWF C 

47 SWF C 

48 MWFC 

50 MWF C 

61 SWF C 

52 OP L 

65 OPL 

66 OPL 

67 OPL 

60 OPL 

69 OPL 

70 OPL 

71 OP L 

72 OP L 

73 OP L 

74 OF L 

75 OP L 

76 OPL 

77 OP L 

Qh'L 

' ''• OPL 

: ' OPL 

St OPL 

32 OPL 

83 AWF C 

84 

65 

. B6 

B7 

88 

HIRTU 

LODTU 

HLBTU (see note 1) 

LOBTU (see note 1) 

SPECIALITY FEED 

=>2Q12*HR EXCEEDE D 

=>1993fflHR EXCEEDE D 

LOSS OF SIGNAL 

LOSS OF SIGNAL 

LOSS OF SIGNAL 

NORTH & SOUTH IPS ALAKMS FA5LED C&MrfflJllKWTKWB TIMED our FOR BOTH 

NORTH a SOU fH IPS SERVERS FAILED COMMUNICATION'S TIMED OUrFOFL GOTH 

DIRECT INJECT COMMON ALAR M 

Bag Leafc Detection System (Tribe) 

Pumpable 1 Hour Rolling Total OPL 

Non-Pumpable f Hour Rolling Total OPL . 

Total waste 1 I lour Rolling Total OPL 

CL1 2 Hour Rolling Total OPL 

Lavt Volatile 12 Hour Rolling Total OPL 

Semi. Volatile 12 Hour Rolling Total OPL 

Mercury 12 Hour Rolling Total OPL 

Ash 12 Hour Rolling Total OPL 

P C C Temperature 1 Hour Rolling Average Low OPL 

S C C Temperature 1 Hour Rolling-Average Low OPL 

S DA Outlet Temperature 1 Hour Rolling Average High OPL 

Baghouse Differential Pressure 1 Mfnute Averago Low OPL 

Baghouse Differential Pressure 1 Minute Average High OP L 

...fitadt.aCL.CD3lsctsd..i.H.BiJf..Rolling. Average High OPL 

Stack C O Corrected 1 Hour Rolling Average Hluh OPL 

Stack Flow 1 Hour Rolling Average High OPL 

BTU 1 Hour Total OPL 

Hit Cl/Hra Lime Flaw 1 Minute Average High OPL 

Lime Slurry Density 1 Hour Rolling Average Low 

WILL NOT ACCEPT SOLID CHARGES >750 KBTUfljJ 

(DO NORTH TANK FARM, BIWEEKLY CHECKS) 

Hlrol Atomizing Air Low Pressure alarm (manual check) 

Lo/DI Atomizing Air Low Pressure alarm (manual check) 

Specialty Feeder Atomizing Air Low Pressure alarm (manual cheek) 

00965 

00967 

03010 

03020 

03021 

05703 

05705 

03132 

0S205 

08Z06 

03203 

08211 

08214 

08216 

08218 

08220 

08222 

06224 

0S226 

0B2Z7 

03229 

08232 

'''08236 

08244 

08244 

08251 

0315S 

00442 

00443 

00445 

00446 

00447 

0044B 

00450 

00451 

04113 

04114 

04115 

' 04116 

04117 

04118 

04110 

04120 

04121 

04122 

C4123 

04124 

0412$ 

04126 

''04127'' 

0412B 

D4129 

04130 

04132 

~7 

^ , 

/ 

LT 

~Z 

y 

y t _ 

y 

O C L =CONDfflON LIMIT 

AWF C -AUTOMATIC WASTE FEED CUTOFF 

MWF C =MISC WASTE FEED CUTOFF 

SWF C ^SPECIFIC WASTE FEED CLFTOFF 

Comments 

CHECKE D BY : DATE: A>-/V-B' ? TtME: / A M (PM 

P^WED : J^g&L?^ far* PLACE : Control Room 

b,^-EEKLY_3 

W 0 7 HK. 
BJWEEKLY liff f #3 (CMS Task EC4039) PAGF 1 OF 

OPERATING PARAMETERS PLC COIL BW COIL PASS 

n O CL TRV POSITION Cap Open 0D7S1 00401 V 

2 OCL UPPE R CHAMBL-R TEMP. <l7B4fcr1MtNAVG 00867 00402 

3 OCL ' HI BTU if/HR MAX ^82 8 #HR 00964 Q0403 

4 OCL LOWER CHAMBE R TEMP. <159GfoMMINAVG 0086S 00404 

5 OCL LO BTU #/HR MAX = 1322 Mi R 00966 00405 . V 

F3 OCL FLU E GA S HCL >10TJ PPM 1HR Rolling avg. 00371 00406 is" _ 

7 OCL FLU E GA S C O >100 PPM 1HR Rolling avg. 00872 00407 

8 OCL FLU E GA S OPACITY =>30% for 480 SecJHr. 0087.3 C04OB . 

5 O CL FLU E GA S OPACITY =>60% Instantaneous 00674 00409 . s 

.10 OCL FLOE GA S FLOW RATE >17,198 ACF M for >1 MIN. 0Q&75 00410 

11 O CL HEAT [NPUT =>1G M BTU/HR 003G5 00411 s 

12 O CL CHLORIN E INPUT >217 Ibs/HR GOSBO 00412 

13 O CL SOLIP FEE D #/HR MAX f=>l041 #/HR 00SBO 00413 / ' 

14 OCL UPPE R CHAMBER TEMP. <\ 845 DEGF1 IR ROLLING AV G oafsas 00414 

15 OCL SPECIALITY FEEDED #/HR MAX ->50BWHR 00852 00415 r 

17 AWFC SDAO U llfTTEMP . >500 dog. F 1 MIN avg. 00687 00417 / 

18 AWFC B A G HOUS E DiFF.Pft. DROP. =<2"WCOR=>10"WC 1 MIN avg. 0DBCS 00413 

19 AWFC FLU E GA S CO =>50Q PP M 1MIN avg. 0QSBO 00419 

20 AWFC FLU E GA S 0 2 -=<3% 1M1H avg. 00392 00420 

21 AWF C FLU E GA S HC =>10PPM 1 MIN avg; 00893 00421 s ' 

22 AWFC FLU E GA S HCL =*500PPM1MINaV£. • 00894 00422 / 

23 AWFC FLU E GA S FLOW RATE =>, 720 ACF M mst. 00595 • 00423 C 

-4 ...AWFC ... .ELUE.GAJS..QFAC1JY «>1D% 1 MIN avg. 0OB97. 00424 -4 

AWFC LOW CHAMBE R TEMP. <1Sl7deg. F VAR rolling avg. 

00S32 00425' r 

• AWFC LOWER CHAMBE R PRESS =;>-.1" wefof 5 sees 0Q3B4 00426 

27 AWFC UPPE R CHAMBE R PRESS =>-.1"wcfor 5 sees 00895 00427 

2S AWF C FAILER O F PROCESS MONITOR LOSS OF SIGNAL 00864 0O42B y 

29 AWF C ID FA N FAILURE LOSS OP IE FAN M CONTACT 0RV|Q>5HW 00663 00429 •s 

30 AWF C UC/L C TEMPS, TEMPERATURE > 2400 DEG. F 01600 00430 / 

32 MWFC A L L WAST E FEED OFF FROM FIX WF SHUTDOWN MANUALLY FROM FIX 00680 00432 / 

35 MWFC FLU E GA S HCL =^50 PP M 1HR rolling avg. oo&7a 00435 

3 e MWFC HEAT INPUT =»15.5 MBTU/HR anticipated QD8B0 00436 •r 

37 MWFC CHLORINE INPUT =>233 Ibs^HR 00831 00437 s 

38 MWFC E-STOPS orT/C MODULE E-STOF & TIC MODULE Inactive 00890 00433 f 

39 MWFC FLU E GA S C O ->50 PPM 1HR rolling avg. 

00891 00439 X. 

40 MWFC ATOMIZER HE-Hi "Vibration sw. >5 minutes 00662 00440 '* 

AA SWFC SPEC , FEE D *>724#fHR EXCEEDE D 00963 00441 / 
BIWr-EKLYUNlr#3 [CMS Task PACtd2 0F 2 

OPERATING PARAMETERS PLC COIL BWCOI L • PASS 

42 SWF C HIBTU =>2012#HR EXCEEDED 00065 00442 X, 

43 SWF C LOBTU =>1$93*HR IrXCEEDED 00967 00443 / 

45 SWF C HiBTLf (see note 1) LOSS O F SIGNAL 03019 O044!5 X 

40 SWF C LOBTU {see note 1) LOSS OF SIGNAL 03020 00446 / 

47 SWF C SPECIALITY FEED LOSS OF SIGNAL 03021 00447 X 

46 MWF C WORTH 6. SOUTH IPS ALARMS FASLED CQumWbTi^'STir/zfrwrFaRncmt 05703 00448 / 

50 MWF C WORTH a somH irs SERVERS PAH-ED COMMUUICATIDHSTIMCLI ciurFDR BOTH 05705 00450 x 

51 SWF C DIRECT INJECT COMMON ALARM 03132 00451 x 

52 O PL Bag Leak Detection System (Tribo) X 

65 O PL Pumpable 1 Hour Rolling Total OPL D82Q5 04113 • 

66 O PL Non-Pumpable 1 Hour Rolling Total OPL 04114 

"67 O PL Tola! waste 1 Hour Rolling Total OPL 06208 04115 s~ 

63 O PL CL1 2 ffourRcllfng Total OPL 08211 04118 s60 O P L Low Volatile 12 Hour Rolling Total OPL 08214 04117 .X 

70 O P L Semi. Voiatilo 12 Hour RcKIng Total OPL 08216 04118 X 

71 O P L Mercury 12 Hour Rolling Total OPL 08216 04119 X 

72 O P L Ash 12 Hour Roiling Total OPL 08220 04120 X 

73 O PL P C C Temperature 1 Hour Rolling Average Lew OPL 08222 04121 X 

74 O PL S C C Temperature 1 Hour RoIETng Average Low OPL 08224 04122 X 

75 O PL SDA Outlet Temperature 1 Hour Rolling Average High OPL 08226 04123 / 

7G O PL Baghouse Differential Pressure 1 Minute Average Low OPL 06227 04124 X 

77 O PL Baghouse Differential Pressure 1 Minute Average High OPL 03223 04123 / 

. ...DEL .Stack HC L Corrected 1 Hour Rolling Average High OPL 03232 04126 X 

y' '" \OP L Stack CO Corrected 1 Hour Roiling Average High OPL 09235 04127 x 

"v. O PL Stack Row 1 Hour Rolling Average High OPl. 03244 04128 X 

G1 O P L BTU 1 Hour Total OPL 08244 04129 X 

82 OPL. Hrt CVtfra Lima Flow 1 Minute Average High OPL 08251 ' 04130 X 

83 AWF C Lime Slurry Density 1 Hour Rolling Average Low 0815S 04132 X 

84 WILL NOT ACCEPT SOLID CHARGES ^750 KBTU/LB X 

85 (OO NORTH TANK FARM, BIWEEKLY CHECKS) 

-S6 HifDl Atomizing Air Low Pressure alarm (manual chock) y 

87 LoflUl Atomizing Air Low Pressure aJarm (manual check) y 

88 SpeciaKy Feeder Atomizing Air L w Pressure alarm (manual cheek) X* 

O C L ^CONDITION UMIT 

AWF C -AUTOMATIC WASTE FEED CUTOFF 

MWF C =M1SC WASTE FEED CUTOFF 

SWF C ^SPECIFIC WASTE FEEO CUTOFF 

Comments 

CHECKE D BY ; 

APT-WED : 

r '• 

u • • • . i 

E L ' ^-EKLY^a 

4/4/07 l-iK 

DATE: tQ-ZOr-Df . mB . g}<f y 

PLACE: Control Room 
BI WEEKL Y UNIT #3 

^MPLIANCt i CHEC K SHEET 

(CMS Task | C4039) PAG E1 OF 2 

OPERATIN G PARAMETER S PLC COtL B W COIL FAIL 

1 O C L T R V POSITION Cap Open • 00791 00401 

2 C3CL UPPE R CI EAMBERTfrMP. <1794 fori MIN AVG 00B67 0O402 

3 O C L I \\ #/HR MAX =i*82S *H R 00064 00403 

4 O C L LOWER CHAMBE R TF.MP. <l590for1M1NAV(5 00B60 00404 

5 O C L LO BTU #/HR MAX kW22#/HR 00966 D0405 

e O C L FLU E GAS HCL >100 PP M 1HR Rolling avg. 00&71 G040B 

7 O C L FLU E CAS C O MOO PPM.1HR Rolling avg. 00872 00407 

8 O C L FLU E GAS OPACITY =>30%for4SOSecJHr. 00373 00406 

9 O C L FLU E GAS OPACITY =>6Q% instantaneous D0874 00409 

.10 O C L FLOE CA S FLO W RATE >17,1 S3 ACF M for >1 MIN, 00875 00410 

11. O C L HEAT INPUT =s>16 MBTU/HR. 00365 00411 

12 O C L CHLORINE INPUT >217 Ibs/I-IR • 00B60 00412 

13 O C L SOLID FEE D MI R MAX =*>1041 S/HR OOOfiO 00413 

14 O C L UPPE R CHAMBER TEMP. <1H45-DEGF HR ROLLING AVG 00B33 D0414 

15 O C L SPECIALITY FEEDED &H R MAX ->60SS/H R C09B2 00415 

17 AWF C SDA OUTLAY TEMP. >5Dflceg. F 1 MIN avg. 00887 00417 

18 AWF C B AG HOUSE DIFF.PR . DROP. *<2"WC OR =>10"WC 1MIN avg. 00689 00418 

1 9 AWF C FLUEGASC O ^>500 PP M 1 MIN avg. 00890 00419 

20 AWF C FLU E GAS 07. -<3% 1MIN &<sg. 00892 00420 

21 AWF C FLU E GAS H C =M0PPM1MINavg . 00893 00421 

22 AWF C FLU E GAS HCL =^500 PP M 1 MIN avg. 00804 00422 

AWF C FLU E GAS FLOW RATE =>, 720 ACF M Tnat. 00805 00423 

XT" ...AWFC ELUEGAS.DPACtrY. =H0% IMlNavg. 00807 00424 

AWF C L OW CHAMBER TEMP. . <1.617 deg. F1H R rolling avg. 00392 00425 

AWF C LOWER CHAMBER PRES S ->-.1"wcfof 5 sees 00884 00426 

27 AWF C UPPE R CHAMBE R PRESS =s>-1"wcfor 5 sees 00885 00427 

23 AWF C FAILER OF PROCES S MONITOR LOSS OF SIGNAL O0BG4 00428 

29 AWF C ID FAN FAILURE LPSS CF ID FMJ M coimc f OH va=>E MIN 0D8G3 00420 

30 AWF C UC/L C TEMPS. TEMPERATURE > 2400 DEG, F 01600 D0430 

32 MWF C ALL WAST E FEED OFF FROM FIX W F SHUTDOW N MANUALL Y FRO M FIX 00650' 00432 

35 MWF C ' FLU E GAS HC L s=>50 PP M 1HR rolling avg. 00870 0043 5 

36 MWF C HEAT INPUT • =*>1$.$ MBTU/HR anticipated 00830 00435 

37 MWF C CHLORINE INPUT ~>233 Ibs/HR • 00881 00437 

3B IWVFC E-STOPS or T7C MODULE &STO P & T/C MODULE inactive 00899 00438 

39 MWFC FLU E GAS C O =>50 PP M 1HR roiling avg. 00691 00433 

40 MWFC ATOMIZER HI-HI Vibration sw. >5 minutes 00662 00440 

41 SWF C SPEC . FEE D ==>724*i4R EXCEEDE D 00953 00441 

zzr 

y 

y 

y L 

yL\ 

~y~ 5 
n I WEEKL Y UNIT #3 

COMPJ .IANCE CHECK 3HE E f 

(.CMS Task 1C4039) PACE 2 C F 2 

42 

43 

45 

46 

47 

48 

50 

51 

52 

65 

GO 

D7 

ea 

70 

71 

72 

73 

74 

75 

76 

77 

61 

62 

63 

S4 

B5 

-. S6 

87 

=>2012iWUK EXCEEDE D 

=>1993/HHR EXCEEDED 

LOSS OF SIGNAL 

LOSS OF SIGNAL 

LOSS OF SIGNAL 

OPERATING PARAMETERS 

SWFC HIBTU 

SWFC LOBTU 

SWFC HIBTU (see note 1) 

SWFC LOBTU {see note 1} 

SWFC SPECIALITY FEED 

MWFC NORT H i-SOUT H fF5 ALARM S FAILE D C0MMUMWTiQN,a'iMKiJ0,Jr FOR Bern i 

MWFC MONTH & SOUTH IPS SERVERS FAILED COMMtJNlDVnON'5 TMt0 OUrFORLDTK 

SWFC DIRECT INJECT COMMON ALARM 

OPL Hag Leak, Detection System (Tribe) 

OPL Pumpable 1 Hour Rolling Totai OPL 

OPL Non-Pumpabfe 1 Hour Rolling Total OPL 

OPL Total wassto 1 Hour Rolling Total OPL 

OPL CL1 2 Hour Rolling Total OPL 

OPL Low Volatile 12 Hour Rolfing Total OPL 

OPL Semi. Volatile 12 Hour Rolling Total OP L 

OPL Mercury 12 Hour Rolling Total OPL 

OPL Ash 12 Hour Rolling Total OPL 

OPL PC C Temperature 1 Hour Rolling Average Low OPL 

OPL SC C Temperature 1 Hour Rolling Average Lo«r OPL 

OPL SDA Outlet Temperature -1 Hour Rolling Average High OPL 

OPL Bagboitse Differential Pressure 1 Minute Average Low OPL 

O PL Baghouse Dffferential Pressure t Minute Average High OPL 

.. OPL StackJICL.Cone ^ Average High OPL 

OPL Stack C O Corrected 1 Hour Rolling Average Hiuh OPL 

OPL Stack Flow 1 Hour Rolling Average High OP L 

OPL BTU 1 Hour Total OPL 

OPL Krt CE/Hra Lime Flow 1 Minute Average High OPL 

AWFC Lime Slurry Density 1 Hour RoRino. Average Low 

WILL NOT ACCEPT SOLID CHARGES >750 KBTUAJB 

(DO NORT H TANK FARM ; BIWEEKLY CHECKS) 

Hi/D3 Atomizing Air Low Pressure alarm .(manual check) 

Lo/DI Atomizing Air Low Pressure alarm (manual check) 

Specially Feeder Atomizing Air Low Pressure alarm (manual cheek)' 

PLC COIL DWCOIL 

00965 

D0967 

03019 

03020 

03021 

05703 

05705 

03132 

0B2D5 

03206 

08205 

08211 

08214 

06216 

08218 

0B22Q 

03222 

03224 

0322© 

03227 

03228 

08232 

'08236 

08244 

08244 

DS251 

00442 

00443 

00445 

00446 

00447 

00443 

004SQ 

00451 

PASS FAIL 

OCL =CONDmON UMFT 

AWFC ^AUTOMATIC WASTE FEfcD CUTOFF 

MWFC -MIS C WASTE FEED CUTOFF 

SWFC =SPEClH C WASTE FEED CUTOFF 

Comments 

CHECKE D BY : ftfihVL- DATE: W^ZS^H TIME': $? )2*\ Cg > M 

| p ;^OVED : ^//aA/^ZC J(^fr* PLACE : Control Room 

b. :dEKLY_3 

4/4/071-IK 
B i WEEKL Y U N IT m 

^OMPLIANC R CHECKSHTn T 

•... '.'> OPERATING ' PARAMETERS 

(CMS Task 1C4030) PAR tl \ OF 

P L C COIL BWCOi L 

1 OCL TRV POSITION Cap Open 00791 00401 

2 OCL UPPER CHAMBTiR TEMP. <l734fD /1MINAV G 00BS7 004O2 

3 OCL Ml BTU S/HRMA X =>82BffiflHR 0D964 00403 

4 OCL LOWER CHAMBE R TEMP, <l590for1MLN AV G 00863 00404 

5 OCL LO BTU #JHR MAX -1B22#/HR 00966 00405 

C OCL FLUE GAS HC L H00PPM1H R Rollins avg. 00871 00406 

7 OCL ' FLU E GAS C O >-100FFM1HR Roilinnavg. 00872 00407 

8 OCL FLU E GAS OPACITY *>30% for 430 SecJJlr. 00873 00408 

9 OCI. FLU E GAS OPACITY ^>60% instantaneous 00874 00409 

10 OCL FLU E GAS FLO W RATH >\7, 1&3 ACF M for >1 MIN. 00375 0041O 

11 O C L HEAT INPUT ^ 1 6 MBTU/HR 00365 00411 

12 O CL CHLORINE IMPUT >217lbs/llK 00300 00412 

13 OCL SOLID FEED WH R MAX =>1041 Ml R .00060 00413 

14 OCL UPPE R C1-IAME3ER TEMP. <1B45 DEG F HR ROLLING AV G 00383 (10414 

15 O CL SPFXIALITY FEEDE D #/HR MAX =:>S0B#/HR 00962 00415 

17 AWFC SDA OUTLET TEMP. ^500 rfeg. F 1MIN avg. 00887 00417 

16 AWF C BAG HOUSE DIFF.FR. DROP. =<2"WC OR =>10"WC 1MIN avg. 00889 00418 

19 AWFC FLUE GAS C O *=>500 PP M 1 MIN avg. 00890 0D419 

20 AWFC FLUE: GAS 0 2 -<3% 1MIN ai/g. 00892 00420 

21 AWF C FLUE GA S HC *s>10 PPM 1MIN avg. 00693 •00421 

22 AWFC FLU E GAS HC L =>500 PP M 1M1N fevg. 0OB94 . 00422 

23 AWFC FLU E GAS FLO W RATE 720 ACF M insL 00395 00423 

...AWFC FLUE.QAS..QPAC.ITY. =>10% 1 MIN avg. 00397 00424 

AWFC LOW CHAMBE R TEMP, <1617 deg. F1H R rolling avg. 00332 00425 

. y AWFC LOWE R CHAMBE R PRES S =>-.!" wc for 5 sees 00884 00426 

27 AWFC UPPE R CHAMBE R PRES S =>-.1''wefor 5 sees 00886 00427 

23 AWFC FAILER O F PROCESS MONITOR LOSS OF SIGNAL 00864 00428 

29 AWFC ID FAN FAILURE LOSS 0t 10 FAN M CONTACt' OR WES >S MIN 00863 0Q429 

3D AWFC UC/L C TEMPS. TEMPERATURE > 24D0 DEG. F 01600 00430 

32 MWFC ALL WASTE FEE D OFF FROM FIX WF SHUTCOWN MAN LfALLY FROM FJX ooeao 00432 

35 • • MWFC FLU E GAS HC L =>50 PPM 1 HR rnlling avg. Q087B 00435 

36 MWFC HEAT INPUT =>15.S MBTU/HR anticipated 00330 00436 

37 MWF C CHLORINE INPUT =>233 Ibs/HR 00B81 00437 

38 MWFC E-STOPS orT/C MODULE E-STOP a T/C MODULE Inactive 00899 0G43B 

39 MWFC FLU E GAS C O P P M 1HR colling avg. 00891 00439 

40 MWFC ATOMIZER Hl-Hi VibTaHioh aw. >5 rninutes 00862 00440 

41 SWF C SPEC . FEED =>724#/HR EXCEEDE D 00963 00441 

PAS S 

- y 

1 

I 

I 

Ik 
BIWEEKL Y UNIT m 

I COJWPLJANC E CHEC K SJIB ^ 

(CMS Task 104038) PAC E 2 OF 2 

P LC COIL B W COIL PASS 

AZ SWF C 

43 SWF C 

45 SWF C 

46 SWF C 

47 SWF C 

43 MWF C 

50 MWFC 

51 SWF C 

52 OPL 

65 . OPL 

SS OPL 

67 OPL 

6 8 OPL 

69 OPL 

70 OPI71 OP L 

72 OPL 

73 OPL 

74 OPL 

75 OPL 

76 OPL 

77 OP L 

O P L 

;

T ' \ OPL 

i OP L 

51 DE L 

82 OP L 

83 AWF C 

84 . 

B5 

. 36 

37 

O C L 

AWF C 

MWF C 

SWF C 

=>2012J!yi-tR EXCEEDE D 

=-1&93ff/HR EXCEEDED 

LOSS O F SIGNAL 

LOSS OF SIGNAL 

LOSS O F SIGNAL 

O0SG5 

0UH67 

03019 

03020 

03021 

05703 

05705 

03132 

00205 

08206 

08208 

08211 

03214 

06216 

DS21S 

03220 

03222 

08224 

08226 

0B227 

0B22B 

0S232 

"03238" 

03244 

08244 

08251 

06156 

00442 

00443 

00445 

00446 

00447 

QQ448 

00450 

00451 

04113 

04114 

04115 

04116 

04117 

04115 

04119 

04120 

04121 

04122 

04123 

04124 

04125 

04126 

''04127*' 

04128 

04129 

04130 

04132 

e x 

"77" 

\y 

T7~ 

±XL 

OPERATING PARAMETERS 

HEUTU 

LOBTU 

HI BTU (see note 1) 

LOtfi'U (see note 1} 

SPECIALITY FEED 

NORTH &. SOUTH IPS ALARMS FAILED cohaiUNlCATioN'siiMiji^ DirrnoRBorrt 

NORTH & SOUTH Wt. SERVERS FAILED COMMUNICATION'S 11MB! niJTFORBOrcH 

DIRECT INJECT COMMON ALAR M 

Bag Leak Detection System (Tribo) 

Pctuipablts 1 Hour Rolling Total OPL 

Non-Pumpabfe | Hour Rolling Total OPL 

T'ofal waste 1 Hour Rolling Total OPL 

CL1 2 Hour Rolling Total OPL 

Lew Volatile 12 Hour Rolling Total OPL 

Semi. Volatile 12 Hour Rolling Total OPL 

Mercury 12 Hour Rolling Total OPL 

Ash 12 Hour Rolling Total OPL 

P C C Temperature 1 Hour Rolling Average Low OPL 

S C C Temperature 1 Hour Rolling Average Low OPL 

SDA Outlet Temperature 1 HOEF Rolling Average High OPL 

Baghouse Differential Pressure 1 Minute Average Low OPL 

Baghouse Differenlia! Pressure 1 Minute Average High OPL 

JSaaiLti^Csest^^Xii^^Mm Average High OPL 

Stack C O Corrected 1 Hour Rolling Average High OP L 

Stack Rov/1 Hour Rolling Average High OPL 

BTU 1 Hour Total OPL 

Hrt Cl/Hra Lime FIDW 1 Minute Average High OPL 

Llrne Slurry Densfty 1 Hour Rolling Average Low 

WILL NOT ACCEP T SOLID CHARGES >750 KBTUA.B 

(DO NORTH TANK FARM, BIWEEKLY CHECKS) 

HiVDI Atomrang Air Low Pressure alarm (manual check) 

Lo/DI Atomrang Air Low Pressure alarm (manual check) 

Specialty Feeder Atomizing ATr Law Pressure alarm (manual cheek) 

CONDITION LIMIT 

=ALTrOMATlC WASTE FEED CUTOFF 

=MISC WASTE FEED CUTOFF 

=SPEC1FIC WASTE FEED CUTOFF 

Cement s 'SCfr U l^f[0SJ£ \ DOm r&tl Jji ft J O . IOT A 

FAIL 

17 

~7> if 

•1 £ 

CHECKE D BY 

AC-^PVED ; 

$ •' 

Y-.,EEKLY_3 ' 

4/4/07 HK 

\y 

DATE ; //"//H P 9 TIME : <g ! 3S^MJM 

PLACE : Control Room 
ABSOLUTE CALIBRATION AUDIT {ACAJ UAIA SHfcfc \ 

Unit # Serial #. 

COSA 

Parameter 

> 02 25% 

r CO-low range 200pp m 

r CO-high range 3000ppm 

r HC l IGOOppm 

Parameter NIST Traceable Calibration Standards 

> 02 25% 

r CO-low range 200pp m 

r CO-high range 3000ppm 

r HC l IGOOppm 

Gas Concentration 

Parameter 

> 02 25% 

r CO-low range 200pp m 

r CO-high range 3000ppm 

r HC l IGOOppm 

Low [Zero) 0 + 0.5 

Parameter 

> 02 25% 

r CO-low range 200pp m 

r CO-high range 3000ppm 

r HC l IGOOppm 

Mid 8.93 ± 0,5 

Parameter 

> 02 25% 

r CO-low range 200pp m 

r CO-high range 3000ppm 

r HC l IGOOppm High • 15 ± 0.5 

Run Number Concentration Difference 

Reference Analyzer Low • Mid • High 

1-Low 0 0.2 -0.2 — — 

2-Mid • 8.93 6,SB 0.05 

15 15,1 — -0.1 

4-Low 0 D.2 -0.2 — — 

5 M d . 8.93 3.33 — 0.1 — 

6-High ts • 15.1 — -0.1 

7-Low 0 0.2 -0,2 — 

8-Mld 3.93 8,83 — 0.1 

9-High 15 15 — 0 

Mean Difference -

Calibration Error = 

Mean Difference - -0.20 o.oa -0,07 

Calibration Error = -0.80% 0,33% • -0.27% 

.Calibration Error = Mean Difference / Span Value * 100 

Bill Adams 

Name 

Has atfa 

Signature 

E/fTech 

Title 

9/23/2009 

2/4/2Q10 

Date 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

Unit # Serial # 154 

Parameter 

r 02 25% 

'** CCMow range 200ppm 

r CO-high range 3000ppm 

r HCE 1000ppm 

Parameter MST Traceable Calibration Standards 

r 02 25% 

'** CCMow range 200ppm 

r CO-high range 3000ppm 

r HCE 1000ppm 

Gas Concentration 

Parameter 

r 02 25% 

'** CCMow range 200ppm 

r CO-high range 3000ppm 

r HCE 1000ppm 

Low [Zero] 0 ± 10 

Parameter 

r 02 25% 

'** CCMow range 200ppm 

r CO-high range 3000ppm 

r HCE 1000ppm 

Mid 68.9 ± 10' 

Parameter 

r 02 25% 

'** CCMow range 200ppm 

r CO-high range 3000ppm 

r HCE 1000ppm High 152 10 

Run Number Concentration Difference 

Reference Analyzer Low Mid High . 

1-Low 0 0,8 • ^O.B — 

2-Mid 69.9 73.3 — 4.4 — 

3-High 152 152.9 — — 

4-Low 0 1 -1 — 

5-Mid . 6B.9 72.1 — -3.2 — 

6-High 152 148,3 — 3.7 

7-Low 0 -0.3 0.3 — 

8-Mld 68.3 71,6 -2.7 — 

9-Hsgh 152 148,1 — — 3.9 

Mean Difference = 

Calibration Error -

Mean Difference = -0,50 -3.43 2.23 

Calibration Error - -0,25% -1.72% 1.12% 

Calibration Error - Mean Difference / Span Value * 100 

Bill Adams E/l Tech 

Name 

•R/AJ a A art 

Signature 

Title 

9/23/2009 

2/4/2010 

Date 
ABSOLU t h UALIBKA JIUK AUU U (AUA J ut\ i A onpc t 

Unit# Serial # 154 

Parameter NIST Traceable Calibration Standards 

r 02 25% Gas Concentration 

r CO-low range 2D0ppm Low (Zero) D ± 150 

i*' CO-high range 30Q0pprn Mid 1079.1 ± 150 

rHC I IDOOppm High 2283 ± ISO 

• 

Run Number Concentration Difference 

Reference Analyzer Low Mid High 

1-Low 0 0.8 — — 

2-Mid 1079.1 1127.1 •-48 — . 

3-High 2285 2237.5. — -2.5 

4-Low 0 0.9 -0.9 

5-M3d .' 1079.1 1081,6 — ' -2.5 

22S5 2265.1 — — 19.9 

7-Lcw 0 -0.3 0,3 — 

8-Mid ' 1079.1 107S.1 3 — 

9-High 2285 2252.4- — — 32,6 

Mean Difference = -0.47 -15.83 16,67 

. Calibration Error - -0,02% -0.53% •0.56% 

Calibration Error = Mean Difference / Span Value * 100 

Bill Adams E/l TECH 

.Name Title 

9/23/2009 

Signature 

2/4/2010 

Date 
AB5ULU I £ LAUBKAI iUN AUU! I (AL-AJ Urtlftoncc i 

Unit* J L . Serial # 

Parameter 

r 02 25% 

f* CO-low range 200pprn 

f CO-high range 3000ppm 

^ HCl 10G0ppm 

Parameter NIST Traceable Calibration Standards 

r 02 25% 

f* CO-low range 200pprn 

f CO-high range 3000ppm 

^ HCl 10G0ppm 

Gas Concentration 

Parameter 

r 02 25% 

f* CO-low range 200pprn 

f CO-high range 3000ppm 

^ HCl 10G0ppm 

Low (Zero) 0 ± 50 

Parameter 

r 02 25% 

f* CO-low range 200pprn 

f CO-high range 3000ppm 

^ HCl 10G0ppm 

Mid 31B ± 50 

Parameter 

r 02 25% 

f* CO-low range 200pprn 

f CO-high range 3000ppm 

^ HCl 10G0ppm High 730 ± 50 

Run Number .Concentration Difference 

Reference Analyzer Low Mid High 

f-Low 0 0.8 -0.8 — — 

2-Mld 318 326,8 — — 

3-High 730 742.9 — _ -12.9 . 

44.ow 0 0.9 — 

313 345.2 — -27.2 • — 

6-High 730 737.9 — -7.9 

7-Low 0 -0,3 0.3 — 

8-Mid 318 353.1 -35.1 — 

730 737,1 — -7.1 

Mean Difference - -0.47 -23.70 -9,30 

Caitbration Error= -0.05% -2.37% -0.93% 

Calibration Error - Mean Difference / Span Value * 100 

Bill Adams 

Mama 

&JAJ 

Signature 

E/ITech 

Title 

9/23/2009 

Date 

2/4/2010 
Tahiti 1 

Summary of Relative Accuracy Teat Audit Results 

Veolia KS Teclinical Solutions 

Saa^ct, Illinois 

Jnne 22, 23 and 24,2005 

CEMS Psirumeter Units Measured RA Criteria .Pass/Fail 

TJnit 2 CO ppm @.7^02 U.004 ppm5 TJni Pass t 2 

02 l dry • L0 W Pass 

TJnit 2 

Oa, wet 0.13%>a 1.0

 w Pass 

U»rt3 CO ppm @ 7% 02

 _ 0.0(53 ppm'1 5°'b U»rt3 Pass 

Oj, dry (1.02%£ 1.0

 w Pass 

U»rt3 

02, wet 0.3] 96a 1.0

 s 'c Pass 

Unit 4 CO ppm @ 7% 0; 1.14^ ppm* Unit 4 j*,* Pass 

On, dry 0.1 S^ 1 1.0 PassUnit 4 

wot &o2 , 0.46 ft1 Pass 

* Percen( of emission standard or absolute average dif&rcfice (ppitL or %). 

'

uPi>4B. 

0

 PS 3. • 

SNCINJ5RATOR CEt*J RATA 5 JULY 7,2fJ0? 

CECPiejuctOW-Rei 
Incinerator 

Data Point 

liuviranmtmtfli Services 

Saugif;!, Illinois 

Created 

Period Stai-c 

1 Min 1 iii n 

A V G AVG 

Wara. Shut 

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l/L-2010 6:00 A M 

1; 1:7010 6:00 A M 

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AVG OIL 

Therrnodynamic BTU 

HC-LtoLime 

Stack CO Corrected 

LlmeSlurry Density 

Stack HCL Corrected 

Stack HCL RCRA 

Stack 02 Corrected' 

Stack 02 Raw 

Stack Opacity 

Stack Ffow 

SDA Outlet Temp 

Baghouse Diff Press Low JJ.oaoocm z.Daoooa 

Baghouse Diff Press High fcocaoun ICOOOOO 

2fT.flQQDD 23.00000 33.5[H]{J0 

*5(],OOD0 RKJ.QQDB 

4SD,nao0 BOO.O0Q0 

4!jfl,000D 500.0000 

+.ooopoa 

4-OBM00 S.OOtfQ* ' 

B.000QBD m.QQODO 

15000.00 

430.0000 500,0000 

Tot TotShic Tot OFL Roll Tot- Roll Tot Roll Tot Warn 

Warn Warn. ShoL ' OPL 

Shut OPL 

^.COOOO la,5U0C(J 15.0CODO 

30.0M0O 75.000 0-3 100-OC&-0 

67J5oaoo 67.30000 S7.cn aco 

5G.0OOGD 32.00000 

20.ocTM 25.00000 100.00110 

14300.0fi 14ES0.00 }5147|ao 

417.00QQ 418.0000 420.CI500 
Stack TH C 

• Low BT U Weight 

Special Feed Weight 

High BT U Weight 

Solids Weight 

P C C Temp 

S C C Temp 

Stack C O RCR A 

Liquid Weight 

Weight 

Chlorine 

Mercury 

Asri 

Low Volatile 

SemiVolatilc 

s.OOOOOn i o.ooooo 

175D.000 1fi9(J,IK]a 

1B60.0QD 17S+.000 

450.0000 600.0000 

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1000.000 1020.001: ias3,oco 

Created 1/1/20 IC 6:00 A M 

P criod Start 1 /1 f 201D fi :WJ A\ i 

Period Ba L'L'2010 fcOQAM. 

Page 4 of 7 

13QQ.C0O 1333.000 '.SEIS.O&C 

600.0000 f>£i.OOOC 724.0CBD 

1930.00C 1352.DC3 2G12.000 

1000.CC3 102Q.2QO -iC-53.0C0 

1775,000 1745.000 1734.000 

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&o .oiiQoo ao.ooooo ioo.on bo 

255D.D00 K950.00Q 3107.000 

3750.000 oSSO.OOD 4017.000 

'200.0000 218,0000 

0.003000 0.QO34DO 

62S.C0Q0 673.0-300 

40.MOOO 46-ocnaa 

56,00000 O'd.OOOGO 

2400.030 2500,000 2810,000 200.U300 217. DOC 0 233X 030 

0.03B-3OO 0.034000 O.D4t)30C . . 

7EDO.00Q OOOO.OGO ao7e.ee o 

soc.aaoo sao.oooo 552.000c 

YOO.C00O 730.0000 75E.C030 
CMS Performance Evaluation 
TWI INSTRUMENT CALIBRATION RECORD 

TAG: 

LOOP: 

. DESCRIPON; 

SERVICE: 

LOCATION; 

LP-SST: 

P&ID: 

REMARKS; 

IFTSTL - RMKS: 

SPRC-EMKS: 

£/N: 

UlSttT #4 

QOARTERIxt 

PT 

300 

PRESS TRANSM 

Kim HOOD 

PTRNSP 

300 

F015 

Raranged 1/19/96 

MODEL: 

SCALE: 

CALIB-BT: 

CALIB-OUT: 

PROCESS-SP: 

ROSEMOWT 

1151DR2F 

-9.0" TO 1.0" WC 

4-20 ma 

Atmosphere = 13,40 ma 

1/2"x 29" SS PIPE insid e Kil n INST-S?: Set Dampening pot ful l CW 

ACTIOS: 

I/O MTJMBKR: Kl:2 5 

CALIBRATION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AMD LOOP 

CALIBRATOR. INPUT PHEUMATIC SIGNAL AMD READ OUTPUT WITH 

LOOP CALIBRATORSee Manufactures literatur e fo r detaile d instruction . 

Fil l ou t and affi x a new calibratio n sticker , 

0.1 lb/h r 

Car.TRRfl.TION REPORT 

I«»UT VALUE ' T^mWSO^Ws^^' 

^ f f Before Calibration ./ , A 

After Calibration 

Comments: 

CAL IBRATj^QN SOTTTfCE REFHRBMCE 

Performed hy: lac k?foi Data: ff^P -0? Time; S *oV AM 

J B ' Place : , ^_ 

CALSHEET.WEXB (Field or Shop) 
Tlf l INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

TAG: PT 

LOOP: 324 

DESCRIPON: PRESS TRANSM 

SERVICE: SCC OUTLET 

LOCATION: £T,D 

LP-SHTi 324 

P&ID 

.REMARKS 

IHSTL-RMKS 

SPEC-RlflES 

S/N 

MAHUFACT 

MODEL 

SCALE 

CALIB-IN 

CALIB-OOT 

PROCESS-SB 

IMST-SP 

ACTION 

I/O NUMBER 

ROSEMONT 

115X65312 

-15" TO +5" WC 

4-20 MADC 

CALIBRATION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e fo r detaile d instruction s 

Pil l out and affi x a new calibratio n sticker . 

Q.l lb/h r 

CALIBRATION REPORT 

INPUT "VALUE 

r-ff 

INSTRUMENT READIMG 

Befor e Calibration 

After Calibration 

Comments 

CALIBRATION SQURCB RKFEREKCB 

Performed by 

JB 

CALSHEET.WDB 

Place: . 

(Field or Shop) 
TAG: 

LOOP: 

DESCRIEQKT: 

SERVICE: 

LOCATION:-

X.P-SHT: 

P&ID: 

REMARKS: 

INSTD-RMKS: 

SPEC-RMKS: 

S/N; 

TUT INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

PDT 

439 

DP TRANS 

BAGHOUSE PRESSTJER 

WAPC 

437 

FOI 7 

W/GAS CLEANING TRAIN 

NORTH/EAST BAGHOUSE 

MAMUFACT: POXBORO 

MODEL: 823 DPI 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCRSS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

0-15" WC 

4-20 MADC 

CALIBRATION NOTES 

TJSE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR, INPUT PNEUMATIC SIGNAL AMD READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l ou t and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

. Before Calibration , 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: J/^/ M KJ^ Vatai£Lz£?-Qf Time:Q^- i _.£M)PM 

JB Place : . 

CALSHEET. WDB (Field or Shop) 
TAG: 

1 LOOP: 

DEGCRIPOW: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID; 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS : 

S/N: 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

PDT 

440 

DP TRANS 

BAGHOUSE PRESSDER 

WAPC 

437 

P017 

W/GAS CLEANING TRAIN 

1TORTH/ CENTRAL BAGHOUSE 

MANUFACT; FOXBORO 

MODEL: 023 DPI 

SCALE: 

CALIE-IN: 0-1S" WC 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

CALIBRATION NOTES 

USS PWETJMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e fo r detailed , instructions . 

Fil l cu t and affi x a new calibratio n sticker , 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

Before Calibration «, ~ _ 

a . _ <l?9/* 4 , _ 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: $ L Ch^/s bm,A'CT A 

Performed by: £/ft.eL&€ fan* Pate : /^fa-Of Time:.//-' fO Q P M 

7 JB Place : 

CALSEEET.WDB (Field or Shop) 
TAG: 

LOOP: 

•' DE SCR I PON: 

SERVICE: 

LOCATION: 

LP-SBT: 

P&ID : 

REMARKS: 

IMSTL-HMKS : 

SPEC-RMKS: 

S/N: 

T »I nrerauMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

PDT 

4 41 • 

DP TRANS 

BAGHOUSE PKESSUER 

WAPC' 

4 37 

P017 

W/GAS CLEANING TRAIN 

• NORTH/WEST BAGHOUSE 

MANUFACT: FOXBGRO 

MODEL: 823 DPI 

SCALE: 

CALIB-IN: 0-15" WC 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER; 

CALIBRATION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

•LOOP CALIBRATOR. 

See ManufacLures literatur e fo r detaile d instructions . 

Fil l out and affii c a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT -VALUE 

Before Calibration 

INSTRUMENT READING 

After Calibration 

/ 9 . JO, M$ 

CALIBRATION SOURCE REFERENCE 

Comments: 

=erformed by: /f&>&/ J?/'**-. Date -Jf^/l-^ J Time*: /*^gg L 

J B 

CALSHEET.WDB 

Place: . 

(Field or Shop) 

Pi" 
TffI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

TAG: PDT 

. LOOP: 442 

• .

;i ' DESCRIPOH: DP TRASS MANUFACT: FOXBORO 

SERVICE: BAGHOUSE PRSSSUER MODEL: S23 DPI 

LOCATION: WAP-C SCALE: 

LP-SHT: 43 7 , CALIB-IN: 0-15" WC 

PS-ID: F017 CALIB-OOT: 4-20 MADC 

REMARKS: W/GAS CLEANING TRAIN PROCESS-SP? 

IHSTL-RMKS: SOUTH/EAST BAGHOUSE INST-SP: 

SPEC-RMXSr ACTION: 

S/N: I/O DUMBER: 

. CADIBRRTION NOTES 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e fo r detaile d instructions ! 

Fil l out and affil e a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REEORT 

INPUT VALUE INSTRUMENT READING 

Before Calibration / „ / ^ A 

& ^ of /PA 

After Calibration 

CALIBRATION SOURCE REFERENCE 

CommentsJ 

Performed by; jffa / nr. • Date:^/!- ^ Time: (t&k PM. 

JB Place : . 

CALSHEET,WDB (Field or Shop) 
TAG: 

LOOP: 

'•• DESCEIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-RMRS: 

SPEC-RMKS: 

S/N: 

THI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

PDT 

443 

DP TRANS 

BAGHOUSE PRESSUER 

WAPC 

43 7 

F017 

W/GAS CLEANING TRAIN 

SOUTH/CENTRAL BAGHOUSE 

MANUFACT: 

MODEL: 

SCALE; 

CALIB-IN : 

CALIB-OTJT: 

FROCKSS-SP: 

INST-SP: 

ACTION": 

I/O NUMBER: 

EOXBORO 

823 DPI 

0-15" WC 

4-20 MADC 

USE PNEUMATIC CALIBRATION BENCH WITH MANOMETER AM) LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l ou t and affi x a new calibratio n sticker . 

0.1 lb/h r 

INPUT VALUE INSTRUMENT READING 

A Before Calibration ^ f „. r A 

J^LRi ^A 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments": • 'A/n •cL&J. (2&yfi 

forme d by: fhh*> L&C k/ m Date: ? Time:A'f e c j S PM 

JB Place : 

CALSHEET.WDB ffiel d or Shop) 

Per. 
TAG-' 

LOOP: 

•

; DBSCRlPOB: 

• SERVICE: 

LOCATION; 

LP-SHT: 

P&ID: 

REMARKS: 

IHSTL-RMKS: 

SPEC-RMKS: 

S/ST:' 

TWI INSTRUMENT CA L X BRATION RECORD 

UNIT #4 

QUARTERLY 

PUT 

444 

DP TRANS 

BAG-HOUSE PRE8SUER 

TCAPC 

437 

F017 

W/GAS CLEANING TRAIN 

SOUTH/WEST BAGHOUSE 

MANUFACT: 

MODEL; 

SCALE: 

CALIB-IN: 

CAL IB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

FOXBOSO 

823 DPI 

0-15" WC 

4-20 MADC 

CALIBRATION NOTES 

USS PNEUMATIC CALIBRATION BENCH WITH MANOMETER AND LOOP 

CALIBRATOR. INPUT PNEUMATIC SIGNAL AND READ OUTPUT WITH 

LOOP CALIBRATOR. 

See Manufactures literatur e .for detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . • 

O . l lb/h r 

CALIBRATION REPORT 

INPUT VALUE i^STBOOnW^""^^^ ^ 

Before Calibration n X 

Afte r Calibration A 

O <* /nA 

CALIBRATION SOURCE REFERENCE 

Performed by: J?afcL&^. Pftrj Date:/A/2-<?9 Time: $>~3& 

JB . " Place ; 

CALSHEET.WDB (Field or Shop) 

PM 
TAG : 

LOOP r 

!

 DESCRIPON; 

SERVICE : 

LOCATION: 

LP-SHT : 

P&ID i 

REMARKS: 

INSTL-RMKS : 

SPBC-RMJCS : 

TWI INSTRUMENT r^ALIBRATtON RECORD 

UNIT #4 

QUARTERLY 

WIT 

ooa 

WT TRANS 

SHREDDED SOLIDS 

FTRNSP 

I 

FOI 2 

W/SOLIDS FEED SYSTEM 

S/N: E12S65900A 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

. CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: Nl: 5 

TOLEDO 

8140 

0-3GQ0# 

O-3QO0# 

4-20 MADC 

Check scale,.digita l Calibratio n per . Toledo instructions . 

Then wit h no weight on scal e adjus t analo g zero . {NOTE: HMI 

wil l no t displa y numbers les s tha n zero) . Next add weight 

= t o 10& are more o f scale s range r then adjus t analog span, 

t o indicat e weight on scale , as rea d on HMI screen . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker , 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT 

rf-. Before CaJ.jMra.tion 

O . <~> , 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments; 

Performed by': &UJTC"< JK/U^J$ . .. Pate : i(-£-Q? Time: *V ; 0 0 j&Mfpi 

JB 

CALSHEET« WDB 

R 

Place i 

fiel d hr Bhop) 
THI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

QUARTERLY 

TAG: WIT 

LOOP: 014A 

' DESCRIPOlf; WT TRANS 

SERVICE: DRUM EEED 

LOCATION: FTRNSP 

LP-SET: 

P&ID: 

REMARKS': W/DRUM FEED NEMATRON 

INSTL-RMKS: 

SPEC-RMKS; 

S/N: 42S01574NS 

MANUFACT: TOLEDO 

MODEL: 8140 

SCALE: 0-1,000 lb . 

CALIB-IN: 0-1,000 lb . 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTIOS: 

I/O NUMBER: HI:35 

CALIBRATION; jgsreg 

Check scale , digita l Calibratio n per . Toledo instructions . 

Then, wit h no weight on scal e adjus t analog zero . (NOTE: HMI 

wil l not displa y numbers les s than zero) . Next add weigh t 

* to 10% are more o f scales - range, then adjus t analog- span, 

t o indicat e weight on scale , as rea d on HMI screen . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE 

D. 

INSTRUMENT READING 

Befor e Calibration. 

SO 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: hxST , ^ 0 Date: /A (^Cf l Time : 3\£ > AM 6? ) 

JB 

CAL SHEET. WDB 

1 

Place:. 

(Fieljd or Shop) 
TWI JITS TRUMEHT CALIBRATION RECORD 

TAG: 

"' LOOP: 

• DESCRIPOW: 

SERVICE: 

LOCATION: 

LF-SET: 

P&TD: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

UNIT #4 

QUARTERLY 

WIT 

014B 

WT TRANS 

AUX. DRUM 

FTRNSP 

FEED 

HEW AUX DRUM FEED 

MANUFACT: 

MODEL; 

SCALE: 

CALIB-IN: 

CALEB-OUT: 

PROCESS-SP: 

TNST-SP: 

ACTIOS; 

I/O NUMBER: 

CALIBRATION NOTES 

TOLEDO 

B140 

O-200# 

0-200# 

4 - 3 0 MADC 

Check scale , digita l Calibratio n per , Toledo instructions . 

Thsn wit h no weigh t on scale- adjust'analo g aero. (NOTE: HMI 

wil l not displa y numbers les s than 2;ero) ,. Next add weight 

= t o 10% are more o f scale s range, then adjus t analo g span, 

t o indicat e weigh t on scale , as rea d on HMI screen . 

See Manufactures literatur e fo r detaile d instruction s 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

INPUT VALUE 

O 

CALIBRATION REPORT 

INSTRUMENT READIES 

before Calibration 

After Calibration 

D 

s o 

CALIBRATION SOURCE REFERENCE 

Cotftmfints 

Performe d by:. 

CALSHEET.WDB 

Date:, Time : m (p^ 

Place : . 

({Field hr Shop) 
TAG; 

v- LOOP: 

DESCRXPON: 

SERVICE: 

LOCATION; 

LP-SET: 

p£TD; 

REMARKS: 

JNETL-RMKS: 

SPEC-RMKS : 

S/KTr 

TffI INSTRUMENT C&LIBRATTON RECORD 

UNIT #4 

QUARTERLY 

S5UA 

Trib o 

Baghouse Leak: Detection . 

FLD 

MANUFACT; 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUTi 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBERr 

CALIBRATION NOTES 

Auburn 

TRIBO.dgd 

0-l00Opa 

0-lDOOpa 

4-20ma 

Disconnect: the inpu t cabl e a t th e BNC connector on the inpu t 

card , and check fo r zero . Use AuburnF Triboflow , file d tes t 

unit , model 2902, t o inpu t a Pico-Amp signa l o f 500pa and 

recor d these values . 

0.1 lb/h r . 

CftLlftKATION REPORT 

INPUT VALUE INSTRUMENT HEADING 

Befor e Calibration 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: 

fitU 0(j ~ Date :it ^?Time : 9 

JB Place : ^ ^ 

CALSHEET,WDE {iFiei§/6r Shop} 

PM 
„f£U4 (1C4034) 

'• ^UAKFEJRLY CARBON INJECTION PREVENTIVE MAINTENANCE CHECK SHEET 

1 Disconnect AC Power to the Digi Drive. 

2 Inspect A C & Motor drive screw terminal connections for 

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

3 Replace the two Dig l Drive fuses 

4 Verify any external safety switches or lockouts arc stil l operation 

5 Remove Screw feeder cover & blow out carbon 8s dust. 

6 Inspect G ears Ss Belts for wear or damage. 

7 Check Operation of Motor & Gears for abnormal noise or movement. 

•&• Repiaee..aiiy...needed.p.&xl^ 

COMMENTS ; 

Name: Date://- 6-t?1 Time: 3 » ? 3 A M 0S. 

QUARTER. 4 

11/1/06 KF 

PAG E I O F I 

PASS FAIL 

/ 

/ 

/ 
TAG': 

•r% . LOOP: 

•'.•J DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHI: 

P&ID: 

REMARKS: 

INSTL-RMES: 

SPEC-RMKS; 

S/N: 

TWI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

ANNUAL 

FT 

129 

FLOW TRMS 

PCC LOW GRADE WDJ? X-10 

P-BMS 

129 

E013 

W/BMS 

101499 

MANUFACT: 

MODEL: 

SCALE: 

CALTB-IN: 

CALIB-OOT: 

PROCESS-SP: 

INST-SP; 

ACTION: 

I/O NUMBER: 

MICRO MOTION 

DS100S 120 

0-7,000 #/HR 

4-20 MADC 

CALIBRATION NOTES 

Flus h process piping , connec t water hose t o upstream sid e o f 

flo w meter, se t contro l system t o appropriat e rat e control , 

and rea d totalizer , flo w wate r int o a containe r and compare 

t he toltalize r reading" t o th e meaauxed amount i n container . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affix : a new calibratio n sticker . 

CALIBRATION REPORT 

TfJPTJT VALUEINSTRUMEN T REftDING 

\r~ w . o (.Before Calibration . 

lb lbs , pe r w\\r>. W \ fri!*. t^tS l.b s 

After Calibration 

CATiTRRATljQK SOURCE REFERENCE 

Comments 

Performed toy: J Date: Time: 

J B P i ace: 

CAL SHEET. WDB (Field)or Shop} 

I 
TWI INSTRUMENT CALIBRATION RECORD 

UNIT #4 

ANNUAL 

TAG: 

.LOOP: 

. DESCRIPOW; 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: W/BMS 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

FT 

145 

PLOW TRANS 

PCC SLUDGE 

P-BMS 

145 

J?013 

103056 

X-12 

MANUFACT: MICRO MOTION 

MODEL: DL100S-SS 

SCALE: 

CALIB-IN; 

CALIB-OUTi 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: NT;28 

0-8,000 #/HR 

4-20 MADC 

CALIBRATION NOTES 

Flus h proces s piping,, connect water hose t o upstream a±d& o f 

flo w meter, se t contro l system t o appropriat e r-ate control , 

and rea d totalizer , flo w wate r int o s containe r and compare 

t h e toltalize r readin g t o th a measured atnonnt i n container . 

CALIBRATION REPORT 

INPUT VALUE INSTRUMENT READING 

r> ^Before Calibration q q I - j 

jO \bS~ p T mm , \l) r 1 <wn. „ l> ' ' >P^' 

After Calibration 

CAL IE RATION SOURCE REFERENCE 

Comments: 

Performed hy: IsibXCL E^/^bp Date: il-H^O' t Time: ^"-OO m 

J B Place ; 

CALSHEET.WDB (field]or Shop) 
TWI INSTRUMENT CALIBRATION RECORDTAG: 

LQOP: 

DESCRIPOOtf; 

SERVIC2: 

LOCATION: 

LP-SHT; 

PfiTD: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

UNIT #4 

ANNUAL 

FT 

212 

FLOW TRANS 

WDF TO X-22 

S-BMS 

212 

F014 

W/BKS 

101775 

MANDFACT 

MODEL 

SCALE 

CALIB-IN 

CALIB-OOT 

PROCESS-SP 

INST-.SP 

ACTION 

I/O NUMBER 

CALIBRATION NOTES 

MICRO MOTION 

D1D0QS-SS 

0-7,000 #/HR 

4-20 MADC 

Flus h proces s piping , connect water hose t o upstream sid e of 

flo w meter, set contro l system t o appropriat e rat e control , 

and rea d totalizer , flo w water int o a containe r and compare 

t h e toltalize r readin g t o the measured amount i n container . 

See Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker , 

lb/fee- /O^o 

CALIBRA1 

INPUT VALUE 

}5 fes. £>er t^ffi . 

Before Calibration 

Afte r Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

performed by s hh/^O Date: )l^D°i Time: H'OO AM ( g h 

J B Place : 

CALSHEET. WDB {Field} or Shop) 

l 
TV7I INSTRUMENT CALIBRATION" RECORD 

UNIT #4 

AKNUAL 

TAG: 

LOOP: 

• DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SET: 

P&ID: 

REMARKS: *?/BMS 

INSTL-RMKS ; 

SPEC-RMKS: 

S/N: 1155343 

FT 

138 

FLOW TRANS 

PCC AQ L1Q X-l l 

P-BMS 

133 

F013 

MANUFACT: MICRO MOTION 

MODEL: D100S-HY 

SCALE: 

CALIB-IN: 0-6,000 #/HR 

CALlB-OUTt 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: 

CALIBRATION NOTES 

Flus h proces s piping-, connect water hose t o upstream sid e of 

flo w meter, se t contro l system t o appropriat e rat e control , 

and rea d totalizer , flo w wate r int o a containe r and compare 

t he toltalize r readin g t o th e measured amount i n container . 

Sea Manufacture s literatur e fo r detaile d instructions , 

Fil l ou t and affi x a new calibratio n sticker . 

lb/h r /DVa 

CALIBRATION REPORT 

''iNPuT''vALtfETNSTOTMBN T RIDING 

, f r j Before Calibration t u v J / -

\S Iks , pg r m\n Sbv I ttun . ' * <•

 Q >£>s 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Coroments: 

Performe d by: .ftfi /t) ^ Date :\^^0 ^ Time: )V OOl 

JB Place : 

CALSHEET.TOB fjfreljjo r Shop) 
:b:V-r-'h 

TAG: 

LOOP : 

DESCRIPOJtf: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID; 

REMARKS; 

INSTL-RMKS: 

SPEC-RMKS: 

S/ET: 

Ttfl INSTRUMENT CALIBRATION RECORD 

UNIT #4 

ANNUAL 

TT 

317A 

TC ASSEMBLE 

SCC OUTLET 

FDD 

317 

F015 

TC PfELL INCONEL 601 24" 

MANUFACT; CHESSEL 

MODEL: 3510 

SCALE: Type R TC 

CALIB-IN: 0-300,0 F • 

CALIB-OUT: 4-20 MADC 

PROCESS-SP; 24" INCONEL 601 WELL 

INST-SP: 

ACTION; 

I/O NUMBER: N1;S1 

CALIBRATION NOTES 

U se col d junctio n compensated thermocouple calibrato r t o 

inpu t a .teitjperature signa l o f 500 deg F. and 2,000 deg.F. a t 

inpu t of transmitter , then verif y thi s singl e i n contro l 

room, • 

S ee Manufactures literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

CALIBRATION REPORT 

INPUT VALUE 

Before Calibration 

INSTRUMENT READING? 

20OD 

After calibration 

CALIBRATION SOURCE REFERENCE 

Comments: ^ 0 CMJ fcrATl. ^ 

• Performe d by: §zUj CkJjtAWr\^_ Date: lhj"l-& ci Tima: AM^PM^) 

JB Place : 

CALSHEET.WDB (Field or Shop) 

R 
TAG-' 

LOOP: 

' DESCRIPOEr 

SERVICE: 

LOCATION: 

LP-SHT; 

P&ID: 

REMARKS: 

IWSTL-RMKSr 

SPEC-RMKSS/N: 

TWI INSTRUMENT CALIBRATION" RECORD 

UNIT #4 

ANNUAL 

TT 

3I7B 

TC ASSEMBLE 

SCC OUTL5JT 

ELD 

317 

pgi s 

TC WELL INCONEL £01 24" 

MAJJUFACT: CHRSSEL 

MODEL: 3510 

SCALE': Type R TC 

CALIB-IH: 0-3000 F 

CALIB-O'OT:. 4-20 MADC 

PROCESS-SP: 24" INCONEL 601 WELL 

INST-SP: 

ACT!OH: 

I/O NUMBER: 1*1:52 

. CALIBRATION' NOTES 

Use col d junctio n compensated 'thermocouple calibrato r to 

inpu t a temperature signa l o f 500 dag F. and 2,000 detj.F, at 

inpu t o f transmitter , the n verif y thi s singl e i n contro l 

room. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l ou t and affix : a neur calibratio n sticker . 

-OH. lb/hr -

CALIBRATION REPORT 

INPUT VALUE 

2cxx) 

Before Calibration 

INSTRU^ 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments : . „ . „_ 

Performed by: Date: /f^f T-^ffirime : A 7 9 AM 

JB Place : . s— 

CALSHEET.WDB \^ield)or Shop) 

R 
TWI INBTROMENT CALIBRATION RECORD 

UNIT #4 

AKNUAL 

TAG: TT 

LOOP: -305A 

DESCRIPON: -PYROMETER 

SERVICE; KILN OUTLET 

LOCATION: ELD • 

LP-SHT: 305 

P&ID: F015 

REMARKS: 44-99-F-1-0-1 

INSTL-RMKS: 55" Targe t Tube 

SPEC-RMKS: 

S/N; 

MANUFACT: IRCON ' 

MODEL: M0DLIHE4 44-99-F-l-0-1 

SCALE; Type R TC 

CALIB-IN: 0-3,000 deg F 

CALIB-OOT: 4-20 MADC 

PROCESS-SP: EMIS. 85Sr 

INST-SP: 

ACTION: 

I/O NUMBER; Nl:51 

CALIBRATION MOTES 

Instal l factor y calibrate d Pyrometer. 

See Manufactures.literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

INPUT1 VALUE 

CALIBRATION REPORT 

Befor e Calibration. 

READING 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: ^/^m/ W Fluke 

Performed by:. 

JB 

•CAL SHEET. TOB 

3 

Date:. 

Place : 

Time: 

(Field or Shop) 

AM PH 
TWI msraOMEKT CALIBRATION RECORD 

UNIT #4 

ANNUAL . 

TAG T I T 

LOOP:- 3D3B 

DESCRIPON; P^RQr *ETE R 

SERVICE: KILN OUTLET 

LOCATION: FLD 

LP-SHT; 305 

P&ID: F015 

. REMARKS: 44-99-F-l-0-1 

INSTL-RMKS; 551 1 Target Tuba 

SPEC-RMKS: 

S/N: 

MANUFACT: IRCON 

MODEL: MODLINE4 

SCALE: Type R TC 

CALIB-IN: 0-3,000 deg F 

CALIB-OUT: 4-20 MADC 

PROCESS-SP: EMIS. 85^ 

INST-SP; 

ACTION; • 

I/O NUMBER: HI;52 

44-99-P-1-0-

CALIBRAT1QN NOTES 

Instal l factor y calibrate d Pyrometer. 

See Manufacture s literatur e fo r detaile d instructions , 

Fil l out and affi x a new calibratio n sticker . 

0.1 lb/h r 

INPUT VALUE 

CALIBRATION REPORT 

INSTRUMENT HEADING 

Befor e Ca.libra.txon 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by:. 

JB 

CAL SHEET. WDE 

S 

„ Date:. 

Place : 

Time: JW PM 

(Field or Shop) 
TBI INSTRUMENT CALIBRATION RECORD 

TAG: 

LOOP: 

DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS; 

UNIT #4 

ANNUAL 

TT 

404A 

TC TRANS 

TC GAS OUTLET 

WAPC 

404 

F01S 

W/GAS CLEANING TRAIN 

MANUFACT; 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-GUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: Nl:ll 4 

MOORE 

TIY/K2-0-1-4-20MA 

0--1500 deg F 

Type K TC 

4-2D MADC 

CALIBRATION NOTES 

Use col d junctio n compensated thermocouple calibrato r to 

inpu t a temperature signa l o f 200 deg F. and 1,000 deg.F. a t 

inpu t o f transmitter , the n verif y tbl s singl e i n contro l 

room. 

See Manufactures literatur e fo r detaile d instructions . 

Fil l ou t and affi x a new calibratio n sticker . 

-0.1 lb/ha?-

CALIBRATION REPORT 

INPUT VALUEINSTRtfM W RKADINe 

' J DDD P • [ 00O & 

After Calibration 

CALIBRATION SOURCE REFERENCE 

Comments: 

Performed by: Date: i { f 1 Time:. //.3^fiMjb M 

JB Place : , , 

CAL SHEET. TOB • (Fd^ldjir Shop) 
THI INSTRUMENT CALIBRATION RECORD 

DNIT #4 . 

ANNUAL 

TAG: TT 

; LOOP: 404B 

!• DRSCRIPON; TC TRANS 

SERVICE: TC GAS OUTLET 

LOCATION: KAPC 

LP-SHT: 

PSblD: P016 

REMARKS: W/GAS CLEANING TRAIN 

INSTL-SMKS: 

3PHC-RMKE: 

S/N: 

MANUFACT: MOORE 

' MODEL: T1Y/K2-0-1-4-20MA 

SCALE: 07 1500 deg F 

CAL'IR-IN: Type K TC 

CALIB-QUT; 4-20 MADC 

PROCESS-SP: 

INST-SP: 

ACTION; 

I/O NUMBER: HI:115 

CALIBRATION NOTES 

Use col d junctio n compensated thermocouple calibrato r t o 

inpu t a temperature signa l o f 200 deg F. and 1,000 deg.F. a t 

inpu t o f transmitter , the n verif y thi s singl e i n contro l 

room, 

See Manufactures literatur e fo r detaile d instructions . 

Fil l ou t and affi x a new calibratio n sticlter . 

INPUT VALUE 

D 

CALIBRATION REPORT 

Before Cs.li~bra.tion 

INSTRUMENT READING 

?.qo° 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Conments: t^O CaU QJrATlOlO NttOtzQ 

Performed by: Date: (f~l"7~Q ?lime : // '^ IfrffiJpM 

JB P i ace : 

CALSHEET.MDB (Field or Shop) 

I 
TAG: 

LOOP: 

DESCRIPON: 

. SERVICE: 

LOCATION": 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-RMKS t 

SPEC-RMKS: 

S/N: 

W I INSTRUMENT CALIBRATION RECORD 

OMIT #4 

ANNUAL 

FT 

53 9A 

dp Transmitte r 

STACK FLOW 

FLD 

559 

F01S 

FSE averagin g pito t tube 

Eas t sid e of'Stac k 

1222931 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP: 

INST-S-P: 

ACTION: 

I/O NUMBER: N00l;0093 

Automation Servic e 

11S1DR2F22B3 

OKI. 73 i n wc 

0-£5r00Q ACFM 

4-20 MADC 

CALIBRATION NOTES 

lb/fogCALIBRATION REPORT 

jfs Before Calibration / J , v J 

~ After Calibration / j, ^ 

17-3 2JOJ> 

CALIBRATION SOURCE REFERENCE 

Comments': 

Performed hy:, fe*--^T7^/ Data: 12--r?^1 Time: f'foaOjQj PM 

J B Place : , _ 

CAXiSHEET.WDB {Fiel d osf Bhopf1 
TAG: 

LOOP : 

) DESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-RMKS: 

SPBC-RMKS: 

S/N: 

TWI INSTRUMENT fCALIBRATION RECORD 

UNIT #4 

ANNUAL 

FT 

559B 

dp Transmitte r 

STACK FLOW 

FLD 

F018 

PSE averagin g pito t tube 

Nort h sid e o f Stac k 

1222931 

MANUFACT: 

MODEL; 

SCALE: 

CALIB-IN": 

CALIB-OUT: 

PROCESS-SP; . 

' INST-SP: 

ACTION: 

I/O N0MBBR: NODI:0093 

Automation Servic e 

11S1DR2F22B3 

0-1.73 i n wc 

0-55,000 ACFM 

4-20 MADC 

CALIBRATION" NOTES 

"OTTrXDTtrr 

INPOT VALUE INSTRUMENT READING" 

. Q Before Calibration • ^-/.(3 ^ jf -

)r?3 " Ui- C A 

Q , After Calibration ^ Q ^ 

)~H> ~~ ~ 2.0.0 ^ A 

C&T.TBRaTTnW RODRCE REFERENCE 

Comment $ • 

Performe d by; • Date: Time:, woo 

JB Place : ^T^. 

CALSHEET.WDB (Fleld\>r Shop) 
Ttf l INSTRUMENT CALIBRATION RECORD 

TAG: 

LOOP: 

.'• DESCRIPOST! 

SERVICE: 

LOCATION": 

LP-SHT; 

P&ID: 

REMARKS: 

INSTL-RMKS: 

E3&EC-RMKS: 

S/N: 

UNIT #4 

ANNUM. 

FT 

425 

MAC METER 

X-18 DIL SLURRY 

WAPC 

425 

F016 

W/GAS CLEANING TRAIN 

MANUFACT: 

MODEL; 

SCALE: 

CALIB-IN: 

CALIB-OUT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: Nl:112 

Fische r & Forto r 

14 7 5EN0 9 PL2 9KDHCACL 

Q-20 GPM 

0-20 GPM 

4-20 MADC 

Flus h proces s piping , connect water hose to upstream sid e o f 

flo w meter. Se t contro l system t o appropriat e contro l rate , 

and rea d totalizer , flo w water int o a container ' and compare 

t h e toltalise r readin g t o th e measured amount in' container . 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker . 

-0.1 lb/h r 

CALIBRATION REPORT 

INPUT VALUE "•1T3ETRIJMENT READTJIG 

- i Before Calibration ^ i 

r 3 GCL\ Q. Qr<. 

Afte r Calibratio n 

CALIBRATION SOURCE REFERENCE 

Performed > j A ,« > x_f^Q ^&A.i3<Xy^-> pat e -.[2^1 "C^j Time: 

J B Place : V',-eJg^ 

CALSHEET.WDE (Field o r Shop) 
TWT INSTRUMENT CALIBRATION RECORD 

TAG: 

LOOP: 

1 PESCRIPON: 

SERVICE: 

LOCATION: 

LP-SHT: 

P&ID: 

REMARKS: 

INSTL-RMKS: 

SPEC-RMKS: 

S/N: 

UNIT #4 

ANNUAL 

FT 

426 

MAG METER 

D IL SLURRY 

WAPC 

426 

F0I6 

W/GAS CLEANING TRAIN 

Siz e 1: o r 25mm 

MANUFACT: 

MODEL: 

SCALE: 

CALIB-IN: 

CALIB-OOT: 

PROCESS-SP: 

INST-SP: 

ACTION: 

I/O NUMBER: N i : 11-3 

Fische r & Porte r 

10D1475C 

0-20 GPM 

0-20 GPM 

4-20 MADC 

CALIBRATION NOTES 

Flus h proces s piping , connec t water hose to upstream sid e o f 

flo w meter. Set contro l syste m t o appropriat e contro l rate , 

a nd rea d totalizer , flo w wate r int o a containe r and compare 

t he toltali^e r readin g t o th e measured amount i n container . 

See Manufacture s literatur e fo r detaile d instructions . 

Fil l out and affi x a new calibratio n sticker * 

0,1 lb/h r 

INPUT VALUE 

Before Calibrat e ox; 

INSTRUMENT READING 

O G 

After Calibration 

CALIBRATION SOTIRCE REFERENCE 
mWEHMX UNIT#4 [CMSTask IC4Q32) PAGE 11 OF 3 • 

^$SJJ|fJ>E B C.yX-?---- • FAf L 

1 TSUI [-3H5 KILN HIGH IUGI f 

2 T3HH-3T7 SC C HIGH HIGH 

3 PAHH-300 KIF.N HIGH PRESSURE 

4 PAHH-324 EC-C HIGH PRESSURE ^ 

B TAMM0 4 TEMPERING CHAMBER HIGH 'lEMP. 

7 VIOLATION OPACITY! IIGU INSTANTATEOUS i 

8 PROCESS MONITOR FAILED 

3 WASTE FEE D MONITOR FAILED 

12 VIOLATION STAC K FLOW HIGH 1 MIN ^ ~ 

13 VIOLATION y£AC~3t6 (TRV) OPHN ' ~- -

14' VIOLATION ZAG-DZS SURGE VENT OPE N ^ 

, -; : 1 5 UA^5 7 ANALY^ R 

UA-553 ANALYZE R FAiL CO ' -, X~ 

17 UA-56Q-ANALYZER FAiL 02 

15 UA-562 ANALYZE R FAIL HC ; y 

19 PDAL-5S3 LO W DELTA P. (ID FAN FAiLJKE) ^ 

2D WFD-OFF CARBON INJECTION SYSTEM FAtlJ-.D ' ^ 

21 PEL-10Q/P5L-200 SCC COMB. AIR FA N FAILED '"' 

23 FSL-209 X-14 PRIOR Y FUEL LOW PRESS , (ONLY APPLICABLE FOR #2 FUEL OIL). y 

25 STACK FLOW HIGH INSTANTANEOUS ' 

35 VIOLATION SC C TEMP. LOW 1 MIN AVERAG E ' . 

3 5 VIOLATION KILN TEMP. LOW \ MfN AVERAG E 

37 WFD-OFF HC L HIGH 1 MIN AVERAG E 

38 WFD-OFF OPACITY HIGH \ MIN AVERAG E ^ 

39 WFD-OFF C O HIGH 1 MIN AVERAGE ^ 

%] .' b WFD-OFF-HC (THC) HIGH 1 MFN AVERAG E " 

41 WFD-OFF BAGHOUSE DELTA P HIGH 1 MIN AVERAG E . 7 
'WEEKL Y U N IT #4 

isrri r-EKD CUT-OF F 

(CMSTssfc IC4032) PAG t 2 OF 3 

PASS FAIL 

4 2 WFn-OF F SPA OUTLET HIGH TEMP. 1 MIN AVI-1iAGE 

4 3 WFD-OFF OXYGEN (02) LOW 1 MIM AVERAGE ' 

4 4 VIOLATION HCL HIGH 1 HOUR AVERAGE 

40 V301.ATiON C O H \G H 1 HOUR AVERAGE; 

4-6 VIOLATION SC C TEMP, LOW 1 HOUR AVERAGH 

4 7 WFD-OFF KJLN TEMP . LOW 1 WW AVERAG E 

4 5 VIOLATION OPACITY HJG.H -190 SEC/HOUR 

4 9 WFD-OFF BAGKOU S E D ELTA P LOW 1 Ml H AVERAG E 

5 2 Bag Leak Detection System (Tribe) 

S 5 Pumpable 1 Hour Roiling Total OPL 

6 6 Non-Ptimpable 1 Hour Rolling Total OPL 

<J7. I<M.Waste1.H ^ 

' J BTU 1 Hour Total OPL 

5 3 CL1 2 Hour Rolling Total OPL 

70 Low Viotatlle 12 Hour Rolling tola! OP L 

71 Semi VlolalSte 12 Hour Rolling Total OPL 

72 Mercury 12 Hour Rolling Total OPL 

7 3 Ash 1 2 How Rolling Total 0 PL 

74 PC C Temperature 1 Hour Rolling Average Low OPL 

7 5 SC C Temperature 1 Hour Rolling Average Low OPL 

76 SDA Outlet Temperature 1 Hour Rolling Average High OPL 

77 Bagrtouse Dffferential Pressure 1 Minute Average Low OPL ' 

75 Bagftfju&e Differential Pressure 1 Minute Average .Hfgh OPL 

79 Stack HCL Corrected 1 Hour Roiling Average High OFL 

60 Stack C O Corrected .1 Hour Rolling Average High OPL 

'; • .I Stack Flow 1 Hour Rolling. Average High OPL 

82 Hrt CWra Lime Flow 1 Minute Average OPL 

X" 

7 
BIWhEKLY UN IT iPi 

E FEED CIJT-Ol'h' 

CHECKSHEE T PAGE 3 OF 3 

50 WASTE FEED CUT-OFF TEST BY OPERATOR 

UNIT' #4 OPERATOR TO CLOSE MANUAL HAND VALVE AT LIQUID INJECTOR BEFORE FLEX LIME & AIR I INF, TO 

SCRfi F.NED FEEDE R XV-013 SLIDE GATE. 

UNIT #4 OPERATOR TO VERIFY CUT-OFF BY PRESSING EACH START BUTTON. 

(THEN INITIAL S SIGNSHEET) 

SHREDDED 

X-10 

SCREENED^ 

X-11 

MAIN CONVEYOR AUX CONVEYOR 

. X-12 X-22" 

VERF Y ATOMIZING AIR ALARM BY MANUALLY SHUTTING AJR TO PRESSURE SWITCH. 

(NOZZEL MUST BfjOPE N FOR ALARM TO FUNCTION} 

X-11 X-12 X-22 

A! SO CHECK OPERATION OF RAM COOLING WATER LOW FLOW Al AR M (MSG#>27G) 

CHECKE D BY : ^ 3 QL I 

83 Lime Slurry Densffy Low 1 Hour Rolling Average Shpufdown 

' '' \ LOG CHECKS IN OPERATIONS BOOK. 

85 ROD OUT KILN PRESSURE LjNE (PT^QD) 

COMMENTS ; 

CHECKE D BY : 

APPROVED BY : 

\ t \ R rltlQxU "SO. t /ds • Date: iO'^~CP( Time: 3'^~ > ^T<gM> 

He A^/H ^ Place: Control Room 

BIWEEKLY_4 

9/10/07 HK 
WEEKL Y UWET#4 (CMS Tosk IC4Cf32) PAG E 10 F 3 

'^IET^E P 9yt9f f ^ -^- ^ - . _PASS_ 

1 TSHI 1-305 KILN HIGH HIGH ^ _ 

2 TSHH-317 SC C HIGH HIGH ^ 

•3. PAHH-300 KILN HIGH PRESSUR E 

13 VIO LATION ZA0 3 16 (TRV) OPE N 

4 PAHH-324 SC C HJGIJ PRESSUR E ^ 

6 TAHH^}D4TEMPER1MG CHAMBER HIGH TEMP ^ 

7 VIOLATION OPACFfYHIGH INSTAhFTATEDUS , • f 

8 PROCES S MONFTOH FAILED 7 

9 WAST E FEED MONITOR FAILED 

12 VIOLATION STACK FLOW I UGH 1 MIN 

14 VIOLATION 7A C 026 SURG E VENT OVEN /*__ 

45 4JA^ 7 ANALYSE R RAIL44CI.. 

(6 UA-55E ANALYZER FAIL CO '• , 

17 UA-5GD ANALYZER FAILG2 . f" 

1fi UA-562 ANALYZE R FAIL HC ' 7 

19 PDAL-5S3 LOW DELTA P. (IP FAN FAILURE) 7 

20 WFD-OF F CARBON INJECTION SYSTEM FAILED / 

£1 PSMGQ/PSL-20 D SC C COMB. AIR FAN FAILED • 

23 PSL-Z09 X-t4 PRIMARY FUEL LOW PRltSS, (ONLY APPLICABLE FOR #2 FUEL OIL) 

STAC K FLOW HIGH INSTANTANEOUS _.Xf , 

35 VIOLATION SC C TEMP, LOW 1 MIN AVERAG E . 7 

35 -'VIOLATION KILN TEMP. LOW 1 MIN AVERAG E ^ ' 

37 WFD-OF F HC L HIGH 1 MIN AVERAGE 

33 WFD-OF F OPACITY HIGH 1 MLN AVERAG E i 

,.39 WFD-OF F C O HIGH 1 MIN AVERAG E 

' -fO WFD-OF F HC (THC) HIGH 1 MIN AVERAGE " S\_ 

41 WFD-OF F BAGHOUSE DELTA P HIGH 1 M)N AVERAG E . C 
BlWtEKLY UNFT #4 [CMS Task SC4032) PAG H 2 OF 3 

^^£FE^qjr-QFF _ _r .-==— w. i,-= ^ ^====== = ^£^L^- = 

42 WFD-0FF SDA 0UTLET HIGH "E EMP. 1 MIN AVF: RAGE ^ 

43 WFD-OFF OXYGb'N (Q2) LOW 1 MIN AVERAG E ^ 

44 VIOLATION HCL HIGH 1 HOUR AVERAGF - 7 

4 5 VIOLATION CO HIGH 1 I [OUR AVERAGE ^ 

4E VIOLATION SC C TEMP. LOW 1 HOUR AVERAGE"! ^ 

4 / WrD-OFF KILN TL'MP. LOW

 ;1 ISOTAVfcKAGE f 

4H VIOL A'liON OPACITY HIGH 480 SEC/HO!JR 7 

40 WFD-OFF BAGHOUSE DELTA P LOW t MIN AVERAGE X 

52 Rag Leak • election System (Tribe) / 

$5 Pumpable 1 Hour Rolling Total OPL / 

jv.; - - y 

56 Non-Pumpablel Hour Rolling Total OPL--" ^ ' ^ - '-, • 

*$7- T^.Wa^..l.Hni^.J3£iaitJ.TjQtai..QPL I 

J8 BTU 1 Hour Total OPL • 7 

69 CL12 Hour Railing Tote! OPL , f 

70 Low Volatile 12 Hour Rolling Total OPL 

71 Semi Vtolatiio 12 Hour Rolling Total OPL 7 

7 2 Mercury 12 Hour Ro Iting Total OPL ' ^ 

73 Ash 1 2 Hour Rolling Total OPL ^ 

74 PCC Temperature 1 Hour Rolling Average Low OPL ' ^ 

75 SCC Temperature 1 Hour Rolling Average Low OPL 

7fJ SDA Outlet Ternperaturci 1 Hour Rolling Average High OP L " 

77 Baghouse DEfferentusI Pressure 1 Minute Average Low OPL 

73 Baghouse DifferontjRl Pressure 1 Minute Average High OPL • 

7$ Statk HC L Corrected 1 I lour Rolling Average High OPL ^ ' 

.. SO Stack C O Corrected 1 Hour Rolling Average High OPL ^ 

j'1 Stack Flew 1 Hour Rolling Average HTgh OPL 

fl2 Hit Cl/Hra Ume Flow 1 Minute Average OP L S . 
WEEKLY UN IT #4- CHEC K SHF.ET " l-'AGE 3 OF 3 

. '^T E Fl-liU CUT-OFF _ : ; 

50 WASTE FEED CUT-OFF 1 EST BY 0 PERATOR 

UNJT#4 OPERA 1 OR TO CLOSE MANUAL HAND VALW? AT LIQUID INJECTOR BEFORK FLEX LIME & AIR I .INE TO 

SCREENE D FEEDER XV-DT3 SLIDE GATE. 

UNff* 4 OPERATOR TO VERIFY CUT-OFF BY PRESSING EACH START BUTTON. 

fTi I EN INITIAL & SIGN SHEET) 

SHRfcDDED S SCREENE D MAIN CONVEYOR ^ AU X CONVEYOR 

X-10 X-11 X-12 y X-22 

VEERIFYATOMiZlNG AIR ALARM BY MANUALLYSHU1 TING AIR TO PRESSURE SWITCH. 

(NOZZEL MUST BE OPEN FOR ALARM TO FUNCTION) 

X-10 ^ X-11 ^ X-12 ^ . X-22 ^ 

ALSO CHEC K QPEROTK3N OF RAM CODUJjIGfWATER LOW FLfi W ALARM [MSGS >278> 

CHECKE D BY : V Vwj-dX^. T 0 ^ KL\ 5 

S3 LimeSlurryDensity Lew 1 Hour Rolling Avonagfi • Shoubdcwn 

;A LOG Ci IEGKS IN OPERATIONS BOOK. 

85 ROD OUT KJLN PRESSUR E LINE (PT-300) 

COMMENTS: • 

CHECKE D BY : 

APPROVE D J3Y: Place: Control Room 

BtWEEKLY_4 

9/10/07 HK 
Si' -

. (UNIT #4 (CMS Task 104032) PAGE 1 OF 3 

1 TSJIH-3DliJ<n.M NIGH HIGH 

2 TSHH-317 SC C HJGH HfGH 

3. PAHH-300 KILN HIGH PRESSUR E 

4 PAHH-324 SC C HIGH PRESSUR E 

•6 ' 7A1-II-M04 TEMPERING CHAMBE R HIGH TEMP 

' 7 VIOLATION OPACITY H1GIIJNSTANTATEOUS 

B PROCESS MONFTOK FAILED 

9 WASTE FEE D MONITOR FAILED 

12 VIOLATION STAC K FLOW \ UGH 1 MIN 

7 

1 3 VIOLATIO N ZAC-31 6 (TRV ) OPE N ' ( y 

1 4 V|O I ATI O N ZAC-D2 6 SURG E VEN T OPE N 

1 5 UA-55 7 ANALYZE R FAiL HCL _ .. _ 

_.: UA-5S B ANALYZE R FAI L C O ' - i 

17 UA-SS O ANALYZE R FAI L 0 2 

1 8 UAH56 2 ANALYZE R FAI L H C ; y 

1 &' PDAL-5G3 LO W DELTA P_ (ID FAN FAILURE) 

'7,0 WFD-OFF CARBO N INJECTION SYSTEM FAILED 

r .i 

21 PSL-1D0/PSL-2DQ SCC COMB, AiR FAN FAILED ' '" S 

£3 PSL-209 X-14 PRIMARY FLIEL LOW PRESS. (ONLY APPLICABLE FOR #2 FUEL OJL) 

25 STAC K FiJUW HIGH INSTANTANEOUS 

35 VIOLA' RON SC C TEMP. LOW 1 MIN AVERAGE 

3(3 VIOLATION KILN TEMP. LO W 1 MIN AVERAGE 

37 WFD-OFF HC L HIGH 1 MIN AVERAG E 

38 WFD-OFF OPACITY HIGH 1 MJN AVERAG E 

39 WFD-OFF C O HIGH 1 MfN AVERAG E 

7 

7 

/ 

\.. •••• WFD-OFF-HC (THC) HIGH 1 MIN AVERAG E 

41 WFD-OFF BAGHOUS E DELTA P HIGH 1MIN AVERAGE 

Z . 
» ^FtE^UT-OF F ^ _ ^ 

42 Wr-D-OFF SDA OUTLF1 ' HIGH 17':MP- i MIN AVERAGE 

4 3 WFD-OFF OXYGE N [02) LOW 1 MiN AVERAGE 

A4 VIOLATION HCL HIGH 1 HOUR AVERAGE 

4 5 VIOLATION CO HIGI11 HOUJ? AVHliAC ^ 

4 6 • VIOLATION SCC TEMP . LOW 1 1IOUR AVERAGE 

4 7 WFD-OFF KILN TEMP'.' LOW 1 IWfff AVERAG E 

4H VIOLATION OPACFIT HiCH 430 SEC/HOUR 

49 WFD-OFF BACHOU^ E DELTA P LOW 1 MIN AVERAG E 

3 2 Bag Leak Detection System (Fri bo) 

55 Pumpable 1 Hour Rolling Total OPL 

56 Non-PurapabSe 1 Hour Kolling Total OPL 

f}7 Total Waste 1 I lour Roiling Total OP L 

(i'M5 Tack 1040:52) PAGE 2 OF 3 

PASS 

74 PC C Temperature 1 Hour Roiling Average Lnvt OPL 

75 SC C Temperature 1 Hour Rolling Average Low OPL 

76 SDA Outlet Temperature 1 Hour Rolling Average High OPL 

77 Baghouse Differential FTOSKIPG 1 Minute Average Low OPL' 

78 Baghouse Differential Pressure 1 Minute Average High OPL 

70f Stack HCL Corrected 1 How Rolling Average High OPL 

SO Sfacfc CO Coirected 1 Hour Rolling Ave?t*ye High OPL 

'' iv Stack Flow 1 Hour Rolling Avefago I llrjh OPL 

B2 Hrt Cl/Hra Lime Flow 1 Minute Average OPL 

/ 

• • BTU 1 Hour Total OP L - r ^ 

m CL 12 Hour Rolling Tnfai OPL 

7 0 Lov/Vlolatiic.12; Hour Rolling Total op l 

71 Semi Violatile 12 Hour Rolling Total OPL _ 

' ' ' / 

72 Mercury 12 Hour Rolling Total OPL . X 

Z " 

73 Ash VZ Hour Rolling Total OPL -7^ 

r 

7, 
.( !JW!'#4 

,\ Pi 1-iD CUT-OFF 

CHECKSHEE T PAGE 3 OF 3 

50 WAbTF FEED CUT-QFF TEST BY OPERATOR 

UNIT 1t4 OPERATOR TO CLOSE MANUAL HAND VALVE AT LIQUID INJECTOR BEFOR E FLEX LM~. & AIR LINE TO 

SCREENED FEEDE R XV-Ot 3 SLIDE GATE. 

UN IT #4 OPERATOR TO VEIN FY CUT-OFF BY PRESS I NO EAC H START BUTTON. 

O'HEN INITIALS SIGN KHEEl ) 

• 'SHREI3DF.D ffafa^ SCRTENF-D S^/V MAIN CONVEYOR AU X CONVEYOR !^V?X _ 

X-10 ^J^-^W- - x-11 ^h^f^-^ X-12 H*^'— - x-22 '?i--^ri^2^_ 

VERJF Y ATOMIZJKG AfR ALARM B Y MANUALLYS J JUTTING AIR TO PRESSURE SWJTCH . 

(NOZZEL MUS T BE OPE N FO R ALAR M TO FUNCTION ) 

ALS O CI lECK OPERATION OF RAM COOLING WATER LOW FLOW ALAR M (MSGS >?J$) 

CHECKED BY : 

53 Lime Slurry Density Low 1 Hour Rolling Average Shoutdcwn 

L OG CHECKS IN OPERATIONS BOOK. 

85 ROD OUT KILN PRESSUR E LINE (PT-300) 

COMMENTS: 

CHECKE D BY : Date: / / 

APPROVED PY: Place: Control Roam 

BfWEEKLY_4 

9/10707 HK 
^ IWEEKLY UN IT #4 (CMS Task K >W32) PAOE 1 OF 3 

\&TE FEED OU T-OFF PASS 

1- TSFiH- 305 KILN HIGH HIGII 

2 TSHH-3-17SCC HIGH HIGH 

3 PAHIk^OG KILN HIGH PRESSUR E ./ ^ 

4 PAHH-324 SC C HFGI f PRESSUR E 

6 TAHH- 404 TEMPERING CI I AMBE R HIGH TEMP 

7 VIOL ATPON ORACH YHIG H INSTANIWTEQUS 

H PROCES S MONITOR FAILED 

9 WAST E FEE D MONITOR FAILED 

12 VIOLATION STAC K FLOW HIGH 1 MiN 

13 VIOLATION ZAC-316 (TRV) OPE N 

14 VIOLATION 7AC-Q26 SURG E VEN T OPEN 

.15 UA-GS7 ANALYZER FAIL HCL_ 

' J UA-5SR ANALYZER FAIL CO. •, 

17 UA-5B0 ANALYZER FAIL OZ 

18 UA-5S2 ANALY^ R FAIL HC 

19 PDAL-563 LO W DfcLTA P. (ID FA N FAILURE) 

' 2 0 WFD-OFF CARBO N INJECTION SYSTE M FAILED 

21 PSL-^100VPSL-20D SC C COMB, AIR FAN FAILED

 ; r 

23 FSL-209 X-14 PRIfMRY FUEL LO W PRESS. (ONLY APPLICABLE FOR #2 FUEL OIL^ 

25 STAC K FLO W HIGH INSTANTANEOUS 

35 VIOLATION SC C TEMP. LOW 1 MIN AVERAGE . 

35 -VIOLATLON KILN TEMP. LOW 1 MlN AVERAGE 

37 WFD-OFF HC L HIGH 1 MIN AVERAG E ^ 

33 WFD-OFF OPACITY HIGH 1 Ml W AVERAG E ' x / f 

39 WFD-OFF C O HIGH 1 MIN AVERAGE: • 

• WFD-OFF-H C (THC) HtGH 1 MIN AVERAG E ' 

41 WFD-OFF BAGHOUSE DELTA P HIGH iMI N AVERAGE .3 • 
BIWEEKLY UNIT M (CMS Task IC4032) PAGE 2 OF 3 

^fEn'Fi^LJT^Pr ^ _ = ^ = __ .. c = = „ = . c ....^ = _ =.„._„_

PAS S 

•12 WFD-OFF SDA OUTLET HIGH TEMP, 1 MIN AVERAGE ./ ^ i 

4 3 WFD-OFF OXYGE N (02) LOW 1 MIN AVERAGE ^/ ^ 

4 4 VIOLATION IJCLH3GI11 HOUR AVERAG E 

45 VIOLATION CO HIGH 1 HOUR AVERAG E 

46 "VI OtAHON SC C '1 E M P. LO W 1 H OUR AVERAG E 

47 WFD-OFF KILN TEMP- LOW T fJlflS AVERAGE y 

43 VIOLATION OPACITY HIGH 480 SEC/HOUR 

m WFD-OFF BAGHOUSE DELTA P LOW 1 MJN AVERAG E 

52 Bag Leak Detection System (Tribo) 

65 Pumpable 1 Hour Rolling Total OPL 

65 Non-Pompable 1 Hour Rolling Total OPL 

^.....Xofc^Wa^.! ^ 

. A D'i'U 1 Hotir-Tofal OF L 

69 CL1 2 Hour Rolling Total OPL - . ^ 

70 Low Viokflle 12 Hour Rolling Total OPL 

71 Seml Violstfle 12 Hour Rolling Total OPL 

72 Mercury 12 i lour Rolling Total OPL 

73 Ash 12 Hour Rolling Total OPL 

74 PC C Temperature 1 Hour Rolling Average L3w OPL , 

75 SC C Temperature 1 Hour Rolling'Average Ltnv OPL 

75 SDA Outlet Temperature 1 Hour Rolling Average High OPL 

77 • Baghouse Differential Pressure 1 Minute Average Lowf OPL" 

7B Baghouse Differential Pressure 1 Minute Average High OPL . 

73' Stack HCL Conrect-ed 1 Hour Roiling Average High OPL 

.. BO Stack C O Corrected 1 Hour Rolling Average High OPL 

V J1 Stack Flow 1 Hour Rolling Average High OPL 

£2' Hrl Ci/Hra Limo Row 1 Minute Average OPL _ 
"* WEEKLY UNFT #4 CHECK SI <r-[-T PAG E 3 OF 3 

ASTE FEED CUT-OFF^ ^ _t ^ „ ;,_„__^_ = 

so WAST E FEE D cur-orFr TES T BY OPERATO R 

UMFT #4 OPERATOR TO CLOSE MANUAL HAND VALVE AT UGUJD INJECTOR BEFORE FLEX I.IME & AIR LINE TO 

SCREWED FEEDER XV-O-H SLIDE GATEUNIT #4 OPERATOR TO VERIFY" CUT-OFF EY PRESSING EACH STAR T BUTTON. 

(THEN INITIAL & SIGN SHEET) 

SHREDDED SCREENED MAIN CQNVI=YOR AUXCOtfv/EYQR 

X-10 \Ff • X-11 \Py^ X-12 CT^ T X-22 V/ ^ 

~ r 

VEPJFY" ATOMIZIMG AI R ALARM BY MANUALLY SI JUTTING AIR TO PRESSURE SWITCH. 

(NOZZEL MUS T BE OPEN FO R ALARM TO FUNCTION) 

x-10

 v 7 ? r

 x-11 VA ' x-12 x-22 VT^. . 

ALS O CHECK OPERATJ O N O F RAM COOLING WATER LO W F LO W ALARM (MSG* >27B) 

CHECKED BY : 

B3 Lime Sfuny Density Low 1 Hour Rolling Average Sriouldown 

V LOG CHECKS IN OPERATIONS BOOK! 

85 ROD OUT KiLN PRESSUR E UN E (PT-300) 

COMMENTS: 

CHECKED BY: f ^ t ^jf i ' P a te://:/?-Q l Time: 7.' S O AM <PM ^ 

APPROVED 0Y : /J^r^^ O Place: Corrtrol Room 

BIWEEKLYj l 

9/10/07 HK 
"~R i WEEK! ,Y U NIT #4 (CMS Task lt>1032) ' PAG E 1 OF 3 

"-•xmSTF. FEED CUTOF F PASS 

1 TSI-f] L-3DS KILN HIGH HfGH 

?. TSHH-31T SC C 1IIGH HIGH 

3 PAHH-300 KILN HJGH PRESSUR E S 

4 PAHH-324 SC C HIGH PRESSUR E / 

6 TAHM- W TEMPERING CI (AMBER HIGII TEMP ' X 

7 V30LATION OPACIIYHI6H I^^STA^F^ATEOUS 

8 PROCES S MONJTOR FAILED' ^ 

9 WASTE FEE D MONITOR FAILED ^ 

XI VIOLATION STACK FLOW HIGH 1 M!M 

13 VIOLATION ZACXJlti (FRV) OPE N X 

14 VtOI-ATtON ZAC- 025 SURGE VEN T OPE N ' S~ 

, 4 5 UA-6S7.AWALYZEREAiLl.LCL X . 

•16 UA-55S ANALYZER FAIL CO ; _ f 

17 UA-S80 ANALYZER FAIL 0 2 

1& UA-5B2 ANALYZER FAIL H C 

19' PDAL-5S3 LOW DELTA P. (ID FAN FAILURE) / 

20 WFD-OFF CARBON INJECTION SYSTE M FAILED 

21 PSL-10D/PSI--2DQ SCC COMB. AIR FAN FAILED 

23 PSL-209 X-14 PRIMARY FJF L LOW PRESS . (ONLY APPLICABLE FOR #2 FUEL OIL) 

25 STACK FLOW HIGH INSTANTANEOUS 

35 VIOLATION SC C TEMP, LOW 1 M IN AVERAG E 

33 VIOLATION KILN TEMP, LOW 1 MIN AVERAG E 

.37 WFD-OFF HCL IIIGH1 MiN AVERAG E 

3B WFD-OFF OPACITY HIGH 1 MIN AVERAG E 

39 WFD-OFF CO" HIGH 1 MIN AVERAG E 

; WFD-OFF-HC rJHC) HIGH 1 MIN AVERAG E 

41 WFD-OFF BAGHOUSE DELTA P HIGH 1 MIN AVERAGE . X 
'I WEEKLY UNIT #4 

,:*STT; FEED CUT-UFF 

(CMS Task IC4032) PAGE 2 OF 3 

PASS FAJL 

42 WFD-OFF SDA OUTLET HIGH TEMP. 1 MtN AvHiAG E 

4 3 WrD-OFF OXYGE N (02) LOW 1 MIN AVERAG E 

4 4 VIOLATION HOL HIGH 1 HOUR AVERAG E 

4 5 VIOLATION C O HIGH 1 HOUR AVERAG E 

46 VIOLATION SC C TEMP. LOW 1 HOUR AVERAG E 

4 7 WFD-OFF Kl LN TEMP. LOW 1 Km AVERAG E 

4& VIOLATION OPACIT Y HIGH 4flD SEC J TIOU R 

49 WhD-OFF BAGHOUS E DELTA P LOW 1 MtN AVERAGE " 

57, Bag Leak Detection System (Tribo) 

65 Pumpable 1 Hour Rolling Total OP L 

6ti iNon-Pumpabte 7 Hour Rolling Total OPL 

'.•§7. Total Waste i Hour Kotling Total OPL 

jo BT U 1 Hour Total OF L 

G9 CL1 2 Hour Rolling Total OP L 

7U Low VIolatite 12 Hour Rolling Total OPL 

71 Serni Violate 12 Hour Rolling Total OPL 

72 Mercury 12 Hour Roiling Total OPL 

73 Ash 12 Hour Rolling Total OPL 

74 PC C Temperature 1 Hour Rolling Average Low OPL 

75 SC C Temperature 1 Hour Rolling Average Law OPL 

7G SDA Outlet Temperature 1 Hour Rolling Average High OPL 

77 Baghouse Differentia} Pressure 1 Minute Average Low OPL' 

78 Baghouse Differential Pressure 1 Minute Average High OPL 

79 Stack HCL Corrected \ Hour Rolling Average High OPL 

80 Stack CO Can-Grted 1 Hour Rolling Average High OPL 

:

 Slack .Flow \ Hour Rolling Average High OPL 

62 ' Hrt CWr a Lame Flow 1 Minute Average OPL 

/ 

r 
BIWEEKLY UN FT Sf4 

.g^STF : FEED_CUl'.OFF_ 

CHF-CK SHEET PA«E 3 OF 3 

EiD WAST E FEED OUT OFF TEST BY OPERATOR 

UNIT #4 OPERATOR TO CLOSF. MANUAL HAND VAI ,VE AT LIQUID INJECTOR BEFORE FLEX LIME & AIR LiNETO 

SCREENE D FEEDJ'KXV--D13 51JDE GATE. 

UNIT iP\ OPERATOR TO VERIFY CUT-OFF B Y PRESSING EAC H START BOTTOM. 

(THEN INHIAL & SIGN SNFET) 

St IKEDDED 

X-10 

_SCRhENED_ 

X-11 

_MAIN CONVETYOli 

X-12 

A U X CONVEYOR 

X-22 

VERIFY ATOMIZING AIR ALARM BY MANUALLY SHUTTING AIR TO PRESSURE SWITCH. 

(NOZZEL MUST BE OPE N FOR ALARM TO FUNCTION) 

X-10 f XA1 S x.-12

 y X-22 S 

ALS O CHEC K OPERATION OF RAM COOUN G WA'lER LOWiFl .OW ALAR M (MSG# ^-278) 

CHECKE D BY : V . Vu r V . I QU. 3 & ^XTl S 

83 Lime Slurry Density Low 1 Hour Roiling Average 

' } LOG CI [ECKS IN OPERATIONS BOOK. 

B5 ROD OUT KILN PRESSUR E LINE (PT^300) 

Shouidowji 

COMMENTS: 

CHECKE D BY 

APPROVED BY : 

Oate:l3.—1J'6 C 3 l Time:- 1 - US (A^PW -

Place: Contro!Room 

B!WEEKLY_4 

9/10/07 HK 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

Unit # ' 4 Sedaf # 

Parameter 

02 25% 

r CO-low range 2QQppm 

r CO-hfgh range 3000ppm 

r HQ lOOQppm 

Parameter NIST Traceable Cafibration Standards 

02 25% 

r CO-low range 2QQppm 

r CO-hfgh range 3000ppm 

r HQ lOOQppm 

Gas Concentration 

Parameter 

02 25% 

r CO-low range 2QQppm 

r CO-hfgh range 3000ppm 

r HQ lOOQppm 

Low [Zero) D 0.5 

Parameter 

02 25% 

r CO-low range 2QQppm 

r CO-hfgh range 3000ppm 

r HQ lOOQppm 

• Mid S.S3 ± 

Parameter 

02 25% 

r CO-low range 2QQppm 

r CO-hfgh range 3000ppm 

r HQ lOOQppm High 15 ± D.E 

Run Number Concentration Difference 

Reference Analyzer Low High 

• 1-Low 0 0.1 -0.1 — — 

2~Mid 8.93 8.98 • — -0,05 

3-High 15 15.3 — -0.3 

4-L6w o 0:1 _ ; 

5-Mid 6.93 9 — . -0.07 — 

6-High 15 15,2 — -0.2 

. 7rLow . 0 .... . . D.1. . . -OJ . . — . ... — . . 

B-Mid 0.93 8.9 0.03 

9-Hrgh 15 15.2 — . — -0.2 

• Vlean Difference = -0.10 -0.03 -0.23 

Calibration Error = -0.40% -0.12% -0,93% 

Calibration Error - Mean Difference / Span Valne * 100 

E/l Tech 

Title 

9/22/2009 
ABSOLUTE CALIBRATION AUDIT fACA) DATA SHEET 

Unit #_ . L .. Serial # 

Parameter 

02 25% i 

CO-low range 200ppm ; 

r CO-high range 3000ppm 

r HC3 lOOOppm 

Parameter MST Traceable Cafibration Standards 

02 25% i 

CO-low range 200ppm ; 

r CO-high range 3000ppm 

r HC3 lOOOppm 

Gas • Concentration 

Parameter 

02 25% i 

CO-low range 200ppm ; 

r CO-high range 3000ppm 

r HC3 lOOOppm 

Low (Zero) Q + 10 

Parameter 

02 25% i 

CO-low range 200ppm ; 

r CO-high range 3000ppm 

r HC3 lOOOppm 

Mid 68,9 ± 10 

Parameter 

02 25% i 

CO-low range 200ppm ; 

r CO-high range 3000ppm 

r HC3 lOOOppm High 154 ± 10 

Run Number Concentration Difference 

Reference Analyzer Low Mid High1-Low 0 -0.2 6.2 

2-Mid • 68.9 667 — 2,2 — 

3-High 154 152,6 — — 1.4 

A • _n A {1.4 

u 

5-Mid 68.9 66.8 2.1 

6-High 154 154.5 — — -0.5 

. . 7-Low.. . ." . 0 .. . ..... .-0.1 0.1 — 

Mfid S3,9 67 — 1.9 — 

9-High 154 153,4 — 0.6 

Mean Difference = 

Calibration ErrorMean Difference = 0.23 2.07 0.50 Calibration Error- 0,12% 1.03% 0.25% 

Calibration Error - Mean Difference / Span Value * 100 

E/l Tech 

Title 

9/22/2009 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

: V UnJtff • 4 ' • Serial # '_

 13 2 

Parameter 

<~02 25% 

c CO-low range 200ppm 

f CO-high range 3000pprn 

r HC! 1000ppm 

Parameter NIST Traceable Calibration Standards 

<~02 25% 

c CO-low range 200ppm 

f CO-high range 3000pprn 

r HC! 1000ppm 

Gas Concentration 

Parameter 

<~02 25% 

c CO-low range 200ppm 

f CO-high range 3000pprn 

r HC! 1000ppm 

Low {Zero} • o • ± 150 

Parameter 

<~02 25% 

c CO-low range 200ppm 

f CO-high range 3000pprn 

r HC! 1000ppm 

Mid 1075,1 ± 1.50 

Parameter 

<~02 25% 

c CO-low range 200ppm 

f CO-high range 3000pprn 

r HC! 1000ppm High 2239 ± 15Q 

Run Number Concentration Difference 

Reference Analyzer Low Mid High 

1-Low. . 0 • -0.2 0,2 — — 

Z4M • 1079.1 1086,5 -7.4 — 

3-Hfgh 2289 22B7 — 2 

n .rj i Od 

5-Mid 1079.1 1077.6 — 1.5 

2289- 2317.4 — — -28.4 

7-Low 0 -0.1 0,1 — — 

8-Mld 1073,1 1077.7 • — 1.4 — 

9-High 2289 2301.9 -12.9 

Mean Difference -

Calibration Error = 

Mean Difference - 0.23 -1.50' -13.10 

Calibration Error = 0,01% -0,05% -0.44% 

Calibration Error - Mean Difference / Span Value * 100 j 

i 

E/ITech 

. Title 

9/22/2009 ; 

Date : I 
ABSOLUTE CALIBRATION AUDIT (ACA) DATA SHEET 

UnEt#

 4 Serial # 

' Parameter 

C 0 2 25% 

r CO-low range 200pprn 

r CO-high range 3000ppm 

* HCl 1000ppm 

' Parameter NIST Traceable Calibration Standards 

C 0 2 25% 

r CO-low range 200pprn 

r CO-high range 3000ppm 

* HCl 1000ppm 

Gas Concentration 

' Parameter 

C 0 2 25% 

r CO-low range 200pprn 

r CO-high range 3000ppm 

* HCl 1000ppm 

Low (Zero) D ± 50 

' Parameter 

C 0 2 25% 

r CO-low range 200pprn 

r CO-high range 3000ppm 

* HCl 1000ppm 

Mid 318 ± 50 

' Parameter 

C 0 2 25% 

r CO-low range 200pprn 

r CO-high range 3000ppm 

* HCl 1000ppm High 707 ± 

Run Number Concentration Difference 

Reference Analyzer Low Mi • High 

1-Low 0 -0,3 0,3 — 

2-MirJ 318 264.9 — '33.1 — 

3-High ' • 707 713.1 -6.1 

4-tuw 0 o 0 : 

5-Mid 316 306,2 — 11.8 

6-High 707 ' 707.1 -0.1 

7-Low 0 0,6 -0.6 — 

. 8-Mid 318 314.2 3.8 — 

9-High 707. 708:6 — — -1,6 

Mean Difference ~ -0.10 16.23 -2.60 

Calibration Error - • -0,01% 1.62% -0,26% 

Calibration Error = Mean Difference / Span Value * 100 

CE E/l Tech 
Table 1 

-Summary o£ Relative Accuracy Test Audit Hcsulte 

Veolia ES Technical Solutions 

Siiuget, Illinois 

June 22, 23 and 24,2005 

CEM S Parameter units Measured R A Criteria 

' Unit % CO ppm @ 7$ 0,004 ppm1 Pass ' Unit % 

Oj, dry 1.0"" Pass 

' Unit % 

Oj, W5t %0-z 0.l3%a t-f)"" Pltfft 

Unit 3 CO ppm ©• 7% O2 0.063 ppra3 5

 s Uni * Pass; t 3 

02, diy %0» 0.02%a .1.0 • Pass 

Unit 3 

Oj, wet. % Oa 

• 0.31%* 1.0

 w Pass 

Unit 4 CO ppm @ 7% 0 2 1,146 ppm£ Unit 4 5"* Pass 

Oi, dry %'Oi 0.15ft" 1.0'* Pass 

Unit 4 

02 s wot %02

 . 0.46%a 1.0* Pstss 

" Percent of emission standard or absolute average difference (ppm or %). 

h

Pfl4B. 

c

 PS 3. 

INCINERATOR. mj £ RAT A 

VEOU A 

5 JULY 7,20CS 

CSC Project 093-567 
Incinerator 

Data Point 

"Veofia 

KtiVitunrricntRl Services 

SausStitrilinois 

Created 

Period Stm 

Period En 

1/I/2010 6;00 AM 

1/1/2010 6:00 A M 

1/i/ZOlO 6:00 A M 

Page 5 of 7 

1 Min J. M n I Min 1 Hi- Rail 1 Hr Roll L Hr RiA: L Hr RDII 11-Ir Roll 1 Hr.RoIl 12 Hr J.2 Hr llH i 11-Ir Tot i Hr Tot t Hr Tut 

AYG- AV G AV G Warn Shut OFI-j Tot Tot Shut Tut OPL Roll Tot Roll Tut Roll Tot \V?JT. Shut OPL 

Warn Stmt OPL, Warn Warn Shu; OPT 

Carbon injection Flow 

Lime Slurry Density 

Stack Opacity 

Stack CO RCRA 

SDA Ouflet Temp 

Baghouse Diff Press Low 

Baghouse Diff Press High 

Stack TKC 

X11 Weight 

X22 Weight 

X12 Weight 

X1Q Weight 

Stack HCL RCRA 

6.6UOCOD G.2DC-000 

65.00000 

S.DtJMaO . 10.0DMQ 

450.0MK] 5Q0.O00D 

440.000Q 5DCI.U0UO 

a.naoooo Z.IJQQOOO 

9.0Q00Q0 10,00000 

s.onnooo 10.D&000 

as.5onaa 115,400m sri^ooii} 

30.QDOOO 40.tlDa00 10P.Q3QO 

429.D000 431.0000 434.00^ 

AQQ.UUQQ 500.0000 

. 900.CDOO 950.000 0 IClOQ.&Dil 

1550.0CC 1CSQ,OCa 1700.0'JO 

asQ.oofjc L'S-D.OOCD 1005.000 

lmo,ODD 1-550X00 1'C-C.00C1590.DOD ' 16S0.CU0 17C-C.00C15,00000 32.tinaao 35.PGCI1IO 
Ydotia. 

Em'h'utiraepial Services 

Sauget TJlinnifs 

4,000000 3.000000 

3P.Q0D[!n 33,5000r> 37.20000 

Stack 02 RCRA 

HGLtopme 

Shredded Weight 

Tempering Chamber Temp 8OO.0000 1200.000 

P C C Temp 

S C C Temp 

Stack CO Corrected 

Stack HCL Corrected 

Stack OZ Corrected 

Stack Fiow 

Low BTU Liquid Weight 

High BT U Liquid Weight 

Liquid Weight 

Containerized Weight 

Soirtfs Weight 

Weight 

130Q.PD3 1S40.0UD 

1850.001} 1825.000 

450.0000 500.0000 

"100.0000 150.0000 

4.OO0UUU 

asoaa.on 

1570.000 151S.003 1507.00Q 

1905.000 1B90.000 13BS,Ood 

30.00000 7E .00000 100.000(1 

SCO 0000 32.00000 

37000.00 37300.00 M O 6-3.01? 

2300.000 305D.000 325S.0D0 

1500.000 

IDtiOQ.QD 

12soo.ua iaaoo.ua I3796.cn 

Created 

Period Start 

Period Eii 

1/1/20T.0 6:00 A M 

V1/2CUG 6:00 A M 

VV20L0 6;C0 AlVl' 

13-MO.CD 14500,30 ';i"C-CD.0C1600.M0 IBS 3.ODD 1700.1] DO 

1 n no.oc-o 105O.C ao ; 1 c n,ooc 

2500,000 £750.000 30CO.OCO 

1 a aoo.ee 14000.00 15000.0c 
STU 

Chlorine 

Mercury 

Asli 

Low Volatile 

Semi Volatile 

F.uvjrnjmiejnia.1 Services 

Saugui Tlliruris 

Create*: 

Period Start 

Period En 

2S5.0000 £62,0300 

ojiamaa o,02ftOO-3 

BOOD.G0Q 0777.000 

43.00000 47. a 0000 

U1/20I0 6:0GA M 

L'l/2010 G ; 0 G A M 

b';/20lu 6:00AM 

Page 7 of 7 

. 45D30QCB 43300053 530CC300 

2&CU.-300 2503.000 3D24.QQG 4OC.0O0O 46C-.D0OO 5C0.OCC0 

g,S5t00O O.K7530O 0.31230Q 

90000.03 1000GB .0 10£324.-3 

50C.OOQO 540.00DU 5B4.00DC 

60.0 D000 64.00000 700,0000 740.D000 768.0300 


Certification Statement 

1 certify under penalty of the law that this document was prepared under my direction or 

supervision in accordance with a system designed to assure that qualified personnel properly 

gather and evaluate the information submitted. Based on my inquiry of the person or persons 

who manage the system, or those persons directly responsible for gathering the information, the 

information submitted is, to the best of my knowledge and belief, true, accurate, and complete. 

I am aware that there are significant penalties for submitting false information, including the 

possibility of fine and imprisonment for knowing violations. 

Doug Harris 

General Manager 

Veolia ES Technical Solutions, L.L.C. 

Sauget, IL 

Signature: 

1 
Notification of Compliance (NOC) 

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

40 CFR 63 Subpart EEE 

Hazardous Waste Combustor MACT Standard 

Compliance Date: June 18-25, 2012 

Owner/Operator/Title: Veolia ES Technical Solutions, L.L.C. 

Street Address: 7 Mobile Avenue 

City: Sauget State: IL Zip Code: 62201 

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

Plant Contact / Title: Doug Harris / General Manager 

Plant Address (if different than owner/operator's) 

Street Address: 

City: State: Zip Code: 

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

Air Pollutants. 
Introduction 

Veolia ES Technical Solutions, L.L.C, in Sauget, Illinois (Veolia-Sauget) operates three (3) 

incinerators: two (2) fixed hearth units (Units 2 and 3) and one (1) rotary kiln unit (Unit 4), All 

three units operate under Title V Permit Number V-IL-1716300103-08-01 issued by U.S. EPA, 

Region 5. Each incinerator is subject to the National Emission Standards for Hazardous Air 

Pollutants (NESHAPs) for Hazardous Waste Combustors (Title 40 of the Code of Federal 

Regulations, Part 63 [40 CFR Part 63], Subpart EEE), i.e., the HWC MACT. Per the 

requirements of the HWC MACT at 40 CFR 63.1207(d)(2), a Confirmatory Performance Test 

for polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofurans (dioxins/furans) must 

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

Comprehensive Performance Test. 

The previous Comprehensive Performance Test for the Unit 2 Incinerator began on December 8, 

2009, which required the Confirmatory Performance Test (CfPT) to begin by July 8, 2012, 

Veolia-Sauget commenced the Unit 2 CfPT on June 18, 2012, 

The previous Comprehensive Performance Test for the Unit 3 Incinerator began on December 1, 

2009, which required the Confirmatory Performance Test (CJPT) to begin by July \. 2012. 

Veolia-Sauget commenced the Unit 3 CfPT on June 20, 2012. 

The previous Comprehensive Performance Test for the Unit 4 Rotary Kiln Incinerator began on 

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

16, 2012. Veolia-Sauget commenced the CfPT on June 25, 2012. 

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

Table 1. 

Ta ble 1. 40 CF R 63 Subpart EEE Emissions Standards 

Parameter Limit 

Dioxins and Furans 

0.20 ng TEQ/dscm, corrected to 7% oxygen for incinerators 

with dry air pollution control system and inlet temperature to 

initial particulate matter control device >400°F; 

0,40 ng TEQ/dscm, corrected to 7% oxygen for incinerators 

with dry air pollution control system and inlet temperature to 

initial particulate matter control device <400°F. 

3 
The applicable dioxins/furans standard of the HWC MACT for Units 2 and 3 is 0.20 ng 

TEQ/dscm, corrected to 7% oxygen, and the applicable dioxins/furans standard of the HWC 

MACT for Unit 4 is 0.40 ng TEQ/dscm, corrected to 7% oxygen. These standards were met 

during the Confirmatory Performance Tests of Units 2, 3, and 4. 

Results of Confirmatory Performance Tests 

The results of the Confirmatory Performance Test are provided in Attachment 1, Final Reports, 

Dioxins/Furans Confirmatory Performance Test Report for the Unit 2 Fixed Hearth Incinerator, 

Unit 3 Fixed Hearth Incinerator, and Unit 4 Rotary Kiln dated June 2012. The Confirmatory 

Performance Test reports include: 

• The methods that were used to determine compliance; 

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

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

• The emissions of dioxins/furans, reported in units and averaging times, and in 

accordance with the test methods specified in Subpart EEE, 

Table 2 summarizes the results of the emissions sampling during the June 2012 Confirmatory 

Performance Tests of Units 2, 3, and 4. 

Table 2. Summary of HWC MACT Confirmatory Performance Test Results 

June 2012 

HWC MACT 

Standard Test Method Units Limit 

Average Test 

Result 

Unit 2 

Dioxins/Furans 

EPA SW-846 

Method 0023A 

ng TEQ/dscm, 

corrected to 7% Oz 

0.20 0.00178 

Unit 3 Dioxins/Furans 

EPA SW-846 

Method 0023A 

ng TEQ/dscm, 

corrected to 7% Oz 

0.20 0.00068 

Unit 4 

Dioxins/Furans 

EPA SW-846 

Method 0023A 

ng TEQ/dscm, 

corrected to 7% Oz 

0.40 0.195 

4 
Operating Conditions 

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

performance tests to: (i) Demonstrate compliance with the dioxin/furan emission standard when 

the source operates under normal operating conditions". "Norma! operating conditions" are 

defined as: 1) the average carbon monoxide emission level over the previous 12 months to the 

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

dioxin/furan standard within the range of the average value over the previous 12 months and the 

maximum, or minimum, allowed; and 3) chlorine feedrates at normal or greater. As such, no 

new or additional operating limits (OPLs) were established during this confirmatory performance 

test. 

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

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

mix of waste streams that were representative of typical operations were fed to the incinerator, 

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

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

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

feedrate, total pumpable hazardous waste feedrate, .stack gas flowrate, carbon injection rate (Unit 

4, only) and the total chlorine feedrate. A variance was requested and approved for the 

concentration of carbon monoxide (CO) in the stack gas to allow the operation of the incinerator 

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

to 7% oxygen. Tables 3, 4, and 5 present the results of the key parameters monitored during the 

CfPTs for Units 2, 3, and 4, respectively. 

5 
Table 3. Summary of Utjiit 2 Operations 

Operating Parameter 

i 

Units Run 1 F tin 2 Run 3 

Average 

During 

CfPT 

Target Operating 

Range 

Target 

Achieved? 

Baghouse Inlet Ter iperature (HRA) °F 405.1 A 05.2 405.0 405.1 400-420 Yes 

Primary Combusts 

(HRA) 

n Chamber Temperature op 1,750.5 1, 748.8 1,746.6 1,748.6 1,845-1,686 Yes 

Secondary Combustion Chamber Temperature 

(HRA) | °F 1,895.1 1, 895.3 1,895.0 1,895.1 1,917-1,877 Yes 

Stack Carbon Monoxide (HRA) ppmv (7% 0 2 

corrected) 0.6 1.5 1.4 1.2 0-100 Yes 

Stack Gas Flowrate (HRA) acfm 14,063.1 14 ,173.5 14,074.3 14,103.6 13,317-15,147 Yes 

Stack Oxygen Concentration % 11.3 10.9 11.2 11.1 N/A N/A 

Chlorine Feed (HRiA) lb/hr 61.2 51.7 61.2 61.4 36.0-218 Yes 

Pumpable Waste Feed (HRA) 

i 

lb/hr 1,950.9 1 967.2 1,972.7 1,963.6 1,571-3,107 Yes 

Total Waste Feed (jHRA) lb/hr 2,173.6 2 189.5 2,188.1 2,183.7 1,761-4,017 Yes 

! 

HRA - Hourly Rolling Average 
Table 4. Summary of Unit 3 Operations 

Operating Parameter Units Run 1 B .un 2 Run 3 

Average 

During 

CfPT 

Target Operating 

Range 

Target 

Achieved? 

Baghouse Inlet Temperature (HRA) op 406.3 4 05.3 404.5 405.4 399-420 Yes 

Primary Combustion Chamber Temperature 

(HRA) ! °F 1,784.6 1, 785.8 1,793.2 1,787.9 1,865-1,686 Yes 

Secondary Combustion Chamber Temperature 

(HRA) I 

a

F 1,905.1 1, 305.0 1,905.1 1,905.1 1,913-1,877 Yes 

Stack Carbon Monoxide (HRA) ppmv (7% 0 2 

corrected) 0.0 0.0 0.0 0.0 0-100 Yes 

Stack Gas Flowrate (HRA) acfm 14,303.1 14 ,347.8 14,051.4 14,234.1 13,499-15,147 Yes 

Stack Oxygen Concentration % 12.8 12.9 13.1 12.9 N/A N/A 

Chlorine Feed (Hl|A) lb/hr 55.1 56.0 61.0 57.4 37.5-218 Yes 

Pumpable Waste Feed (HRA) lb/hr 1,962.8 1, 957.0 1,913.6 1,944.5 1,562-3,107 Yes 

Total Waste Feed (HRA) lb/hr 2,202.9 2. 180.1 2,1.22.3 2,168.4 1,768-4,017 Yes 

HRA - Hourly Rolling Average 

7 
Table 5. Summary of Uriit 4 Operations 

Operating Parameter Units Run 1 P <un 2 Run 3 

Average 

During 

CfPT 

Target Operating 

Range 

Target 

Achieved? 

Baghouse Inlet Temperature (HRA) = F 389.8 3 89.8 389.8 389.8 384-400 Yes 

Primary Combustion Chamber Temperature 

(HRA) 

op 1,668.9 1, 569.2 1,717.3 1,685.1 1,865 - 1,499 Yes 

Secondary Combustion Chamber Temperature 

(HRA) i 

op 1,898.4 I, 901.0 1,902.2 1,900.5 1,917-1,886 Yes 

Stack Carbon Motjoxide (HRA) ppmv (7% 0 2 

corrected) 0.1 0.1 0.1 0.1 0-100 Yes 

Stack Gas Flowrate (HRA) acfm 35,290.7 35 ,093.8 35,602.9 35,329.1 33,439-37,432 Yes 

Carbon Feed (HRA) ib/hr 6.7 6.7

 1 6.7 6.7 7.26-6.2 Yes 

Stack Oxygen Concentration % 13.2 12.9 13.0 13.0 N/A N/A 

Chlorine Feed (HRA) lb/hr 118.6 20.1 118.2 119.0 88.2-229 Yes 

Pumpable Waste Feed (HRA) lb/hr 1,663.5 1 741.0 1,738.7 1,714.4 1,336-3,291 Yes 

Total Waste Feed jriRA) lb/hr 5,359.1 5 800.1 5,953.0 5,704.1 4,335-12,897 Yes 

Secondary Combdstion Chamber Liquid Feed 

(HRA) lb/hr 540.0 \ 42.9 510.3 531.1 400-1,176 Yes 

HRA - hourly rolling average 

i 

8 
Hazardou s Wast e Residenc e Tim e 

Because of the fixed-hearth nature of the Units 2 and 3 Incinerators, solid waste residence time is 

based on the elapsed time between solids charges or the travel length of the ash ram feeder, 

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

time of one hour or an ash ram travel length of 110 inches have been established as the criteria 

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

Since atomized liquid waste vaporizes almost instantaneously upon entering the combustion 

chambers, the residence time of these wastes is much less than for solids. During the Units 2 and 

3 CfPTs, the incinerators were operated at normal conditions. Liquid and gaseous wastes 

entering the Unit 2 incinerator demonstrated a residence time of approximately 5.4 seconds, 

Liquid and gaseous wastes entering the Unit 3 incinerator demonstrated a residence time of 

approximately 5.4 seconds. 

The hazardous waste gas residence time for Unit 2 is calculated as follows using the three-run 

average for the stack gas flowrate during the Unit 2 CfPT: 

• FnmaryCOT "~""~~'~~~ " 

o Secondary Combustion Chamber Volume - 635 ft 3; 

• Total Volume-1,270 ft 3; 

• Average Flue Gas Flowrate -14,104 acfm (235 frVsec); and 

• Total Combustion Zone Residence Time = (1,270 ft3) / 235 frVsec) = 5.4 sec. 

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

average for the stack gas flowrate during the Unit 3 CfPT: 

• Primary Combustion Chamber Volume - 635 ft 3; 

a Secondary Combustion Chamber Volume - 635 ft3; 

• Total Volume -1,270 ft 3; 

» Average Flue Gas Flowrate - 14,234 acfm (237 ftVsec); and 

• Total Combustion Zone Residence Time = (1,270 ft 3) / 237 frVsec) = 5.4 sec. 

Solids residence time in the Unit 4 kiln is dependent upon the kiln rotation rate, solids bed depth, 

and a number of other parameters set by design. The maximum solids hazardous waste residence 

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

equation from Chemical Engineering Handbook, Perry's 5t h Edition. 

9 
Since atomized liquid waste vaporizes almost instantaneously upon entering the combustion 

chambers, liquid and gaseous waste entering the incinerator has a residence time of 

approximately 7.5 seconds. 

The hazardous waste gas residence time for Unit 4 is calculated as follows using the three-run 

average for the stack gas flowrate during the Unit 4 CfPT: 

« Primary Combustion Chamber Volume - 1,346 ft 3; 

• Secondary Combustion Chamber Volume - 3,084 ft3; 

• Total Volume-4,430 ft 3; 

« Average Flue Gas Flowrate - 35,329 acfm (589 frVsec); and 

« Total Combustion Zone Residence Time = (4,430 ft3) / 589 frVsec) = 7.5 sec. 

10