Post on 05-Jan-2019
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
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-
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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
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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.
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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 -
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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
Spanish Fork, Utah 84660 565 So. Birch Drive 80 1-266-7 1 1 1
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
Nozzle Dia. Stack Temp
Velocity head o f stack gas Pitot Tube Coefficient Static Pres
Absolute Pres Area stack
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
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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
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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
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
Volumetrlc flow rate d ry basis
standard conditions lsokinetic variation
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
Spanish Fork, Utah 84660 565 So. Birch Drive 80 1-266-7 1 1 1
FIELD AND LABORATORY DATA TABLE VI I
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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
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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
Nozzle Dia. Stack Temp
Velocity head of stack gas Pitot Tube Coafficient Static Pres
Absolute Pres Area stack
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
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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
Conditions Volume water
vapor collected B standard conditions
Proportion by volume of water
vapor in gas stream ddimensionless Dry molecular
weight Wet molecular
weight Stack gas velocity
Volumetric flow rate d ry basis
standard conditions lsokinetic variation
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
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APPENDIX A (caliibration Data)
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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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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.
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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
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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 -
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.. , . ' .
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
:/
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. . , . ..,. . .. . .
. . .
. ..
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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
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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. . . .... ., ~ , .
PARTICULATE COLLECTED
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
PARTICULATE COLLECTED
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
FRONT-HALF ANALYSIS (Nozzle,Probe,Filter,and Hot Box Glassware)
(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 )
BACK-HALF ANALYSIS (Impingers,and Connccting Glassware)
(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
PARTICULATE COLLECTED
FRONT-HALF ANALYSIS (Nozzle,Probe,Filter,and Hot Box Glassware)
(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 )
BACK-HALF ANALYSIS (Impingers,and Connccting Glassware)
(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
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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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- 0 - -" A . ' # '
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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
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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 . -^