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# OAR Box 1413 Prepped by Ollie Stewart



## Document

Number: 

# 48 ) 11-1-4 8 Docket Number: 

# A-94-5 2

Printed 7/9/2008 3:11:22 PM

Sheet 48 of 114

## A• P. 2 

# A^fy-5-? - • 3T-2 ' V8 ,

,Incinerato r Efficienc ySampling •Fibercas t Compan

y San d Springs , O K Apri l 10 , 199 2 ; Armstrong Environmental , Inc . j Projec t W-1181-9 2

Repor t Prepare d For : Mr . LarryMoor e Fibercas t Compan

y 2 5 Sout hMai n San d Springs , O K 7406 3

Repor t Prepare d Apri l 15 , 199 2 by : i Armstrong Environmental , Inc . 474 7 Irving Blvd . #20 4 Dallas " , Texa s 7524 7 (214 ) 631-002 1P. 3



## TABL E O F CONTENT S
I . INTRODUCTIO

N Pag e 1
II . SUMMAR

Y 2 - 4
III . PROCEDURE S IV . APPENDICE S A- CALCULATIONSUMMARIE S B - STRI P CHAR T SUMMARIE S C - FIEL D DAT

ASHEET S D - STANDARD GA S CERTIFICATION S E - INCINERATOR PARAMETER S F - EQUIPMEN

T CALIBRATION S 6-1 1 1 2 - 2 0 2 1 - 2 8 2 9 - 3 2 3 3 - 3 4 3 5 - 4 0

2 _P. 4



## 1 ^ INTRODUCTIO

N Aserie s o f test s wer e performe d o n the incinerato r inle t an d exhaust , stack s a t th e Fibercas t Compan yfacilit ylocate d i n San d Spring s r



## _ OK o n Apri l 10 , 1992 . Th e purpos e o f thi s tes t serie s wa s t o determin e th e incinerato r destructio n efficiency . Th e incinerato r i s manufacture d b yAngui l EnergySystem s an d i s a Mode l 150 , seria l # CN M 067 . I t i s equippe d wit ha nicke l catalys t be d an d variabl e spee d fan . Incinerato r parameter s durin g testing ar e locate d i n the summary tables . ; •

_ ' Testing wa s conducte d following procedure s detaile d i n 40:CFR . Emission s testing wa s performe d b yLarr yWhicher , TomArmstrong , an d Da n Barrer a o f Armstron g Environmental , Inc . using tw o Beckma n Mode l 400 Ahydrocarbo n analyzer s an d a NAP P tfodel 3 1 Metho d 5 samplingitrain . Testing wa s performe d ove r a four hou r period . Submitte d by : Armstrong Environmental , Inc . Larr^yWhiche r Projec t Manage r LW/m s

. i


# 3 .P. 5



## II . SUMMARY Aserie s o f test s wer e performe d o n th e inle t an d exhaus t duct s o f the^incinerato r a t th e Fibercas t Compan yfacilit ylocate d i n San d Springs , O K o n Apri l 10 , 1992 . Sampling wa s performe d following USEP Ates t method s a s detaile d i n Titl e 40 : Cod e o f Federa l Regulation s (40:CFR) . Thre e run s wer e performe d simultaneousl yo n the inle t an d exhaust . Al l thre e run wer e on e hou r i n duratio n wit hth e exceptio n o f ru n 3 . During run thre e concentration s wer e abov e scal e o n the inle t fo r a perio d o f si x minutes . Ful l scal e concentration s wer e use d i n averaging the char t during thi s time period . (Destructio n efficiencydurin g thi s perio d wa s stil l ove r 95% ) . Result s o f the tes t serie s indicat e th e following : Run # Exhaus t Emissions , lbs/hr Inle t Emissions , lbs/hr Destructio n Efficiency , % 1 4.4 7 150.7 0 97.0 3 2

4.4 9 136.6 2 96.7 1 3

5.6 5 216.7 5 97.3 9 Avg .

4.8 7 168.2 3 97.0 4



## IP. 6



## SUMMARY O F EMISSION S TES T DAT A TABLE : 1 PLANT : .Fibercas t Company , San d Springs , O K LOCATION, : Incinerato r Inle t OPERATOR - 

## : L . Whicher , T . Armstrong , D . Barrer a TES T DATE : Apri l 10 , 199 2 REPETITION : i 1 2 INCINERATOR PARAMETER S Burne r Temperature , F Ca t Bed , Ou t Fa n Speed , % STAC K GA S Temperature , F Velocity , fp s Volum e Flow , acf m

scf m scf h Moisture , % C02 , % 02 , % SAMPL E Star t Time , hrs:mi n Finis hTime , hrs:mi n VO C a s C3H 8 Concentration , pp

m Emissions , lb/hr 67 6 75 6 3 9 78. 7 10.7 0 2745. 4 2603. 8 15622 6 1. 4 0. 0 21. 0 8:36a m 9:36a m 8486.6 2 150.7 0 67 5

76 7 3 8 78. 4 10.8 3 2779. 6 2637. 9 15827 2 1. 4 0. 0 21. 0 9:50a m 10:53a m 7593.9 2 136.6 2 67 5

81 1 • 3 5 - 87. 0 10.9 4 2806. 5 • 2624. 4 15746 3 1. 3 0. 0 21. 0 11:10a m 12:16p m 12110.3 9 216.7 5



# JP. 7



## SUMMAR Y O F EMISSION S .TEST DAT A TABLE : 2 PLANT : Fibercas t Company , San d Springs , OK LOCATION : Incinerato r Inle t <3M.TI^> T 

## TvXOPERATOR - 

## : L . Whicher , T . Armstrong , D . Barrer a TES T DATE : Apri l 10 , 199 2 REPETITION : 1 2 INCINERATOR PARAMETER S Burne r Temperature , F Ca t Bed , Ou t Fa n Speed , % STAC K GA S Temperature , F Velocity , fp s Volum e Flow , acf m

scf m scf h Moisture , % C02 , % ' . 02 , % SAMPL E Star t Time , hrs:mi n Finis hTime , hrs:mi n VO C a s C3H 8 Concentration , pp

m Emissions , lb/h r 67 6 75 6 3 9 37 6 11.6 5 5360. 5 . 3258. 1 19548 8 2. 0 0. 0 20. 0 8:36a m 9:36a m 201.1 0 4.4 7 67 5

76 7 3 8 37 5 13.3 8 6157. 3 3716. 8 22300 5 2. 8 0. 0 20. 0 9:50a m 10:53a m 177.2 1 4.4 9 67 5

81 1 - 3 5 - 37 0 1.1.7 8 5422. 2 ' 3299. 5 19796 8 2. 6 0. 0 20. 0 11:10a m 12:16p m 250.9 9 5.6 5P. 8



## III . PROCEDURE S Th e procedur e fo r emission s sampling followe d USEP Ates t method s a s detaile d i n Titl e 40 : Cod e o f Federa l Regulations . Th e followin g method s wer e used : Metho d Titl e > 1 Sampl e an

d Velocit yTraverse s fo r StationarySource s 2 Determinatio n o f Stac k Ga s Velocit yan d Volumetri c Flow 3 Ga s Analysi s fo r C02 , 02 , Exces s Ai r an d Dry'Molecula r Weigh t \ 

## 4 Determinatio n o f Moistur e Conten t i n Stac k Gase s 25 ADeterminatio n o f Tota l Gaseou s Organi c Concentratio n

Using a Flame Ionizatio n Analyze r C0 2 an d 0 2 wer e determine d using Fyrit e analyzers . Velocit ytravere s wer e performe d a t 1 6 points , 1 2 point s pe r travers e o n bot hth e inle t an d the exhaust . Th e traverse s wer e don e during the run wit ha standard pitot . Moistur e o n the exhaus t wa s determine d b ypulling a know

n amoun t o f stac k ga s throughth e bac k hal f o f a Metho d 5 sampling train . Th e firs t an

d second impinge r containe d 10 0 mi s o f H20 , the thir d wa s empty , an

d the fourt himpinge r containe d 20 0 gram s o f silic a gel . Moistur e o n th e inle t wa s determine d using we t bulb/drybul b calulations . Th e concentration s o n th e incinerato r exhaus t an d inle t wer e take n using two Beckman Mode l 400 AContinuou s FI D analyzers . Th e analyze r o n the inle t wa s spanne d wit h999 2 ppm , 988.4 , an d 202. 7 ppmpropan e i n nitroge n standards.Th e exhaus t analyze r wa s spanne d wit h988. 4 ppm , 202. 7 ppm , an d 27. 2 ppmpropan e i n nitroge n ga s standards . Tedla r ga s bag s wer e use d t o span th e analyzer s fro

mth e en

d o f the teflo n sampl e line .P. 9

APPENDIX A

•« ••7,;;-;,77
. :,.,.,_

_v 

# tfP.1 0



## Fibercas t Incinerato r Repetitio n # 1 4/10/9 2 MOLECULA

R WEIGHT-O F STAC K GAS , DRY BASIS , M D (.4 4 * %C02 ) + (.3 2 * % 02 ) + (.2 8 * (N2 + CO) ) = 28.8 4 MOLECULA

R WEIGH T O F STAC K GAS , WE T BASIS , M S MD * ( 1 - BWS ) + (1 8 * BWS ) = 28.6882 4 STACK GA S PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.362 5 ; 

## STACK GA S VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (P S * MS)) ) = 10.7005 8 VOLUM E FLOW RATE , ACF M 6 0 * A S * V S = 2745.40 6 VOLUM E FLOW RATE , SCF H 360 0 * ( 1 - BWS ) * V S * A S * ((52 8 * PBAR ) / (T S * 29.92) ) = 156225. 9 %C0 2 = 0 %0 2 = 2 1 %C O = 0 %N 2 = 7 9 STACK TEMPERATURE , F = 78. 7 SQUAR E ROO T O F DELT AP = .158 1 STATI C PRESSURE , I NH2 0 = -.5 1 BAROMETRI C PRESSURE , I NHG = 29. 4 PERCEN T WATE R VAPOR (BW

S * 100 ) = 1. 4 ARE AO F STACK , SQUAR E FT . = 4.276 1 PITO T CO-EFFICIENT , C P = .9 9



# 1

## Fibercas t Incinerato r Inle t Repetitio n # 2 4/10/9 2 MOLECULA

R WEIGHT " O F STACK GAS , DRY BASIS , M D (.4 4 * %C02 ) + (.3 2 * % 02 ) + (.2 8 * (N2 + CO) ) = MOLECULA

R WEIGH T O F STACK GAS , WE T BASIS , M S M D * ( 1 - BWS ) + (1 8 * BWS ) = 28.6882 4 STAC K GA S PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.3647 1 STAC K GA S VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (PS * MS)) ) = 10.8338 8 VOLUM E FLOW RATE , ACFM 6 0 * A S * V S = 2779.60 4 VOLUM E FLOW RATE , SCFH 360 0 * ( 1 - BWS ) * V S * A S * ((52 8 * PBAR ) / (TS * %C0 2 = 0 %0 2 = 2 1 %C O = 0 %N 2 = 7 9 STAC K TEMPERATURE , F = 78. 4 SQUAR E ROO T O F DELT AP = .1601 2 STATI C PRESSURE , I NH2 0 = -.4 8 BAROMETRI C PRESSURE , I NHG = 29. 4 PERCENT WATE R VAPOR (BW S * 100 ) = 1. 4 ARE AO F STACK , SQUARE FT . = 4.276 1 PITO T CO-EFFICIENT , C P = .9 9

V . - 1


## 7 28.8 4

29.92) ) =

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## 15827 2

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# . 0 P.1 1

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## Fibercas t Incinerato r Inle t Repetitio n # 3 4/10/9 2 MOLECULA

R WEIGH T O F STAC K GAS , DRY BASIS , M D (.44 * %C02 ) + (.3 2 * % 02 ) + (.2 8 * (N2 + CO) ) = 28.8 4 MOLECULA

R WEIGH T O F STAC K GAS , WE T BASIS , M S M D * ( 1 - BWS ) + (1 8 * BWS ) = 28.6990 8 STAC K GA S PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.3669 1 STAC K GAS VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (P S * MS)) ) = 10.9387 2 VOLUM E FLOW RATE , ACFM 6 0 * A S * V S = 2806.50 5 VOLUM E FLOW RATE , SCF H 360 0 * ( 1 - BWS ) * V S * A S * ((52 8 * PBAR ) / (TS * 29.92) ) = 157462. 6 %C0 2 = 0 %0 2 = 2 1 %C O = 0 %N 2 = 7 9 STAC K TEMPERATURE , F = 8 7 SQUAR E ROO T O F DELT AP = .1604 3 STATI C PRESSURE , I NH2 0 = -.4 5 BAROMETRI C PRESSURE , I NH G = 29. 4 PERCENT WATE R VAPOR (BWS * 100 ) = 1. 3 ARE AO F STACK , SQUAR E FT . = 4.276 1 PITO T CO-EFFICIENT , C P = .9 9



# IfP.1 3



## Fibercas t Incinerato r Exhaus t i Repetitio n # 1 ' 4/10/9 2 •__

. | MOLECULA

R WEIGHT~ O F STAC K GAS , DRY BASIS , MD (.4 4 * %C02 ) + (.3 2 * ! % 02 ) + (.2 8 * (N 2 + CO ) ) = 28. 8 i 

## MOLECULA

R WEIGH T O F STACK GAS , WE T BASIS , M S MD * ( 1 - BWS ) + (1 8 * BWS ) = 28.5829 2 i 

## STACK GA S PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.3985 3 STACK GA S VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (PS * MS)) ) = 11.6483 2

i 

## VOLUM E FLOW RATE , ACF M 6 0 * A S * V S = 5360.48 5 VOLUM E FLOW RATE , SCF H 360 0 * ( 1 - BWS ) * VS; * A S * ((52 8 * PBAR ) / (TS * 29.92) ) = 195488. 4 %C0 2 = 0 %0 2 = 2 0 %C O = 0 j %N 2 = 8 0 , STACK TEMPERATURE , F = 376. 4 SQUAR E ROO T O F DELT AP = .1379 5 STATI C PRESSURE , I NH2 0 = -.0 2 BAROMETRI C PRESSURE , I NH G = 29. 4 PERCEN T WATE R VAPOR (BW

S * 100 ) = 2.0 1 ARE AO F STACK , SQUAREiFT . = .7.669 9 PITO T CO-EFFICIENT , C P = .9 9



# /2 -P. M



## Fibercas t Incinerato r Exhaus t Repetitio n # 2 4/10/9 2 MOLECULA

R WEIGH T O F STAC K GAS , DR Y BASIS , M D (.4 4 * %C02 ) + (.3 2 * % 02 ) + (.2 8 * (N2 + CO) ) = 28. 8 MOLECULA

R WEIGH T O F STAC K GAS , WE T BASIS , M S MD * ( 1 - BWS ) + (1 8 * BWS ) = 28.4965 2 STACK GA S PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.3981 6 STACK GAS VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (PS * MS)) ) = 13.3798 6 VOLUM E FLOW RATE , ACFM 6 0 * A S * V S = 6157.33 1 VOLUM E FLOW RATE , SCF H 360 0 * ( 1 - BWS ) * V S * A S * ((52 8 * PBAR ) / (TS * 29.92) ) = 223005. 4 %C0 2 = 0 %0 2 = 2 0 %C O = 0 %N 2 = 8 0 STACK TEMPERATURE , F = 375. 3 SQUARE ROO T O F DELT AP = .1583 2 STATI C PRESSURE , I NH2 0 = -.02 5 BAROMETRI C PRESSURE , I NH G = 29. 4 PERCEN T WATE R VAPOR (BW

S * 100 ) = 2.8 1 ARE AO F STACK , SQUAR E FT . = 7.669 9 PITO T CO-EFFICIENT , C P = .9 9

1 0 

# / 3P.1 5



## Fibercas t Incinerato r Exhaus t Repetitio n # 3 4/10/9 2 MOLECULA

R WEIGHT " O F STACK GAS , DRY BASIS , M D {.44 *%C02 ) + (.3 2 * % 02 ) + (.2 8 * (N2 + CO) ) = 28. 8 MOLECULA

R WEIGH T O F STACK GAS , WE T BASIS , M S MD * ( 1 - BWS ) + (1 8 * BWS ) = 28.5181 2 STACK GAS PRESSURE , I NHG , P S PBA R + (STATIC/13.6 ) = 29.3977 9 '- STACK GAS VELOCITY , FP S 85.4 9 * C P * (SQ

R P(T S / (PS * MS)) ) = 11.7824 9 VOLUM E FLOW RATE , ACF M 6 0 * AS * V S = 5422,22 9 VOLUM E FLOW RATE , SCF H 360 0 * ( 1 - BWS ) * V S * A S * ({52 8 * PBAR ) / (TS * 29.92) ) = 197968. 2 %C0 2 = 0 %0 2 = 2 0 %C O = 0 %N 2 = 8 0 STACK TEMPERATURE , F = 370. 3 SQUAR E ROO T O F DELTAP = .1398 9 STATI C PRESSURE , I NH2 0 = -.0 3 V ; BAROMETRI C PRESSURE , I NHG = 29. 4 PERCEN T WATE R VAPOR (BW

S * 100 ) = 2.6 1 ARE AO F STACK , SQUAR E FT . = 7.669 9 PITO T CO-EFFICIENT , C P = .9 9

1 1 

# IHP.1 6

APPENDI

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# / 5P.1 7



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# Scot t Specialt yGase s a divisio n o f Scot tEnvironmenta l Technology , Inc . 120 0 COMBERMER E STREET . TROY , MICHIGA N 4808 4 (313 ) 680-205 0 luitoie rt ARHSTRON B ENVIROMENTA L TO HARKSTRON B 474 7 IRVIN GBLV D SUIT E 20 4 DALLAS , TI . 7524 7 • I " 

### til t CERTIFICAT E OF ANALYSI S - EPA PROTOCO L GASE S ttt t PERFORMEDACC0RDIN 6 TOSECTION 3.0. 4 Certifie dPe r Traceability Procedur e I 6 1 Protoco l I 1 Fil e I P0405 B Certifie dAccuracy

1 XNB S Traceabl e Shippe dFro a l Scot t Tro y Ou r Projec t I I 52072 2 You r P.O . I i 100 2 ExpirationDat e i 9-14-9 2 Cylinde r Huebe r ALH-00437 4 Cylinde r Preiiur e 190 0 psi g 

# 6 )

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: • . » GHIS t BALANC E 6A S l NITROGEN I 

## tmiftfmttttittmmttmttttuttttttttt CYLINDE R NUNBER CONC . H^ODE&SERlA g BECl(fi?N/400/lo0205 9

ZERO 6AS dV ) 0.0 0 0.0 0 0.0 0 ANALYSIS

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### 9 i

,' REFERENC E REFERENC E RESULT S ! PP N ! 6A S CONC . GA S

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H 96.4 0 96.4 0 96.4 0 RESULT S

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th U Compan y fo rf

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### ANALYTICAL PRINCIPL E FLAN E IONIZATION

DETECTOR•



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CALIBRATION

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# ---. CERTIFICATION ANALYSI S * T



# _"EP A PROTOCO L #1 " OR0ER # 192090 7 CYLINDE RNUMBERS : CC-10076 4 ' CERTIFIE DCONCENTRATION : 202. 7 PPM PROPANE BALANC E GAS : . - NITROGEN

^ CYLINDE RPRESSURE : 201 5 PS I DAT E O F CERTIFICATION : FEBRUARY3 , 19S 2 CERTIFICATION

EXPIRATION : AUGUS T 3 . 199 3 SR M INFORMATION : SR M NUMBERCYL . NUMBE RCONCENTRATION 26.44 CAL-310 9 244. 2 PP M C3H8/N 2 THIS.ASSAY/CERTIFICATION WA S PERFORME DACCORDIN GT O SECTION - 3.0.4* .

B YMICHAE L SICKMILLER . QUALIT YCONTRO L SUPERVISOR INSTRUMENT S USED : TOTAL HYDROCARBON : HORIBA 0PE-4O5XB0R 0 ANALYTICAL TOTAL HYDROCARBON SERIAL # 850U9011 0 CALIBRATION

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# EPA40 8 - <32^^yS ^ MICHAE L SICKMILLER" ^ QUALIT YCONTRO L SUPERVISOR

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APPENDIX F



# */ 3P.4 5



### SUMMARY-QE-ERE,METER_.BQX-CALIBRA1IQM_ . METE RBO X NUMBER

: 2 CALIBRATIO

N DATE:4/3/9 2 CALIBRATE

D BY:Larr y Whiche r BAROMETRIC.PRESSURE : 29. 8

********************************************** * * * 

## * DELT

AH = ORFIC E PRESSURE * * V

W = VOLUME O F WE T GA S METE R * * T W = AVERAGE D TEMPERATUR E O F WE T METE R * * . V

D = VOLUM E O F DRY GA S METE R * * T D = AVERAGE D TEMPERATUR E O F DR Y GA S METE R * * TIM E = DURATIONO F EAC H POIN T RU N* * * ****************************************************** * 

## POIN T 1 DELT AH = . 5 VW = 5 TW = 58. 5 V D = 5.31 6 TD = 6 5 TIM E = 11. 7 TES T METE R Y = METE R BO X Y = .941662 7 METE R BO X H = 1.49136 1 

## .9 9
POIN T 2 DELT AH = 1 VW = 5 TW = 58. 8 V D = 5.29 9 TD = 6 7 TIM E = 8.9 3 METE R BOX Y = .947523 8 METE R BO X H = 1.73298 7 TES T METE R Y = .99 1
POIN T 3 DELT AH = 1. 5 VW = 1 0 TW = 6 1 V D = 10.74 1 TD = '78. 8 TIM E = 14.4 1 METE R BO X Y = .951595 5 METE R BO X H = 1.66920 7 TES T METE R Y = .99 2
POIN T 4 DELT AH = 2 VW = 1 0 TW = 6 2 V D = 10.74 4 T D = 8 1 TIM E = 12.8 3 TES T METE R Y = METE R BO X Y =.952213 9 METE R BO X H = 1.76388 4 .99 2
POIN T 5 . DELT AH = 3 VW = 1 0 TW = 62. 3 V D = 10.64 8 T D = 82. 3 TIM E = 10.5 8 METE R BO X Y = .962132 8 METE R BO X H = 1.7969 5 TES T METE R Y = .99 4
POIN T 6 DELT AH = 4 VW = 1 0 TW = 62. 8 V D = 10.59 7 TD = 83. 5 TIM E = 9.0 3 TES T METE R Y METE R BO X Y = .966582 3 METE R BO X H = 1.74481 8 = .99 5

AVERAG E Y = .953618 5 AVERAG E H = 1.69986 8 

## 3 5 

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## POIN T 1 DELT AH = 1 V

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POINT 2 DELT AH = 1 V

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AVERAG E Y = .960406 6 AVERAG E H= 1.69709 1

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