AP42 chapter 9 reference - US EPA · The file name refers to the reference number, the A P42...

AP-42 Section Number: 9.10.1.2

Reference Number: 12

Title: EPA Method 5 Particulate Emissions Tests Conducted on Western Sugar's Boiler and Pulp Dryer Stacks Located in Billings, Montana

American Environmental Testing Company, Inc.

American Environmental Testing Company, Inc.

January 1990

EPA

Text Box

Note: This is a reference cited in AP 42, Compilation of Air Pollutant Emission Factors, Volume I Stationary Point and Area Sources. AP42 is located on the EPA web site at www.epa.gov/ttn/chief/ap42/ The file name refers to the reference number, the AP42 chapter and section. The file name "ref02_c01s02.pdf" would mean the reference is from AP42 chapter 1 section 2. The reference may be from a previous version of the section and no longer cited. The primary source should always be checked.

r

AP-42 Section Reference Lk. Report Sect - Reference -

"EPA METHOD 5 PARTICULATE EMISSIONS TESTS CONDUCTED

ON WESTERN SUGAR'S B O I L E R AND PULP DRYER

STACKS LOCATED I N B I L L I N G S , MONTANA"

'EPA METHOD 5 PARTlCULATE EMISSIONS TESTS CONDUCTED

ON WESTERN SUGARS BOILER AND PULP DRYER

STACKS LOCATED IN BILLINGS

MONTANA- [:

PreDared for : Mr. Randy A Mielk, Regional Engimer

Westen Sugar Company P. 0. BOX 3aan Sdhgs,Matma 59107

I:;.,. 1::

: V. Brent Banson. Technical Director

American Eniviimentd Testing, 1% 5135 soum ~irch rive

I i Spanish Fal( Utah 84880 I

V.Bmnt BauM

r' CERTIFI CATION OF REPORT INELWE

AMERICAN ENVIAONMENTALTESTING COMPANY, INC. (AET) arciff.r (htWUY@ffWtW

I made to obtain accurate and RpRsentarive data Whin Um guidelines est&bhOd by the Utah BUnraU of

Air Quality and the U. S. Environmental Protedon Agency tor Memod 5 pnfUcuU Emispionq 8s set fcflh

in the Federal RegisW and the "Ouality Assummx Handbook *Air FWlution Measummnt Syalsmr'.

I

ti [, V. Bmnt Bents,

T e d n i c s l D i

1- . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . y a m m y . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

Table I -Emi i - summery . . . . . . . . . . . . . u. ............................

A

A PhntOpedngRocaduras.. . . . . . . . . . . . . . . . . .. . 1.RJpDI)erBBoiler . . . . . . . . . . . . . . . . . . . . . . . . .

e. Emiopiw T e s t i n g . . . . . . . . . . . . . . . . . . . . . . . . . . .

1. W p D . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

a FgweI-StdcD@rarn . . . . . . . . . . . . . . . . . . . b. T a b l e I I - T ~ p o i n t s . . . . . . . . . . . . . . . . . . .

2 m k r . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

a FtgweU-StedtD@am . . . . . . . . . . . . . . . . . . . . b. TablaM-TMpOintP ...................

N. m r d C . . . . . . . . . . . . . . . . . . . . . . . . . . . . A Pulp- ..................................

1. TablelVFMandLebaabryaatS . . . . . . . . . . . . . . . 2 TebleVWSUmmrry ......................

e. Bdler . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1. TableVlFeHandhbomt~yDS$ . . . . . . . . . . . . . . . . 2 TablevuDElnsumrmuy ......................

PaoeS

1

1

2

1

1

1

1

1

3

4

1

5

6

r r 8&9

10811

r 12

13

'EPA MEMOD 5 PARnCUlATE EMlSSlONS TESTS CONDUCTED

ON WESERN SUGARS BOlm AND PULP DFWER

STACKS LOCATED IN BllllNGS

MONTANA'

.. . .

I . 1rnrmnrCmm:

At the request of Western Sugar Companfs Randy Mielk Amerioan U w i r o n m Testing,

Inc.. (AET) Conducted €PA Method 5 Particulate E m i r Teptr QI mS W k and pulp Dlyer S W S .

The testing was accomplished at meir plant si@ located in Billings, Monmnn Tha llesb w~lle CcnduUed

on JanUary 2324 8 25 1980.

11. s u m ; The results of the part~culala emissions compliance tests for the Boiler and Pulp Dryer S M are

summarired In Table 1.

111. PRoGFD URESAWD Y m

A GmetalplentOpera(1ons:

Flgure I d e p b me Pulp D~)~Stadcr. Figure 0 daplctsllm Bdkr SDack mducaondamb

included in Appendix "D" lor the days when emissiom compliance teata wen3 conductad on the 8~lrcea

8. EmissionsTestlng:

All of me ksts procedures emploved were BS spedlled in 40 CFR 80.424 (7-1-85 and a8 m & d )

and in the EPA's "Ouality Assurance Handbook tor Air Pollutlon Measurement SystenW.

-1-

i..

Test No

I . South

2. North

3. South

4. North

5. South

6. North

Average =

Test No ! , :

2. '*

3. .'

Average = I I

Table I Particulate Summary

Pulp D r y e r

Particulate Volume Emissions Rate Collect ed (ma) D S t F i b s / h r a r a i n s / D S t F

33.7 62.98 1.4884 0.0083

49.2 -2.25250.0125

50.2 62.95 2.3505-

53.9 64.662.4203 0.0129

85.2 60.29 3.7197 0.02 18

63.6 59.0 1 2.79030.0166

67.57 61.32 2.9768 0.0171

Boiler

Particulate Volume Emissions Rate Collected (ma) DSCF Ibs/h r. arains/DSCF

270.5 53.42 66.5697 0.0781

265.5 51.18 66.1 117 0,080 1

276.8 52.05 68.8066 0.082 1

270.93 52.2267.1627o.0801

-2-

1 of 3 WEE1 NO 1 CALCUUIEDOV VB D i l l 1- 25-90 Spanish For* Utah 84860

(801) 266-71 11

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TRAVEKSE POINT CALCULATIONS

P l a n t Western Surrar Co. ~

Date 1 - 2 2 - 9 0 Sampling locat ion West Dryer ( N E S I Inside of far wall to outside

of port (d is tance , X ) 8 1 . 2 5 ' Inside of near wal l t o outaide

of port (distance, Y) 3 . 2 5 ' Stack 1.tD. 7 8 . 0 " = 3 3 . 1 8 3 ft 2 xs

I I I I-

schematic of sampling location

distance ., 3 . 2 5

traverse point location from outside of ports. (sum of columns 4 6 5 )

4 . 0 0 8 = 4 7 /0"

0 . 4 7 6 = 0 l / 2 1 1 . 2 . 4 5 4 = 1 2 1/21!

. 7 . 0 5 6 = 17 1 /8" ! 2 . 7 5 0 = 22 3 /4"

01 8 - - 7, I,

i 3 . 4 8 4 = 53 1 / 2 "

~1 750 3 / 4 1 , - - i 7 . 4 4 4 = 67 1 / 2 1 046 - - 72"

' 6 . 0 2 4 = 76" ' 9 . 6 0 2 = 79 5 /0"

-5- 112 inch rule for = 24 inch I . D . stacks. 1 . 0 inch rule for = 24 inch I.C. stacks.

Y I

I- C' I i ! t .

I

I I, I'

1

I

I i

1; ...

! I ~

, .

. .

TRAVERSE POINT CALCULATIONS

p l a n t Western S u g a r Company

Date 1 - 2 5 - 9 0 Sampling location B i l l i n g s . Montana Inside of far wall to outside

of port (distance, X ) 11' 7 1 /4"

Inside of near wall t o outside

of port (distance, Y) 2 1 .4"

Stack 1.aD. 1 1 ' 5 " = 102.4 f t . 2

traverse

I

stack 'I.D. inches

137.0 ' '

11

1 .

product of co l . 2 d 3 ( t o i t a i n )

2.877

9 .179

16.166 24.249 35.250

48.772 88.728

u2.751 L20.834 L27.821 134.123

1/2 inch rule for = 24 inch I .D. stacks. NA 1 . 0 inch rule for = 24 inch I . C . s tacks. NA

1 I I I.

acheamtic of eampling . location

traverse point location

Y I (sum of columnti 4 6.5) I

- 6 -

AHERICAN ENVIRONtlENTAL TESTING. INCORPOrUTED

Spanish Fork, Utah 84660 565 So. Birch Drive 80 1-266-7 1 1 1

FIELD AND LAB ORATORY DATA TABLEiVa

--_ Plant o r Job Descriotio n - I v D e : m e E P A ' 5

Western Suaa rComoanv - L&d In Billinas. Y ~ I M i 1 I Date 1123-24190

Svmbol Descriation Units 1 south mm Vm

Pb AH

Tm

Y i v w

c02 02

N2 + CO Rn TS

Sqr rt AP

CP

PS

Pabs AS

Tt

R I P

Volume dry gas sampled e meter

conditions Barometric Pre:

Average Pres drop across the orifice meter Average gas meter temp

Meter Coefficient Total H20

collected. impingers h silica gel

Nozzle Dia. Stack Temp

Velocity head of stack gas Pitot Tube Coefficient Static Pres

Absolute Pres Area stack

Net time o f test Total

Particulate

F t 3

'Hg abs "20

'R 'F

ml

x x x in. 'R 'F "20

"20 -H9 Ft2 min.

mg

66.554

26.38 3.8189

536.7 1 76.71 1.07 268

2.6 10.8 86.6

0.5037 582.58 122.58 0.242

0.8484

0.03 26.38 33.183

72

33.7

64.264

26.42 3.57

535.38 75.38 1.07 249

2.4 10.93 86.67 0.5037 584.54 124.54 0.2413

0.8484

0.03 26.42 33.183 72

49.2

65.52

26.79 3.770 I

53 1.58 71.58 1.07

229.1

2.73 1 1.2

86.07 0.503 589.42 129.42 0.2509

0.8484

0.03 26.79 33.183 M ... . . ,

50.2

i -8-

AHERICAN ENVIRONMENTAL TESTING. INCORPORATED


FIELD A ND LABORATORY DATA A B L E IVb

Plant or Job Descriotion : Wet Scrubber On Pulo Drver Jvoe : Complizlace EPA ''5 Date : 1/23-24/90

Western Suaar Comoanv - LoC -inBillinas. Mo ntana

Svmb 01 DescriDtion Units Am- Ft3 67.27 62.806 6 1 5123 Vm

Pb AH

Tm

Yi v w

c02 02

N2 + CO Rn Ts

Sqr rt AP

CP

Ps Pabs As Tt

MgP

Volume dry gas sampled 8 meter

conditions Barometric Prec

Average Pres drop across the

orifice meter Average gas meter temp

Meter Coefficient Total H20

collected, impingers h slllca gel

'Hg abs "20

26.79 3.9678

26.79 3.4535

26.78 3.3218

I I

t. I

533.33 73.33 1.07 295.1

'R 'F

534.42 74.42 1.07 271.2

536.9 76.9 1.07 302.2 ml

x x x in. 'R 'F "20

1.96 12.13 05.91 0.503 597.29 1 37.29 0.253 1

2.2 12.1 85.7 0.503 595.5 135.5 0.2354

2.37 11.87 85.76 0.503 605.7 1 145.7 1 0.2335


Velocity head o f stack gas Pitot Tube Coefficient Static Pres


Net time o f test Total

Particulate

0.8484 0.8484 0.8484

0.03 26.79 33.183 72

0.03 26.78 33.183 72

"20 'Hg

F t 2 min.

0.03 26.79 33.183 72

53.9 85.2 63.6

!

-9-

AHERICAN ENVlRONflENTAL TESTING. INCORPORATED 565 So. Birch Drive 80 1-266-7 1 1 1

Spanish Fork, Utah 84660

DATASUNNARY n

Plant : Wet Scrub ber On PluD Drver h e : C o n - d h f e E P A *5 Date : 1/23-24/90

Western Sugar Co mDanv - Locate m. tlonta na

SYMBOL Vm std Volume dry gas dscfm 0.8747 0.8453 0.8742

sampled @ standard dscf 62.9784 60.86 1 62.945 1

Vw gas

Bws

Md

MS

v s

os

I so

cs

Emr

Conditions Volume water

vapor collected 0 standard conditions

Proportion by volume of water

vapor in gas stream ddirnensionless Dry molecular

weight Wet molecular

weight Stack gas velocity

Volumetric flow rate dry basis

standard conditions lsokinetic variation

Conc. particulab matter in stack gas. d ry basis Emission rate

scf

Ib/lb mole

Ib/lb mole

fVsec

f W h r

x

Ib/scf

lbs/dscf

gr/dscf Ibs/hr

12.6148

0.1669

28.848

27.0377

15.8635

1.2617 X 106

99,3405

5.35 1 X 1 0 4

1.1797 x 10-6 0.0083 1.4884

1 1.7204

0.1615

28.82 12

27.0738

15.818

1.2639 X 106

95.7276

8.084 X 1 0 4

1.7822 x 10-6 0.0125 2.2525

10.7837

0.1463

28.8848

27.2928

16.341 2

1.3369 X 106

94.4232

7.9752 X 1 0 4

1.7582 x 10-6 0.0123 2.3505

-10-

AIlERlCAN ENVlRONIlENTAL TESTING. INCORPORATED

Spanlsh Fork, Utah 84660 565 So. Birch Drive 80 1-266-7 1 1 1

DATA SUMMARY n

Plant : Wet Scrubber On P I U D Drver Tvoe : CpmnlianceEPA ' 5 Date 1/23-24/90

Western Suaar Cornoanv - LGcaLed In 3 illinos. f l ~ t z z I 1 I _ 1

Vm std Volume dry gas dscfm sampled @ standard dscf

Vw gas

Bws

Md

ms

v s

as

150

c s

Ernr


vapor collected 0

standard conditions Proportion by

volume of water vapor in gas stream

ddirnensionless Dry molecular



Volumetrlc flow rate d ry basis


Conc. particulab matter in stack gas, dry basis Emission rate

scf

Ib/lb mole

lb/lb mole

rusec

ft3/hr

x

Ib/scf

Ibs/dscf

gr/dscf Ibs/hr

-1 1-

0.898 1 64.66 1

12.7654

0.1649

28.7988

27.0184

16.6776

1.317 X 106

98.0207

0.3358 X 10-4

1 .e377 x 10-6 0.0129 2.4203

0.8373 60.2859

14.2246

0.1909

28.836

26.7673

15.5576

1.1939 X 106

100.634

1.4133 X 10-3

3.1 157 x 10-6 0.0218 3.7197

0.8196 59.01 14

13.8904

0.1905

28.854

26.7859

15.5646

1.1744 X 106

100.5Oll

1 .On8 X 10-3

2.376 x 10-6 0.0166 2.7903

AMERICAN ENVIRONMENTAL TESTING. INCORPORATED


FIELD AND LABORATORY DATA TABLE VI I

i I

Plant o r Job Descriution Wet Scrubber On Boiler JvDe. -e EPA +5 Date 1/25/90

Western Susar Companv - Located In Billinas. Montana

Svmboi DescrlDtlon Units 4 North m- I

i I

I i

I I

I' !

Vm Volume d r y gas mmpled @ meter

conditions Pb Barometric Prer AH Average Pres

drop across the orifice meter

Tm Average gas meter temp

Yi Meter Coeificient v w Total H20

collected, impingers

co2 02

N2 + CO Rn

L I I Ts

Sqr rt AP

CP I... i

.. Pabs

AS I Tt

I ' m? !.

h silica gel


Velocity head of stack gas Pitot Tube Coafficient Static Pres


Net time (4 test Total

Particulate

F t3

"Ha abs -H20

'R 'F

ml

5: x x in. 'R 'F

"H20

"H20 "9 Ft2 min.

my

56.127

26.61 2.7659

531.94 71.94 1.07

252.6

5.2 10.6 84.2 0.375 570.08 110.08 0.373

0.8484

0.18 26.62 102.4

72

270.5

54.058

26.49 2.5042

536.77 76.77 1.07

257.9

6.8 I O

83.2 0.375 572.04 I 12.04 0.368

o . a m

0.18 26.50 102.4 72

265.5

55.166

26.39 2.597

536.4 76.4 1.07

263.1

7.17 10.13 82.7 0.375 569.96 109.96 0.374 1

0.8484

0.18 26.40 102.4 72

276.8

-12-

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i..:

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AMERICAN ENVIRONMENTAL TESTING. INCORPORATED

Spanish Fork, Utah 84660 565 So. Birch Drive 801-266-71 11

DATA SUMWA RY L A t L U l L

Plant ' Wet Scrubber On Bo i ler J V D ~ : Co-eEPA "5 Date ' 1/25/90

Western Suaar ComDanv - Located In Billinas. EOfitXIZ

SYMBOL DESCRlPTlON UNITS 4 North 5 South 6 North Vm std Volume dry gas

sampled @ standard

Vw gas

BWS

Md

MS

vs

Qs

Is0

CS

Emr


vapor collected B standard conditions

Proportion by volume of water

vapor in gas stream ddimensionless Dry molecular



Volumetric flow rate d ry basis


Conc. particulatl matter in stack gas, dry basis Emission rate

dscfm dscf

scf

Ib/lb mole

Ib/lb mole

fWsec

ft3/hr

x

Ib/scf

Ibs/dscf

grldscf Ibslhr

0.7419 53.4156

1 1 .8899

0.1821

29.256

27.2067

24.003

5.9628 X 106

99.6568

5.0641 X 10-3

1.1 164 x 10-5 0.078 1 66.5697

0.7108 51.1794

12.1394

0.1917

29.488

27.2855

23.7358

5.7807 X 106

97.776 1

5.1876 X 10-3

1.1437 X 10-5 0.080 1 66.1 117

0.7229 52.049

12.3841

0.1922

29.5524

27.33 19

24.1 139

5.8685 X 106

98.0007

5.3184 X 10-3

1.1725

0.0821 68.8066

X 10-5

-13-

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APPENDIX A (caliibration Data)

I

!

i- I .

~

I

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I

Referenc, Point

Tempera turc Source

I4

' I

Rc ference Thermometer Temperature

/w 2 6 3

' f 5 b

Thermocouple Temperature D e V . %

565 South. Birch Dr. . .

Spanish Fork, Utah 84660

801/266-7111

!

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0.01)

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r c. I .

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1. .

, : \'-

I I

I .

BALANCE NAXE Sartorius-A 200 S ( A n a l y t i c ) NUMBER 35120053

BALANCE NAME S a r t o r i u s U 3'600 (Top Loader) NklEE!! 35120087

CLASSIFICATION OF STANDARD :JEIGHTS T y n e "S" N.B.S .

DATE

4/1-86

4/1-87

1/7-80

8/5-88

2/24-89

? / I - 0

4/1-86

4/1-87

1/7-88

8/5-88

2/24-89

0 .500g

R 200 s 0.50!31

0.5000

0.5000

a 5 0 0 1

0 . so00 0.5001

J3600

0.5

as as a 5

0.5 0.5

1 f oooog

3.9999

L.0000

L.0001

L. 0000

1.9999 D. 9999

1 . 0

1 . 0

1.1

1 . 0

1 . 0 /. 0

10.0

10 .0

10.0

1 0 . 1

1 0 . 1

10. i,

1o.oooog

L O . 0001

L O . 0001

L O . 0000

LO. 0001

.o .0001

q.9q99

50.OOQ!lq

50.0001

49.9999

50.0000

49.9999

50 -0001 Co .oo a o

50 .0 '

49.3

50.0

50.0

49.9

49. 9

100. ooooq

100.0001

100.0001

100.0000

100.0001

100.0000 moa 0 0 0 I

100.0

100.1

100.0

100.0

LOO .1 /oo. I

ANALYST

V.B.B.

V.B.B.

V.B.B.

V.B.B.

3.

V.B.B.

V.B.B.

V.B.B.

V.B.B.

I

1- r I , ..

I

i .I:.

1 i .

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Source" (specify)

STACK TEMPERATURE SENSOR CALIBRATION SATA FOX! * f Thermocouple # I 6 &r!

U C Barometric Pressure t ~ : I j in. Hg

Calibrator: Paference : mercury-ia-glaae a z . 7 ~ a A m 1/45

Reference Thermometer Tem erature

gc

Reference Point Number

Thermocouple Potentiometer

Tem erature gc

3Y 11 9

3 O L 2 93

. 29t Yj I

Temperaturab difference

e

awoe of calibration system used. b i--

[(ref temp, OC + 273) - (test thermom temp, OC + 273) ref temp8 "C + 273 l O O U . 5 0 I -

r 5 -4

.G

L

n

e ' 0 .o .I

t 3 5

5 U

- I u

s

u -4 metican E'nvilronrnmtrr e

kcer In

kcer Our

Conrrol Box 1

CIP 7y

Box 1 A

A 3y

'74 box 2A

73

7 3

3L/

Meter In

llater Out

Ilopinger In

Impinger Out

Oven

Iopinger In

Impinger Out

Oven

Impinger In

Impinger Out

Oven

13 1 3

-22-

If

.. . ...

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! NOZZLE CALIBRATION

Cal ibrated by

D 1 , 2 , 3 , = n o z z l e diameter measured on a d i f f e r e n t diameter, nun ( i n . ) . Tolerance = IIkitsurc wi th in 0 . 2 5 mm (0 .001 i n . ) .

Tolerance = 0 . 1 mm ( 0 . 0 0 4 i n . ) .

, . ,. . AD = maximum d i f f e r e n c e i n any two measurements, mm ( i n . ) . . . .

i I Davg = average of D ~ , D ~ , L ) ~ .

NOZZLE CALIBRATION

Cali brat ed b y B s / d d & / / A

c . nun, (in.) m, ( i n . ) mm, .) nun, AD, (in.) Davg

Nozzle

number iden ti f i c a t i o n

I

where :

1..

0.575;. I 0.375 I 0. U O L I I 0.371'

, = nozz le diameter measured on a d i f f e r e n t diameter, mm ( i n . ) . Tolerance = nirasurr within 0 . 2 5 nun (0 .001 i n . ) .

Tolerance = 0 . 1 nun ( 0 . 0 0 4 i n . ) .

D1'2' 3

A D =I maximum d i f f e r e n c e i n any t w o measurements, nun ( i n . ) .

avg = average of DL, D 2 , D3. D

r -

i

I'

.. .... ..

.. , . ' .

I Hdnt 2 LltV 3 Llh3tiUl 4 b e r a t w 5 Uate

6 Stack Draeter Irni 7 Sdmle tu kdw e meter Em Hubff 9 &tw H

IO 11 I2 13 I4 15 16 I 7 18 19 20 21 22 23 24 i3 2b 27 28 29 30 31

78 *I

1 2.245 1 .u7

u.w

Starnl e55 Stecl f4a

a i

ib.&

1J v.uJ

3 U.Ul

1124 u.w/ I+

U . I M

24.2 WD-I

b-

J 2.8 lU.8 6 . 6

:/

.I .~ ...

. . , . ..,. . .. . .

. . .

. ..

I -

I .- i

r I ! I:::..

. ..

1 .

i I

i c. 1 I ! i . .

i..:: . . ' .

I LI i.- I

\

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1sOYI)IEIIC 'H 'H = 2.3519

tmstmt n49.w *Ha I .m ms 2 B . W n 2a.m - I 28.5927 'P (1.31w

'H 2.W15

..

. . . 1.

r L

1.

avo 'F avg 'H

&ter 1 EKW aturr

Inlet I 'F ,

7: 72 72 i3 73 i3 73 i 3 73 a 73 73 73 i 4 73 74 74 72 71

72 7; 73 il

.I I'

Stack b S

rs V 1

I'FI IttJl Iib5.223

1;) lio8.ib

122 17n.M 123 li7o.ai I22 1779.67 ILI 1782.il 122 176.7 I22 1M.iI 112 1791.75 124 17Y4.a 123 1797.65 Iz1 Illrh).M

118 11ru2.58 115 1w.91 126 18u7.27 125 1BA.U 125 1812.37 124 1814.YI Ii4 1817.69 124 l @ J A 12) i U . I ? 121 I&.; 154 liJii.23 123 1u.m

lm VOIWR

124 m i .us

h 5

Volume difference

If UI

2.5 2.79 2.78 2.84 3.0u 3.03 2.99 3 4 3.02 3.03 2.87 2.B 2.a 2.33 2.36 2.5 2.55 2.5 2.78 2.12 2.78 3.u1 3.u3 3.a

.--

I.

I

. :.

I

i- t

... .. . .

3.21 3.110

3.87 4.53 1.55 4.53 J.9 4 .% 1.52 3-58 3.61 1 .KO i d 2.59 3.22 2 . 2 3.2: 3.60

3.80 3.67 J .% 4.51 4.51

3.87

Sart ’ PS

saaOllfl4

1I.e

lain1

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

C l a d 1 LIB

vacw

( i n W

5.7 1.2 1.3 7.7 9.1 9.1 9.2 9.3 9.4 9.5

8.2 4.2 5.4 5.5 6.3 b.4 6.5 6.9 1.3

9 (2

9 .u

a.3

7.8

9.b

. .

Pmbe i ewvatwe

Exit I 'FI

Filter lemerrture

I 'FI

Itminqer l m w r t w

ltutlet I'Fi

Kp 63.19 H = 15.6A.E

n 23.7 cs = .5,33ILx+4

l b v d r f = 1.1797E-k Pitot Tubs qainddrcf IO.-

I I = 01( IWhr = 1.4884 B = l X

Uar. = 23.2 Final Lrd Ulrck Rate Pitot Tubs

Finish 1W.4b3 w = & Start I W A52 B = l &

b t e U.UllU

uac. = 23.3 , .:

-- Run No. */ com&L D a t e kCr3-w - S a m p l i n g L o c a t i o n

I STU!7E COLLECTED -

IMPINGER 1

IMPINGER 2

IYPINGE!? 3

IMPINGER 4

F i n a l Neight /Volume I n i t i a l Meight /Vol . Increase

F i n a l Weight/Volme I n i t i a l I ' l e igh t /vo l . Increase

F i n a l Weight/Volume I n i t i a l Weight/Vol . Increase

F i n a 1 Weigh t/Vol ume I n i t i a l Weight/Vol. Increase

t /gq. 0

t 73.3

'r 9.0

PARTICULATE COLLECTED ?.d > FXONT-HALF ANALYSIS (Nozzle,Probe,Filter,and Hot Box Glassware)

(1) F i l t e r & P a r t i c u l a t e s c? 7738' -Go-'

( 2 ) F i l t e r T a r e Weight ( 3 ) N e t Dry P a r t i c u l a t e s ( 1 & 2 ) ( 4 ) P a r t i c u l a t e s C a u q h t i n

Nozzle,Probe,Classware (5) T o t a l F r o n t C a t c h ( 3 & 4 ) J r * Z . O 7 .

BACK-IIALF ANALYSIS ( I m u i n g c r s ,and C o n n c c t i n g Glassware) 0

(1) P a r t i c u l a t e C a u g h t i n I r n o i n g e r s Evaporated Down a t L e s s Than 1 2 0 F 6 .9 r q . u

TOTAL PARTICULATE CATCH (Sum of F r o n t and Back-Half Catches

I

,

ORSAT A N A L Y S I S - ( A v e . of 3 Analyses Each)

- -------_

.

i

I:.:

!..:~

! j

i

1:: I

t

1 Plant 2 L1tr

3 LacatlM I heratm 5 bate

6 Stack Iliameter (in1 7 sawle b u n ~Clabw

6 Meter nox Nuabw ? k t w HCI

IO k t w Ldlibrdtrm,l 11 Pitot Idle.. cr, I2 Probe Lrnqth iftl 13 Frobe Linw Hatwral 14 Probe Heatff Setting I'FJ 19 hmbient lmerature I'FI 16 B m t w i c h ' K 5 . . h irnHgJ 17 mwlaed tioisture ill 18 StaticFres~lre. Ps IinHHIJ 19 C Factw W Reiffence P \inH2Ul 21 Nozzle ldentif icatimliumbw 22 Nozzle Diameter ilnJ 23 Ihwwmetw Nruphw 24 Pretest Leak Hate IUNJ 25 L e d LhecL Vacuum IinlLW, 26 FiIterNumber 27 bds knalrsi5 28 LO 12)

29 LUL I11

AI 02 t i J

31 In2 (1,

i a a-I

I 2 .AI

1.0; U.W

b' Stain1 ess Steel

240

26.12 16

u.u3 u

3.37 1/24

v.5037 l-h

3 J . d

Zk.2 WE-2

b9.b

u 2.1

lu.93 b.67

..?

'*

t.:.

i

NOZZLE D I H E R Dn 0 i1.%37

constant 819.m "1 1 .m MS 28.8212 n 28.8212 - I( 26.913 'P 3 . w )

'W = 1.m

I

.. ..

I

!

Samole Fornt

start1nr I 2 3

S b 7

4

a Y 10 I1 I2 13 I 4

I5 10

17 Id 19 20 11 22 25 24

Uetw lwerrture

h t l e t I'FI

7b l b .

75 73 71 77

..

_ . I(r .. I ,

78 tb _. n i 7 78 a 77 7t7 78 a

7t7 78 3 79 3

73

;i.3 k t w

k t w l m a t u r e

Inlet I'FI

73 2 12 12 12 n 72 73 74 i 4 73 73

i5 73 i 4 74 71 74 i5 75 i 4 73 74

n

A.3 124.5) 535.d SM .*

6u ValW

dlffserwr 1ft3i

2.17 2.26 2.40 2.5 2-62 2.73 2.12 2.93 2.w 2.94 2.- 2.94 u ;32 4.24 2.49 2.51 2.68 2.72 2.72 2.72 2.91 2.93 2.92 2.96

.

I

I

! ! I --

I- ,.

t I !

...

... .:.

1U.104 2.43 V.U.4 2.44 li.115 3.113 ll.U5 3 . U U.Uh 3.b4 1I.ll.j 3-00

U.6b 2.65

18.iJi 4.h 6.07 4.25 0.Oi 4.25 0.67 4.23 0.07 4.23 0.04 2.44 0.04 2.44 0.65 3.M 0.05 3.04 O.Ub 3.6s 0.06 3.& U.W 3.M (1.h 3.66 0.07 4.25 0.U; 4 . 3 V.07 4 . 3 0 .Ui 4 .a

Sort " f S

3.570~ (1.2413 o.usei5

Velocity hessure Sort

b d d Olff -Ps T S 'M

Satal inu Tlme

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

Clock T I P

1.24 hml 15iN 1% 1% IW IS12 1515 l5lU 1521 1524 1527 1524 1533 153 IML3 I* IhW I612 1615 lbld lb21 1621 I627 lap, I d I&

vanu

IinMl

4.3 4 J 5.6 5.8 b.9 i.1 73 8.3 0.3 8 3 8.7

4.9 4.V 5.9 6.1 7.1 7.1 7.2 7.3 b.3 8.6 8.7 8.9

8.8

Iminqer lwoerature

atlet I 'Fi

37 36 37 36 37 37 33 41 42 41 JZ 43 33 d5 Ai 37

3P a 39 w 42 42 42

38

24.63 M I c t lVolrlqer

tmnuatwe I 'Fi

4 . . .

I

I -.

ISoKINErlC WCULATIM bhll = 1.38JBE-u3

IS0 = 95.7276

l n i t i r l Lrit Check Rate Finish IdU. 78 Start ia3i.~c/a

Rate = I).ulZO

b 85.49 Us = 15.8183

)In 49.2

lbvdaf = 1.7KGE-06 CS = a . w +

Pitot Tubes galOr/dacf =1>.0129 k - OK lWhr =La25 B = u k

vu. = 2.2 Final Le& ChecK Rat, Pitot Tubes

Finish lt197.lbb II = a start IBY7.lbl B = &

Rite = u.wh,

Vac. = 22.3 I

- i ~

I- I

I

, ...

i !

I [-

I. I I !. ,

!..:

i 1' I_ I

.- LABORATORY DATA (YETHOD 5 )

olume Gain

IMPINGER 1

IMPINGER 2

IMPINGER 3

IMPINGER 4

Final ;geight/Volume 231.6 Initial Weight/Vol.

Final Weight/Volume (,,70 .ti' Initial Weight/Vol .

Increase -S222i -t- /5y-.3

Increase =4 + 7?.7 Final Weight/Volume 4 6 0 . 4 Initial I.leiaht/Vol. - - Increase 455.7 t c . 7

Final Weight/Volume g(33.(/ Initial Weight/Vol. Increase W6.3 + 17.1

PARTICULATE COLLECTED

FRONT-HALF ANALYSIS (Nozzle,Probe,Pilter,and Hot Box Glassware)

(1) Filter h Particulates 0 .6BF9 ( 2 ) Filter Tare Weight c2-o-T ( 3 ) Net Dry Particulates (162) 0 . 0 2 # 4 = 24.V ( 4 ) Particulates Cauqht in

Nozzle, Probe ,Glassware (5) Total Front Catch ( 3 & 4 )

BACK-HALF ANALYSIS (Impingers,and Connecting Glassware)

(1) Particulate Caught in Irnoingers Evaporated Down at Less Than

TOTAL PARTICULATE CATCH (Sum of Front and Back-Half- 0

120 F 3 3 - .

I '

I IF.

I

I 1. .

( A v e . of 3 Analyses h c h )

------ --- I--- T I 1 VOLUME PE TEST I

I AVERACE

i .

[-- : :

1 Pldnt 2 c i t y 3 Lucatim 4 $eratw

Date

6 Stack Diameter ( m i

7 S a l e hu W w 8 &tw boa Wer 9 bter 'It?

10 Meter Cal ibrat im, l 11 Pitot lube. LO

12 Frobe Length t f t r 13 P t w e Linertlaterial 14 F'mbe Heater Setting (TI

16 b m t w i r Fre55.. F8 tinliqi 17 H5suaed Noisture t l l 18 S t a t i c h e s s w . Ps (inHiUI 19 5 Factor 20 hefwence 'P IinMOl 21 Nozzle I d e n t i f i c a t i m b b a 22 Nozzle Oiametw Iin, 23 Ihermmetw Nuber 24 Fretest Leak fiate (CFtlr 25 Leak Check Vacuur (mWI 26 FilterNuaber 27 6as rinalvsis 28 M (1)

M 172 ti) 31 N2 (11

I5 APblMt IecaPWdtUW t 'F )

29 w2 IIJ

.

Yestan kqar co. E i l I ings,htana

Pwr Stack, CDsliuwe U - S J . Paul bRMD 1124-W

18 Of-I

1 2.245 1.07

3 . w b'

StainlessSteel 241i QP.0

&.Pi IO

L b 3

u.u7 IrM U.W Id

U . W

22.1 w3

v

J 2.73 11.2 b.07

. . . ..

6.0357 3;n 26.79 3.03

26.1922 U.8W

w u

3.16 1 3 59u

28.8848 27.1432 26.79 0.03

ib.7922 3.06

n

IsOKuinC 'H 'H = 1.5906

cnstml 849 .w "7 1 .@MI IUS 28.8818 n 26.- - K 26.5104 'P 0 . W

'H = 1.W

SarOlC

Point

stut1n9 1 2 3 4 S 6 7 8 9 13 11 12 13 14 15 Ib

17 18 19

,:J 21 22 23 14

avq 'F a w 'R

kter l e m w a t w e

Uutlet ('FI

M 73 70 71 71 72

74 73 74 75 i 4 73 16 76

75 75 75 il 7s 3 76 75

n

n

hter leperdture

In le t I'FJ

M 07 67 M1 68 09 b9 69 b9 09 70 70

7u 71 71 71

lil 70 71

71 n

71 71 71

Stack 1-

1s IT)

128 127 127

127 IN I29 127 127 127 129 128 127 126 126 127 129 I31 132 134 135 136 1 1 133

im

71.58 129.42 531 .sa 589.12

b s VOlW

V I l f t3I

iw7.w 1aw.u 1wz.25 1901.b9 1W7.11 19W.n 1912.42 191S.W 1917.93 192u.82 1pzl.Z

1m.823 1932.32 1934.79 1937.43 IY4u.11

199.65 1940.54 1951.42 1954.33 1W.17 19tQ.06

1962.9t.3

19z.n

1942.a1

2.38 2.43 2.44 2.42 2.M 2m5 2.u

2.89 2.90 3.e 3.09 2.50 2.17 2.M z.hd 2.70 2.8) 2.89 2 .a 2.91 2.84 2.09 2.90

2m

total 65.52 65.52 dveraqe 73.541&&&7 69.625 129.4lbb6667 Smle n e t w h t w Stack 6as 6r,

Paint r m w a t u r e lemwature r e p (*FI VOlW VOlU Inletl'F) @.itlet ( 'FI I V I VI

,.:

t L I

Velocitv Ressure Head Diff " P I "

(inHZO1 (inHiU)

0.05 2.96 0.35 2.97. 0.05 2.97 0 .lis 2.97 0.60 3.51 0.a 3.56 0.06 3.57 li.07 4.10

0.07 4.16 0.08 4.77 0 .% 4.a 0.65 2.99 0.05 3.N 0.06 3.61 0.04 3.65 0.66 3.58 0.07 4 . l b 0.07 4.lb 0.07 4.14 0.07 4.14 0.07 4.13 0.07 4.14 0.0; 4.15

0.67 4.18

Su.t 'Ps

0.2236 0.2% 0.2224 0.2236 0.2449 0.2449 0.2449 3.2& 0.2646 0.204h 0.2828 0.2820 0.2236 0.23h 0.244Y 0.2449 0.2449 0.2646 0.2646 3.2646 0 .2M 0.26)b 0.2646 o.zM6

SMPl ins CI od: Tim Tim

Iran) (24 h)

3 a 3 836 3 839 3 842 3 745 3 7 4

3 €34 3 85) 3 puu 3 903 3 pub

3 933 3 9 3 3 939 3 Y42 3 9 4 3 940 3 951 3 954 3 9 9 3 Im 3 1003 3 1u16

r n '

3 mi

(inltgll

5.8 5.9 6.1 b.1 7.3 7.6 7.7 9.1 9.3 9.5

10.8 6.5 6.5 7.0 8.1

9.5 9.8 9.9 9.9

14.1 10.1 10.2

10.8

8.2

72 72 U.Od3W3.U 3.7701 0.2W 3 932.41666667 8 . U l W 7

Velocitv Preswve 501 t 5 m l 1 n u . Clock VIcuur

Head Olff -pP T1m lim ' PS "

,.:

c

!

Prabe lmera twe

hlt I TI

23 I 238 24 I 24tl 243 24s 233 249 ih ZbO

2bU 269 2bd 266 3 Y 253 2 4 i 265 2% 2% ihl 236 23i 251

F i l t e r leqerature

('FJ

242 245 2% 258 259 3 9 250 243 252 254 247 2h2 2k2 is1 249 249 249 243 23 227 w 2rl 2% 258

3 33 33 34 35 36 35 36 31 38 37 30 41 41 40 41 43 U 45 46 .Id 49 49 49

vou)(E "ws Wdrtd) = 62.9451

I

1 r' 1 I

Is0 = 94.4232

In i t ia l Leak Chtck Rate Finish 1897.364 Start 1697.355

Rate = 0.m

PARllalnTE aNmmT1M Cs = 1.975E-M

lb 50.2 cs = 7.975E-0)

lbudsci = 1.7582Ea Pitot Tubs prainddscf ru.0123

n = m Ibdbr - 2 . a B = K

Vac. = 22.2 Final Ltd Beck Rate Pitot Tubtr

Finish 1963.119 A = & Start 19U. 1 I I a = &

Rate = 0 . W vu. = 22.3

IMPINGER 1

IMPINGER 2

I-WINGER 3

IMPINGER 4

FRONT-HALF

F i n a l Xeight/volume 7/9 .c I n i t i a l Weisht/Vol . - . I n c r e a s e s 2 L z A. F i n a l Weight/Volume - i 6 3 . I n i t i a l Meiqht/Vol . - Increase S Z K L &

Increase .EuL- L. 3

F i n a l Meight/Volume ‘/6Z .< I n i t i a l I.leight/Vol.

F i n a l Weight/Volwne - g m Increase

.. . I n i t i a l Wei.ght/Vol. . . .... ., ~ , .


ANALYSIS (Nozzle,Probe,Pilter,and Hot Box Glassware)

(1) F i l t e r & Part iculates 0. G8g?#. ( 2 ) F i l t e r Ta re Weight 0.LLOq: - LJ-0-3 (3 ) N e t Dry P a r t i c u l a t e s (1&2) 0 D1 ./v 9, ( 4 ) P a r t i c u l a t e s Cauqht i n

Nozzle,Probe,Glassware ( 5 ) Total F ron t Catch ( 3 6 4 )

BACK-HALF ANALYSIS (Impingers ,and Conncct ing Glassware)

(1) P a r t i c u l a t e Caught i n Imningers Evaporated Down a t L e s s Than 120 F /o.o,, .

I TOTAL PARTICULATE CATCH (Sum of Front and Back-Half Catches

ORSAT ANALYSIS

( A m . o f 3 Analyses Each)

1

II

!. 1 ' :

i

78 Ch-1 i

1.245 I .37

0 . m 0 '

Strinl ess Sterl 248 b4.b 24 .i9

14 0.U

0 U.U?

u2-h u.503

I+ tO.312 2 . a

w - 4

3 1 .YO

12.13 L(5.91

!

f

cmrtant 8 4 9 . m *Ha- 1.1240 MS 28.7w m 28.1988 - K 30.9765 'P 0 . w

'H 1.8586

1

i::. !.: .. .

k l S

Point

StWKlng

1 2 3 1 c

0

d 9 IO 11

13 I4 15 16 17 I&i

I? 20 21 '12 '3 24

a i L.

&trr hKW

Temperature Teaperatme Uut I et Inlet

(TI (TI

Stack Terp

15 ('FI

1 37 139 141 1 3 135 1-33 E9 131

132 130 131 113 138 139 142 I44 143 141 142 140 139 139 140 142

6ds Voluae

v4

(ft31 1963.404 19bs.83 19k4.34 1971.02 1973.75 1970.41 IY79.19 1m.1 lY65.02 1337.96 1W.M 1994.M 1997.142 1999.48 2001 .?I m.4 ~W7.11 m .a2 2012.55 2015.45

zozl.32 2024.43 2027.55 m.074

m.3

6a5 Vol Lue

d l f i e m X R (f t3 i

2.43 2.51 2.68 2.73 1.72 2.72 2.91 2.92 2.94 2.92 3.1b 3.13 22-4 2.43 2.49 2.71 2.71 2.73 2.90 2.91 2.93 3.11 3.u 3.12

74.42 137.3 %.*L 597.29

t o t d 67.27 61.21 average 70.2- 72.015

I

I

....

[-

I

I .

U.05 3 . h 1j.a A i & 0.Ob 3.a 0.04 3.&

0.00 3 . X 3.07 4.25 0.0; 4.33 u.07 4.32 0.Ui 4.34 0.M 4.96 5.M 4.Yi U.M 2.45 0.35 3.& 0.05 3.b5 3.06 3.65 0.bh 3.M G.& 2.d b.U7 4 . 3 6.37 4.3

G.U7 4.3! ':I *uti 4.92 b.iJir 4.51 3 .ud 4.JO

U.bb 3.bY

iwt %dml ins . P5 Ilme

3 3 ' 3 3 3

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

J

72 0.2531 3

5art Sa-Il In9 'F'S 11-

5.7 5.6 1.1 7.1 7.1 7.2 8.3

8.5 8.5 9.9 ? .? 5.1 b.1 b.1

1.3 1.3 7.4 8.7 8.6 9 .:

10.0 10.8 10.7

a ;3

Frwe Twowature

hit I'Fi

FiItw Twerature

I 'F i

I n i t i a l Leak Chock Rate Finish i W . j b ?

Start 1963.357 Ratr = u . W O

rcn 53.9 Cr = 8.3.mhi4

IWkf = i.a?i€* P i t o t Tubs gra inddscf =0.3129

a = u: lbdhr = 2.4ZG3 E-&.

Ux. = 2.6 Final Lrak Check Rate P i t o t Tubes

Finish i V J V . 8 4 4 rl 'LR Star t ZU$J.iiA B = U 1

Rate = t.s.uiJb

uac. = '2.8

I

i .

I

!

. . .. . c..

IMPINGER 1

IMPINGER 2

I Y P I N G E R 3

IMPINGER 4

F i n a l ;veight/Volume 674 9 I n i t i a l weight/Vol. I n c r e a s e s22L t l f 7 . Y F i n a l Weight/Volume 70 / I n i t i a l Weight/Vol. I n c r e a s e <n.y i- 1 1 0 . 7

F i n a l Neight/Volume 4q ff I n i t i a l Vieight/Vol. Increase -%L . 0- i 2 3.5-

L, "UIUIIIC- &3.y sht /Vol . - F i n a l Neigh' 'lrrrl .*--

I n i t i a l Weit- .

I n c r e a s e


FRONT-HALF ANALYSIS (Nozzle,Probe,Filter,and not Box Glassware)

(1) F i l t e r & P a r t i c u l a t e s ( 2 ) F i l t e r Tare Weight ( 3 ) N e t Dry P a r t i c u l a t e s ( ( 4 ) P a r t i c u l a t e s Caught i n

Nozzle,Probe,Glassware ( 5 ) Total F ron t Catch ( 3 . ~ 4

O , b F 6 8' & 2 )

BACK-HALF ANALYSIS (Impingers,and Connccting Glassware)

(1) P a r t i c u l a t e Caught i n I a n i n g e r s Evaporated Down a t L e s s Than 120 F

TOTAL PARTICULATE CATCH (Sum of Front and Ba

I

i I I' I. i

ORSAT ANALYSIS

( A v e . o f 3 Analyses Each)

--

... . .. . . ..

!

i I Y

!

i

i I . L

P IO 11 12 13 14 15 16 17 18 19 M 21 22 23 24 25 26 27 28 29 30 31

Uestw %gar cu. B i l I ings.Nintana

byw Stack. Coroliance 115 - 5 J. Paul Bmvn

lJ24-7iJ

78 GRI

I 2.245

I .37 U.W

a' StainlessSteel

2M b9.6 h.79

14

0.03 u

3.u: 11% 3.m

1-h

3.016 3 . 8

tu-5

0 2.2 12.1 85.7

i

PRmST MTA lS9KlNEllC 'H 'H 1.6537

castrat e49 .w a Ha I . L w

M5 a.m n ia.8kA.l !! 27 &24 'P 0.w

'H = l.&l

i

i '

. . 1 I 1.

...

7b

id 77 ..- 18 I t

76 , I .- 75 75 14 74 73 75 74 n 75 !i 74 75 74 75 73 n 72

156 1 . 3 133 136

135 1% 137 135 137 136 136 137 135 135 137 135 134 I 3 4 13a 1 3 136 136 137 135

7O.iG 135.50 530.93 595.3

6as wli ure

vn ltt3J

LWI .549 m . 6 7 X5.N 2037.92 2010.38 m 2 . a 2015.3) m . 1 2 2050 .l6 2053.55 m.34 2059.25

Lod.153 m.45 -%7.?6 -W.W 2JZ.Ul 374.14 377.49 2 m . 2 m.97 :185.87 ,w.a 2091 3 9

2094.35

b S

Volure a i i f m c e

t1t3

2.12 2.12 2.13 2.G 2.50 2.51

2.73 2.10 2.79 2.91 2.91 2.29 3.51 1.53 2.52 2.73 2.75

2.76 2.w 2.45 2 . 7

2.73

2.72

2.77

!

6,s 2 .a +.b4 2.49 Oh4 2.s 0.05 3.10 u.u5 3.11 0.u5 3.1.j

(1.60 3.71 u.36 3.72 0.h :.7b i j .36 3.71 u.u: 4.32 3.3; 4 .a U.64 2.17 0.05 3.UY 0.115 3.08 0 .35 3.19 0 . k 3.71 0.h 3.72 0.06 3.71 d.06 3.71 0.07 4.33 d.ui 4.32 0.00 3.70 v .ci6 3.71

0.m 3 0.m 3 G.-W 3 5.2230 3 u.m 3 Ij.Zh 3 0.1439 3 O . N ? 3 U.2442 3 0.2449 3 0.:* 3 u .2* 3 0.2w 3 0.22% 3 0.224 5 0.236 3 0.i449 3 0.2449 3 6.2449 3 0.2449 3 0.2h44 3 0.m 3 0.2449 3 d.2449 3

I24 fE.1 (1nm1

IMJ 1m 5.2 I& 5.3 lbo9 5.1 IbU 6.5 lb15 h.b

161U b.4 1621 0.3 Id4 d.4 1627 0.4 163) #.+ Ibu 9.8 I& 10 1653 5.9 I& 7.1 1659 7.1 Ihn 7.2 1 705 8.8 1708 8.9 1711 9 1714 9 1717 IO.? li2J 11.2 1723 9.2 l72h Y .3

R lb59.5 6.0125 Clocf VXUr TIP

i

i

I .

30 36 37 3a 3 39 39 40 41 43 43 44 45 45 44

49 41 4a 4? e ' ,L'

51

53 53

C" .ti

I I r L I

I n i t i a l L t J Check Rate Finish iUi.ijl Stut 2UJI.llS

Ratr = u.Oiod

KP 65.49 VI = 15.5516

m a5 .z CS 1.41XE-U3

IWdSCf 3.1157E4 Pi tot Tubs qainr/dscf = 0.u21d

A : I& IWhr = 5.7191 B = W

uac. = 2 . B Final LtaK Check Rate Pitot Tubs

Finish m0.w II = o k S t u t 2031 B = &

Rate = w.1Lu V u . = 22.8

i

IMDINGER 1 F i n a l Xeight/Volume I n i t i a l Meight/vol . I n c r e a s e d - . .If/.O

Increase ms 4n,4,

Increase 44r.f" .A,

IMPINGER 2 F i n a l Weiglit/Volume f I n i t i a l Meight/Vol.

IYPINGER 3 F i n a l tleight/Volume f f i ? I n i t i a l Weight/Vol.

IMPINGER 4 F i n a l Irleight/Volume ?fy. 7 I n i t i a l Weight/Vol. Increase

PARTICULATE COLLEWED k.. .

FRONT-HALF ANALYSIS (Nozzle,Probe,Filter,and Hot Box Glassware)

(1) F i l t e r & P a r t i c u l a t e s O.?// B 0.66&" /&I -a- (2 ) F i l t e r Tare Weight

( 3 ) N e t Dry P a r t i c u l a t e s (1&2) ( 4 ) P a r t i c u l a t e s Caught i n

Nozzle,Probe,Glassware ( 5 ) T o t a l F ron t Catch ( 3 6 4 )

BACK-HALF ANALYSIS (Impingers ,and Connccting Glassware)

(1) P a r t i c u l a t e Caught i n Irnningers Evaporated Down a t Less Than 120 P

TOTAL PARTICULATE CATCH (Sum of F r o n t and Back-tfalf Catches

ORSAT A N A L Y S I S

( A v e . of 3 Analyeae Each)

. :

.. .

. . . - . . .

i

I

I Plant

2 c i t y

4 Goerator 5 Date

3 L X d t l M

ia a-1

2.245 1.37

u .w b'

Stainles$teel z*

OY .D

26.76 I4

LU3 0

0.07 1/24 U.W

l-il 6 . U 22.8 UD-b

I

0 2.37 ll.ti7 85.76

cmrtrnt a4?.rn a n a 1 .w MS 28.m tb 23.m - K 2 3 . w 'P 0 . L W

'H = 1.-

f t

.:. . . . .. i.

i

rvg 'F dVq 'R

74 75 E i 4 74 75 74 74 75 i5 l b ;5

75

16 :e 7a

76 to

70 77 i 7

.. IO

_I.

IO

-

n , I

71 71 71 70 70 71 71 74 70 n 71 71 71

72

i1 n 72 7i 71 72 72

n 7- ,L

Y I &

139 14 143 1 45 141 146 142 148 149 1% 144 1 43 137 143 144 143 147 151 1% 14; 149 1 49 14d 1%

73.33 145.71 533.33 a5.a

Gas U S

Volume 'Jolrue Vm d1fterencr lft5J 1f151

LW4.809 2091.02 2.21 209.21 2.19 uo1.7 2.49

2104.17 2.4; 21G6.65 2.48 2109.12 2.17 u11.62 2 . 3 214.3 2 .OB 2117.01 2.71 2119.62 2.01 2122.49 2.01

2125.Jal 2.90 2127.65 2.2h 2129.85 2 . 8 2132.3 2.35

21J4.70 2.d 2137.25 2.47 Zl59.il 2.b 2142.33 2.2 21*.01 2 . M 2147.69 2.h 2153.57 2.u 2153.45 2.M

2155.332 2.M

8.

I

2.44 :;u 3 .u3 I .Ui

3.01

3.02 3.M 3 . d 3.a 3.03 4 2 4 4.25 2.45 2.43 3.03 3 . s 3.u2 3 .oo 3.60 2.02 3.61

4 2.2 4 2 2 4.19

U.ZlHJ1~

J .Llkju u .xo u .a U.Z& 0.m 0.22% 0.2449 v.2449 0.2449 0.2646 5.2trk 0.2ilw d . & W 6.2236 0.22% 0.m 0 .-a 6.2449 5.2449 0.2449 0.2646 (I.%

U.?&

3 3 3 3

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

J

(24 h W I i n W 1824 lW 4.9 I& 1.9 1839 0.1 1842 0 2 IS5 b .j IW b.4 im~ 6.2 lti54 7.4 167 7.5 IW 7.0 1903 9.2 1% Y .3 1933 5.4 1% 5.4 1939 6.7 1042 h d 1945 b.6 194 6.6 1951 7.3 I S 4 7.3 1957 7.5 iwo 9.d

,wu IO 2003 9.a

.... I

Prcae iwerature

Exlt (T,

Fi l te r leaperatwe

17 a 36 35 3 37 w 39 40 41 43 45 41 42

43 43 13

44 w 44 46 47 48 48

.

i

t

IS0 = lW.5011

I n i t i a l Leak Check Rate Finish ictq.02 Start iljy4.014

R i t e = u.W

Vicialr) 2Y5.1 W r t d ) = 13.W

DRY STm R(y RITE Btstdl 1.1744Et06

MTICUATE I~NIBTWTIIB Cs = I:0778Eir3

m h3.h CS = 1.077E-03

IWkf = 2.37wE4.b Pitot Tubs c)rrial/dKf =U.l)lt4

H = k lWhr = 2.7303 B = &

Vac. = 2 . 6 Final Leak Check Rite Pitot Tubrr

Finish 215h.53 I , = &

Start 2156.521 6 = o k Ritr = 0 . M

vu. = 22.a

i_ 1

i I ! ,. :

I

I I

I i

t I

I

, -

. . I.

!

i

I I

Compan a$$ /&. -- Sampling Locati

IMPINGER 1

IMPINGER 2

PlPINGER 3

IiWINGER 4

Final ;Veight/Volume 7, g Initial Meisht/Vol. - . Increase Y 2 f /42,9 Final Weight/Volume 7/.7.a Initial Weight/Vol. - Increase a L L A Final Weight/Volume 964.7 Initial Weight/Vol . Increase A ! ! /2.0

830.0 Final Weight/Volume , f i ' f iA ./ Initial Weisht/Vol. f

I 7 u / - .

Increase - - PARTICULATE COLLECTED


(1) Filter 6 Particulates . 3 d 68 w ( 2 ) Filter Tare Weight ( 3 ) Net Dry Particulates (162) ( 4 ) Particulates Cauqht in

Nozzle,Probe,Glassware (5) Total Front Catch ( 3 6 4 )


(1) Particulate Caught in Imninsers

/2*3z-+* Evaporated Down at L e s s Than 120 F -

TOTAL PARTICULATE CATCH (Sum of Front and Back-Half Catches v

-_

. .

I O R S A T A N A L Y S I S

( A v e . o f 3 Analyses Each)

-- TEST

I

-.- ... . . . .

I - i -.

I.. I

..

137 Ol-I

1 2.245 1.37

6 . W b;

5tainless Steel 2% 41 .L

&.*I 14

U.18

3 u.14

j lt i - 4

0.375 l-fl

U.llU 2.8 B-1

3 5.: 10.6

84.2

I

I . ;

CO U . W

Im Vidui id) 67.5030 GEI .%'0131 1 2 . m

,i;.Mjuo V G i m 1.1 1

Velitcti 4Y .m 'h a i 9 3.2330 \r*c a.u1:5 VK 46 .m tw = u.1145

ISlKuETlC 'H 'H 1.2248

cmrtaot w 9 . m "3 1 .w MS 29.2560 m 29.25bo - k 8.7484 'P 0.1401

'H = 1.228

I

7: id 71

71 72 73 72 74 75 15 75 77 76 i s 74 A 77 ;0

3 ?4

73

71

-c I 4

. t O

t4 05 ha

od bti 08 71 h6

71 71 70 n i 0

71 09

71 R

? I io 72 71 -7 l i

-7 71 I &

115 111 I16 111 112 110 1W 105 111 109 112 113 lG9 108 110 1CW 167 112 169 111 116 IW 166 157

645

vol rue Va i f t 3

21%.liYI 2155.d

2161.552 2163.92 Zlia.31 2168.7

2171 .W 2173.22 2l75.38 2171.57 2 1 n . n 2181.97

21tM.24Y 21Bb.45 2188.79 2191.14 2193.5

21Sd.111 m.00

izO3.z 2205.69 LzM.13 210.58

2213.310

2195.78

Gas V O l W

ditierencr 1ft51

1.32 2 . 3 2.37 2.39 2.39 2 . 3 2.13 2.16 2.19 2 . 3 2 .a 2 .a 2.20 2.34 2.35 2.36 2.28 2.3 2.5: 2.5 2.47 2.* 2.45 2.44

110.w 570.03

56.127 56.127 110.08333333

Stan 6as 6a5 T a o I'FJ 'ialum VOlW

1 VP vm

I.. I

0.14 U.14 0.15 3.15 U.15 j . 1 :

u.11 11.12 0.1; u.12 6.12 0.12 11.12

3.14 U.14 0.14 v.13 sJ.14 U.17 0.17 0.15 0.15 u . s 0.15

Pressure Diti -tl

linwillr

2.74 2.74 2.95 ?.Y5 2.95 2.52 2.12

2.k) 2.L 2.3 i.27 2.5 5 js

2.79 2.77 2.n

2.71 3.38 3.37 2.98 2 .?V 3.w 3.w

-.

- .. i .OU

0.i742 0.3742 0.3873 3.33i3 0.3873 o ; m b.3317 0.304 d.S(c4

U.M

0.3444 0 .a 0.w O.i7+2 0.2742 0.3742 u.jLlim

d.3742 0.4123 0.4123 0.3873 3.3873 0.3n U.38873

tain)

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

Clack Ttm

I24 h r s ) 1030 1033 I& 1039 1312 1045 1018 1113 Ill4 1119 1122 1125 1128 1143 II4d 1149 1152 1155 11%

1206 1209 1212 1215 121s

1203

VXUr

5.3 5.2 5.5 5.b 5.6 5 .d 4.8 4.9

5.1 5.2 5.3 5.a 5.4 6.1 6 .2 4.4 6.2 6.3 7.h 1.7 7.3 7.3 7.3 7.3

i

I i E. 1 I I

FI I ter Temerature

WUQ DRY GAS ckistd) = 53.4150

In i t ia l L e d heck Rate Finish L&.;i start 115o.C

Ratr = u.lldW

WylTlCWTE UHCWIIWTIOY Cs = 5.0641E-A

h 270.5 Cs = S.MlE-03

IWdscf = l.lldt-Q5 Pitot Tubs qrainr/dsci =0.3781

. A = 6 I W r = bb.%97 b = &

Uac. = 22.u Final Ctly Check Ratr Pitot Tubs

F i n i s h W13.1Y7 k = L k Start ??13.18;1 B = &

Ratr = U.Ul4b

uac. = 22.8

Volume Gain

IMPINGER 1

IMPINGER 2

I?lPINGER 3

IiWINGER 4

‘7bt/9 F i n a l ;Veight/Volume I n i t i a l Weight/Vol. I n c r e a s e S2L.k 9- I f T , 3 _ -

L ”& F i n a l Weiglit/Volume . d$g3b I n i t i a l Irleisht/Vol. - . a*/ + q6. L Increase

F i n a l Neiqht/Volume qsy: 3 I n i t i a l Weiqht/Vol.

F i n a l IJeiqht/Volume TOz. 9 I n i t i a l Weight/Vol.

Increase Y5S.Y 4 2.5-

-

F,PONT-HALF ANALYSIS (Nozzle,Probe,Filter,and Hot Box Glassware) P

B . 90 c/o O . G / 7 - R - [

: 2uz3

(1) F i l t e r L Part iculates ( 2 ) F i l t e r Tare Weight ( 3 ) Net Dry P a r t i c u l a t e s (1&2) ( 4 ) P a r t i c u l a t e s Cauqht i n

Nozzle,Probe,Glassware (5) Tota l F ron t Catch ( 3 & 4 )

R,2 Y 7 3’ -7‘ 9 z z g -77.

BACK-HALP ANALYSIS (Imningers ,and Connccting Glassware)

(1) P a r t i c u l a t e C a u g h t In Imningers Evaporated Down a t L e s s Than

I 3 . 1 n - 9 . 120 F v

TOTAL PARTICULATE CATCH (Sum of Front and Back-Half

270.5

j

I ' I !

i !

i I r L I I

. . I...

I

I l~

OBSAT ANALYSIS

( A v e . of 3 Analyses Bacb)

--------- - I

1

I

['

!

L

137 Ch-1

I 2.245 I .ui u.m

0'

Stain1 e55 Steel 240 47.7

26.49 18

u 3.14

3 8 - 4 u.375

I+ u.311 2.8 b-2

3.18

r

I

, ..

NOZZLE DIC)(EN( Dn = u.22

IsOyINElIC 'H 'H = 1.1330

constant b49.11viu "a I .m M5 29.mll m 2 9 . w

'P 0.lW 'H = 1.1330

- K B.UJ2b

, , ,~ ;,, . . ...,, .,. . , .

.. . . .. . . .

s w l e Point

ne tw i e r o w a t w

Ilut I et ( 'Fi

MtK

Tenperatwe In let I 'F,

73 74 7? 71 7? 71 71 72 13 _.. 4

I* -. 75 70 78 7: 75 70 _. ( 0

70 77 7: 77 w 78

Stack TEm

rs ( 'FJ

110 114 110 111 113 110

113 I12 112 113 IlU 111 Ib9 110 110 112 111 110 113 114 113 115 113 114

10.77 112.w 5.b.77 572.3,

his vol upe

diffaence ifUi

2.27 2 . 8 2.29 2.& 2.35 2.37 2.05 2.N 2.63 2.55 1.M 2 . a 2.21 2.21 2 .2 2.3 2.31 2 .8 2.25 2.42 2.44 2.31 2.31 2 . 3

%rt 'F5

0 . i X aj.3742 b.3742 0.2373 b.;a7>

0.373 v.3317 d . 9 1 7 u.2317 9.31; G.3317 U.Jki0 0 . u 5 . a ir.3742 5.332 0.3142 3.3i.12

d.ujrjir

0.4W s.34: 0.2?4? u.371:

U . m

S a d ins Tlne

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 j

iloctc Tlre

(2.1 n-1 1433 1433 1436 1433 1442 1445 1440 1Wl 1% 1509 1512 1515 1518 1533 1% 1539 132 Ed5 1% 1hO3 I& 16M la12 1h15 lDld

VXUr

5.1 5.1 5.1 5.5 5.1 5.1 4.3 4.3 4.3 4.3 4.5 5.2 5.1 5.2

h 6.1 b.1

0.1 h.2 h.? 7 0.3 0.2

0.J

. . .

i I

L

IsPinqw TePwriture

Out I et I 'FI

4a 41 24 39 0 41 43 43 3 i 42 44 44

15 45 12 44 m

47 4a

44 45 4i 4: k3

VOLW DRY w W s t d ) = 51.1794

I n i t i a l hat Check Rrtc Finish 213.43? Stut 2213.4ib

Ritr = 0.3llu

m 265.5 Cs = 5.187aE-03

Ibddui * 1.1437E-M Pi tot Tubti qiiaddrcf = 3 . 0 ~ 1

6 = M( l M r = 6b.1117 B=M

V X . = 22.8 Final Leak Check Rite Pitot T u k r

ii =ilk Finish z a 8 . i - i

S t u t ~ ~ 0 7 . ;I j t r = & kste = C!.U!llb

in. -, _.,..

..

VIC. = 2 . a

...: ... . .

I -. ,

I I

I c 1. j i

!.. i."

!

1 . I.

I ' - - Sampling Location&,/,< SA,/ , Date

!.IO1 STU-32 COLLECTED _.

*?3%$ \

-t 1 7 3 . B -4- -P= IMPINGER 1 Final ;Jeight/Volume

Initial Weight/Vol . Increase

IMPINGER 2 Final Weiglit/Volume L m -- Initial Weight/Vol. Increase 1851 t 63.7

Increase y96.- + 3.3

IYPINGER 3 Final (.Jeight/Volume ye, y Initial Weight/Vol.

IIWINGER 4 Final Weight/Volume aO.(., - Initial Weight/Vol. Increase

FRONT-HALF ANALYSIS (Nozzle,Probe,Pilter,and Hot Box Glassware)

(1) Filter 6 Particulates ( 2 ) Filter Tare Weight ( 3 ) Net Dry Particulates (162) (4) Particulates Caught in

Nozzle,Probe,Glassware (5) Total Front Catch (3&4)

BACK-HALF ANALYSIS (Imoingcrs,and Connccting Glassware) U

(1) Particulate Caught in Imningers Evaporated Down at Less Than 120 F /6.J,,

TOTAL PARTICULATE CATCH (Sum of Front and Back-Half Catches

1

, .

I -- I_

I 8 . .

! I .

I I r I

' I

. . . . 1.:.

I I

II I :-

I

. . .

I

ORSAT A N A L Y S I S

( A v e . o f 3 Analyses h c h )

I

. . .. .. . .. . .. ..

I

I.....

I

E I- j

I I

... , . .

u 7.17 lU.13 82.7

I I

I I

i" b

NOZZLE D I r n Dn = u.375

IsoyIt€fIC 'H " = l.IW

cmrtaot w9.wxki *Ha 1 .m MS 29.5524 m n.5524 - K tr.uy41 'P U.IW

'H 1.1333

. ..

I.' .. . ...

!

I ' i I

Swle Foinc

startin4 1

L

J

4 5 0

7 6 9

10 I1 11 15 I4 15 la l i id ;+ !I)

Ll ..̂ . . - .. ii

LJ

k t w leepwature

In le t i 'F!

76 re _IC I , - #a

i4 -.. I d

73 i 4 )5

73 74 73 73 73 75 74 75 74 _.. io 7 <

?j

74 74 i5

lb7

16 11 1 112 137 IiJd IW 114 IN 112 la 110 114 110 111 112 IN 113 139 loir 1M lOa I12

Gds Volume

Va lft31

214 -2.2 2 i o & ZN.1 2261.3 m.73 2B.u m.4ry 22w.47 2292.47 2294.59 2296.7 2298.83

2351.118 m3.26 2335.52 2307.83 2310.15 2312.45

2314.815 2317.31 2319.a 2322.29 2324.07 2327.03

?322.30

Gds vol uy

d i i t m c e (fWi

2.44 2.42 2.B 2.3 2.3 2.35 2.64 2.00 2.1: 2.11 2.19 2.23 2.14 2.26 2.31 2.32 2.30 2.36 2.49 2.51 2.47 2.3 2.56 2.k

j

.:: I

I I

L I I

Wesire h f f "

c1ntial1

2.bl

2.03 2.60 2.77 2.76

2.M 2 .LIJ 2.21 2.22 2.39 2.41 I.2 &..A

;.;a

. _ _ .1 F - i.59 2 . 3 I' =a 2 .x 5.14 3.15 2.90

2.78 L.7

-."

x a

* I In9 Tim

Irml

3 3 3 3 3 3

. 3 3 3 3 3 3 5 3 3 i 3 3 3 3 3 3 3 3

1710 1713 1?1b 1719 I Z ? lR5 1726 I743 I i* 1749 1752 1755 1758 MI3

la19 16Z 1825

la45 la& lb49 la52 1855 1858

lhlb

wn

5 5.1 5.1 5.4 5.5 5.6 4.3 4.4 4.9 4.9 5.2 5 .5 5.1 5.Y b

0.1

b.1 - 0.d

7.4 1.4 7.2 7.1 7.1 7.1

,-.. ,-.... ,:: !- !.

I . _:

. .. ..

, . . i

Prmr T w w a t u r e

Exit ( ' F I

F l l t e r lwerature

Ilppinser Temerarure

Jut I et (Ti

j i

3 35 3 ' 5 I"

11 31

43 3

41 41

43 42

4u 3 i 3 37

40 39 4i; 39

42 43

4b

In1 t i r l L e d Check Rate ' / ' . . I , Finish Li , .? .5 /

Stu t Lil. .,*>

Rate = aj,&nu

-..'.,.. c

np B.44 VS = 24.1139

UX. IE.ij

F i n d L i d ChtcK Rate Pitot Tubes Finish im .54 Ill

S t u t i d i Y ,531 Rate = G.WU

::,./

U l C . = z2.U

i I I

r I i

. . ..:.

1.'

I I I. I I i

I

, :. 1 : . ..

! I

I I I

IMPINGER 1

IMPINGER 2

I.hlPINGER 3

IMPINGE!? 4

Final :ieight/Volume -" Initial Weiaht/Vol.

Final Weight/Volume A- Initial Weiaht/Vol. . , , Increase b3.3 + 6 7 d Final Weight/Volume Wf. 7 Initial Weight/Vol. Increase . c / s . r :3 f- 3. f Final Weight/Volume B7,y Initial tIeight/Vol, Increase



(1) Filter 6 Particulates 0, ? a ~q . - , ( 2 ) Filter Tare Height 0. LK7.d e3 ( 3 ) Net Dry Particulates (162) ( 4 ) Particulates Cauaht in

Oa7dq4- = L y q * y - ~ ~~

Nozzle,Probe,Glassware (5) Total Front Catch ( 3 & 4 )


(1) Particulate Caught in Imningers Evaporated Down at Less Than 1 2 0 F

U TOTAL PARTICULATE CATCH (Sum of Front and Back-Half Catches

!

1 NO. D E S C R I P T ~ ~ N I ' NITKOCEN

d?m#Aa&. i F20 *?

&m. ---- ; Yd'l

--- $2.7

AVERAGE $2.7 I

. .

CAXBOU CARBON OXYGEN DIOXIDE MONOXIDE

L O . I 7 . L i o . I

/o 2 7, I KO, I

/o, I 7. z C O , I

/0./3 7-17 I

< o s / I . . . ..

ORSAT ANALYSIS

( A v e . of 3 Analysee Bacb)

Volune L i q u i d Final Weight Tare Weight ~ e s idue

RUN 1 - Volme Liquid Color F ina l Weight Tare Weight Residue & Blank - Blank Residue

m2 - Volune Liquid Color Final Weight Tare Weight Residue & Blank - Blank REs idue

RUN 3 - V o l w Liquid Color Final Weight Tare Weight Residue L B l a n k - Blank Residue

R U N 1 - Weight C o w A '+inal Weight

/IO, I T Lr Residue & Blank 0 . o d 3 ~ -

Residue - 0.00 33

'' Tare Weight

- Blank u.00 0 L

Weight Collected F i n a l Weight Tare Weight Residue 6 Blank - Blank Residue :,.

I I- I I

I

I

I ~

1 :' ,.. 1

I I

I: I I

@

1 , ...

ii@ I !

I I I ..

!

- Tare Weiqht

Volm Liquid Color Final Weight Tare Weight Residue 6 Blank - Blank &idue

RUN 3 - Volm Liquid Color Final Weight Tare Weight Residue & Blank

Residue - B l a n k

=vzz) Y . < # Y I F

"

Weight Collected 22-17, yfiL Final Weight

Residue E, Blank

Y6*+~.3 3. Y?? @ Tare Weight *- - Blank

Residue dLLWL-m P

Weight Collected Final Weight Tare Weight Residue 6 Blank - Blank Residue

0 . 0 0 0 f

i

f !

APPENDIX C ( E O Test Forms - EPA Method 9)

AMERICAN ENVIRONMENTAL TESTING INC. 565 So. Birch Dr. Spanish Fork U t . 84660

P l m l GI- J G ~ fiescriplion:

Control Davice:

DistGnce: Direction: 3%- IC;

I ..

I. I . $

i i

i I: I

I

i !

i I

8 . 1 . . . . , .

:. ..

I

Height ~i Point: 75 ArrrbirnL Temperature: 4

r c I

.

. . I :

I I [1 I I I

t :.. !. :

i i

I !

!

L-.

-a .-2 AMERICAN ENVIRONMENTAL TESTING INC.

565 So. Birch Dr. Spanish Fork Ut. 84660 x Pled or Jeb Ijescriplion:

&'G+ _-,

Test.: 4 7% :A. r$)y Location; /

AMERICAN ENVIRONMENTAL TESTING INC.

c I

!

I I 1: I. I

j

.., . .... :. :

I: i I

565 So. Birch Dr. Spanish Fork U t . 84660 n

Plrinl GI- Jot Lescription:

Test:

Dalr:

Obrrsrrvalion Timr: 6 -8-L.. kffiliation: &

, DistcmcrP 23-0

I - Height of Point: @9 73

Wind Speed: c8 1 4 4

Localion: LYh 2

Crrtiiication Date:

Control Device:

Observer:

Direction: si5

Arnbiant Temperature:, 277

Wind Direction: h, Plume Color:

Olher Info:

AMERICAN ENVIRONMENTAL TESTING INC. 565 So. Birch Dr. Spunish Fork Ul. 84660

/-

' f ' I

, ,

Pltint GI- Jot firscriplion: .

Control Drvice: . '-

Oberswvation Tinir: a& ' Certification hk

- I Height of Point: @'73 AmbienL Temperature: 73. '

m M Wind Speed: ~ # / c L A Wind Direction: S'd,

& I ! * Plume Color: Sky Condition: q'&=&-&-* Other Info: w n _-

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AMERICAN ENVIRONMENTAL TESTING INC. 565 So. Birch Dr. Spunish Fork Ut. 64660

Plsrnl GI- Jot Iiescripticn:

Cm-~Lrol Device:

Oberservaiion Time: -&&@. Certification h i e :

, Observer:

. I : Height ~l Poini: 63 7 5

Wind Spzd:.c :I/? Wind Direction:

Arnbirni Temperature: -,

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AMERICAN ENVIRONMENTAL TESTING INC. 565 So. Birch Or. Spanish Fork Ut. 84660 1

Plant 0)- Jot. liescription: I- r

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Date: / 2 4 - 5 b Control &vice: I

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/ ~im-srrvation T ~ S : &a& Certification Date:

ObSWVQr: J

d-JLd r Distunce: m2-0 Direction:

Y/ O F , I

Height of Point: J@ I 7 5 Ambient Temperature:

Wind SpCrd: & wlrrd Direction: w d Sky Condition: Plume Color:

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AMERICAN ENY IRONMENTAL TESTING INC. 565 So. Birch Or. Spanish Fork Ut. 84660

P l e n l or Job firscription:

Cljntrol D+vice:

Distance: 64 gfll Direciion: s-J-f- /

Height of Point: Ambirnl Temperature: Y7 7 Wind Direction: JUJ Wind Speed: GW . 2 2- 7r 14

Sky Condition:

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AMERICAN ENVIRONMENTAL TESTING INC. 565 So. Birch Dr. Spanish Fork Ut. 84660

PlunC or Jot Description:

Dat+: Control &vice:

Oberscrvation Time:

Affiliation:

Distmce: Direction: I

Height of Point: ' 0 3 AmbienL Temperature: 45°F

Sky Condition: Plume Color:

APPENDIX 0

0

Date /a2-90 Amb. Temp. O F Y3

Bar. rem. ("Hg) ,2d . .Ys I Static Press.("H2Q) + 6. U r ,

Pitot Tube (Cp) I: B = C..YU,FY Stack Dlmeneioae ..78: 0 x i z 3 3 ' 8 y z

1 I

Velocity Traverse head

number i n . $0 O F

point b P 1, Stack temp.,

I 8.07 // 9

. Cvclonic flow determinntion

~p~ at 0' which yields reference a n u l l ~p

Angle (6 )

- . o I 7

a Average of CC must be (10 degrees to be acceptable

Run No.

Operator &g4-pjq - 0

Amb. Temp. 'P 7 F f 2 4 3 1 L

Bar. Press. ("Hg) 36.qb Static Preaa.("H2Q) t o . 0 3

Pitot Tube (Cp) 6 fi = 0.3Y.5V Stack Dinemione ?go '20 - 3

& , J

Velocity , Cvclonic flow determination

point ( A P 1, Stack temp., ~p~ at 0' which yields Traverse head h g l e (CC )

number i n . i i , ~ "F reference a n u l l ~p I

I

Average of= must be < 10 degrees to be acceptable a

I

.

i I

I I t

which yields

Velocity Traverse head poinc

number (.P.), Stack temp.,

in. i i , ~ 'F

i

1

I !.. I 1 .

MIXHOD 2 CYCLONIC FLOW DETERMINATION DATA FO \

"

Run No.

Operator -

Amb. Temp. O F

, 0

Bar. Press. ("Hg) 26-93 Static Press.("H2Q) 0. IV

Stack Dimensions /97 ' I= ,ff&, , ' Pitot Tube (Cp)

i 1

O % + f q - 6 b

I I 1

I '. I I I

I I I I I I I

Average o f = must be < 10 dcgress to be acceptable a

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7-

STATE OF UTAH OIVlS1OW OF PWVIAOWYEWTAL HDILTN

".ma*"," APR 1 9 1990

I STATE OC UTAH

DIVI8ION OF ENVIROMY~WTAL HULTW

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Montana Department of Health and Environmental Sciences Air Quality Bureau

Wslble Emlsslon Fiald Lhxummlatlon

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SOURCE LAmUTSKRcH

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Montana Department of Health and Environmental Sciences Air Quality Bureau

MONTANA DEPARTMNT OF HEALTH & ENV IRONCIENTAL SCIENCES A I R QUALITY BUREAU

F I E L D DATA REDUCTION PROCRAA AND ISOKINETIC CHECK

suumcE RUN DATE SAMPLE TIME Y TRAVERSE PTS LEAK RATE

VOLUhE CETEREI) UELTA P - I N H20 DELTA H - I N H20 AVC. MTR.TEMP - F AVI;. STK TEMP - F ABS. STK PRESS - I N HC UAW. PRESS - I N ffi x coz 2.. I 02 I ti2 CP Y - MTR U L FACTOR STACK AREA - SQ FT IMPINGERS - 6MS &?O t.l us TEST TIHE - MIN. NUZZLE DIM. - INCHES EIU - LB/LB HOLE DELTA H B

VMSTD '6'2.624 DSCF

vs AVC. ISO.

LB/LB HOLE

[ K 1 FACTOR 59. 0'76

SOURCE PROCESS RATE ZI. 0 7aus/hf SOURCE AIR POLLUTION CONTROL PARAMETERS

h, AT; ........................... SOURCE FUEL TYPE 645 IN H20

H20 FLOWRATE PRESSURE DROP

SOURCE FUEL FIRING RATE /778 MHS/W

DATA CHECKED BY:

DATE: , '

Montana Department of Health and Environmental St Air Quality Bureau

:iences

COMMENTS (Descrlb

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S I I I i I I I s I I I I I 1 I s I I I I , . I LBS. CAUS71C: BOILER NALCO 796 I LSS. U U S ; l Z . BOILEZ - 7 . v us. ~ , ~ ~ - c T I I c . a u . s 12%

NALL- E 6 , , N A G 3 7 5 6 . IC . -^

AP42 chapter 9 reference - US EPA · The file name refers to the reference number, the A P42...

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Transcript of AP42 chapter 9 reference - US EPA · The file name refers to the reference number, the A P42...