p. 1



# OAR Box 

# 1413 Prepped by Ollie Stewart



## Document

Number: 

# 72 ) 11-1-7 2 Docket Number: 

# A-94-5 2

Printed 7/9/2008 3:11:23 PM

Sheet 72 of 114P. 2 

# Jp-Z-7 2

DESTRUCTIO N EFFICIENC Y REPOR T AMERICA N STANDAR D SALEM , OHI O
Octobe r 10 , 1997

Project No
. 455-12-100 2

•i .-. , r • r°Ar.iH:.;*o,sr. r 

## Preparedfor : America nStandar d 605 Sout hEllswort hAvenue Salem , Ohio 4446 0

Preparedby : Optima l Technologies , Incorporated 57 5 Willia mPit t Wa y Pittsburgh , Pennsylvani a1523 8 (412 ) 828-733 0P. 3



## Addendu m DestructionEfficienc

y Repor t ofth e Polya

dVO C Abatemen

t Syste m Conducte da t America nStandard , Inc. , Salem , Ohi o o nSeptembe

r 16 , 199 7
Captur e Efficiency A captur e efficienc y determinationfo

r eachofth e 4 source s discharging t o th e abatemen t syste mwas requiredso tha

t a noverall control efficiency couldb e calculated
. The source s wer

e designedto provid

e 100 % captur

e of VOCs
. I nthe presenc e o

f Nort h Ohi o Valle

y Ai r Authorit y (NOVAA) officials , America nStandar ddemonstrate d100 % captur e o f VOC s b y utilizing ahand-hel ddevic e tha t propel s tal c dus t

inthe for mofa cloud
. Ever

y openin g i neachsourc e was unde

r negativ e pressur

e whil e norma

l productionactivitie s wer

e occurring
. Thi s reducedth e contro l efficiency determination t o adestructionefficienc

y measurement . Productio n Rate s NOVA A requestedtha

t the 4 source s discharging t o th e abatemen t syste mb e operate da

t 100 % capacit

y fo r th e destructio nefficiency test . While America nStandar ddoe s not clai mtha t th e source s operatedat

theoretica l maximu mcapacit y fo r thi s test , they wer

e operate da t the highes t

level tha t coul db e achievedwit

hcurren t resources . A tabl e showing the productionrate fo r eachsourc e fo

r eachtes t ru ni s give nbelow : SOURC E NO
. R00 8 P00 8 R01 8 P009 RU

N # 1 2 2 unit s 2 2 unit s 1 coa t 1 batc h RU

N # 2 1 9 unit s 1 9 unit s 1 coa t 1 batch RU

N # 3 2 1 unit s 2 1 unit s 1 coa t 1 batch AVERAG E 20.6 7 20.6 7 1 1 R00 8 average coating weight/unit = 4 8 lb s P00 8 accelerate s curing of

coating applie di

nR00 8 R01 8 average coating weight/coa t = 10 0 lb s P009 batc hsize = 150

0 lb s The average hourl

y controlledemissionrat

e fo r the 4 combinedsource s was 2.4 3 lbs/hr
.

.'- ) <-> -P. 4



## TABLEO FCONTENT S
1. 0 EXECUTIV

ESUMMAR

Y 1 SUMMAR

Y O FRESULTS 2 Ru nNo
. 1. ! 2 Ru nNo
. 2 2 Ru nNo
. 3 2 2. 0 TES T PROCEDURES 3 3. 0 QUALIT

Y ASSURANC

E4 ATTACHMENT S 1
. Sample Strea

mFlow Calculation s an

dTota l HydrocarbonAnalyze

r Measurement s 2
. FieldDat

aSheets an

dProces s Information 3
. Qualit

y Assuranc e 4
. Laborator

y Result sP. 5

American

Standard Salem, OH

Facility DRAFT DE Report


## 1.0 EXECUTIV ESUMMAR Y AmericanStandardoperate s a nacryli c an dfiberglas s bathin g vesse l manufacturin g facility i n Salem , Ohio
. Durin g th e manufacturin g andcoatin g processes , volatil e organi c compound s (VOCs ) eithe r

evaporat e int o th e air

or are drive nof

f whil e insid e ovens . Th e VOC s emitte db y thes e processe s are collecte db y hood s o r booth s an dar e directe dto th e contro l device
. I t wa s th e inten t

o f America nStandardto perfor mDestructio nEfficienc y (DE ) testin g for th e bathin g vesse l manufacturin g proces s line s a t it s Salem , O H facility
. Th e purpos e o f D Etestin g wa s to detennin e th e destructio nefficienc y o f th e capture dvolatil e organi c compoun d(VOC ) emission s inth e contro l syste m(incinerator)
. Optima l Technologies , Inc
. (Optimal ) was hire db y America nStandardto performDestructio n Efficienc y (DE ) testin g at thi s facility
. Thi s report describe s specifi c tes t

procedure s followe d durin g D Etesting-o nAmerica nStandard' s contro l device
. Wher e practical , th e principal s o f Unite dState s Environmenta l Protectio nAgenc y (EPA ) Method s 2 throug h4 wer e utilize dt o measur e th e volumetri c flo w rate , oxyge n(0 2 

### ) , carbo ndioxid e (C0 2 

### ) , an dmoistur e conten t o f th e ga s streams . Optima l performe dD Etestin g utilizin g tota l hydrocarbo n(THC ) analyzer s with flam e ionizatio ndetector s (FIDs ) complyin g withth e tes t guideline s describe di nU.S
. EPA' s Metho d25A , Determinatio no f Total Gaseou s Organi c Concentratio nUsin g aFlam e Ionizatio n Analvzer
. Durin g th e D Etesting , appropriat e proces s line s wer e operatin g unde r require d conditions
. Optima l als o collecte don e ga s streamsampl e fromth e inle t an doutle t

for eac htes t ru nt o determin e methan e an daceton e concentrations
. Tedlar ® bag s were use dt o contai nth e ga s . \Vi*\ / 

### streamsamples
. Th e sample s were sen t to tw o qualifie dai r

quality laboratorie s for

analyse s o f

_'r„ ' methan e an daceton e content . Th e result s o f the~analysi s enable dOptima l t o subtrac t of f an y [ ^(-„ ; methan e an daceton e contributio nto FI D concentratio noutputs . .- , .\' ' Th e .averag e o f

tlire e run s th e incinerato r D Ei s 94.7%
. Al l result s ar e reporte das/propane; 1 

### equivalent*
. ^ ' ' '. / - . r\P. 6

American Standard Salem, OH

Facility DRAFT DE Report



### SUMMAR Y O FRESULT S Ru n No
. 1 Averag e Inle t

Concentratio n(a s propane ) 24 5 pp m Averag e Outle t

Concentratio n(a s propane ) 1 7 pp m Inle t Methan e Concentratio n(a s propane ) 1. 5 pp m Outle t Methan e Concentratio n(a s propane ) 1. 2 pp m Inle t Aceton e Concentratio n(a s propane ) 18. 8 pp m Outle t Aceton e Concentratio n(a s propane ) 4. 8 pp m Destructio n Efficienc y (with methane/aceton e compensation ) 94.4 %
Ru n No
. 2 Averag e Inle t

Concentratio n(a s propane ) 24 8 pp m • Averag e Outle t

Concentratio n(a s propane ) ; 1 9 pp m Inle t Methan e Concentratio n(a s propane ) 0. 6 pp m Outle t Methan e Concentratio n(a s propane ) 1. 3 pp m Inle t Aceton e Concentratio n(a s propane ) 3. 7 pp m Outle t Aceton e Concentratio n(a s propane ) 5. 5 pp m Destructio n Efficienc y (with methane/aceton e compensation )
. . 94.9 %
Ru n No . 3 Averag e Inle t

Concentratio n(a s propane ) 27 5 pp m Averag e Outle t

Concentratio n(a s propane ) ;. • 2 0 pp m Inle t Methan e Concentratio n(a s propane ) 3. 6 pp m Outle t Methan e Concentratio n(a s propane ) 4. 0 pp m Inle t Aceton e Concentratio n(a s propane ) 2. 5 pp m Outle t Aceton e Concentratio n(a s propane ) 2. 4 pp m Destructio nEfficienc y (withmethane/aceton e compensation ) 94.7 % Refer t o Table s 1 an d2 fo

r th e D Ecalculation s a s wel l a s methan e an daceton e concentrations
.

LP. 7

American Standard Salem, OH

Facility DRAFT DE Report


## 2. 0 TES T PROCEDURE S Thi s sectio ndescribe s specifi c tes t procedure s followe ddurin g preliminary D Etestin g o nth e incinerator
. Durin g th e D Etesting , th e proces s line s were operatin g at ful l capacity
. Th e principal s o f

EP A Method s 2 throug h4 were utilize dt o measur e th e volumetri c flo w rate , oxyge n(0 2 

### ) , carbo ndioxid e (C0 2 

### ) , an dmoistur e conten t ofeac hofth e five inle t

ga s stream s an d th e singl e outlet

ga s streams . T o determin e th e D Eo f

th e incinerator , measuremen t o f th e inle t andoutle t

(incinerated ) THC s too k plac e inside th e ductwork , before an dafte

r th e incineratio nprocess . Two TH C analyzer s withFID s wit

hheate dsampl e train s continuousl y measure dth e THC s enterin g an dexitin g th e incinerator
. Clea nstainles s stee l probe s wer e inserte dint o th e ga s stream s (inle t an doutlet ) an d attache dt o th e heate dsampl e line s (HSLs)
. Thi s samplin g procedur e followe dth e principal s describe di nEP A Metho d25A
. Optimal utilize dJUM Mode l VE 7 FIDs
. On e FID/HS Lsampl e trai nmeasure dth e THC s inth e sampl e streamfromth e inle t o f th e contro l device
. Th e othe r FID/HS Lsampl e trai nmeasure dTHC s i nth e sampl e streamexitin g th e outle t o f th e contro l device
. Th e concentration s were continuousl y measure dan drecorde devery thirty second s b y a datalogger
. Eac hFI D wa s calibrate dt o propan e a s describe di nth e method
. D Etes t samplin g wa s performe dove r

thre e 1-hou

r samplin g runs . Spreadsheet s i nAttachmen t 1 lis t th e TH C emissio nconcentration s for eac htes t run . Attachment s 2 an d3 contai nth e fielddat asheet s an d quality assuranc e information , respectively
. Tedlar ® bag s wer e use dto collec t ga s streamsample s t o b e analyze dJOT ..methane an daceton e content . Optima l sen t

th e ga s sample s t o experience dan dqualifie dlaboratorie s t o b e analyze d for methan e conten t

an dacetone . Th e sample s wer e analyze dwithi n7 2 hour' s o f collection
. Th e ga s sample s wer e analyze db y ga s chromatograph y (GC ) whic hha s ar i FI D calibrate dwith methan e calibratio ngas . Optimal' s JUM Mode l VE 7 FID s hav e a43.2 % respons e facto r fo r methan e whe ncalibrate dwit hpropane . Therefore , concentration s o f methan e (calibrate da s methane ) wil l b e converte dt o a n"a s propane " respons e andsubtracte dfromth e averag e FI D outputs . Optimal' s JU M Mode l VE 7 FID s hav e a120 % respons e facto r for aceton e whe n calibrate dwithpropane . Therefore , concentration s o f aceton e (calibrate da s acetone ) wil l b e converte dt o a

n"a s propane " respons e an dsubtracte dfro mth e averag e FI D outputs . Attachmen t

4 contain s laborator

y analyse s results
.

I



# I vP. 8

American Standard Salem, OH

Facility DRAFT DE Report



## 3. 0 QUALIT Y ASSURANC E Qualit y assuranc e o

f the FI D was determinedb

y initia l calibrations , sample bia s checks , calibratio ndrif

t checks , an

ddeterminationo

f respons e times
. Eac

hFI D was calibrate dprior

t o the tes t ru nwit hzer o ai r fro maspecialt

y gas supplie

r andup t o three certifiedconcentration s (low , middle , an

dhighrange ) of

propane . Secondly , asampl e bia s chec k wa s performedby comparing th

e calibrationgas respons e throug hthe sample trai nan

ddirectly int

o th e instrument
. Respons e time s fo

r on e sample line (pe

r instrument

) was determine dprior

t o the first tes t runand recorded
. A

t th e en do f eac htest , zer o ai r an don e representativ e calibrationconcentratio nwa s introducedt

o eac hFI D t o determine calibrationdrift
. All calibrationdatai s containe di n Attachmen

t 3
. -



# ' 1P. 9



### TABL E1 AMERICA N STANDARD SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T

Septembe r16,199 7 Destructio n Efficiency Result s v/l methan e and aceton e compensatio n

Poin tj 

### rrib-iir. '••

- i n IOI


### i n 10 1



### m 10 1

/O C Destruc t Poin tj ID # II I 10 1

II I 10 1

II I IO I Poin t

Nam e IncineratorInlet IncineratorOutlet

* IncineratorInlet IncineratorOutlet

IncineratorInlet IncineratorOutlet

o n Efficiencie s Fro m Eac h In c

Poin t Nam e IncineratorInlet IncineratorOutlet

IncineratorInlet IncineratorOutlet

IncineratorInlet IncineratorOutlet Tes t Ru n 1 1

2 2

3 3

inerato r(kg/k g Tes t Ru n 1 1

2 2

3 3 CO)

(ppm ) 224. 7 1 1

243. 7 12. 2

268. 9 13. 6
) C(Fj )

219. 0 10. 0

236. 2 11.7

262. 9 13. 0 C(DO ) 1

0. 6

1 0. 4

- 2 0.1 5

Q(Fj ) 738.1 8 873.06

831.6 2 851.7 5

784.4 2 847.3 3 C(DH )

505. 5 25. 9

508. 5 25. 1

50 7 25. 4

T(F ) 6 0 6 0

6 0 6 0

6 0 6 0 C(H ) 49 4

24. 4

49 4 24. 4

49 4 24. 4

K(l ) 1.83E-0 6 1.83E-0 6 Ru n # 1 DE = I.83E-0 6 1.83E-0 6 Run WI DE = 1.8 3 E-0 6
' I.83E-0 6 C(Fj ) >

(ppm ) 219. 0 10. 0

236. 2 11. 7

262. 9 13. 0

F(Bj ) (kg ) 17. 8 1. 0 94.4 % 21. 6 1.1 94.9 % 22. 6 1. 2 Run # 3 DE = 94.7 % AVERAG E D E = WHERE : C(Fj ) = correcte daverag e VO C concentration s o f emission s a

t poin t j , pp mpropan e C(j ) = correcte d(for

methan e andacetone ) averag e VO C concentration s measure da t poin t j , ppmpropan e C(DO ) = averag e syste mdrif t chec k concentratio nfo

r zer o concentratio ngas , pp mpropan e C(D I I) = averag e measure dconcentratio nfo r th e drif t chec k calibratio ngas , pp mpropan e C(H ) = actua l concentratio no f th e drif t chec k calibratio ngas , ppmpropan e C(Fj) = (C(j)-C(DO) ] x |[C(H)/[C(DH)-C(DO)] J F(Bj ) = total VO C conten t o f emission s frompoin t

j , k g = C(Fj)xQ(Fj)xT(F)xK(l ) Q(I'j ) = averag e effluent

volumetri c flo w rate correcte dto standardcondition s a t poin t j , m3/min=dscf

mx 0.028 3 T(F ) = tota l duratio no f

samplin g run , min
. K ( 1 ) = 1.8 3 x IOE- 6 kg/(m3-ppm ) (facto r fo r propane ) 94.7 %



# 'IP.1 0



## TABLE2 AMERICA

NSTANDAR

D SALE M OHI O FACILITY DESTRUCTIONEFFICIENC Y TES T
' September

16,199 7 Destructio nEfficienc

y Result s methan e an daceton e consentration s FI D Respons e Methan e Acetone Ru nNo
. 1 Methane Acetone Ru nNo
. 2 Methan e Acetone Ru nNo"
. 3 Methane Acetone Factor s

=43 % =120 %
Concentration(ppm

) Concentration(ppm

)
Concentration(ppm

) Concentration(ppm

)
Concentration(ppm

) Concentration(ppm) La b Result s Inle t 3. 5 15. 6
1. 5 3. 1
8.4 2. 1 Outle t 2. 7 4. 0
3. 1 4. 6
9. 3 2. 0 ( O ('• l



### a s Propan e Inle t Outle t 1. 5 1.

2 18:8 , 4. 8
0. 6
.. i 1.3 3. 7 * v

### 5. 5
3. 6 4. 0 2. 5 2. 4



# aP.1 1



# ATTACHMEN T1 SAMPL E STREA M FLOWCALCULATION S AN D TOTA L HYDROCARBO N ANALYZE R

MEASUREMENT SP.1 2

AMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r16,199 7 Ru n No

. 1

DATE/TIM E 09/16/9 7 10:09:1 6 09/16/9 7 10:09:4 6 09/16/9 7 10:10:1 6 09/16/9 7 10:10:4 6 09/16/9 7 10:11:1 6 09/16/9 7 10:11:4 6 09/16/9 7 10:12:1 6 09/16/9 7 10:12:4 6 09/16/9 7 10:13:1 6 09/16/9 7 10:13:4 6 09/16/9 7 10:14:1 6 09/16/9 7 10:14:4 6 09/16/9 7 10:15:1 6 09/16/9 7 10:15:4 6 09/16/9 7 10:16:1 6 09/16/9 7 10:16:4 6 09/16/9 7 10:17:1 6 09/16/9 7 10:17:4 6 09/16/9 7 10:18:1 6 09/16/9 7 10:18:4 6 09/16/9 7 10:19:1 6 09/16/9 7 10:19:4 6 09/16/9 7 10:20:1 6 09/16/9 7 10:20:4 6 09/16/9 7 10:21:1 6 09/16/9 7 10:21:4 6 09/16/9 7 10:22:1 6 09/16/9 7 10:22:4 6 09/16/9 7 10:23:1 6 09/16/9 7 10:23:4 6 09/16/9 7 10:24:1 6 09/16/9 7 10:24:4 6 09/16/9 7 10:25:1 6 09/16/9 7 10:25:4 6 09/16/9 7 10:26:1 6 09/16/9 7 10:26:4 6 09/16/9 7 10:27:1 6 09/16/9 7 10:27:4 6 09/16/9 7 10:28:1 6 09/16/9 7 10:28:4 6 09/16/9 7 10:29:1 6 09/16/9 7 10:29:4 6 09/16/9 7 10:30:1 6 09/16/9 7 10:30:4 6 09/16/9 7 10:31:1 6 09/16/9 7 10:31:4 6 09/16/9 7 10:32:1 6 09/16/9 7 10:32:4 6 09/16/9 7 10:33:1 6 09/16/9 7 10:33:4 6 09/16/9 7 10:34:1 6 09/16/9 7 10:34:4 6 09/16/9 7 10:35:1 6 09/16/9 7 10:35:4 6 09/16/9 7 10:36:1 6 09/16/9 7 10:36:4 6 09/16/9 7 10:37:1 6 09/16/9 7 10:37:4 6 09/16/9 7 10:38:1 6 09/16/9 7 10:38:4 6 09/16/9 7 10:39:1 6 INLE T THC s (ppm ) 24 7 23 2 21 7 17 0 22 2 30 8

- - 24 9 21 2 16 2 28 7 25 4 28 3 22 1 24 5 28 9 25 0 22 1 169 - 13 7 179 - 29 1 242

. 191

. 17 2 245 - 275 - 29 2 20 3 23 9 24 8 27 9 25 4 21 2 260 28 6 32 4 28 8 20 9 19 4 21 7 29 2 28 1 25 3 23 5 24 7 24 0 33 4 30 5 300 270 22 7 33 5 34 1 29 8 24 3 34 5 23 8 34 5 30 0 31 3 22 5 OUTLE T THC s (ppm ) 9 1 0 9 9 1 0 9 9 9 9 9 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 1 0 9 9 9 9 9 9 9 9 9 9 1 0 1 0 1 0 1 0 1 1 1 5 1 8 1 9 2 0 2 1 2 1 2 2 2 3 2 3 2 4 2 4 2 2 2 4 2 4 2 3 2 3 2 3 

# KAMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r16,199 7 Ru n No

. 1 P.1 3

i DATE/TIM E I 09/16/9 7 10:39:4 6 I 09/16/9 7 10:40:1 6 ! 09/16/9 7 10:40:4 6 09/16/9 7 10:41:1 6 09/16/9 7 10:41:4 6 ) 09/16/9 7 10:42:1 6 i 09/16/9 7 10:42:4 6 09/16/9 7 10:43:1 6 09/16/9 7 10:43:4 6 09/16/9 7 10:44:1 6 09/16/9 7 10:44:4 6 09/16/9 7 10:45:1 6 09/16/9 7 10:45:4 6 09/16/9 7 10:46:1 6 09/16/9 7 10:46:4 6 09/16/9 7 10:47:1 6 09/16/9 7 10:47:4 6 09/16/9 7 10:48:1 6 09/16/9 7 10:48:4 6 09/16/9 7 10:49:1 6 09/16/9 7 10:49:4 6 09/16/9 7 10:50:1 6 09/16/9 7 10:50:4 6 09/16/9 7 10:51:1 6 09/16/9 7 10:51:4 6 09/16/9 7 10:52:1 6 09/16/9 7 10:52:4 6 09/16/9 7 10:53:1 6 09/16/9 7 10:53:4 6 09/16/9 7 10:54:1 6 09/16/9 7 10:54:4 6 09/16/9710:55:1 6 09/16/9 7 10:55:4 6 09/16/9 7 10:56:1 6 09/16/9 7 10:56:4 6 09/16/9 7 10:57:1 6 09/16/9 7 10:57:4 6 09/16/9 7 10:58:1 6 09/16/9 7 10:58:4 6 09/16/9 7 10:59:1 6 09/16/9 7 10:59:4 6 09/16/9 7 11:00:1 6 09/16/9 7 11:00:4 6 09/16/9 7 11:01:1 6 09/16/9 7 11:01:4 6 09/16/9 7 11:02:1 6 09/16/9 7 11:02:4 6 09/16/9 7 11:03:1 6 09/16/9 7 11:03:4 6 09/16/9 7 11:04:1 6 09/16/9 7 11:04:4 6 09/16/9 7 11:05:1 6 09/16/9 7 11:05:4 6 09/16/9 7 11:06:1 6 09/16/9 7 11:06:4 6 09/16/9 7 11:07:1 6 09/16/9 7 11:07:4 6 09/16/9 7 11:08:1 6 09/16/9 7 11:08:4 6 Average s INLE T

THC s (ppm ) 17 9 15 5 22 1 274 33 7 25 8 18 1 16 1 16 1 26 3 24 8 28 9 17 6 23 3 22 2 29 0 33 8 27 2 19 7 39 6 29 3 26 2 18 0 23 9 24 8 24 2 20 9 23 8 17 7 35 2 30 5 274 24 7 18 1 150 13 3 21 8 30 1 26 2 22 4 16 4 13 5 34 2 26 9 22 6 21 1 21 6 15 5 25 3 26 9 30 6 23 9 17 7 294 32 8 30 6 19 5 16 1 13 8 24 5 OUTLE T THC s (ppm ) 2 3 2 3 2 4 2 4 2 4 2 3 2 2 2 1 2 2 2 3 2 3 2 3 2 2 2 1 2 1 2 2 2 3 2 2 2 2 2 1 2 2 2 3 2 3 2 3 2 3 2 4 2 3 2 2 2 2 2 2 2 2 2 2 2 1 2 0 2 0 2 2 2 2 2 1 2 1 2 0 1 9 1 8 1 9 2 0 2 0 1 9 1 8 1 7 1 7 1 8 1 8 1 8 1 8 1 8 1 7 1 7 1 7 1 8 1 7 1 7

1P. M

AMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r16,199 7 Ru n No . 2

DATE/TIM E 09/16/9 7 11:21:4 3 09/16/9 7 11:22:1 3 09/16/9 7 11:22:4 3 09/16/9 7 11:23:1 3 09/16/9 7 11:23:4 3 09/16/9 7 11:24:1 3 09/16/9 7 11:24:4 3 09/16/9 7 11:25:1 3 09/16/9 7 11:25:4 3 09/16/9 7 11:26:1 3 09/16/9 7 11:26:4 3 09/16/9 7 11:27:1 3 09/16/9 7 11:27:4 3 09/16/9 7 11:28.1 3 09/16/9 7 11:28:4 3 09/16/9 7 11:29:1 3 09/16/9 7 11:29:4 3 09/16/9 7 11:30:1 3 09/16/9 7 11:30:4 3 09/16/9 7 11:31:1 3 09/16/9 7 11:31.4 3 09/16/9 7 11:32:1 3 09/16/9 7 11:32:4 3 09/16/9 7 11:33:1 3 09/16/9 7 11:33:4 3 09/16/9 7 11:34:1 3 09/16/9 7 11:34:4 3 09/16/9 7 11:35:1 3 09/16/9 7 11:35:4 3 09/16/9 7 11:36:1 3 09/16/9 7 11:36:4 3 09/16/9 7 11:37:1 3 09/16/9 7 11:37:4 3 09/16/9 7 11:38:1 3 09/16/9 7 11:38:4 3 09/16/9 7 11:39:1 3 09/16/9 7 11:39:4 3 09/16/9 7 11:40:1 3 09/16/9 7 11:40:4 3 09/16/9 7 11:41:1 3 09/16/9 7 11:41:4 3 09/16/9 7 11:42:1 3 09/16/9 7 11:42:4 3 09/16/9 7 11:43:1 3 09/16/9 7 11:43:4 3 09/16/9 7 11:44:1 3 09/16/9 7 11:44:4 3 09/16/9 7 11:45:1 3 09/16/9 7 11:45:4 3 09/16/9 7 11:46:1 3 09/16/9 7 11:46:4 3 09/16/9 7 11:47:1 3 09/16/9 7 11:47:4 3 09/16/9 7 11:48:1 3 09/16/9 7 11:48:4 3 09/16/9 7 "11:49::i3 " " 09/16/9 7 11:49:4 3 09/16/9 7 11:50:1 3 09/16/9 7 11:50:4 3 09/16/9 7 11:51:1 3 09/16/9 7 11:51:4 3 INLE T THC s (ppm ) 28 7 24 9 33 0 24 1 32 3 36 3 314 23 7 17 7 23 6 16 2 22 8 20 0 25 1 26 9 25 1 18 0 31 1 26 7 34 6 22 2 30 9 34 5 41 7 33 2 29 5 23 8 33 3 38 8 32 7 27 6 21 1
• 29 3 30 8 32 1 32 1 24 9 22 7 21 5 19 2 25 2 16 5 14 2 24 4 18 5 29 0 28 1 31 1 24 0 32 2 18 3 39 9 30 8 27 5 26 4
" " 30 5 20 6 34 3 27 2 35 5 23 6 OUTLE T THC s (ppm ) 1 5 1 7 1 8 1 8 1 7 1 7 1 8 1 8 1 8 1 9 1 9 1 9 1 9 1 9 1 9 1 9 1 8 1 7 1 8 1 7 1 8 1 8 1 8 1 8 1 9 1 9 1 9 1 9 2 0 2 1 2 1 2 1 2 0

. 2 1 2 1 2 2 2 1 2 1 2 1 2 1 2 0 2 1 2 1 2 0 2 0 1 9 2 0 1 9 1 9 1 9 1 9 2 0 2 1 2 1 2 1 2 1 2 2 2 1 2 2 2 2 2 2

•J)P.1 5

AMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r16,199 7 Ru n No

. 2

DATE/TIM E 09/16/9 7 11:52:1 3 09/16/9 7 11:52:4 3 09/16/9 7 11:53:1 3 09/16/9 7 Y i :53:43 " 09/16/9 7 i 1:54:1 3 09/16/9 7 11:54:4 3 09/16/9 7 11:55:1 3 09/16/9 7 11:55:4 3 09/16/9 7 11:56:1 3 09/16/9 7 11:56:4 3 09/16/9 7 11:57:1 3 09/16/9 7 11:57:4 3 09/16/9 7 11:58:1 3 09/16/9 7 11:58:4 3 09/16/9 7 11:59:1 3 09/16/9 7 11:59:4 3 09/16/9 7 12:00:1 3 09/16/9 7 12:00:4 3 09/16/9 7 12:01:1 3 09/16/9 7 12:01:4 3 09/16/9 7 12:02:1 3 09/16/9 7 12:02:4 3 09/16/9 7 12:03:1 3 09/16/9 7 12:03:4 3 09/16/9 7 12:04:1 3 09/16/9 7 12:04:4 3 09/16/9 7 12:05:1 3 09/16/9 7 12:05:4 3 09/16/9 7 12:06:1 3 09/16/9 7 12:06:4 3 09/16/9 7 12:07:1 3 09/16/9 7 12:07:4 3 09/16/9 7 12:08:1 3 09/16/9 7 12:08:4 3 09/16/9 7 12:09:1 3 09/16/9 7 12:09:4 3 09/16/9 7 12:10:1 3 09/16/9 7 12:10:4 3 09/16/9 7 12:11:1 3 09/16/9 7 12:11:4 3 09/16/9 7 12:12:1 3 09/16/9 7 12:12:4 3 09/16/9 7 12:13:1 3 09/16/9 7 12:13:4 3 09/16/9 7 12:14:1 3 09/16/9 7 12:14:4 3 09/16/9 7 12:15:1 3 09/16/9 7 12:15:4 3 09/16/9 7 12:16:1 3 09/16/9 7 12:16:4 3 09/16/9 7 12:17:1 3 09/16/9 7 12:17:4 3 £9/16/9 7 12:18:1 3 09/16/9 7 12:18:4 3 [09/16/9 7 12:19:1 3 09/16/9 7 12:19:4 3 09/16/9 7 12:20:1 3 09/16/9 7 12:20:4 3 09/16/9 7 12:21:1 3 Average s INLE T!

THC s j (ppm ) j 176 | 28 7 28 3 25 3 j 207' j 18 4 24 1 18 3 35 8 29 2 26 0 17 7 29 1 26 1 25 3 32 5 19 5 24 1 384 29 7 25 5 25 5 16 8 29 8 30 1 25 6 28 7 20 6 16 4 13 4 27 9 27 8 28 2 17 7 25 9 16 9 13 7 11 8 14 5 36 6 29 2 23 8 154 " 19 6 29 3 26 7 33 3 19 4 15 0 12 6 11 5 10 1

. 9 1 10 2 13 7 11 0 9 6 23 3 24 9 24 8 OUTLE T THC s (ppm ) 2 3 22 '

. 2 2 2 2 2 1 ~2 T 21 "
" 2' i 2 1 2 1 2 1 2 0 1 9 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 8 1 7 1 7 1 7 1 7 1 7 1 7 1 7 1 7 1 7 1 7 1 7 1 6 1 6 1 6 1 6 1 7 1 7 1 6 1 6 1 6 1 7 1 7 1 7 1 7 2 0 1 9 1 9 

# HP.1 6

AMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r 16,199 7 Ru n No . 3

I DATE/TIM E 09/16/9 7 13:03:3 8 I 09/16/9 7 13:04:0 8 09/16/9 7 13:04:3 8 " 09/16/971305:0 8 i 09/16/9 7 13:05:3 8 ! 09/16/9 7 13:06:0 8 09/16/9 7 13:06:3 8 09/16/9 7 '13:07:08 " 09/16/9 7 13:07:38" " " 09/16/9 7 13:08:0 8 09/16/9 7 13:08:3 8 09/16/9 7 13:09:0 8 09/16/9 7 13:09:3 8 09/16/9 7 13:10:0 8 09/16/9 7 13:10:3 8 09/16/9 7 13:11:0 8 09/16/9 7 13:11:3 8 09/16/9 7 13:12:0 8 09/16/9 7 13:12:3 8 09/16/9 7 13:13:0 8 09/16/9 7 13:13:3 8 09/16/9 7 13:14:0 8 09/16/9 7 13:14:3 8 09/16/9 7 13:15:0 8 09/16/9 7 13:15:3 8 09/16/9 7 13:16:0 8 09/16/9 7 13:16:3 8 09/16/9 7 13:17:0 8 09/16/9 7 13:17:3 8 09/16/9 7 13:18:0 8 09/16/9 7 13:18:3 8 09/16/9 7 13:19:0 8 09/16/9 7 13:19:3 8 09/16/9 7 13:20:0 8 09/16/9 7 13:20:3 8 09/16/9 7 13:21:0 8 09/16/9 7 13:21:3 8 09/16/9 7 13:22:0 8 09/16/9 7 13:22:3 8 09/16/9 7 13:23:0 8 09/16/9 7 13:23:3 8 09/16/9 7 13:24:0 8 09/16/9 7 13:24:3 8 09/16/9 7 13:25:0 8 09/16/9 7 13:25:3 8 09/16/9 7 13:26:0 8 09/16/9 7 13:26:3 8 09/16/9 7 13:27:0 8 09/16/9 7 13:27:3 8 09/16/9 7 13:28:0 8 09/16/9 7 13:28:3 8 09/16/9 7 13:29:0 8 09/16/9 7 13:29:3 8 09/16/9 7 13:30:0 8 09/16/9 7 13:30:3 8 09/16/9 7 13:31:0 8 09/16/9 7 13:31:3 8 09/16/9 7 13:32:0 8 09/16/9 7 13:32:3 8 09/16/9 7 13:33:0 8 09/16/9 7 13:33:3 8 INLE T THC s (ppm ) 28 5 17 5 "124 " 29 1 24 3 28 2 17 7 397 ' 31 2 27 0 16 6 26 2 25 6 31 2 17 8 23 9 16 1 34 4 29 7 27 1 16 7 28 5 28 8 27 9 30 3 18 0 13 3 35 7 28 2 37 9 .17 9 37 0 29 2 38 9 23 5 16 3 13 3 19 3 12 8 20 8 150 41 3

. 30 1 36 7 19 1 45 9 36 7 31 9 30 9 33 6 30 9 37 9 269 , 19 3 43 8 38 9 35 0 43 9 31 3 45 8 404 OUTLE T THC s (ppm ) 8 1 0 9 9 9 1 0 1 1

. 1 3 1 3 1 3 1 3 1 4 1 5 1 5 1 6 1 6 1 6 1 6 1 6 1 6 1 6 1 6 1 6 1 5 1 7 1 7 1 7 1 7 1 7 1 7 1 8 1 8 1 7

. 1 7 1 8 1 8 1 8 1 8 1 9 1 9 2 2 2 1 1 9 1 8 1 7 1 8 1 8 2 1 2 1 2 2 2 1 2 4 2 3 2 3 2 2 2 3 2 3 2 3 2 2 2 1 2 3

I K .P.1 7

AMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC YTES T Septembe r 16,199 7 Ru n No . 3

DATE/TIM E 09/16/9 7 13:34:0 8 09/16/9 7 13:34:3 8 " T 09/ i 6/9 7 13:35:0 8 09/16/9 7 13:35:3 8 , 09/16/9 7 13:36:0 8 09/16/9 7 13:36:3 8 09/16/9 7 13:37:0 8 09/16/9 7 13:37:3 8 09/16/9 7 13:38.0 8 09/16/9 7 13:38:3 8 09/16/9 7 13:39:0 8 09/16/9 7 13:39:3 8 09/16/9 7 13:40:0 8 09/16/9 7 13:40:3 8 09/16/9 7 13:41:0 8 09/16/9 7 13:41:3 8 09/16/9 7 13:42:0 8 09/16/9 7 13:42:3 8 09/16/9 7 13:43:0 8 09/16/9 7 13:43:3 8 09/16/9 7 13:44:0 8 09/16/9 7 13:44:3 8 09/16/9 7 13:45:0 8 09/16/9 7 13:45:3 8 09/16/9 7 13:46:0 8 09/16/9713:46:3 8 09/16/9 7 13:47:0 8 09/16/9 7 13:47:3 8 09/16/9 7 13:48:0 8 09/16/9 7 13:48:3 8 09/16/9 7 13:49:0 8 09/16/9 7 13:49:3 8 09/16/9 7 13:50:0 8 09/16/9 7 13:50:3 8 09/16/9 7 13:51:0 8 09/16/9 7 13:51:3 8 09/16/9 7 13:52:0 8 09/16/9 7 13:52:3 8 09/16/9 7 13:53:0 8 09/16/9 7 13:53:3 8 09/16/9 7 13:54:0 8 09/16/9 7 13:54:3 8 09/16/9 7 13:55:0 8 09/16/9 7 13:55:3 8 09/16/9 7 13:56:0 8 09/16/9 7 13:56:3 8 09/16/9 7 13:57:0 8 09/16/9 7 13:57:3 8 09/16/9 7 13:58:0 8 09/16/9 7 13:58:3 8 09/16/9 7 13:59:0 8 09/16/9 7 13:59:3 8 09/16/9 7 14:00:0 8 09/16/9 7 14:00:3 8 09/16/9 7 14:01:0 8 09/16/9 7 14:01:3 8 09/16/9 7 14:02:0 8 Average s INLE T| OUTLE T

THC s THC s (ppm ) (ppm ) 48 8 31 4 25 3 26 6 24 7 35 6 40 1 32 1 24 8 31 5 28 0 30 7 23 6 16 7 21 8 17 4 29 8 36 0 28 3 26 8 32 3 21 1 26 5 374 29 9 29 3 21 9 17 7 37 2 31 4 28 3 38 1 20 6 24 8 32 7 43 2 33 1 27 6 27 2 18 9 14 2 12 7 20 3 140 11 6 24 0 32 8 27 8 24 8 18 8 29 6 34 4 27 5 29 6 18 8 14 7 12 1 27 5 2 4

2 4 2 5 2 4 2 5 2 6 2 7 2 5 2 4 2 3 2 3 2 4 2 5 2 4 2 3 2 3 2 4 2 3 2 2 2 1 2 1 2 1 2 2 2 3 2 2 2 3 2 3 2 2 2 2 2 4 2 3 2 3 2 1 2 2 2 4 2 3 2 4 2 4 2 2 2 2 2 3 2 5 2 4 2 4 2 3 2 2 2 0 2 0 2 0 1 9 1 9 2 0 2 2 2 2 2 2 2 3 2 2 2 0


# i £AMERICA N STANDARD SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T

Septembe r16,199 7 OXIDIZE RINLE T FLOW S RU N NO . 1

SYMBO L DESCRIPTIO N Nort h South Toolin g Cur e Spra y Spra y Booth Ove n Mixe rBooth Booth



# fr 6 

# :l,*fiO s 

# W! 0.33 0 82.0 ^ 0.0 0
'

. 20.0 0 180.0 0 28.9 6 -0.0 3 28.9 6 - 0.9 9 28.1 0 0.37 0

88.0^'' * 0.0 0 20.0 0 80.0 0 28.9 6 0.6 0 29.00-

- 0.9 9 12.0 0 SQRT(dP= Averag e o f

squar e root s o f

pito t pressure , in
. wate r T s = Averag e stac k temperature , deg
. F C0 2 = C0 2 instac k gas , % 0 2 = 0 2 instac k

gas , % CO+N 2 = C O an dN 2 instac k gas , % ' Pba r = Barometri c pressure , in
. Hg
. Pa= Stati c pressure , in
. wate r P s = Stac k

pressur e (absolute) , in
. Hg
. Cp = Pito t

correctio nfactor , dimensionles s D s = Diamete r

o f stack , in
. Bw s = Moistur e conten t ofth e ga s stream , % CALCULATE D VALUE S A s = Are aofth e stack , sq . ft
. M d= Dr

y molecular

weigh t o f stac k gas , dr y basis , lb/lb-m o : M s = Molecula

r weigh t o f stac k gas , wet basis , lb/lb-mol e

GA S FLOW , V s = Stac k

velocity , ft/se c = 22.6 1 25.4 5 Q s = Stac k

ga s flow , acf

m= 584 2
. 119 9 Qs d= Stac k

ga s flow, dscf

m= 539 3 1100 TOTA L FLO W O F AL L INLE T SOURCES , dsc f = 2608 4 1.140 85.054 ' 0.0 0 20.0 0 80.0 0 28.9 6 6.3 0 29.42

- 0.9 9 6.0 0 1.9- ^

. / • 0.196 4
" 28JW
. "28.5 9

77.6 6 91 5 85 5 0.34 0
' 76.0- ' 0.0 0 20.0 0 80.0 0 28.9 6 -0.3 0 28.9 4 * 0.9 9 34.0 0 1.9 63050 ' 28.8 0 28.5 9
23.1 6 87 6 r 818 9 0.44 0



### 80.0^? ° 0.0 0 20.0 0 80.0 0 28.9 6 -0.4 0 28.93

- 0.9 9 34.0 0 2.0- ^ 6.3C 28.8 0 '28.58}/ ^
30.0 9 1138 3 1054 7

T J c oAMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T

Septembe r16,199 7 OXIDIZE ROUTLE T FLOW S

RUN NO . 1 GA S FLO W 

# \ l I OK 7 X Y\

SYMBO L DESCRIPTIO N SQRT(dP= Averag e o f

squar e root s o f

pito t pressure , in
. water T s = Averag e stac k temperature , deg
. F= C0 2 = C0 2 i

nstac k gas , % 0 2 = 0 2 i

nstac k gas , % C0+N 2 = C O an dN 2 i nstac k gas , % Pba r = Barometri c pressure , in
. Hg
. = P a= Stati c pressure , in
. wate r = P s = Stac k

pressure (absolute) , in
. Hg
. = Cp = Pito t

correctio nfactor , dimensionles s = D s = Diameter

o f stack , in
. = Bw s = Moisture conten t ofth e ga s stream , % = CALCULATE D VALUE S A s = Are aofth e stack , sq . ft. = M d= Dr

y molecula

r weigh t o f stac k gas , dr y basis , Ib/lb-m o = M s = Molecula

r weigh t o f stac k gas , wet basis , lb/lb-mol e = Incinerato r Outle t
106.0^ > 0.0 0

. 20.0 0 80.0 0 28.9 6 (28.96 ^ r t "6.9 9 43.0 0 B>"V

5 1-5 „ _/&> .10.0847 3 A•

> ' -20 0 "S^- 0 0 2&64"2?f.8'Z
- A* : GA S FLO W V s = Stac k

velocity , ft/sec Q s = Stac k

gas flow , acf m Qs d = Stac k

ga s flow , dscf m ^ 3 3 5 6 -I * 3468 9 .3085 0 ^oiy ?

C OAMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T Septembe r16,199 7 OXIDIZE RINLE T FLOW S RU N NO . 2

O SYMBO L DESCRIPTIO N SQRT(dP= Averag e o f

square root s o f

pito t pressure , in
. wate r T s = Averag e stac k temperature , deg
. F C0 2 = C0 2 i

nstac k gas , % 0 2 = 0 2 i n stac k gas , % CO+N 2 = C O an

dN 2 i nstac k gas , % Pba r = Barometri c pressure , in
. Hg
. P a= Stati c pressure , in
. water P s = Stac k

pressure (absolute) , in
. Hg
. Cp = Pito t

correctio nfactor , dimensionles s D s = Diameter

o f stack , in
. Bw s = Moistur e conten t ofth e ga s stream , % CALCULATED VALUE S A s = Are aofth e stack , sq . ft. M d= Dr

y molecula

r weight o f stac k gas , dr y basis , lb/lb-m o : M s = Molecula

r weight o f stac k gas , wet basis , lb/lb-mol e

GA S FLO W V s = Stac k

velocity , ft/sec Q s = Stac k

ga s flow , acf

m Qs d= Stac k

ga s flow , dscf

m TOTA L FLO W O F AL L INLE T SOURCES , dsc f = 2938 6 Toolin g Booth 0.35 0 84.0-j 1

- ! 0.0 0 20.0 0 80.0 0 28.9 6 0.3 1 28.9 8 v / 0.9 9 28.1 0 2. 1 •*.•-•£ C " 4366 7 28.8 0 28,5 7
24.0 1 620 4 571 1 Cur e Ove n Mixe r 0.37 0 1.08 0 L * 92. 0 C

J C y 92. 0 -'' ' 0.0 0 20.0 0 80.0 0 28.9 4 0.3 8 28.97^ ' 0.9 9 12.0 0 1. 9 .-5 ' 0.785 4 28.8 0 28.5 9
25.5 7 120 5 109 5 0.0 0

20.0 0 80.0 0 28.9 6 6.3 0 29.42 " 0.9 9 6.0 0 1. 9 0.196 4 28.8 0 28.5 9
74.0 4 87 2 80 5 North Spra y Booth 0.43 0 "-'Jm 80. 0 5 ' 0.0 0 20.0 0 80.0 0 28.9 6 -0.4 8 28.92 - 0.9 9 34.0 0 1. 8



### . ; 

### H ' 6305 0 28.8 0 28.6 1
29.4 0 1112 2 1032 4 South

Spra y Boot h 0.48 0 

## ^ 

## se^ o y i / ? 0.0 0 20.0 0 80.0 0 28.9 6 -0.5 2 28.92 ^ 0.9 9 34.0 0 1. 9

* ' • • > 6.305 0 " ' 28.8 0 28.5 9
33.0 1 1248 8 1145 1

h oAMERICA N STANDARD SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T

Septembe r16,199 7 

## V l OXIDIZE ROUTLE T FLOW S

RU N NO . 2 GA S FLO W
SYMBO L DESCRIPTIO N Incinerato r Outle t SQRT(dP= Averag e o f

squar e root s o f

pito t pressure , in
. wate r T s = Averag e stac k temperature , deg
. F C0 2 = C0 2 instac k gas , % 0 2 =0 2 i

nstac k gas , % C0+N 2 = C O an dN 2 instac k gas , % Pba r = Barometri c pressure , in
. Hg
. P a= Stati c pressure , in
. wate r P s = Stac k

pressur e (absolute) , in
. Hg
. Cp = Pito t

correctio nfactor , dimensionles s D s = Diameter

o f stack , in
. Bw s = Moistur e conten t ofth e ga s stream , % CALCULATE D VALUE S A s = Are aofth e stack , sq . ft. Md= Dr

y molecular

weigh t o f stac k gas , dr y basis , lb/lb-m o : M s = Molecula

r weigh t o f stac k gas , we t basis , lb/lb-mol e 0.800-4 P 106. 0 5&'- :



### V-z GA S FLO W V s = Stac k

velocity , ft/sec Q s = Stac k

ga s flow, acf

m Qs d= Stac k

ga s flow, dscf

m 45,9 3 Cfi& 3384 2 20O97 yx^

h oAMERICA N STANDAR D SALE M OHI O FACILIT Y DESTRUCTIO N EFFICIENC Y TES T

Septembe r16,199 7 OEXIDIZE

RINLE T FLOW S RU N NO . 3

- J SYMBO LDESCRIPTIO N SQRT(dP= Averag e o f

squar e root s o f

pito t pressure , in
. wate r T s = Averag e stac k temperature , deg
. F C0 2 = C0 2 i

nstac k gas , % 0 2 =0 2 i

nstac k gas , % CO+N 2 = C O andN 2 i nstac k gas , % Pba r = Barometri c pressure , in
. Hg
. P a= Stati c pressure , in
. wate r P s = Stac k

pressure (absolute) , in
. Hg
. C p = Pito t

correctio nfactor , dimensionles s D s = Diamete r

o f stack , in
. Bw s = Moistur e conten t ofth e ga s stream , % CALCULATE D VALUE S A s = Are aofth e stack , sq . ft. M d= Dr

y molecula

r weigh t o f stac k gas , dr y basis , lb/lb-m o : M s = Molecula

r weight o f stac k gas , we t basis , lb/lb-mol e

GA S FLO W V s = Stac k

velocity , ft/sec Q s = Stac k

ga s flow , acf

m Qs d= Stac k

ga s flow , dscf

m TOTA L FLO W O F AL L INLE T SOURCES , dsc f = 2771 8 Toolin g Booth 0.28 0 Cur e Ove nMixe r 0.33 0
_ 86.(X/ ^ 96. 0 £5'-

- 0.0 0 20.0 0 80.0 0 28.9 6 -0.0 5 28.96 " 0.9 9 

### ~28ii o



# - 

# M\ E4.306 7 28.80 " 28.57 '
J-9.2 5 497 4 455 8 0.0 0

20.0 0 80.0 0 28.9 6 0.5 6 29.0 0 " 0.9 9 12.0 0 

# !f a 0.785 4 28.8 0

. 28.6 3
22.8 6 107 7 97 6 1.15 0

91.0 * 0.0 0 20.0 0 80.0 0 28.9 6 6.4 0 29.43 ' 0.9 9 6.0 0 1. 8 0.196 4 28.8 0 28.6 1
78.7 3 92 8 85 9 Nort h Spra y Booth 0.42 0 

## y so.o^ 1 0.0 0 20.0 0 80.0 0 28.9 6 -0.4 8 28.92

- 0.9 9 34.0 0 1. 8 6.305 0 28.8 0 28.6 1
28.7 1 1086 1 1008 2 Sout h

Spra y Boot h 0.47 0
. ^ 84.0^ ( ( 0.0 0 20.0 0 80.0 0 28.9 6 -0.4 1 28.93 ' 0.9 9 34.0 0 1. 8 

## •"'iJ. 6.305 0 28.8 0 28.6 1
32.2 5 1220 0 1124 3AMERICA NSTANDARD SALE M OHI O FACILIT Y DESTRUCTIO NEFFICIENC Y TES T

Septembe r

16,199 7 \

'• •i '. < --'.>' (- 

# - .y

i •

OXIDIZE ROUTLE T FLOW S

RUNNO
. 3 GA S FLO W



# S > SYMBO LDESCRIPTIO N SQRT(d P= Averag e o f

square root s o f

pito t pressure , in
. wate r T s = Averag e stac k temperature , deg
. F C0 2 = C0 2 instac k gas , % 0 2 = 0 2 i

nstac k gas , % CO+N 2 = C O an dN 2 instac k gas , % Pbar = Barometri c pressure , in
. Hg
. P a= Stati c pressure , in
. water P s = Stac k

pressur e (absolute) , in
. Hg
. C p = Pito t

correctio nfactor , dimensionles s D s = Diameter

o f stack , in
. Bw s = Moistur e conten t ofth e ga s stream , % CALCULATE D VALUE S A s = Are aofth e stack , sq . ft. M d= Dr

y molecula

r weigh t o f stac k gas , dr y basis , Ib/lb-m o : M s = Molecula

r weigh t o f stac k gas , wet basis , lb/lb-mol e Incinerato r Outle t IO.SOOV- V 112. 0 r."'-' 

## o.o o 20.0 0 80.0 0 28.9 6 -0.0 3 •'.28796 V"
. 0.9 9 43.0 0 1-5 , „ . 10.084 7 V 28:8 0 :? ° • " -28:6 4 ~:\<3/lsP.'. 

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## 1000 

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### i-o rlecnnica i inTormano n oai i

1-800-752-159 7 

# PRODUCTS X= i

Ai r Product s andChemicals , Inc . * 1272 2 S . Wentwort hAvenue , Chicago , IL 6062 8 

## IS O CERTIFICATION : 900 2 

# CEFrriie)t!6WA ^

PERFORME D ACCORDIN G T O EP ATRACEABILIT YPROTOCO L FO R ASSA YAN D CERTIFICATIO N O F GASEOU S CALIBRATIO N STANDARD S (PROCEDUR E *G1 j Customer : APCI

- C P FREEPOR T RD , ROUT E2 8 CREIGHTO NP A 15030

- Orde r No : 148-014213-0 7 Batc hNo : 861-3811 6 PO : Release : Cylinde r No : SG9133459BA L B a r Cod e No : BXH31 3 Cylinde r

Pressure* : 200 0 psi g Certificatio nDate : 03/10/9 7 Expiratio nDate : 03/10/0 0

CERTIFIE D CONCENTRATIO N
Componen t PROPAN E Certifie d Concentratio n 84 6 ±4. 0 PP

M REFERENC E STANDARD S

Cylinde r Numbe r SG9128533BA L Standar d Typ e GHI S Standar d Concentratio n 102 7 PP M ANALYTICA L INSTRUMENTATIO N

Instrumen t Hake/Hode l Gow-Ma c75 0 Seria l Numbe r 59405 U Las t

Calibratio n 03/05/9 7 Measuremen t Principa l GC-FI 0 NITROGE N Balanc e Ga s

' ^ Note s * STANDARD SHOUL D NO T B EUSE D BELO W15 0 PSI G

Analyst : Approve d By : Richar d Fr y
(16921 ) Pub

. No

. 32Q-970 2
O )

### i-o rlecnnica i inTormauo n oa n

1-800-752-159 7 

# PRODUCTS

Ai r Product s an

d Chemicals , Inc . * 1272 2 S . Wentwort h Avenue , Chicago , I L 6062 8 

## IS O CERTIFICATION : 900 2 

# GERTIIilC^BiifflMlSiSlIl E

PERFORME D ACCORDIN

G T O EP ATRACEABILIT

Y PROTOCO L FOR ASSA

Y AN D CERTIFICATIO

NO F GASEOU S CALIBRATIO NSTANDARD S (PROCEDUR E «G1 ; Customer : APCI
- C P FREEPORT RD , ROUT E 2 8 CREIGHTO

NPA15030

- Orde r No : 148-014388-0 1 Batc h No : 861-2720 9 PO : Release : Cylinder

- No : Ba r Cod e No : Cylinde r Pressure* : Certificatio n Date : Expiratio n Date : SG9162729BAL DDP90 1 200 0 psi g 08/31/9 5 08/31/9 8

CERTIFIE D CONCENTRATIO N
Componen t PROPAN E Cert i fie d Concentra t io n £9-4 *3. 0 PP M REFERENC E STANDARD S Cylinde r Numbe r SG91?863SBA L Standar d Typ e GHI S Standar d Concentratio n 503. 9 PP

M ANALYTICA L INSTRUMENTATIO N

Instrumen t Make/Mode l Gow-M3 c75 0 Seria l Numbe r 59405 U Las t

Calibratio n CS/IS/9 5 Measuremen t Principa l G C FI O NITROGE N Balanc e Ga s

TT " * STANDARD SHOUL D NO T B E USE D BELO W 15 0 PSI G

Notes :

Analyst : Jame s Laa s Approve d 

# Bv ; 

# \LM^ %Xu^^

/Lji
Rober t HcNea r
(16921 ) Pub . No . 320-970 2P.5 8 

# | H Scot t Specialt y Gase s
614 1 EASTO N ROAD

. P O BO X 310

. PLUMSTEADVILLE

. P A18949O31 0 (215)766-886 1 FAX : (215 ) 76&O32 0 

## CERTIFICAT E O F ANALYSIS : EP APROTOCO L GAS Custome r Oplim.i l Tivhnoloftio s l m 57 5 Willia mPil l Wa y Pillsl-nirj'.h , P

A 1523 8 ANALYTICA L INFORMATIO N Assa y Laborator y Scot l Speciall y Gases , Inc.
. 614 1 Easlo n Roa d P.O
. Box EMI

) Plunislciuivillo , P A 18949-031 0 Purchas e Orde r 53251 2 Scot t Projec t #01-71905-00 1

litis certification was performed according to EPA iraccability Protocol For Assay & Certification of Caseous Calibration Standards; 1 Procedure «C7 , Section Number 3.0.4; September, 7.W.

L Cylinde r Numbe r

ALM03264 0 Certificatio nDat e 10-05-9 5 Expiratio nDat e 10-05-9 7 Cylinde r Pressur e 21XX

1 psig + Previou s Certificatio nDate s Non e ANALYZE D CYLINDE R Component s Propan e Balanc e Gas : Nitroge n Certifie dConcentratio n 24. 4 pp m Analytica l Uncertainty * ± 1 % NIS T Traceabl e

+ D o no tus e whe n cylinde ri s les s tha n 15 0 psig . •Analytica l uncertainl y i s inclusiv e o f usua l know n erro rsource s whic h a l leas tinclude s referenc e standar d erro r& precisio n o f th e measuremen tprocesses . REFERENC ESTANDAR D Typ e Expiratio nDat e SRM1667B 11-15-9 7 Cylinde r Numbe r CLMM527 8 Concentratio n 47. 3 pp mC3H « i n N 2

INSTRUMENTATIO N Instrumenl/Model/Seria l # C3H8 : Varian /

VA3300/794 5 Las t Dal e Calibrate d 10-21-9 5 Analytica l Principl e FI D

ANALYZE R READING S (Z=Zer o Ga s R=Referenc e Cas T=Tes t Ga s r=Correlatio n Coefficient ) Component s Firs t

Tria dAnalysi s Propan e Secon dTria dAnalysi s Calibratio nCurv e

Specia l Notes : Dale : 10-05-9 5 Respons e Units : Are a 7.1=00000 0 Rl=51011 8 Tl=26436 8 R2=51011 3 Z2=00000 0 T2=26405 5 Z3=00O00 0 13=26356 0 R3=51215 2 Avfj . Cone , o f

CusL Cyl . 24. 4 pp m Concentraiion: 3 r= l .0000 0 Constants : B=1.0172E-0 4 D=0.0000£+0 0 A+Bx+Cx 2 +Dx 3 +Ex 4

NTRM166 8

, A=-9.9237E-0 3 C=0.00OOE+0 0 E=0.0000£+0 0



# r-)J^ valys t Jame s T
. Krau s 

# Jl

### Fo rTechnica l Informatio n Cal l

1-800-752-159 7 

# PRODUCTS

Ai r Product s andChemicals , Inc . * 1272 2 S . dentwort hAvenue , Chicago , IL 6062 8 

## IS O CERTIFICATION : 900 2 

# liitilliMii^

^

i-ERFGRME D ACCORDIN G T O EP ATRACEABILIT YPROTOCO L FO R ASSA YAN D CERTIFICATIO N O F GASEOU S CALIBRATIO N STANDARD S ..PROCEDUR E - G 1 Customer : AI RPRODUCT S AN D CHEMICALS , INC
. 1020 2 STRAN GROA D L A PORT ET X 7757 1 Orde r No : SRP-573952-0 5 Batc hNo : 861-3596 4 PO : Release : Cylinde r No : SG9132935BA L B a r Cod e No : DDJ68 9 Cylinde r

Pressure* : 200 0 psi g Certificatio nDate : 12/04/9 6 Expiratio nDate : 12/04/9 9



### * 0 CERTIFIE D CONCENTRATIO N

Componen t PROPAN E Certifie d Concentratio n 85. 5 i0.5 6 PPM REFERENC E STANDARD S Cylinde r Numbe r SG9128479BA L Standar d Typ e GMI S Standar d Concentratio n 100. 7 PPM ANALYTICA L INSTRUMENTATIO N
Instrumen t Make/Mode l Gow-Ma c75 0 Seria l Numbe r 59405 U Las t

Calibratio n 11/12/9 6 Measuremen t Principa l GC-FI D NITROGE N Balanc e Ga s

* STANDAR

D SHOULD NO T B E USE D BELO W 15 0 PSI G
Notes :

Analyst : Approve d By : Richar dFr y

•it"!'.. " I : Pii h Mr. . 32 0 070 2 U l c oP.6 0



# SPECTR A GASE S 27 7 Col t St.
- Itvinglon

. N J 0711 1 USATel. : (201 ) 372-206 0 • (800 ) 932-062 4 • Fax : 201 ) 372-655 1 Shippe d From : 8 0 Industria l Driv e • Alpha

. N.J

. 0886 5


## CERTIFICAT E O F ANALYSI S EP A PROTOCO L MIXTUR E PROCEDUR E n:

G 1 CUSTOMER : SG I ORDE R # : ITEM # : P.O. # : Optima l Technologie s 12613 6 1 P43622 CYLINDE R # : SG91060348A L CYLINDE R PRES ; 130 0 PSI G CG A OUTLET : 35 0
CERTIFICATIO N DATE : 7/25/9 7 EXPIRATIO N DATE : 7/25/200 0 CERTIFICATIO N HISTOR Y COMPONEN T Propan e DATE O F

ASSA Y 7/25/9 7 MEA N

CONCENTRATIO N 5.03 pp m CERTIFIE D

CONCENTRATIO N 5.03 pp m ANALYTICA L

ACCURAC

Y +/-1 %

BALANC E
REFERENC E STANDARDS Nitroge n

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A CYLINDER *

SX2014 8 CONCENTRATIO N

99. 1 pp m

INSTRUMENTATIO N COMPONEN T Propan e MAKE/MODE L

H

. Packard-669 0 SERIA L #

US00001434 DETECTO R

G C - FI D CALIBRATIO N

DATE(S ) 6/26/9 7

THI S STANDAR D WA S CERTIFIE D ACCORDIN G T O TH E EP A PROTOCO L PROCEDURES . D O NO TUS E THI S STANDAR D I F TH E CYLINDE R PRESSUR E I S LES S THA N 16 0 PSIQ .
ANALYST : 

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# AI RQUALIT

Y SERVICES , INC
. 452 7 Clairto nBoulevar d Pittsburgh , P A 1523 6 (412) 881-563 0

TABL E I ANALYSI S O F SAMPLE S FO R ACETONE/METHANO L AN D METHAN E CONTEN T OPTIMA L TECHNOLOGIES , INC . 57 5 WILLIA M PIT T WA Y PITTSBURGH , P A1523 8 PURCHAS E ORDE R #1907 7 SAMPLE S RECEIVED : SEPTEMBE R 17 , 199 7

OPTIMA L SAMPL E 

## I D

========== = 

## I- l 9-16-9 7 102 5 

## 1- 2 9-16-9 7 115 5 

## 0- 1 9-16-9 7 103 5 

## 0- 2 9-16-9 7 115 4 AQ S

LABORATOR Y NUMBE R

================= =


### AQS-7643 0

AQS-7643 1

AQS-7643 2

AQS-7643 3 ACETON E PP M

—— — —=;:= : = = = = : :



### 15. 6



## 3. 1

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## 4. 6 METHANO L



## PP M

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## <0. 1

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TH E SAMPLE S WER E ANALYZE D B Y GA S CHROMATOGRAPH Y USIN G AFLAM E IONIZATIONDETECTOR .

-•4ry-7, ; 

### :; / />--Af-.ih/ r AI R QUALIT Y SERVICES , INC , JO B 576 9 REPORTED : SEPTEMBE R 23 , 199 7 

# fr 

# >P.6 7 

# blectro-Anaiytica i Grou p Environmenta

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s • Certifie d laboratorie

s
Ie$f rResult s b vSampl e iample : 01 A

Aethano tee ton e > tyren e inknowns *
•ample : 02A

tethane iceton e etrahydrofura n ityron e Inknowns * 10Q2-O3 Outlet Strea m Rejufts 2. 8 1. 8 5 3 2. 9 Reportin g

limi t 1. 0 1.0 1.0 1.0

1002-1 3 Inlet Strea m Result s 2 6 1.6 1. 1 7 8 3 2 Reportin g

Limi t 1. 0 1. 0 1.0 1.0 1. 0 Unit

s ppm a s propane pp m as propane pp m as propane pp m a s propane

Unit s pp m a s propane pp m as propane ppm a s propane pp m a s propane ppm a s propane Analyzed

9/19/9 7 9/19/6 7 9/19/9 7 9/19/9 7

Analyzed 9/19/9 7 9/19/9 7 9/19/9 7 9/19/9 7 9/19/9 7

lotdir : Eesuft s er e reported "a

s propane " ample s analyze d by GC/FID , confirmed b y GC/MS Unknow n peak s probable Identification a s Isomers o f divinylbenzen e 

# 3o/<*7 UM AJjCLA/* @ ^^iAX^C-C^^ vS^lxJ. 

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# fcOAmerica nStaiidard Inc
. "' " " ' • - K-VK-.I-.- J!•.** » U.S
. Plumbin g Product s 60 S Sou * EJIswon b Avenu e S<xler nO H 4446 0 Telephon e 21 6 332-S95 4 •J'O.l y?. , 3.95*C

>
Bruc e Weinber g Performance * Te a Liu yS«clivi i Divisio n o f Ai r PoUutio n Contro l Ohi o EP A Dea r Mr . Weinberg : I n a meetin g wit h Karol d Stiohrocy? r s t MCVAAtoday , w e discusse d d: i f ferem : option s fo r deteminii-. g captur e efficienc yfo r sever;- 1 ai r emission s source s s t thi s facility
. W vbuv ©reviewe d Method s <0 4 throug h 204 F i n U.S . EPA' s Januar y199 S Guidanc e Document . Mr . Strehnoye r suggeste d tha t w e contact : yoi i .i f we > wante d t o propo; * «• > a n alternativ e metho d fo r determinin g captur e efficiency
. Ther e ar e -

1 source s fo r whic h w* a mus t determin e a captur e efficiency
. Tw o o f thes e source s d o ho t meet th e criteri a fo r a permanen t tota l enclosur e define d byMetho d 204 . Cu e sourc e i s a PeVilbis s paint spra y boot h recentl yi. o stalle d her-,* . Thi s boot h i s a totall yenclose d tunne l excep t fo r a 4ft. b y8ft . conveyo r openin g a t eac h en d t o ^Ho vi.h a passag e o f products . Th e othe r sourc e i s a lo wtemperatur e cu;in g ove n whic h is
. als o a tunne l wit h a 4ft . b y1 -6ft . openin g a t eac h en e (se o attache d drawings)
. Wit h regar d t o th e curin g oven , 1 wa s tol d b ya consultan t tha i i t woul d no t b e necessar yt o cos " captur e efricienc yi r w e coul d sho wa r inwar d movemen t o f ai r a t eac h end . 1 woul d lik e t o verif yi f thi a i i true . Th e Deviibis s -spra yboot h wa s designe d » o achiev e 100 % captur e erriciency
. I t meet s al l ci e criteri a fo i - a fe±-M(dii««t tvlo l wxlysw e excep t fo r one . Th e natura l draf t opening s wher o th e product s ente r an d exi t ar e to o clos e t o th e VOC-smittin g ppints
. 1 o mproposin g t o cove r ch e are a betwee n th e e«-i t en d o f th e spra yboot h an d th e entrat.e e en d o t r.h e cur e over , wit h a permanen t enclosure . A t th o o n tranc e on d vC th o spra ybooth , 1 a mproposin g t o add a n automati c doo r tha t open ! whe n th e conveyo r bel t start s advancin g th « produc t int o th o boot h the n close s whe n th e conveyo r bel t stops . Thi s woul d creat e a ver ysmal l i aturu l draft op«nin< 3 -a

t Lh * -?ni.r<(rr

t o f th e hooi-h nnrin g rh< ? spra yoperation
. Wit h thes e modifications , ca n J assum e J00 % captur e cCf.ioicnc yfo r thes e tw o souccos' ? T mus t hav e thos e source s teste d b yAugus t 15 . Therefore , I mis t fil e a n Inten t t o Test for mb yJul y3 5 . J f yo u ar o available , I wo t I d lik e t o cal l yo u tomorro w(Wednesday ) t o discus s thi s proposal . Yoi
. ma y contac t m e b yphon e a t (330 ) 337-222 4 o r fa x a t (330 ) 337-2203 .



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