# Wast e Fee d Profile sReport ! R7O0 B DATE : 11/30/05 ONY XENVIRONMEN

TAl l SERVICES , LL

C WAST E PROFIL E SUMMAR Y BUSINESS : DEP T ADDRES S 1 ADDRES S 2 VST
. . ACT
. . ARCHE

R DANIEL S MIDLAND

, COVITAMI N E PLAN

T 3 7 O O E
. DIVISION STREE

T DECATU R I L6252 6 DAVI D BROADHACKE

R WAST E NAME: SOLVEN

TRECOVER

Y PROCES S GENERATIN

G WASTE : SOLVEN TRECOVER

Y SHIP
. NAME: WAST

E FLAMMABL

E LIQUIDS , N.O. S ADDL
. DESC: (ACETONE, METHANOL ) Versio n 06.0 4 TWI-02869 1 SELLIN G REGIO N LA B NUMBE R : 142-8-7B

9 PHON E : 217/451-439

2 EXPIRE S : 01/11/1 1 STATU S : APP

R FO R SER V FEDERA LEP AID : ILR00002155

0 STAT E EP AID.. : 115015534

S EP ASTATU S
. . . . : CH2

C RESTRIC T SALE S OFFICE.. ; RP

R

CHEMICA LCOMPOSITIO

N ACETON E HEPTAN E METHY LALCOHO I WATE R BENZENE NON-TRI CHEMICAL

S EMULSIFIED OI L 1 5 UNI TDESCRIPTIO

N 2 5 3 5 % 2 5 3 5 % 2 5 3 5 % 1 3 8 % 1 3 B PP M 2 5 % METAL S E P TOX/TCL P PHYSICA LCHARACTERISTIC

S Physica l State... ; Liqui d Flas h Poin t > = 20 0 C

L p H : 04. 0 - 09. 0 Colo rVARIE S Odo rNON

E Layer s ; Singl e Laye r Specifi cGravity. : 0.95

0 - 1.15 0 Free Liquid s : 9

9 - 10 0 Cyanides < 5 : PP M TOTA

L Sulfide s < 3 PP M TOTA

L PCB* s : ppm . Regulated b y4 0 CF R 761 : Phenolics : < 1 0 PP M % Taxabl e : DO TUN/N ANBR: UN199

3 Treatmen t Codes.. : T0

7 CR Q RP TQT Y: Materia l Class : EP APermi t : EXP : Hazar d Clas s : 3 Stat e Code

s : 09000 1 Benzene 3

8 NESHAP

: Controlle d Benzen

e NESHA P Packin g Group.... : I I process Codes.... : CB

C Cer to £Dstrc t Rq : Federa l Codec; DOO

l D01 8 F00

3 KEO
. GRE YGLOVE S TYPE C RESPI

S CONS TFLO W HANDLIN G H-DE XINNE R GLOV E INDEX/BLU E NimiL E (INNE R GLOVE ) BENZENE NESHA

P CONTROL S REQUIRED

; N O CER T CANCE R SUSPEC TAGENT : BENZEN E Inhalation : 2 DO TPROPERTIE

S Oral : 2 Flammable : 0 Health : 0 Wast e Typ e For m Cod e B21 9 1 CHARG E CODE: IT S BENZEN E NESHA P CONTROL S REQUIRED

; COMMENT

S REVIEWE D FO R MAC TMETAL S

VES01799 5Report : R700 8 DATE : 11/24/09 ONY XENVIRONMENTA

LSERVICES, WAST E PROFIL E SUMMAR Y BUSINESS i DEP T ADDRES S l i ADDRES S 2 : I"" " VST
. . : .CT
. . : IMPERIA

LCLEANER S 221 0 WISCONSI

N AV E NE KHOLSTEIN KE N WALKE R WAST E NAME : fBTRACHLOROETHYLEN E CONTAMINA

TE D SOI L PROCES S GENERATIN

G WASTE: CLEANU

P O F TETRACHLOROETHYLEN

E SOI LFRO

M DR YCLEA N SKIP
. NAME: HAZARDOU

S WASTE , SOLID , N.O. S ADDL
. DESC: E

Q (TETRACHLOROETHYLENE

) Versio n 06.0 4 TWI-09611 0 SELLIN G REGIO N LA B NUMBE R : 144-0-059 PHONE
. : 920/898-480 0 EXPIRES 10/01/1 1 STATU S : APP

R FO R SER V FEDERA LEP AID : WID98154004

0 STAT E EP AID.. : 955001999

9 EP ASTATU S CH KRESTRIC T SALE S OFFICE
. . ; CS

H

CHEMICA LCOMPOSITIO

N TETRACHLOROETHYLEN

E SOI L NON-TRI CHEMICAL

S PAPER, PLASTIC , 9 - MA XUNI TDESCRIPTIO

N 0 1000 0 PP M 9 5 10 0 % 0 5 % METAL S E P TOX/TCL

P PHYSICA LCHARACTERISTIC

S Physica l State... : Soli d Flas h Poin t : > = 20 0 C

L p H : 05. 0 - 10. 0 Colo r, : BROW

N Odo r: NON

E Layer s : singl e Laye r Specifi cGravity. : 0.00

0 Free Liquid s : 0 Cyanides : < 5 PP M TOTA

L Sulfide s : < 3 PP M TOTA

L PCB' a : ppm . Regulated b y4 0 CF R 761 : Phenolic s < 1 0 PP M H Taxabl e : DO TUN/N ANBR : NA307 7 Treatment Codes.. : T0

7 CR Q RP TQT Y: 10

0 Materia l Class : EP APermi t : EXP : Hazar d Class..... : 9 Stat e Codes...... : 09000 1 Benzene NESHAP : Packin g Group.... : Il l Process Codes..,. : BS

L Cer tofDstrct Rq : Federa l Codes : F00

2 HANDLIN G NEO
. GRE YGLOVE S N-DE XINNE R GLOV E TYP E C RESPI R CONS

TFLO W INDEX/BLU E NITBILE (INNER GLOVE ) Jcappler s che m tape 2 DO TPROPERTIE

S Inhalation : 2 Dermal : 2 Oral : 2 Flammable : 0 Wast e Typ e For m Cod e B301 1 CHARG E CODE: N S PE EVEN TEXPIRE S 12-31-09 COMMENT S REVIEWE D FO R MAC TMETAL S

VES01799 6Report ! R70 0 8 DATE ! 11/24/0

9 BAS F COR P

. .HANNIBA LPLAN T 31 5 0 HW YJ J ONY

XENVIRONMENTA

LSERVICES , LL

C WAST E PROFIL E SUMMAR Y

M O £346 1 BUSINESS: DEP T ADDRES S 1 ADDRES S 2 : « " ' r/ST , . : PALMYR

A vCT
. . : WAST E NAME : IMI- 2 HERBICIDE ORGANI C WAST E SPILLCLEANU

P PROCES S GENERATIN

G WASTE: ORGANI

C WAST E SPILLCLEANU

P SHIP
. NAME: HAZARDOU

S WASTE, SOLID , N.O. S ADDL
. DESC : (TOLUENE , METHANOL

) Versio n 06.0 4 TWX-09780 2 SELLIN G REGIO N LA B NUMBE R 10S-7-00

2 PHONE
. : EXPIRE S ! 10/27/1 1 STATU S : APP

R FO R SER V FEDERA LEP AID : MOD05022607

5 STAT E EP AID.. ! 929001999

9 EP ASTATU S : CH KRESTRIC T SALE S OFFICE.. : RP

K

CHEMICA LCOMPOSITIO

N METHANO L TETRAHYDROFuaU

J TOLUEN E WATE R NON-TR I CHEMICAL S SOI LAN D GRAVE L SPILLCLEAN-UP DEBRI

S HERBICID E BY-PRODUCT

S 0 0

. 1 0 9 5 0 0 UNI

TDESCRIPTIO

N

. 1 %

. 1 % 2 % 1 % 9 9 % 1 %

. 1 % METAL S EP TOX/TCL

P PHYSICA LCHARACTERISTIC

S Physica l State... : Soli d Flas h Poin t N/

AC

L p H : 0

4 . 0 - 0 9
. 0 Colo r: BROW

N Odo r; NON

E Layer s . : Singl e Laye r Specifi cGravity. : 0.00

0 Fre e Liquid s : 0 Cyanides : < 5 PP M Sulfide s : < 3 PP M PCB' S : PP"> , Regulate d b

y4 0 CF R 761 : Phenolics ....,...: < 1 0 PP M % Taxabl e : DO TDN/N ANBR : NA 3 07 7 Treatmen t Codes.. : T0

7 CR Q RP TQT Y: Materia l Class : EP APermi t EXP : Hazar d Clas s : 9 Stat e Code

s : 09000 1 Benzen e : NESHAP : Packin g Group.... : II I Process Codes.... : BS

L Cer tofDstra t Rq : Y TOTA L TOTA L

Federa l Codes

s DOO l F00 3 F00 5 HANDLIN

G NEO
. GRE YGLOVE S N-DE XINNER GLOV

E TYP E C RESPIR CONS

TFLO W INDEX/BLU E NITRILE (INNE R GLOVE )
DO

TPROPERTIE

S Inhalation: 2 Dermal : 2 Oral : 2 Flammable : 0 Health : 0 SUMMAR Y Wast e Typ e B 3 01
. For m Cod e 1 COMMENT S CHARG E CODE: N S REVIEWE D FO R MAC TMETAL S P E 10-28-1 0 REPOR TWEIGH T

VES01799 7

### Report : R700 8 ONY XENVIRONMENTA L SERVICES , LL C DATE : 11/30/0 9 WAST E PROFIL E SUMMAR Y TWI-TW251 9 SELLIN GREGIO N BUSINESS : VEOLI A E S TECHNICA L SOLUTION S 110-9-72 2 DEP T ADDRES S 1 7 MOBIL E AV E EXPIRE S 11/30/1 4 ADDRES S 2 CONTRAC T NO T I N PLAC E 

### r"-/st. . SAUGE T I L 6220 1 FEDERA L EP A ID : ILD09864242 4 CT . . STAT E EP A ID . . : 163121000 9 E P A STATUS . . . . : CH KRESTRIC T WAST E NAM E I OW-SIT E RAINWATE R S t AS H WATE R SALE S OFFICE . . : RP K 

### PROCES S GEHERAriN

G WASTE: COLLECTIO

N O F ON-SIT E STORMWATE

R & PRECIPITATION ; SHIP
. NAME

: HAZARDOU

S WASTE, LIQUID , N.O. S ADDL
. DESC : CHEMICA

LCOMPOSITIO

N WATE R NON-TR I CHEMICAL

S ASHWATE R MIS C SOLIDS , WAST

E RESIDUE

S MI N - MA XUNI TDESCRIPTIO

N 9 9 

### 1 0 0 % 5 0 % 1 % METAL S Arseni ca s A s Cadmiu m a s C d Lea d a s P b Mercur ya s H g Seleniu m a

s S e Chromium He

x Nicke l a s N i Thalliu m a

s T l E P TOX/TCL

P 5. 0 1. 0 5. 0

. 2 1. 0 mg/l

mg/l mg/l mg/l mg/l PHYSICA LCHARACTERISTIC

S Physica l State... : Liqui d Flas h Poin t: > - 20 0 C

L p H : 02. 0 - 12. 5 Colo r: VARIE

S Odo rNON

E Layer s ... : Singl e Laye r Specifi cGravity. : 0.95

0 - 1.15 0 Free Liquid s : 9

9 - 10 0 Cyanides.. ; : < 5 PP M TOTA

L Sulfide s : < 3 PP M TOTA

L PCB'S : ppm. Regulated b y4 0 CF R 761 : Phenolics..-
. : < 1 0 PP M % Taxabl e : DO TUN/N ANBR: NA 3 0 8 2 Treatmen t Codes.. : T0

7 CR Q RP TQT Y: Materia l Class : EP APermi t EXP : Hazar d Class..... : 9 State Coda

s : 09000 1 Benzen e : NESHAP : Packin g Group.... : Il l process Codes.... : Cer tofDstrctRq : Federa l Codes: D00 7 D00 8 D00 4 D00 5 D00 6 D00 9 DOl O D01 1 D01 2 D01 3 D01 4 D01 5 D01 6 D01 7 D01 8 +

SIT E GENERATE D WAST E



### Inhalation : 0 DO TPROPERTIE

S Dermal : 0 Oral : 0 Flammable : 0 Health : 0 TW I Signed Addendu

m SIT E GENERATE

D

VES01799 8Report : R700 8 DATE : 11/ 3 0/0 9 ONY XENVIRONMENTA

LSERVICES, WAST E PROFIL E SUMMAR Y BUSINES S : DEP T ADDRES S 1 ADDRES S 2 f—-Y/ST
. . ICT
. . U S ARM YFL W

. .DIRECTO R O F PUBLIC WORK

S IMWE-LNW - PWE,BLD G 2101 , DP W 13 3 4 1S TS T FOR TLEONAR D WOO D M O 65473 - SHANNO N CAI N nAST E NAME : DECO

N WATER-TREATE

D V XS G B T O DRINKIN

G WATE R STANDARD

S PROCES S GENERATIN

G WASTE: DECO

N O F CHEMICA LWEAPON S RECOGNITIO

N TRAININ G CO M SHIP
. NAME : NON-REGULATE D MATERIA L ADDL
. DESC : Versio n 06.0 4 TWI-07688 6 SELLIN G REGIO N LA B NUMBE R : 143-8-39

3 PHON E : 57

3 59 6 068 2 EXPIRE S : 02/19/1 1 STATU S APP

R FO R SER V FEDERA LEP AID : MO321372097

9 STAT E EP AID.. : 929001999

9 EP ASTATU S : UNDETERMINAB

L SALE S OFFICE.. : TW

I

CHEMICA LCOMPOSITIO

N WATE R SODIU M HYDROXID

E NON-TR I CHEMICAL S SUPE R TROPICA LBLEAC H COMMENT S TRACE S O F V XAN D G B AGEN TAR E NEUTRALIZED WIT

H BLEAC H AN D RINSED WIT H THOUSAND

S O F GALLON S O F WATER , THE N COLLECTE

D FO R INCINERATION
. AL

LWATE R I S TESTE

D PRIO R T O SHIPMEN TT O ENSUR E COMPLIANC E WIT H DRINKIN G WATE R STANDRADS

. V XAN D G B CONCENTRATIO

N AR E CERTIFIE D T

O B E BELO W2 0 PP B AN D AR E USUALL Y < 2 PPB
. (3

XLEVEL ) UNI TDESCRIPTIO

N 9 3 1 10 0 % 2 % 5 %

E P TOX/TCL P PHYSICA LCHARACTERISTIC

S Physica l State... : Liqui d Flas h Poin t > =

. 20 0 C

L p H : 05. 0 - 09. 0 Colo r: VARIE S Odo r: NON

E Layers
. s Singl e Laye r Specifi cGravity. : 0.95

0 - 1.15 0 Free Liquid s : 9

9 - 10 0 Cyanides : < 5 PP M TOTA

L Sulfide s < 3 PP H TOTA

L PCB' s : N/

Appm . Regulate d b y4 0 CF R 761 : Phenolics : < 1 0 PP M % Taxabl e : DO TUN/N ANBR: Treatmen t Codes
. . : T0

7 CR Q RP TQTY,..... : Materia l Class : EP APermit
. EXP : Hazar d Class..... : Stat e Code

s : 09000

2 Benzen e : NESHAP : Packin g Group.... : Process Codes.... : DI2 Cer tofDstrct Rq : Y Federa l Codes : NEO
. GRE YGLOVE S TYP E C RESPI R CONS

TFLO W HANDLIN G N-DE XINNE R GLOV E INDEX/BLU E NITRILE (INNE R GLOVE ) DI-WATER WIT

H DECOMPOSITIO

N PRODUCT

S O F GB/VX
. REACTIV E CATEGORY

: A(FO R SCHEDULIN

G ONLY ) Inhalation : 2 Dermal : 3 DO TPROPERTIE

S Oral : 2 Wast e Typ e For m Cod e B21 9 1 .CHARG E CODE : N

S HIV E CATEGORY

: A(FO R SCHEDULIN

G ONLY ) jj-18-1 0 "BILLING : TRI P TICK, W

TTIC , CO D AN D COP YO F TA G T O RETUR N WIT H MANIFES

TT O GENERATO

R ALSO
. REVIEWE

D FO R MAC TMETAL S CO D REQUIRE

D VEOLI ATRANSPORTATIO

N ONLY
. WIT H INVOICE
. WHE

N CO D I S PRINTED, COP

YT O CS R

VES01799 9TW I Laborator yAnalysi s Repor t

Receive r# : TK30 4 Visua l Inspection : Glov e Bo x/ Hoode d Feede r # o fDrums : 1 Date : 6/29/200 1 Profil e #:2ZZ2ZZ Generato rTRAD E WAST E INCINERATIO N Descript : Process Code(s) :

Dru m Storag e Compatabilit y Profiled DO

THazar d Class 9 P = Pass F = Fail 8 A8B 4/

5 Sample Number Drum Re p /

Comp 303022]_iL00000001 j

1/ 

# III I 1 1 30302 2 Free Liquid (%

) 

# III I 1 1 30302 2 Profil e Confor m Dat e Initial s Pumpable N

O 

# III I 1 1 30302 2 wwww v Yes No 11/06/0 9 M T Layers/Phases -

% Ea
. www w Colo r 

# ^\\\ Turbidit y www w W W Viscosit y L X Physica l Stat

e www w Wate rMiscibilit

y WWW W W \ V Add
. Description Wate rReactivit

y www w W W Radiation Scree n =BK G X Flam
. Pot
. Scree n See Flashpoin t X p H Scree n 5 a t10 0 pent 2-12. 5 X Oxidize rScree n PaintFilte rTes

t WWWN W Cyanide Scree n WWW W Sulfide Scree n WWW W Incidenta l Odo r www w 

# ^\\\ Speci e Gravit

y 1.0 1 11/04/0 9 M T BTU/L b 157

0 11/04/0 9 B D % Chloride 1.2 W W i 11/04/0 9 K D Flas h Poin t - De g F w w 01/01/00 PCB s B yG C - mg/k

g <50pp m 11/06/0 9 p H b yMete r wwww J W W 01/01/0 0 Arseni cmg/k

g 4.76

8 0 Berylliu m mg/k

g 4.76

5 0 Cadmium mg/k

g 4.76

5 0 Chromiu m mg/k

g 4.80

5 0 Lea d mg/k g 4.78

4 0 Mercur ymg/k g 0.05

6 0 W W Profil e Revie

wfo rAppendixWAP- C Consitituenf s by : Date : Add
. Comments : The dat

a i n the sampl e information section(6/29/2001)i s dat e profil e 777777

wa s created
.

VES01800 0File Inventor yPrin t Approval s Chemis tReceivin g Laborator

yTan k Far m Proces s Plannin g Windo wBillin g Hel p I Laborator

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b Manage rApproval = M Discrepan t = D ^
_ Rejecte d = R Conforms/Accepte

d = AY

p Wate rReactivit y TN o RX N f " RXN :
•Radiatio n Scree n r=BK G r>BKG : Value

-Flam . Po t Scree n rNe g rPo

s TBOC pp H Screen Value f g " W

100 % r10 * rOxidize rSaeen TNe g rPo

s
•Pain t Filte rTes t rPas s TFai l H V-Fai l TN/ A Specifi c Gravit

y BTU/l b £Chlorid e Flas h Poin

t (Deg . F ) PCBs b yG C (mg/kg

) PCB G C Commen

t PCBs-Scree n (ppm

) 1 .01 157 0 1. 2 jl/1/190 0 1/1/190 0
p Cyanid e Screen J TM Negf " Pos P N/

Aj ~ Cyantesm

o 2.4,5 - T(ppm

) Silve x(ppm ) (1/1/1900 " |
-Sulfide Scree

n rNe g rPo

s TN/

A PC P Screen (ppm ) pH b yMete r rKI TFS C |W190 Q rioox r10^)1^1 /190

0 -Metals-— — A s j4.7S 8

P b 14.78 4

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As h % -

VES01800 1I W l Laborator yAnalysi s Kepor t

Receive r# : TK31 0 Visua l Inspection : Glov e Bo x/ Hoode d Feede r # o fDrums : 1 Date : 6/29/200 1 Profil e #.7777.7.7 Generator: TRAD E WAST E INCINERATIO N Descript : Proces s Code(s) :

Dru m Storag e Compatabilit y Profile d DO THazar d Clas s 9 P = Pass F=Fai / 8 A8 B 4/

5 Sampl e Numbe

r Dru m Rep /

Com p 301556J_IL0000000 1

1 / 

# I I 11 1 

# 1 1 301556 Free Liquid (%

) 

# I I 11 1 

# 1 1 301556 Profil e Confor m Dat e Initials Pumpabt e N

O 

# I I 11 1 

# 1 1 301556 wwww v Yes No 10/01/09 S L Layers/Phases -

% Ea
. \\\\\\\ w 

# ^\\\ Colo r wwww v Turbidit y Viscosit y L X Physica l Stat

e Wate rMisdbilit

y \\\w\\\ v W W " Add
. Description Wate rReactivit

y wwww v W W Radiatio n Scree n =BK G X Flam
. Po tScree n Se e Flashpoint X p H Scree n 3 a t 10 0 pent 2-12. 5 X Oxidize rScree n wwww v PaintFilte rTes

t wwww v Cyanid e Screen wwww v 

# ^\\\ Sulfid e Screen \\\\\\\ w 

# ^\\\ Incidental Odo r wwww v 

# ^\\\ Specifi cGravit

y 0.8

3 

### ^ 10/01/09 S L BTU/Lb 960 0 

# ^\\\ 10/01/09 M T % Chlorid e <0.S 

# ^\\\ 10/01/09 J F Flas h Poin t- De g F w w ^ 01/01/00 PCB s ByG C - mg/k

g <50pp m 10/01/09 p H b yMeter 01/01/00 Arseni cmg/k

g 0 0 Berylliu m rtig/k

g 0 0 Cadmiu m mg/k

g 0 0 Chromiu m mg/k

g 0 0 Lea d mg/k g 0 0 Mercui ymg/k

g 0 0 W W Profil e Re/iewfo rAppendixWAP- C Consitituent s by : Date : Add
. Comments : The dat

a i n the sampl e infonnatio n section(6/29/2001)i s dat e profil e 7.77777

wa s created
.

VES01800 2Fi e Inventor yPrin tApproval s Chsmis tReceivin g Laborator yTan k Far m Proces s Plannin g Windo wBilin g Help , •S 1 utip fdlgr ySiiiripl e Analysi

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. Vie

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d » A Layers/Phase s J Ei S [-Wate rReaotivil y f ~ N o RX N F * RXN : •Radiatio n Scree n P -BK G r>BKG : p Ram
. Po tScree n f " Ne g i ~ Po s rBO C •p H ScreenValu e J 5 jy 1005 £r

- m -Oxidize rScreenrNe o rPo

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- Pain tFilte rTes t rPa wrFai l I ~ V-Fai l TN/ A f Cyanid e Saee n f " Negr " Pos TN/ A( ~ Cyantesm o rSulfid e Scree n TNe g TPo

s rN/ A Valu e Dat

e Specifi cGravit y BTU/lb 2 Chlorid e Flas h Poin t(Deg
. F ) PCB s b yG C [mg/kg ] PC B G C Commen t PCBs-Scree n (ppm ) 0.8 5 [SB1 0 j<0.5 B Initial s |11/15/200 9 |M T |li/15/200 9 ~ |m T (11/15/200 9 [M T h/1/190 0
2,45- TIppm ) Silve x(ppm ) 1/1/190 0 PC P Scree n (ppm ) p H b yMete r rKI

TrG C |V1/19C 0 rlOO^ r10*1,1/1/190

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- Incidenta l Odo r rN o TYes

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VES01800 3I W I LaDorator

yAnalysi s Kepor

t Receive r# : 35292 0 Sampl e Required # o fDrums : 1 Date : 10/22/200

9 Profil e # . 07688 6 Generator: U S ARM YFL

W Descript : DECO N WATER-TREATE D V X& G B T O DRINKIN G WATE R STANDARD S Process Code(s) : DI2

Dru m Storag e Compatabilit y Profile d DO THazar d Clas s 9 P = Pass F <> Fail 8 A8 B 4/

5 Sampl e Numbe r Dru m Rep /

Com p 302522j_005389778J J

BULK/ 1 

# ' mi n 

# II I Free Liquid (%

) 10

0 Profil e Confor m Dat e Initials Pumpable YE

S 30252 2 www w Ye s N o 10/22/09 B

D Layers/Phases -

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. Pot
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# \\\ \ PaintFille rTes

t N/

A www w 

# ^\\\ N Cyanid e Scree n NEGATIV E www w 

# ^\\\ Sulfid e Scree n NEGATIV E wwww ^ 

# ^\\\ Incidental Odo r N

o www w Specifi cGravit

y 1.0 1 0.950-1.15 0 10/22/09 B D BTU/L b <50 0 1 -500 0 10/22/09 K D % Chloride <0.5 2 - 0 10/22/09 A J Flas h Poin t - De g F >14 0 W W i 01/01/00 PCB s B yG C - mg/k

g <50pp m 10/22/0 9 p H b yMeter www w W W 01/01/00 Arseni cing/k

g 0 0 W W Berylliu m mg/k

g 0 0 W W Cadmiu m mg/k

g 0 0 

# ^\\\ Chromiu m mg/k

g 0 0 Lea d mg/k g 0 0 W W Mercur ymg/k g 0 0 W W %Ml

--3,1! Additional Comments : MA

YSHO WPO S O XSCREE N DU E TO BLEACH-OKA YTO ACCEPT
. Profil e Revie

wfo rAppendixWAP- C Consitituent s by: KMEREDIT H Date : 3/13/200

9 Add
. Comments : DI-WATE R W/DECOMPOSITIO N PRODUCT S O F GB/VX

VES01800 4

# C M S Performanc e Evaluatio n

VES01800 5TA G LOO P DESCRIPO N SERVIC E LOCATIO N LP-SH T P&I D REMARK S INSTL-RMK S SPEC-RMK S

S / N TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y W T 20 4 WEIGH TTRANSMITTE R SPECIALT YFEEDE R MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : CALIBRATIO N NOTE S TOLED O 814 0 EX P 0-4,00 0 # 0-4,00 0 # 4-2 0 MAD C 0#-81 9 Ct S 200#=98 3 Ct S 1#=.81 9 ct s 3005 2
Chec k scale , digita l Calibratio n per . Toled o instructions
. The n wit h n o weigh t o n scal e adjus t analo g zero . (NOTE : HM I wil l no t displa ynumber s les s tha n zero)
. Nex t ad d weigh t = t o 10 % ar e mor e o fscale s range , the n adjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INSTRUMEN TREADIN G Before Calibration

s*\

_is i After Calibration INPU TVALU E

Q
_ 

## ISO

CALIBRATIO N SOURC E REFERENC E

Comment s

Performe d by: ^

Date : Time : Z.A M (v\ Place : J B CALSHEET
. WD B /(Field)or Shop)

VES01800 6TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y W T 21 0 WEIGH TTRANSMITTE R SOLI D CHAR G CONV
. FIEL D 303 1 MANLTFACT : MODEL : SCALE : CALIB-IN : CALIB-ODT : PROCESS-SP : INST-SP : ACTION : TOLED O

814 0 0-40 0 # 0-40 0 # 4-2 0 MAD C 0#=81 9 Ct S 200#=245 7 Ct S 1#=8.1 9 Ct S I / O NUMBER : 3007 0 CALIBRATIO N NOTE S Chec k scale , digita l Calibratio n per . Toled o instructions
. The n wit h n o weigh t o n scal e adjus t analo g zero . (NOTE : HM I wil l no t displa ynumber s les s tha n zero )
. Nex t ad d weigh t = t o 10 % ar e mor e o fscale s range , the n adjus t analo g span , t o indicat e weigh t o n scale , a s rea d o n HM I screen . S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E 

# o so INSTRUMEN TREADIN G Before Calibration

^

Afte rCalibration 

# 50.2 -

CALIBRATIO N SOURC E REFERENC E

Comments :

Performe d b y : ,fe^
—f•Date : ifi'l 0 !-® ! Time : 2-)S" " AMTg p J B Place : CALSHEET.WD B QFieli^or Shop)

VES01800 7TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y PD T 25 0 PRESSUR E DIFF
. TRANSMITT E MANUFACT : YOKOGAW A BAGHOUS E INLET/OUTLE T FIEL D 203 5 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : 0-1 5 i n w c

4-2 0 

### M A

CALIBRATIO N NOTE S U S E PNEUMATI C CALIBRATIO N BENC H WIT H MANOMETE R AN D LOO P CALIBRATOR
. INPU TPNEUMATI C SIGNA LAN D REA D OUTPU TWIT H LOO P CALIBRATOR
.

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G 0 W. c• Befor e Calibratio n ^.OU X

q After Calibration. (_j q ^ 

# 2.0,0^ACALIBRATIO N SOURC E REFERENC E

Comments :

Date : Time:
. M± am(pF ) Performe d by : — - _t - - , •= ^ ^^ ^ J B Place ; CALSHEET.WD B [Field dr Shop)

VES01800 8TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y P T 20 0 PRESSUR E TRANSMITTE R LO WCHAMBE R FIEL D 203 2 MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R •7. 5 t o +2. 5 in
.

4-2 0 M A wc .

CALIBRATIO N NOTE S Connec ttransmitte rt o b e calibrate d t o pressur e sourc e an d calibrate d referenc e (Manometer) , inpu t appropriat e pressur e a n d verif ywit h curren t meter .

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G

-7. S if

Before

Calibration W.C -

-7-S " After Calibration 

# 2S 2.0
. 

# A

CALIBRATIO N SOURC E REFERENC E

Comments :

Performe d bv : -i^* — I •Date JD-Z2-0 C J Time.-Z'fl O AM^T ) J B Place : ; ^=r> v CALSHEET.WD B (Field o^Shop))

VES01800 9TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y TAG : P T LOOP : 21 9 DESCRIPON : PRESSUR E TRANSMITTE R SERVICE : UPPE R CHAMBE R LOCATION : FIEL D LP-SHT : 303 3 P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R 7 . 5 t o +2. 5 in
. wc .

4-2 0 M A

CALIBRATIO N NOTE S Connec ttransmitte rt o b e calibrate d t o pressur e sourc e an d calibrate d referenc e (Manometer) , inpu t appropriat e pressur e a n d verif ywit h curren t meter .

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T XNPU TVALU E

—~.— //
. - Before

Calibration INSTRUMEN TREADIN G

Afte rCalibration Z.S ' 2.0. 0 y^ A CALIBRATIO N SOURC E REFERENC E

Comments :

Performe d by : _ Date : Time : Z'/S ~ AM(P M Place : J B CALSHEET
. WD B (Field oifShop))

VES01801 0TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y TAG : A T LOOP : 28 9 DESCRIPON : OXYGE N MANUFACT : COS A SERVICE : STAC KGA S ANALYZE R LOCATION : STAC K LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : 203 5 MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R 0-25 %

0-25 % 4-2 0 MAD C

CALIBRATIO N NOTE S Flo wcalibratio n ga s a t 2- 3 psi g an d 3 scf h

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E 

# 3 - 0 INSTRUMEN TREADIN G Before Calibration 2\.i s 20- f 

### 1 -Q After Calibration

CALIBRATIO N SOURC E REFERENC E ZER O GA S CY L ft: CC 111 <T33 SPA KGA S CY L #:

_SA
Comments :

Performe d b y J B CALSHEET
. WD B zjhfjJt/ J DatezlMlA l Time : /t )

*'OQ t Place : P M

((Field'hor

Shop)

VES01801 1TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 QUARTERL Y TAG : LOOP : DESCRJPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : A T 288 B H C STAC KGA S ANALYZE R STAC K 55 6

63 0 O n MC S 10 0 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : Therm o Elec.co
.

5 1 C 0-10 0 PP M 4-2 0 MAD C

CALIBRATIO N NOTE S 1 ) Ope n sampl e ga s bottl e valves
. 2 ) Pres s MEN U Butto n 3 ) Pres s CALIBRATIO N 4 ) Pres s ZER O ADJUS T 5 ) Pres s SPA N ADJUS Tafte r4)finishe d 6 ) Pres s RU N afte r5)finishe d 7 ) Clos e sampl e ga s bottles
. S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/hr
. CALIBRATIO N REPOR T INPU TVALU E

0 

# ISA INSTRUMEN TREADIN G Befor e Calibration 0 ~?5. After Calibration

CALIBRATIO N SOURC E REFERENC E G A S CY L# :

Comments :

Performe d b J B CALSHEET.WD B Date:i0^d23

_Time : fg h P M Place:
. (Field br Shop)

VES01801 2TW I INSTRDMEN TCALIBRATIO N RECOR D UNI T#2 - QUARTERL Y TAG : A T LOOP : 288 B DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMK S : SPEC-RMKS :

S/N : OPACIT Y STAC KGA S STAC K

2.0 0 t o 5.70m a MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R TELEDYN E INST
.

LightHaw k

560D I 0-100 % 4-2 0 MAD C

CALIBRATIO N NOTE S Clea n window s

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G Befor e Calibration

After Calibration

CALIBRATIO N SOURC E REFERENC E

Comment s

Performe d by : CKuc k £du]&.Cofs

Date : Time : j^AM$)P M J B Place : ^ CALSHEET.WD B ffield\> r Shop)

VES01801 3TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRDMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 200 A P L C THERMOCOUPL E INPU TMANUFACT : LOWE R CHAMBE R MODEL : FIEL D SCALE : CALIB-IN : 203 2 CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : MODICO N

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

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
.
S e e Manufacture s literatur e fo rdetaile d instructions , Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E S0o °

F ZQoQ °

F INSTRUMEN TREADIN G

Befor e Calibration S O I -t> 

## ZOOO After Calibration

CALIBRATIO N SOURC E REFERENC E

Comments :

Performe d by : Date : Time : .a m (miT) J B Place : CALSHEET.WD B (Fielde r Shop)

VES01801 4TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 200 B P L C THERMOCOUPL E INPU T LOWE R CHAMBE R FIEL D 203 2 MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R MODICO N

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

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
. S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G 

## ^dQO°

f~Befor e Calibration



## ^0O° 7j00O° F ZQOO c

After Calibration

CALIBRATIO N SOURC E REFERENC E

Comments : )\) o CaUiocg 'T-ic)/ \ n-eedeJ.

Date : _AM(PM^ ) Performe d by : .T B CALSHEET.WD B Place : (Field) or Shop)

VES01801 5TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRDMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 219 A P L C THERMOCOUPL E INPU TMANUFACT : MODICO N UPPE R CHAMBE R FIEL D 203 3 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I/ O NUMBER : 0-250 0

TYP E K deg
. F
.

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
. S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G 

# 5~0<0

D F

Bef ° r e

Calibration

^QQ ® X06O °

F Zooo °

After Calibration

CALIBRATIO N SOURC E REFERENC E

Comments : K)o

CfllibcaiiP/ \ needed.

Performe d by:
. Date : Time : _ am(pm ) J B Plac e CALSHEET
. WD B ((Field)or Shop)

VES01801 6TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRDMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 219 B P L C THERMOCOUPL E INPU TMANUFACT : MODICO N UPPE R CHAMBE R FIEL D 203 3 MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I/ O NUMBE R 0-250 0

TYP E K deg
.

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a'typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
.
S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G r-/~\ s\° f —Before Calibration

—s^/>° 

# \^QO tz 6 0 0 2.006 ° Afte rCalibration

CALIBRATIO N SOURC E REFERENC E

Comments :
b y : fe^-TTT&y__^j2 ^ n a te://-/0-O < 7Time:Z'3 ^ A M 

# <gf t Per forme d J B CALSHEET.WD B Place : (FieldSor Shop)

VES01801 7TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMIARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 22 3 P L C THERMOCOUPL E INPU TMANUFACT : MODICO N SD AINLE T FIEL D 203 3 MANUFAC T MODE L SCAL E CALIB-I N CALIB-OU T PROCESS-S P INST-S P ACTIO N I / O NUMBE R 0-250 0

TYP E K deg
.

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
. S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INSTRUMEN TREADIN G Befor e Calibration —, o

ZQQ\ ° After Calibration INPU TVALU E 

# bOO°F Zooo eF

CALIBRATIO N SOURC E REFERENC E

Comaents : D aalibra'f/ai ^ needed.

Performe d by:
. Date : Time : Z- ^ J B Place : / < = a v . CALSHEET
. WD B ((Field) or Shop)

VES01801 8TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L T T 27 0 P L C THERMOCOUPL E INPU TMANUFACT : MODICO N SD AOUTLE T FIEL D 203 4 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : 0-250 0 deg
.

TYP E K

CALIBRATIO N NOTE S U s e col d junctio n compensate d thermocoupl e calibrato rt o inpu t a typ e Ktemperatur e signa l o f50 0 de g F
. an d 2,00 0 deg.F
. a t inpu t o fPLC , the n verif ythi s singl e o n th e contro l pane l CRT
.
S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E SOO °

F -zoo o

F INSTRUMEN TREADIN G

Before Calibration 

# SOO

After Calibration

CALIBRATIO N SOURC E REFERENC E

Comments : K) o CcS lUra-Ko ^

n€eo/ei ,

Performe d by : (
. 

## — Qj? 0 Date : M-lO-Cft

Time : "2J

3S~AM(PM^ ) J B Place : CALSHEET.WD B ((Fiel'djor Shop)

VES01801 9TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L TAG : F T LOOP : 28 3 DESCRIPON : STAC K SERVICE : STAC K LOCATION : FIEL D LP-SHT : P&ID : 203 5 REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : FLO WTRANSMITTE R MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : Rosemoun t

0-20,00 0 ACF M 0-.5"W C 4-2 0 MAD C S e tDamp/po t t o mi d poin t
CALIBRATIO N NOTE S U S E PNEUMATI C CALIBRATIO N BENC H WIT H INCLIN E MANOMETE R AN D LOO P CALIBRATOR
. INPU TPNEUMATI C SIGNA LAN D REA D OUTPU T WIT H LOO P CALIBRATOR
.

S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou tan d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G 

# Q /f , . _Before Calibration

o o > • > A U C
. 3 .% 3 * A . £ * W. C 1%2L„A - <•> /' After Calibration

, ., _. 

# H HO

CALIBRATIO N SOURC E REFERENC E

Comments :

J^cJT T&j_ J ^ Date : tl -

Time : /

Cf-

( /S~ ~ (m) ] Performe d by:-J^<L
— \ , <J >^ jC^CT

Date : Time:/U-v: > (J\M7P M J B Place : CALSHEET.WD B /Field J > r Shop)

VES01802 0TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L F T 21 5 FLO WTRANSMITTE R HIG H BT U F L D 203 1 Change d Rang e 11/12/9 6 SENSITIVIT Y5.5 8 SW1,2,3,4 , OF F 9719 3 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : MICR O MOTIO N

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

CALIBRATIO N NOTE S Flus h proces s piping , connec t wate rhos e t o upstrea m sid e o f flo wmeter , se t contro l syste m t o appropriat e rat e control , a n d rea d totalizer , flo wwate rint o a containe ran d compar e t h e toltalize rreadin g t o th e measure d amoun t i n container
.
S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G i
. i , n Before

Calibration

da/
— w 10 |k> , pe rmm . Wl.l S lbs
.
After Calibration

CALIBRATIO N SOURC E REFERENC E

Comment s : M o m(<kr<a f

Performe d b y J B CALSHEET.WD B Date : //-)*)-O l Time : Z'ZO AM^P*M^ ) Place : (Field/or Shop)

VES01802 1

### TAG : LOOP : DESCRIPON : SERVICE : LOCATION : LP-SHT : P&ID : REMARKS : INSTL-RMKS : SPEC-RMKS :

S/N : TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L F T 21 6 FLO WTRANSMITTE R LO WBT U FL D 203 1 Change d Rang e 11/12/9 6 SENSITIVIT Y5.1 6 S W1,3,4 , OF F 3293 6 MANUFACT : MODEL : SCALE : CALIB-IN : CALIB-OUT : PROCESS-SP : INST-SP : ACTION : I / O NUMBER : MICR O MOTIO N

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

CALIBRATIO N NOTE S Flus h proces s piping , connec t wate rhos e t o upstrea m sid e o f flo wmeter , se t contro l syste m t o appropriat e rat e control , a n d rea d totalizer , flo wwate rint o a containe ran d compar e t h e toltalize rreadin g t o th e measure d amoun t i n container
.
S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E INSTRUMEN TREADIN G i ~ , , o Befor e Calibration C\ O, i n IO lbs , fe C

Wurs. torI

Y~>\n.
_I'l l \&S>

•
After Calibration



### CALIBRATIO N SOURC E REFERENC E

Comment s

Performe d b y J B CALSHEET
. WD B . Date : ll-\°i-0^ Time : Z-00

A M /PM ' Place : ((Fieldjor Shop)

VES01802 2

### TW I INSTRUMEN TCALIBRATIO N RECOR D UNI T# 2 ANNUA L TAG : F T LOOP : 28 8 DESCRIPON : FLO WTRANSMITTE R MANUFACT : E- H SERVICE : LIM E SLURR YT O HEA D TAN KMODE L LOCATION : FIEL D SCALE : 0-2 0 GP M LP-SHT : CALIB-I N P&ID : 203 4 CALIB-OUT : 4-2 0 MAD C REMARKS : PROCESS-S P INSTL-RMKS : INST-S P SPEC-RMKS : ACTIO N

S/N : I/ O NUMBE R CALIBRATIO N NOTE S Flus h proces s piping , connec t wate rhos e t o upstrea m sid e o f flo wmeter . Se t contro l syste m t o appropriat e contro l rate , a n d rea d totalizer , flo wwate rint o a containe ran d compar e t h e toltalize rreadin g t o th e measure d amoun t i n container
.
S e e Manufacture s literatur e fo rdetaile d instructions
. Fil l ou t an d affi xa ne wcalibratio n sticker
. 0 . 1 lb/h r CALIBRATIO N REPOR T INPU TVALU E

^ o rone . ryj'mu L 'he.' 

### INSTRUMEN TREADIN G

Before Calibration

After Calibration



### CALIBRATIO N SOURC E REFERENC E

Comments : jvJ o Calikca4 ^ AYlecr^J. 

# b^A^TTi 2 

# ^

S>J2>

Date : XL-UCft



## Time:iH2_AM(g ) Performe d J B CALSHEET
. WD B Place:
. (Field)or Shop)

VES01802 3540 4 Jedme d Ct
. - St
. Louis, M

O E312 9 Business : (314

) 845-777 8 - Fax : (314 ) 845-777 9 Scal e Inspectio n Report C V-4-

y<~-n<-^

Customer : ONY XENVIRONMENTA L # 7 MOBIL E AVENU E SAUGET , I L 6220 1 Location : Direc

tInjectio n MFG/Model : WI130 Scal e Type : VEHICL E Capacity : 60000L B escription : Clas s II I L Seria l No : 011150 Scal e No : 2 Divisions : 5L B Scal e wa s foun d i n Tolerance : Xye s Shif t Tes t Sides/Corners

/ Section s Weight

s Applie d Scale Readin

g (A s found ) Error(+/-

) Toleranc

e Maintenanc e Scale Readin

g After Adjustmen t (A s Left ) Accept

/ Rejec t Sectio n 1 21,00 0 l b 21,00 0 l b + 0 l b +/- 4 5 l b ACCEP T Sectio n 2 21,00 0 l b 21,00 0 l b + 0 l b +/- 4 5 l b ACCEP T Sectio n 3 21,00 0 l b 21,00 0 l b + 0 l b +/ - 45 l b ACCEP T Sectio n 4 21,00 0 l b 21,00 0 l b + 0 l b +/- 4 5 i b ACCEP T Sectio n 5 21,00 0 l b 21,00 0 l b + 0 l b +/ - 45 l b
. ACCEP T Sectio n 6 21,00 0 l b 21,00 5 l b + 5 l b +/-.4 S l b ACCEP T

Buildu p Weigh t Weight

s Applie d Scale Readin

g (A s found ) Error(+/-

) Toleranc

e Maintenanc e Scale Readin

g After Adjustmen t (A s Left ) Accept

/ Rejec t Sectio n 4 3,00 0 l b 3,00 0 l b + 0 l b +/ - 1 0 l b ACCEP T 6,00 0 l b 6,00 0 l b + o l b +/ - 1 5 l b ACCEP T 9,00 0 l b 9,00 0 i b " + 0 l b +/ - 20 l b ACCEP T 12,00 0 l b 12,00 0 i b + 0 l b +/ - 25 l b ACCEP T 15,00 0 l b ' 15,00 0 l b + 0 l b +/ - 30 l b ACCEP T 18,00 0 l b 18,00 0 l b + 0 l b +/- 4 0 l b ACCEP T Sectio n 4 21,00 0 l b 21,00 5 l b + 5 l b +/ - 4 5 l b ACCEP T

Tes tProcedur e follow s QSPOO9-O01/O0

2 NISTifcMO : 259883/253250 39598 OBS04-0268/03-0450 274998 Rice Lake : 822/266926-0

2 822/272801-06 822/274081-06 ^ „ / r

_ ^ p , jOjctftCn

.

- a Or /HAP***** CalDate : 11/09/200

9 Nex

t Ca l due : 9

0 Day s Service Technicia n Registratio n # : 0524-M Calibrated B

yServic e Technician : Ji m Koerkenmeie r Calibratio n Dates : JA N AP R JU LOC T Jo b Queue* : LT217651 Repor t ID : 6896338

5 Uncertaint yo fMeasurementprovided o n reques t FOR CUSTOME R US E ONL Y£ Reviewe d B yDat e Reviewe d Thi s documen t shal no tb e reproduced , excep ti n full , withou t th e approva l ol Accurat e Superio rScal e Company.
. pag e 1 0fi For m 030, Re v15,08/19/0 9

VES01802 4BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 1 O F 2 OPERATIN G PARAMETER S PL C COI LBWCOI L 1 OC L TR VPOSITIO N (OPEN ) 0160 2 0040 1 2 OC L UPPE R CHAMBE R TEMP
. 1 mi n avg . 0160 3 00402 3 OC L H I BT U Ibs/h rMa x 0160 4 0040 3 4 OC L LOWE R CHAMBE R TEMP
. 1 mi n avg . 0160 5 00404 5 OC L L O BT U Ibs/h rMa x 0160 6 0040 5 6 OC L FLU E GA S HCL , 1 hr
. rollin g avg . 0160 7 0040 6 T OC L FLU E GA S CO , 1 hr
. rollin g avg . 0160 8 0040 7 8 OC L FLU E GA S OPACITY , hig h fo r48 0 sec/hr
. avg . 0160 9 0040 8 9 OC L FLU E GA S OPACITY , hig h instantaneou s 0161 0 0040 9 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min
. avg 0161 1 0041 0 1 1 OC L HEATINPU Thig h mbtu/h r 0161 3 0041 1 1 2 OC L CHLORIN E INPUT , hig h Ibs/h r 0161 4 0041 2 1 3 OC L SOLI D FEED , hig h Ibs/h rMax
. 0152 6 0041 3 1 4 OC L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 8 0041 4 1 5 OC L SPECIALITYFEEDE D hig h Ibs/h rMax
. 0151 6 0041 5 1 7 AWF C SD AOUTLE TTEMP , high l min
. avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DIFF.PR
. DROP
. Low1 min
. avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min
. avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min
. avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min
. avg . 0159 7 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 8 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h irist
. 0159 9 0042 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min
. avg . 0160 1 0042 4 ', ) AWF C LO WCHAMBE R TEMP. , lo w1 hr
. avg . 0158 6 0042 5

_ 6 AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . 0158 8 0042 6 2 7 AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 0158 9 0042 7 2 8 AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min
. 0162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 0043 0 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 0 00432 3 5 MWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 2 00435 3 6 MWF C HEATINPU Thig h anticipate d 0162 2 00436 3 7 MWF C CHLORIN E INPUT , hig h Ibs/h r 0162 3 0043 7 3 8 MWF C E-STOP S orT/ C MODUL E inactive 0161 5 0043 8 3 9 MWF C FLU E GA S CO , hig h 1 hr
. avg . 0159 5 0043 9 4 0 MWF C ATOMIZE R hig h hig h vibratio n for 5 sec . 0162 4 0044 0 4 1 SWF C SPEC
. FEE D Ibs/h rhig h 0157 6 0044 1 PAS S y ~ Z 2 FAI L

ZZL

1ZL 

# 5

VES01802 51 BIWEEKLYUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k 1C4039 ) PAG E 2 O F 2 OPERATIN G PARAMETER S PL C COI L B WCOI L 4 2 SWF C HIBT U Ibs/h rhig h 01578 00442 4 3 SWF C LOBT U Ibs/h rhig h 0158 0 0044 3 4 5 SWF C HIBT U los s o fsigna l 0301 9 0044 5 4 6 SWF C LOBT U los s o fsigna l 0302 0 0044 6 4 7 SWF C SPECIALIT YFEED/COMPRESSE D GA S FEE D los s ofsigna l 0302 1 0044 7 4 8 MWF C NORT H & SOUT H IP S ALARM S FAILE D 0570 3 0044 8 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 0302 2 0044 9 5 0 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 5 1 SWF C DIREC TINJEC T(commo n alarm ) 03132 0045 1 5 2 OP L Ba g Lea k Detectio n Syste m (Tribo) 65 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3 6 6 OP L Non-Pumpabl e 1 Hou rRollin g Tota l OP L 0820 6 0411 4 6 7 OP L Tota l wast e 1 Hou rRollin g Tota l OP L 0820 8 0411 5 6 8 OP L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 6 6 9 OP L Lo wVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 7 0 OP L Sem i Volatil e 1 2 Hou rRollin g Tota l OP L 0821 6 0411 8 7 1 OP L Mercur

y1 2 Hou rRollin g Tota l OP L 0821 8 0411 9 7 2 OP L As h 1 2 Hou rRollin g Tota l OP L 0822 0 0412 0 7 3 OP L PC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 2 0412 1 7 4 OP L SC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 4 0412 2 7 5 OP L SD AOutlet Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 7 6 OP L Baghous e Differentia l Pressure 1 Minute Averag e LowOP L 0822 7 0412 4 7 7 OP L Baghous e Differentia l Pressure 1 Minute Averag e Hig h OP L 0822 8 0412 5 OP L Stac k

HC LCorrecte d 1 Hou rRollin g Averag e Hig h OP L 08232 0412 6 OP L Stac k

C O Correcte d i Hou rRollin g Averag e Hig h OP L 0823 6 0412 7 8 0 OP L Stac k

Flo w1 Hou rRollin g Averag e Hig h OP L 08244 0412 8 8 1 OP L BT U 1 Hou rTota l OP L 0820 9 0412 9 8 2 OP L Hr

tCl/Hr a Lim e Flo

w1 Minut e Averag e Hig h OP L 0825 1 0413 0 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0815 6 04132 84 WIL LNO TACCEP TSOU D CHARGE S >750 KBTU/CHARG E 8 5 Hi/D I Atomizin g Ai rLo wpressure alar m (Manua l Check) 8 6 Lo/D I Atomizin g Ai rLo wpressure alar m (Manua l Check) 8 7 SpecialtyFeede rAtomizin g Ai rLo wPressure alar m (Manua l check ) OC L =CONDITIO N LIMI T AWF C =AUTOMATI C WAST E FEE D CUTOF F MWF C =MIS C WAST E FEE D CUTOF F SWF C =SPECIFl C WAST E FEE D CUTOF F PAS S FAI L

~7~

~ Z 1 ~ZL
z z ~ Z 7

ZZL

z z z

Comment s

CHECKE D BY : DATE:/l%/^O l TIME : /^< TAM<g ^ APPROVED : j/t%&L-/J*. /<^'M' PLACE : Contro l Roo m ,EEKLY_ 2 4/4/0 7 H K

VES01802 6J BIWEEKL YUNI T# 2 COMPLIANC E CHfC KSHEE T (CM S Tas k IC4039) PAG E 1 O F 2 OPERATIN G PARAMETER S PL C COI LBWCOI L 1 OC L TR VPOSITIO N (OPEN ) 01602 0040 1 2 OC L UPPE R CHAMBE R TEMP
. 1 mi n avg . 0160 3 00402 3 OC L H I BT U Ibs/h rMa x 0160 4 0040 3 4 OC L LOWE R CHAMBE R TEMP
. 1 mi n avg . 0160 5 00404 5 OC L LOBT U Ibs/h rMa x 0160 6 0040 5 6 OC L
. FLU E GA S HCL , 1 hr
. rollin g avg . 0160 7 0040 6 7 OC L FLU E GA S CO , 1 hr
. rollin g avg . 0160 8 0040 7 8 OC L FLU E GA S OPACITY , hig h fo r48 0 sec/hr
. avg . 0160 9 0040 8 9 OC L FLU E GA S OPACITY , hig h instantaneou s 0161 0 0040 9 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min
. avg 0161 1 0041 0 1 1 OC L HEATINPU Thig h mbtu/h r 0161 3 0041 1 1 2 OC L CHLORIN E INPUT , hig h Ibs/h r 0161 4 0041 2 1 3 OC L SOLI D FEED , hig h Ibs/h rMax
. 0152 6 0041 3 1 4 OC L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 8 0041 4 1 5 OC L SPECIALITYFEEDE D hig h Ibs/h rMax
. 0151 6 0041 5 1 7 AWF C SDAOUTLE TTEMP , high l min
. avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DIFF.PR
. DROP
. Low1 min
. avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min
. avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min
. avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min
. avg . 0159 7 . 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 8 00422 2 3 AWF C FLU E GA S FLO WRATE , hig h irtst
. 0159 9 0042 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min
. avg . 0160 1 00424 / 5 AWF C LO WCHAMBE R TEMP. , lo w1 hr
. avg . 0158 6 0042 5 1 6 AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . 0158 8 0042 6 2 7 AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 0158 9 0042 7 2 8 AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min
. 0162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 00430 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 0 00432 35 MWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 2 00435 3 6 MWF C HEATINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h Ibs/h r 0162 3 00437 3 8 MWF C E-STOP S orT/ C MODUL E inactive 0161 5 00438 3 9 MWF C FLU E GA S CO , hig h 1 hr
. avg . 0159 5 0043 9 4 0 MWF C ATOMIZE R hig h hig h vibratio n fo r5 sec . 0162 4 00440 4 1 SWF C SPEC
. FEE D Ibs/h rhig h 0157 6 0044 1 PAS S 

# / z z :

/ Z7Z

~ r z z . J

T / FAI L

VES01802 7" BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 2 O F 2 OPERATIN G PARAMETER S PL C COI L BWCOI L PAS S / 4 2 SWF C HIBT U Ibs/h rhig h 0157 8 0044 2 4 3 SWF C LOBT U Ibs/h rhig h 0158 0 00443 J. 45 SWF C HIBT U los s ofsigna l 0301 9 00445 J 4 6 SWF C LOBT U los s ofsigna l 0302 0 00446 4 7 SWF C SPECIALITYFEED/COMPRESSE D GA S FEE D los s ofsigna l 0302 1 00447 

## :/ , 4 8 MWF C NORT H & SOUT H IP S ALARM S FAILE D 0570 3 00448 h 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s ofsigna l 0302 2 00449 J 5 0 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 J 5 1 SWF C DIREC TINJEC T(commo n alarm ) 03132 0045 1 J 5 2 OP L Ba g Lea k Detectio n Syste m (Tribo) 

# / 6 5 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3 

# / 6 6 OP L Non-Pumpabl e 1 Hou rRollin g Tota l OP L 0820 6 0411 4 j 6 7 OP L Tota l wast e 1 Hou rRollin g Tota l OP L 0820 8 0411 5 

# / 6 8 OP L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 6 6 9 OP L Lo

wVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 7 0 OP L Sem i Volatil e 1 2 Hou rRollin g Tota l OP L 0821 6 0411 8

- J r - 7 1 OP L Mercur

y1 2 Hou rRollin g Tota l OP L 0821 8 0411 9

- J r - 7 2 OP L As h 1 2 Hou rRollin g Tota l OP L 0822 0 0412 0 — f - 7 3 OP L PC C Temperature 1 Hou rRollin g Averag e Lo wOP L 0822 2 0412 1 7 4 OP L SC C Temperature 1 Hou rRollin g Averag e Lo wOP L 0822 4 04122 

# / ' 75 OP L SD AOutlet Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 - 7 - 7 6 OP L Baghous e Differentia l Pressure 1 Minute Averag e LowOP L 0822 7 04124 - 7 - 7 7 OP L Baghous e Differentia l Pressure 1 Minute Averag e Hig h OP L 0822 8 0412 5 

## / OP L Stac k

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

C O Correcte d 1 Hou rRollin g Averag e Hig h OP L 0823 6 0412 7 v / 8 0 OP L Stac k

Flo w1 Hou rRollin g Averag e Hig h OP L 08244 0412 8 

# / 8 1 OP L BT U 1 Hou rTota l OP L 0820 9 0412 9 y. 8 2 OP L Hi t Cl/Hr a Lim e Flow1 Minute Averag e Hig h OP L 0825 1 04130 y 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Lo w 0815 6 0413 2 

## / 8 4 WIL LNO TACCEP TSOLI D CHARGE S >750 KBTU/CHARG E


# . / 8 5 Hi/D I Atomizin g Ai rLowpressure alar m (Manua l Check) y . 8 6 Lo/D I Atomizin g Ai rLo wpressur e alar m (Manua l Check) 

### / 8 7 SpecialtyFeede rAtomizin g Ai rLo wPressur e alarm (Manua l check ) 

### / OC L CONDITIO N LIMI T AWF C =AUTOMATI C WAST E FEE D CUTOF F MWF C =MIS C WAST E FEE D CUTOF F SWF C =SPECIFI C WAST E FEE D CUTOF F

Comments

CHECKE D BY : A.&^ IM DATE : /&- /Q -6 f TIME : / 0

J &A M (ti p APPROVED : PLACE : Contro l Roo m ,EEKLY_ 2 4/4/0 7 H K

VES01802 8•BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 1 O F 2 OPERATIN G PARAMETER S PL C COI LBWCOI L PAS S FAI L 1 OC L TR VPOSITIO N (OPEN ) 0160 2 0040 1 2 OC L UPPE R CHAMBE R TEMP
. 1 mi n avg . 0160 3 00402 3 OC L HIBT U Ibs/h rMa x 0160 4 0040 3 4 OC L LOWE R CHAMBE R TEMP
. 1 mi n avg . 0160 5 00404 5 OC L L O BT U lbs/h rMa x 0160 6 00405 6 OC L FLU E GA S HCL , 1 hr
. rollin g avg . 0160 7 00406 7 OC L FLU E GA S CO , 1 hr
. rollin g avg . 0160 8 0040 7 8 OC L FLU E GA S OPACITY , hig h for48 0 sec/hr
. avg . 0160 9 0040 8 9 OC L FLU E GA S OPACITY , hig h instantaneou s 0161 0 0040 9 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min
. av g 0161 1 0041 0 1 1 OC L HEATINPU Thig h mbtu/h r 0161 3 0041 1 1 2 OC L CHLORIN E INPUT , hig h Ibs/h r 0161 4 0041 2 1 3 OC L SOLI D FEED , hig h Ibs/h rMax
. 0152 6 0041 3 1 4 OC L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 8 0041 4 1 5 OC L SPECIALITYFEEDE D hig h Ibs/h rMax
. 0151 6 0041 5 1 7 AWF C SD AOUTLE TTEMP , high l min
. avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DIFF.PR
. DROP
. Low1 min
. avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min
. avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min
. avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min
. avg . 0159 7 0042 1 2 2 AWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 8 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h inst
. 0159 9 0042 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min
. avg . 0160 1 0042 4 ; 5 AWF C LO WCHAMBE R TEMP. , lo w1 hr
. avg . 0158 6 0042 5 z 6 AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . 0158 8 0042 6 2 7 AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 0158 9 0042 7 2 8 AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min
. 0162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 00430 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 0 00432 3 5 MWF C FLU E GA S HCL , hig h 1 min
. avg . 0159 2 00435 3 6 MWF C HEATINPU Thig h anticipate d 0162 2 0043 6 3 7 MWF C CHLORIN E INPUT , hig h Ibs/h r 0162 3 0043 7 3 8 MWF C E-STOP S orT/ C MODUL E inactive 0161 5 00438 3 9 MWF C FLU E GA S CO , hig h 1 hr
. avg . 0159 5 0043 9 4 0 MWF C ATOMIZE R hig h hig h vibratio n fo r5 sec . 0162 4 00440 4 1 SWF C SPEC
. FEE D Ibs/h rhig h 0157 6 0044 1 

# 5 1ZL 

# 5 z z 

# ± z : z 2 " 

# ^ 1

VES01802 9BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 2 O F 2 OPERATIN G PARAMETER S PL C COI L B WCOI L PAS S 42 SWF C HIBT U Ibs/h rhig h 0157 8 00442 4 3 SWF C LOBT U Ibs/h rhig h 0158 0 00443 

# y 4 5 SWF C HIBT U los s ofsigna l 0301 9 00445 

# <> 46 SWF C LOBT U los s ofsigna l 0302 0 00446 

# y 4 7 SWF C SPECIALITYFEED/COMPRESSE D GA S FEE D los s ofsigna l 0302 1 0044 7 4 8 MWF C NORT H & SOUT H IP S ALARM S FAILE D 0570 3 00448 

# y 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s ofsigna l 0302 2 0044 9 5 0 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 

# y 5 1 SWF C DIREC TINJECT(commo n alarm ) 03132 0045 1 

# y 5 2 OP L Ba g Lea k Detectio n Syste m (Tribo) 

# y 6 5 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3 

# y 6 6 OP L Non-Pumpabl e 1 Hou rRollin g Tota l OP L 0820 6 0411 4 

# y 6 7 OP L Tota l waste 1 Hou rRollin g Tota l OP L 0820 8 0411 5 

# y 6 8 OP L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 6 6 9 OP L LowVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 

# y 7 0 OP L Sem i Volatil e 1 2 Hou rRoilin g Tota l OP L 0821 6 0411 8 

# \y^<- 7 1 OP L Mercur

y1 2 Hou rRollin g Tota l OP L 0821 8 0411 9 72 OP L As h 1 2 Hou rRollin g Tota l OP L 0822 0 0412 0 

# y 7 3 OP L PC C Temperatur e 1 Hou rRollin g Averag e Lo wOP L 0822 2 0412 1 

# y 74 OP L SC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 4 0412 2 

# y 7 5 OP L SD AOutlet Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 7 6 OP L Baghous e Differentia l Pressure 1 Minute Averag e Lo wOP L 0822 7 04124 

# y 7 7 OP L Baghous e Differentia l Pressure 1 Minute Averag e Hig h OP L 0822 8 0412 5 OP L Stac k

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

# y t » OP L Stac k

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

# y 8 0 OP L Stac k

Flow1 Hou rRollin g Averag e Hig h OP L 08244 0412 8 

# y 8 1 OP L BT U 1 Hou rTota l OP L 0820 9 0412 9 8 2 OP L Hr

tCI/Hra Lim e Flow1 Minute Averag e Hig h OP L 0825 1 04130 

# y 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Low 0815 6 04132 

# y 8 4 WIL LNO TACCEP TSOLI D CHARGE S >750 KBTU/CHARG E 

# s 8 5 Hi/D I Atomizin g Ai rLo wpressure alar m (Manua l Check ) 8 6 Lo/D I Atomizin g Ai rLo wpressure alar m (Manua l Check ) 

# y 8 7 SpecialtyFeede rAtomizin g Ai rLowPressur e alar m (Manua l check ) 

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

Comments

CHECKE D BY : 

# ^^TT^^ ^ DAT E ://-//-£ ) TIME : 

## (am)p M A n °ROVED : ^//(Z^/^jc^ Jj' ^

PLACE : Contro l Roo m L -..v T£EKLY_ 2 4/4/0 7 H K

VES01803 0BIWEEKL YUNIT# 2

COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 1 O F 2 OPERATIN G PARAMETER S 1 OC L TR VPOSITIO N (OPEN ) 2 OC L UPPE R CHAMBE R TEMP
. 1 mi n avg . 3 OC L H I BT U lbs/h rMa x 4 OC L LOWE R CHAMBE R TEMP
. 1 mi n avg . 5 OC L LOBT U Ibs/h rMa x 6 OC L FLU E GA S HCL , 1 hr
. rollin g avg . 7 OC L FLU E GA S CO , 1 hr
. rollin g avg . 8 OC L FLU E GA S OPACITY , hig h fo r48 0 sec/hr
. avg . 9 OC L FLU E GA S OPACITY , hig h instantaneou s 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min
. avg 1 1 OC L HEATINPU Thig h mbtu/h r 1 2 OC L CHLORIN E INPUT , hig h Ibs/h r 1 3 OC L SOLI D FEED , hig h Ibs/h rMax
. 1 4 OC L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 1 5 OC L SPECIALITYFEEDE D hig h Ibs/h rMax
. 1 7 AWF C SD AOUTLE TTEMP , high l min
. avg . 1 8 AWF C BA G HOUS E DIFF.PR
. DROP
. Lo w1 min
. avg . 1 9 AWF C FLU E GA S CO , hig h 1 min
. avg . 2 0 AWF C FLU E GA S 02 , lo w1 min
. avg . 2 1 AWF C FLU E GA S HC , hig h 1 min
. avg . 2 2 AWF C FLU E GA S HCL , hig h 1 min
. avg . 2 3 AWF C FLU E GA S FLO WRATE , hig h inst
. 2 4 AWF C FLU E GA S OPACITY , hig h 1 min
. avg . ' 5 AWF C LO WCHAMBE R TEMP. , lo w1 hr
. avg . Js AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . 2 7 AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 2 8 AWF C FAILE R O F PROCES S MONITO R 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min
. 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 3 2 MWF C AL LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 3 5 MWF C FLU E GA S HCL , hig h 1 min
. avg . 3 6 MWF C HEATINPU Thig h anticipate d 3 7 MWF C CHLORIN E INPUT , hig h Ibs/h r 3 8 MWF C E-STOP S o rT/C MODUL E inactive 3 9 MWF C FLU E GA S CO , hig h 1 hr
. avg . 4 0 MWF C ATOMIZE R hig h hig h vibratio n fo r5 sec . 4 1 SWF C SPEC
. FEE D Ibs/h rhig h PL C COI LBWCOI LPAS S FAI L 01602 0040 1 

# / 0160 3 0040 2

- y 01604 0040 3 0160 5 00404 0160 6 0040 5 0160 7 0040 6 0160 8 0040 7 0160 9 0040 8 s/ 0161 0 0040 9 0161 1 0041 0 s 

# y 0161 3 0041 1 v / 0161 4 0041 2 y 0152 6 0041 3 0153 8 0041 4 0151 6 0041 5 

# y 0159 1 0041 7 

# y 0159 3 0041 8 

# y 0159 4 0041 9 

# y 0159 6 0042 0 

# y 0159 7 0042 1 

# y 0159 8 0042 2 

# y 0159 9 0042 3 0160 1 0042 4 

# y 0158 6 0042 5 

# y 0158 8 0042 6 

# y 0158 9 0042 7 

# y 0152 7 0042 8 0162 5 0042 9 0160 0 0043 0 

# y 0174 0 00432 

# y 0159 2 00435 

# y 0162 2 00436 

# y 0162 3 0043 7 

# y 0161 5 00438 

# y 0159 5 0043 9 

# y 0162 4 0044 0 

# y 0157 6 0044 1 V

VES01803 1BIWEEKLYUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039 ) PAG E 2 O F 2 OPERATIN G PARAMETER S PL C COI LBWCOI L PAS S FAI L 4 2 SWF C HIBT U Ibs/h rhig h 0157 8 0044 2 43 SWF C LOBT U Ibs/h rhig h 0158 0 0044 3 4 5 SWF C HIBT U los s o fsigna l 0301 9 0044 5 46 SWF C LOBT U los s o fsigna l 0302 0 0044 6 47 SWF C SPECIALITYFEED/COMPRESSE D GA S FEE D los s ofsigna l 0302 1 0044 7 48 MWF C NORT H & SOUT H IP S ALARM S FAILE D 0570 3 0044 8 49 SWF C UPPE R CHAMBE R SECONDAR YFUE Llos s o fsigna l 0302 2 0044 9 50 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 5 1 SWF C DIREC TINJEC T(commo n alarm ) 03132 0045 1 52 OP L Ba g Lea k Detectio n Syste m (Tribo) 65 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3 66 OP L Non-Pumpabte 1 Hou rRollin g Tota l OP L 0820 6 0411 4 67 OP L Tota l wast e 1 Hou rRollin g Tota l OP L 0820 8 0411 5 68 OP L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 6 69 OP L LowVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 70 OP L Sem i Volatil e 1 2 Hou rRollin g Tota l OP L 0821 6 0411 8 7 1 OP L Mercur

y1 2 Hou rRollin g Tota l OP L 0821 8 0411 9 72 OP L As h 1 2 Hou rRollin g Tota l OP L 0822 0 0412 0 73 OP L PC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 2 0412 1 7 4 OP L SC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 4 0412 2 7 5 OP L SD AOutlet Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 7 6 OP L Baghous e Differentia l Pressur e 1 Minute Averag e Lo wOP L 0822 7 0412 4 7 7 OP L Baghous e Differentia l Pressure 1 Minute Averag e Hig h OP L 0822 8 0412 5 OP L Stac k

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

C O Correcte d 1 Hou rRollin g Averag e Hig h OP L 0823 6 0412 7 80 OP L Stac k

Flo w1 Hou rRollin g Averag e Hig h OP L 08244 0412 8 8 1 OP L BT U 1 Hou rTota l OP L 0820 9 0412 9 8 2 OP L Hr

tCl/Hr a Lim e Flo

w1 Minute Averag e Hig h OP L 0825 1 0413 0 8 3 AWF C Lim e Slurr

yDensit y1 Hou rRollin g Averag e Low 0815 6 0413 2 8 4 WIL LNO TACCEP TSOLI D CHARGE S >75 0 KBTU/CHARG E 85 Hi/D I Atomizin g Ai rLowpressure alar m (Manua l Check) 86 Lo/D I Atomizin g Ai rLowpressure alar m (Manua l Check) 8 7 SpecialtyFeede rAtomizin g Ai rLo wPressure alar m (Manua l check ) OC L =CONDITIO N LIMI T AWF C =AUTOMATI C WAST E FEE D CUTOF F MWF C =MIS C WAST E FEE D CUTOF F SWF C =SPECIFI C WAST E FEE D CUTOF F 

# ./ _ z z

_^X
_

- X 

# 1
_ x _ 

# : £ 

# i

Comments

CHECKE D BY : J-S^-
. 1 .^A-M ? 0ATE

jD~Z<Z-d1 TIME : j^g> M APPROVED : /^^^Z-/^ ^ /^V WPLACE : Contro l Roo m L , . , cEKLY_ 2 4/4/0 7 H K

VES01803 2BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 1 O F 2 OPERATIN G PARAMETER S PL C COI LBWCOI L 1 OC L TR VPOSITIO N (OPEN ) 0160 2 0040 1 2 OC L UPPE R CHAMBE R TEMP
. 1 mi n avg . 0160 3 00402 3 OC L H I BT U Ibs/h rMa x 0160 4 0040 3 4 OC L LOWE R CHAMBE R TEMP
. 1 mi n avg . 0160 5 00404 5 OC L L O BT U lbs/h rMa x 0160 6 00405 6 OC L FLU E GA S HCL , 1 hr
. rollin g avg . 0160 7 00406 7 OC L FLU E GA S CO , 1 hr
. rollin g avg . 0160 8 00407 8 OC L FLU E GA S OPACITY , hig h fo r48 0 sec/hr
. avg . 0160 9 00408 9 OC L FLU E GA S OPACITY , hig h instantaneou s 0161 0 0040 9 1 0 OC L FLU E GA S FLO WRATE , hig h 1 min
. av g 0161 1 0041 0 1 1 OC L HEATINPU Thig h mbtu/h r 0161 3 0041 1 1 2 OC L CHLORIN E INPUT , hig h Ibs/h r 0161 4 0041 2 1 3 OC L SOLI D FEED , hig h Ibs/h rMax
. 0152 6 0041 3 1 4 OC L UPPE R CHAMBE R TEMP , lo w1 h rrollin g avg . 0153 8 0041 4 1 5 OC L SPECIALITYFEEDE D hig h Ibs/h rMax
. 0151 6 0041 5 1 7 AWF C SDAOUTLE TTEMP , high l min
. avg . 0159 1 0041 7 1 8 AWF C BA G HOUS E DIFF.PR
. DROP
. Lo w1 min
. avg . 0159 3 0041 8 1 9 AWF C FLU E GA S CO , hig h 1 min
. avg . 0159 4 0041 9 2 0 AWF C FLU E GA S 02 , lo w1 min
. avg . 0159 6 0042 0 2 1 AWF C FLU E GA S HC , hig h 1 min
. avg . 0159 7 0042 1 2 2 AWF C FLU E GA S HC U hig h 1 min
. avg . 0159 8 0042 2 2 3 AWF C FLU E GA S FLO WRATE , hig h iiist
. 0159 9 0042 3 2 4 AWF C FLU E GA S OPACITY , hig h 1 min
. avg . 0160 1 00424 '•> 5 AWF C LO WCHAMBE R TEMP. , lo w1 hr
. avg . 0158 6 0042 5 2 6 AWF C LOWE R CHAMBE R PRESS , hig h fo r5 sees . 0158 8 0042 6 2 7 AWF C UPPE R CHAMBE R PRESS , hig h fo r5 sees . 0158 9 0042 7 2 8 AWF C FAILE R O F PROCES S MONITO R 0152 7 0042 8 2 9 AWF C I D FA N FAILUR E o rhig h hig h vibratio n fo r5 min
. 0162 5 0042 9 3 0 AWF C Uppe ro rLowe rChambe rTemp , hig h 0160 0 00430 3 2 MWFC AL LWAST E FEE D OF F FRO M FI X(manuall yshu toff ) 0174 0 0043 2 3 5 MWFC FLU E GA S HCL , hig h 1 min
. avg . 0159 2 00435 3 6 MWF C HEATINPU Thig h anticipate d 0162 2 00436 3 7 MWFC CHLORIN E INPUT , hig h Ibs/h r 0162 3 00437 3 8 MWFC E-STOP S orT/ C MODUL E inactive 0161 5 00438 3 9 MWF C FLU E GA S CO , hig h 1 hr
. avg . 0159 5 0043 9 4 0 MWFC ATOMIZE R hig h hig h vibratio n fo r5 sec . 0162 4 00440 4 1 SWF C SPEC
. FEE D Ibs/h rhig h 0157 6 0044 1 PAS S

ZZLZ 

# I

r z :

zlz i FAI L

VES01803 3BIWEEKL YUNI T# 2 COMPLIANC E CHEC KSHEE T (CM S Tas k IC4039) PAG E 2 O F 2 OPERATIN G PARAMETER S PL C COI L BWCOI L PAS S 42 SWF C HIBT U Ibs/h rhig h 0157 8 00442 

# / 4 3 SWF C LOBT U Ibs/h rhig h 0158 0 00443 

# y 4 5 SWF C HIBT U los s ofsigna l 0301 9 00445 

# y 4 6 SWF C LOBT U los s o fsigna l 0302 0 00446 

# y 4 7 SWF C SPECIALITYFEED/COMPRESSE D GA S FEE D los s ofsigna l 0302 1 00447 

# y 4 8 MWF C NORT H & SOUT H IP S ALARM S FAILE D 0570 3 00448 

# y 4 9 SWF C UPPE R CHAMBE R SECONDAR YFUE Lios s o fsigna l 0302 2 0044 9 

# y 5 0 MWF C NORT H & SOUT H IP S SERVERSFAILE D 0570 5 0045 0 

# y 5 1 SWF C DIREC TINJEC T(commo n alann ) 0313 2 0045 1 

# y 5 2 OP L Ba g Lea k Detectio n Syste m (Tribo) 

# y 6 5 OP L Pumpabl e 1 Hou rRollin g Tota l OP L 0820 5 0411 3 

# y 6 6 OP L Non-Pumpabl e 1 Hou rRollin g Tota l OP L 0820 6 0411 4 

# y 6 7 OP L Tota l wast e 1 Hou rRollin g Tota l OP L 0820 8 0411 5 

# y 6 8 OP L C L1 2 Hou rRollin g Tota l OP L 0821 1 0411 6 6 9 OP L LowVolatil e 1 2 Hou rRollin g Tota l OP L 0821 4 0411 7 

# <y 7 0 OP L Sem i Volatil e 1 2 Hou rRollin g Tota l OP L 0821 6 0411 8 

# y 7 1 OP L Mercur

y1 2 Hou rRollin g Tota l OP L 0821 8 0411 9 

# y 7 2 OP L As h 1 2 Hou rRollin g Tota l OP L 0822 0 0412 0 7 3 OP L PC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 2 0412 1 

# y\ 7 4 OP L SC C Temperatur e 1 Hou rRollin g Averag e LowOP L 0822 4 0412 2 

# y y 7 5 OP L SDAOutlet Temperatur e 1 Hou rRollin g Averag e Hig h OP L 0822 6 0412 3 

# y y 7 6 OP L Baghous e Differentia l Pressure 1 Minut e Averag e Lo wOP L 0822 7 0412 4 7 7 OP L Baghous e Differentia l Pressure 1 Minut e Averag e Hig h OP L 0822 8 0412 5 / 8 OP L Stac k

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

# y 7 9 OP L Stac k

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

- y 8 0 OP L Stac k

Flo w1 Hou rRollin g Averag e Hig h OP L 0824 4 0412 8

- y 8 1 OP L BT U 1 Hou rTota l OP L 0820 9 0412 9 

# y. 8 2 OP L Hr

tCl/Hr a Lim e Flo

w1 Minute Averag e Hig h OP L 0825 1 0413 0 y 8 3 AWF C Lim e Slurr yDensit y1 Hou rRollin g Averag e Low 0815 6 04132 

# y 8 4 WIL LNO TACCEP TSOLI D CHARGE S >750 KBTU/CHARG E 

# y 8 5 Hi/D I Atomizin g Ai rLowpressure alar m (Manua l Check ) 

# y 8 6 Lo/D I Atomizin g Ai rLowpressure alar m (Manua l Check) 8 7 SpecialtyFeede rAtomizin g Ai rLowPressure alarm (Manua l check ) 

# y OC L =CONDITIO N LIMIT AWF C =AUTOMATI C WAST E FEE D CUTOF F MWFC =MIS C WAST E FEE D CUTOF F SWF C =SPECIFI C WAST E FEE D CUTOF F

Comments

DATE : P M PLACE : Contro l Roo m CHECKE D BY : A^-T TA „ ^1/ "PROVED : ^/<SL&L/^ c /<ft'i^ t$IWEEKLY_2 4/4/0 7 H K

VES01803 4

### ABSOLUT E CALIBRATIO N AUDIT(ACA ) DAT ASHEE T

Unit # 2Seria l #
Paramete r NIS TTraceabl e Calibratio n Standard s > 0 2 25 % G a s Concentratio n r CO-lo wrang e 200pp m Lo w(Zero ) 0 

# + 0. 5 r CO-hig h rang e 3000pp m Mi d 8.9 3 

# ± 0. 5 rHC I 1000pp m Hig h 1 5 

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

Referenc e Analyze r Lo w Mi d Hig h 1-Low 0 0 0 — — 2-Mi d 8.9 3 9. 1 — -0.1 7 — 3-Hig h
. 15 15. 1

— • — -0. 1 4-Lo w 0 0 0 — — 5-Mi d 8.9 3 9 — -0.0 7 — 6-Hig h 1 5 15. 3 — — -0. 3 7- I n w n n n 8-Mi d 8.9 3 9. 1 — -0.1 7 — 9-Hig h 1 5 •15. 2 — — -0. 2 Mea n Differenc e = 0.0 0 -0.1 4 -0.2 0 Calibratio n Erro r= 0.00 % -0.55 % -0.80 % Calibratio n Erro r=

= Mea n Differenc e /

Spa n Valu e * 10 0

Bria n Bunfil l E/J Tec h Nam e Titl e 9/25/200 9 Signatur e 2/4/201 0 Dat e

VES01803 5

### ABSOLUT E CALIBRATIO N AUDIT(ACA ) DAT ASHEE T

Unit # Seria l # 34 6
Paramete r r 0 2 25 % '< * CO-lo wrang e 200pp m rCO-hig h rang e 3000pp m r HC I 1000pp m NIS TTraceabl e Calibratio n Standard s Paramete r r 0 2 25 % '< * CO-lo wrang e 200pp m rCO-hig h rang e 3000pp m r HC I 1000pp m G a s Concentratio n Paramete r r 0 2 25 % '< * CO-lo wrang e 200pp m rCO-hig h rang e 3000pp m r HC I 1000pp m Lo w(Zero ) 0 

# ± 1 0 Paramete r r 0 2 25 % '< * CO-lo wrang e 200pp m rCO-hig h rang e 3000pp m r HC I 1000pp m Mi d 68. 9 

# ± 1 0 Paramete r r 0 2 25 % '< * CO-lo wrang e 200pp m rCO-hig h rang e 3000pp m r HC I 1000pp m Hig h 15 3 

# ± 1 0 •

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

Bria n Bunfil l E/ l Tec h Nam e Signatur e Titl e 9/25/200 9 2/4/201 0 Dat e Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w Mi d Hig h 1-Lo w 0 0. 1 -0. 1 — — 2-Mi d 68. 9 71. 7 — -2. 8 — 3-Hig h 15 3 152. 7 — — 0. 3 4-Lo w 0 0. 4 -0. 4 — — 5-Mi d 68. 9 71. 9 — - 3 — 6-Hig h 15 3 152. 8 — — 0. 2 0 0. 6 ,0.6 — — « 8-Mi d 68. 9 71, 6 — -2. 7 — 9-Hig h 15 3 152. 6
. — — 0. 4 Mea n Differenc e = -0.3 7 -2.8 3 0.3 0 Calibratio n Erro r= -0.18 % -1.42 % 0.15 %

### ABSOLUT E CALIBRATIO N AUDIT(ACA ) DAT ASHEE T

Unit # Seria l # 34 6
Paramete r r0 2 25 % f" ' CO-lo wrang e 200pp m CO-hig h rang e 3000pp m r HC I 1000pp m NIS TTraceabl e Calibratio n Standard s Paramete r r0 2 25 % f" ' CO-lo wrang e 200pp m CO-hig h rang e 3000pp m r HC I 1000pp m G a s Concentratio n Paramete r r0 2 25 % f" ' CO-lo wrang e 200pp m CO-hig h rang e 3000pp m r HC I 1000pp m Lo w(Zero ) 0 

# ± 15 0 Paramete r r0 2 25 % f" ' CO-lo wrang e 200pp m CO-hig h rang e 3000pp m r HC I 1000pp m Mi d 1079. 1 

# ± 15 0 Paramete r r0 2 25 % f" ' CO-lo wrang e 200pp m CO-hig h rang e 3000pp m r HC I 1000pp m Hig h 2220 

# + 15 0 Ru n Numbe r Concentratio n Differenc e

Referenc e Analyze r Lo w Mi d Hig h 1-Low 0 0. 1 -0. 1 — — 2-Mi d 1079. 1 1151. 9 — -72. 8 — 3-Hig h 222 0 2217. 4 — — 2. 6 4-Lo w 0 0. 4 -0. 4
. — — 5-Mi d 1079. 1 1095. 3 — -16. 2 — 6-Hig h 222 0 2182. 5 — — 37.5
. 7-Lo w . _ 0 —0J 3
. _,0.6..
. — r— 8-Mi d 1079. 1 1091 2 — -12. 1 — 9-Hig h 222 0 2178. 4 — — 41. 6 Mea n Differenc e = -0.3 7 -33.7 0 27.2 3 Calibratio n Erro r= -0.01 % -1.12 % 0.91 % Calibratio n Erro r= Mea n Differenc e / Spa n Valu e * 10 0
Bria n Bunfil l E/ITec h Nam e 

# U S Signatur e Titl e 9/25/200 9 2/4/201 0 Dat e

### ABSOLUT E CALIBRATIO N AUDI T(ACA ) DAT ASHEET

Unit # 2Seria l #
Paramete r NIS TTraceabl e Calibratio n Standard s r0 2 25 % G a s Concentratio n r CO-lo wrang e 200pp m Lo w(Zero ) 0 

# + 50 r CO-hig h rang e 3000pp m Mi d 31 8 

# + 5 0 HC I 1000pp m Hig h 74 3 

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

Referenc e Analyze r Lo w Mi d Hig h 1-Lo w 0 0 0 — — 2-Mi d 31 8 276. 5 — 41. 5 — 3-Hig h .74 3 741. 1 • — — 1. 9 4-Lo w 0 0 0 — — 5-Mi d 31 8 312. 4 — 5. 6 — 6-Hig h 74 3 738. 1 — — 4. 9 7-Lo w 0 0
. . . . 0

— ... . .. . 8-Mi d 31 8 323. 1 — -5. 1 — 9-Hig h 74 3 73 9 — — 4 Mea n Differenc e = 0.0 0 14.0 0 3.6 0 Calibratio n Erro r= 0.00 % 1.40 % 0.36 % Calibratio n Erro r= Mea n Differenc e / Spa n Valu e * 10 0

Bria n Bunfil l Nam e Signatur e

VES01803 8 E/ l Tec h Titl e 9/26/200 9 Dat e 2/4/201 0Tabl e 1 Summar yo fRelativ e Accurac yTes tAudi t Result s

Veoli a E S Technica l Solution s Sauget , Illinoi s Jun e 22,2 3 an d 24,200 9 CEM S Paramete r Unit s Measure d R A Criteri a Pass/Fai l Uni t 2 C O pp m @ 7 % 0 2 0.00 4 ppm a Pas s Uni t 2 0 2 , dry % o 2 0.09% a 1. 0 a ' c Pas s Uni t 2
Oi, we t % o 2 0.13% a 1. 0 a ' c Pas s Uni t 3 C O pp m @ 7 % 0 2 0.06 3 ppm a 5 a. b Pas s Uni t 3 0 2 , dry % o 2 0.02% a 1. 0 a - c Pas s Uni t 3 Oi, we t % o 2 0.31% a 1. 0 a ' c Pas s Uni t 4 C O pp m @ 7 % 0 2 1.14 6 ppm 1 5 a. b Pas s Uni t 4 O z , dry % 0 2 0.15% a 1. 0 a ' c Pas s Uni t 4 0 2 , we t % o 2> 0.46% a 1. 0 a ' c Pas s

aPercen to femissio n standard o rabsolut e averag e differenc e (pp m o r%)
. b PS4B
. cP S 3
.

/

JUL Y7 , 200 9 CE C Projec t 090-86 1 INCINERATO R CEMS RAT

A VEOLIAES
VES01803 9Incinerato r Dat a Poin t "Veoli a Environmenta

l Service

s Sauge tIllinoi s Create d Perio d Star t Perio d E n 1/1/2010 6:0 0 A M 1/1/2010 6:0

0 A M 1/1/201 0 6:0 0 A M Pag e 1 of 7

IMi n AV G War n 1 Mi n AV G Shu t IMi n 1 H rRoll 1 H rRol l 1 HrRol l I HrRoll 1 HrRol l 1 H rRol l 1 2 H r1

2 H r1

2 H rlHrTo tlHrTo tlHrTo t AV G War

n Shu

tOPL TotTo tShu tTotOPL Rol l TotRoll To tRol l TotWar

n Shu

tOPL OPL War n War n Shu

tOPL Thermodynami cBT U HCLtoLim e Stac k C O Correcte d LimeSlurryDensity Stac k HC L Correcte d Stac k HC L RCR A Stac k 0 2 Correcte d Stac k 0 2 Ra w Stac k Opacity Stac k Flo w SD AOutle t Tem p Baghous e Dif

f Pres s Lo w Baghous e Dif

f Pres s Hig h 9.00000 0 10.0000

0 25.0000 0 28.0000

0 33.5000

0 450.000 0 500.000

0 67.5000 0 0.00000

0 450.000 0 500.000

0 450.000 0 500.000

0 4.00000 0 4.00000 0 3.00000

0 8.00000 0 10.0000

0 15000.0 0 . . 430.000 0 500.000

0 3.00000 0 2.00000

0 30.0000 0 75.0000

0 100.000

0 67.5000 0 67.3000

0 67.0000

0 25.0000 0 32.0000

0 20.0000 0 25.0000

0 100.000

0

14600.0 0 14950.0

0 15147.0

0 417.000 0 418.000

0 420.000

0 15.0000 0 15.5000

0 16.0000

0

VES01804 0Stac k TH C Lo wBT U Weigh t Specia l Fee d Weigh t Hig h BT U Weigh t Solid s Weigh t PC C Tem p SC C Tem p Stac k C O RCR A Liqui d Weigh t Weigh t Chlonn e Mercur y As h Lo wVolatil e Sem i Volatil e 8.00000 0 10.0000

0

1750.00 0 1590.00

0 1860.00 0 1794.00

0 450.000 0 500.000

0 Veoli a Environmenta

l Service

s Sauge tIllinoi s

1000.00 0 1020.00

0 1053.00

0 1775.00 0 1742.00

0 1734.00

0 1880.00 0 1854.00

0 1849.00

0 50.0000 0 90.0000

0 100.000

0 2850.00

0 2950.00

0 3107.00

0 3750.00 0 3850.00

0 4017.00

0 200.000 0 218.000

0 0.00300 0 0.00340

0 625.000 0 673.000

0 Create d Perio d Star t Perio d E n 1/1/201 0 6:0 0 A M 1/1/201 0 6:0 0 A M 1/1/201 0 6:0 0 A M Pag e 2 of 7

. 1900.00

0 1933.00

0 1993.00

0

. 600.000

0 664.000

0 724.000

0

. 1900.00

0 1952.00

0 2012.00

0

. 1000.00

0 1020.00

0 1053.00

0

40.0000 0 46.0000

0 56.0000 0 63.0000

0 . 2400.00 0 2500.00

0 2616.00

0 200.000

0 217.000

0 233.000

0

. 0.03000

0 0.03400

0 0.04080

0

. 7500.00

0 8000.00

0 8076.00

0

. 500.000

0 530.000

0 552.000

0

. 700.000

0 730.000

0 756.000

0

VES01804 1

## Facilit yOxyge n Data

VES01804 2December , 200 9 Averag e Oxyge n Concentration s fo rUnit s 2 , 3 , an d 4
Uni t 2 Metho d 5/2 6 Metho d 0023 A

Dat e We t 0 2 Dr y0 2 We t 0 2 Dr y0 2

(% ) {%

) (% ) (%

) 12/8/200 9 5. 6 10. 3 4. 8 9. 1 12/9/200 9 5. 8 10. 4 5. 1 9. 3 12/10/200 9 5. 1 9. 3 4. 3 8. 2

Uni t 3 Metho d 5/2 6 Metho d 0023 A

Dat e We t 0 2 Dr y0 2 We t 0 2 Dr y0 2

(% ) (%

) (% ) (%

) 12/1/200 9 5. 7 9. 5 4. 0 7. 3 12/2/200 9 4. 5 7. 8 4. 1 7. 3 12/3/200 9 6. 2 10. 4 5. 6 9. 5

Uni t 4 Metho d 5/2 6 Metho d 0023 A

Dat e We t 0 2 Dr y0 2 We t 0 2 Dr y0 2

(% ) (%

) (% ) (%

) 12/16/200 9 8. 6 12. 7 7. 7 12. 6 12/17/200 9 7. 9 12. 5 8. 0 12. 4 12/18/200 9 7. 3 12. 6 6. 9 12. 3C D

VES01804 4

# AECOM

Appendi xB Referenc e Metho d Fiel d Dat a an d Calculation s

VES01804 5Metho d 5/26 A

VES01804 6Particulat e Result s Summar y Uni t 2 Veoli a E S Technica l Solution s

Sauget , I L Tes tResults : Ru n 1 Ru n 2 Ru n 3 Average Particulat e Emission Concentration : grains/dsc f0.0009 6 0.0013

0 0.0006

7 0.0009

8 grains/dscf@7

% 0 2 0.0012 6 0.0017

2 0.0008

0 0.0012

6

Where : Particulat

e Emissio n CoricentFatiorr

VES01804 7Parameter : Molecular Weight Ru n 1

(Total mg)'mg/dscm;

(ppm®

(IWhr) 7%02) Result s Summar y Uni t 2 Veoli a E S Technica l Solution s

Sauget , I L Ru n 2 (Total mg)'mg/dscm' t (ppm@

(Ib/hr) 7%02) Ru n 3 (Total mgymg/dscm)

(ppm@

(Ib/hr) 7%02) Averaq e (mg/dscm)

(ppm@

(Ib/hr) 7%02) HC I CL 2 Tota l I 38.4

6 | I 16.

7 O S | 0. 4 13. 2 0. 2 13, 4 0.3 1 0.0 1 2.0

| 18. 2 I 0. 5 I 0. 4 15. 9 0. 2 16. 0 0.4 1 0.0 1 I 32.

4 | 27. 6 21.

8 0.6 1 20.

4 17. 0 04 4 I 4. 9 | 4. 2 1. 7 0.0

9 1.

7 0. 7 0.0

4 23. 5 17. 7

Where :

pprtw d @ 7%Q ? * part ? pe rmillio n « 7ViOxyaett=^maiHssltl'2 4 0 4 [it$tS/mo(Jftno

l Svfn*«a o 8-?}r(2 D S-QS'M S j

VES01804 8Calculation s Summar y Uni t 2 Veoli a E S Technica l Solution s

Sauget , I L
Vw(std) , sc

f= Vm(std) , dsc

f= Bws = Md = Ms = Vs , ft/se c = Qs , acfm = Qs(std) , dscfm = Isokineti c Samplin g Rate , % Ru n 1 30.78 4 38.51 0 0.44 4 29.79 24.55 31. 0 15,45 3 5,35 2 98. 2 Ru n 2

32.139 42.729 0.42 9 29.7 3 24.69 33. 4 16,63 4 5,96 3 97. 8 Ru n 3

31.523 41.44 7 0.43 2 29.6 7 24.6 3 33. 5 16,661 5,921 95. 6 Averaq e

31.48 2 40.89 5 0.43 5 29.7 3 24.6 2 32. 6 16,25 0 5,74 5 97. 2

Where : Vwfstd ^ =

, volume ofwatervapo ri n gas , standar d renditions ; = 0.O4707'*Vlc

M d > = nttteeula rweight o

fstadias , dr

ybasts = (

Q 4 4 x%CQ2) + (0.3

2 x%02) + [&28 X(%N2+ %CO) J |Vs = Stack

ga s velocit y= 85.4- 9 xC p XS q Rf . dP) xfSq.Rf . (Ts(R»W s XPS) ] QS(S« ) *-stackga s flowrate, standar d eondilwn s *Q s xt>Bws) x$287{rs{Rft. x(Ps/2S.92 >Tes t Dat a Summar y Uni t 2 Veoli a E S Technica l Solution s

Sauget , I L Paramete r Ru n Dat e Star t Tim e Stop Tim e Duratio n o

fRun , Minute

s Ave . Nozzl e Diameter, inches Pito t Calibratio n Factor , C F Mete rGamm a Mete rDelta H , inche

s o fH2 0 Stac k Diameter , inche

s Rectangula rWidth , inches Rectangula rLength , inches Stac k Area , sq.ft . Barometri c Pressure , inches o fH g Stati c Pressure , inche

s o fH2 0 Dr vGa s Mete rSampl e Volume . rVM)ft 3 Initia l Fina l Difference Ave . Stac k

Temperature , Ts(F

) Ave . Mete rTemperature , Tm(F ) Ave . Ru n Delta H , inche s o fH2 0 Ave . Square Roo

t o fDelt a P Ru n 1 12/08/09 10:0 5 11:1 1 6 0 0.43 1 0.84 0.99 1 1.801 3 9

8.3 0 29. 6 -0.0 7
55.894 93.807 37.91 3 378. 0 51. 3 1.3 5 0.402 6 Ru n 2 12/09/0 9 9:4 6 10:4 9 6 0 0.43 1 0.8 4 0.991 1.80 1 3 9

8.30 29. 3 -0.07
204.08 245.11 2 41.032 363. 1 34. 0 1.6 1 0.4363 Ru n 3 12/10/0 9 11:0 0 12:0 3 60 0.43 1 0.8 4 0.991 1.80 1 3 9

8.30 29. 8 -0.06
373.656 414.056 40. 4 380. 4 50. 0 1.5 7 0.4356 Moistur e Data Volum e o

fwate rcollected , mi s Silic a Gel , gram s Tota l Collected , mi s 64 6 I 8 65 4 675 7. 8 682. 8 654 15. 7 669. 7 ORSA TData

%0 2 %C0 2 %CO 10. 3 8. 6 10.4 8. 2 9. 3 8. 1

VES01805 0Fiel d Dat a Summar

y Uni t 2 Veoli a E S Technica l Solution s Sauget , I L
Stack TempJF) Delta

P Do/ M W SQR

r Delta? Slac

k Tempff ) Delta P Delt a H TmtF) SQRT

Delta P Stack

Tempfff Delta

P Delta H TmF) SQRT

Delta P Stack TempJF) Delta

P Do/ M W In out SQR

r Delta? Slac

k Tempff ) Delta P Delt a H in

out SQRT

Delta P Stack

Tempfff Delta

P Delta H In out SQRT

Delta P 37 9 0.1 8 1. 5 4 3 4 6 0.424 3 35

4 0.2 1 1.7 5 2 9 3 4 0.458 3 i : •i 37 7 0.2 1 1.7 0 3 0 3 8 0.458 3 38 0 0.19 1. 6 4 3 4 8 0.435 9 3S

4 0.2 3 1.S 0 3 0 3 7 0.479 6 37

8 0.2 1 1.7 0 3 4 4 6 0.468 3 36 0 0.19 1. 6 4 4 5 2 0.435 9 36

4 0.2 2 1.8 0 3 0 3 8 0.469 0 : • j : 37 9 0.2 0 1.6 5 3 7 5 2 0.447 2 37 9 0.19 1. 6 4 5 5 4 0,435 9 36

6 0.2 0 1.7 0 3 0 3 9 0.447 2 [ : : | 37 9 0.2 2 1.8 0 3 9 5 6 0.469 0 37 6 0.1 4 1. 2 4 5 5 5 0,374 2 36

4 0.1 5 1.2 5 3 0 3 9 0.3B7 3 ! : 37

8 0.18 1.5 0 4 2 5 8 0.424 3 37 5 0.0 9 0.7 5 4 6 5 5 0.300 0 35

2 0.10 0.8

3 3 0 3 8 0.316 2 i ; I : 37

2 0.10 0.8 2 4 3 5 9 0.316 2 37 6 0.19 1. 8 4 0 5 5 0.435 9 36

3 0.2 1 1.7 5 2 9 3 7 0.456 3 i : 38

3 0.2 2 1.8 0 4 9 5 9 0.469 0 37 9 0.18 1. 5 4 S S S 0.424 3 36

3 0.2 0 1.7 0 3 0 3 8 0.447 2 i l 38

4 0.2 2 1.8 0 4 7 6 1 0.469 0 37 7 0.18 1. 5 4 9 5 0 0.424 3 36

4 0.2 3 i.9 0 3 0 3 9 0.479 6 • ; 38 5 0.2 0 1.6 5 4 8 6 2 0.447 2 37 9 0.1 8 1. 5 5 0 6 1 0.424 3 36

4 0.2 1 1.7 5 3 0 4 0 0.458 3 i : 38

5 0.2 1 1.7 0 4 9 6 3 0.468 3 37 9 0,16 1. 3 5 1 6 2 0.400 0 36

5 0.2 0 1.7 0 3 0 4 0 0.447 2 ; i ! ; 38 4 0.19 1.6 0 5 1 6 3 0.435 9 37 8 0.10 0, 8 5 2 6 2 0.316 2 36

4 0.1S 1.2

5 3 0 4 0 0.387 3 : • i l 38 1 0.1 4 1.1 5 5 2 6 4 0.374 2

378. 0 0.16 4 1.3 5 4 7 '5 6 0.402 6 363.1 0.1 9 1.6 1 3 0 3 8 0.436 3 380.

4 0.1 9 1.5 7 4 3 5 7 0.435 6 Travers a Pain t A 1 2 3 4 5 6 8 1 2 3 4 5

Averag e laborator

yResult s Fue l F-factor,dscf/MMBt

u FlterlD Fon t Hal fResidues : Fiterwt. g Aceton e rinse volume

, m l Aceton e wt , g F.H
. Total , g flick Hal fResidues : BH .Total. g Aceton e Blan k Residues : Aceton e blan k volume , m t Aceton e Blan k vwight , g Aceton e weigh t galn. g Aceton e Blan k concentratio n ,0>1 % o fAceton e Blan k Weigh t Weiqh t o fResidu e i n Aceton e Wash , a Correcte d Aceton e Blan k Value , g (f.H , Total+B.H

. Total-Blank) : Ru

n 1

I 0.000 6 J L " J L "

I 0.0019 I 0.002 5 I 0.002

6 I 3 I 1 Z 1

153.899 2 I I 153.899

2 ~ 1 I 0.001 6 I 0.001 9

I 19 6 I 0.0000 0 I I 0.001 5 | I 0.000 1 1 I 0.000

3 1 f j I 0.0000 0 I C a = Ma/VaP a I 0.001 5 I W a = CaVawP

a 0.000 1 I I 0,00003

9 ~ l I 0,000

1 Total , g

VES01805 1Dr yGa s Mete rCalibratio n Dat a Summar y Uni t 2 Veoli a E S Technica l Solution s

Sauget , I L Paramete r Ru n I D Ru n Dat e Mete rBoxI D Duratio n o

fRun , Minutes Mete rGamm a Delt a H@ , inche s o

fH2 0 Barometri c Pressure , inches o fH g Sampl e Volume , dc

f(Vm ) Ave . Mete rTemperature , F (Tm) Dr yMolecula rWeigh t (Md) Ave . Delta H , inches o fH2 0 Ave . SQR TDelta H , inche s o fH2 0 Yq a (calculate d calibratio n factor ) % Difference 12/8/200 9 00 2 6 0 0.99 1 1.801 29. 6 37.91 3 51.3 3 29.7 9 1.35 1.1 5 0.99 5 0. 4 12/9/2009 002 6 0 0.99 1 1.801 29. 3 41.032 34.04 29.7 3 1.61 1.2 6 0.99 3 0.2 12/10/2009 002 6 0 0.99 1 1.801 29. 8 40.40 0 49.9 6 29.6 7 1.5 7 1.2 5 1.00 7 1. 6 Averaq e

0. 7 Yq a = (test duration/Vm ) x(SQRT(0.0319*TmR)/(Delt a H @ x(Pba r+ Ave . Delta H/13.6)) x(SQRT(29/Md) ) xAve.(SQR TDelt a % Difference = (Yq a - Mete rGamma)/Mete rGamm a Three ru n Averag e % Difference mus t b e < = 5 %

VES01805 2

# AECO M Samplin g Trai n Ru n Numbe

r Clien t E P AISOKINETI C SAMPLIN G Barometri cPressur e FIEL D DAT ASHEE T
Veoli a E S Technica l Solution s Facilit yLocatio n Sourc e Dat e Operato r Stac k Dia
. - iii
. Star t Tim e Sto p Tim e Sauget

, I eU L Stati cPressur e (+/- ) "Oi O"/ Probe/Pilo tNumbe rS /HjT" . */-P ~ Pito t Coefficien t LEA KCHECK S i n "Hg INITIA LVA C IS" MID VAC
. — - FINA LVAC
. ts) FilterBo xNo
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. Orific e Coefficien t (Y ) Delt a H @
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w*VOLUM E A TEMPERATUR E READING S ° F 

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VES01805 3E P AISOKINETI C SAMPLIN G - FIEL D DAT ASHEE T Samplin g Trai n Ru n Numbe

r Clien t Barometri cPressur e Stati cPressur e (+/- ) 3 Veoli a E S Technica l Solution s Probe/Pito t Numbe rSf^S~~^

C> Facilit yLocatio n Sourc e 

### D:'.!iOperato r Stac k Dia
. - in
. Star t Tim e Sto p Tim e Sauget,, I L

QH'tt # 3 -

2 f l Pito t Coefficien t FilterBo xNo
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. Orific e Coefficien t (V ) Delt a H @ Nozzl e Size/No
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. / > MID VAC
. •

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. jO CF

M CF M CF M INIT
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LPITO T FILTE R DAT

A 

### MJ-M mmmmm 

## 160

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VES01805 4A3CO M EP A

### ISOKINETI C SAMPLIN G - FIEL D DAT ASHEE T

rIMPINGER VOL 'S
. Orsa t 

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KCHECK S in "Hg INITIA LVAC
. /5 ^ in
. CF M CS.O/S 

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. — in
. CF M — i o o " 

### S. ( 1 3 Facilit yLocatio n Sausct

, I L Pito t Coefficien t FINA LVAC
. /CS in
. CFMtf .«t 7 7 

### f C o 1=1 7 

### Sourc e FilterBo xNo
. m k + y y 

### a s Dat e Mete rBo xNo
. •mm 

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. PITO T* ^ " FINA LPITO T I t

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### b I bO Stac k Dia.-in
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VES01805 5

# AZCOM

, , r_SAMPL E TRAI N MOISTUR E RECOVER YDAT A SHEE T Referenc e Metho d / Samplin g Trai n : 00,5 \ d-bft Recovere d by : ^ MOftfaS Recovere d b y: <J
. •f*V O <t f Recovere d b y: > T |T^ S Ru n No . U3 --(^ l Date : IJ -l^I& l Ru n No . U3l — i ^-Dat e : RunNo .UJ^J ^ J Date : X A D Modul e No. : fsj|A - X A D Modul e No. : N | r V X A D Modul e No. : f" i | fir FilterNo. : Tl8 "9" ^ ©.^3 7 FilterNo.:^! ! 0"If i 7 1 Filtu rNo. : I m pinge rNo . sn d Volum e I m pinge rNo . an d Volum e I m pinge rNo . an d Volum e No . Initia l

(mL ) Fina l

(mL ) Rins e

(mL ) No . Initia l (mL ) Fina l

(mL ) Rins e

(mL ) No . Initia l (mL ) Fina l

(mL ) Rins e

(mL ) 1 1 1 2 tot > 2 l o o 2 3 (" ^ 

### \ 3 3 \ox>. I f / 

### \ J 4 o r 4 0 

# > 4 0 f 11
5 / D O 5 ) o o 5 

# i 6 / O o /ot > 6 ( 0 0 6 t o o 7 7 7 DIFF : DIF F : 7 DIFF : Total s f £ 5 0 Total s HSO H a s 6 7 5 Total s

Initia l (g ) Fina l

(g ) 

# tin Initia l (g ) Fina l

(g ) 

### / \ Initia l (g ) Fina l

(g ) Initia l (g ) Fina l

(g ) DIFF : 

# tin Initia l (g ) Fina l

(g ) DIF F : 

### / \ Initia l (g ) Fina l

(g ) DIFF : Silic a Ge l y . o Silic a G e l Silic a 1 Ge l Silic a Ge l y . o Silic a G e l Silic a 1 Ge l Fina l Ne t Moistur e Gain : Fina l Ne t Moistur e Gain : Fina l Ne t Moistur e Gain : C:\Oocument s an d SettlngMrnlos10estoop\[Molstur

e Recovery.xls]

A

VES01805 6

## Metho d 0023A

VES01805 7PCDD / Veoli a PCD F Emi s Metho d 0 Ru n No . Dat e Star t Tim e E S Technica l S c

sio n Result s - T l 023 A Samplin g I

1 08-Dec-0 9 12:3 0 )lution s

E Q Basi s - Fron i
3 arameter s 2

09-Dec-0 9 12:5 9 Hal f 3 10-Dec-0 9 13:0 0 Sampl e Volum e Sto p Tim e Unit s dsc f 15:3 6

107.85 7 16:5 4

121.80 9 16:06
.

121.52 9 Sampl e Volum e m 3 3.0 5 3.4 5 3.4 4 Moistur e Conten t % v/ v 47. 3 43. 9 46. 1 0 2Concentratio n % v/ v(dry ) 9.1 0 9.3 0 8.2 0 C 0 2Concentratio n % v/ v(dry ) 8.4 3 8.1 4 7.9 0 Isokinetic s % 9 8 9 5 9 7 Stac k Flowrat e dscf m 4,98 7 5,84 0 5,68 2 PCDD/PCD F Parameter s TE F (a ) p g ng/m 3 TE Q p g ng/m 3

TE Q p g ng/m 3

TE Q 2,3,7,8-TCD D 1.0 0 2.8 7 9.4E-0 4 2.2 7 6.6E-0 4 2.3 7 6.9E-0 4 1,2,3,7,8-PeCD D 0.5 0 4.1 3 6.8E-0 4 3.3 4 4.8E-0 4 3.7 0 5.4E-0 4 1,2,3,4,7,8-HxCD D 0.1 0 5.2 2 1.7E-0 4 7.6 8 2.2E-0 4 4.9 8 1.4E-0 4 1,2,3,6,7,8-HxCD D 0.1 0 4.1 1 1.3E-0 4 6.0 4 1.8E-0 4 3.9 2 1. 1 E-0 4 1,2,3,7,8,9-HxCD D 0.1 0 4. 3 1.4E-0 4 6.3 4 1.8E-0 4 4.1 1 1.2E-0 4 1,2,3,4,6,7,8-HpCD D 0.0 1 8.0 3 2.6E-0 5 5.4 1 i.6E-0 5 8.7 0 2.5E-0 5 OCD D 0.00 1 8.8 9 2.9E-0 6 17. 6 5. 1 E-0 6 14. 2 4. 1 E-0 6 2,3,7,8-TCD F 0.1 0 2.5 8 8.4E-0 5 3.8 4 1. 1 E-0 4 3.0 2 8.8E-0 5 1,2,3,7,8-PeCD F 0.0 5 3.9 2 6.4E-0 5 4.3 3 6.3E-0 5 3.5 2 5. 1 E-0 5 2,3,4,7,8-PeCD F 0.5 0 4.1 5 6.8E-0 4 4.5 8 6.6E-0 4 3.7 3 5.4E-0 4 1,2,3,4,7,8-HxCD F 0.1 0 3.9 3 1.3E-0 4 3.1 1 9.0E-0 5 2.6 1 7.6E-0 5 1,2,3,6,7,8-HxCD F 0.1 0 4.6 0 1.5E-0 4 2.4 8 7.2E-0 5 1.5 7 4.6E-0 5 2,3,4,6,7,8-HxCD F 0.1 0 1.6 8 5.5E-0 5 3.1 3 9. 1 E-0 5 1.9 8 5.8E-0 5 1,2,3,7,8,9-HxCD F 0.1 0 1.8 9 6.2E-0 5 1.8 5 5.4E-0 5 2.2 2 6.5E-0 5 1,2,3,4,6,7,8-HpCD F 0.0 1 3.1 1 1.0E-0 5 9.3 5 2.7E-0 5 6.4 9 1.9E-0 5 1,2,3,4,7,8,9-HpCD F 6.6 i 4.1 0 1.3E-0 5 3.5 6 1.0E-0 5 2.2 8 6.6E-0 6 OCD F 0.00 1 6.3 3 2. 1 E-0 6 5.7 5 1.7E-0 6 7.4 4 2.2E-0 6 TOTA LTEQ s (ng/m 3 ) = 3.3E-0 3 i 

### q p 2.9E-0 3

i 

### £P n* * 2.6E-0 3

O O P f\1 1U 1 AJ- i i s (ng/ m (g j 7 y o SJi) — TOTA LTEQ s (g/s ) 7.9E-1 2 8.1E-1 2 6.9E-1 2 (a ) U.S
. EP A(1989 ) Toxi cEquivalenc yFacto r

S:\_JOB\2009Weolia\Tes t DataVUnit 2\(unil2_M0023A.xlsx]TEQS-F H

VES01805 8Veoli a E S Technica l Solution s PCD D /

PCD F Emissio n Result s - TE Q Basi s - Bac k Metho d 0023 A Samplin g Parameter s Hal f
Ru n No . 

### 1 2 3 Dat e 08-Dec-09 09-Deo-09 10-Dec-0 9 Star t Tim e 

### . 12:3 0 12:5 9 13:0 0 Sto p Tim e 1 Init c 

### 15:3 6 16:5 4 16:0 6 Sampl e Volum e dsc f 107.85 7 121.80 9 121.52 9 Sampl e Volum e , m 3 

### 3.0 5 3.4 5 3.4 4 Moistur e Conten t % v/ v 47. 3 43. 9 46 . 1 0 2

### Concentratio n % v/ v(dry ) 

### 9.5 0 9.5 0 9.5 0 C 0 2

### Concentratio n % v/ v(dry ) 

### 9.2 0 9.2 0 9.2 0 Isokinetic s % 

### 9 8 95 9 7 Stac k Flowrat e dscf m 4,98 7 5,84 0 5,68 2 PCDD/PCD F P 9 ng/m 3 

### p g ng/m 3 

### p g ng/m 3 

### Parameter s TE F (a ) TE Q TE Q TE Q 2,3,7,8-TCD D 1.0 0 4.1 4 1.4E-0 3 3.3 4 9.7E-0 4 4.8 0 1 .4E-0 3 1,2,3,7,8-PeCD D 0.5 0 21. 1 3.5E-0 3 18. 6 2.7E-0 3 17. 1 2.5E-0 3 1,2,3,4,7,8-HxCD D 0.1 0 27. 0 8.8E-0 4 21. 9 6.3E-0 4 17. 7 5. 1 E-0 4 1,2,3,6,7,8-HxCD D 0.1 0 49. 0 1.6E-0 3 43. 2 1.3E-0 3 32. 2 9.4E-0 4 1,2,3,7,8,9-HxCD D 0.1 0 31. 0 1.0E-0 3 24. 7 7.2E-0 4 23. 7 6.9E-0 4 1,2,3,4,6,7,8-HpCD D 0.0 1 20 3 6.6E-0 4 19 4 5.6E-0 4 14 9 4.3E-0 4 OCD D 0.00 1 16 7 5.5E-0 5 18 2 5.3E-0 5 11 7 3.4E-0 5 2,3,7,8-TCD F 0.1 0 22. 5 7.4E-0 4 15. 0 4.3E-0 4 14. 1 4. 1 E-0 4 1,2,3,7,8-PeCD F 0.0 5 32. 5 5.3E-0 4 21 8 3.2E-0 4 16. 6 2.4E-0 4 2,3,4,7,8-PeCD F 0.5 0 10 4 1.7E-0 2 56. 3 8.2E-0 3 50. 1 7.3E-0 3 1,2,3,4,7,8-HxCD F L

### 0.1 0 55. 1 1 .8E-0 3 46. 1 1.3E-0 3 25. 9 7.5E-0 4 1,2,3,6,7,8-HxCD F L

### 0.1 0 47. 0 1 .5E-0 3 32. 8 9.5E-0 4 23. 7 6.9E-0 4 2,3,4,6,7,8-HxCD F 0.1 0 96. 0 3.1E-0 3 55. 0 1.6E-0 3 44. 0 1.3E-0 3 1,2,3,7,8,9-HxCD F 0.1 0 24. 8 8.1E-0 4 15. 3 4.4E-0 4 11. 2 3.3E-0 4 1,2,3,4,6,7,8-HpCD F 0.0 1 11 4 3.7E-0 4 13 3 3.9E-0 4 63. 5 1.8E-0 4 1,2,3,4,7,8,9-HpCD F 0.0 1 22. 5 7.4E-0 5 19. 2 5.6E-0 5 11. 6 3.4E-0 5 OCD F r

### 6.6o' i 42. 5 1.4E-0 5 73. 0 2. 1 E-0 5 21. 0 6. 1 E-0 6 TOTA LTEQ s (ng/m 3 

### ) 0.03 5 0.02 1 0.01 8 TOTA LTEQ s (ng/m 3

### @ 7 % 0 2 

### ) 

### 0.04 3 0.02

5 0.02

2 TOTA LTEQ s (g/s ) = 8.3E-1 1 5.7E-1 1 4.7E -1 1 (a ) U.S.EP A(1989) Toxi cEquivalenc yFacto r

S:\_JOB\2009\Veolla\Tes t DataUJni t 2Munit2_M0023A.xlsx]T£QS-F H

VES01805 9Veoli a E S Technica l Solution s - Uni t 2 Fixe d Heart h Kil n # 2 Metho d 0023 A Samplin g Parameter s Ru n No
. 1 08-Dec-09 12:3 0 15:3 6 2

09-Dec-0 9 12:5 9 16:5 4 3

10-Dec-09 13:0 0 16:0 6 AVG S Dat e 1 08-Dec-09 12:3 0 15:3 6 2

09-Dec-0 9 12:5 9 16:5 4 3

10-Dec-09 13:0 0 16:0 6 AVG S StartTim e Unit s 1 08-Dec-09 12:3 0 15:3 6 2

09-Dec-0 9 12:5 9 16:5 4 3

10-Dec-09 13:0 0 16:0 6 AVG S Sto p Tim e 1 08-Dec-09 12:3 0 15:3 6 2

09-Dec-0 9 12:5 9 16:5 4 3

10-Dec-09 13:0 0 16:0 6 AVG S Nozzl e Diamete r inche s •0.43 1 29.4 0 180. 0 109.42 2 0.43 1

29.5 0 180. 0 119.06 7 0.43 1

29.8 0 180. 0 121.77 3 0.43 1 Barometri cPressur e iri
. H g •0.43 1 29.4 0 180. 0 109.42 2 0.43 1

29.5 0 180. 0 119.06 7 0.43 1

29.8 0 180. 0 121.77 3 29.5 7 Ne tSamplin g Tim e min
. •0.43 1 29.4 0 180. 0 109.42 2 0.43 1

29.5 0 180. 0 119.06 7 0.43 1

29.8 0 180. 0 121.77 3 180. 0 Volum e Metere d dc f •0.43 1 29.4 0 180. 0 109.42 2 0.43 1

29.5 0 180. 0 119.06 7 0.43 1

29.8 0 180. 0 121.77 3 116.75 4 Avg
. DG M Temp
. ° F 63. 2 46. 1 64. 1 57. 8 Av g Delt a H i n H 2 0 1.2 0 1.4 6 1.5 1 1.3 9 Av g Delt a H in
. H g \ 0.088 5 0.107 4 0.111 4 0.102 4 DG M Calibratio n Facto r — 0.991 0 0.991 0 0.991 0 0.991 0 Ga s Sampl e Volum e dsc f 107.85 7 121.80 9 121.52 9 117.065 Tota l Wate rCollecte d m L 2051. 9 2021. 5 2205. 3 2092. 9 Volum e o fWate rVapo r sc f 96.74 7 95.31 4 103.98 0 98.68 0 Moistur e ^measured ) % v/ v i 47. 3 43. 9
. 46. 1 45. 8 Moistur e ( @ saturation ) % v/v 101. 8 101. 4 100. 4 101. 2 Dr yMol e Fraction , 100-% M — 0.527 1 0.561 0 0.538 9 0.542 4 C 0 2atStac k %dr y 8.4 3 9.1 0 8.1 4

9.3 0 7.9 0

8.2 0 8.1 6 O zatStac k % dr y 8.4 3 9.1 0 8.1 4

9.3 0 7.9 0

8.2 0 8.8 7 C O + N 2 %dr y 82.4 7 82.56 83.9 0 82.9 8 Dr yMolecula rWeigh t Ib/lb-mol e 29.7 1 29.6 7 29.5 9 i 29.6 6 We tMolecula rWeigh t Ib/lb-mol e 24.1 7 24.5 5 24.2 5 24.3 2 Exces s Ai ratStac k % 71. 8 74. 4 58. 8 68. 3 Stac k Diamete r inche s 39. 0 39. 0 39. 0 39. 0 Stac k Are a sq . in
. 1194. 6 1194. 6 1194. 6 1194. 6 Stati cPressur e i n H a O -0.0 4 -0.0 8 -0.0 6 -0.0 6 Stac k Pressur e in
. H g 29.4 0 29.4 9 29.8 0 29.5 6 Avg
. Stac k

Temp
. ° F 379. 3 373. 2 386. 0 379. 5 Avg
. Sqroo to fDelt a P 

### -- 0.394 5 0.435 4 0.439 8 0.423 3 SD E Averag e — 11.43 0 12.56 9 12.79 3 12.26 4 Pito tCoefficien t — 0.8 4 0.8 4 0.8 4 0.8 4 Stac k Ga s Velocit y afp m 1,84 8 2,01 3 2,05 1 1,97 0 Stac k Flowrat e we tacf m 15,32 8 16,69 8 I 17,01 4 16,34 7 Stac k Flowrat e we tscf m 9,47 4 10,43 1 i6,57 5 10,16 0 Stac k Flowrat e dscf m 4,99 4 

### 5,85 2 5,69 9 

### 5,51 5 Isokinetic s % 

### 9 8 9 5 97 9 7 Mete rBo xNo
. — 2 1.801 0 2

1.801 0 2

1.801 0 — Delt a H @ ....L n -.. H 9...
. 2 1.801 0 2

1.801 0 2

1.801 0 

# - Fiel d Q AYq c — 1.00 0 0.99 4 1.00 3 0.99 9 [Deviation ] Pre- Y % 0.9 % 0.3 % 1.2 % 0.8 % S:\_JOB\2009\Veolia\Tes t DataUJni t 2\[unit2_M0023A_nswdata.xlsx]DAT A

VES01806 0Metho d 0023 A Samplin g Parameter s PT RU N 1 AVG S - PCDDs/PCDF s RU N 2 AVG S - PCDDs / PCDF s RU N 3 AVG S - PCDDs/PCDF s PT D P SQR T

D P DG M

I N DG M

OU T D H STAC K

TEM P D P SQR T D P DG M

I N DG M

OU T D H STAC K

TEM P D P SQRT D P DG M

I N DG M

OU T D H STAC K

TEM P a 1 0.1 9 0.435 9 5

6 5

9 1.6

0 37

8 0.2

3 0.479

6 2

3 2

5 1.7

0 37

4 0.2

2 0.469

0 5

3 5

6 1.8

0 38

8 1 0.1 9 0.435 9 5

6 6

0 1.6

0 38

0 0.2

3 0.479

6 2

7 3

2 1.7

0 37

4 0.2

4 0.489

9 5

3 5

9 2.0

0 38

9 a 2 0.1 8 0.424 3 5

7 6

4 1.5

0 37

9 0.2

3 0.479

6 2

7 3

2 1.7

0 37

5 0.2

3 0.479

6 5 4 6

1 1.9

0 39

0 2 0.1 8 0.424 3 5

7 6

5 1.5

0 38

0 0.2

3 0.479

6 2

7 3

3 1.7

0 37

7 0.2

3 0.479

6 5 5 6

5 1.9

0 39

0 a 3 0.1 8 0.424 3 5

7 6

5 1.5

0 38

3 0.2

1 0.458

3 2

7 3

3 1.6

0 37

9 0.2

0 0.447

2 5

7 6

8 1.6

5 39

0 3 0.1 7 0.412 3 5

8 6

6 1.3

0 38

1 0.21 0.458 3 2

7 3

4 1.6

0 37

8 0.21 0.458 3 5

8 6

8 1.7

0 39

1 a 4 0.1 7 0.412 3 5

8 6

6 1.3

0 38

0 0.2

2 0.469

0 2

7 3

4 1.7

0 37

8 0.21 0.458 3 5

9 6

8 1.7

0 39

0 4 0.1 7 0.412 3 5

8 6

7 1.3

0 38

0 0.2

2 0.469

0 2 8 3

5 1.7

0 37

6 0.2

2 0.469

0 5 9 6

8 1.8

0 38

9 a 5 0.1 3 0.360 6 5

9 6

7 1.0

0 38

0 0.2

0 0.447

2 2 9 4

0 1,5

0 37

5 0.1 9 0.435 9 6

0 6

7 1.4

0 38

8 5 0.1 4 0.374 2 5

9 6

7 1.0

0 38

0 0.2

0 0.447

2 3

6 5

2 1.5

0 37

4 0.1 9 0.435 9 6 0 6

6 1.4

0 38

7 a 6 0.1 0 0.316 2 6

0 6

7 0.7

5 37

7 0.1 0 0.316 2 4

0 6

0 0.7

5 37

0 0.1 0 0.316 2 6 0 6

7 0.7

5 38

5 6 0.1 0 0.316 2 6

0 6

7 0.7

5 37

7 0.1 0 0.316 2 4 5 6

3 0.7

5 37

0 0.1 0 0.316 2 6 2 7

0 0.7

5 38

5 b 1 0.1 7 0.412 3 6

1 6

6 1.3

0 38

0 0.2

3 0.479

6 5

0 6

3 1.7

0 37

1 0.2

1 0.458

3 6 3 7

0 1.6

0 38

5 1 0.1 7 0.412 3 6

1 6

8 1.3

0 38

2 0.2

3 0.479

6 5

1 • 6

3 1.5

0 37

1 0.2

1 0.458

3 6

4 7

2 1.6

0 38

5 b 2 0.1 7 0.412 3 6

1 6

8 1.3

0 38

0 0.1 8 0.424 3 5

2 6

3 1.3

5 37

0 0.2

0 0.447

2 6 5 7

2 1.5

0 38

4 2 0.1 7 0.412 3 6

2 6

9 1.3

0 38

0 0.1 8 0.424 3 5

2 6

3 1.3

5 36

9 0.2

1 0.458

3 6

5 7

2 1.6

0 38

4 1) 3 0.1 6 0.400 0 6

2 6

9 1.2

0 38

1 0.2

0 0.447

2 5

4 6

4 1.5

0 37

0 0.2

2 0.469

0 6 3 6

8 1.6

5 38

5 3 0.1 6 0.400 0 6

2 6

9 1.2

0 38

0 0.1 8 0,424 3 5

5 6

4 1.3

5 37

0 0.2

0 0.447

2 6 2 6

8 1.5

0 38

5 t> 4 0.1 5 0.387 3 6

2 6

8 1.1 0 38 1 0.1 8 0.424 3 5

5 6

2 1.5

0 37

2 0.2

2 0.4690' 6

1 6

8 1.5

0 38

4 4 0.1 5 0.387 3 6

2 6

8 1.1 0 38 1 0.1 8 0.424 3 5

5 61 1.5 0 37

2 0.2

0 0.447

2 6 2 7

1 1.5

0 38

4 b S 0.1 4 0.374 2 6

2 6

8 1.0

0 38

0 0.1 8 0.424 3 5

5 6

0 1.5

0 37

2 0.2

0 0.447

2 6 2 7

1 1.5

0 38

3 5 0.1 4 0.374 2 6

2 6

8 1.0

0 37

9 0.1 8 0.424 3 5

4 5

8 1.5

0 37

3 0.1 8 0.424 3 6

3 7

2 1.3

5 38

3 b e 0.1 4 0.374 2 6

2 6

8 1.0

0 37

7 0.1 5 0.387 3 5

3 5

8 1.2

0 37

3 0.1 5 0.387 3 6

3 7

2 1.1 5 38 0 e 0.1 4 0.374 2 6

2 6

8 1.0

0 36

7 0.1 5 0.387 3 5

3 6

0 1.2

0 37

3 0.1 5 0.387 3 6

4 7

3 1.1 5 38 0 AV G 0.1 6 0.394 5 63. 2 1.20 37 9 0.1 9 0.435 4 46. 1 1.4 6 373 0.2 0 0.439 8 64. 1 1.5 1 38 6

VES01806 1

## A-COM E P AISOKINETI C SAMPLIN G - FIEL D DAT ASHEE T Samplin g Trai n Run Numbe

r Clien t 

## X Barometri cPressur e Stati cPressur e (+/- ) Veoli a E S Technica l Solution s Facilit yLocatio n Sourc e Dat e Operato r Stuc k Dia
. - in
. Star t Tim e Sto p Tim e sauget

, JL . Probe/Pilo t Numbe riS /Wj" ' Pito t Coefficien t G 1$ FilterBo xNoMete rBo xNo
. Orific e Coefficien t (V ) Delt a H @ Nozzl e Size/No
. f t - LEA KCHECK S In ^H g INITIA L VAC . ' ' MI D VAC.
_ FINAL VAC . :K S In ''H g 7W CF

M ^ C YP CF M 

### INI

T

FINA LPITO T FILTE R DAT

A
%5E > XA

D Thermocoupl

e ID : Im p Outle t T C ID : L£
. —<^3 — 

### •••>n.um'bf.rv: :

. — IMPINGF H VOL'S
. FINA L Iff?** 

### 9 <r
5r.;>^lWCA--PELi. , » - ..- • 35X 4 I 3&r-3 MA Orsat 

### C02 , 1. 1

Fina l Purg e Bat e ti j fi, Fina l P H
____ _ SVM I 1 I I'tll N 1 ( 1 (Xk

IIM I \ i n n u t



### hi - \ n DriMP i n w e ORIFir t MIlr K\O I IM1»I 1 inw c 

### •\ S M l I I I I TEMPERATUR E READINGS , ° F | 1 IIM P v\ru i 

### m in.Hf COMMENT S SVM I 1 I I'tll N 1 ( 1 (Xk

IIM I \ i n n u t



### hi - \ n DriMP i n w e ORIFir t MIlr K\O I IM1»I 1 inw c Mi l 1 M l M M h PRjBB ^I i llll.VM i MOBULL- ' » TGA S METER 1 IIM P

v\ru i 

### m in.Hf COMMENT S SVM I 1 I I'tll N 1 ( 1 (Xk

IIM I \ i n n u t



### hi - \ n DriMP i n w e ORIFir t MIlr K\O I IM1»I 1 inw c Mi l 1 M l M M h PRjBB ^I i llll.VM i MOBULL- ' #IN ^ ou r- 1 IIM P v\ru i 

### m in.Hf COMMENT S f ) l<? a s ? 3 ? £/ r A•/? a r t 2vQ St. CO /o }$~%IS '

D.fS c ~l /O 

## ®- US ZD z.rr to f>r*r 3 D 7* 5 I

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o.n A 3 ^6/ f -S"S> - to .Of f a n ZS(o 

## ^! 9 £ K " 6 0 f . 3 u,t r ? s& 1 AS Or\h h° 

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. 5 ft 7 6 OAO 0-7S ~ MX* A r n 2

SI is-) i i4>Q 

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## ^ 7 (a eo. cm '

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VES01806 2E P AISOKINETI C SAMPLIN G - FIEL D DAT ASHEE T

iHSZoX> •uC] ^IMPINCEB VO LS Orsa

t Sampling Trai n l*i<H> Barometri cPressur e At • \ LEA

KCHECK S i n "Ug 'INIT,*', " FINA L RINS

E CC02 - 0 2 Ru n Numbe

r Stati cPressur e INITIA LVAC
. In
. CF

M £ > t( u Clien t Veoli

a E S Technica l Solution s Probe/Pito t Numbe r MID VAC
. in
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, I L Pito t Coefficien t FINA LVAC
. / % in
. CF

M £>. d>

/iQ Sourc e FilterBoi No
. + - •• + Dat e 13.- Mete rBo xNo
. INIT
. PITO T« / FINA

LPITO T Operato r Orific e Coefficien t (Y ) (3. . KH/ FILTE R DAT A Stac k Dia
. - i n 

### ? Delt a I I @ ISHbM'bIrII I Star t Tim e ty /2 L / < 4- Si^ozzl e Size/No

. Sto p Tim e /Jf¥f o 5f °&A D Thermocoupl

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• VP I 1 ICb r*S\ h F R TEMPERATUR E READINGS , ° F | MIM P P I N H A D \O L M l IIKl.\M l \ U IIII M onfMer

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VES01806 3

## ASCOM E P AISOKINETI C SAMPLIN G - FIEL D DAT A SHEE T



# Al

A t 

## M <2tS o WglMPINC fR\<II ' S Orsa t Samplin g Trai n Barometri c Pressur e <2tS o LEA KCHECK S i n "H g INITIA L VAC . If/? i^INIT , . ^ tlNAI . RINS E C02' : 0 2 : Ru n Numbe r 

## 3 Stati c Pressur e (+/- ) - 0 , LEA KCHECK S i n "H g INITIA L VAC . If/? in . CF M z^?^?/ / 

# 0 1.9 Client Veoli a E S Technica l Solufions Probe/Pito t Numbe r ayte-s c MI D VAC . 

# in . CF M O'-'dlT- 1 

## 1.9 Facilit yLocatio n Sauget, I L Pito t Coefficient FINAL VAC . /t / in . CF M 

# r> Sourc e Filte rBo xNo . Aft" ? 

## - /- / / Dat e MeterBo xNo . <?t>P INIT . PITO T* ^ FINA L PITO T 

# u Operato r Wt tHUA V T -

# VatiSOUPi/ Orifice Coefficient (V

) 0. t} < J I FILTE R DAT A 

# u Stac k Dia . - i n Delt a K @ 1 . 

# 8o( w e ,; ""Vv . -*tiStar t Tim e Nozzle Size/No . Stop Tim e XA D Thermocoupl e ID ; ^fiK I —jt > ;SrLICA:CEL: 4-:;r Fina l Pu r geRat e | J A - Im p Outle

t T C ID : lO: ^ 7- 5 

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### VES01806 4

# AECOM

_^ SAMPL E TRAI N MOISTUR E RECOVER YDAT ASHEE T Referenc e Metho d /

Samplin g Trai n : (A, o a d~3 f\ Recovered by : ^^fiYllS Recovered by : ZT- Recovere d by : <£ •kH«

> I ^-K- U RunNo.tU'R tDate : ixjflo i Ru n No
. U3L-rt-2-Dat e : Ru n No.U/J^tf- 3 Date : XAJ D Modul e No. : C<jWs.^rV> 1 UMT XA D Modul e No. : (kV<A^OfO° l l U ( f XA D Modul e No. : Ao ^ / / ^ Filte rNo. : <£f = - Pci~o \IK* 4 Filte rNo. : fdL-'cA««O o Filte rNo. : fipL-cj>*~~~JI m pinge rNo
. an d Volum e I m pinge rNo
. an d Volum e l m pinge rNo
. an d Volum e No
. Initia l

(mL ) Fina l (mL ) Rins e (mL ) No
. Initia l

(mL ) Fina l (mL ) Rins e (mL ) No
. Initia l

(mL ) Fina l (mL ) Rins e (mL ) 1 

### 0 1 

### 0 1 d 2 2 

### pro 2 

### IP* 3 

### 0 °[( 

# / 3 

### 0 \ 3 

### 0 3 • N / 4 4 1 4 5 A f t 

### - 0 6 i As**/ ' < r^ 6 ' 7 7 7 DIFF : DIF F : 7 DIFF : Total s 

### 3.0 \<° Total s Total s Initia l •(g) Fina l

(g ) Initia l (g) Fina l

(g ) i Initia l (g) Fina l

(g ) Initia l •(g) Fina l

(g ) DIF F Initia l (g) Fina l

(g ) DIF F i Initia l (g) Fina l

(g ) DIFF : Silic a Ge l
. 3 ^ 

### m i 35.H Silic a Ge l Silic a Ge l Fina l Ne tMoistur e Gain : •205I
. * ! Fina l Net Moistur e Gain : Fina l NetMoistur e Gain : 

# f t IK r; L*;i/ " /Wc M j

VES01806 5 C:\Document s an d SeKings\milos\Oesktop\[lvloisture Recovery.xls ] A

## Metho d 25 A

VES01806 6

### AVERAGE D CE M DAT A Jo b Nurnber : 6013 Ru n ID : R1B Dat e Tim e TH C 12/8/200 9 12:32:0 0 0.5 8 12/8/200 9 12:34:0 0 0.5 5 12/8/200 9 12:36:0 0 0.5 2 12/8/200 9 12:38:0 0 0.4 5 12/8/200 9 12:40:0 0 0.3 8 12/8/200 9 12:42:0 0 0.4 6 12/8/200 9 12:44:0 0 0.4 1 12/8/200 9 12:46:0 0 0.4 6 12/8/200 9 12:48:0 0 0: 5 12/8/200 9 12:50:0 0 0.4 2 12/8/200 9 12:52:0 0 0.3 9 12/8/200 9 12:54:0 0 0.4 6 12/8/200 9 12:56:0 0 0.4 1 12/8/200 9 12:58:0 0 j 0.4 9 12/8/200 9 13:00:0 0 j 0.5 2 12/8/200 9 13:02:0 0 I 0. 5 12/8/200 9 13:04:0 0 | 0.5 2 12/8/200 9 13:06:0 0 ; 0.4 6 12/8/200 9 13:08:0 0 0.5 2 12/8/200 9 13:10:0 0 0.5 1 12/8/200 9 13:12:0 0 0.5 4 12/8/200 9 13:14:0 0 0.5 4 12/8/200 9 13:16:0 0 0.5 5 12/8/200 9 13:18:0 0 0.5 4 12/8/200 9 13:20:0 0 0. 5 12/8/200 9 13:22:0 0 0.5 4 12/8/200 9 13:24:0 0 0.5 3 12/8/200 9 13:26:0 0 0.5 1 12/8/200 9 13:28:0 0 0.5 2 12/8/200 9 13:30:0 0 0.5 1 Averag e Value : 0.4 9 Correcte d Average : .3 5 Star t Time : 12:30:00 Star t Date : 12/08/09



### VES01806 7

### AVERAGE D CE M DAT A Jo b Number : 6013321 6 Ru n ID : R2B Star t Time : 13:49:00 Star t Date : 12/09/09 Dat e Tim e TH C 12/9/200 9 13:51:0 0 0.2 9 12/9/200 9 13:53:0 0 0.2 7 12/9/200 9 13:55:0 0 0.2 8 12/9/200 9 13:57:0 0 0.2 4 12/9/200 9 13:59:0 0 0.3 1 12/9/200 9 14:01:0 0 0.2 9 12/9/200 9 14:03:0 0 0.2 7 12/9/200 9 14:05:0 0 0.2 7 12/9/200 9 14:07:0 0 0. 2 12/9/200 9 14:09:0 0 0.2 7 12/9/200 9 14:11:0 0 0.3 2 12/9/200 9 14:13:0 0 0.2 9 12/9/200 9 14:15:0 0 0.2 9 12/9/200 9 14:17:0 0 0.2 1 12/9/200 9 14:19:0 0 0.2 3 -12/9/200 9 14:21:0 0 0.2 5 12/9/200 9 ' 14:23:0 0 0.2 2 12/9/200 9 14:25:0 0 0.2 1 12/9/200 9 14:27:0 0 0.2 2 12/9/200 9 14:29:0 0 0.2 1 12/9/200 9 14:31:0 0 0.2 3 12/9/200 9 14:33:0 0 0. 2 12/9/200 9 14:35:0 0 0. 3 12/9/200 9 14:37:0 0 0.3 5 12/9/200 9 14:39:0 0 0.2 3 12/9/200 9 14:41:0 0 0.2 8 12/9/200 9 14:43:0 0 0.3 3 12/9/200 9 14:45:0 0 0.3 4 12/9/200 9 14:47:0 0 0.2 8 12/9/200 9 14:49:0 0 0.2 7 Averag e Value : 0.2 7 Correcte d Average : .1 6 

### VES01806 8

### AVERAGE D CE M DAT A Jo b Number : 60133216 Star t Time : 14:00:00 Ru n ID : R3B

Start Date : 12/10/09 Dat e Tim e TH C .12/10/200 9 14:02:0 0 0.4 6 12/10/200 9 14:04:0 0 0.5 1 12/10/200 9 14:06:0 0 0.4 3 12/10/200 9 14:08:0 0 0.4 3 12/10/200 9 14:10:0 0 0.3 9 12/10/200 9 14:12:0 0 0.4 8 12/10/200 9 14:14:0 0 0.3 8 12/10/200 9 14:16:0 0 0.4 1 12/10/200 9 14:18:0 0 0.3 8 12/10/200 9 14:20:0 0 0.3 9 12/10/200 9 14:22:0 0 0.3 9 12/10/200 9 14:24:0 0 0.4 3 12/10/200 9 14:26:0 0 0.4 2 12/10/200 9 1.4:28:00 0.3 5 12/10/200 9 14:30:0 0 0.4 5 12/10/200 9 14:32:0 0 0. 4 12/10/200 9 14:34:0 0 0.3 7 12/10/200 9 14:36:0 0 0.3 1 12/10/200 9 14:38:00
. 0.3 8 12/10/200 9 14:40:0 0 0.3 5 12/10/200 9 14:42:0 0 0.3 5 12/10/200 9 14:44:0 0 0.3 4 12/10/200 9 14:46:0 0 0.3 7 12/10/200 9 14:48:0 0 0.3 6 12/10/200 9 14:50:0 0 0.3 1 12/10/200 9 14:52:0 0 0.2 9 12/10/200 9 14:54:0 0 0. 3 12/10/200 9 14:56:0 0 0.2 8 12/10/200 9 14:58:0 0 0.2 9 12/10/200 9 15:00:0 0 0.3 5 Averag e Value : 0.3 8 Correcte d Average : .0 9


### VES01806 9

# I i

I

o



### VES01807 0

# AECOM

5



## Appendi xC Referenc e Metho d Calibrations , Verifications , an d Certification s

VES01807 1Calibrator : Mik e O'tool e Referenc e Thermometer: SYR-CAL- 1 Filte rBo xCalibratio n Ho t Box# 5 HotBox#8 D Manufacturer : Seria l No. : Dat e received/place

d i n servi c Anderso n NUTEC H

N/ A Pr e 199 5 Manufacturer :

Seria l No. : Dat e received/place

d i n servi c Anderso n NUTEC H

N/ A Pr e 199 5 Calibratio n Date : 8-Jan-0 9 Calibratio n Date : 8-Jan-0 9 Ambien t Ho

t Ambien t Ho t Referenc e Temperature

s 6

7 25

0 Referenc

e Temperature

s 6

9 25

0 Actual Temperature

s 6

6 24

9 Actual Temperature s 6

9 24

9 Tem p Differenc

e (tol . = +-2

) 1 1 Tem p Differenc e (tol . = +-2

) 0 1 Ho t Box# 6 Ho t Box# 9 Manufacturer : Anderso n NUTEC H Manufacturer : Anderso n NUTEC H Seria l No. : N/ A Seria l No. : N/ A Dat e received/place

d i n servi c Pr

e 199 5 Dat

e received/place

d i n servi a Pr

e 199 5 Calibratio n Date : 8-Jan-0 9 Calibratio n Date : 8-Jan-0 9 Ambien t Ho

t Ambien t Ho t Referenc e Temperature

s 6

9 25

0 Referenc

e Temperature

s 6

8 25

1 Actual Temperature

s 6

9 25

0 Actual Temperature s 6

6 25

0 Tem p Differenc

e (tol . = +-2

) 0 0 Tem p Differenc e (tol . = +-2

) 0 1 Ho t Box# 7 Ho t Box#1 0 Manufacturer : Anderso n NUTEC H Manufacturer : Anderso n NUTEC H Seria l No. : N/ A Seria l No. : N/ A Dat e received/place

d i n servi c Pr

e 199 5 Dat

e received/place

d i n servi o Pr

e 199 5 Calibratio n Date : 8-Jan-0 9 Calibratio n Date : 8-Jan-0 9 Ambien t Ho

t Ambien t Ho t Referenc e Temperature

s 6

8 25

0 Referenc

e Temperature

s 7

1 25

0 Actual Temperature

s 6

9 24

9 Actual Temperature s 7

1 25

0 Tem p Differenc

e (tol . = +-2

) - 1 1 Tem p Differenc e (tol . = +-2

) 0 0 Ho t Box#7

A Ho t Box#1 1 Mianufacturer : Anderso n NUTEC H Manufacturer : Anderso n NUTEC H Seria l No. : Dat e received/place

d i n servi c N/

A Pr e 199 5 Seria l No. :

Dat e received/place

d i n servi c N/

A Pr e 199 5 Calibratio n Date : 8-Jan-0 9 Calibratio n Date : 7-Jan-0 9 Ambien t Ho

t Ambien t Ho t Referenc e Temperature

s 6

9 25

0 Referenc

e Temperature

s 7

0 25

1 Actual Temperature

s 6

9 24

9 Actual Temperature s 6

9 25

0 Tem p Differenc

e (tol . = +-2

) 0 1 Tem p Differenc e (tol . = +-2

) 1 1 Ho t Box# 8 Manufacturer : Seria l No. : Dat e received/place

d i n servi c Anderso n NUTEC H

N/ A Pr e 199 5 Calibratio n Date : 8-Jan-0 9 Ambien t Ho

t Referenc e Temperature

s 6

9 25

0 Actua l Temperature

s 6

9 24

8 Tem p Differenc

e (tol . = +-2

) 0 2 Checke d amp h connector , t-coupl e an d plug s Q C checke

d b yS Mil o 2/9/0 9



### VES01807 2

## AZCOM Calibrator : Date : Steve n Mil o Referenc e Thremomete rID : CL-100 0 12/16/200

8 Las t Impinge rThermocoupl e Calibratio n 200 7 Thermocoupl e Referenc e Difference (+/-2"> Thermocoupl e Referenc e Differenc e (+/-2° ) LI- 1 Ho t 21 0 21 2 - 2 LI-1 8 Ho t 21 0 21 2 - 2 LI- 1 Col d 3

2 3

3 -

1 LI-1 8 Col d 3 2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 T-coupl e 200

6 Dat e received/place

d i n service : Pr

e 199 0 LI- 3 Ho t 21 1 21 3 - 2 LI-2

0 Ho t 21 1 21 2 - 1 LI- 3 Col d 3

2 3

2 0 LI-2 0 Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr

e 199 0 LI- 4 Ho t 21 2 21 3 - 1 LI-2

2 Ho t 21 3 21 2 1 LI- 4 Col d 3

2 3

2 0 LI-2 2 Col d 3

2 3

2 0 Manufacturer: Anderson NUTEC H Manufacturer: Serial No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 T-coupl e 200

6 Dat e received/place

d i n service : Pr

e 199 0 LI- 8 Ho t 21 2 21 3 - 1 LI-22

A Ho t 21 0 21 2 - 2 LI- 8 Col d 3

2 3

2 0 LI-22 A Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr

e 199 0 Ho t 0 LI-2 4 Ho t 21 0 21 2 -2 Col d 0 LI-2 4 Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr

e 199 0 Ho t 0 LI-2 S Ho t 21 2 21 2 O Col d 0 LI-2 S Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No, : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr

e 199 0 LI-1 3 Ho

t 21 0 21 2 - 2 LI-2

8 Ho t 21 3 21 2 1 LI-1 3 Col d 3 3 3

2 1 LI-2 8 Col d 3

2 3

2 0 Manufacturer: Manufacturer: Anderso n NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d in service : Pr

e 199 0 LI-1 5 Ho

t 21 0 21 2 - 2 LI-1 5 Col d 3 2 3

2 0 ManufacturerAnderson NUTEC H Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Aftercalibration showe

rheads wer

e cleane d and leak

checke d Q C check

S . Milo



### VES01807 3Calibrator : Date : Bil l Hardy

1/18/201 0 Referenc e Thremomete rID : CL-1000
Last ImpinqerThermocoupl e Calibratio n 200 7 Thermocoupl e Referenc e Differenc

e (+/-2° ) Thermocoupl e Referenc e Differenc e (+/

- 2° ) LI- 1 Ho t 21 0 21 2 - 2 LI-2

0 Ho t 21 1 21 2 - 1 LI- 1 Col d 3

2 3

2 0 LI-2 0 Col d 3

2 3

2 0 Manufacturer: Anderson NUTEC H Manufacturer: Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 T-couple 200

6 Dat e received/place

d i n service : Pr e 199 0 Li-3 Ho

t 21 2 21 2 0 LI-2 2 Ho t 21 1 21 2 - 1 Li-3 Col d 3

2 3

2 0 LI-2 2 Cold 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr e 199 0 LI- 4 Ho t 21 0 21 2 - 2 LI-22

A Ho t 21 1 21 2 - 1 LI- 4 Col d 3

2 3

2 0 LI-22 A Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H ManufacturerAnderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 T-couple 200

6 Dat e received/place

d i n service : Pr e 199 0 LI-1 3 Ho

t 21 2 21 2 0 LI-2 4 Ho

t 21 1 21 2 - 1 LI-1 3 Col d 3 3 3

2 1 LI-2 4 Col d 3

3 3

2 1 Manufacturer : Manufacturer : Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e receivedfolace

d i n service : Pr e 199 0 LM 5 Ho

t 21 1 21 2 - 1 LI-2

5 Ho

t 21 0 21 2 - 2 LM 5 Col d 3 3 3

2 1 LI-2 5 Col d 3

3 3

2 1 Manufacturer : Anderson NUTEC H Manufacturer : Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr e 199 0 LI-1 8 Ho

t 21 0 21 2 - 2 LI-2

8 Ho t 21 1 21 2 - 1 LI-1 8 Col d 3 3 3

2 1 LI-2 8 Col d 3

2 3

2 0 Manufacturer : Anderson NUTEC H Manufacturer : Anderson NUTEC H Seria l No. : Seria l No. : Dat e received/place

d i n service : Pr

e 199 0 Dat e received/place

d i n service : Pr e 199 0 Afte rcalibration showe

rheads wer

e cleane d an d leak checke d Q C chec k

S . Mil o



### VES01807 4M 5 Thermocoupl e Calibration s - 200 9 Date : 12/16/0 8 Calibrator : Steve n Mil o BP : 30.0 8 Ambien t Tem p (F) : 6 5 Referenc e Thermomete rID# : CL-100 0 Fluk e Digita l RT D 213103 5 Manufacture : Fluk e Dat e place d i n Service : Pr e 198 0
Ic e Bat h Boilin g Wate r Thermocoupl e ID # Referenc e

Tem p ' XA D

Tem p Tem p

Differenc e To l = +-2 F Referenc e

Tem p X A D

Tem p Tem p

Differenc e To l = + - 2 F M5-TC 1 21 2 21 2 0 3 2 3 3 1 M5-TC 2 21 2 21 1 - 1 3 2 3 3 1 XAD- 6 3 2 3 2 0 21 3 21 2 - 1 XAD- 7 3 2 3 2 0 21 3 21 2 - 1 Q C chec k

S
. Mil o



### VES01807 5

# AsCOM

M 5 Thermocoupl e Calibration s - 201 0 Date : 1/17/201 0 BP : 30.0 8 Referenc e Thermomete rID# : Manufacture : Dat e place d i n Service : Calibrator : Bil l Hard y Ambien t Tem p (F) : 6 5 CL-100 0 Fluk e Digita l RT D 213103 5

Fluk e Pr e 198 0
Ic e Bat h Boilin g Wate r Thermocoupl e ID # Referenc e

Tem p X A D

Tem p Tem p

Differenc e To l = + - 2 F Referenc e

Tem p X A D

Tem p Tem p

Differenc e To l = + - 2 F M5-TC 1 3 2 3 3 1 21 2 21 2 0 M5-TC 2 3 2 3 3 1 21 2 21 1 - 1 XAD- 6 3 2 3 2 0 21 3 21 2 - 1 XAD- 7 3 2 3 2 0 21 2 21 2 0 Q C chec k

S
. Mil o



### VES01807 6

# AZCOM DR YGA S METE R CALIBRATIO N Mete rBo

xNo. : 2 Chac k one : Annua ) Calibratio n Recalibratio n bate : 7/10/200 9 Operator : S . Mil o Barometri c Pressure : 29.8 1 (i n Hq ) Theoretica l Critica l Vacuum : 14.0 6 (i n Hg ) Manufacturer

. Environmental Suppl y Dat e Received/Place

d i n service : 200 2 Seria l No. : 2 Pretes t Lea k Check s Allowabl e Actual Positiv e 0 0.0 0 (a t 5-7in . H;0

) in . H 2 0 permin . Negativ e 0 0,00 0 - (a t 3 In . H9

) cf

m _ ^ cf

m

DR YGA S METE R DAT A •CRITICA L ORIFIC E DAT A

Volume Tem p critica l KOrific e Actual Ambien t Temperatur

e 4 H Tim

e Initia

l Fina l Total Initia l Rna l Orific e Calibratio

t Vacuu m Initia l Final Averag e (i n HjO) (min

) (ft !) (ft 5 ) (ft J ) ° F ° F Seria l f Coefficie n (I n Ha ) ° F ° F ° F 0.2 9 2 0 0.05 0 6.37 8 6.32 6 7 1 7 3 4 0 0.24 0 24 7 0 71 7 1 0.6 4 1 5 6.40 2 13.32 5 6.92 3 7 2 7 6 4 8 0.35 0 22. 5 7 2 7 2 7 2 1.1 5 1 5 13.39 6 22.53 3 9.13 7 7 5 77 5 5 0.46 0 21 7 3 72 7 3 1.9 0 1 0 22.57 7 30.45 1 7.87 4 7 7 7 9 6 3 0.59 4 1 9 7 3 72 7 3 3.7 0 1 0 30.50 7 41.27 1 10.76 4 7 8 8 2 7 3 0.80 9 1 6 7 3 74 7 4 CORRECTE D VOLUM E OryGa s Critica

l DR

YGA S METE R DR

YGA S METE R Mete r Orific

e 'CALIBRATIO N CALIBRATIO N V m (st d ft 3 ) Ve r(st d ft 1 ) FACTO

R Y FACTO R Um 6,25 9 6.21 2 0.99 3 0.00 1 1.69

1 -0.11 1 6.83 1 6.77

9 0.99

2 0.0 0 1.76

2 -0.03 9 8.98 9 8.91 9 0.99 2 0.0 0 1.83

0 0.O2 8 7.73 2 7.66

8 0,99

2 0.0 0 1.81 8 0.0 2 10.58 2 10.44

6 0.98

7 0.0 0 1.90

7 0.1 1 Avg . Y 0.99

1 Avg . AH @ 1.80 1
1 ) Fo rvali d test results, th e Actual Vacuu m should b e 1 t o 2 In. H g greatertha

n th e Theoretical Critica l Vacuu m show n above. 2 ) The Critica l Orific

e Coefficient, K

\ mus t b e entere d i n Englis h units, (ft)*3*(de g R)*0.5/{(ir>.Hg)*(min)) . 3 ) Th e minimu m numbe

ro fsampl e volume require

d pe rorific

e i s 5 cubi c fee

t 4 ) Fo rCalibration FactorY , th e rati o o fth e reading o

fth e calibration metert

o th e dr yga s meter , acceptabl

e toleranc

e o findividua

l value s fro m th e averag e is ±0.0 2 5 ) Fo rOrific

e Calibration FactorAH@ , the orific e differential pressur

e i n inche

s o fH 2 0 tha t equate s t o 0.7 5 cf m o fai ra t 6 8 F an d 28.9 2 inche s o fHg , acceptable toleranc

e o fIndividua

l value s fro m th e average i s ±0.2.

Dr yGa s MeterThermocoupl e Calibratio n Ref.TCIO * RE F -SY R -TC 2 MetfO* : 002-I N Outle t lot * 002-OU T Ref. Sourc

e Ref.' F 

### °f 4 

### °e A Amb . Ai r 6 5 6 6 - 1 6 6 1 Ho t Wate r 11 8 11 8 0 11 7 - 1 Potentiomete r Calibratio n Lo w 100' F 9 9 Mi d 40

0 " F 40 0 Hig h 90

0 °F 89 9

1 ) Ho t Watert o b e i n th e rang e o f10 4 -12 2 °F . 2 ) Toleranc

e allowe d foral l thermocoupl

e individual readings : ±5, 4 ° F 3 ) Toleranc

e allowe d fo ral l potentiomete

rindividual readings : ±2 ° F

= 1 7.«<?,)

—liA _ v cr(al)
' m(Hd) .75 0 cr[s!d)AECOM SAMPL E PROB E CALIBRATIO N DAT A FOR M TYP E "S " PITO TTUB E ASSEMBL YAN D NOZZL E

Thermocoupl e Calibratio n j PROB E ID : 

## j ENS R RT O #2131035 Omeg a CI10OO . #06022200 Omeg a C M COO . W06O222O

O
S-M54 D •1 Furrae o poo -- S-M54 D »-—» » T C r TM ' 7 r c Z r c ? Date : 1/28(230 9 1 34 27 4 3 4 27 4 0 21 2 373 21 2 37 3 0.0 45 1 506 45 0 50 5 - 0 1 j S-M5-4 0 3 4 27 4 3 4 27 4 0 21 2 37 3 21 2 37 3 0 0 45 1 506 45 0 50 6 •0 1 i"*;;*V;r " st ° 3 4 27 4 3 4 27 4 0 21 2 373 21 2 37 3 0.0 45 1 50 6 45 0 50 5 - 0 1 i"*;;*V;r " st ° 3 4 27 4 3 4 27 4 0 21 2 373 21 2 37 3 0.0 45 1 50 6 45 0 50 5 . 0 1 Typ e "S " Pito t Tub e Calibration : Leve l an d Perpendicula r Obstructio n Damage d
a , (-10 ° S a , s + 10" )
a 2(-10 ° s a 2 ^ + 10° ) fi , (-5 °s a , < +5" ) fi 2(-5° < IJ 2 < *5' ) Y e

z= ATany(± £0.125" ) W= ATana(± s 0.03125" ) D , (3/1 6 S D, s 3/8") A A72D , (1.0

5 s P A /D, s 1.5

)

Pito t Tub e t o Nozzl e Calibration : jgg-i^°t>--«. "

} Pilo t t o nozzl e separatio

n j2 ) Therniocatpla l

o ptlo l separatio n i3 ) Pilo t en d t o prob e unio n distanc e Prob e Informatio n Manufacture r Date Receive d an d place d I n Service : Conditio n ofProb e whe n placed i n se n QA/Q C Chec k Completenes s _X

_Legi b rtjf ytha t th e Typ e Spito

t tube/prob e ID#_

_ criteri a and/o rapplicabl e desig n features an d
iCertifie d by ; Stevenlylil o 1/26/09 Ape x pre-198 5 NE WUSE D RECONDITIONE D (circl e one)
Reasonablenes s meets o rexceed s al l Specification s

. hereb yassigne d a pi to ! tube calibratio n facto rC Do f0.84
Steve n Mil o 2/18/0 9 Personne l (Sig n a tore/Dale) Tea m Leade r(Signature/Date) |AI I constructio n criteri a (o ra n isolate d *S * typ

e pilot ar e withi n give n tolerance s prescribe d i n SQualit yAssuranc e Handboo k fo rAi rPollutio n Measutemen t Systems : Volum e III . Stationar ySource-Specifi c Methods . EPA/6O07R-94/038c , Septembe r199 4



### VES01807 8

### AUCOM SAMPL E PROB E CALIBRATION DAT AFOR M TYP E "S " PITO

TTUB E ASSEMBL

YAN D NOZZL E Thermocoupl e Calibratio n PROB E iO : ThofrvotncleM D i » ENS R RT O #2131035 Omeg a C l 1000 . #0602220 0 Omeg a C110O0 . #0603220 0 S-M5-5 C fed Bait , Boilin g Walc r Tub e F.mac o pee r•W

r , S-M5-5 C T C tr T C T " 'M «r n Date : U2&72U0 9 3 4 27

4 3

4 27

4 0 21 2 373 21 1 37 3 -0. 1 450 50 5 44 7 50

4 -

0 3 S-M5-5 C 3

4 27

4 3

4 27

4 0 21 2 373 21 1 37 3 -

0 1 450 50 5 44 7 60

4 0 3 3 4 27

4 3

4 274 0 21 2 373 21 1 37 3 -0. 1 450 50 5 44 7 50

4



### -- - 3

4 27

4 3

4 27

4 0 21 2 373 21 1 373 -0. 1 1 450 50 5 44 7 50

4 -

0 3 Typ e "S " Pito t Tub e Calibration : Leve l an d Perpendicula r Obstructio n Damage d a, (-10° < ct,< * 10" ) (i 2 (-10 ° < et 2 £+ 10° ) (! , (-5 " < R, 5 * 5° ) B 2(-5 ° <Ej5t5' )

z = ATany(± £0.125" ) W= ATan0(i S 0.03125" ) D , (3/1 6 < D, s 3/8") A A/2D , (1.0

5 s P A /D, s 1.5

) aetemlnlngT/the n calculat e z . Pito t Tub e t o Nozzl e Calibration :

ID , Ty wS mt* Tup . ^ | j ^ > 

# HSU — * i n Ml

1 ) P to t l o nozzl e separalto

n 2 ) Thermacouol

e l o p.to l b e pal a Hu n 3 ) Pito t en d t o prab s unio n distanc e >3ifl"(w'E0 0 nozzte i

Prob e Informatio n
Manufacturer : Dat e Receive d an d placed I n Service : Conditio n o

fProb e whe

n place d i n ser

v QA/Q C Chec k Completeness X_

_Legib i I certif ytha t the Type S pilot tube'pro& e ID#
_ pre-1.995 . NE WUSE D RECONDITIONE D (circl e one ) Specification s Reasonablenes s
rileri a and/o rapplicabl e desig n features an d i s hereb yassigne d a pilo

t tub e calibratio n facto rC, o f0.8 4 ;eed s al l Specifications ,

Certifie d by : Steve n Mil o 1/29/0 9 Personne l (Signature/Date) Sieve n Mil o 2/15/0 9 Tea m Leade r(Signature/Date) Al l constructio n criteri a fo ra n isolate d "S " typ e pito t ar e withi n give n tolerance s prescribe d i n QualityAssuranc e Handboo k fo rAi rPollutio n Measuremen t Systems : Volum e ill , Stationar ySource-Specifi c Methods . EPA/60O/R-94,O38c , Septembe r199 4



### VES01807 9DAIL YCALIBRATIO N REPOR T Date : 12/8/2009 Start Time : 07:58:49 En d Time : 08:10:09 Methods : 3A , 6C , 7 E an d 1 0 Jo b Number : 6013321 6 Spa n Para m Valu e C0 2 1 1 TH C 1 0 Calibratio n Erro r= Syste m Bia s = Mid-Ga s Standard 5.0 2 5.1 0 Analyze r

Zer o Respons e 0.0 2 N/ A Analyze r

Mi d Respons e 5.01 N/ A Zer o

Ca l Erro r 0.3 % 1.0 % Mi d

Ca l Erro r -0.1 % 0.2 % Syste m

Zer o Respons e 0.0 6 0. 1 Syste m

Mi d Respons e 5.0 6 5.1 1 100 % x(Analyze rRespons e - Cylinde rGa s Standard Value) / (Spa n Value) 100 % x(Syste m Respons e - Analyze rResponse) / (Spa n Value) Fo rTH C Measurements : Calibratio n Erro r= 100 % x(Syste m Respons e - Cylinde rGa s Standard Value ) / (Cylinde rGa s Standard Value ) Syste m Bia s = 100 % x(Syste m Respons e - Cylinde rGa s Standard Value ) / (Spa n Value

) Syste m Zer o Bia s 0.3 % 1.0 % Syste m Mi d Bia s 0.4 % 0.1 %

VES01808 0CALIBRATIO N CHEC K REPOR TStart Time : 11:16:23 Ru n ID : R1B

Date : 12/8/2009 En d Time : 15:48:57 EP AMethods : 3A , 6G , 7 E an d 1 0 Jo b Number : 6013321 6 Analyze rAnalyze rSyste m Syste m Syste m Syste m Syste m Syste m Syste m Syste m Zer o Mi d Pre-Zero Pre-Mi d Pre-Zero Pre-Mi d Post-Zero Post-Mi d Post-Zero Post-Mi d Para m Respons e Respons e Respons e Respons e Bia s Bia s Respons e Respons e Bia s Bia s Zer o Drif t Mi d Drif

t C0 2 0.0

2 5.0

1 0.1 5 5.1 1 1.1 % 0.8 % 0.1 2 4.98 0.8 % -0.3% -0.3 % -1.1 % TH C N/

A N/

A 0.1 3 5.31 1.3 % 2.1 % 0.1 6 5.2 5 1.6

% 1.5

% 0.3

% -0.6

% Syste m Blas = 100

% x(Syste m Respons e - Analyze rResponse) / (Spa n Value) Syste m Drift 9100

% x(Syste m Pos t Respons e - Syste m Pr e Response) /

(Spa n Value

) Fo rTH C Measurements : Syste m Bias = 100

% x(Syste m Respons e - Cylinde rGa s Standard Value) I (Spa n Value

) Syste m Avg-Zer o Respons e 0.1 4 0.1 4 Syste m

Avg-Mi d Respons e 5.0 5 5.2 8

VES01808 1

### DAIL YCALIBRATIO N REPOR T Date : 12/9/2009 Start Time : 08:12:31 En d Time : 08:25:26 Methods : 3A , 6C , 7 E an d 1 0 Jo b Number : 6013321 6 Spa n Para m Valu e C0 2 1 1 TH C 1 0 Calibratio n Erro r= Syste m Bia s = Mid-Ga s Standard 5.0 2 5.1 0 Analyze r

Zero Respons e 0.0 8 N/ A Analyze r

Mi d Respons e 5 N/ A Zer o

Ca l Erro r 0.8 % 1.5 % Mi d

Ca l Erro r -0.2% 1.9 % Syste m

Zer o Respons e 0.1 4 0.1 5 100 % x(Analyze rRespons e - Cylinde rGa s Standard Value) / (Spa n Value) 100 % x(Syste m Respons e - Analyze rResponse) / (Spa n Value) Fo rTH C Measurements : Calibratio n Erro r= 100 % x(Syste m Respons e - Cylinde rGas Standard Value) / (Cylinde rGa s Standard Value) Syste m Bia s = 100 % x(Syste m Respons e - Cylinde rGa s Standard Value

) / (Spa n Value

) Syste m Mi d Respons e 5.0 5 5.1 9 Syste m

Zer o Bia s 0.5 % 1.5 % Syste m Mi d Bia s 0.5 % 0.9 %



### VES01808 2

### CALIBRATIO N CHEC KREPOR T Ru n ID : R2B

Date : 12/9/2009 Start Time : 10:57:03 En d Time : 17:11:27 EP AMethods : 3A , 6C , 7 E an d 1 0 Jo b Number : 6013321 6 Analyze r Analyze r Syste m Syste m Syste m Syste m Syste m Syste m Syste m Syste m Syste m Zer o Mi d Pre-Zero Pre-Mi d Pre-Zero Pre-Mi d Post-Zero Post-Mi d Post-Zer o Post-Mi d Avg-Zer o Para m Respons e Respons e Respons e Respons e Bia s Bia s Respons e Respons e Bia s Bia s Zer o Drif t Mi d Drif

t Respons e C0 2 0.0

8 5 0.0 9 4.9

8 0.0

% -0.2% 0. 1 5.0 9 0.2

% 0.9

% 0.1 % 1.1 % 0.0 9 TH C N/

A N/

A 0.0

6 5- 1 0.6 % 0.0

% 0.1 6 5.0 8 1.6

% -0.2% 0.9 % -0.2% 0.1 1 Syste m Bias = 100

% x(Syste m Respons e - Analyze rResponse) / (Spa n Value

) Syste m Drifts 100

% x(Syste m Pos t Respons e - Syste m Pr e Response) /

(Spa n Value) For.TH C Measurements : Syste m Bias - 100

% x(Syste m Respons e - Cylinde rGa s Standard Value ) / (Spa n Value

) Syste m Avg-Mi d Respons e 5.0 4 5.0 9



### VES01808 3DAIL YCALIBRATIO N REPOR T Date : 12/10/2009 Start Time : 09:32:24 En d Time : 09:40:21 Methods : 3A , 6C , 7 E an d 1 0 Jo b Number : 6013321 6 Spa n Para m Valu e C0 2 1 1 TH C 1 0 Calibratio n Erro r= Syste m Bia s = Mid-Ga s Standard 5.0 2 5.1 0 Analyze r

Zero Respons e 0.0 6 N/ A Analyze r

Mi d Respons e 5.0 6 N/ A Zero

Ca l Erro r 0.6 % 2.7 % Mi d

Ca l Erro r 0.4 % 0.4 % Syste m

Zer o Respons e 0.1 1 0.2 7 100 % x(Analyze rRespons e - Cylinde rGa s Standard Value) / (Spa n Value

) 100 % x(Syste m Respons e - Analyze rResponse) / (Spa n Value) Fo rTH C Measurements : Calibratio n Erro r= 100 % x(Syste m Respons e - Cylinde rGas Standard Value ) / (Cylinde rGa s Standard Value) Syste m Bia s = 100 % x(Syste m Respons e - Cylinde rGa s Standard Value ) / (Spa n Value

) Syste m Mi d Respons e 5.1 2 5.1 2 Syste m

Zer o Bia s 0.5 % 2.7 % Syste m Mi d Bia s 0.5 % 0.2 %

VES01808 4

### CALIBRATIO N CHEC KREPOR Tstar t Time : 12:12:30 EP AMethods : 3A , 6C , 7 E an d 1 0 Ru n ID : R3B

Date : 12/10/2009 En d Time : 16:26:00 Jo b Number : 6013321 6 Analyze r Analyze r Syste m Syste m Syste m Syste m Syste m Zer o Mi d Pre-Zero Pre-Mi d Pre-Zero Pre-Mi d Post-Zer o Para m Respons e Respons e Respons e Respons e Bia s Bia s Respons e C0 2 0.0

6 5.0

6 0.1 7 5.3 9 1.0

% 2.9

% 0.0

4 TH C N/

A N/

A 0.3

9 5.0

4 3.9

% -0.6% 0.1 9 Syste m Bias = 100

% x(Syste m Respons e - Analyze rResponse) / (Spa n Value) Syste m Drift= 100

% x(Syste m Pos t Respons e - Syste m Pr e Response) /

(Spa n Value

) Fo rTH C Measurements : Syste m Bias - 100

% x(Syste m Respons e - Cylinde rGa s Standard Value) / (Spa n Value

) Syste m Syste m Syste m Syste m Syste m

Post-Mi d Post-Zero Post-Mi d Avg^Zer o Avg-Mi d Respons e Bia s Bias Zero Drif t Mi d Drif

t Respons e Respons e 5.1 1 -0.2% 0.4 % -1.2% -2.5% 0.1 1 5.2 5 5.2 9 1.9

% 1.9

% -2.0

% 2.5

% 0.2

9 5.1 6



### VES01808 5

# Initia l TH C Monito rCalibration s
Plan tI.D
. Comments : Sourc e I.E X Pollutan t _ Dat e Projec tNo
. 

## kotv^l k Operato rJ .dorrta^ Analyze rI.D
. V

J j& - M Spa n Valu e i o Analyze rSeria l No
.
Initia l Calibratio n (Tim e )

Cylinde rValu e (ppm ) Syste m

Respons e (ppm ) Predicte d

Valu e (ppm ) Syste m

Respons e (ppm ) Calibratio n

Erro r ( % o fSpan )
Zer o Ga s 

# O.O 

# O f |Iil|il|lll f

Lo wLeve l Ga s i 

# 2 5 7 2-f t
- o.tf Mi d Leve l Ga s 

# liiiSiiillPisiS P

- / Hig h Leve l Ga s

Cylinde rI D
. Zer o Ga s Lo wLeve l Ga s Mi d Leve l Ga s Hig h Leve l Ga s

Calibratio n Erro r(Syste m Respons e - Predicte d Value ) X10 0 Calibratio n Ga s Predicte d Valu e [ (Hig h Respons e - Zer o Respo n XMi d o rLo wLeve l Ga s ] + Zer o Respons e Hig h Leve l Ga s



### VES01808 6AZCO M 

# Initia l Monito rCalibration s
Plan t 

# I.D
. Ufol. d Comments : Sourc e I.D
. U N > , f2 Pollutan t Dat e Projec tNo
. lg D\352 I b Operato rj
. Lar^c^ Co i Analyze rI.D. ^ i) 0 u£j ci^^jo Spa n Valu e ( ( Analyze rSeria l No
.
Initia l Calibratio n (Tim e )

Cylinde rValu e (pp m o r% ) Analyze r

Respons e (pp m o r% ) Calibratio n Erro r ( % o fSpan ) Syste m

Respons e (pp m o r% ) Syste m Bia s (% o fSpan )
Zer o Ga s 0 . 0 

### 0 -OT- 

# D-oio 0 - 3 Lo wLeve l Ga s — . — . — 

# . Mi d Leve l Ga s 

# -0
. 1 * Hig h Leve l Ga s ICM G \io i 

# 0-4 S
— - —

Cylinde rI.D
. Zer o Ga s Lo wLeve l Ga s — Mi d Leve l Ga s 

## Sir

mu5i 3 Hig h Leve l Ga s

Calibratio n Erro r(Analyze rRespons e - Cylinde rValue ) X10 0 Spa n Valu e Syste m Bia s = (Syste m Respons e - Analyze rResponse ) X10 0 Spa n Valu e



### VES01808 7

# Initia l TH C Monito rCalibration s
Plan tI.D
. 

### VJf t • CL Cornments : Sourc e I.D ^ Pollutan t _ Dat e Projec tNo
. &oitfzilo 

### Operato r&
. 6

>arMQ^ i 

## H C Analyze rI.D
. 

## UlV ? M-ZO Spa n Valu e j p Analyze rSeria l No
.
Initia l Calibratio n (Tim e )

Cylinde rValu e (ppm ) Syste m

Respons e (ppm ) Predicte d

Valu e (ppm ) Syste m

Respons e (ppm ) Calibratio n

Erro r ( % o fSpan )
Zer o Ga s 

# O-o 0 \ S Lo wLeve l Ga s a •> « Mi d Leve l Ga s 5-1 5 

# r . i t Hig h Leve l Ga s 

# M 3

Cylinde rI.D
. Zer o Ga s Uli P -^ 1 Lo wLeve l Ga s C C 2 \1 47 0 Mi d Leve l Ga s Hig h Leve l Ga s 

# $6

Mrt f

Calibratio n Erro r(Syste m Respons e - Predicte d Value ) X 10 0 Calibratio n Ga s Predicte d Valu e [ (Hig h Respons e - Zer o Respo n X Mi d o rLo wLeve l Ga s ] + Zer o Respons e Hig h Leve l Ga s



### VES01808 8AECO M



# Initia l Monito rCalibration s
Plan tI.D
. 'J60i< a Comments : Sourc e I.L T Pollutan t _ Dat e Projec tNo
. foQlhlx \G Operato rj -tor^o ^ Co 1 Analyze rI.D
. Vr^^ * <vy o Spa n Valu e \ \ Analyze rSeria l No
.
Initia l Calibratio n (Tim e )

Cylinde rValu e (pp m o r% ) Analyze r

Respons e (pp m o r% ) Calibratio n Erro r ( % o fSpan ) Syste m

Respons e (pp m o r% ) Syste m Bia s ( % o fSpan )
Zer o Ga s 0 -o% 

## o x
Lo wLeve l Ga s

- — — — Mi d Leve l Ga s 

## S -OCS t 

## C M Hig h Leve l Ga s 

## 1 0 

# 0 -1 ? — - —

Cylinde rI.D
. Zer o Ga s L » H ?- - 0 3
_ Lo wLeve l Ga s — Mi d Leve l Ga s Hig h Leve l Ga s

Calibratio n Erro r(Analyze rRespons e - Cylinde rValue ) X10 0 Spa n Valu e Syste m Bia s = (Syste m Respons e - Analyze rResponse ) X10 0 Spa n Valu e



### VES01808 9AECO M 

# Initia l Monito rCalibration s
Plan tI.D
. a. Comments
. Sourc e I.D ^ Pollutan t _ Dat e Projec tNo
. Lol¥>2/L Operato r~J. Lcrrtct^J Co 

### il- \ Q-o

L Analyze rI.D
. 

# Scryon ?y: n/t /p Spa n Valu e jo Analyze rSeria l No
.
Initia l Calibratio n (Tim e )

Cylinde rValu e (pp m o r% ) Analyze r

Respons e (pp m o r% ) Calibratio n Erro r (% o fSpan ) Syste m

Respons e (pp m o r% ) Syste m Bia s ( % o fSpan )
Zer o Ga s o n O S Lo wLeve l Ga s — —
Mi d Leve l Ga s 

### S ".| 2 Hig h Leve l Ga s 

## )0M 0 - 5 — —

Cylinde rI.D
. Zer o Ga s Lo wLeve l Ga s Mi d Leve l Ga s Hig h Leve l Ga s c cHosgx

Calibratio n Erro r(Analyze rRespons e - Cylinde rValue ) X10 0 Spa n Valu e Syste m Bia s = (Syste m Respons e - Analyze rResponse ) X10 0 Spa n Valu e



### VES01809 0

# AECOM Initia l TH C Monito rCalibration s Plan tI.D
. o i > a. Comments : Sourc e I.D

_U \~'X Pollutan t Dat e 

### M C Projec tNo
. hbil'b'xiL* Operato r~Z

•WacMo-.-^ Analyze rI.D
. (1 ( 6 - aA-IO Spa n Valu e )Q Analyze rSeria l No.
_
Initia l Calibratio n (Tim e )

Cylinde rValu e (ppm ) Syste m

Respons e (ppm ) Predicte d

Valu e (PPm ) Syste m

Respons e (ppm ) Calibratio n

Erro r ( % o fSpan ) Zer o Ga s 

# 0

• 0 Lo wLeve l Ga s 

### - 4.24 = Mi d Leve l Ga s 

### 5,13 3 Hig h Leve l Ga s

Cylinde rI.D
. Zer o Ga s U HP-^riLowLeve l Ga s 

## CC

DH mo Mi d Leve l Ga s Cf r<ii O 1155 5 Hig h Leve l Ga s

Calibratio n Erro r(Syste m Respons e - Predicte d Value ) X10 0 Calibratio n Ga s Predicte d Valu e f(Hig h Respons e - Zer o Respo n XMi d o rLo wLeve l Ga s ] + Zer o Respons e Hig h Leve l Ga s



### VES01809 1I 

## I

I

J

t 

### i VES01809 2