United States Industrial Environmental Research EPA-600/7-78-099b
Environmental Protection Laboratory December 1978
Agency Research Triangle Park NC 27711
Emission Reduction on
Two Industrial Boilers
with Major Combustion
Modifications
(Data Supplement)
Interagency
Energy/Environment
R&D Program Report
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the INTERAGENCY ENERGY-ENVIRONMENT
RESEARCH AND DEVELOPMENT series. Reports in this series result from the
effort funded under the 17-agency Federal Energy/Environment Research and
Development Program. These studies relate to EPA's mission to protect the public
health and welfare from adverse effects of pollutants associated with energy sys-
tems. The goal of the Program is to assure the rapid development of domestic
energy supplies in an environmentally-compatible manner by providing the nec-
essary environmental data and control technology. Investigations include analy-
ses of the transport of energy-related pollutants and their health and ecological
effects; assessments of, and development of, control technologies for energy
systems; and integrated assessments of a wide-range of energy-related environ-
mental issues.
EPA REVIEW NOTICE
This report has been reviewed by the participating Federal Agencies, and approved
for publication. Approval does not signify that the contents necessarily reflect
the views and policies of the Government, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/7-78-099b
December 1978
Emission Reduction on Two
Industrial Boilers with Major
Combustion Modifications
(Data Supplement)
by
K.T. Fisher, J.J. Buening, W.A. Carter,
and S.C. Hunter
KVB, Inc.
17332 Irvine Boulevard
Tustin, California 92680
Contract No. 68-02-2144
Program Element No. EHE624A
EPA Project Officer: Robert E. Hall
Industrial Environmental Research Laboratory
Office of Energy, Minerals, and Industry
Research Triangle Park, NC 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, DC 20460
-------
Limitations On Application Of Data Reported
The data cited in this report are test results of measured pollutant
emissions from two industrial boilers. These emission levels are not suitable
for use in estimating mean emissions from industrial boilers as a class nor
are they suitable in compiling areawide emission inventories. They are not
suitable for predicting emissions from any one boiler or as regulatory limits or
emission standards. Use of emissions as emission standards automatically
would place a large proportion of the industrial boiler population in noncompliance.
-------
CONTENTS
Page
FOREWORD
INSTRUMENTATION
GLOSSARY _ viii
CONVERSION FACTORS ix
SITE LOCATION NUMBER 19
Industrial Boiler Design Data 1
Mobile Laboratory Data 2
Unit Operating Data 56
Fuel Analyses 108
Particulate and Impactor Data 111
Plume Opacity Data 177
Velocity Traverse Data 194
SO Data Sheets 206
x
SASS Test Data 246
SITE LOCATION NUMBER 38
Industrial Boiler Design Data 291
Mobile Laboratory Data 292
Control Room Data 312
Fuel Analyses 332
Particulates and Impactor Data 335
Velocity Traverse Data 372
Staged Combustion Air Flow Data 397
111
-------
FOREWORD
The purpose of this Data Supplement Volume is to document data in
greater detail than was practical in the final report for this contract. It
is intended to provide the necessary details to other researchers who are
interested in performing their own analysis.
Readers are referred to the contract final report for information as
to objectives, selection of units, measurement procedures, interpretations
and conclusions.1
All data presented for gaseous emission concentrations of NO, NO ,
X
CO, HC, SO_, and SO_ are expressed in parts per million by volume (ppm) on
a dry basis corrected to 3 percent O by volume (dry) in the flue gas.
The data are arranged in this volume by Location Number for Locations
19 and 38. A location is defined as one company or plant in which one or
more units were tested. Each boiler tested at a location is identified by
a unit number. The contract final report refers to the test number when data
are discussed. The test number is of the form XX/YY-ZZ, where XX = location
number, YY = unit number, and ZZ = test number on that unit. For sites where
only one unit was tested the /YY unit number is deleted.
JCarter, W. A., et al., "Emissions Reduction on Two Industrial Boilers with
Major Combustion Modifications," PB 283 109, EPA 600/7-78-099a, June 1978.
IV
-------
For each unit tested, the data supplement contains the following
information:
1. Industrial Boiler Design Data
Design data tabulations include: unit description, installation
date, steam conditions, furnace characteristics, burner type and
spacing, fuels burned, and design temperatures for fuel, air and
stack gas.
2. Mobile Laboratory Data (Gaseous Emissions)
Emission measurements tabulated for each test include test type
test load, combustion conditions (excess 02, CO2), gaseous emissions
(NO , NO, CO, HC,.SO , and SO0 all at the measured O_ and at 3% O , dry)
x x £ £ £
3. Unit Operating Data
Control room data tabulated include steam pressure and temperature,
combustion air and stack temperatures, fuel flow, fuel temperature
and pressure, furnace pressure, and burner air register setting.
4. Fuel Analysis
Laboratory reports of fuel analysis are included.
5. EPA Method 5 Particulates and Cascade Impactor Data
Data sheets for EPA Method 5 include control console data,
particulate calculation sheet, and particulate emission calcula-
tions . Data sheets for cascade impactors include control console
data, cascade impaetor weight data, calculated aerodynamic particle
size for each stage, and particulate emission calculations.
The impaetor used was an Anderson 2000 Model III with the follow-
ing stage dimensions:
Jet No. Jet Diameter, cm
1 0.1638
2 0.1253
3 0.0948
4 0.0759
5 0.0567
6 0.0359
7 0.0261
8 0.0251
-------
6. Plume Opacity Observation Record
Opacity observations by EPA Method 9 are recorded.
7. Velocity Traverse Data
Stack traverse data for 02, velocity and temperature as a
function of position in the stack are included.
8. SOX Data Sheets
SOV calculation data for each of three runs with the wet chemistry
A
train are included.
9. SASS Test Data (Location 19 only)
Data sheets include sampling conditions, control console data,
particulate emission calculations, sample recovery logs, and
sample concentration results by atomic absorption, spark source
mass spectrometry, gas chromatography, and gas chromatograph-
mass spectrograph.
Dash marks entered on the data, forms indicate that data were not
available.
vi
-------
INSTRUMENTATION
The emission measurements were made with instrumentation contained in
a 2.5 by 9 meter (8 by 30 ft) laboratory trailer. The gaseous emission measure-
ments were made with analyzers located in the measurement console in the trailer.
The particulate concentration, particulate size, sulfur oxides, and trace species
concentration measurements were made with instrumentation prepared in the wet
chemistry area of the laboratory and taken to the sample port. The weighing
and titration were done in or near the laboratory.
The emission measurement instrumentation used for the program was that
shown in Table 1. The operation of the instrumentation is discussed in detail
in the contract final report.
TABLE 1. EMISSION MEASUREMENT INSTRUMENTATION
Emission
Symbol
Measurement Method
Equipment Mfgr & Model
Nitric oxide
Oxides of nitrogen
Carbon monoxide
Carbon dioxide
Oxygen
Hydrocarbons
Sulfur dioxide
Sulfur dioxide
and trioxide
Total particulate
matter
Particulate size
Smoke spot
Opacity
Trace species
and organics
NO
NO
x
CO
co2
°2
HC
so2
so ,
so3
PM
K
Chemiluminescent*
Chemiluminescent*
Spectrometer*
Spe c tr ome te r *
Polarographic *
Flame ionization*
Photometric*
Absorption/titration
EPA Standard Method 5
Cascade impactor
Reflection
EPA Standard Method 9
EPA SASS Train
Thermo Electron, 10A
Thermo Electron, 10A
Beckman, 864
Beckman, 865
Teledyne, 326A
Beckman, 402
Dupont, 400
KVB Equipment Co.
Joy Mfg. Co.
Anderson 2000, Mark III
Research Appliance Co.
Acurex/Aerotherm SASS
*Precision, + 1% of Full Scale
VII
-------
GLOSSARY OF SYMBOLS USED ON DATA FORMS
Burner Type
Air
Ring
Spud
Steam
Air Atomizer
Natural Gas Ring
Natural Gas Gun
Steam Atomizer
Test Fuel
NG
#2
#6
Natural Gas
No. 2 Grade Fuel Oil
No. 6 Grade Fuel Oil
Test Type
Air Reg
Atom Press
BOOS
Base
BrTune
Damper
HiAir
HiLoad
LowAir
LowLoad
LowNOx
NrmlAir
OFA
SCA
Steamlnjec
VPH
Viscosity
FGR
SASS
Air Register Adjustment
Burner Atomizing Pressure Adjustment
Burners Out Of Service
Baseline
Boiler Tuneup
Air Damper Adjustment
High Excess Air
High Load
Low Excess Air
Low Load
Low NO Condition
X
Normal Excess Air
Overfire Air
Staged Combustion Air
Steam Injection
Variable Combustion Air Temperature
Fuel Oil Viscosity
Flue Gas Recirculation
Source Assessment Sampling System
Vlll
-------
CONVERSION FACTORS
SI Units to Metric or English Units
To Obtain ppm
*These conversions depend on fuel composition.
The values given are for typical fuels.
Multiply*
Concentration
To Obtain
g/Mcal
106 Btu
Btu
lb/106 Btu
ft
in.
ft2
ft3
Ib
Fahrenheit
Fahrenheit
psig
psia
iwg (39.2 °F)
g
10 Btu/hr
GJ/hr
From
ng/J
GJ
gm cal
ng/J
m
cm
2
m
m
kg
Celsius
Kelvin
Pa
Pa
Pa
MW
MW
Multiply By
0.004186
0.948
3.9685xlO~3
0.00233
3.281
0.3937
10.764
35.314
2.205
t_ = 9/5 (t ) + 32
F c
t_ = l.St.. - 460
F K .
-4
P . = (P ) (1.450x10 )-14.7
psig pa
P . = (P ) (1.450x10 )
psia pa _
P. = (P ) (4.014x10 )
iwg pa
3.413
3.60
at 3% 0_ of
£.
Natural Gas Fuel
CO
HC
NO or NO
X
SO_ or SO
2 x
Oil Fuel
CO
HC
NO or NO
X
SO_ or SO
2 x
Coal Fuel
CO
HC
NO or NO
x
SO,, or SO
2 x
in ng/J by
3.23
5.65
1.96
1.41
2.93
5.13
1.78
1.28
2.69
4.69
1.64
1.18
-------
English and Metric Units to SI Units
Multiply*
To Obtain
ng/J
ng/J
GJ
m
cm
2
m
3
m
kg
Celsius
Kelvin
Pa
Pa
Pa
MW
MW
From
lb/106 Btu
g/Mcal
106 Btu
ft
in.
2
ft
3
ft
Ib
Fahrenheit
Fahrenheit
psig
psia
iwg (39.2 °F)
c.
10 Btu/hr
GJ/hr
Multiply By
430
239
1.055
0.3048
2.54
0.0929
0.02832
0.4536
t = 5/9 (tp - 32)
t = 5/9 (t_ - 32) + 273
K F
P = (P . + 14.7) (6.895x10 )
pa psig
P = (P . ) (6.895x10 )
pa psia
P = (P. ) (249.1)
jpci iwy
0.293
0.278
To Obtain C
ng/J of in
Natural Gas Fuel
CO
HC
NO or NO (as NO )
x 2
SO_ or SO
2 x
Oil Fuel
CO
HC
NO or NO (as NO)
x 2
SO_ or SO
2 x
Coal Fuel
CO
HC
NO or NO (as NO )
X £,
SO or SO
£i X
^oncentrat
ppm @ 3% (
0.310
0.177
0.510
0.709
0.341
0.195
0.561
0.780
0.372
0.213
0.611
0.850
*These conversions depend on fuel composition.
The values given are for typical fuels.
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Unit No.
Unit Description
Installation Date
Steam Output (Ib/hr x 103)
Design Pressure, psig
Operating Pressure, psig
Final Steam Temp. , °F
Feedwater Temp. , °F
Furnace Type
Furnace Size L-W-H (ft)
Total Heating Surface, ft
2
Radiant Heating Surface, ft
2
Convection Heating Surface, ft
Furnace Volume, ft
Burner Description
Test Fuel
Primary Air Temp. , °F
Stack Temp. , °F
1370
t7>f
Z.STO
/S0
sjrv*4r£0
2-J-0
Mr££TV8£
-------
Test No. f
Unit No.
Dnit Type
1 ~ 3 Date \ t
Fuel &
PS 1-3.
MOBILE LABORATORY DATA Test No.
/V/77 Location /f Engr. G^OTfE
:-2. Capacity \7S~OO /6.S//J/-
Burner Type W0 / J7.J sAB£&
11-1 11-2* /7-J /f-V /f-5"
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
n.K'SQLftA (APftox. fto/l S°a.}
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Data Sheet 6002-2
2
-------
Test No.
Unit No.
Unit Type
/ Date
Fuel &
D5 7-2
MOBILE LABORATORY DATA
Location / /
>2 Capacity //^ £00 ^
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Test No.
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1. Test No.
2. Date
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8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NOj (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. ("F/«fc)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. $5 £ IN f(J£t-
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Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date I "fO-77 Location /f
Test No.
Engr.
Fuel
Capacity_
Unit Type
OS 1-2-
Bumer Type FAB*A
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. N02_ (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
.4. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atraos. Temp. (0F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ^ 5 //V fU£L
23.
24.
25.
26.
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Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date / "//•" 7 "7 Location /
Fuel "2* Capacity ''
Test No.
Engr
Unit Type P$ f - 2.
Burner Type
-If /?-//
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. N02 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppjn) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. %5 /A/ /?tSft~
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24.
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Data Sheet 6002-2
-------
Test No.
Unit No.
Date / •'
Fuel -^ .J~
Unit Type f v " -
MOBILE LABORATORY DATA
Location
Capacity •'
Test No.
Enar.
Burner Type fA P£&.
-zi
14-23 /1-3-j
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (CF/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % ^ //J FUEL
23.
24.
25.
26.
27.
28.
29.
30.
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fo
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3
60
I
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0
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61
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0
3o.y*6
75"
4/13
.
///Z//7
0120
tzy
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date J ''', I'-, Location
Test Mo.
Engr. Ml £ fit Z A
Fuel
Capacity_
Unit Type
P'-'f
Burner Type Wff l/j.S"
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnrjs. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % 5 W FUFL
23.
24.
25.
26.
27.
28.
29.
30.
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115-00
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to 7
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73
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3
70
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3.03
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73- 73-
O
87 ?7
/o /o
3 3
70 JO
y
fo
30. 2. 1
SS
>(*l
*Correction to 3% 0- should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA Test No.
Test No.
Unit No.
Unit Type
Date I//2/77
Fuel •-rr' 2—
£53. -2-
Location / 7 Engr. pft/£A/£-A
Capacity /7S"OO
tiJ A // fJ £~ JCJ1 ££* 4
Burner Type '*' O ff ~> j rn*}*- AL
ft,3f /?-3z fq.jj /?-_?y tf-jf
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
L4. Carbon Monoxide (ppm) uncor/cor
if
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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3.60
63
63
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53
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60
63
63
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60
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-------
Test No._
Unit No.
Date
Fuel
MOBILE LABORATORY DATA
Location //
Capacity
Test No.
Engr
I
Unit Type
Burner Type V/8
f
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date Location / 7
Fuel " o Capacity
Test No.
Dnit Type P'5 ^ "
Bumer Type ft/I ///• 5"
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atrros. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ^ S itf F
22-f
/?
S
270
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236
236
0
25S
2f
s
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r
7
3o.11
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1/13/77
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173
173
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160
160
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O
(U
2.32
f
336
7
7
36.4
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location //
Test No.
Engr.
Fuel
Capaci ty / 75 &O
Unit Type
Burner Type
//i-
//7WX-
/f-//
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ^ s /M FL/£L.
23.
24.
25.
26.
27.
28.
29.
30.
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30.0*1
42
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62
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20
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Unit No.
Date
MOBILE LABORATORY DATA
Location /7
Test No.
Engr.
Fuel
Capacity
/
Unit Type_
Burner Type W'B //V.
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/CC)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.7o -S /AJ /=U£L
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27.
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Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location / f
Test No.
Engr
Fuel
Capacity
Dnit Type
Burner Type l*/S
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A tiros. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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/
30, £0
*Correction to 3% 0_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
1 3
-------
Test No.
Unit No.
Date
Fuel •?
^ <2
Unit Type &S^~JL
MOBILE LABORATORY DATA
Location / 7
Capacity
Test No.
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Op (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (CF/°C)
19. Dew Point Temp. (°F/CC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % -T //I/ fV£L
23.
24.
25.
26.
27.
28.
29.
30.
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Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location / 7
Test No.
Engr
Fuel
Capaci ty
Unit Type
PS 1-
Burner Type If/6
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ft, S //t/ fV£L
23.
24.
25.
26.
27.
28.
29.
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Data Sheet 6002-2
1 5
-------
Test No._
Unit No.
Date
Fuel
MOBILE LABORATORY DATA
///$/ 77
Location_
Capacity
Test No.
Engr
I7500
Unit Type
Burner Type V& i/f.S
11-73-
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/ 3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO, (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atltos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % S fAJ fO£t-
23.
24.
25.
26.
27.
28.
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Unit No.
Unit Type
Date ///?///
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MOBILE LABORATORY DATA
/
Location /^
Test No.
Capacity
17.500
Burner Type
J?-7f
11-74 M-77
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
•if
IS. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (CF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % S W FV&L.
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MOBILE LABORATORY DATA
Date I/2O/77 Location
Test No
Engr
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Capacity_
Unit Type
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10.
1. Test No.
2. Date
3. Time
4. Load
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6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atltos. Temp. (°F/°C)
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20. Atinos. Pressure (in. Hg)
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1/10/77
1/5'
/IffOO
2.5
cs-tfTfA,
1- 77
7i M
7/ ££
o 0
& 0 "7 *?
ff-&** r f
£&> V£2
SO /J
- \
S.e
2S~
J-9.&0
/ S~
=^c-
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V*
w
3,
CfM
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77
77
O
$7
tfo
8
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6-
3
*%
£.
*/t
*2. £•.
6/77
~f
roo
j
V& 1JL
/f /£•
/oo jy
7.0
1 7
7- v. tiT
£S~
.//JL
Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
1 8
-------
MOBILE LABORATORY DATA
Test No.
Test
Unit
Unit
Mo.
No.
Type
Date
Fuel
051-2-
1/20/77
Location
Capacity
i
Burner Type
/*
17 &
W8
M-f2 M-*3
f
)0
//*,
f
Engr . /• £ ' Jr A/2 '*
f/30*S
/f-fi /i-tr
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. N02 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 03 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (0F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ^5
23.
24.
25.
26.
27.
28.
29.
30.
?fTb~l
1/20/77
H?*°
2-F
cf*T£A
___$ _£~^l-~f^~— "• ~-
l/2o/77
wee
MSAO
2.5-
c£*IT££.
.I*
21
21
0
3?
21
f
f?
26
26
0
31
21
5-
76
O
2.
7
21.? 6
&5~
0.131
~f \^ **- ^ "
\/3-0/77
/f00
Mf0t
2.-S*
C-fAfT^
• 70
30
JO
0
34
zr
s~
27
2?. ?6
4£~
0./3?
=^^Z^T'
\/*0/77
H30
/isoo
2^
C.£AlTfA.
0.6
3/
31
0
37
#0
y
?$
't
27
27
33
71
y
si
27.JI
a./2
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
1 9
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date / ~~2I~ 7 / Location _ / V
Fuel -& 2-
Test No.
Engr.
Capacity / 7* 5~
Dnit Type
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO, (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
IB. Atraos. Temp. (°F/°C)
19. Dew Point Temp. (0F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
t
1-3-1-17
W2.-7
lf.5- K
2.5'
££*}&#,
2,
7i
72
2L
$2
r
3*.
03
I-2/-7 7
ff35~
jl.S'K
2,5-
C£/JT£A
3..
£2
61
I
70
S
g 1
/^>
/
£1
105-
i
£o
6.
/ol
3
51
S'
30.
03
.-,.:.-. - .
/-J/-77
13*5-
It.fK
Z'S'
ceMTeg.
2,
67
66
\
77
£
65-
61
1
75-
/
7$
3
23
21,15"
£0%,
ir-.
/-Z/-77
/V00
H.&K.
2-r
ceurzA
Z.ff
ft 5-7
ft 57
& 0
SZ 66
61 62.
0 0
20 7&
f.S'
23
2 ?<7S
f^% ^9r
01s s&
l-U-77
W2£>
H-fK
Z'S'
ceAjre/L
Ztf'S'
S7 5"6
S6 SS
I I
£6 6V
1% i7
& o
&° 71
£.5"
Z3
27<1f
£ ^j&7
& ^^ rn
*Correction to 3% C»2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
2 0
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
Pate (~2/ ~ 77 Location
Fuel &2 011 capacity / 7' 5~ <
Test No.
Engr. > >
Onit Type
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% ©2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (CF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
/-JZ/-77
/yjj-
*{t g*-
2.Z
c&tret
"2~, *
6i
62
2
61
tol
0
9O
6.
15
62
£0
2-
67
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0
7X
5-
23
Zf.ff
{0%
I-2/-77
/£00
IH.S-
2-f
eeAJTfA
1.4
£
Z-f
zr.ri
£T5%>
~^£^~.^- -
1-21-77
l5~/3~
/y.f
2-f
CGMT££
/.£
6t 5-f
62 *7
2 1
72 66
3X0\3V?
1 \ H
*0 7f
/••5"
25~
^ ^9 &£f
j^ f~S^
1-21-77
;5j
if
/i'f
2-f
c.£AJT£#
f.jf
62
61
/
•71
foo
H
&
6.
57
S6
/
j£~
3Jf
1
7f
0
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zi.ltf
ss%
1-21-77
J5Hf
IH.f
2-^
G£*IT£K
I.*?
71 6?
6 £>
& 71
7.*
2-f
ZLt.n
&5%
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
2 1
-------
Test No.,
Unit No.
Date
MOBILE LABORATORY DATA
Location , /
Test No.
Engr. /_..
Fuel
Capacity
Dnit Type 05 J ~ 2-
Bumer Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (0F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. To £ /rf PL}£L-
23.
24.
25.
26.
27.
28.
29.
30.
" "V ". :
1/2*
1 77
$25'
/tfeo
2-5
C£MT££
3./0
W3
163
0
1/7
0
II?
$
s~
60
/3
3J$
77
- -
f *
0.
2
3oo
£-
e>
30J£
7
7
#-52.
^,_,^
/ 2V 77
/(3o
/ifao
Z.f
tetJTffi.
3.3
Mi
/f/
0
2/3.
/*>
2.^
g0
.122.
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No.
Vast Ho.
Obit No.
Date
Location
Fuel
Doit Type f> 5 5 /A* f^fi-
23.
24.
25.
26.
27.
28.
29.
30.
5~4
>h
//IS/77
/&£
>0
/1^ao
2.5-
cf/urfA
3.0 y
5T3
5"S
G
£1
6
5
zf
/..
^3
S3
0
//
t
.$""
tt
r
3o
3-9.77
I*
//
J-'S'
eertTF*
2-*,
^» A/
? £/
0
HO
/ff
3
#0
W
31
3i
0
ye
/o
3
?o
5
3/
21.75-
70
,/3#
^-'c/k
//2f/77
1125-
/1$oo
2--5~
Cf A] *rfj&
C fY / F^^
_j ^? ^r
2-5- J-S"
O 4^ ^y g^
0 0
2-7 27
IS- /?
3 3
$?/^ £?J)
O w' O ^^
2.
3f
2~f.75~
-------
Test No.
Unit No
Unit Type
Date
Fuel " -
DS.
*0
2£
26
0
23
^—
16
3
So
3L
34
21.
2*5~
ce*)Te#.
3.20
/f7
/&7
&
/7f
6
y.g£>
/57
/37
/77
£
0
2S"5
3*0
3£
2-1. 6 X
72
, yzf
-l*.*4*.
lte/7?
l3fO
(15&0
2-5'
c-eMTe*
3./1
/57
0
/7i
%
2-
2?o
/..
PI
/76
f/2£/77
13*0
/*f500
2.f
centre*.
3.07
JSt
JSl
0
J73
tf
2.
2ZO
*f.
Iff
151
0
/73
/5
J2.
2?0
?-
3*
2?.S?
72.
.iZ3
!;p/^
1/2S-/77
/y&o
(H5oo
Z 5~
ceAjrf*,
3.11
ISO if/
fS~0 /ft
/7£> ///
32 33-
£~ f
2?5" /£-?
5"- /
3£
2?
-------
MOBILE LABORATORY DATA
Test No.
Test No.,
Date
Unit No.
Fuel
Capacity
Unit Type
Burner Type
l/*f,$~
/1-//Z
/9-//Y
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (CF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % S /rf f(S£ I.
23.
24.
25.
26.
27.
28.
29.
30.
"=^se—
— — s.
/125-/77
W20
lifOO
2..S-
efAJTe*
3.05-
/3l
132.
t>
ISO
6#
5"
2?*-
6.
133.
j32.
0
/so
60
f
2ge
$•
J Q
^? ^f jf ^
72
'ffj
1*.
/YJ
&7
if
itsreo
2.
5~
ceMTe*.
3./0
/3o
130
0
H?
20
,r
2f£
^
>*/
/3/
0
IH1
%e>
f
276
O
36
27,66
72-
rffJ
— a-^_
//2Z/77
/ft
70
IH500
2.
5"
cEitre*.
/•7?r
127
127
0
f/B
/a>
/2
I/I
//
••
'-."7
1/26/77
0f0O
Jffoo
2.5-
CEtlTgft.
3, 1 &
10? 10%
JO? /£>&
0
/2f /24
6 6
0
60 S0
0
2-6
2?>7V
7*
./e>3
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
25
-------
Test No._
Unit No.
Date
Fuel
MOBILE LABORATORY DATA
"' Location /7_
Capaci
Test No._
Engr. .:
Dnit Type I.? f ~
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (0F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. %f ffO FC/EL fxfly s&3.
23.
24.
25.
26.
27.
28.
29.
30.
//Z*//7
/*t
'0
/&
Z-?
CEtiTffi.
3.
$2
22
0
14
3f
J~
go
1
33
$3
0
17
3?
5
ft
i
21.7f
7$~
12. 00
ft/ft*?
2.f
ce*)T£*
3J1
$3
*3
0
17
&y
o
1&
5.
%H
$i
0
If
*i
O
*?/
5"
3^
21,70
2//f/77
WIO
/yf&>
2*5'
C£M7££
J.2
//7 //?
//7 f/f
£> 0
132 13 1
1 1
5~ S-
go */
£>
31
21.97
&>%
Ji7e>
•* — J---4-,
lfti/77
I0JS"
/
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1/5
g
3
W
1
/&>
£>
//*
8
J
1#
0
J1
3& [2.
H7%
.155%
2/U/77
///o
I*/?**
2.?
cetiT**.
£.3
&7 /#7
27 /o7
£> £>
12 //?
6 7
2. 2.5"
70 $4
0
2.0
30-tl
I77*e
Jtjg%
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No.
Unit No.
Unit Type P
MOBILE LABORATORY DATA
Date Location /f
Fuel 2+2 #/ L Capacity /7 ' £"&&
-5 7 " 2- Burner Type /*/^ // V* 5"
Test No.
Engr. dv "*-" 7/V
ffCfl. /?, feVc-cj-j
M*£A
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide JEgin) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppro) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atroos. Pressure (in. Hg)
21. Relative Humidity (%)
•23..%SOLFVR. /AJ ftJfi- FRQF1 30±
23.
24.
25.
26.
27.
28.
29.
30.
CJt
?/*
//J
MS
2,
££M
&>
Zf
tff
&
?£
^
&
7e
6
3L<
30<>
y
ffl~~
f/77
^
$-
f*
2
ICtf
/€>3
£>
If*
7
o
&£
>
9
(/
7
17
^~~
2/X
//$
/?*>
2<
H
-//
~ipy-^.
5~
r/X
75"
/«z
/&z
0
//3
f
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££~
2.
Of
r
z
Z////f7
fjLZg'
Mff&o
2,£~
Cf/tTf/t
5^75-1
ff7 /03
~£7^o3
0 0
ff ///
r5T?~
^—^-\
J2.2.
3&^*L
is"
>/f3
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
2 7
-------
Date
MOBILE LABORATORY DATA
Location'•
Test No._
Engr.
5. Process Rate
6. Flue Diam. or Size, ft
^-J
\*5~
2.!T
7. Probe Position
8. Oxygen (%)
2-1
9. NOx (hot) read/3% 02 (ppm)*
gg
2.00
13
10. NO (hot) read/3% 02 (ppm)*
2*3
/37
13
13
11. NO? (hot) read/3% O2 (ppm)*
&
0
12. NO (cold) read/3% O2 (ppm)*
//*
/as
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
331
15. Hydrocarbon (ppm)
uncor/cor
7
16. Sulfur Dioxide (ppm) uncor/cor
7*
I/
330 &f
.730
122
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
-2-2-
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
30-02-
21. Relative Humidity (%)
H5*
is-
io
22.
/A)
,13$
,/SZ
,$78
23.
24.
25.
26.
27.
28.
29.
30.
Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
28
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No._
Engr. ^
Fuel
& ' 6
Capacity
Dnit Type Pff-
Burner Type_Jjt^^,_,1L*L^_
*Correction to 3% O_ should not be perfoirmed if
the value is measured on a wet basis.
Data Sheet 6002-2
29
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No.
Engr. C$
Fuel
Capacity_
Unit Type P5 f ~~ -
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (0F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
~
7£T.
2/S&77
/o*
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fi&o
Z-S'
CftJTfA.
/'.
///
//&
1
?z
J*
J/*
?
/o3
/02
1
f/7
3}
2f
2&
2' 5"
13
30. / 3
75"
*.V1
2-//1/7-7
/0yy
/fS'00
2 -IT
G f^J/fff^
t ^^*yj
.S3~
1-//S/77
3.00
rf5*0
2'3~
tf*l7££.
2.J
jol /oo
/of foo
0 0
/** //*
13-6
&6 8J
&~ /y
JJ0 3/f
/•S~
32.
30.03
*J0
ass
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
30
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No.
Engr.
Fuel
Unit Type
Capacity
Burner
/ 7,
ff-/3f tf'/i0 tf'/il W'Ji2- /ef-/f3
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. <7*f*J:t'A M pV£U(fitoH-*9L
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26.
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Data Sheet 6002-2
3 I
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location / v
Test No.
<,--- - - JTl'
Enar.
Fuel
Capacity / 7,
Unit Type
Burner Type
f/*f'S
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
it
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (eF/0C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22 . % -S J*t £U£L (f/?0Al £&*.)
23.
24.
25.
26.
27.
28.
29.
30.
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Chit No.
Date
MOBILE LABORATORY DATA
Location /7
Test No.
Engr.
r#
Fuel
Capacity
i. •'•J-'•<•> j/ 'J
Onit Type
Burner Type
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
2.5-
2.
7. Probe Position
8. Oxygen (%)
0.90
9. NOx (hot) read/3% 0? (ppm)*
75-
75~
£-0
76
77
10. NO (hot) read/3% 02 (ppm)*
Zl
74
11. NO? (hot) read/3% 02 (ppm)*
&
12. NO (cold) read/3% O2 (ppm)*
77
I/O
91
/eg
97
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
2/2.
S37
15. Hydrocarbon (ppm)
uncor/cor
i
16. Sulfur Dioxide (ppm) uncor/cor
<£>
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
2-5-
2.ST
3-5-
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
2-*?-
2-1.SI
21. Relative Humidity (%)
63
63
£3
22.
23.
24.
25.
26.
27_.
28.
29.
30.
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
33
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location ' I
Test No.
Engr. ^ ••'•
Fuel
£4* Capacity /7JTOO
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atiros. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No._
Engr. '.
Fuel £4S # £ Capacity
Unit Type
Burner Type
f£f - / X" 7 ia "fffi
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A tiros. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.% S /A* /^/£"£ (ifXOfil •& 3-)
23.
24.
25.
26.
27.
28.
29.
30.
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Test No._
Unit No.
Date
Fuel
MOBILE LABORATORY DATA
Location //
Capacity_
Test No.
Engr.
/
* GAS
Unit Type_
Burner Type
/f-//0 11 -Iff tf-163- ft- M '3 /?-/£¥
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
B. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A twos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. To S CALCl/t+TE f%t>H &>*.
23.
24.
25.
26.
27.
28.
29.
30.
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2/23/77
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10
2-1*13
0
Data Sheet 6002-2
3b
-------
Test No.
Unit No.
Unit Type
MOBILE LABORATORY DATA Test No.
Date Location /7 Engr.
Fuel &A ^ Capacity / 71T00
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/"C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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the value is measured on a
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Data Sheet 6002-2
bas
37
-------
Test No.
Unit No.
Unit Type
MOBILE LABORATORY DATA Test No.
Date Location / 7 Enqr . •• ' .'.
Fuel *fr, £ 6/1- Capacity / 7^0^ srlh- STfrf/^
Burner Type
/r-/*7
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen {%)
9. NOx (hot) read/3% Op (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. %f PJOSI J^a.
23.
24.
25.
26.
27.
28.
29.
30.
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Correction to 3% O2 should not be pjr_Fprmed if
the value is measured on a wet b= - v
not t
wet' 1
Data Sheet 6002-2
-------
Test Ho.,
Unit No.
MOBILE LABORATORY DATA
Date -? ~2~77 Location //
Test No
Engr.
Fuel A/, &, Capacity /75~00
Unit Type_
Burner Type
/?-/// 19-172 13-173 1 1-171 tf~/7f
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (CF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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the value is measured on a wet basis.
Data Sheet 6002-2
39
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
~2 ~~ 7 / Location _ / V
Test No.
Engr.
Fuel
Unit Type
Burner Type_
11-17* ff-177
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atncs. Temp. (CF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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Data Sheet 6002-2
4 0
-------
Test NO._
Unit No.
Date_
Fuel
MOBILE LABORATORY DATA
Location / /
Test No
Engr.
Capacity /
Unit Type_
Burner Type
'1-/7X
X7-/77
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (0F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
ii.% 5 SAJ ?U£L ftfoH SO^
23.
24.
25.
26.
27.
28.
29.
30.
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Data Sheet 6002-2
4 1
-------
Test No.
Unit No.
Onit Type
MOBILE LABORATORY DATA Test No.
Date 3~ 3 ~77 Location // Engr. B ^ H
Fuel #.2 &16? Capacity / "75^0& */^/*
Burner Type
J
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% ©2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. *?& S
23.
24.
25.
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the value is measured on a wet basis.
Data Sheet 6002-2
4 2
-------
Test No.
Itoit No.
Unit Type
MOBILE LABORATORY DATA Test No.
Date Location /^ Engr tftjJtf
Fuel tf, &, Capacity 17 5 && ^/J)T
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
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8. Oxygen (%)
9. NOx (hot) read/3% Op (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NOj (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atraos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
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22.% >"
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Data Sheet 6002-2
4 3
-------
Test No.
Unit No.
Date_
Fuel
MOBILE LABORATORY DATA
Location / /
Test No.
Engr. ffU^ff
', Q>, Capacity_
Dnit Type_
Burner Type
/?-,
1. Test No.
2. Date
3 . Time
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5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/'C)
19. Dew Point Temp. (0F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % f
23.
24.
25.
26.
27.
28.
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Data Sheet 6002-2
44
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Test No.
Unit No.
Unit Type
MOBILE LABORATORY DATA Test No.
Date 3/7/77 Location / ff-MI
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20
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Data Sheet 6002-2
45
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date J/f/77 Location / 1
Fuel M £ Capacity /
Test No
Engr.
Unit Type_
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
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12. NO (cold) read/3% O2 (ppm)*
:3. Carbon Dioxide (%)
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*
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16. Sulfur Dioxide (ppm) uncor/cor
.7. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
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Data Sheet 6002-2
46
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Test No.
Unit No.
MOBII
Date
Fuel X/, £„
£. LABORATORY DATA Test No.
_ Location / *f Engr. &&#
Capacity I75~&£> ^/Ar
Unit Type Burner Type
9-
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2. Date
3. Time
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7. Probe Position
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9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppro) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
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Data Sheet 6002-2
4 7
-------
MOBILE LABORATORY DATA
Vest Mo.J9-/-5/te.S Date 3-/Q-77 Location
I •; NO.
Test No.
Engr.
Fuel #& Q.l Capacity /^S'OO
Unit Type_
Burner Type_
1. Test No.
2. Date
3, Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) -
9. NOx (hot) read/3% Oj (ppm)
10. NO (hot) read/3% 02 (ppm)
11. NOp (hot) read/3% 02 (ppm)
12. NO (cold) read/3% O2 (ppm)
13. Carbon Dioxide (%)
Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (1>F/0C)
20. Atmos. Pressure (in. Hg)
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Data Sheet 6002-2
48
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I rest No.
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MOBILE LABORATORY DATA
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Test No.
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Fuel &£ O-/ Capacity /? <~OO
Unit Type
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9. NOx (hot) read/3% O2 (ppm)
10. NO (hot) read/3% O2 (ppm)
11. NO? (hot) read/3% 02 (ppm)
12. NO (cold) read/3% O2 (ppm)
13. Carbon Dioxide (%)
Carbon Monoxide (ppm) uncor/cor
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
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20. Atmos. Pressure (in. Hg)
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16. Sulfur Dioxide (ppm) uncor/cor
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IB. Atmos. Temp. (°F/"C)
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22. so S in Fi/eS
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Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No./?-/ 51.SS Date 3/77/77 location
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Test No.
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Fuel #£ O,'l Capacity 17 5 QQ
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9. NOx (hot) read/3% 03 (ppm)
10. NO (hot) read/3% O2 (ppm)
11. KOj (hot) read/3% O2 (ppm)
12. NO (cold) read/3% 02 (ppm)
13. Carbon Dioxide (%)
Carbon Monoxide (ppm) uncor/cor
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (eF/°C)
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Data Sheet 6002-2
5 1
-------
MOBILE LABORATORY DATA
Test No. /?-3~54£-S Date 3 A.//77 Location_
No. '
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Test No.
Engr.
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2. Date
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9. NOx (hot) read/3% O2 (ppm)
10. NO (hot) read/3% 02 (ppm)
11. NO? (hot) read/3% O2 (ppm)
12. NO (cold) read/3% O2 (ppm)
13. Carbon Dioxide (%)
Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. SmoXe Spot (Bacharach)
18. Atmos. Temp. ("F/°C)
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20. Atmos. Pressure (in. Hg)
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22. °)t £ /n r^f]
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16. Sulfur Dioxide (ppm) uncor/cor
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-------
Test No.
IT *«: No. /
MOBILE LABORATORY DATA
Date 3 - Z 3 - 77 Location
/
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13. Carbon Dioxide (%)
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54
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Tent No._
Ur -' - No.
MOBILE.LABORATORY DATA
Date 3-23-77 Location
Test No.
Engr.
Fuel #6 O,'/ Capacity QTOO
Unit Type_
Burner Type_
'
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) -
9. NOx (hot) read/3% ©2 (ppm)
10. NO (hot) read/3% 02 (ppm)
11. NO? (hot) read/3% O2 (ppm)
12. NO (cold) read/3% 02 (ppm)
13. Carbon Dioxide (%)
? Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. SmoXe Spot (Bacharach)
18. Atmos. Temo. (CF/°C)
19. Dew Point Temp. (BF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. % S ,„ fuel
23.
24.
25.
26.
27.
28.
29.
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Test No.
Fuel
UNIT OPERATING DATA
Date 74*1- 7 7 Location_19
Atom.Type X//C Capacity
Engr.
Test Comments iff 7', P
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/f'
1. Test Number
2. Date
3. Time
4. Load //ir
5 Test Purpose
6 Excess 02 Condition
7 Cont. Room 02 (%)
8. Pres.Furn/Windboxliwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR("F)
15. Stack Temp (°F)
16. Fuel Flow (£FM-er GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct ( °F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27 Vortex SA Fan Blades
29 . * FGR
30. Total Oil Burned *2/#6
31. Total Gas Burned
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UNIT OPERATING DATA
Test No.
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Date ^ MH
Atom. Type
77 Location 19 Engr. 5"
jt/X Capacity / 7 *ff1-.
1. Test Number
2. Date
3. Time
4. Load
^^ Test Purpose
6. Excess 02 Condition
•}, Cont. Room Oj (%)
8. Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @FDFan/CR(°F)
i5. Stack Temp (°F)
16. Fuel Flow (CFM Of GPM)
17. Fuel Pres/Temp(psi/cF)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
v f. PPI » ^* ^ -^ ^>
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfin)
29. * FGR
30. Total Oil Burned *2/#6
31. Total Gas Burned
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57
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Test No.
Fuel
Date
BNIT OPERATING DATA
location 19
Engr.
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_Capacity
Test Comments
/f-AZ /?-/-?
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2 . Date
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9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
L3. Air FD Fan Amps
14. Air Temp @ FDFan/CR(°F)
15. Stack Temp (°F)
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.9. Primary Reg. Setting
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22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct ("F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
27 Vortex SA Fan Blades
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29. * FGR
30. Total Oil Burned #2/#6
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Test No.
Fuel
Date
UNIT OPERATING DATA
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59
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Test No.
Fuel & 2-
Date
UNIT OPERATING DATA
Location
Enar. 6.
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Capacity 17, £00
Test Comments
2-
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2. Date
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5 Test Purpose
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12. F. Water P/T (psig/°F)
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15. Stack Temp ("F)
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17. Fuel Pres/Temp(psi/°F)
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19. Primary Reg. Setting
20. FGR Reg. Setting
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27 Vortex SA Fan •£j/a J9s
28. SA Depth/Flow (ft/cfm)
29. * FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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DHIT OPERATING DATA
Location 19
Engr.
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4J& Capacity 17,
Test Comments
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UNIT OPERATING DATA
Location 19
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Test Comments
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2. Date
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5 Test Purpose
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7 Cont. Room 02 (%)
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24. Pstat FGR Duct (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Elades'j
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
31. TotU Gas Burned
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UNIT OPERATING DATA
Test No. Date
Fuel59^ <0C *V 01 i- A torn. Type
Location 19
Engr.
_ Capacity
Test Comments
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2. Date
3. Time
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f,f Test Purpose
6. Excess 02 Condition
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11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/CR (°F)
15. Stack Temp (CF)
16. Fuel Flow (€F*tor GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig>-
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26 Vortex FD Fan -Bi4d«e-
27. Vortex SA Fan Rl*dee''jr
28. SA Depth/Flow (ft/cfm)
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31. Total Gas Burned
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Date
UNIT OPERATING DATA
Location19
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3"
64
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UNIT OPERATING DATA
Test No.
Fuel
Date
Location 19
Engr.
Atom.Type
Capacity
Test Comments
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1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room Oj (%)
8. Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig!
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR(0F)
IS. Stack Temp (°F)
16. Fuel Flow CCPM-or GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
FACE T° HAHfLE.
20. FGR Reg. Setting, m.
2i. AP Pitot FGR Duct(iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct ("F)
24. Pstat FGR Duct (paig)
25. Pstat S.A. Fan (psig)
26. Vortex Fb Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
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Test Comments
UNIT OPERATING DATA
Date Location 19 Ensr. frrr/-/L
Atom. Type ^// Capacity / 7. ^ t-f/Hf>
77
1 . Test Number
2 . Date
3. Time
4. Load
5 Test Purpose
6 Excess 02 Condition
7 Cont. Room Oj (%)
8 Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR(°F)
15. Stack Temp (°F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2\, AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct(iwg)
22. Temp. FGR Duct (eF)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex Fb Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. » FGR
30. Total Oil Burned #2/t6
31. Total Gas Burned
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Data Sheet 6003-16
66
-------
Test No.
Date
UNIT OPERATING DATA
Location 19
Engr.
Fuel J*2-
Atom. Type
Capacity / 7, fffff
Test Comments /Pf „ T £>AJ f (7, /g.
T flVCTtSJT£5
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess Oj Condition
7. Cont. Room C>2 (%)
8. Pres.Furn/Windboxtiwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/"F)
13. Air FD Fan Amps
14. Air Temp @ FDFan/CR(°F)
15. Stack Temp (CF)
16. Fuel Flow (CPM-oc GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22 AP Orif. FGR Duct(iwg)
23 Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. -Fan (pci»)
26 Vortex Fb Fan Blades
27 Vortex SA Fan BladotT
28. SA Depth/Flow (ft/cfm)
29. % PGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No.
Date
UNIT OPERATING DATA
Location 19
Enqr.
Fuel ?t 2-
AIR (LO*-fXtfS') Capacity
Test Comments
1. Test Number
4. Load
5 Test Purpose
6 Excess C/2 Condition
7 Cont. Room 02 (*)
8 Pres.Furn/Windbox(iwg
9. Uptake (iwg)
10. Final Stm Press (psig
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR(°F)
15. Stack Temp (°F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct(iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct (CF)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blaflr"!
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No
Fuel
Date
Location 19
Engr.
A torn. Type
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Test Comments
1. Test Number
2. Date
3. Time
4. Load
g. Excess 02 Condition
7. Cont. Room Oj (%)
8. Pres.Furn/WindboxCiwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @FDFan/CR(°F)
15. Stack Temp ("F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp (psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22 AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No.
Date
Fuel -"Y
A torn. Type //X?
UNIT OPERATING DATA
Location19
Capacity /7
Engr.
1. Test Number
3. Time
4. Load
5 Test Purpose
6 Excess 02 Condition
7 Cont. Room 02 (*)
8. Pres.Furn/windi>ox(iwg;
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR (°F)
15. Stack Temp (°F)
16. Fuel Flow (WM-ar GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct(iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct (*F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
26. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No.
Date
DNIT OPERATING DATA
. Location 19
Engr.
Fuel 3? 3- 0IL.
Atom.Type
_Capacity /'7 $' £> 0
Test Comments
11-
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (%)
8. Pres.Fum/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/'F)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/CR (°F)
15. Stack Temp (°F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22 AP Orif. FGR Duct (iwg)
23 Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26 Vortex FD Fan Blades
27 Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned t2/#6
31. Total Gas Burned
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Test No.
Fuel ^ 2-
Date
UNIT OPERATING DATA
Location 19
Atorn.Type
Capacity > 7,
Engr.
Test comments
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11-
1. Test Number
2. Date
3. Tine
4. Load
5 Test Purpose
6 Excess 02 Condition
7 Cont. Room 02 (*)
8 Pres.Furn/Windbox (iwg
9. Uptake (iwg)
10. Final Stm Press (psig
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/SR < ° F )
15. Stack Temp (°F>
16. Fuel Flow (CFH«« GPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan {psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. » FGR
30. Total Oil Burned «2/#6
31. Total Gas Burned
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UNIT OPERATING DATA
Test No.
Fuel
Date
Location 19
Engr.
Atom.Type
Capacity / 7,
Test Comments
If- Z7
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1. Test Number
2. Date
3. Time
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5. Test Purpose
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7. Cent. Room 02 (%)
8. Pres.Fum/Windboxiiwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/CR (CF)
15. Stack Temp («F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp (psi/°F)
IB. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22 AP Orif . FGR Duct(iwg)
23 Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26 Vortex FD Fan Blades
27 Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. » FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No.
Fuel & 2- 0f I
Date
ONIT OPERATING DATA
Location 19
Engr.
Atom.Type
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Test Comments
/f-
1. Test Number
2 . Date
3. Time
4. Load
5 Test Purpose
6 Excess 02 Condition
7 Cent. Room Oj (*)
g. Pres.Furn/Windlaox (iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FDFan/CR(°F)
15. Stack Temp (CF)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct(iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duet (»F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
31. Total Gas Burned
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Test No.
Fuel •
Date
DNIT OPERATING DATA
Location 19
Engr.
*£ GIL A torn. Type
_Capacity >7
Test Comments
/?-'
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (*)
8. Pres.Furn/Windbox (iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @ FD Fan/CR(°F)
15. Stack Temp (°F)
16. Fuel Flow (CFM-e* GPM)
17. Fuel Pres/Temp(psi/cF)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
21 AP Pitot FGR Duct (iwg)
22 AP Orif . FGR Duct(iwg)
23 Temp. FGR Duct (°F)
24. Ps tat FGR Duct (psig)
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26 Vortex FD Fan Blades
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26. Vortex FD Fan Blades
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26 Vortex FD Fan Blades
27 Vortex SA Fan Blades
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UNIT OPERATING DATA
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Test Comments
Date
Atom. Type
Locatic
x/x:
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1. Test Number
2. Date
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•j Cont. Room 02 (*)
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15. Stack Temp (°F)
16. Fuel Flow (CTW-e*GPM)
17. Fuel Pres/Tempfpsi/T)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (gaigt
26. vortex FD Fan Blades
27. Vortex SA Fan Blades
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Test No.
Fuel
Date
UNIT OPERATING DATA
Location 19
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Atom.Type
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Test Comments
1. Test Number
2. Date
3. Time
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7. Cont. Room 02 (*)
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13. Air FD Fan Amps
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16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i AP Pitot FGR Duct (iwg)
22 AP Orif. FGR Duct(iwg)
23 Temp. FGR Duct (*F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan {psig)
26. Vortex Fb Fan Blades
27 Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#6
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26 Vortex FD Fan Blades
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Capacity
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Date
UNIT OPERATING DATA
Location 19
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Capacity
Test Comments
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24. Pstat FGR Duct (psig)
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27. Vortex SA Fan Blades
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UNIT OPERATING DATA
Test No.
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Capacity
Test Comments
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Test No.
Fuel
Date
UNIT OPERATING DATA
Location 19
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A torn. Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
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5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (%)
8. Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14 . Air Temp 6 FD Fan/CR (" F )
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18. Fuel Atom Pres (psig)
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20. FGR Reg. Setting
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23. Temp. FGR Duct <»F)
24. Pstat FGR Duct (psig)
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26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. * PGR
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Test No._
Fuel # (,
Date
UNIT OPERATING DATA
location 19
Engr.
2 ?*
Atom. Type _
Capacity
Test Comments
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1. Test Number
2. Date
3. Time
4. Load
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18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct(iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. » FGR
30. Total Oil Burned «2/#6
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Test No.
Fuel /I/,
Date
DNIT OPERATING DATA
location 19
Engr.
Atorn.Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
6. Excess 02 Condition
7. Cont. Room 02 (%)
8. Pres.Furn/Windboxtiwg)
9. Uptake (iwg)
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11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
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22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct (8F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfin)
29. % FGR
30. Total Oil Burned #2/#6
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27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
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88
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Test No._
Fuel 3?
Date
UNIT OPERATING DATA
Location 19
Engr.
6 '//
Atom. Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (%)
8. Pres.Furn/Windboxtiwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
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16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/eF)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
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23. Temp. FGR Duct ("F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
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28. SA Depth/Flow (ft/cfm)
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Test No. _ Date _
Fuel 3F£ J- J(l G Atom. Type
UNIT OPERATING DATA
location 19
Engr.
Capacity
Test Comments
1. Test Number
2. Date
3. Time
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7. Cont. Room 02 (»)
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14. Air Temp @ FD Fan/CR (°F)
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16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp (psi/T)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
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23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
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Date
UNIT OPERATING DATA
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Capacity
Test Comments
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11. Drum Press (psig)
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25. Pstat S.A. Fan (psig)
26. Vortex Fb Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
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9 1
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Test No.
Fuel
Date
UNIT OPERATING DATA
Location 19
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Atorn.Type
Capacity
Test Comments
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2. Date
3. Time
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11. Drum Press (psig)
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20. FGR Reg. Setting
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23. Temp. FGR Duct (°F)
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UNIT OPERATING DATA
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/S ?0f>
M/ti **
#/ CO
/,
-------
Test No.
Date
UNIT OPERATING DATA
Location 19
Engr.
. GAS
Atorn. Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (%)
8 . Pr es . Furn/Windbox ( iwg )
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14. Air Temp @FDFan/CR(° F)
15. Stack Temp (eF)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/eF)
18. Fuel Atom Pres (psig)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct (»F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Pan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned *2/#6
31. Total Gas Burned
H-/2?
0
r?A< $
t/ov
0,13
z.r
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^ 7
7~7
2I£
22-3-
10
117
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~1
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.
iff, &
#,62-
f-H
y
/'i, 0ee>
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17
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77
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77
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5~/o
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7X
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ifo
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1'1
-------
Test No._
Fuel^y^
Date
UNIT OPERATING DATA
Location 19
+jr{0/t. Atom. Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6. Excess 02 Condition
7. Cont. Room 02 (%)
8. Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/cF)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/CR ( " F )
15. Stack Temp (°F)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (pgag)
19. Primary Reg. Setting
20. FGP. Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct ("F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/crm)
29. % FGR
30. Total Oil Burned «2/#6
11. Total Gas Burned
/1-/fe
7 Wf- 77
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it? 111
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0.73-
Fl*!
V.I
-------
Test No.
Date
UNIT OPERATING DATA
Location 19
Engr.
Atom.Type
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
g. Excess 02 Condition
7. Cont. Room 02 (*)
8. Pres.Furn/Windbox(iwg)
9. Uptake (iwg)
10. Final Stm Press (psig)
11. Drum Press (psig)
12. F. Water P/T (psig/°F)
13. Air FD Fan Amps
14 . Air Temp @ FD Fan/CR ("F)
15. Stack Temp (eF)
16. Fuel Flow (CFMorGPM)
17. Fuel Pres/Temp(psi/°F)
18. Fuel Atom Pres (psig-)
19. Primary Reg. Setting
20. FGR Reg. Setting
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct(iwg)
23. Temp. FGR Duct («F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. » FGR
30. Total Oil Burned «2/#6
31. Total Gas Burned
I1-/12
2-Z-77
1'-2-5~
li^ee
£S/s%f r«*r.
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1
Sheet 6003-16
10
,000 $^00 7300
-------
Test No.
Fuel
- / '
UNIT OPERATING DATA
Date 3 -/O - 77 Location_19
A torn. Type ,/,>•
Engr.
Capacity
Test Comments
"V
1. Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6 Excess 02 Condition
7. Cont. Room Oj (%)
8. Drum Press (psig)
g. Final Stm Press (psig
10. F. Water P/T (psig/°F
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR(°F
13. Stack Temp (°F)
14. Fuel Flow (CFff or GPM
15. Fuel Pres/Temp(psi/°F
15. Fuel Atom Pres ( fl'S
17. Pres . Furn/Windbox (iwg
19. Primary Reg. Setting
19. FGR Reg. Setting
2o. uptake (iwg)
2i. AP Pitot FGR Duct (iwg
22. AP Orif . FGR Duct (iwg
23. Tempi FGR Duct (°F)
24. Pstat FGR Duct (psJ^)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
£7. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/#&
31. Total Gas Burned
3 Sean* I/ft*/ rafc
0if 6tft* /psft'/ieu \
/ -77
// •£ &
/ & 2
3J{f-feH9/,
Ifffrt^ia /
e.?
16
?/$
-
£?£,
—
81
S3
S/l
•r3s/
36
Z/8
-
£20
—
It
£6
j-//
S£i/c>6a/.
/2
46
£/
/bV
e?./
96
36
^3 /Q
—
zee
—
G *^
9£
j~/$
&-6/S&*/
'29
i
-------
Test No.
UNIT OPERATING DATA
Pate 3- /*a/.
I23
>~ \/e*i rate. 1 io,£~
Data Sheet 6003-K
1 0
-------
Test No.
Fuel
UNIT OPERATING DATA
Date 3~/7 77 Location 19
Atom.Type ///'/•
Engr.
Capacity
Test Comments
1. Test Number
2. Date
3. Time
4. Load
5 Test Purpose
6 Excess 02 Condition
7. Cont. Room 02 (*)
B. Drum Press (psig)
9. Final Stm Press (psig)
10. F. Water P/T (psig/°F)
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR(°F)
13. Stack Temp (°F)
14. Fuel Flow (CFM or GPM)
15. Fuel Pres/Temp(psi/°F)
15. Fuel Atom Pres (/5f'<
S-/7
/0:t
/3.
£d££
h0/u*
ft
qg
ezo
9,2£~
-
/g
'S~
7
»7
*/.
S"
£&
8
7
•7
'^
-
j?
-
'"
/f:
w.
*
/£>
f'
13£~
3
• 6~
-6
- .
^
/
7
—
<5?2
-------
Test No
Fuel
UNIT OPERATING DATA
3/465 Date 3~/7- 77 Location 19
Atom.Type
,-r
Capacity
Test Comments
— _ —
1. Test Number
2. Date
3. Time
4. Load
5 Test Purpose
6. Excess O2 Condition
7. Cent. Room 02 (%)
g. Drum Press (psig)
g. Final Stm Press (psig)
10. F. Water P/T (psig/°F)
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR(°F)
13. Stack Temp (CF)
w. Fuel Flow (CFM or GPM)
15. Fuel Pres/Temp(psi/°F)
16. Fuel Atom Pres (f'g )
17. Pres. Furn/Windbox (iwg)
18. Primary Reg. Setting
ig. FGR Reg. Setting
2o. Uptake (iwg)
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct ("F)
24. Pstat FGR Duct (ps*g!
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. * FGR
30. Total Oil Burned #2/#6
.31. Total Gas Burned
J-//'- 77
/r-^
W.7
MSJ- Test
ver^af
—
-------
Test Mo. t*~3
Fuel
UNIT OPERATING DATA
Date 3 -/' 7-7
/'/*>
S.&
—
.f**~
-,/
&*!.
/
33.6-
.g \
1 \
/
—
£20
^
W
SI
&.6 //rf-/.
/23
£}
g£
J~f/
S3
33£~
.86
-8
3.6
~-
- ,/96~
. /
. 72
3~40
bbf
—
/. /
" —
—
—
—
fc
-
-
Data
•—
-^~~
ft: Jo
/4>.4
**•
^-
.8
97
17 -
£?
fy.b
.^
I.I
—
-
—
- ^
—
Sheet 6003-1JE
1 04
-------
Test
Fuel
UNIT OPERATING DATA
Date 3 •£/ • "7 7 Location 19
Atom.^
Engr.
Test comments 3/4 $ j
Capacity
//'' &ci'ff. f Street x//
r
1 Test Number
2. Date
3. Time
4. Load
5. Test Purpose
6 Excess 02 Condition
7. Cont. Room 02 (%)
8. Drum Press (psig)
9. Final Stm Press (psig)
10. F. Water P/T (psig/°F)
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR(°F)
13. Stack Temp ("F)
14. Fuel Flow (Gfft or £PM)
15. Fuel Pres/Temp(psi/°F)
16. Fuel Atom Pres (pf'S )
17 . Pres . Fum/Windbox ( iwg)
18. Primary Reg. Setting
19. FGR Reg. Setting
20. Uptake (iwg)
2i. AP Pitot FGR Duct (iwg)
22. AP Orif. FGR Duct (iwg)
23. Temp. FGR Duct (DF)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. * FGR
30. Total Oil Burned *2/«6
ill. Total Gas Burned
ire 'a 1+1 (/tuj Rote
MM. x,v Preu,
& {inset Pos.
JM2 ,9 £ A £ £ m J&- ^ *C A £ £
/*7 3 *Jfi3j H // v ^"<3o
3~/** \
\ 1
Data Sheet 6003-16
1 05
-------
•Test No. _t4-V
Fuel # <£"
Test Comments
UNIT OPERATING DATA
Date 3-fJ - 7~? Location 19
Atom.Type /j/ /
/5v / £&/
Engr.
Capacity
//V '
1. Test Number
2. Date
3. Time
4. Load
$ Test Purpose
6 Excess 02 Condition
7 Cont. Room 02 (%)
8. Drum Press (psig)
g. Final Stm Press (psig)
10. F. Water P/T (psig/cF)
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR("F)
13.' Stack Temp (°F)
14. Fuel Flow (CPPTor GPKT
15. Fuel Pres/Temp(psi/°F)
16. Fuel Atom Pres (p*'f )
17. Pres. Furn/Windbox ( iwg)
18. Primary Reg. Setting
19. FGR Reg. Setting
2o. Uptake (iwg)
2i. AP Pitot FGR Duct (iwg)
22. &P Orif. FGR Duct (iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (ps*g)
25. Pstat S.A. Fan {psig)
26. Vortex FD Fan Blades
27. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. * FGR
30. Total Oil Burned #2/#6
31. Tctal Gas Burned
frf/fiff 00 f, •?,£>„ "
rffa&T ^fPi f X?4S '*\
j, ' V\
e*™ "*" ** }
S?-*JS*J
3-
S
S4g
W?/s-«-'
/?3
ez/
33
—
_
-
—
— .
1.0
te:to
/£&
. ?
-------
'Test Ho.
UNIT OPERATING DATA
Date 3 -c>3 - ? 7 Location 19
Atom.Type J, r
Engr.
Capacity
Test Comments J//S f />^/. A/r'
1. Test Number
2. Date
3. Time
4. Load
5 Test Purpose
g. Excess 02 Condition
7. Cont. Room 02 (%)
8. Drum Press (psig)
9. Final Stm Press (psig)
10. F. Water P/T (psig/T)
11. Air FD Fan Amps
12. Air Temp@FD Fan/CR(°F)
13. Stack Temp (°F)
14. Fuel Flow (CESi or GMT)
15. Fuel Pres/Temp(psi/°F)
15. . Fuel Atom Pres (/>*''% )
17 . Pres . Furn/Win dbox ( iwg )
18. Primary Reg. Setting
19. FGR Reg. Setting
2o. Uptake (iwg)
2i. AP Pitot FGR Duct (iwg)
22. AP Orif . FGR Duct (iwg)
23. Temp. FGR Duct (°F)
24. Pstat FGR Duct (psig)
25. Pstat S.A. Fan (psig)
26 Vortex FD Fan Blades
2j. Vortex SA Fan Blades
28. SA Depth/Flow (ft/cfm)
29. % FGR
30. Total Oil Burned #2/*6
.31. Total Gas Burned
tf-tsjssA/f-WfS
3 ?s- r-\3',tj
64 3 6 K?J +
/aitj
,s
97
3-7
zzt
-
&%
J. /•
/2&
£?
-------
LOCATION 19
FUEL GAS CHROMATOGRA2HIC ANALYSIS
Test 19-190
March 7, 1977
Oxygen < 0.009% by volume
Nitrogen 0.29
Carbon Dioxide 0.54
Metbane 95.84
C 2 2.92
C 3 0.22
C 4 0.099
C 5 0.039
C 6 plus 0.054
Heating Value 1035 BTU/SCf (dry)
108
-------
o
CO
Fuel
Date
Laboratory No.
Carbon , %
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, %
Oxygen, %
API Gravity
HHV, Btu/lb
HHV, kJ/kg
#2 Oil
1/6/77
13520
86.45
13.01
<0.001
0.16
<0.001
0.38
37.8
19,680
45,775
#2 Oil
1/10/77
13520
85.62
12.99
<0.001
0.10
<0.001
1.09
37.7
19,680
45,775
#2 Oil
1/19/77
14009
86.49
13.17
0.008
0.14
0.001
0.19
37.5
19,610
45,613
#6 Oil
12/15/76
13042
87.55
11.49
0.20
0.56
0.020
0.18
20.7
18,910
43,984
#6 Oil
1/19/77
14009
86.91
11.78
0.20
0.54
0.019
0.55
20.7
19,000
44,194
#6 Oil
2/16/77
14667
87.55
11.40
0.23
0.60
0.034
0.19
17.0
18,780
43,682
#6 Oil
3/2/77
14667
87.30
11.34
0.22
0.60
0.026
0.51
17.3
18,850
43,845
#6 Oil
3/10/77
16554
87.23
11.34
0.23
0.55
0.027
0.62
17.5
18,850
43,845
#6 Oil
3/17/77
16554
86.06
11.11
0.32
1.17
0.025
1.32
14.3
18,670
43,426
#6 Oil
3/21/77
16554
86.25
11.25
0.32
1.18
0.024
0.98
15.7
18,740
43,589
#6 Oil
3/23/77
16554
86.55
11.26
0.30
1.02
0.025
0.85
15.8
18,750
43,613
-------
P L AIIT
LOCATION /y "
OPERATOR a s°-
DATE /"-?-/
METHOD 5 CONTROL CONSOLE READINGS
_
RUN NO. /9-~p~
SAMPLE BOX NO.
METER BOX NO. '
DIETER H ~~
2 FACTOR~@
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
/O
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
wr.uAGr
Sampling
Time
(e)Min.
093*'
o 9 -TO
/o o3.o o
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
Outlet
(T )
* mout'
op
7o
7^
8^
9°
9^
/€>0
AVG.
AVG.
Sample
Box
Temprta-
ture
°F
3~?0
3(.s'
3C.O
3>(.S"
3L-*'
$(.*'
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
oF
O
(,1
-------
Test Mo._/?'-5"
Box No. /
Test Description
Pate
PARTICULATE CALCULATION SHEET
Location /9
Test Crew /?.
Sample Probe Position
Dry Gas Meter Vol. (ft )
Final x1^ 7,?. c «
Initial ;? 2/0.00
Total ^-?. 8-*'
Wt. 2 /e>o.o7%?-
3
4
5
6
Avq /00.072?
Bottle No.
Impinger
Content (Water)
Rinse (ml) 7Z^
Date Weighed
or 250 Bake '/I1 /?7
Final 1 /<9i9, / ? ? A
Wt. 250 2 /cfi . /9?V
3
4
5
6
Avg /CO. / f ig/.a. /o/y.'S.
Initial /o c /co o (,S$.o *S"9- e
& Vol 20 VJ ^ ^?. «- /rs. »
//A o rf££Tt>M£
SU.J/1K. 6t-g.
3 * ~T £
/o/ . $g¥Z
/•/. St?-?
jo/, tevt
Probe
(Acetone)
V«*'
/at. ??/V
j*l. 99/9
/o/. $?/7
. 0669
99.i/s/77
.*s*1
. tszl
. ?r^9
J//1/77
. f t'9£
. Si 9*
. S69V
. e> /7°
Blank
No. /^
//*?'-7-7
. v**-*-
. «V sv
. gy^s
,SV-r*
, £ Vi'3
. £ V s" ?
-6-
11 1
-------
Test NO. /9-
Unit No. /
PARTICULATE EMISSION CALCULATIONS
Date X/2./77 Location >9
Engr. g.
Fuel
Sampling Train and Method _£PA M-e.+L<,el
Pitot Factor, Fs
. £3
Barometric Pressure,
' Z
Total Particulate, «
n
gm
Tot. Liquid Collected, V
Velocity Head, AP . .3 £6 ivg Stack Temp., Ts 937 "R Stack Area, As
Sample Volume, Vm {S.O ft3 Stack Press., Psq - - * iwg Excess 02, X02%
Orifice Press. Dif f . , H /. SCF
*T.
g. .g^
'
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
5", (.
,-z.
'° Ib/MMBtu
ng/j oule
%
•Multiply Vm by 530/T (eR) if meter not temp, compensated.
Data Sheet 6002-4
1 1 2
-------
Test Vo._/9-
Onit No. /
FARTICULATE EMISSION CALCULATIONS
Date /- 6 -77 Location
Engr .jg.
/ Fuel *V? O/£. Sampling Train and Method
Pi tot Factor, Fs O • S* 3 Barometric Pressure, Pt
_
bar
Hg
Tot. Liquid Collected, V /-5"3.3. ml auliul Particulate, M^ /-5".S m gin
Velocity Head, AP .02C> iwg Stack Temp., Ts__2r£7__«R stack Area, As •?190 ft2
.3
Volume, Vm
ft
Stack Press., Psg
iwg Excess 0 , XO %
Orifice Press. Dif f . , H A V-*" Iwg Stack Gas Sp. Gravity, Gs /. O
n.d.
Sangple Time,
min Nozzle Dia., Dn
in. Meter Temp., T_
•1. Sample Gas Volume Vm = 0.0334 Vm(P + H/13.6)
Suu JD&2T
2. Water Vapor Vw = 0.0474 V
3. Moisture Content Bwo = Eq. 2/(Eq. 1 -t- Eq. 2)
4. Concentration a. C = 0.0154 MnAm
b. C = 2.205 x 10~6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
std
3
5. Abs. Stack Press. Ps = P. x 13.6 + Psg
bar
407 1.00
Ps X Gs
6. Stack Gas Speed Vs = 174 Fs /APIs /;
7. Stack Gas Flow a. Qsw = Eq. 6 X As x —— x -Trr-
Rate @ 700F
b. Qsd = Eq. 7a x (1. - Eq. 3)
B. Material Flow Ms « Eq. 7b x Eq. 4b x 60
X02f = 2090/(20.9 - X02%)
10. Emission a. E « Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
11 • * Isokinetic
9. XO factor
14077
I =
6 x Vs x Ps x Dn
fe SC Feet/104 Btu
Rn SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm by 530/T (°R) if meter not temp, compensated.
7. 2C-
SCF
SCF
N.D.
,00387 grains/DSCF
lb/DSCF
g. g7g
'
• S
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
}
Ib/MMBtu
ng/joule
Data Sheet 6002-4
1 1 3
-------
PLANT
LOCATION
OPERATOR"
DATE
METHOD 5 CONTROL CONSOLE REftDINGG
RUN NO. /.?- • 7
SAMPLE BOX NO. >/7T
METER BOX NO. H-J—
DIETER H
C FACTOR @
A)*,
AMBIENT TEMPFRATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
.„.
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
1 TOTAL
\\Vr.ttAGF.
Sampling
Time
t a \ N i n
\<~ t 11X11 .
/5-ao
/f^0
KVO
/5SO
Iff 00
Iktf)
Static
Pressure
In. 'Her.
3
-o.^
\
Stack
Tempera-
ture
(TS)"F
1?
<10
90
IF
/oo
/03
Outlet
(T ,.)
mout
op
j 1 /J
f\J fi
t
AVG.
AVG .
Sample
Box
remprta-
ture
"F
V/f
AVG.
Temperature
of Gas
Leaving
Condenser on
jast Impinger
fJA
,
l
-------
Test NO.
Impactor No.
/
Stack Temperature
ANDERSEN CASCADE IMPACTOR DATA
Location l°j Owner
Nozzle Size
Filter No.
Impactor Flow Rate
CFM
Plcite
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (VI)
too.o
Oao>
X/-»V
0,0033
/0.~7
HH.3
\~
0 - d° 28
3/.1
I.?
\-
to
8
28,
0.00.SO
fa.1
Back Up
Filter
7? 315-
\O
Data Sheet 6002-5
-------
Test No.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date /-£•- 77 Location Q
Engr.
Fuel A/0.3 0', I Sampling Train and Method
Pilot Factor, Fs . 83 Barometric Pressure, fba^°'i
'"4 ml Total Particulate, MR
in. Hg
m gm
Tot. Liquid Collected, V I"
Velocity Head, AP 0.0^ iwg Stack Temp., Ts ft3
Stack Press., Psg
iwg Excess O2>
Orifice Press. Dif f . , H O.le^ iwg Stack Gas Sp. Gravity, Gs l-° n.d.
Sample Time, 6 5P- 3- min Nozzle Dia. , Dn Vg in. Meter Temp., Tm _ °R
0.0334 Vm(Pbar + H/13.6)
*1. Sample Gas Volume Vm
2 . Water Vapor VWgtd = 0. 0474 V^ , K>i (
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eg. 2)
. \ 1 +
) *
std
4. Concentration a. C = 0.0154 Mn/Vin
b. C = 2.205 x 10~6 Mn/Vm
c. C = Eq. 4b x 16.016 x 10
5. Abs. Stack Press. Ps
std
3
P x 13.6 + Psg
1.00
Gs
6. Stack Gas Speed Vs = 174 Fs /APTs Jj^- x
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x -TT:
Rate @ 70"F TS 4°'
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms « Eq. 7b x Eq. 4b x 60
X02f = 2090/<20.9 - X02%)
10. Emission a. E = Eq. 4b x Fe X Eq. 9
9. XO factor
11. % Isokinetic
b. E = Eq. 4c x Fa x Eq. 9 x 1000
14077
6 x Vs x Ps X Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm by 530/T (CR) if meter not temp, compensated.
30.'7
1,0.11 SCF
?- 5O_ SCF
_ N.D.
_ grains/DSCF
Ib/DSCF
?213
0- 07-83 grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
%
?. /
Data Sheet 6002-4
1 1-6
-------
PLANT
LOCATION /y
OPERATOR
DATE_/£Z£^Z5
RUN NO. l<)-~
SAMPLE BOX NO.
METER BOX NO. '
1ETER H ~
: FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
!/*
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
Zesr/iXT
TOTAL
WDRAGH
Sampling
Time
(e)Min.
//2-J
//2/
I/ Ji%
//3~?
it^y
>t 3-7
/30~}
/H/7
/sal
/23«
11 /»!*>
Static
Pressure
(V'
In. 'Kg.
.s/y^/r j7,
Stack
Tempera-
ture
(TS)°F
f7ir
•)tjJ*>
^7^
Vso
"
V9o
Velocity
Head
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
•F
^i"
—
V4
-5"0
70
7-5."
£0
.5V
i-»
-------
•test No. / 9 -
Box No.
PARTI CULATE CALCULATION SHEET
Date /-/9-77 Location
Sample Probe Position
Test Crew
_
Test Description
Dry Gas Meter Vol. (
Final Jltv.ol
Initial gioa .3^
Total e, I, ?J>"
Beaker No. ~J
Date
Weighed
Tare 1 /o^.ooS^
Wt. 2 /» S3.
Bottle No.
Impinger
Content (Water)
Rinse (ml) V 9 o
Date Weighed
or 250 Bake
Final 1 /0jZ-
3
4
5
6
Avg /oV. C7&1fi
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Final 650-Tare
Comments:
ftJ)
]
99, 3368
9J. 33ii'
99. 334.7
Probe
(Acetone)
/7-r
f?, SV^i"
99. 3^44
99- 3V£7
.«/•«
Final /?
[nitial /^
A Vol 5
9
/CO, /S5"i"
/oo , HS-f
/oo. tfSf
Probe
(Water)
/?«
/ee. /??ii
/o». /g9i"
/*o, /896
'dfiV'
Impinger
1 2
^ / a^
& J0t>
f S~0
Cyclone
(Acetone)
Water Vc
3
/o
o
JO
Flask
(Dry)
>1 (ml)
S. Gel 1
6>So-*~
(,6,0.0
2o. f
Filter
No.
, g.s-/jz
• S.r/y
. gr'y'S
,^7C.S
.4770
- ?749
'^^
Data SI
^otal
/7£~.y
Blank
No.
^799^
.799?
.200°
, 7?"?^
,79^ 9
. ?SS 1
. 799 ?
O
leet 6002-3
8
-------
Test No. /?- ?
Unit No. /
SOLID PARTICULATE EMISSION CALCULATIONS
Date /-/?-77 Location / ?
Engr.
Fuel
Pi tot Factor, Fs ,83
Tot. Liquid Collected,
Velocity Head, AP
O'<- Sampling Train and Method M^-^Lo
Barometric Pressure,
y
bar
2 5,
T
in. Hg
ml
Particulate, M 39, ~7 m gm
iwg Stack Temp., Ts 9/Q °R stack Area, As_ ?,*)0 ft2
Sample Volume, Vm
stack Press., Psg T
_iwg Excess 0 , XO % /' / %
Orifice Press. Diff., H AVS>" iwg Stack Gas Sp. Gravity, Gs /' °
Sample Time, 6 7f min Nozzle Dia., Dn ^? in. Meter Temp., T
*1. Sample Gas Volume Vm = 0.0334 Vm(P, + H/13.6) &'•&?
sta bar
n.d.
Vw = 0.0474 V,
sta lc
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eg. 2)
std
4. Concentration a. C = 0.0154 Mn/Vm
b. C = 2.205 x 10'
c. C = Eq. 4b x 16.016 x 10
5. Abs. Stack Press. Ps = P^ x 13.6 + Psg
bar
std
3
6. Stack Gas Speed Vs = 174 Fs /APIs
1.00
Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x -- x ^
Rate @ 70°F - Ts 40
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
XOjf = 2090/C20.9 - X02%)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
9. X02 factor
10. Emission
11. % Isokinetic
14077
9 x Vs x PS x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm by 530/T («R) if meter not temp, compensated.
$.33.
SCF
SCF
N.D.
grains/DSCF
'
3<87/ X /o' Ib/DSCF
~
<£. XT.3
9C.
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
•7.3.1
. 99.f
lb/MMBtu
ng/joule
Data Sheet 6002-4
1 1 9
-------
Test No._
Unit No.
TOTft<- PARTICULATE EMISSION CALCULATIONS
'- 7V Date / -/9-77 Location >/ 7
Engr.
/
Fuel ** *
Sampling Train and Method
. /
5
Pitot Factor, Fs
• "
Barometric Pressure,
Tot. Liquid Collected, V
Total Particulate, M
?• 73 j.n- Hg
m gm
A58'
,
std
3
Pbar * 13.6+ Psg
6. Stack Gas Speed Vs = 174 Fs /APTs l~- x -^
* V Ps Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x ——
Rate @ 70"F TS 4°7
b. Qsd = Eq. 7a x (1. - Eq. 3)
B. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. X02 factor
10. Emission
11. % Isokinetic
XO f = 2090/(20.9 - XO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
Velocity Head, AP_^_°2£__iwg Stack Temp., Ts 9VO °R Stack Area, As ^ ^" iwg Stack Gas Sp. Gravity, Gs /' ° n.d.
Sample Time, 6 7X min Nozzle Dia. , Dn ^ in. Meter Temp., T^ "R
•1. Sample Gas Volume Vmgtd = 0.0334 Vm(Pbar + H/13.6)
2. Water Vapor Vw = 0.0474 V
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
sta
b. C = 2.205 x 10~6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps
SCF
N.D.
OZT2. grains/DSCF
" Ib/DSCF
I
7. 5/X/o~'
t '° grams/DSCM
in. w abs.
ft/min
^ WSCF/min
DSCF/min
0. O 37
N.D.
Ib/MMBtu
ng/joule
•Multiply Vmgtd by 530/Tni(cR) if meter not temp, compensated.
Data Sheet 6002-4
1 2 0
-------
PLA H T
LOCATION }Cj
OPERATOR'
DATE *//«/:> 7
RUN NO._ i4--jb
SAMPLE BOX NO.
METER BOX NO. /l-flWT
1ETER H ' ' 1J-
z FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OP STACK CROSS SECTION
Traverse
Point
Number
TOTAL
\VCRACr
Sampling
Time
IliS
)V30
M*Z
/soo
(SOC,
Static
Pressure
!u)&
M
Stack
Tempera-
ture
(T ) *F
^
0
Velocity
Head
i
6,01
]
,$
•
Press
Diffe
tial
Orifi
Meter
(AH),
In. H
a Gas
Sample
Volume
X<-1.0*
jyri,oo
'tmoo
WO. SO
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
%0
y0
^5"
JO
Outlet
Op
A/
,
4
-AVG.
AVG.
Sample
Box
Temprta-
ture
/I/A
^
-
AVR.
Temperature
of Gas
• Leaving
Condenser on
Jast Impinger
op
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Impactor No.
Stack Temperature
CT --'/.
Location
Nozzle Size
_°F Impactor Flow Rate_
Owner
Filter No.
o.
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (y)
O. 003 1
5 3
0*00*7
tl-l
90. 3
. 4
CO
fc
0.0033
/7
llootu
8
Ba,clc Up
Filter
7? M
(00.0
Data Sheet 6002-5
-------
PARTICIPATE EMISSION CALCULATIONS
Test No.__[£i7L_ Date ///<)/ 17 Location JG
Engr.
Unit No.
Fuel
Q~ / Sampling Train and Method
Pi tot Factor, Fs
ft •& I*
Barometric Pressure, P _ £ C7. 73
O3.IT ™
in. Hg
ml Total Particulate, M 29, V m gm
Tot. Liquid Collected, V^
Velocity Head, AP 0*0 frS" jwq Stack Temp., Ts ffrfr °R stack Area, As H-1Q ft2
Sample Volume , Vm
ft Stack Press . , Psg ~®' 3~ iwg Excess 0 , XO % /, 01 %
Orifice Press. Dif f . ,
Sample Time, 6 SY
*1. Sample Gas Volume
2. Water Vapor
3. Moisture Content
4. Concentration a.
b.
c.
5. Abs. Stack Press.
6. Stack Gas Speed
7. Stack Gas Flow a.
Kate @ 70°F
b.
8. Material Flow
9. XO factor
10. Emission a.
b.
11. % Isokinetic
H <
min
' 2' 2 =
9'Lf iwg Stack Gas Sp. Gravity, Gs /'& n.d.
Nozzle Dia., Dn ~^'% in. Meter Temp., T S'1^?- "R
Vmgtd = 0.0334 VrnfP^ + H/13.6)
Vw . = 0.0474 V
std lc
Bwo = Eq. 2/(Eq. 1 + Eq. 2)
C = 0.0154 Mn/Wn „
std
C = 2.205 x 10~6 Mn/Vm „
std
C = Eq. 4b x 16.018 x 103
Ps « P. x 13.6 + Psg
bar
Vs «
Qsw
Qsd
Ms =
E =
E =
I =
11* •o A^m /407 1.00
• 174 Fs /APTs /- x —
V Ps Gs
= Eq. 6 x As x — — x -Tfi?
= Eq. 7a x (1. - Eq. 3)
= Eq. 7b x Eq. 4b x 60
f = 2090/(20.9 - XO %)
Eq. 4b x Fe x Eq. 9
Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts (Vm + Vw )
Z'i.lf'i SCF
1. 0 3 SCF
Otl/3 N.D.
0.0/5" grains/DSCF
•2.11^0'^ lb/DSCF
0 i 0 ?5 grams/DSCM
/-/ nu i .
i u~ ' 1 in. w abs.
/ ^^ (f3 f t/min
^$"5"^ WSCF/min
3 1 3 1 DSCF/min
Q-tfO?' lb/hr
I OS. ^ N.D. ">
0. OZI ib/MMBtu
7, Of ng/ joule
1^-3 %
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fa SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm . by 530/T (°R) if meter not temp, compensated.
sta in
Data Sheet 6002-4
1 2 3
-------
PLAN T
LOCATION j y
OPERATOR
DATE / -20- 7->
RUN NO. /? - g;
SAMPLE BOX NO."
METER BOX NO.
DIETER H
: FACTOR~@~
METHOD 5 CONTROL CONSOLE READINGS
AMBIENT TEMmRATUKE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
\VCRAGr
Sampling
Time
(e)Min.
/"/so
/m"
ttr&d
ts-ty
tf&>
trf*' _
*^?£'Alf-J
Static
Pressure
'
In. 'Hg.
Stack
Tempera-
ture
(T JOF
S
s-^O
s-yo
s-£/<5
,o9^
.oH
, o<)?-
,0^7-
,0<)?~
,oiz
Pressure
Differen-
tial Acros
Orifice
Meter
(AH) ,
In. H2O
/.*7
/.*">
AS'7
/. S"?
/•st
/.f?
s Gas
Sample
Volume
(VJ ft3
13 9',0o
XM7.*~£>
3VI.O . (• 8
66. xd
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
Outlet
^mout'
°P
9-0
W
9s"
/o
-------
PARTICULATE CALCULATION SHEET
Test Crew £.
„..» *,. /"?- §3, rv
par No- /
Test Description
Drv Gas Meter Vol.
Date /-So- 77
Sample
(ft3)
Location
Probe Position
C£*JT£ JZ
Inpinger Water Vol (ml)
Dry Gas Meter Vol. (
Final JlLo.6,%
jnitial K'W.-S-*-
•mtal £6 • /<£•
Rpaker No. /<9
Date
upiahed /-S--77
Tare 1 / DO . *)3 ? &•
wt. 2 /oe . 9 3 2 »"
3
4
5
e
Avq /CO. 93 S<-
Bottle No.
Inpinger
Content (Water)
Rinse (ml) 77J>"
Date Weighed I-Z4-77
or 250 Bake
Final 1 /oo,(f?s-<~
Wt. 250 2 ;oo. ? 74-*
3
4
5
6
Avg /DO. 97S~f
Residue wt . 03(,Z
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Bt. 650 2
3
4
5
6
Avg
Residue Wt
Comments:
ft )
]
//
99,80*?
^9.*c9«-
9^. 8C 9 3
Probe
(Acetone)
y-K>
99. S/VO
99, f/vo
9 3.1/VO
.0047
Final ^/
[nitial so
A Vol //
/*
/OO. 97X7
/eo. ^ai''
/ȣ>. 972 (.
Probe
(Water)
3i-»
ASO . 9 7^"^
/*>«-
3
/0A 9^2?
/OA f« S^
/o/. tZZl
Cyclone
(Acetone)
£f>O
/o/. 9s.s-.r-
/*;/. 98^S"
/
/oo.eSto
/no .O7f^
/eo.oltl
.0022
>1 (ml)
S. Gel I
»S2. C n
Sl.O S
^3. 0 /
Filter
No.
/?
. X^OJ'
. 65"e-i"
. sror
J-3f-f? —
.£i^3-
. 8
0'f
Data SI
total
'£~0.0
i-9.B
?/.o
Blank
No.
/*
. ^
. Sc3S
- so to
. love
. ScS-7
. lo 3 •>"
.8036
_ .00 O "
icet 6002-3
1 25
-------
PARTICULATE EMISSION CALCULATIONS
Date J-20-T? _ Location
Test No. /9- E3, $H
Unit No. / Fuel *.? 0/<- __ Sampling Train and Method /^£_
,*/r
Pitot Factor, Fs • ? 3
Tot. Liquid Collected, V^
Velocity Head, AP .0°2_ iwg
Barometric Pressure
ml
Parti culate, H^ /^/ •
_in. Hg
m gm
Stack Temp. , Ts_/£££_eR Stack Area,
ft
Sample Volume, Vm
ft3 Stack Press., Psgjv2££_iwg Excess 0,,, XC>2%
Orifice Press. Dif f. , H / .T? iwg Stack Gas Sp. Gravity, Gs
Sample Time, Q 7 ^ min Nozzle Dia. , Dn ^ in. Meter Temp., T^
n.d.
•1. Sample Gas Volume Vm = 0.0334 Vm(Pbar + H/13.6)
2. Water Vapor Vwstd = °-0474 Vlc
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm,
-.-6
std
b. C = 2.205 x 10 Mn/Vm
c. C = Eq. 4b x 16.018 X 10
std
3
5. Abs. Stack Press. Ps = P^ x 13.6 + Psg
bar
6. Stack Gas Speed Vs = 174 Fs /APTs ~
1.00
Gs
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x -rrr
Rate @ 70"F W
b. Csd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms » Eq. 7b x Eq. 4b x 60
= 2090/(20.9 - XO %)
10. Emission a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 X 1000
11. % Isokinetic
9. XO factor
14077 x Ts(Vm + Vw )
stu sta
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply
by 530/T (*R) if meter not temp, compensated.
.// SCF
Ot? _ SCF
N.D.
. CO 3 3 grains/DSCF
7S% X /t>~ grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
>
Ib/hr
i
Ib/MMBtu
ng/joule
Data Sheet 6002-4
1 26
-------
Test No. /9-
Unit No. /
PARTICULATE EMISSION CALCULATIOKS
Date /-.? ft2
Sample Volume, Vm
Stack Press., Psg -.
iwg Excess O , XO %
Orifice Press. Diff. , H /• -f? iwg Stack Gas Sp. Gravity, Gs
Sample Time, 6 7^> min Nozzle Dia., Dn '2 in. Meter Temp., T
ni
*1. Sample Gas Volume Vm
s
2. Water Vapor
n.d.
0.0334 Vm(P
+ H/13.6)
Vw , = 0.0474 V,
std Ic
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
!
-6
std
std
3
b. C = 2.205 x 10 Mn/V»
!
C. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P. x 13.6 + Psg
car
6. Stack Gas Speed Vs = 174 Fs /APTs
407 1.00
Ps Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x -- x =-
Rate @ 70eF TS 4°
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow
9. XO factor
10. Emission
11. % Isokinetic
Ms = Eq. 7b x Eq. 4b x 60
XO f = 2090/C20.9 - X02%)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vmgtd + ^^^
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0-002346
Coal
96.2
0.002636
•Multiply Vm , by 530/T (eR) if meter not temp, compensated.
std m
9,
SCF
SCF
O.IX.O N.D.
. 00 *>*} grains/DSCF
,
I. 4/8 X ID Ib/DSCF
-?
ID grams/DSCM
ft/min
WSCF/min
DSCF/min
Ib/MMBtu
ng/joule
Data Sheet 6002-4
1 27
-------
PLAWT_
LOCATION
OPERATOR"
DATE r
RUN NO. /V-a<"
O A M T* r trt *•* n 1. ..Li" ** IM
METHOD 5 CONTROL CONSOLE READINGS
SAMPLE BOX NO"
SIETER BOX
DIETER H
: FACTOR"
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
Avbetisa*) ZfifAc T-^/£ SCHEMATIC OF
Traverse
Point
Number
TOTAL
WERAGH
Sampling
Time
(e)Min.
bco^o
/4./S'.' 00
lbJO'-00
lt,K-oo
HfW
Static
Pressure
In. '44*.
Stack
Tempera-
ture
*<
'0
STACK CROSS SECTION
Velocity
Head
o.c
,^
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
In. H2O
0.7
,
•
s Gas
Sample
Volume
( v j" ft3 7
**(,/. Ql
MW*0
^177,QO
WU.oO
yyi/. 0}
T.0.0
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
oF
/OO
170
/IO
Outlet
(T )
v mout'
AJ
/»
AVG
AVG.
Sample
Box
Temprta-
ture
•JA
f
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
60
f n
bo
(?3>
ro
oo
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Impactor No.
Stack Temperature
Location
Owner
Nozzle Size
°F Impactor Flow Rate_
Filter No.
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cvun. %
BCD (y)
O.oolip
0' oo/7
0.00/5"
, 7
7Z.O
ro
cc
n
9.3
-$3,0
17.
O.OOJ 3
ll.O
23.7
8
. 7
/A, 7
Back Up
Filter
/-1/-77
Data Sheet 6002-5
-------
PARTICIPATE EMISSION CALCULATIONS
Test No. ii- %> Date j-?Q-~>~l Location _ / *! _
Engr.
Unit No.
/
Fuel Mi>/hr
(01.1 N.D.
0, Q0?tt3 Ib/MMBtu
3, (til ng/joule
Data sheet 6002-4
\ 30
-------
PLANT
LOCATION / y
METHOD 5 CONTROL CONSOLE READINGS
- 97. 5
'
OPERATOR^.
DATE / - j? «/ - 7 7
RUN NO . /?- 97.
SAMPLE BOX NO.'
METER BOX NO. #-
*ETER H ~
^ FACTOR"!
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE ~
ASSUMED MOISTURE, % "
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
/> 7
3o.
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
Wr.RAOE
ampling
Time
(e)Min.
/eo-?
/O 2*
/o t,-?
/OJT2
// 07
// fif
b%Ai'*/
Static
Pressure
-
n. 'Hg.
Stack
Tempera-
ture
(Tg)«F
ygo
y^o
y*o
*rto
f90
Velocity
Head '
(Ps'
.» H"
.o<)S
. c9^
.t><**
.*1S
Pressure
Differen-
tial Acros
Orifi'ce
Meter
(AH),
In. H2O
/.&S
/.&$'
/,L*'
/.t.S
/,t.ir
s Gas
Sample
Volume
(vm) ft3
Ay?/.3J»"
•3^0^.00
ifrt. oo
tmz3.t>o
PJTV7. oO
2jT.ry.S0
63'Vi"
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
oF
Outlet
(T )
umout'
op
$0
tS
90
9^
/ oo
AVG.
AVG.
Sample
Box
Temprta-
ture
Op
320
3/0
3Vo
3V>"
35"c>
AVG.
Temperature
of Gas
Leaving
-ondenser on
Last Impinger
OF
yo
ss-
70
&o
w
-------
Test No. I1)-
Test Description
PARTI CULATE CALCULATION SHEET
Date _/-2V-77 Location,
Sample Probe Position _
/9
Test Crew Z.
Dry Gas Meter Vol. (
Final x?.r.5-y. £<2
Initial ,?f ?/ • 3-S~
Total <£ 3 , y-S"
Beaker No. '
Date
Weighed /- 2^-77 *_
Tare 1 9 9.;?i..s~<3
Wt. , 29^ 3C.S-O
- 3
4
5
6
Avq ct1.2<,S~l>
Bottle No.
Impinger
Content (Water)
Rinse (ml) "7 S~O
Date Weighed
or 250 Bake /-3l>-'>
Final 1 ??, 32C»-
Wt. 250 2 $$. J260
3
4
5
6
Avg I^.Sao/
Residue wt . o Sf'l
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Final 650- Tare
ft3)
J"
98-?3/9
9?. 133-0
IS. tea*3
Probe
(Acetone)
S-A'O
A2.T-77
9_8, 9^2C.
98. 9V^7
9S- ?^7
.O to->
Final /^
Initial /*
A Vol ^
^
/«o.V?J?
/so. VS ?«"
/0<5. tfSVO
Probe
(Water)
3S~&
too- sns.it
/o o . yo a (,
/cvr srcsif
. 0/E6.
Impinger
1 2
& //<£
& /0e>
&. yt>
s)trn>J<=
£t.**H<-
•7
/0O
/o'f.aci V2
/of . oo <+L
/o>t . oo .»366
99.336S
Flask
(Dry)
P«-t>
9l336i'
»?. 334!>'
?9, -J36^
. ,5£>o 3
>1 (ml)
S. Gel 1
f 73. J- 5
SV.lf g
Jfs. o />
Filter
No./y
,syy*-
,sv=-v
. syrs
. ?22S-
. 9*^8
, 92^i
, O 77i"
total
•27. f
5-0- -T
37- 0
Blank
No. ,
/£
. 79?S
.?m
. •goco
. 79f
.7? 5?
/
.7*99
0
Comments: •
Data Sheet 6002-3
-------
I P PARTICULATE EMISSION CALCULATIONS
Test Mo./?- f> ?&Date /-ay-?7 Location / f __
3* -
Unit Mo. / Fuel_
Engr.
-------
TOTAL- PARTICULATE EMISSION CALCULATIONS
Test No. /?- 9? 5
Unit No. /
Pitot Factor, Fs
£ Date
Fuel
. 23
Tot. Liquid Collected, V
Velocity Head, AP .09*"
/-2i-?-? Location I ^
C O't- Sampling Train and Method f^
Barometric Pressure, P, SO*/*
/3~?-° ml Total Particulate, M 3.3;
iwg Stack Temp. , Ts 9-5~"# °R stack
Engr. & £O t 7
wieo' r
in. Hg
S", ? m gm
Area, As Y, 9 O ft2
Sample Volume, Vm d2.¥J>" ft3 Stack Press., Psgjv££^jiwg Excess 0 , XO % 3-
Orifice Press. Diff. , H /• &•$ iwg Stack Gas Sp. Gravity, Gs n.d.
Sample Time, 6 <£ £ min Nozzle Dia. , Dn /j£ in. Meter Temp., T^
•1. Sample Gas Volume Vm . = 0.0334 Vm(P,_ 4 H/13.6)
std oar
Vwstd = 0.0474 V
"std
~6
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm_
b. C = 2.205 x 10~
c. C = Eq. 4b x 16.018 x 10"
5. Abs. Stack Press. Ps = P x 13.6 4 Psg
bar
6. Stack Gas Speed Vs = 174 Fs
std
,3
/
«
' PS " GS
530 Ps
Ts 407
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
2090/(20.9 - XO %)
10. Emission a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
11- % Isokinetic
7. Stack Gas Flow a. Qsw = Eq. 6 x As x 2 x £§_
Rate @ 70°F
9. X02 factor
14077
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
4
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
7.
•Multiply vmstd by 530/T^R) if meter not temp, compensated.
SCF
SCF
N.D.
grains/DSCF
(.
Ib/DSCF
. in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
. ng/joule
Data Sheet 6002-4
1 34
-------
<-fl-77
PLANT
LOCATION
OPERATOR"
DATE
RUN NO. , , ,-,
SAMPLE BOX NO. '
METER BOX NO. ty~;/ -to? )
DIETER H
: FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
0; I
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
So -1=
/A/Df/Zja-O mffleTCfi- SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
WERAGr
ampling
Time
(e)Min.
1 WO
tHHO
\isL/
3V~
Static
'ressure
.(PB>,
n _ •Ui-r .
'"1
-0. a;^
v
Stack
Tempera-
ture
(Ts)'F
V5r
\
\
Velocity
Head
(PS)
tVJJ
^o<}S
\
\
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
In. H20
ss3-*7
2 ?(>0 ,C)Q
^s^g. y?
IS, 00
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
OF
&>o
6-5T
70
Outlet
^mout'
OP
ti/\
|
1
AVG.
AVG.
Sample
Box
Temprta-
ture
Op
/J/f
1
AVG.
Temperature
of Gas
Leaving
Condenser on
Jast Impinger
Op
£o
6-0
Go
CO
en
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Location
13-
Owner
Impactor No.
Nozzle Size
a
Filter No.
Stack Temperature
A^ /-XY-c "
Impactor Flow Rate
0> t'~ J 7
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
ECD (VI)
/oo.o
¥/¥/
. oo
0. 0032.
~ 3
6,3
5^,0
CO
CD
17.
(2,3) 2.
0.
Hi. If
17.
31,8
8
0.0023.
f.i
Back Up
Filter
, 77 Jf F
0. 00
13.Z
13.?
Data Sheet 6002-5
-------
Test No.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date /'*V 7? Location / O.£)C> in. Hg
ml Total Particulate, M "ZCe* I m
Tot. Liquid Collected, V
Velocity Head, AP P-O^b iwg Stack Temp. , Ts ? V5" "R Stack Area, As
gm
ft
Volume, Vm
/5
ft
Stack Press., Psg
Excess 0 , XO % 5,1
Orifice Press. Dif f . , H
Stack Gas Sp. Gravity, Gs
n.d.
Jarai
1.
2.
3.
4.
5.
6.
7.
B.
9.
LO.
)le Time, 6 ^'
y min Nozzle Dia. , Dn 0,"\T*S in. Meter Temp., T &£~ £»-'
Sample Gas Volume Vm . . = 0.0334 Vm(P. + H/13.6)
std Dar
Water Vapor Vw = 0.0474 V,
sta Ic
Moisture Content Bwo = Eq. 2/ (Eq. 1 + Eq. 2)
Concentration a. C = 0.0154 Mn/Vm ^,
std
b. C = 2.205 x 10~6 Mn/Vm
std
c. C = Eq. 4b x 16.018 x 103
Abs. Stack Press. Ps = P. x 13.6 + Psg
bar
Stack Gas Spee
Stack Gas Flow
Rate i 70"F
Material Flow
X02 factor
Emission
a. Qsw = Eq. 6 x As x -^- x ||y
b. Qsd = Eq. 7a x (1. - Eq. 3)
Ms = Eq. 7b x Eq. 4b X 60
X02f - 2090/(20.9 - X02%)
a. E * Eq. 4b x Fe x Eq. 9
1 ^. P (* SCF
/. S'o2- SCF
0,0^. N.D.^
0 . 0 1 (o~l grains/DSCF
Z.'ZZllO lb/DSCF
0,O(0I"2. grams/DSCM
L-jfl 7 "> C/ .
~u '• 'o in. w abs.
/ "Z,b 7 ft/min
37
-------
PLANT
LOCATION
OPERATOR
DATE /T^r;
RUN NO. /^
SAMPLE POX NO!' / ~
METER BOX NO. £-,, .'/ex?,
DIETER H — —
- FACTOR @ ,y o^
METHOD 5 CONTROL CONSOLE READINGS
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
"/-
40
tf£THOD S~ SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
wr.RAor
Sampling
Time
(e)Min.
^
<&
J'
In. 'ttif.tft?
-.£>?£'
-£>,A-
Stack
Tempera-
ture
(TS)°F
^
&>f
f/0
£-10
&A'
f/S
3'0"/
Velocity
Head
0./00
0. 126-
ff./So
-------
Test No. /^
Box No. /
Test Description
PARTICULATE CALCULATION SHEET
Date /
Location
Test Crew
Sample Probe Position
Dry Gas Meter Vol. (
Final l& Z
Beaker Ho. /
Date
Weighed ' ?J ''
Tare 1 /v*.e>77&
Wt. 2 /et>, C? 776
3
4
5
6
Avcf /0£?r & 7 7p
Bottle No. /_t 2
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake ^'^ ~77
Final 1 /off. 0'• f(?CZ
/&/• 3g43
/&/ ' f&VS
3
Probe
(Acetone)
2-/JT- 77
/f£ : &{? £&
/02 - &&££?
/, J&S~/
i,
Probe
(Water)
£?. 1 (ml)
S. Gel 1
6J.0 .8f?j~
0- £f 7?
il?,&?7j~
0, &3 7t/
total
-------
Test No. /f
Unit NO.
/
PARTICULATE EMISSION CALCULATIONS
Date /'^ - 7 7 Location /f
Fuel
Engr.
ff'l Sampling Train and Method
0, g 3
Barometric Pressure, P
bar
in-
Pitot Factor, Fs
Tot. Liquid Collected, V^ /A'iff- £ ml Total Particulate, Mn 6 7. 6 - m gm '*/*'
velocity Head, AP 0./Z6 iwg Stack Temp., Ts
"R Stack Area, As
ft
Sample Volume, Vm_^£_£_ft Stack Press., Psg
Orifice Press. Dif f. , H /£. 4<73 s& ' WDSCF
' ^"grains /DSCM
•Multiply Vmgtd by 530/T^C'R) if meter not temp, compensated.
. <77 in. w abs.
ft/min
WSCF/min
DSCF/min
lb/hr
N.D.
ng/ joule
fft.2
Data Sheet 6002-4
1 4 0
-------
PLA NT
LOCATION /7
OPERATOR
DATE .? 1,7/7-7
RUN NO. /9-/a
SAMPLE BOX NO.
METER BOX NO. «/~
'IETER H
- FACTOR~T"
METHOD 5 CONTROL CONSOLE READINGS
o.'
AI1DIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING'
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
lumber
TOTAL
WCRAGr.
ampling
Time
(e)Min.
ll?Ji
II 33-
11*1
II Hi
Static
Pressure
~ '
ii ft
nlfr
,.
Stack
Tempera-
ture
(TS)»F
Hl£
Velocity
Head
(P.)
0.01
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
In. H2O
on
.
s Gas
Sample
Voluins
370&.00
3-?iA.fib
Jiig.oo
P7P '/. 00
IVtt)
Gas £
Temper at
Dry Gas
Inlet
(Tmin.)
op
// 'ft
no
I/O
11*
ample
.ure at
Meter
Outlet
(T )
* mout'
op
AV/J
, r
AVG.
AVG.
Sample
Box
Temprta-
ture
°F
tiA
% '
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
^0
JT_T
$?
rr
-------
Test No.
Impactor No.
Stack Temperature
ANDERSEN CASCADE IMPACTOR DATA
Location
Owner
Nozzle Size
Filter No.
Impactor Flow Rate
p. CQ/ re. c "•> •'c IA
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (y)
3(1. 307 /
/.I
7.7
7*. /
!7-?f33
mi
/ 7 9073
(A a) AS"
, OOZl,
79
8
3A /
Back Up
Filter
0.007$
0,032%
Data Sheet 6002-5
-------
PARTICUIATE EMISSION CALCULATIONS
Test Mo.
Unit No.
'3 3.
Date
Location
Engr.
Fuel
"^
Sampling Train and Method
Pitot Factor, Fs
Barometric Pressure, P 3Q.
Tot. Liquid Collected, V
Velocity Head, AP (.0? iwg Stack Temp., Ts
Sample Volume, Vm
ml Total Particulate, M ?2.
_in. Hg
m gm
°R stack Area, As 4.9 ft2
/>
ft
stack Press.,
iwg Excess O , XO % .^ £"
Orifice Press. Diff. , H Q•! iwg Stack Gas Sp. Gravity, Gs
n.d.
Sample Tijne, 9 2o
*1. Sample Gas Volume
2. Water Vapor
3. Moisture Content
4. Concentration a.
b.
c.
5. Abs. Stack Press.
6. Stack Gas Speed
7. Stack Gas Flow a.
min Nozzle Dia., Dn -5 '^ in.
Vm = 0.0334 Vm(P,_ + H/13.6)
std bar
Vw . = 0.0474 V,
std Ic
Bwo = Eq. 2/{Eq. 1 + Eq. 2) P***
C = 0.0154 MnAm „
sta
C = 2.205 x 10~6 Mn/Vm ,
std
C = Eq. 4b x 16.018 x 103
Ps = P. x 13.6 + Psg
bar
Vs - 174 Fs /APTs J^- x
, 530 Ps
Qsw = Eq. 6 x As x TT— x -rr=
Meter Temp., T_ °R
{f'lHp SCF0'&$St
f. ?/ SCF
kr jo&ef N.D.
0. 9^14 grains/DSCF
-If
H.VfT I'.Q Ib/DSCF
0. 0"l'j>(o grams/DSCM
40^ » H in. w abs.
Ic-^y f t/min
3^7^ WSCF/min
Rate 8 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. X02 factor
10. Emission
11. % Isokinetic
XO f = 2090/(20.9 - X02%)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vmstd + Vw^)
I = j
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
51 07 DSCF/min
/0«/,9 N.D. ^
0' O^fc
/^.9
lb/MMBtu
ng/ joule
/24 *
•Multiply Vin . . by 530/T (CR) if meter not temp, compensated.
Data Sheet 6002-4
1 4 3
-------
PLANT
LOCATION /^
OPERATOR'
DATE , S3
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
1 TOTAL
|\vr.UAGr
Sampling
Time
(e)Min.
09J&
WOA'
/
tesf
/
Static
Pressure
,06?j~
£>,46
/• ft3
36to~*q
?6 &&, 0
e6?j.
j'; . e?
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
°F
^^
gs~
*?&
/£>
-------
PARTICULATE CALCULATION SHEET
Itoet NO. W- /3S
pov NO. /
Date S -/S -'/ S Location /fZ
Initial / 0 <£.4~3 jf*"7
A Vol ff>5 43 4~~ tz>& x/"?
Beaker No. fy J~ £ "7 S
Date
Weighed /•
Bottle No. / /-/0 -77
Sen?, &£££?
/e&r ?£6j~
/&? 4£<* ?
g?,e?e?e>e?
/0V. 0(?&e?
/e>^, 0o&g
/£>#• etf^f?
Cyclone
__-{A-ce-E6ne)
e.,,
, g&g 4-
0-&
-------
{ $OLt P pARTICULATE EMISSION CALCULATIONS
Test No. /?- /S2 _ Date 1-/7- 77 Location /£
Fuel ^ ^
Unit NO.
/
Sampling Train and Method #? /A- .
Engr.
Pitot Factor, Fs
Barometric Pressure,
Tot. Liquid Collected,
ml Total Particulate, M
_in. Hg
'm gm
°R Stack Area, As 4 ftf- ft
Velocity Head, tS ff.f^^S' iwg Stack Temp. , Ts_
sample Volume, Vm_^£_ft3 Stack Press., Psg -0.?3 iwg Excess Q^, XO2%_£^_
Orifice Press. Dif f. , H_
Sample Time,
/
iwg Stack Gas Sp. Gravity, Gs
n.d.
min Nozzle Dia., Dn_
_in. Meter Temp.,
TOTAL
*1. Sample Gas Volume Vm = 0.0334 Vm(Pbar + H/13.6)
Vwstd = °-0474 vlc
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vn>sta
b. C = 2.205 x 10~6 Mn/Vm J_.
std
c. C = Eq. 4b x 16.018 x 103
5. Abs. Stack Press. Ps
O- II I
P x 13.6 + Psg
* / 4U / X.UU
6. Stack Gas Speed Vs = 174 Fs /APIs y|^~ x -^~
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x -rry
Rate @ 70°F S
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
XO f = 2090/C20.9 - XO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E - Eq. 4c x Fm x Eq. 9 x 1000
9. XO factor
10. Emission
11. % Isokinetic
14077 x Ts(Vm . + Vw J
^_ std std
6 x Vs x Ps x Dn2
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm td by 530/T^CR) if meter not temp, compensated.
4f3 grains/DSCF
~J^ Ib/DSCF
' ^ grams/DSCM
', 4& in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
Data Sheet 6002-4
1 4 6
-------
PLANT
LOCATION
OPERATOR"" —
DATE J.l3t!~r-l
RUN NO. /?^/V3 -H
SAMPLE BOX NCT.
METER BOX NO. y- ,c"p1l
DIETER H ' 4
2 FACTORlf~
METHOD 5 CONTROL CONSOLE READINGS
AMDIENT TEMrrn/VTURE
BAROMETRIC PRESSURE ~
ASSUMED MOISTURE, % ~
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
I ?, 6 *? /
AflJ&£/ts0v tMPAc.TO(L SCHEMATIC OF
Traverse
Point
Number
TOTAL
ampling
Time
(e)Min.
//.ITS'
noz
/?/5-
I?M
31
Static
Pressure
-ft. 2.
^
•
Stack
Tempera-
ture
(Tg)"F
W$
f
Velot
Hea
(Ps
6.
,
STACK CROSS SECTION
3ity
d
^
0^
-
•
Pressure
Differen-
tial Acres
Orifice
Meter
(AH) ,
In. H_0
i
^
S->n00
3711-00
J7<)S. l//
Xs.cw
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
l°%
>0%
HO
no
Outlet
(Tmout>
AJ
A
AVH.
AVG.
Sample
Box
lemprta-
ture
"F
/O
<
/)
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
6^
5V
rr
^
-------
Test No.
Impactor No.
Stack Temperature
H&
ANDERSEN CASCADE IMPACTOR DATA
Location
Nozzle Size
_°F Impactor Flow Rate
Owner
/n
Filter No.
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (y)
A 1. 1106
no
.4 )
to
00
7-7
V/. /
7-7
J3-V
8
Back Up
Filter
Data Sheet 6002-5
-------
PARTICULATE EMISSION CALCULATIONS
Test No. /y- '7.5
Unit No. / .
Pitot Factor, Fs
Date <3TT£ ^
in. Hg
Tot. Liquid Collected, V
_ml Total Particulate, M 33i % m gm
Velocity Head, AP
iwg Stack Temp., Ts
°R Stack Area, As
ft
Sample Volume, Vm
• 00ft Stack Press., Psg "" Q- 2- iwg Excess 0 , XO % 3.
Orifice Press. Dif f . , H £<• > > iwg Stack Gas Sp. Gravity, Gs
Sample Time, 6_f_7_min Nozzle Dia., Dn •37?' in. Meter Temp., T
n.d.
*1. Sample Gas Volume Vm ^^ = 0.0334 Vm(Pw + H/13.6)
sta bar
2. Water Vapor Vw . = 0.0474 V
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
"6
std
b. C = 2.205 x 10 Mn/Vmr
c. C = Eq. 4b x 16.018 x 10
std
3
5. Abs. Stack Press. Ps
^
bar
x 13.6 + Psg
407 1.00
Ps X Gs
6. Stack Gas Speed Vs = 174 Fs /APTs /
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x -rrr-
Rate @ 70°F Ts 4°7
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms " Eq. 7b x Eq. 4b x 60
9. X02 factor
10. Emission
11. % Isokxnetic
XO f = 2090/C20.9 - SCO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vm . , + VW )
sta sta
6 x Vs x Ps x Dn
5
Pe SC Feet/104 Btu
Pm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vmgtd by 530/T («R) if meter not temp, compensated.
. 0
0.
SCF
SCF
N.D.
O. 03^"? grains/DSCF
ti.Ql+lCr'' lb/DSCF
0- 019 (f grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
H.D.
Ib/MMBtU
23i ^3 ng/joule
/00.4 %
Q.98J
Data Sheet 6002-4
1 4 9
-------
/«?.
_/£_
PLANT
LOCATION
OPERATOR'
DATE ^
RUN NO.
SAMPLE DOX NO^
METER BOX NO
DIETER H
: FACTOR
METHOD 5 CONTROL CONSOLE READINGS
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
^fc-fl^ocf S~ SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
Nvr.UAor.
Sampling
Time
(e)Min.
0:?3
*y:?0
/t~3
»:/0
";33
W0
&?
Static
Pressure
In. 'iler.
-0.3
\
Stack
Tempera-
ture
(TS)°F
*K'
4g*
403
4gj-
*
Velocity
Head
(P.)
**»?
tfi £?& ft3
zw.se
??& , 00
t76
Outlet
(T )
v mout'
OF
AVG.
AVG.
Sample
Box
Temprta-
ture
OF
3/0
Z?0
Z30
S?<9
&0
S
AVR.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
«F
^
60
to
^7
&r
S3T
i
-------
PARTICULATE CALCULATION SHEET
test No.
Box No.
3
Date ?•?/•
location
Test Crew Ap
/
Test Description
Sample Probe Position_
Dry Gas Meter Vol. (
Final ^7f3. ?8
Initial t7?/.j8
Total <£"«? 00
Beaker No. X
Date
Tare 1 fc*. 0 ?
wt. 2 /et>, e>?ff0
3
4
5
6
Avq /**?, ff?0*?
Bottle No. / $ 2
Impinger
Content (Water)
Rinse (ml) 7J&
Date Weighed
or 250 Bake ?•??-?•}
Final 1 /e>e>. /t>6/, ?&&£
/e>/. 90£f
W' ?&&J~
S
Probe
(Acetone)
£• f>S28
/e>z. &3t*?
/£>? • &3 '. /#&&
/e>f. /&£0
/as?. /ff6f>
4
Probe
(Water)
SJ-*
?-??-7->
/£>&, /?&.*/*&
Inroinger
1 2
'£ Mj>
>0 /
'2 &£
Cyclone
(Acetone)
Water Vc
3
j- t
-& t
^~
Flask
(Dry)
>1 (ml)
S. Gel "\
te* ? %
f&#. e> &
/*?. 2 /
Filter
No.
& sy ' 7
£>. g4/££~
0,0^ f£
e?,04jg
?'^-7?
ff. <7j~/3
&.£?J~/2
&• 7J~/3
0, /#7?
total
*#£. £
?4>g 0
'f&. 2
Blank
No.
/ c 7 7 ~
«?. ge r/
0, gO 7/
7/
?-£?-77
ff.go??
ff. g& 7?
& f%£t f&
&f ^? & & S
Comments:
Data Sheet 6002-3
1 5 1
-------
Test No._
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date ?-?' - ?? Location Xf
Fuel
Engr.
c,'/ sampling Train and Method
Pitot Factor, Fs
?- & 3
Barometric Pressure, P.
.
bar
Tot. Liquid Collected, V
. .SCF
lb/DSCF
27.
/
-------
LOCATION
OPERATOR
DATE '_
RUN NO.
NO.
METER BOX NO. y~
1IETER H —
- FACTOR"?
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE ~
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
-
/
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
r
TOTAL
WE RAGE
Sampling
Time
(e)Min.
Ills'
m?
/f3s"
//vr
3&
Static
?ressure
C^^^^^T^^ •
;^
-O.)l
Stack
Tempera-
ture
(T8)"F
^>°
Velocity
Head
!!s}
o-oin
i
Pressure
Differen-
tial Acres
Orifice
Meter
(AH),
In. H20
O.Z-f
. f
s Gas
Sample
Volume
T^I-I7SHP^*
m
c* D bf , Q$
?%U.oo
P & ~7f. OO
Ptf7d. 00
15,00
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
°F
/pr
IZo
}?o
n*
Outlet
(Vut>
op
*]*
, .
AVG.
AVG.
Sample
Box
Temprta-
ture
"F
W
, f
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
°F
76
G2
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Impactor No.
Stack Temperature
Location
Owner
V? ; *i.
Nozzle Size
°F Impactor Flow Rate
Filter No.
CFM
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (y)
-Z73//4
Ji 7. 3/^3
^.0035*
tt.L
ft,,?
cr
\ 7
0.0023-
9.A
3, /
/7-7/3J
-27. /
11. OS tO
O. OQO 8
3^3
8
Back Up
Filter
tifo-l
Data Sheet 6OO2-5
-------
PARTICULATE EMISSION CALCULATIONS
Test No._/flA£2_ Date_£i2ll22_ Location
Engr.
Unit No. / Fuel
Pitot Factor, Fs • oj
Tot. Liquid Collected, V,
Velocity Head, AP O'6\°t
*(*
iwg
QI 1 Sampling Train and Method Pi*.
Barometric Pressure, P. ^O.O1^
bar • - - '
ml Total Particulate, M 2*1
Stack Temp. , Ts I/O °R Stack
Jer£o*. 2
in. Hg
'0 m gm
Area, As i
^Sff^cfai
/.-
iwg Stack Gas Sp. Gravity, Gs
n.d.
*1. Sample Gas Volume Vm , = 0.0334 Vm(P,_
std bar
std
^3
5. Abs. Stack Press. Ps = P. x 13.6 + Psg
bar
6. Stack Gas Speed Vs = 174 Fs /APIs Jj^- x -^
7. Stack Gas Flow a. Qsw = Eq. 6 x As x —— x -TT;
Rate @ 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
XOjf = 2090/(20.9 - X02%)
10. Emission a. E = Eq. 4b x Fe x Eq. 9
9. XO factor
b. E « Eq. 4c x Fm x Eq. 9 x 1000
11. % Isokinetic
I -
14077 x Ts(Vmgtd + Vw
6 x Vs x Ps x Dn
Fe SC FeeVIO4 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm ^. by 530/T (°R) if meter not temp, compensated.
. std m
Sample Time, 6 /O min Nozzle Dia., Dn
-------
PLA1JT
LOCATION_
OPERATOR
METHOD 5 CONTROL CONSOLE READINGS
^
RUN NO. .
SAMPLE DOX NO.
METER BOX NO.
1ETER H
: FACTOR"@"
AI1DIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, % "
HEATER BOX SETTING
P-ROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
METHOD S~~ SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
dumber
TOTAL
WrnARr
Sampling
Time
(e)Min.
Jff/
/00&
/'
In. 'Her.
tie?
-0,23
Stack
Tempera-
ture
(T )«F
s
S&S'
S30
£"30
&30
£-30
^30
^
s Gas
Sample
Volume
-------
PARTICU1ATE CALCULATION SHEET
Test No.
BOX Bo.
Date
- 77 Location
Test Crew /f?
Sample Probe Position
Test Description
Dry Gas Meter Vol. (
Final c'S^f^ • £ f
Initial i?7
Total £
Wt. 2 /oa. V372
3
4
5
6
Avtj /fcfc* f ^7/
Bottle No. / /<£
0.0332
7 /^^*? S<0//'i'
Final ^tf
initial /£?<
A Vol /^
/&. <97&2
/Off- &7 #2
#**<*
Xr
Impinger
1 2
^ /J3~
•y /c?o
*? J4~
Cyclone
(Acetone)
Water Vo
3
<2 &
-&• t
£>
Flask
(Dry)
1 (ml)
S. Gel 1
1£~& & /&
*<'?.& g
/j~,4> /
Filter
J3.J33 -y-y
0.207?
£>.g&7b
*
0. *?6£3
0.46S3
0. 36 '£3
0.W?
Data SI
total
'£/. ^
Blank
NO.^,/
^' '
£?. &<=>//
0: 0
-------
Test Ho.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date £-j?3-~?-7 Location _ /£
Fuel / <£ gv / Sampling Train and Method
Engr.
//£•/<£,
Pitot Factor, Fs
Barometric Pressure, P 3&.C& in. Hg
1
Tot. Liquid Collected, V
ml Total Particulate,
/?.?
gm
Velocity Head, AP £>•&&•
Solid "'
6i?. && 7 SCF
7. £S0 4 SCF
O./Ofe? N.D.
0.£>463 grains/DSCF
^^^J-XX^^lb/DSCF
&,/&&& grams/DSCH
40 ff. #fg in . w abs .
/349 . $/ f t/min
3£~7/. bJ' WSCF/min
3/82. /e DSCF/min
/,c>66 ff Ib/hr
/0ff.0£' N.D.
£>,06g3 Ib/MMBtu
t?9,36 ng/ joule
//^ ,/ *
6 x Vs x Ps x Dn
Fe SC Feet/10 Btu
4
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas
B7.4
0.002346
Coal
98.2
0.002636
•Multiply Vm by 530/T (°R) if meter not temp, compensated.
Data Sheet 6002-4
1 58
-------
PLANT
LOCATION
OPERATOR
DATE 3 .77?
RUN NO. ig
SAMPLE BOX NO.
METER BOX NO.
METER H
: FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE *
ASSUMED MOISTURE, % "
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
3,/Z
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
WERAGH
Sampling
Time
(e)Min.
/33^
MJL
iw
Itoy,
Static
Pressure
''"?
'-0.33,
Stack
Tempera-
ture
(TS)°F
xtz.
|
1
Velocity
Head
op
/DA
\ '
AVG.
AVC, .
Sample
Box
Temprta-
ture
°F
Mfl
> "
AVR.
Temperature
of Gas
Leaving
-ondenser on
jast Impinger
V/
, ,
en
CC
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Location
6wner
Impactor No.
Stack Temperature
Nozzle Size
°F Impactor Flow Rate
Filter No.
CFM
£V
-1 * 3 r
Plate
Tare (g)
Final (g)
Net (g)
Cum. %
BCD (M)
57 3/4
/oo.o
, V/77
$0.0
d.OO'SL
/7
(7.
0. 0021
r, 1
&$) 3. /
17-
0- Oo/%
f/.*f)
/-&>
fort)
8
at.
o.oo/t,
0*53)
Back Up
Filter
9.1.
73^5-
Data Sheet 6002-5
-------
Test No._
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date ^' \'l/ Location /^
*L Oil
. Fuel
Sampling Train and Method
Pitot Factor, Fs
Barometric Pressure/ P.
bar-
Tot. Liquid Collected, V
ml
',1$ in. Kg
Total Particulate, M j(e ,O m gm
Velocity Head, AP /). //S" iwg Stack Temp., Ts ?7£- »R stack Area, As 4,°l ft2
Sample Volume, Vm /5/'f ft Stack Press., Peg ~,2Z- iwg Excess O , XO % *// £ %
Orifice Press. Dif f., H 0• (r / iwg Stack Gas Sp. Gravity, Gs n.d.
Sample Time, 6 z@ mi" Nozzle Dia., Dn . 37 $~ in. Meter Temp., T
*1. Sample Gas Volume Vm = 0.0334 Vm(P + H/13.6)
2. Water Vapor Vw = 0.0474 V
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
std
b. C = 2.205 x 10~6 MnAm .
sta
c. C = Eq. 4b x 16.018 x 103
5. Abs. Stack Press. Ps = PL x 13.6 + Psg
bar
6. Stack Gas Speed Vs = 174 Fs /APIs ~ x
3
1.00
Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x 7^ x ^r
Rate @ 70°F s 40
b. Qsd - Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. X02 factor XO f = 2090/(20.9 - XO %)
10. Emission a. E « Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c X Fm x Eq. 9 x 1000
11. * Isokinetic
14077
I =
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
R« SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm by 530/T (°R) if meter not temp, compensated.
StU ffi
I'll
0. OS"?
3110
O.
tzs./
SCF
N.D.
grains/DSCF
Ib/DSCF
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
99,
Data Sheet 6002-4
1 6 1
-------
PLANT
LOCATION
OPERATOR"
DATE 3-f-?7
RUN NO. /'
In. -Vkf.
//,
0.t'
0.1'
ff.H
0./I
0.1'
0,"
Pressure
Differen-
tial AcroE
Orifice
Meter
(AH) ,
In. H20
/.?7
/.77
/.77
/.?7
/77
/.77
s Gas
Sample
Volume
(VJ ft3
^er^.e^s'
^936. 3~>o
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(T
umin.)
°F
Outlet
(T )
v mout'
op
<90
AVG.
TV! It*1 \
Sample
Box
Temprta-
ture
°F
3«J-
3?0
403'
te&
AVrt.
Temperature
of Gas
Leaving
Condenser on
liast Impinger
"F
&?
72
6g
4*
fs~
66
1
05
-------
PARTICULATE CALCULATION SHEET
Test Crew
Test Mo.
Box No.
Date 3 - ' - 77
Location
Sample Probe Position
Test Description /of%
Dry Gas Efeter Vol. (
Final 2fS(£> . £~/0
Initial £8?& • c'^^"
Total 60. 303~
Beaker No. /
Date
Weighed 0. f> ?&• o 7<$/
3
4
5
6
Avq /00-e>76?
Bottle No. / £ 2
Impinger
Content (Water)
Rinse (ml) 7<&S~
Date Weighed
or 250 Bake ,?-. '9/6
Residue wt o.,,fi?6q
/&£ ', & C r /
Jt&ffi &£ ?&
e.*<,*5
Final /6
Initial &
A Vol 6
Probe
(Water)
Impinger
1 2
'0 /37
t> /e>o
•§ 37
tfr
9g. 93 ' c?4
-/ e,***8
Water Vc
3
£•
*
f
^
c^~
/tXS'.t'ggf
/£&• &8£3
toa.tgc*/
Jff. &gf&
ja,e>0/&
>1 (ml)
E. Gel 1
*-?£• t '
/g. *s
Filter
c .
'96.4'
Blank
*. ?? 4?
f . 7f&£
IP, rqvg
•0. ?94£
-*.***,
Comments:
Data Sheet 6002-3
1 6 3
-------
PARTICIPATE EMISSION CALCULATIONS
Test No. /9 - / ~?o Date 3 - / - ?"? Location /£
Unit No. / Fuel #&*»'/ Sampling Train and Method
Engr.
Pitot Factor, Fs
Barometric Pressure, P.
.
bar
in. Hg
m gm 50. S"
Tot. Liquid Collected, V /£ grains/DSCF
'f li/DSCF
3
-------
PLANT ._
LOCATION
OPERATOR'
DATE VT]
RUN NO. , .
SAMPLE BOX NO.
METER BOX NO.-7-,/-/o" iHflfcTo/e. SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
WERAOn
ampling
Time
(e)Min.
IT>VD
i3s
Static
Pressure
'-11 4 "ItUf'l
/ (A1 3
0
-6.31
>
Stack
Tempera-
ture
(T i °F
S
rw
^
Velocity
Head
,ll
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
In. H20 .
o.n
^
a Gas
Sample
Volume
Het<,r fte+^!"jjf
&*F*T
3Q/V.57
? o^.OO
303 /. OO
3oyo. 00
3ov8.00
3o5"v. iT /
4^.#;
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
•F
7o
^O
{00
/o
-------
Test No.
ANDERSEN CASCADE IMPACTOR DATA
Location
Owner
Impactor No.
J_
Stack Temperature
Nozzle Size
_°F Impactor Flow Rate
Filter No.
CFM
Plate
Tare (g)
Final (g)
. 3'
Net (g)
Cum. %
ECD (y)
, . oo o y
Data Sheet 6OO2-5
-------
Test No._
Unit No.
PARTICULATE EMISSION CALCULATIONS
>.
Date J?-3~77 Location /9
Engr.
Pi tot Factor, Fs_
Fuel & 2. o 11 Sampling Train and Method /4* ct-e
i ^3 Barometric Pressure, P 3O, J<-/
DcllT
Tot. Liquid Collected, V
_ml Total Particulate, M 2 T. / m gm
Velocity Head, AP O. II iwg Stack Temp., Ts I POO °R stack Area, As_ 4, *) ft2
Sample Volume, Vm *rO. ft Stack Press., Psg ~. 2 3 iwg Excess 0 , XO % ?•
^™-~—
Orifice Press. Dif f . ,
Sample Time ,6 / / ?
*1. Sample Gas Volume
^. Water Vapor
3. Moisture Content
4. Concentration a.
b.
c.
5. Abs. Stack Press.
6. Stack Gas Speed
7. Stack Gas Flow a.
Rate @ 70"F
b.
8. Material Flow
9. XO factor
10. Emission a.
b.
11. % Isokinetic
H .67 iwg Stack Gas Sp. Gravity, Gs
min Nozzle Dia. , Dn /?75 in. Meter
Vm = 0.0334 Vm(P. + H/13.6)
std bar
Vw = 0.0474 V
std Ic
Bwo = Eq. 2/(Eq. 1 + Eq. 2)
C = 0.0154 Mn/Vm .
sta
C = 2.205 x 10~6 Mn/Vm ...
sta
C = Eq. 4b x 16.018 x 103
Ps = P x 13.6 + Psg
* -* * .. 7* — ~ — /407 1.00
530 Ps
Qsw = Eq. 6 x As x — x —
Qsd = Eq. 7a x (1. - Eq. 3)
Ms = Eq. 7b x Eq. 4b x 60
X02f = 2090/C20.9 - X02%)
E = Eq. 4b x Fe x Eq. 9
E = Eq. 4c X Fm X Eq. 9 x 1000
14077 x Ts (Vm . + Vw )
I = § r5
n.d.
Temp. , T °R
VO.S? SCF
^'33 SCF
, /?£" N.D.
tf,00^^£- grains/DSCF
1' ?bif'ftD Ib/DSCF
O • O C. 1 "f grains /DSCM
4'2. 1") in. w abs.
/ £0 f ft/min
^(fO WSCF/min
? ,29G> lb/hr.
/Z0,l H.D.
O.OI 51 Ib/MMBtU
Gi j ng/ joule
^.?7 %
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm ,, by 530/T ("R) if meter not temp, compensated.
std m
Data Sheet 6002-4
1 67
-------
-2S.
PLANT
LOCATION
OPERATOR"
DATE ~
RUN NO.
SAMPLE BOX 'NO'I
METER BOX NO.
DIETER H
3 FACTOR~@;
METHOD 5 CONTROL CONSOLE READINGS
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
M^-J-^-ocC
&0
S&0
j-*
-------
Test No.
Box No. /
Test Description
/?
Beaker No. ^
Date
Weighed «?'.&/*'•?
Final 250-Tare <&-0/s^>
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
comments:
ftj)
:
7
?.&G 6 ff
Final /g
Initial /£>
A Vol 8
g
59. Sbc'S'
?93?££'
&& ?& i^T~
*£^J
Impinger
1 2
^ /£&
0 /e>e>
a e&
<2-£ts-77
&
/?&, //$/
Me #/*„«
^-C^slone
(Acetoftei.
<&e
/ef. //7£
/', /- 4W2
c$Sk>
)1 (ml)
S. Gel 1
^//, ff t
£"^4. &
/*5~ /
Filter
7-^ ^7
0, 7,7*?4>?
ff. g/Jg
ff, 0/^4
0,g /3Q
*e,
-------
Test No. /?•
Unit NO. /
PARTICULATE EMISSION CALCULATIONS
Date 3- 3- 77 Location _ //£
Fuel .^?«p// Sampling Train and Method
Engr.
Pitot Factor, Fs 0.
Barometric Pressure, P. J*
-------
PLANT
LOCATION
OPERATORff. f*
DATE ~T- 9'. -±
METHOD 5 CONTROL CONSOLE READINGS
'9
RUN NO. /$ . /a,?
SAMPLE BOX NO. /
METER BOX NO.^
4ETER H
2 FACTOR"
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
30.07
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
TOTAL
wrj,A(,r
ampling
Time
(e)Min.
0:/S~
/0 '-So
V.*S-
M:*O
//:,*-
;/:<=>&
S*r
Static
Pressure
(P.),
Ih. 'Hg'.
~«*3
Stack
Tempera-
ture
(T )op
a
^7^
^74?
S7S
sir
,//c?^r
Pressure
Differen-
tial Acros
Orifice
Meter
(&H) ,
In. H20
^»
/.76
S.76
/.76
/.76
/.?*
s Gas
Sample
Volume
0
/£>£>
AVG . 103
Sample
Box
Temprta-
ture
330
3*6'
330
33A-
333'
33
-------
PARTICULATE CALCULATION SHEET
Test Crew X?
Test No. /
Box No. /
Date 3- 7 ' 77
Location^
Sample Probe Position
Test Description
Dry Gas Meter Vol. (ft )
Final 3/A£ • 7£
Initial Se^-fy. 7£
Total fg. €?c>
Impinger Water Vol (ml)
1 2 3 S. Gel Total
Final c*40 /44 4 ~£&&0 &77- &
Initial & /fff •& 67/'# 07/,&
A Vol /fra 4? 4 S&.e? t?6>6.3
3
Probe
(Acetone)
4*0
3-8-77
/ff/. ?6
/et, 00£s'
"1o>L
&&&
/0f,ff3?
W.eefl
&fy. fof?
*,***
Filter
No.
23
/•c'7- 77
0.7004'
0, 7f&£~
£?. 7&&£'
ff, 773?
&-?7f3
0.JP&4'
0,7
^-gptz
e? fffaj'
0. 0 &f$
0- #*/£>&
e, g
-------
PARTICULATE EMISSION CALCULATIONS
Test No. /G>&
Velocity Head, AP e-//t?£~ iwg
77 Location / Cj
>C?j Sampling Train and Method tff.
Barometric Pressure, P 3& & '
bar /if
5 ml Total Particulate, M ff
Stack Temp. , Ts 9 ?£~ °R Stack
Engr. £7,
.-hkoJ ~~ min Nozzle Dia., Dn
-------
PLANT
LOCATION
OPERATOR"
DATE j~
RUN
METHOD 5 CONTROL CONSOLE READINGS
NO.
SAMPLE BOX NO.
METER BOX N
DIETER H
- FACTOR" g_
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
Af*eL?-l^d> S SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
1 TOTAL
twrnAGi:
ampling
Time
(e)Min.
dff 'Sf
/& '£& •
// ••*£'
//:*>
///JET
»:&
WS
/gta*
A*jT
Static
Pressure
In. 'Bg'.
-*,ess
i
\
Stack
Tempera-
ture
(T )"F
O
&^?^7~~
^&&
£&&
£00
&0
^)<9&
•f&f
&
/.*?
/.fe
/,00
s Gas
Sample
Volume
3?f
330
340
340
3
3&>
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
j?
*2
f
-------
PARTICIPATE CALCULATION SHEET
Test Mo. /?- /f 3
Box No. /
Date
'8-
Test Description
Sample Probe Position
Location
Test Crew /P,
Dry Gas Meter Vol. (ft3)
Final 3c>/?.£
Initial 31 n.
Total Jpe>. €>
Beaker No. g
Date
Weighed ,3-7- 77
Tare 1 ?
Bottle No. / £,£
Impinger
Content (Water)
Rinse (ml) fct?£~
Date Weighed
or 250 Bake £-/0 -7?
Final 1 -
See. /00. /o. /&
fat?, e, fpef
/#%?- ffeur
£>. 00 &f
Cyclone
(Acetone)
3 S. Gel Total
& 6?7.4~ J&ff&J-
& te~0.J~ g^~e.s~
S0 ,z>70 4& e>
Flask
(Dry)
Filter
No.
ft;
/-c37'77
0.g&e>6
0. ge06~~
J'f- 77
0. &///
0: 8//C
f.e///
e, 0/0f
Blank
No.
c*3~
3 -g • 7 7
0.S&&
0-0 4>4/
#: 046 /
J~
-0-
1 75
-------
PARTICULATE EMISSION CALCULATIONS
Test No. /^
Unit No. /
Pitot Factor
Tot. Liquid
Velocity He a
-S'? grams/DSCM
in- w abs.
. /~? ft/min
WSCF/min
DSCF/min
N.D.
b/MMBtu
C?-/33 ng/ joule
Data Sheet 6002-4
1 76
-------
PLUME OPACITY OBSERVATION RECORD
Test Ron No. ^? • J
LOCATION HO.
OWNER
DATE /-
OBSERVER
_ BOILER NO. / CAPACITY -~ / fr klb/hr
VFUEL TYPE *£• BURNER TYPE
POINT OF EMISSION
POINT OF OBSERVATION
*,Ts?t! ^ <*T 9O ~7O
TEST
No.
Time
am/pm
Type
Test
Load
Opacity
WIND,
Speed
mph
Direct,
Sky
Cond.
Sun
Posi
tion
Comments
/-O
70
/V 0
7
••&•
!0_
II
- *'
&
60-25
1 77
-------
PLUME OPACITY OBSERVATION RECORD
/9
LOCATION NO.
OWNER
DATE / ~/ 9 " 77
OBSERVER /ff.
Test Run No. /f- 7f,
& ff T y
BOILER NO. /
CAPACITY -*>- /
klb/hi
VFUEL TYPE O't~ BURNER TYPE
POINT OF EMISSION .57"^ C.
/ /I. Q 1
POINT OF OBSERVATION *v Jt&& ^Xosft 3~rt£ KL stT 7O 7o IjJ/iJli t>/£.EVT S OS* ^ SUV
O*) f?T.
/f-r ^o" TO og&eR
,o
„
1*-
13
1*4
//
It,
Time
am/pm
/&
MS
two
WtS
f £_/ £ ^^
iy + ^
HIO
/W
nil
tsol
f£~/C>
IS~/t
,*/*
IS -'2
/*"*
l£f>'
Type
/c ^a.
Test
Load
^
Opacity
C>
o
0
0
0
(9
0
• O
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO. /?
OWNER
DATE /
POINT OF EMISSION
POINT OF OBSERVATION •*- Jg>O '
Tt>
Test Run No.
OBSERVER
BOILER NO. /•
CAPACITY
_.'FUEL TYPE 2 OJt- BURNER TYPE
£T#qT C* 9p° 70 {*>,?/£>
&?
klb/hr
No.
TEST
Time
am/pm
. Type
Test
Load
Opacity
WIND.
Speed
mph
Direct
Sky
Cond.
Sun
Posi
tion
Comments
XV
o
To TCT.
0
o
0
o
/ft
H
/*-
o
o
o
If
o
o
1 79
60-25
-------
PLUME OPACITY OBSERVATION RECORD
Test Run No.
LOCATION 110.
OWNER
DATE
OBSERVER
BOILER NO. / CAPACITY /7, TOO klb/hr
/ - £<* - 77
'/FUEL TYPE *,?
BURNER TYPE
POINT OF EMISSION
POINT OF OBSERVATION /fC.ZOi.1
id S*> £>
No.
/
*
J
£'
_T
c
7
2
S
/0
//
r>
/3
/«/
//
/^
TEST
Time
am/pm
y^ri'
lift
Type
/»//•> ^s
Test
Load
Opacity
.20
^0
O
5"
/0
/3-
3-
•/o
sr
*y
t*'
-bo
/*•
/ 0
/o
/y
WIND
Speed
Direct
Sky
Cond,
doY
Sun
Posi-
tion
:S
Comments
Ofrt C f ~r X
Fi.UG.~r t/4T/4)t
180.
60-25
-------
PLUME OPACITY OBSERVATION RECORD
Test Run No. /?-//7
LOCATION NO.
OWNER
DATE
/ 9
OBSERVER
BOILER NO.
// 7.^/7 7
CAPACITY
klb/hr
'.FUEL TYPE
BURNER TYPE
POINT OF EMISSION
POINT OF OBSERVATION
TEST
No.
17
19
/?
2,0
2/
21
23
*
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION MO.
OWNER
DATE
OBSERVER
BOILER NO.
- /?- 7"?
'FUEL TYPE
POINT OF EMISSION
Test Run No.
CAPACITY
klb/hr
BURNER TYPE
POINT OF OBSERVATION "t- fe
// 4/e>r/lr - faJ/ e?S
TEST
No.
/
£
3
*
i"
6
7
o
e
9
/O
//
>*
/J
/^
/{T
/£
Time
^St§7pni
jtorJ
//••sg
//&•/*'
:&
•fe-
J/:&
.'XT
V
:w
l£!0<
'.(£-
• Jo
:tr
Type
Test
Load
k#/hr
Opacity
%
£~
•
WIND
Speed
mph
0-tf~
Direct
/t/K/
Sky
Cond,
c/ear
Sun
Posi-
tion
Comments
60-25
1 82
-------
PLUME OPACITY OBSERVATION RECORD
Test Run No.
LOCATION NO.
OWNER
DATE
OBSERVER
BOILER NO.
CAPACITY
t?-?/ 77
POINT OF EMISSION
POINT OF OBSERVATION T, /£?0
\
Direct
Sky
Cond,
ttfar
^r
Sun
Posi-
tion
Comments
60-25
1 83
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE c
POINT OF EMISSION
POINT OF OBSERVATION
OBSERVER
BOILER NO.
•/FUEL TYPE
Test Run No.
CAPACITY
klb/hr
BURNER TYPE
A/ £~ £?/ ^S /
*» £
TEST
No.
/
2
3
^
6~
&
7
g
1
10
it
/2
'5
w
>6~
/<£
Time
am/pm
H:40
;/j-
:3*
:'/i'
//:«'
:/J-
;&
:K
//:tt
:/r
.•/^
:K
in +3
•If
:fr
:K
Type
Test
Load
k#/hr
Opacity
%
0
e
0
&
e?
a
c
• 0
O
6>
0
0
0
0
o
0
WIND
Speed
mph
^"-/^?
Direct
U/.
Sky
Cond
c£ar
Sun
Posi-
tion
Comments
60-25
1 84
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE
-/~ 7-7
POINT OF EMISSION
OBSERVER
_ BOILER NO.
'."FUEL TYPE
Test Run No.
CAPACITY
klb/hi
BURNER TYPE
POINT OF OBSERVATION •«• /8*
:/j'
'/e>
:«f
1:&
'//-
:&
:fr
r-a*
or
••&
:4r
Type
-
Test
Load
k£/hr
Opacity
%
0
0
0
0
0
O
O
WIND
Speed
mph
* ^
Direct
S.£.
Sky
Cond.
c/e&r
\
i
Sun
Posi-
tion
Comraents
60-25
1 85
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE
POINT OF EMISSION
POINT OF OBSERVATION
OBSERVER
Test Run No.
BOILER NO. /
CAPACITY
'FUEL TYPE #£*>'/ BURNER TYPE
J/. J/E OJ
klb/hl
TEST
No.
/
2
3
t
S
£
7
8
1
la
II
1?
13
/<<
/i
16
Time
arn/pm
W:te>
••/j~
•?"
:r
\
r
Sun
Posi-
tion
Comments
60-25
1 86
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
CATE J
POINT OF EMISSION
POINT OF OBSERVATION
//
OBSERVER
BOILER NO.
_.'FUEL TYPE
Test Run No.
CAPACITY
BURNER TYPE
klb/hr
TEST
No.
/
I
3
t
s'
6
7
$
q
le>
/f
12.
11
tn
ir
t&
Time
am/pm
//•*J
l'J~
:fr
:fr
tf:M
:/j~
l?e>
: H'
:?e
'•<<}'
&i46
:'t~
:?»»
/*/-
Type
Test
Load
k#/hr
Opacity
%
f?
0
0
0
o
c
o
• 0
0
0
G
0
0
0
0
0
WIND
Speed
mph
O'f
Direct
#U/
(
Sky
Cond,
S/ozy
t/Ptfcff
\
\
Sun
Posi-
tion
Comments
)
60-25
1 87
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE
3-7- 77
POINT OF EMISSION
POINT OF OBSERVATION
OBSERVER
BOILER NO.
/FUEL TYPE J/,
Test Run No.
CAPACITY
BURNER TYPE
klb/hr
TEST
No.
;
I
3
it
j"
£
7
8
0
O
0
0
•0
0
0
0
0
0
O
0
0
WIND
Speed
mph
^"'/^
Direct
e
Sky
Cond.
tbfc/y
Sun
Posi-
tion
Comments
60-25
1 88
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWHER
DATE
JS-
3-/Q-T7
POINT OF EMISSION_
POINT OF OBSERVATION_
Test Run No. /-/
OBSERVER
BOILER NO.
CAPACITY
klb/hz
VFUEL TYPE
+C.OH.
BURNER TYPE
TEST
So.
/
J
}
V
V36
JVf^_
/ro>
Type
•
-9-
-&-
0-
WIND
Speed
mph
o-s-
.
/
Direct,
S.IA/
•
Sky
Cond.
CLfAf^
i
\
\
I
1
Sun
Posi-
tion
Comments
60-25
1 89
-------
PLUME OPACITY OBSERVATION RECORD
Test Run No.
LOCATION NO.
OWNER
DATE
OBSERVER
BOILER NO.
CAPACITY
klb/hr
'.'FUEL TYPE
BURNER TYPE
POINT OF EMISSION
POINT OF OBSERVATION
/OO
TEST
No.
n
/y
"t
Jo
Time
am/pm
/r/r
/S^o
iff?
I!*JO
Type
•ZKS
Test
Load
kSAr
Opacity
%
&
-&
•8-
-&
WIND
Speed
mph
0-s
1
.
i>
Direct.
s^
\
/
Sky
Cond.
CL£-/f£,
t
/•
Sun
Posi-
tion
•
Comments
60-25
1 9 U
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE "3 "
OBSERVER S
•BOILER NO.
•-'FUEL TYPE
POINT OF EMISSION
POINT OF OBSERVATION /^/OO X £^57- PC
Test Run No. /?-,?
/// Jg
CAPACITY
klb/hr
BURNER TYPE
TEST
No.
>
3
)
*/
^
^
Time
am/pm
jooo
t/00
1*00
IJoo
Hoo
fSOo
Type
Test
Load
kS/hr
Opacity
%
^
5~
-6>-
i9-
$
-0-
-
WIND
Speed
mph
W'/$
Direct,
£"
1
Sky
Cond .
Uft-
,
Sun
Posi-
tion
Comments
)
60-25
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION NO.
OWNER
DATE ^ ~3I- T)
OBSERVER
BOILER N0._
:'FUEL TYPE
POINT OF EMISSION
Test Run No. /?-5 54 SS
CAPACITY
POINT OF OBSERVATION /OO -fr -c j~ &(, j J~
klb/hi
BURNER TYPE
TEST
No.
/
(?
>
V
$
<*
Time
am/pm
ID50
1/30
I53o
/330
^30
tsw
Type
^-^>5S
^
Test
Load
kS/hr
Opacity
%
^
/o
5
/o
/o
f
WIND
Speed
mph
H>-/Z
Direct
u
f
Sky
Cond
tuz*R.
Sun
Posi-
tion
Comments
60-25
1 92
-------
LOCATION NO.
OWNER
DATE
PLUME OPACITY OBSERVATION RECORD
OBSERVER
Test Run No./?- *j
BOILER NO.
CAPACITY
VFUEL TYPE
BURNER TYPE
POINT OF EMISSION
POINT OF OBSERVATION r-/t>O 5q <./" a -P" e-^'frS/QO ff>(j'i^'
klb/hi
TEST
No.
/
2
J
Y
f
/
Time
am/pm
W*
I0'.3<7
U'-le
ll-'le
1? '>?*
M'.?0
Type
Test
Load
k#/hr
Opacity
%
:T
jT ;
f
$
f
5"
WIND
Speed
mph
^<3 -./£>
ffffffSv,':
\
x
Direct,
; 5,<«/,
\
/
Sky
Cond.
Cl.f*£.
Sun
Posi-
tion
Comments
..<
60-25
1 9 3
-------
Project:
Date:
locat
Unit:
Test:
Fuel:
VELOCITY TRAVERSE
Test Description:
ion: / 7
/ 9
- A3
Personnel :
* 2 Of f-
letric
Press, (in. Hg):
.ute Static Press, in Stack
. Tube Coefficient:
(in. Kg):
. S3
Stack Cross Section
'+
stf
*t>
ul
Velocity
Head
(in. H70)
fiP
. 0^°
. oiz'
.0^
. Ogi"
. ofo
.0^
Gas Temp.
m
*/£<>
ysro
y&Z
170
V?*
V(,0
Gas Temp.
(°R>
Ts
9£o
9 / o
92ft-
130
9 Si"
n
J,.»0
s.iy
3.X-
3,/(,
3./7
3-/3
3,/3
$.>i
3. '3
3,/£>
3.oB
3.0?
3-oS
3,o7
~
6002-13
1 94
-------
froject:
Date: /- /? - 7-7
VELOCITY TRAVERSE
Test Description:
Location: X 7
Unit:_ /
Stack Cross Section
- 7 V. 76"
Personnel:
X o/t-
Test:_
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in stack {in. Hg):_
pitot Tube Coefficient:
.<40
6002-13
1 95
-------
Proj ect:
Date /- S.O -
VELOCITY TRAVERSE
Test Descriptioni
Location: l_
Unit: f_
Test: Is! - I
Fuel; * g
Stack Cross Section
Personnel:
Barometric Press, (in. Hg): «< 7 , £
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient: ' 6 2
c.
85.48 C,,
1/2
Time
Traverse Point
Port Depth
£
7
IS-
n
£2
Velocity
Head
(in. H20)
AP
.0?
-/
,09-i"
.F^
Gas Tenp.
(T)
A'tf^"
SfO
3-3 o
sriO
-S--2JT
Gas Tenp.
(*R)
TS
^^5'
?J^
980
9 f o
9ffi'
Molecular
Wt.
%
Velocity
(ft/secr)
vs
02
Cone.
(% Dry)
6002-13
1 96
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: /-;?y- 7 7
location: / 7 Stack Cross Section
Unit: /
Test: /?- ?^/ Sfc Personnel; X- ^AJ^eSSX
Fuel: ^^ <9'*-
Barometric Press, (in. Hg): 3O , / 1.
Absolute Static Press, in Stack (in. Hg): (PB)
C y _
Pitot Tube Coefficient: - Z> * (CL,) - --
I~T AP~1 '
V .= CE 4fl C S
vs • Cj-4CCP pM :::::::::
L s SJ .-
- _:.~ :: ~_j_
_L
1 1 , i , j
"ij — i i — H~
-]--
! ! ! i 1 _
1 ' I ' ' ; L-j—
j 1
III J
! 1 ' '
1 I 1
1 '• 1
1
i ; i 'i
Tine
Traverse Point
Port Depth
#
•7
)*
If
ii ?-
21
Velocity
Head
(in. H.,0)
fiP
.tf^A"
.0^"
.01*
. /oo
.0^
./oy
Gas Temp.
CF)
VF^
mf
V"
9Vi'
Molecular
Wt.
«S
Velocity
(ft/secl
vs
02
Cone.
(t Dry)
y.W
3.W
3.<57
3.00
3.00
'6.60
6002-13
1 97
-------
Proj ect:
Date: /' ~#&
Location: £
Uni t: /
VELOCITY TRAVERSE
Test Description:
StacX Cross Section
Test: /& '//& Personnel:
fuel: /C* f'f
Barometric Press, (in. Hg): ^^' '^
Absolute Static Press, in Stack (in. 1%):_
pitot Tube Coefficient: tf*. ,
V£ - 65.48 Cp
1/2
Time
Traverse Point
Port Depth
It-el* .
£
7
11
17
£-
0. &9
0. /06
0. H£
0, V6
0.ie<2
0.J00
Gas Temp.
(T)
406~
490
4f6~
4
-------
Proj *ct:
Date: £? • /?' 77
Location: /9
Onit: /_
VELOCITY TRAVERSE
Test Description!
Stack Cross Section
- /J%?
Personnel:
<£>'
Test:
Fuel:_
Barometric Press, (in. Hg):_
Absolute Static Press, in Stack (in. -By): -&.c*3 (P?>
Pitot Tube Coefficient; #, & <* (C_)
S5.4S
1/2
Time
Traverse Point
Port Depth
I*C *T .
a
7
/2
/7
. 0 7
<:?,
-------
Proj ect:
Date:
VELOCITY TRAVERSE
Test Description:
Location:
Onit:
Test:
Fuel:
Stack Cross Section
Personnel:
£p7- & /
~ ~
Barometric Press, (in. Hg):_
Absolute Static Press, in Stack (in. fig):_
pitot Tube Coefficient:
C
Vs •= 85.48 Cp
,1/2
Time
Traverse Point
Port Depth
/)lS,e>9^'
£?,/
0.0 7f
&,
#70
46
-------
VELOCITY TRAVERSE
Prelect:
Date: 8
Absolute Static Press, in Stack (in. jig): "~.,
Pitot Tube Coefficient: <
V - 85.48 Cp
1/2
i±
Tine
Traverse Point
Port Depth
/
} * git .
-.e>ts'
0,0?
0.03
0.0
-------
*roject:_
Date:
Iocation:_
Unit:
J3-
j_
Test: /?- /7C?
Fuel:
VELOCITY TRAVERSE
Test Description:
Personnel:
StacX Cross Section
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in.
/
Pitot Tube Coefficient: tP, SI3
(P.)
Vg - 85.48 Cp
,1/2
Time
Traverse Point
Port Depth
IWC
-------
VELOCITY TRAVERSE
Date: 3 - 3 - 77
location: /.f3 (P,) +
/60 •
Pitot Tube Coefficient: #.03 (Cp) -
I-T^-]1'2 i:::EEEEEEE
vs-«.«cp * :::::::;:::
L s sj
s Section
-(--
ii-i —
+ X_.
' i
__L
1
::::±j|:::::
Time
Traverse Point
Fort Depth
l*ct«
e
7
12
n
.t/
0.11
e>,/e>
£>,/0
Gas Temp.
CF)
^J-
&*>£-
J20
&£
&o
Gas Temp.
CR)
TS
Molecular
Wt.
"s
Velocity
(ft/sert
vs
°2
Cone.
(% Dry)
6002-13
203
-------
Pro j ect:
Date: _-?- 7-77
VELOCITY TRAVERSE
Test Description:
Location:
Onit: /_
Test; /y
Fuel:
Stack Cross Section
Personnel:
/l/al.
, 0 "?
Barometric Press, (in. Hg) :
Absolute Static Press, in Stack (in. Hg) :_
Pitot Tube Coefficient: _ .g3
(
85.48
11/2
Time
Traverse Point
Port Depth
\
}t" f^l .
s
7
/?
/I
S&0
Gas Tenji.
CR)
TS
Molecular
Ht.
«s
Velocity
(ft/seiH
vs
02
Cone.
(% Dry)
6002-13
2 04
-------
Project:
Date: 3-8 -
VELOCITY TRAVERSE
Test Description:
Location: (±
Unit: '
Stack Cross Section
Test:
Personnel:
Fuel: Mat. &
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in.Hgl:^
Pi tot Tube Coefficient; G. g?
(P,)
B5.4B
1/2
Time
Traverse Point
Port Depth
!i*et«.
2
7
IS
n
-------
Date
l/ff-
77
KVB. INC.
SOx DATA SHEET
TEST NO. /*7-S UNIT NO.
f-* ±
FUEL
LOAD
Jclb/hr
Test No.
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
x-/
I/ OS
6,1
0
O. 00d
-30.0$
J? /O
*-l
}/3J>
t-j
O
/.06d
^o.OX
/3JO
Calculation:
Excess 0-,
SO- or SO,, ppm =
_ (A - B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm =
,gm/dsem =
Emission ,E, g/Mcal c
Ib/MBtu =
ng/J =
C « pollutant concentration, g/dscn
F, volume factor
dscw'lO cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
so2
£(*.&
P-vj
10
10*1
•
SQ3
2.7
/
I.I
s°x
60-14
rev. 1/2/75
206
-------
Date
//r/77
K VB. INC
Test No.
SOx DATA SHEET
TEST NO. 7?-3 UNIT NO.
FUEL
LOAD
'___klb/hr
Box No.
Time
Temp, in Gas Meter
Press, in Gas Mete;
Meter Reading
Barom. Press.
Percent Cxyyt-.i:
$2 Purge Time
V/ *-.
\f*o
4f
O.r.r,f>
//'/>
/c-i.
//yy
7^
( * i.'
Ho*
(A
Calculation: SO, or SO,, ppm = —-
B) x N x F x (460 + T) x 24
V (P + p)
Excess 07
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
E
where
Cif 2090 \
EO.S-xOg I
•e L J
Concentration,C,
r^m/dscBt ~
Emission ,E, g/Mcal m
Ib/MBtii =
ng/J =
C = pollutant concentration, g/dscm 4
F, volume factor - dscm/10 cal
_dscf/lt)4 Btu
from Fed. Reg. 9/11/74 p 32856
so2
37.-)
ll&
so3
^-4-5"
)
0.11
S0x
60-14
rev. 1/2/75
207
-------
Date /
K V B. INC.
Test Ho. /f-.T
SOx DATA SHEET
TEST NO.
UNIT NO.
FUEL
LOAD
Jclb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
x-/
o Uo
*1
6
o . coo
?«J.'9
3J3L
J00o
X- /
0 1&
It,
6
j.ooo
"3 0
B = Ml of lead perchlorate used for bland = ££O
N = Normality of lead perchlorate titrant = 0.0/07^
F = Dilution factor = 1 ^
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration, C, ppm = f\\> £>
, gm/dscm =
Emission ,E, g/Mcal =
E - Clj 2090 Ib/MBtu "
where 1- •* ng/J =
C = pollutant concentration, g/dscm
F, volume factor « dscm/10 cal
dscf/lo4 B.
from Fed. Reg. 9/11/74 p 32856
+ T) x 24
so3
3-3-
/
1.0
rev. ;
«.
L/2/75
208
-------
Date
K VB, INC
Test No.
TEST NO.
UNIT NO.
SOx DATA SHEET
FUEL *) o/t. LOAD
_k.lb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N~2 Purge Time
y-O
0-:>
y<3^^
?v
c.
3. 0£a
3o,/-i
7,/x
/osg
Calculation: S03 or S02, ppm = (A ~ B) x-
F x (460 + T) x 24
V (P + p)
Excess On
3,
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant =
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
, gm/dscm
Emission ,E, g/Mcal
Ib/MBtii
ng/J =
E - c:
where
a" 2090 1
EO.g-XOj I
i l» J
C = pollutant concentration, g/dscm ^
F, volume factor - dscVIO
dscf/104
from Fed. Reg. 9/11/74 p 32856
so2
^Tj
=E
„
JO
— :
«
_
_
°ll.(s
m
'
so3
t,,fO
/
o.ez
sox
60-14
rev. 1/2/75
209
-------
Date
.l-n
TEST NO.
UNIT NO.
KVB. INC.
SOx DATA SHEET
FUEL
_klb/hr
Test No.
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Y-l
/oT>0
3i
b
0,000
1o.li
l./i
l/oo
r-l
J0?£
IB
0 '
•$.000
"},/
-------
Date
K VB. INC.
Test No.
SOx DATA SHEET
TEST NO.
UNIT NO.
FUEL
LOAD
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press .
Percent Oxygen
N2 Purge Time
*-/
ins
70
0
0
J1.->1
uii
>r- /
//!£>
7J-
0
1.0
29.73
l*ol
Calculation: S03 or SO.,, ppm = (A - B) x N x^ ^x |460 + T) x 24
Excess 0,
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter (ati) =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
.Concentration^, ppm =
= CF[ 209O I
EO.^-XOj I
lere L J
E
where
Emission ,"E, g/Mcal
Ib/MBtu
ng/J
so2
10.**-
f.r
d ,0 lot')
1°
531
l.o
^"7-75
6
33
so3
3^.^
«?.$•
0.010^
(
5">l
/.o
J?,73
O
/0i.t>
S0x
)
C «= pollutant concentration, g/dscm 4
F, volume factor = _dscm/10 cal
_dscf/lC)4 Btu
trom Fed. Reg. 9/11/74 p 32856
60-14
rev. 1/2/75
2 1
-------
Date
K VB. INC.
Test No.
TEST NO. l1-~>i UNIT NO.
SOx DATA SHEET
FUEL **3 O/i- LOAD
klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
X'^
//V5
Id
0
0
l>l
Calculation: S03 or SO.,, ppm = <* " B) x N x F x (460 + T) x 24
Excess O2 %
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter (*
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
E
where
CfT 2090 [
EO.g-xc^
e L. J
C = pollutant concentration, g/dsca
F, volume factor « dscni
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
V (P + p)
so2
for sample = /£.£•
for bland = ^>S~
e titrant = tf.tfA'Tf
IO
*£) = 5-3 ~7
, gm/dscm "
,E, g/Mcal -
Ib/HBtii "
ng/J =
O4 cal
04Btu
so3
/O.I
9-5
0. Of 6 7-9
/
£">•}
A<3
J9.73
0
?.*>
sox
60-14
rev. 1/2/75
2 1 2
-------
Date
K VB. INC
Test No._/f-7_y
TEST NO.
UNIT NO.
SOx DATA SHEET
FUEL #30/1. LOAD
_klb/hr
Location le,
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
y-/
/2/s
V
0
0
Jl.ll
111?
r-J
/J30
go
o
1.0
P?,?3
flof
= u, or &u_
Excess 0-, %
A = Ml of lead perchlora
B = Ml of lead perchlora
N = Normality of lead pe
F = Dilution factor
T = Average temp, in gas
V = Volume of gas sample
P = Barometric pressure
p = Pressure in gas mete
E = Clf 2090 1
bo.s-xo, 1
where •- *J
C = pollutant concentration,
F, volume factor «
from Fed. Rea. 9/11/74 o 328
' Ppm - v (P + pi--
so2
te used for sample = 10.^
te used for bland = ^-^
rchlorate titrant = O.OfOl0!
10
meter (°#-) = Z'Yb
ft3 ' = 1,0
1 h/MBtil *
ng/J =
/^ r. n
g/dson /^A-p rUR-6
dscm/10 cal v
dscf/104 R^,,
56
so3
?/'>"
b
P?.??
O
)0^
sox
60-14
rev. 1/2/75
2 1 3
-------
Date / -
K VB. INC.
Test No.
TEST NO. /?-7f UNIT NO.
SOx DATA SHEET
FUEL *?fl//. LOAD_
Jclb/hr
Location / j
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
^-/
012Z
7/
0
C
*).lo
0
Ol¥7
-%-/
0 *2-i"
70
O
/.osr
29. to
O
09/3
m
Calculation: SO, or S0_, ppm
Excess 02 0 %
(A - B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
P = Pressure in gas meter =
Concentration^, ppm =
rgm/dscm -
Emission ,E, g/Mcal «
Ib/MBtu "
ng/J =
E
where
CtT 2090 1
bo.9-xc^
e I- ••
so2
3L.4
9.0
.0/079
/O
S2I*R
/.of
2?, W
0
tze*f
so3
/O. 7
9.0
.0/071
/
*3/°Z
/.Of
sl.to
0
7
S0x
C • pollutant concentration) g/dscm
F, volume factor «
dsca/10 cal
-from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
60-14
rev. 1/2/75
2 1 4
-------
Date /-.g<9-7f
KVB, INC.
Test No.
TEST NO./?-7g UNIT N0._
SOx DATA SHEET
LOAD
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
•Z.-Z
o?2?
73
O
O
tf.to
O
ojy?
X-2.
0927
7l
O
/.o
23. SO
£
/007
Calculation: SO3 or S02, ppm = (A - B) x N x^F ^ |460 + T) x 24
Excess O2 0 *
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm =
,gm/dscm =
Emission ,E, g/Mcal -
Ib/MBtu =
ng/J -
E
where
Ct[ 2090 \
bo.a-xoj I
•e L J
S02
33,6
9-o
.0/079
/O
S-37
/.O
£9.$0
a
Ht~J
so3
/O.I
9-0
.0/07*}
/
S-37
/.O^
s9.g£>
O
s-
sox
C = pollutant concentration, g/dscm 4
P, volume factor - _dscn/10 cal
dscf/104 Bfcu
from Fed. Reg. 9/11/74 p 32856
60-14
rev. 1/2/75
2 1 b
-------
Date
- 77_
K VB. INC.
Test No.
TEST NO./7-E2UNIT NO.
SOx DATA SHEET
LOAD
_klb/hr Location /?
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
z-/
/¥£.&
13
O
O
29, to
.9
/•yya
Z'/
/9S^
Z3
O
/, v
29. to
. 9
/s~co
Calculation: SO, or SO-, ppm =
Excess O2 0' i %
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
Emission ,E, g/Mcal
E » CFj 2090 I Ib/MBtii
Co. 9-xo.) I
where *• ^ ng/J
C = pollutant concentration, g/dscm
F, volume factor
cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
x 24
so2
5~. 9
3-3~
.&/07J
/O
S-
^y-2i?
Q
L.I
s°x
60-14
rev. 1/2/75
2 1 6
-------
Date I-2O-77
KVB. INC.
Test No. /9-S3
TEST NO. /?-£? UNIT NO.
SOx DATA SHEET
_ FUEL ^0/6 LOAD /»». rkib/hr Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Z-*
/YW
*??
= / o
meter * «5"r fc
f t3 = /, O
r =0
lb/MRtw * H
g/dscm ,
dscaVlO cal
dscf/lO* Ptl1
te
so3 sox
/,4
5.^
,0/07?
/
f¥(f
/.o
29.80
0
f.*
60-14
rev. 1/2/75
2 1 7
-------
Date
-20-77
KVB. INC.
Test No.
SOx DATA SHEET
TEST NO./9-£? UNIT NO.
FUEL
LOAD
klb/hr _ Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press .
Percent Oxygen
N2 Purge Time
*-/
/J-/^
9o
b
0
*9.go
.9
^- /
/r.*y
«•*
0
/.o
39. BO
.1
= (A- B) x N
(460 + T) x 24
Excess O-> . 7 *
A =
B =
N =
F =
T =
V =
P =
P =
E -
' PF1" V (P + p)
so?
Ml of lead perchlorate used for sample = S~- Z
Ml of lead perchlorate used for bland = g.S'
Normality of lead pe
Dilution factor
Average temp, in gas
Volume of gas sample
Barometric pressure
Pressure in gas mete
CFI 2090
f^c^J
where L J
C « pollutant concentration,
P, volume factor «
from
rchlorate titrant = , £>/(S79
/£>
meter = S~Y9
ft3 = /, 0
2C£D
r = &
Concentration, C, ppm = O /
, mn/dscm =
Emission ,E, g/Hcal "
lb/MBtu =
ng/J =
g/dscm
dscm/10 cal
dscf/104 „_.
Fed. Reg. 9/11/74 p 32856
so3
9.L
3>±"
. 0/079
/
•£~y9
/. 0
tf.lo
o
S.2
sox
60-14
rev. 1/2/75
2 1 8
-------
Date /-,gy -77
KVB, INC.
Test No./?-
SOx DATA SHEET
TEST NO./9-97 UNIT NO.
FUEL *lONLOAD /3. F klb/hr Location /
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
r-/
/ozz.
?6
o
o
30. M
HO?
7>- f
/o^-jr
17
0
2.700
2o./6>
//2f
Calculation: SO, or S0_, ppm =
(A - B) x H x F x (460 + T) x 24
V (P + p)
Excess
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration^, ppm
E - Cti 2090
EO. 9—xf
I *
where u
Emission ,E, g/Mcal
Ib/MBtii
ng/J
so2
22. /
4./
.0/07 9
/o
^••f?
2- 7t>°
so-tt*
O
2/3
so3
&./
r^. /
.0/C79
1
jT/7
Z, 70&
30. /6
O
3.S
sox
C = pollutant concentration, g/dscm 4
F, volume factor - dscm/10 cal
dscf/lO* Btu
from Fed. Reg. 9/11/74 p 32856
60-14
rev. 1/2/75
2 1
-------
Date /- **- 77
KVB. INC.
Test No. /f- ?7
TEST NO. /9-97 UNIT NO.
SOx DATA SHEET
FUEL *6> LOAD /3. % klb/hr Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
7- -2
//oc
?7
O
O
2&. Ho
ti 3J."
%~*
1/20
e *
o
2.200
30. /^
n**'
- B) x N x F x (460 + T) x 24
Excess 02 %
' **"" V (P + p)
so2
A = Ml of lead perchlorate used for sample = /£"•£>
B = Ml of lead perchlorate used for bland = */• 1
N = Normality of lead perchlorate titrant = tC>/t>79
F = Dilution factor
T = Average temp, in gas
V = Volume of gas sample
P = Barometric pressure
/a
meter = 5" f E
ft3 = i?.£0O
^C>.Jlf
p = Pressure in gas meter = O
E - CF[ 2090 \
pO.S-xo. 1
where *- ^
C = pollutant concentration,
F, volume factor •
Concentration, C, ppm = ^?T7
,vnn/dsan "=
Emission ,E, g/Hcal «=
Ib/MBtii *
ng/J =
g/dscm
dscm/10 cal
dscf/104 «,..„
from Fed. Reg. 9/11/74 p 32856
so3
^-. s
y. /
.6/079
/
£"
-------
Date /-.gy-77
KVB. INC
Test No. /9-?7
TEST NO./*-?/ UNIT NO.
SOx DATA SHEET
FUEL
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
/£-/
IIZ^
s?
0
o
30- /&
//si
-%.-'/
S/3&
9o
o
S-7CO
SQ./&
Calculation: S03 or S02, ppm = (A " B) x N
(460 + T) x 24
Excess
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
,gn/dsan
Emission ,E, g/Mcal
Ib/MBtu
ng/J
E
where
dT 2090 j
BO.S-xo, I
* !• ^
S02
J3./
^'. /
.6/C7?
/£>
£~£~C>
a. ?oo
3.O-/&
o
33Z
so3
6.c
?./
.0/C7?
/
S-S-G
ff.fOO
20. /(,
o
5.3
s°x
C = pollutant concentration, g/dson ^
F, volume factor « _dscm/10 cal
_dscf/lt)4 Btu
from Fed. Reg. 9/11/74 p 32856
60-14
rev. 1/2/75
22 1
-------
Date /-•
- 77
KVB, INC.
Test No. J9-//&,
TEST
UNIT NO.
SOX DATA SHEET
FUEL ? o/i LOAD
klb/hr _ Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
£
Oil' 7
77
0
c
21.7Z
/02±"
2
/02G
7~r
o
Z.ooo
*?.?*
/0y-s"
Calculation: SO, or SO., ppm =
- B) x N
Excess 0
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
,gm/dson
Emission ,E, g/Mcal
E » Clf 2090 | It/MBtii
fco.S-xOj
where L J ng/J
C * pollutant concentration, g/dscm
F, volume factor «
dscm/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
M60 4 T) x 24
so2
?.S
x.e*
.0/079
/o
-S-J7
"3. ooo
S9.7Z
0
27
so3
S. 7
y.c
.6*079
/
JT37
2.£>f>o
J9.72
O
/.7
sox
60-14
rev. 1/2/75
222
-------
Date
K VB. INC.
Test No./?- //(.
SOx DATA SHEET
TEST NO. /?-//£ UNIT NO.
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
/
/en?
7*
O
o
29.72
s/oo
/
/o^^r
ID
0
3. oo o
29.72
tt 2,0
Calculation- 50 or -0 ppm - (A ~ B) x N x F x (46° + T) x 24
Excess Oj %
so2
A = Ml of lead perchlorate used for sample = $ - O
B = Ml of lead perchlorate used for bland = -?•£>
N = Normality of lead perchlorate titrant = , O/07?
F = Dilution factor = '0
T = Average tpmp. in gas meter = i-3/
V = Volume of gacs esamplp ft3 = 3-OOO
P = Barometric pr^ssurs ^ *7*7^
p = Pressur© in gas m^ter =s
.?-*'
;
60-14
rev. 1/2/75
223
-------
Date l-
K VB, INC.
Test No.
TEST NO.
UNIT NO.
SOx DATA SHEET
FUEL *?e/cLOAD
fclb/hr
Location /
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
Nj Purge Time
/
/~
Calculation:
Excess O,
S03 or S02, ppm =
- B) x K x F x (460 + T)
V (P 4 p)
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
rtjm/dscm
Emission-,E, g/Mcal
E = Cl] 2090 | * li/MBtu
bo.s-xoj I
where •- J ng/J •.
C = pollutant concentration, g/dscm
so2
s-.*
3.t*
,0/0?9
/o
^/6,
x-otf
X.9.72.
O
£-0
•-
so3
^.8
3.L
.6/07'$
/
£"S6>
2,0*7
21.7T-
•o
,V7
S0x
F, volume factor
from Fed. Reg. 9/11/74 p 32856
cal
Btu
60-14
rev. 1/2/75
224
-------
Date
K VB. INC.
Test No. /9~ S3
SOx DATA SHEET
TEST NO./?-/S2 UNIT NO.
FUEL
LOAD
klb/hr
Location /
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Z-2
,0?2S
6*
O
0
so./*
. 9$
/-/2
O
y..**
sox
'
C = pollutant concentration, g/dsem 4
F, volume factor - dscVIO cal
from Fed. Reg. 9/11/74 p 32856
Btu
60-14
rev. 1/2/75
225
-------
Date S-/7-77
TEST NO. /9-/32UNIT NO.
K VB. INC.
SOX DATA SHEET
Test No. //-/.?
FUEL
LOAD /?. 5*" xib/hr _ Location /?
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Tt-f
so//
7$
0
D
30./2
.<>*
/C3Z
•z.-/
/02C,
«z
O
J, 0
30./2
. 9^
S//3
Calculation: SO, or S0_, ppm =
2'
(A - B) x N X F x (460 + T) x 24
V (P + p)
Excess
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm =
,gm/dscni =
Emission ,E, g/Mcal =
E - CFJ 2090 ' Ib/MBtu =
Lo.S-xc^
where *- J ng/J =
C = pollutant concentration, g/dscm
F, volume factor «
dscm/10 cal
froni Fed. Reg. 9/11/74 p 32856
dscf/104
Btu
so2
/A *
s. y
. 0/07
/O
£-yo
/,0
3&-IS
O
W
"
,
•-
so3
5.y
*. v
.0/07
/
^-c/o
s.o
ZQ.J*
O
*.&
sox
60-14
rev. 1/2/75
226
-------
Date A-/7-77
K VB, INC.
SOx DATA SHEET
Test No. / 9-
TEST NO.
UNIT NO.
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
T£-2
/£>V3
1*.
O
o
-$Q.tZ
.9*
///*'
-z-z
/say
$3
&
/.o
30. / 2.
. 9*'
s/y*
Calculation: SO, or SO_/ ppm =
Excess 0-,
B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm
, gjn/dscm
Emission -,Z, g/Mcal
' Ib/MBtU
ng/J
C = pollutant concentration, g/dscm 4
T, volume factor = dscm/10 cal
so2
J3.0
*.*
.0/01
10
s-vz.
/.o
36. /*
O
Vtf
••
so3
5-7
a.f
.<9/o7
/
m
/.O )
so./*
0
{>
S0x
Btu
from Fed. Reg. 9/11/74 p 32B56
60-14
rev. 1/2/75
227
-------
Date
- 7 7
K VB. INC.
SOx DATA SHEET
TEST NO./9-/43UNIT NO. FUEI/^£_ LOAD S3-(* klb/hr Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
7^-2
;&/7
30
o
o
39.®
3./
/037
?>-*•
/OS'S
zo
cD
/.€>
2
-------
Date
K VB. INC.
Test No.
SOx DATA SHEET
TEST NO.
UNIT N0.
FUEL
LOAD_/£Jp__klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
•z-/
/OV-*
BO
O
0
29-V/
-3,1
?-/
/SOV
31
0
/. 0
29. 8/
3>/
Calculation: S03 or S02f ppm - (A - B) x N x F x (460 + T) x 24
Excess 0
B = Ml of lead perchlorate used for bland
S = Normality of lead perchlor
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
- ClT 2090 I
po.s-xo,
lere "- ^
E
where
C = pollutant concentration, g/dson 4
?i volume factor = dscnv'lO cal
from Fed. Reg. 9/11/74 p 32856
V (P + p)
so2
for sample = /£• O
for bland = V.-S'
e titrant = .QiGI
JO
5-yo
AO
j?9.2/
C>
+ i nn _ P . nnm ^ ^TO
. V i-i/Mr-»l K
lb/MBt" c
na/J =
LO4 cal
"»*Btu
so3
f-/
4.1'
.0/0-7
1
£-
-------
Date
-77
K VB, INC.
Test Mo.
SOx DATA SHEET
TEST NO. /9-/7JUNIT NO. FUEL*"£ LOAD /g
xib/hr
JLocation
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Z-*
///>
*v
0
£
tf.il
3.1
>JV<*
•z~*
MV/
9o
0
AO
jf^SI
3.}
/ZJ^
Calculation: S03 or S02, ppm = (A " B) * N */ (* <**° + T) x 24
Excess O? 3. / %
so
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
K = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm =
S.O
3*1
E
where
Ct{ 2090 |
bo.S-xcij
•e *- ••
Emission-,E, g/Mcal -
Ib/MBtu =
ng/J =
C = pollutant concentration, g/dsem
F, volume factor = dscm/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/104
Btu
so
'. C
S.O
60-14
rev. 1/2/75
230
-------
Date
KVB, INC.
Test No. / ?-
SOx DATA SHEET
TEST NO._/^/£?UNIT NO.
FUEL
LOADyV.Q fcib/hr Location
BOX No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
K-/
ctvz
/o2
o
O
3o.o2
/.?*-
/OOS'
*-/
C9S?
so?
a
/. 0
30. OH
/. 73~
S0SJ3
Calculation- SO or SO ppm - (A ~ B) x N x F x (46°
uaj.i,Lu.cn.xi-iii. ouj ui ^^2' FF"' V (P + p)
Excess O2 /. 7.1 %
so2 j
A = Ml of lead perchlorate used for sample = /^-£
B = Ml of lead perchlorate used for bland — ^'7 I
N = Normality of lead perchlorate titrant = .OJ&7
F = Dilution factor = /^
T ~ Average temp . in gas meter = *5fo &
V = Volume of gas sample ft3 = /*O
P = BaTDTn^t-ri c pf^eeiir1^ = 3^* Oc
pD/S-xbu 1
C = pollutant concentration, g/dscm ^
P. volume factor = dscVlO cal
dscf/104 p.).,,
f T) x 24
so3
7.y
6-7
.0/07
t
5^ VP •*
/,o
_3O • ^o
o
•3.3
60-14
s°x
23
-------
Date
K VB. INC.
Test No.
SOx DATA SHEET
TEST NO. /9-/:> UNIT NO.
FUEL
LOAD_^£_kib/hr _ Location /9
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
?-z
/o/z.
/£>'
*'Z
/o 3,0
/61
O
/.o
30. 0$
/.7
//O^
Calculation:
Excess o, A 7
SO. or S0_, ppm =
- B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm =
/ gjn/dscm =
Emission-,E, g/Mcal =
Ib/MBtii =
ng/J =
C = pollutant concentration, g/dscm
f, volume factor = dscn/10 cal
so2
/y-y
6.7
.0/07
/o
^?
/•o
30. og
0
IT/
••
so3
7,2
4.7
.0/07
/
£-6><}
/,O
36-0?
O
*.
-------
Date 2-2 3-7V
K VB. INC.
Test No.
SOx DATA SHEET
TEST NO. ;?-
UNIT NO.
FUEL
LOAD^£_klb/hr Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
7-/
/£>•/
O
o
36.t>$
/.7
)t07
-z~/
//£>.e>*
&
33 1
so3
7.1
1.7
.0/07
/
S7C
/.o
26.6%
O
1.7
sox
C = pollutant concentration, g/dscm ^
F, volume factor •= dscn/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/!04 Btu
60-14
rev. 1/2/75
233
-------
Date S-/-77
K VB. INC.
Test No. //- J7O
TEST NO./?-/70 UNIT NO.
gOx DATA SHEET
FUEL *<£ LOAD /•/. / klb/hr
Location /J
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
2
S/02
/Of
o
0
*
-------
Date 2-/-?7
TEST NO. /?-/ 70 UNIT NO.
K VB, INC
SOx DATA-SHEET
FUEL
LOAD
klb/hr _ Location
BOX NO.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
»2 Purge Time
/
)/2C
///
O
0
Z9.9S
o o
29.92
y.z
J232,
(A - B) x N x F x (460 + T) x 24
Calculation: SO, or S02 , ppm -
Excess o,
A = Ml of lead perchlorate us
B = Ml of lead perchlorate us
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
E = CFJ2090
K0.9-XC
where ^-
C = pollutant concentration, g/dscm
F, volume factor = __dsan
from Fed. Reg. 9/11/74 p 32856
V (P + p)
so2
for sample = /v?. 3-
for bland = &•'
e titrant = . O/O/
/£>
-T7/
— /, o
-??.?2
- £>
IK/MR+'il =
so3
S.¥
D
.O/ol
/
£-?/
/.O
&.n
0
£,?
S0x
)
LO4 cal
L04 Btu 60-"
Btu rev. 1/2/75
235
-------
Date 3-/- 77
K V B, INC.
Test No. /9- /7O
TEST NO./?-/70 UNIT NO.
SOx DATA SHEET
FUEL *<£ LOAD
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
£
/£//
//2
O
o
ft, 9 8
0
29.<}2
p = Pressure in gas meter = O
E = ClT 2090 I
bo.S-xoJ
where «- J
C = pollutant concentration,
F, volume factor B
Concentration^/ ppm = £fff
,gjn/dsan =
Emission -,E, g/Mcal =
l±>/MBtu =
ng/J =
g/dson J?O /JO7~ /Jj.
dscm/10 cal J-££T /*) /4\>
dscf/104 «...
from Fed. Reg. 9/11/74 p 32856
so3 sox
70
£.9
.0/0 /
/
JT7/
A0O
^?.?^
O
^
-------
Date 2-E-77
TEST NO.. '
UNIT NO.
K V B. INC.
SOx DATA SHEET
FUEL
Test so.
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
•%-/
/C23.
9o
o
o
SO. 39
3.6
JO^Z
I-/
/os-o
92
0
/. ooo
30.3?
5-6
//.ez.
Calculation: SO, or S0_» ppm
(A - B) x
Excess o,
3>6f
x F x (460 + T) x 24
V (P + p)
so
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration^, ppm —
,gm/dscm =
Emission ,£, g/Mcal "
Ib/MBtu *
ng/J -
/o
/•o
97
E
where
CfT 2090 I
bo.g-xoj I
•P L J
C = pollutant concentration, g/dscan ^
F, volume factor = ___ascnv'10 cal
dscf/104
from Fed. Reg. 9/11/74 p 32856
Btu
so
6.Z
S0
60-14
rev. 1/2/75
237
-------
Date 2-3-77
K VB. INC.
Test No.
TEST NO.,
UNIT NO.
SOx DATA SHEET
LOAD
klb/hr _ Location J '?
Box NO.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
V>2 Purge Time
%-.£
//o-z
99
O
o
se.sy
3<&
//*oQ
30.3V
2.(.
//S3
- (A - B) x N x F x (460 + T) x 24
= '
Excess "2 2' d> %
' «"" V (P + p)
so2
A = Ml of lead perchlorate used for sample = ?• V
B = Ml of lead perchlora
N = Normality of lead pe
F = Dilution factor
T = Average temp, in gas
V = Volume of gas sample
P = Barometric pressure
p = Pressure in gas mete
E - CF| 2090 1
bo.s-.cJ
where *- J
C «= pollutant concentration,
T, volume factor =
te used for bland = &.SL
rchlorate titrant = • Q/D /
/O
meter = £~&> 0
ft3 = J.O
30. 3
-------
Date 3-3- 77
K VB. INC.
Test No. / £-
TEST NO./?"'7? UNIT NO._
SOx DATA SHEET
LOAD
Jclb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
•z-/
/A3?
/&-o
o
G
Zo.sy
3--i"
//^6>
?-/
S/^ro
/£>O
0
/,o
30-3Y
3.*'
/zi-y
- B) x N x F x (460 + T) x 24
Calculation: su._ or au_
S<^
- L --* %
' ppm v -(P + p)
so2
A = Ml of lead perchlorate used for sample = ?-^>
B = Ml of lead perchlora
N = Normality of lead pe
F = Dilution factor
T ~ Average temp . in gas
V = Volume of gas sample
p = Pressure in gas mete
E = Cjf 2090 1
ho.e-xoJ
where u J
C = pollutant concentration,
F. volume factor =
te used for bland = 6"*
rchlorate titrant = ,O/t>'
SO
meter = S'teU
ft3 - /- 0
r - 0
Emission ,E, g/Mcal "
Ib/MBtu = ___ _
g/dscm .
dscm/10 cal
dscf/lO* B,.,,
so3 sox
6- y
t.*
.O/O/
/
3-^0
/• o
30. zy
o
t.v
— —
60-14
1 /I /Id
239
-------
Date J?-7- 77
K VB. INC.
Test No.
TEST NO./9-/9O UNIT N0._
SOx DATA SHEET
FUEL g/f s LOAD_
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
t-z
095-X
99
0
o
36.0"?
3.2
/£>/<£'
•Jt-Z
/oo^
99
c
/.o
30.07
3.*>
SQVO
Calculation: SO- or S0_, ppm =
Excess O2 3'& %
_ (A - B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration, C, ppm =
CFJ 209
bo.S-
re »-
E = CF 2090
b
where
Emission -,E, g/Mcal =
- Ib/MBtu =
ng/J =
so2
6.3
*r.*
. 0/0 /
JO
^9
t.o
So. o~?
O
37
•-
so3
*.<*
£-.^"
.£>/&/
/
s-fj
/.o
30.07
O
.C
S0x
C = pollutant concentration, g/dson
F, volume factor = dscm/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
60-14
rev. 1/2/75
240
-------
- 7 - 7 7
K VB. INC.
Test No. II-
TEST NO.UNIT N0.
SOx DATA SHEET
LOAD
_klb/hr Location /'7
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
Nj Purge Time
•Z-/
/OS./
??
o
a
30.07
2.2
Wf
?-/
/037
/oo
0
/.oo
30.Q7
2.«
///J"
Calculation: S03 or S02, ppm = (A - B) x N x^F * U60 + T) x 24
Excess 0,
so
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm —
,tnn/dscm =
Emission-,E, g/Mcal "
Ib/MBtu =
ng/J =
.0/0 /
JO
/.OO
O
E
where
of 2090 I
K0.9-XO, I
-P L J
so
30. o7
so
C = pollutant concentration, g/dson ^
F, volume factor = ason/10 cal
dscf/104
from Fed. Reg. 9/11/74 p 32856
Btu
60-14
rev. 1/2/75
24 1
-------
Date 3-7- 77
K VB. INC.
SOx DATA SHEET
Test No.
TEST NO. /'
UNIT NO.
FUEL £/>*, LOAD
_klb/hr Location / ?
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
"-X.-S.
/e>.r.i-"
/O3.
o
0
30.07
2.2-
j/'Z
t-2
///2-
/OZ- j
o
S.oo
30.07
3.*
j/yo
Calculation:
Excess 02 3-
50
3 or S02, ppm =
- B) x N x F x (460 + T) x 24
V (P + p)
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,Cr ppm =
,gm/dscm -
Emission-,E, g/Mcal =
E = CIf 209° I ' Ib/MBtu -
EO.S-XOj
where L J ng/J =
C = pollutant concentration, g/dscm
so2
&,?>
s.f
.oso/
/o
£•£2
/.OO
30.07
0
3$
•-
so3
f.t
J'.J"
. o/o/
/
*r&*
S,6>0
30.07
0
/.*'
SOX
F, volume factor
dscm/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
Btu
60-14
rev. 1/2/75
242
-------
Date 3- ?- 77
TEST NO./?-/?.£ UNIT NO.
K VB. INC.
SOx DATA SHEET
Test No. /?-
FUEL
LOAD
J<.lb/hr
Location
BOX No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
•z-/
s^zz
/OS
o
0
30.0-7
V.2
ATf£
-z-/
S^-VO j
/03
0
/. 00 0
30.e>~)
V.-3-
/&//
Calculation:
Excess Oj /' •
S03 or SO,, ppm =
%
- B) x N x F x (460 -f T) x 24
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas meter
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
C =•pollutant concentration, g/dson
F, volume factor = dscm
from Fed. Reg. 9/11/74 p 32856
V (P + p)
so2
for sample = A?. £
for bland = •£"• f»
e titrant = • £>/°/
/o
£--Q 7
O
tion , C / ppm -^ '
,gm/dscm " _
,E, g/Mcal •= .
Ib/MBtii " —
ng/J «=
LO4 cal
«»*Btu
SO,
^-.2
^•C
.0/0}
/
£~&2
/,dO)
30.07
0
9
— —
.
.
60-14
rev.
sox
• —
•
1/2/75
24 3
-------
Date 3-7-?7
K VB, INC.
Test No. /!?-/?-^
SOx DATA SHEET
TEST NO. /?-/#? UNIT NO.
FUEL
LOAD
_klb/hr Location / ?
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Baroro. Press.
Percent Oxygen
N2 Purge Time
•z-*
/-r.T2
/£>&
30-07
y./
/£?/
Calculation: SO, or S0_, ppm = (A ~ B*
460 + T) X 24
Excess O->
A = Ml of lead perchlorate used for sample
B = Ml of lead perchlorate used for bland
N = Normality of lead perchlorate titrant
F = Dilution factor
T = Average temp, in gas met«r
V = Volume of gas sample ft3
P = Barometric pressure
p = Pressure in gas meter
Concentration,C, ppm
/gm/dscm
Emission-,E, g/Mcal
* Ib/MBtu
ng/J
C = pollutant concentration, g/dscin
so2
J2>l
^,<*
.£>/£>/
/O
^&y
/,eo
30.0?
o
*9£
• -
so3
^;/
^.6,
.O/O/
/
JT60
30,07
0
O
SOX
F, volvnne factor
dscm/10 cal
from Fed. Reg. 9/11/74 p 32856
_dscf/lo4
60-14
rev. 1/2/75
244
-------
Date
- 77
K VB, INC.
Test No.
SOx DATA SHEET
TEST NO;
UNIT NO.
FUEL
LOAD
_klb/hr
Location
BOX No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
t-2.
St,z2
JOS'
0
o
2.0.0 ~7
?./
/^V3
T-3
-X639
/ 07
O
/,ooo
3o-°~? •
W
J7/0
Calculation:
or
ppm =
(A - B) x N x F x (460 + T) x 24
Excess O2
'f
V (P + p)
so
A = Ml of lead perchlorate used for sample =
B = Ml of lead perchlorate used for bland =
N = Normality of lead perchlorate titrant =
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter =
Concentration,C, ppm
f gm/dscm
Emission-,E, g/Mcal
Ib/MBtii
ng/J
C = pollutant concentration, g/dscm .
F, volume factor = _dscm/10 cal
/£>
20,07
O
so
g./
.6/0 /
20.07
so
from Fed. Reg. 9/11/74 p 32856
_dscf/lC>4
Btu
60-14
rev. 1/2/75
245
-------
KVB
SASS SAMPLING CONDITIONS
Test Site Location //
Sample Port Location
on >"^<^/C c:
Stack Velocity
Stack Temp. $
v/V- (let*- rt'l
f t/min T 60 =
/3 °F + 460 = T =
wz)
v = J*-,
<773
1'°l ft/se.
°R
Stack Moisture; BWQ = OJO
Particulate Loading (Method 5) , C = N * ^ grams/DSm
Probe Hozzle Size for 4.0 ACFM (wet) through cyclones at 400 °F:
Isokinetic Size = 0.1192 x /T /V = #. "*/ inches
s s — * -
Closest Actual Nozzle Size, D = 0, ~?£ inches
n -
% Isokinetic @ 4 WACFM, Actual Nozzle = 1.421 x T /(V xD2) =
s s n
If % Iso not in range of 90 to 110%, Adjust Cyclone Flow by:
Qcyc = 2'814 x (% ISO) x Vs X °n/Ts = ^° Wet ACFM
If % Iso @ 4 WACFM is greater than 110, use (% Iso) = 110
If % Iso @ 4 WACFM is less than 90, use (% Iso) = 90
Orifice Pressure Differential, H
Meter Temp., T = /W °F + 460 = £^3. °R (use 560 °R for estimate)
m — — — •• — -
Meter Flow Rate, Q =Q xT x(l.-B )/860 = .& DCFM
m eye m wo —~ — — — — -
Orifice No. (1, 2, 3) = 2 _ , J = 0.78, D = 0.281 , J x D2 = 0.062
- o - o
Orifice Press Diff . , H = 1.108 x (Q /J D2)2/T = «=?•#£- in. H 0
m o m - 2
Dry Gas Volume to be Collected (5 hour run)
V = Qx60 x5 =
Estimated Condensate Collection
Vlc = Vm X 53° x Bwo/[°'0474 x Tm x (1- * Bwo)] = ^^ ? ml
Estimated Particulate Collection
Mn = C x Vm x 530/ (T x 35.3) = ~" grams 0- V^^ by
246
Data Sheet 6002-17
-------
KVB
SASS SAMPLING CONDITIONS
Test Site Location / I
Sample Port Location_
Stack Conditions: Stack Velocity _ ft/min T 60 = V = j Stack Temp. -S /^> °F + 460 = T= =
s
Stack Moisture; BWQ = 0»Q?O
Particulate Loading (Method 5), C = grams/DSm
Probe Nozzle Size for 4.0 ACFM (wet) through cyclones at 400 °F:
Closest Actual Nozzle Size, D = ' inches
n - = -
% Isokinetic @ 4 WACFM, Actual Nozzle = 1.421 x T /(V xD2) =
s s n
If % Iso not in range of 90 to 110%, Adjust Cyclone Flow by:
Q = 2.814 x (% Iso) x V x D2/T = V> O wet ACFM
If % Iso @ 4 WACFM is greater than 110, use (% Iso) = 110
If % Iso @ 4 WACFM is less than 90, use (% Iso) = 90
Orifice Pressure Differential, H
Meter Temp., T = /•*? °F + 460 = ^& °R (use 560 °R for estimate)
m ~~. -
Meter Flow Rate, Q = Q x T x (1. - B J/860 = £. 3 / DCFM
m eye m wo
Orifice No. (1, 2, 3) = _2 _ , J = 0.78, DQ = 0.281 , J x DQ = 0-062.
in- H°
Orifice Press Diff . , H = 1.108 x (0_m/J D)/^ = ' in- H2
Dry Gas Volume to be Collected (5 hour run)
V = Q x 60 X 5 = /// DCF
m *m tJJ—
Estimated Condensate Collection
x 530 x Bwo/[0.0474 x Tm x (1. - B^,) 1 -
Estimated Particulate Collection
'** T
247
M = C x V X 530/(T X 35.3) = "~ - ?rams
n m m
Data Sheet 6002-17
-------
KVB
SASS SAMPLING CONDITIONS
Test Site Location 7*?
Sample Port Location > ^c £- <*= X / ~ ' ' ' -
Stack Conditions: Stack Velocity ft/min ^ 60 = V= = ^ V> ^? ft/sec
APC O. |
' S'
stack Temp. O °F + 460 = T =
Stack Moisture; BWQ
_
Particulate Loading (Method 5) , C = _ grams /DSm
Probe Nozzle Size for 4.0 ACFM (wet) through cyclones at 400 °F:
Closest Actual Nozzle Size, D = D f~7 £ inches
n -
% Isokinetic @ 4 WACFM, Actual Nozzle = 1.421 x T /(V xD ) =
s s n - —
If % Iso not in range of 90 to 110%, Adjust Cyclone Flow by:
Q = 2.814 X (% Iso) x V x D2/T = ^ • O wet ACFM
eye s n s -
If % Iso @ 4 WACFM is greater than 110, use (% Iso) = 110
If % Iso @ 4 WACFM is less than 90, use (% Iso) = 90
Orifice Pressure Differential, H
Meter Temp., T = /DO °F + 460 = £&&°R (use 560 °R for estimate)
m - -
Meter Flow Rate, Q=Q x T x (1. - B )/860 = ^37 DCFM
m eye m wo -
Orifice No. (1, 2, 3) = _2 _ , J = 0.78, D = 0.281 , J x D2 = 0.062
o - o -
Orifice Press Diff . , H = 1.108 x (Q /J D2)2/! = A&*jf in. HJ3 us, rJ
Estimated Particulate Collection
Mn = C x Vm x 530/(Tm x 35.3) = — grams
Data sheet 6o02-17
-------
KVB
SASS SAMPLING CONDITIONS
Test Site Location / 3 _ 7~^ 7~ Xf-
Sample Port Location ^T/fc/< £ X ) T~
~"
Stack Conditions: Stack Velocity ft/min T 60 = V = 2-Z.fl ft/sec
5 •
0,O%5 stack Temp. ^33 °F + 460 = T =
T'
\
stack Moisture; B
wo
Particulate Loading (Method 5) , C = — grams/DSm
Probe Nozzle Size for 4.0 ACFM (wet) through cyclones at 400 °F:
, 7
-------
KVB, INC. TRACE SPECIES AND ORGANICS SAMPLING DATA
Project:
Date:
Location
Unit:
<— " r /I Personnel: /u|, UAf, ipf fY
3 - /0 - 7 ?
/9
Barometric Press :
Probe Nozzle Diameter (inches); 0.~?£()
Test: / r1 - I *>^S5 Absolute Static Press, in Stack (in. **) :
Fuel: -^r£> Oil- Pitot Tube Coefficient: 6. 2 3
ro
01
o
TIME
Real
IffS
/Iff
/P/>"
&?£
/?/$"
f*>?0
/35>^
/ i^o
Mo
I$X)
1S40
IbZO
*
Elapsed
&
$o
60
Jo
/2,0
190
Iy
Pitot
AP
(in H20)
0,11
f
V
o.iS/e./i
D.I I
fiT*r
Orifice
AP
(in H20)
*.1l
,
i
pRDoe ^
Cum.
Meter
Volume
(ft3)
W./07
%f>2 ,@OQ
<3ijq,000
01 If. 000
Mi. ooo
CHA'Ji
0^.066
I&.OCO
2M. Ooo
2*16.000
%V. oco
Hlo,$oo
wnoo
t*H.U**G
Pump
Suction
(in. Hg)
r-9
(,.1
&.$
1-0
^&&
l-o
7-0
7.r
7.7
?,o
^^
y.^-
MAOOM
3o. / "7
(
- A a / <
<
Dn)
PS)
CP)
TEMPERATURE (°F)
Stack
&J
&f
$M
J>a
bes
-c%?s
MWHt
&K>
So£>
Sff-Ultf
^ (
c
TO Ttu(jj
T/^w«
^w,o
fif Alt f
,
PSS/SUT
XAD-2
61
(,i
(,*
bi
A AJ —
42
6 a.
^Y
s^f
£>3
W
lo
V*Lf IV
Impinger
Out
W
%b
yj,
$0
'/3-
100
>tt)Sfr c
Meter
In/Out
Cl
Ifl
'W
l&
It?
l&
Ift
151
in
W
157
ue
III
IXf
n*
171
w
/yf
m
its
'%
m
m
To
°2
Cone.
» dry
SHtH-r
KVB 6O02-12
-------
KVB, INC. TRACE SPECIES AND ORGANics SAMPLING DATA
C/i
Project: £~PA t/iflsf 2ZT 5/^5 Personnel:
Date: r*>-/7J77
Location:
Units
(<. PfO''tSS#
M. tffl£(£T~y
/9
Barometric Press
^4
^so
i80
JK>
J«t>
n y*J
Pitot
AP
(in H20)
A/0
Orifice
AP
(in H20)
«^-3_
*
Cum.
Meter
Volume
(ft3)
S»tt?3^
$<•%. ooo
<°V.ooo
7o1. 000
779.000
WL.IOI
mm
1 21, QOO
°].*
%0
^
I/. 7
/M
/3.o
/v.o
iS.o
/*!&
3?^
^8
Vo^
Y&4
y^
t/0c|
H'o
Vo1/
Vo?
Vo^
XAD-2
<5/
6V
t>l
m
^
(>t,
^
6s
^V
6.2
6i
i«y
Impinger
Out
£7
77
*0
77
76
~~)u
~*) £-/
%7
97
^3
77
Oven
*-/0/
V«>o
'/^J-
t-foj-
^0?-
3
t(0f
Vc>V
Meter
In/Out
f7
//1
/Pi
/3£>
O»
'?/
^
/^
/3S-
^^
/?
-------
KVB, INC. TRACE SPECIES AND ORGANICS SAMPLING DATA
IS5
cn
Project:
Date:
Location:
Unit:
//y i°//*<^ JZT -•'' - Personnel: />/"-'/'•-/>
J-^V - 77
*y£X •••-<•'
/?
Barometric Press
Probe Nozzle Diameter (inches) : . 7?T
Test: 1. 0 MO* I7~3 X/TT Al
Fuel: & £ #/t- P.
TIME
Real
i'*0
1100
1(30
12-00
1230
IJ00
1302.
1132-
1102-
It32-
1502.
/^-2
Elapsed
#
30
60
10
120
/50
150
/go
2fO
2VO
2.7-0
?oo
Traverse
Point
Depth
1?"^
1 1
ii
n
n
n
/5"j^,
"
"
//
»
//
Pitot
AP
(in H20)
./ff
,/£>
/ $
/ 0
.Iff
.Iff
.10
./ff
.10
.Iff
.re
.10
asolute Static Press, in Stack (in. -t
u
Ltot Tube Coefficient: - %3
Orifice
AP
(in H20)
2.1
2-1
2-1
2-1
7 <9
2 *?
&MV6
2-1
2-f
2-1
2-1
3-1
2-1
Cum.
Meter
Volume
(ft3)
J*/.*XZ
272,500
3^2.200
tj/2 ,00o
ft '6, of"
552,150
ff2*&
£3^0°
(l).ieo
76?, 30°
4K,too
t^.500
7
f.r
1.2
u.r
12 J
ffS/C*
12,?
ts.i
IM
15.0
/t.0
tf,6
TEMPERATURE (°F)
Stack
*f3
f?3
rr?
K2.
r1
Meter
In/Out
112-
13 i
Ml
W
It?
IfO
Hi if
15-0
133
M
It/
W
;«1
nf
l*£
m
irj
i?i
13?
>3f
IZ1
122.
)10
tff
°2
Cone.
* dry
KVB 60O2-12
-------
Project: £.Pft
Date: ^
KVB, INC, TRACE SPECIE' X.ND ORGANICS SAMPLING DATA
VnT Personnel: (J,.. ~i (,'_— \l Barometric Press: A\T. y J
Location:
Unit:
Test: /^
Fuel: ^*r Ca
Probe Nozzle Diameter (inches) : , H ^i
Absolute Static Press, in Stack (in. *f»): -^
Pitot Tube Coefficient:
_(Dn)
JPs)
(Cp)
TIME
Real
Elapsed
Traverse
Point
Depth
Pitot
AP
(in H20)
Orifice
AP
(in H20)
Cum.
Meter
Volume
(ft3)
Pump
Suction
(in. Hg)
TEMPERATURE ("F)
Stack
Probe
XAD-2
Impinger
Out
Oven
Meter
In/Out
Cone.
% dry
.10
67
/OO
ro
en
CO
6?
it
69
39 7
U3
:f?>3
75-
m
12,00.
n
ol
5,27
l£
bi
51
U3
1332
3^0.
M.
$00
tiL
1
KVB 6002-12
T" - /T v '?
-------
Test Mo./f-/
Unit NO.
PARTICULATE EMISSION CALCULATIONS
Date >'/£-?7 Location _ /f
Fuel ^
Engr. HB
Sampling Train and Method SAS_S Tf6_(A
Pitot Factor, Fs
33
Tot. Liquid Collected, V
Barometric Pressure,
fl)
- / "7
Hg
ml Total Particulate,
gm
Velocity Head, AP 0. / / iwg Stack Temp. , Ts ?7/ °R Stack Area, As
ft
Sample Volume, Vm
ft
Stack Press.,
iwg Excess 02> XO2% ^ ' 7 %
Orifice Press. Dif f. , H_
Sample Time, 6_
_iwg Stack Gas Sp. Gravity, Gs
n.d.
Nozzle Dia., Dn
in. Meter Temp., T
•1. Sample Gas Volume Vm . = 0.0334 Vm(P. + H/13.6)
std bar
2. Water Vapor
Vw
std
0.0474 V
Ic
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
std
4. Concentration a. C = 0.0154 Mn/Vm
b. C = 2.205 x 10'
c. C = Eq. 4b x 16.018 x 10
std
3
5. Abs. Stack Press. Ps
^
bar
x 13.6 + Psg
00
6. Stack Gas Speed Vs = 174 Fs /APTs Vr^- x ^
7. Stack Gas Flow a. gsw = Eq. 6 x As x —— x -rrr-
Rate 6 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. XO factor
10. Emission
11. % Isokinetic
X02f = 2090/C20.9 - X02%)
a. E - Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vm + VW )
! = §£ ^td_
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm .. by 530/T (°R) if meter not temp, compensated.
m j
SCF
5?.^ SCF
'•£7C, K.D.
grains/DSCF
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr •
IfL.I N.D.
_ Ib/MMBtu
ng/joule
Data Sheet 6002-4
254
-------
Test No. /f-3l
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date ?'/7'77 Location /2
Fuel * Of '
Engr.
Pitot Factor, Fs
^ Sampling Train and Method
Barometric Pressure, P^ A*^, '
bar
Tra.i f\
ml Total Particulate, M
in. Hg
m gro
Tot. Liquid Collected, V
Velocity Head, AP_&V0___iwg Stack Temp., Ts_T72__°R Stack Area, As V. ?O ft2
Sample Volume, Vm 67%^ ft Stack Press., Psg "0.3O iwg Excess O , XO.,%
Orii
Samj
*i.
2.
3.
4.
5.
6.
7.
8.
9.
10.
Eice Press . Dif f . ,
lie Time, 9 JOO
Sample Gas Volume
Water Vapor
Moisture Content
Concentration a,
b.
c.
Abs. Stack Press.
Stack Gas Speed
Stack Gas Flow a.
Rate @ 70°F
b.
Material Flow
XO factor
Emission a.
b.
H A. 10 iwg Stack Gas Sp. Gravity,
2 2
Gs / n.d.
min Nozzle Dia., Dn O'~J5 in. Meter Temp., T °R
Vm . = 0.0334 Vmte + H/13.6)
std bar
Vw . = 0.0474 V.
std Ic
Bwo = Eq. 2/
-------
Test No. ^1~
Unit No.
Pitot Factor
Tot. Liquid
2 $^J.S Date
Fuel
, FS £-83
Collected, V
PARTICIPATE EMISSION CALCULATIONS
S-2/-77 Location /f
^ Q'i, Sampling Train and Method *
Barometric Pressure, P^^ 3 0 , '
>/*S.S Tro.|V\
in. Hg
/p. / m gm
Velocity Head, AP 6. /O iwg Stack Temp. , Ts
A^/fe °R Stack Area, As V-70 ft
Sample Volume, Vm 7<&V ft3 Stack Press., Psg
Orifice Press. Dif f. . H +.•
'2- iwg Excess 02, X02*
iwg Stack Gas Sp. Gravity, Gs ) _ n.d.
Sample Time, 6 !>00 min Nozzle Dia., Dn 0- ~>f in. Meter Temp., Tm
*1. Sample Gas Volume Vmgtd = 0.0334 Vm(Pbar + H/13.6)
2. Water Vapor Vwstd = °-0474 vic
3. Moisture Content Bwo = Eq. 2/(Eg. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
b. C = 2.205 x 10~6 Mn/Vm
sta
c. C = Eq. 4b x 16.018 x 103
5. Abs. Stack Press. Ps = P,_ x 13.6 + Psg
oar
6. Stack Gas Speed Vs = 174 Fs /APTs -
1.00
Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x - x
Rate @ 70°F TS 4°
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow
9. XO factor
10. Emission
11. * Isokinetic
Ms = Eq. 7b x Eq. 4b x 60 '
XO f = 2090/(20.9 - XO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
I =
14077 x Ts(Vm ^ + Vw
stu
6 x Vs x Ps x Dn2
Fe SC Feet/104 Btu
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vmet<3 by 530/TB(CR) if meter not temp, compensated.
&• i"-
SCF
SCF
0-08V .N.D.
grains/DSCF
"
0.
y/o
3 3 grams/DSCM
V in. w abs.
ft/min
_ WSCF/min
_ DSCF/min
_ Ib/hr
_N.D.
Ib/MMBtu
ng/joule
Data Sheet 6002-4
2 56
-------
Engr.
PARTICULATE EMISSION CALCULATIONS
Test No. /9-45^$S Date 3-2?"77 Location / 9
Unit No. Fuel * 6 0< ' Sampling Train and Method 5X35S 'Trctm
Pitot Factor, Fs 0'• o_3 Barometric Pressure, P 2?, 0 3
in. Hg
Tot. Liquid Collected, V /2-9T ml Total Particulate, M 3?V4. C. m
gm
Velocity Head, &P 0,0*9 iwg Stack Temp., Ts 9 9 ^ °R stack Area, As V, 9 ft2
Sample Volume, Vm701.Mfe ft Stack Press., Psg""0-Z7 jwg Excess O , XO % AS" %
Orifice Press. Dif f . , H 2* £7 iwg Stack Gas Sp. Gravity, Gs / _ n.d.
Sample Time, 6 3o O win Kozzle Dia., Dn 0>"l*> in . Meter Temp., T SS'V »R
Vw . = 0.0474 V,
std Ic
*1. Sample Gas Volume Vm^^ = 0.0334 Vm(PK=^. + H/13.6)
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
std
b. C = 2.205 x 10~6 Mn/Vm ..,
std
c. C = Eq. 4b x 16.018 X 103
5. Abs. Stack Press. Ps = p x 13.6 + Psg
oar
L.OO
6. Stack Gas Speed Vs = 1"?4 Fs /APTs j- x
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x ^— x -j^
Rate @ 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. X02 factor
10. Emission
11. % Isokinetic
XO f = 2090/(20.9 - X02%)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq'. 4c X Fm x Eq. 9 X 1000
14077 x Ts (Vm , + Vw ,)
I = j2
0 x Vs x Ps x Dn
Fe SC Feet/104 Btu
4
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
*Multiply Vm by 530/T (CR) if meter not temp, compensated.
?gr. f SCF
&/•*{ SCF
N.D.
Q, 0839 grains/DSCF
"r li,/DSCF
£' /92V grams/DSCM
£ in. w abs.
ft/min
L WSCF/min
DSCF/min
?,J(a Ib/hr.
(Of,-) • N.D.
g, //5 lb/MMBtu
Si'?- fr ng/joule
Data Sheet 6002-4
257
-------
KVB
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Test No.
Date
Location
Sample Port Position Hi t>~ Po,*jrr
r /
Container
Number
Sample Description
Container
Type
Net
wt/vol .
Comment
/OO£>
675"
PA
y* o
3"
0. 00 3 7
c,1-
Ll-,.0
O.3I9O
Sot-tbS
50- so
GL
GL
3>
r
IP/)
5'W
MAL.
C,L
MO. 6 on-
Data t« 6002-15
5~oo»««.i p/
258
-------
-TS.ST t°i F"U£l_£> TABLE
POLLUTANT
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
ftenganese
Mercury
Nickel
Selenium
Telluriim
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
SAMPLE NUMBER
-f
W-t LF
<.-Z.-=>
-T2_-
-sS
.^
< 10
-------
KEELER BOILER
TEST 19-1 TABLE STACK - #6 OIL BASELINE
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Bariuir.
Beryl liun
Cadmiiim
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
/anadiura
Zinc
Chloride
;luoride
Nitrates
Sulfates
s?r
<7.1
<)
.•=,
M*
0-0$
<0.-L.
o. o3
O.7.?
o. C^^
o.o^**
^o.oos
.ODS
o.fZ.
0.05
^TO.Z.
^0.02.
O.I'Z.
l/
' " ~
^^ O • 1
o.ot
Z.o
1
ps/c
260
-------
KVB
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Test No.
Date
~ 77
Location
Sample Port Position H '5 -
/V
Container
Number
Sample Description
Container
^Pe
Net
wt/vol
Comment
/ /V^j 5
-------
KEELER BOILER
TEST 19-2
TABLE STACK - #6 OIL BASELINE
POLLUTANT
SAMPLE NUMBER
y..
Antinbny
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
ISulfates
566*
o.S
12.0
5^/00
716
33
3/o
So
TZ-oo
ns
tfoo
L/OD
2.05
113
<:i2.oo
/ODOD
tjOD
720
too
52JOOD
•2.10
.10
538
7-OO
-SID
MSoo
fOOD
300-30
-------
KEELER BOILER
TEST 19-2 TABLE STACK - #6 OIL BASELINE
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
lin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sul fates
533
liiplir.at
•C2.S
-^1
Go
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: tii NOHTH LA 1ALLE STREET. CHICAOO, ILLINOIS BOtOI • AREA CODE »I3 729-14I4
INSTRUMENTAL ANAITSIS DIVISION. I*US WEST AilH AVENUE. GOLDEN. COIO8ADO B040I, PHONE: 303-57M5JI
To; Mr. John C. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P O. No.: 27810
Sample No.: Test 19-2 D 566, 716, 720, 538 5/18/77
CONCENTRATION IN PPM WEIGHT
Date: July 1, 1977
Analyst: S. Sweeney
IAD No.= 97-A345-134-21
ELEMENT
Uranium
Thorium
Bismuth
Lead
Thallium
Mercury
Gold
Platinum
Iridium
Osmi urn
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
CONC.
<0.7
1
0.3
380
NR
0.8
0.5
0.1
0.7
0.1
0.5
0.7
1
ELEMENT
Terbium
Gadolinium
Europium
Samari urn
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.3
1
0.3
2
19
11
22
190
MC
0.1
0.4
0.3
26
3
STD
0.6
7
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
MC
0.4
5
1
110
1
0.7
10
18
0.8
12
MC
280
MC
MC
MC
140
96
ELEMENT
Vanadium
titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
.Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
MC
330
0.2
MC
MC
32
MC
MC
MC
MC
MC
MC
=59
NR
NR
NR
18
0.4
' 4
NR
NR - Not Reported
All elements not reported <0.1 ppm
Approved:
264
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
BENERAL OFFICES: 9IB NORTH LA SALLE STREET, CHICABO, ILLINOIS «OOOI • AREA CODE «I2 ?9«->4»4
INSTKUMENIAL ANALYSIS DIVISION, 14335 WEST 4JTH AVENUE. GOLDEN, COLORADO »M>I. PHONE: XD-27>-9531
To: Mr. John C. Michalovic ^^|Pa^
Gal span Corporation JSism*\e&*.
Post Office Box 235 "~
Buffalo, NY 14221
p. 0. No.: 27810
Sample No.: Test 19-2 E 533 5/18/77
D«te: Ju1y lf 1977
Analyst: s. Sweeney
IAD No.: 97-A345-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead <2
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium <0.6
Lanthanum
Barium 1
Cesium
Iodine 0.5
Tellurium
Antimony 1
Tin
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
eCNCHAl OFFICE*: 3I( NORTH IA BAU.E ITKEET, CHICABO, ILLINOIS IOBOI • A*EA CODE «13 79«-l4>4
INSTUJMfNTAl AMALTSI5 DIVISION. I4J35 WEST JJTH AVfNUt, GOLDfN. COLO«ADO BO40I. PHONE: 303-27MS2I
To: Mr. John G. Michalovic ,^|Pm.
Calspa.i Corporation Jasntez*.
Post Office Box 235
Buffalo, NY 14221
P.O. No.: 27810
Sample No.: Test lg_2 f Composites B & C 5/18/77
Date: July 5, 1977
Analyst: s. Sweeney
IAD No.:
97-A345-134-21
CONCENTRATION IN pg/ml
ELEMENT CONC.
Uranium <0.005
Thorium - <0.006
Bismuth
Lead 0.009
Thai 1 i urn
Mercury NR
Gold <0.001
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
NR - Not Reported
All elemenls not reported
Sample was thermally
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymi urn
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
<0.001 vg/ml
ashed & 3500 C
CONC. ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
<0.001 Strontium
0.001 Rubidium
0.002 Bromine
0-02 Selenium
0.002 Arsenic
0.005 Germanium
Gallium
Zinc
0-002 copper
STD Nickel
0-03 cobalt
MC Iron
Manganese
Chromium
Approved; -"""/^
for one hour in a/fabt
CONC.
0.2
0.004
0.003
O.001
0.04
0.003
0.005
<0.001
0.08
0.06
0.8
0.04
5
0.2
4
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
Wta*ffurnace in^TVt
CONC.
0.03
0.006
fO.OOl
I8
3
0.1
MC
0.9
1
0.05
0.08
>1
=0.04
NR
NR
NR
0.001
<0.001
NR
^
fartz crucible
266
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
OENERAL OFFICES: 99» NORTH LA IALLE 1TUEET, CHICAGO, ILLINOIS *0(DI • AREA CODE 113 79S-I4B4
INSTRUMENTAL ANALYSIS DIVISION. 14335 WEST 44TH AVENUE, GOLDEN. COLORADO (0401. PHONE: 903270*531
To: Mr. John C. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
Daie; July 14, 1977
Analyst: S. Sweeney
P.O. No.: 27810
Sample No.: Test 19-2 G LF #6 Fuel Oil 5-18-77
CONCENTRATION IN PPM WEIGHT
IAD No.: 97-A345-134-21
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead 0.8
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmi urn
Rheni urn
Tungsten
Tantalum
Hafnium
Lute ti urn
Ytterbi urn
Thul i urn
Erbium
Hoi mi urn
Dysprosium
NR - Not Reported
All elements not reported
Samole was thermall
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium 8
Cesium
Iodine
Tellurium
Antimony
Tin ±0.4
Indium STD
Cadmi urn
Si 1 ver
Palladium
Rhodi urn
<0.1 ppm weight
v ashed @ 350°C for one
ELEMENT CONC.
Ruthenium
Molybdenum 6
Niobium
Zirconium 0.9
Yttrium
Strontium 1
Rubidium
Brotni ne
Selenium <0.5
Arsenic 0.4
Germanium
Gal 1 i urn
Zinc 3
Copper 2
Nickel 56
Cobal t 3
Iron 63
Manganese °-3
Chromium 0.4
Approved: .sjy/j?
hour in a XaKsr&6
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENE«AL OFFICES: 3J« MOUTH LA SALLE STREET. CMICA8O. ILLIMOI* «O«OI • A»EA CODE >I3 7K-B4I4
Reply to I«T«U««NIAI ANALTSIS DIVISION. uus WEST «TH Avewt. GOIDSN, COLOSADO KMOI. PHONE,
To: Mr. John C. Hichalovic
Gal span Corporation
Post Office Box 235
Buffalo, NY 14221
P. O. No.: 27810
Sample No.: Test 19-2 G IP #6 Fuel Oil Duplicate
5-18-77
Date: July 14, 1977
Analyst: 5. Sweeney
IAD No.: 97-A345-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium
Thori urn
Bi smuth
Lead
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: Sit NORTH LA SALLE STREET. CHICAGO, ILLINOIS 80801 • AREA CODE III 79«-M>4
INS1CUMENIAL ANMrSIS DIVISION. IU3S WES1 A11H AVENUE. GOLDEN. COLORADO KUOI, PHONE: 303-27B-952I
To- Mr. John C. Michalovic
Calspan Corporation
P. 0. Box 235
Buffalo, NY 14221
p. O. NO.:
Sample No.: Test 19-1 H
Date: July 1, 1977
S. Sweeney
IAD No.: 97-A345-1 34-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Urani urn
Thorium
Bismuth
Lead a
furnace in a quartz crucible
269
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: »J« NORTH LA IALIE STREET. CHICAGO. ILLINOH 60601 • ARE,* CODE *1> 79I-C4I4
INSTlUMtNlAl ANALYSIS DIVISION. 1433J W£SI 44TH AVENUE. GOLDEN. COLORADO SO401, fHONf: »]-37»-9531
To: Mr. John G. Michalovic j^ll^-
Calspan Corporation ^falwak.
Post Office Box 235 "~
Buffalo, NY 14221
P. 0. No.: 27810
Sample No.-. Test 19-1 1 685 5/18/77
ELEMENT CONC.
Uranium 0.01
Thorium _<0.01
Bi smuth
Lead 0.02
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten 0.02
Tantalum
Hafnium
Lute ti urn
Ytterbium
Thulium
Erbium
Hoi mi urn
CONCENTRATION
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum 0.01
Barium 0.03
Cesium 0.007
Iodine 0.003
Tellurium
Antimony <0.003
Tin 0.05
Indium STD
Cadmium 0.002
Silver MC
Palladium
Rhodium
Dysprosium
*Heterogeneous
NR - Not Reported
All elements not reported <9.Q01 pg/ml
Sample was thermally ashed (? 350° C for one
IN pg/ml
ELEMENT
Ruthenium
Molybdenum
Ni obi urn
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobal t
Iron
Manganese
Chromium
Date: July 5, 1977
Analyst: S. Sweeney
IAD No.: 97-A345- 134-21
CONC.
0.1
*0.08
0.01
<0.001
0.009
<0.02
0.01
<0.001
1
0.04
0.7
0.09
0.2
0.004
2
Approved:/^ // /•/
hour in a/latbratory'
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium.
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
/^^y-i
furnace in a
CONC.
0.004
0.4
<0.001
6
5
0.2
MC
4
1
0.1
0.4
>3
=6
NR
NR
NR
0.009
0.02
NR
^
quartz crucible
270
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: SJ« NORTH LA lALLt STREET, CHICAGO. ILLINOIS «OBOI - AREA CODE 115 ?9e-*«»4
IKSlHUWENIAl ANAWSIS DIVISION. H331 WESI
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
BEHERAl OFTICEi: tit NOHH L» 1ALLE »THEET. CHICAGO, ILLINOIS »O«01 • ACE* CODE *M T3«-««»<
INS1SUMEN1AL ANAmiS DIVISION. 14335 W£SI *ITH AVtNUt. GOLDEN. COIO«ADO M40I. fHOHl: J03-J7M531
To: Mr. John G. Michalovic ^j|5k.
Calspan Corporation -^2L"j!^^'
Post Office Box 235
Buffalo, NY 14221
P. O. No.: 27810
Sample No.: Test 19-1 K 684 5/18/77
Date: July 1, 1977
Analyst: s. Sweeney
IAD No.: 97-A345-134-21
CONCENTRATION IN pg/ml
ELEMENT CONC.
Uranium
Thorium
Bi smuth
Lead <0.04
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
NR - Not Reported
All elements not reported
Samnlp was thermally
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samari urn
Neodymi urn
Praseodymium
Cerium <0.01
Lanthanum
Barium 0.2
Cesium <0.003
Iodine 0.008
Tellurium
Antimony
Tin
Indium STD
Cadmium
Silver <0.02
Palladium
Rhodium
<0.01 pg/ml -
ashed P 350° C for one
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobal t
Iron
Manganese
Chromium
.^
Approved: •SJy.
£r Jy
hour in a ^/ ' ( s
77 r
y/ S jt
/ • / /'
fra&ry f
ELEMENT
Vanadium
Titanium
Scandi urn
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
/^
&g-^-^f—
« ^>
'urnace in a (
CONC.
0.002
D:08-
<0.002
2
0.5
1
6
2
0.6
0.04
0.9
3
=3
NR
NR
NR
0.008
<0.001
NR
s7
-^4
auartz crucibl
272
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
OENEBAU OFFICE*: 9» NORTH LA »ALLt BTDEET. CMICA8O, ILLINOIS B0>01 • A*E.A CODE »tj 7J«.B4»4
INSTtUMEHTAl ANALYSIS DIVISION. 14335 WEST 44TH AVENUE. COIDEN. COLORADO KUOI. PHONE; 303 J7« 9D1
T°: Mr. John 6. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P. O. No.: 27810
Sample No.-. Test 19-1 L 675 5/18/77
CONCENTRATION IN
Date: July 1, 1977
Analyst: S. Sweeney
IAD No.: 97-A345-134-21
ELEMENT CONC.
Urani urn
Thorium
Bi smuth
Lead <0.2
Thai 1 i urn
Mercury NR
Gold
Platinum
Iridium
• Osmi urn
Rheni urn
Tungsten
Tantal urn
Hafnium
Lutetium
Ytterbi urn
Thul i urn
Erbium
Hoi mi urn
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Bari urn <0 . 1
Cesium <0.02
Iodine
Tellurium
Antimony
Tin .
Indium STD
Cadmi um
Silver
Palladium
Rhodi um
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttri um
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gal 1 i um
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
0.4
<0.1
0.02
0.01
0.09
<0.06
<0.02
<0.03
0.1
0.05
0.07
0.2
0.006
0.04
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
<0.01
0.2
<0.007
0.9
1
2
3
0.6
1
0.2
0.4
0.8
=1
NR
NR
NR
0.03
0.003
NR
NR - Not Reported
All elements not reported <0.04
*Heterogeneous
Approved:
273
-------
KVB Analysis Data
Test Sample Number POM's PCB's
19-1 LF * *
19-2 533 <0.1 ug/g <1 ug/g
533 (duplicate) < 0.1 ug/g < 1 ug/g
C <1 ug/1 < 1 ug/1
C (duplicate) < 1 ug/1 < 1 ug/1
LF *
*Sample extracts too concentrated to be able to determine an analytical value.
274
-------
•rest No.
KVB
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Date ^ -2 /"77 Location
/?
Sample Port Position /V! / £> - £"<£/ ^7~ 1 gTf C £ / — ' <" '"/ /J
Container
Number
Sample Description
Container
Type
Net
wt/vol
Comment
r i »»
(,?.&
zzr
LS9
CL
Z/0
723
H
H
6-L
724
/-
M.
n
&L.
/87
(S-L
n
928
ni
a
HiO
787
tt
1 1
6-L
11,0
723_
tt
6-
612.
n
627
/i
a/r
tl
tl
275
Data Sheet KVB 6002-15
-------
KEELER BOILER
TEST 19-3
TABLE STACK _
t6 0JL LOW NO COND.
POLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
Barium
Berylliun
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
.j
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
722
<. 1
SZOO
to.S
fe.00
zs>
C3o
m
723
3500
450
2.00
noo
•7000
Z.SO
(ffl.O
s'ooft
726
iOODO
-ro. 5
O.O5
<: t
0.5-7
0.30
/&..D
0.005
2-.0
<:o.oZ-
f.S
/8
2-S?
/o2.oo ;
633,628, 627,647
639,638, 653,659
634,640,
641,642,
643,644
665,624
673,635,
630
276
-------
KEELER BOILER
TEST 19-3
TABLE
STACK _ #6 OIL LOW
CONDi
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tel lurium
. Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
C*
>5
o.iz.
^0.010
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
CENEBAl OFFICES: lit NORTH LA IALLE STREET. CHICAOO. ILI.INOII «0«01 - A»EA CODE «13 T5« »4i<
IhlSltUMiNTAl ANALYSIS DIVISION. H335 WES! .UtH AV£NUt. GOIDEN. CO1ORADO (MOI. PHONE: 303.J7H.9SJ1
To: Mr. John C. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
f. O. NO.: 27810
Sample No.: Test 19.3 D 722, 723, 726, 539
CONCENTRATION IN PPM WEIGHT
Date: July 1, 1977
Analyst: s 5vleeney
IAD No.: 97-A345-134-21
ELEMENT CONC.
Uranium 2
Thorium <1
Bismuth
Lead 160
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten <0.7
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium 0.2
Holmium 0.4
Dysprosium 0.8
*(-Jo f*C i^/Minn ASM ir>
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.2
0.7
0.3
2
12
7
19
60
460
0.8
1
0.8
*20
5
STD
0.4
5
ELEMENT
Ruthenium
Molybdenum
Ni obi urn
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt ~
Iron
Manganese
Chromium
CONC.
970
0.7
7
2
42
0.8
2
3
7
0.6
11
570
70
MC
400
MC
44
33
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
MC
300
0.2
MC
MC
160
>800
MC
MC
>130
MC
>330
. =46
NR
NR
NR
1
0.1
2
NR
NR - Not Reported
All elements not reported
<0.t ppm weight
Approved:
278
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICE*: 99ft NORTH LA SALLE KTffECT, CMICAOO, ILLINOIS flOetH • AREA CODE 919 798-8484
Reply to INSTIUAWNIAI ANALYSIS DIVISION. i*J35 WEST aw AVENUE. GOLDEN, COLORADO KUOI. PHONE: M3-z7».»sji
Mr. John C. Michalovic
lo: Calspan Corporation
P. 0. Box 235
Buffalo, NY 14221 Dete: July 1, 1977
Analyst: s. Sweeney
p. O. No.. -
Sample No.: Test 19-3 E S / ' IAD No.: 97-A345-1 34-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium <1
Thorium <1
Bismuth
Lead 1
Thai 1 i urn
Mercury NR
Gold 1
Platinum
Indium
Osmi urn
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
ELEMENT CONC.
Terbi urn
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymi urn
Cerium 0.2
Lanthanum 0.4
Barium 0.4
Cesium O.I
Iodine 0.3
Tellurium
Antimony 17
Tin 0.4
Indium STD
Cadmium <0.3
Silver 0.7
Palladium
Rhodium
ELEMENT CONC.
Ruthenium
Molybdenum *18
Niobium
Zirconium 1
Yttrium
Strontium 0.1
Rubidium O.I
Bromine 1
Selenium O.4
Arsenic 1
Germanium
Gallium O.I
Zinc 3
Copper 4
Nickel 3
Cobalt O.I
Iron 10
Manganese 0.2
Chromium 5
ELEMENT
Vanadium
Ti tani urn
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryl 1 i um
Lithium
Hydrogen
j S
CONC.
0.6
2
0.1
25
20
21
21
n
45
3
16
47
^26
NR
NR
NR
4
<0.1
NR
NR - Not Reported
All elements not reported <0. 2ppm weight Approved:
*Heterogeneous Sample was thermally ashed P350° C
quartz crucible prior to analysis.
279
nalaBorffforyfurnace in a
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
CENEKAt. OFFICES 9J« NORTH LA »ALLE «TI»EET, CHICAGO, ILLINOli «0«OI • AREA CODE >19 >9*->4>4
INSTIUMtNIAL ANALYSIS DIVISION, 1«U5 WEST *4TH AVENUE, GOLDEN. COLORADO BO401, PHONS: 303.27M531
To: Mr. John C. Michalovic y^iRik.
Calspan Corporation •<~E,,JSalk
Post Office Box 235
Buffalo, NY 14221
p. O. No.: 27810
Sample No.: Test 19-3 F
Composite B & C 5/18/77
Date: July 5, 1977
Analyst: S. Sweeney
IAD No.:
97-A345-134-21
CONCENTRATION IN pg/ml
ELEMENT CONC.
Uranium 0.1
Thorium <0.06
Bismuth
Lead 0.05
Thai 1 i urn
Mercury NR
Gold £0.02
'Platinum
Iridium
Osmium
Rheni urn
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
NR - Not Reported
All elements nol reported <0
ELEMENT
Terbium
Gadolinium"
Europi urn
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
.006 yg/ml
CONC. ELEMENT
Ruthenium
Molybdenum
Ni obi urn
Zirconium
Yttri urn
Strontium
0.01 Rubidium
0.03 • Bromine
2 Selenium
0.03 Arsenic
0.02 Germanium
Gallium
0.1 Zinc
<0.03 Copper
STD Nickel
±0.01 Cobalt
MC iron
Manganese
Chromium
Approved: f /'
/ S
280
CONC.
0.3
£0.02
0.04
£0.008
1
0.003
0.3
0.4
0.02
£0.006
2
0.4
1
0.01
4
0.2
2
^
ts s
s
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Ni trogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
'/^^-Z
CONC.
0.02
2
£0.009
MC
MC
8
MC
MC
3
>7
MC
MC
=0.3
NR
NR
NR
0.002
0.001
0.04
NR
<
-------
Reply »o
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 93> NORTH LA BALLE STREET, CMICAOO. ILLINOIS BOSOI • A»EA CODE 113 73« «4S«
INSTKUMENlAl ANALYSIS DIVISION. 14335 WEST 441H AVENUE. GOLDEN, COLORADO SCUOI. PHONE: 303-27t-9I2l
To- Mr. John C. Michalovic V^iP
Calspan Corporation ^.JU
Post Office Box 235 — ~
Buffalo, NY 14221
p. o. No.: 27810
Sample No.: Test 1^9.3
G LF #6 Fuel Oil 5/18/77
k.
E&.
Date: July 14, 1977
Analyst: S. Sweeney
IAD No.:
97-A345- 134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium
^Thorium
Bismuth
Lead <1
Thai 1 i urn
Mercury NR
Gold
Platinum
Iridium
Osmi urn
Rhenium
Tungsten
Tantalum
Haf ni urn
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
NR - Not Reported
ELEMENT CONC.
Terbi urn
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium 6
Cesium
Iodine
Tellurium
Antimony
Tin
Indium STD
Cadmium
Silver 2
Palladium
Rhodium
ELEMENT CONC.
Ruthenium
Molybdenum 8
Niobium <0.4
Zirconium 0.6
Yttrium
Strontium 1
Rubidium <0.1
Bromine <0.5
Selenium 1
Arsenic 0.5
Germanium
Gal 1 i urn
Zinc 2
Copper 2
Nickel 26
Cobalt 2
Iron 13
Manganese 0.6
Chromium 3
. ^-//7/f (
All elements not reported <0.2ppm weight Approved^'X^/ s/
Sample was thermally ashed
-------
Reply to
COMMERCIAL TESTING & ENGINEERING CO.
BENEIIAL OFFICES: tit MOUTH LA »Al.LE »T»EET, CMICAOO. ILLINOIS »O«01 • A*EA CODE 1IJ 79I-I4M
IKSTtUWNIAl ANALYSIS DIVISION. l«Ui *«' *«H AVENUE, GOLDEN. COLOIADO iOJOI. PHONE: 30M7W33I
To: Mr. John C. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
Date: July 14, 1977
P. O. No.: 27810
Simple NO.: Test 19-3 G LF #6 Fuel Oil Duplicate
5"18"77 CONCENTRATION IN PPM WEIGHT
S. Sweeney
IAD No.: 97-A345- 134-21
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead <0.8
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbi urn
Thulium
Erbium
Hoi mi urn
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymi urn
Praseodymium
Cerium
Lanthanum
Barium 2
Cesium
Iodine
Tellurium
Antimony
Tin
Indium STD
Cadmium
Silver <0.2
Palladium
Rhodi urn
NR - Not Reported
All elements not reported <0.2 ppm weight
Sample was thermally ashed @ 350°C for one
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
Approved: ^fj
hour in a Vabo
CONC
10
<0.2
0.6
0.8
0.04
0.8
0.3
3
1
20
2
15
0.3
0.2
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
_ Chlorine .
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
/S
furnace in a q
CONC.
150
1
<0.1
38
16
0.9
MC
8
17
1
17
50
=2
NR
NR
NR
0.8
10.1
NR
uartT crucible
nrinr t.n analysis.
282
-------
KVB Analysis Data (Cont.)
Test Sample Number POM's PCB's
19-3 537 < 0.1 ug/g < l ug/g
537 (duplicate) < 0.1 ug/g < l ug/g
722 < 1 ug/g < l ug/g
B —1450 ug/1 < l ug/1
C . 2 ug/1 < 1 ug/1
LF * *
LF [duplicate) * •*
Sample extracts too concentrated to be able to determine an analytical value.
283
-------
KVB
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Test No.
Date 3-21- ^H Location
Sample Port Position
Container
Number
Sample Description
Container
Type
Net
wt/vol.
Comment
4 »
^/^
• 1
£L
tt
1!
t|
.tzL.
tt
nzL
.1*78
1 90
A£L
3^63
HiQ
4 re
n.
/So,
Ul
n
Jkt.
i r
^L
M
6.L
6-L
5C
6-C
M
/ *
284
Data Sheet KVB 6002-15
-------
KEELER BOILER
TEST 19"4
TABLE STACK - #6 OIL LOW NO COND.
POLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
.{
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
728
2.0
mo
us
13-
-------
KEELER BOILER
TEST 19-4 TABLE STACK - «6 OIL LOW NO COND.
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
C*
S
<:&.!
CO-DO'S
«O.D05
o.-J"?
l.-z~
-------
KVB Analysis Data (Cent.)
Test Sample Number POM1s
PCBVs
< 0.1 ug/g <]
*Sample extracts too concentrated to be able to determine an analytical value.
287
-------
POM QUANTIFICATION
Component
Anthracene
Phenanthrene
Methyl Anthracenes
Fluoranthene
Pyrene
Benzo (c) phenanthrene
Chrysene
Blank Blank-It
684 571
0.71ng 10.0 ng
—
1.9
0.21 1.0
—
—
Test 19-2
#533
367 ng
—
24.1
136
6.1
0.26
2.9
Test 19-3
#537
J57.8 ng
2.3
15.4
16.3
6.3
—
0.52
Benz(a)anthracene
Methyl Chrysenes
Benzo Fluoranthenes
Benz (a)pyrene
Benz(e)pyrene
Perylene
Indeno(1,2,3-cd)pyrene
Benzo(ghi)perylene
0.80
0.48
0.49
0.87
288
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Unit No.
Unit Description
Steam Output (Ib/hr x 10 )
Final Steam Temp. , °F
Burner Description
Test Fuel
Primary Air Temp, °F
Stack Temp, °F
yjr
54TU£AT'£0
I peAaepf GAS RWG
A/Arc/Afil- 645 i #£ 0/L
f3f0
130-J~J~0
Comments:
VA//T WAS
289
-------
Test No.
Unit No.
" Date
MOBILE LABORATORY DATA
Location
Capacity
Test No._
Engr.
Burner Type
1. Test No.
2. Date
3. Time
4. Load A* fhr
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) HOT ' /£<>l- D
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)&?/£//? fX/r)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (0F/°C) P#Y ' /Uj£7
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. STA^K o*.
23. WATft CffAirfVr (% toL,)
24. NO STAC ia
25. Co HOT lcot.pl STACK
26.
27.
28.
29.
30. .
3.00-25
J3
2-lf 2.1
2i5~ 2H
30o 2/$~6
2f.g
4. t
/o
133 2fS
-\25Z\-
2<96-2i
3X
2-1
271
270
1
2.°lt
A £3
^ff 7
217
2- It
1
236
tf.g
70 /S 7
2.1.7$-
67*
/&
y.tS\3*f
22\21\I6
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
290
Data Sheet 6002-2
-------
Test No.
Unit No.
Date
MOBILE LABORATORY DATA
/7V Location 3?
Test No._
Engr.
Fuel
Capacity Y5"
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) HOT \Coi-0
9. NOx (hot) read/3% 05 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO, (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%) 6*tl£& fXlT
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C) W( /U6T
19. Dew Point Temp. (°F/8C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. $TAC% &z_
23. WAT£/t CoftTS^T ffa Mb)
25. £& H°T -Gom! STAC-K.
26.
27.
28.
29.
30.
200-2-5
2,f
26o
260
0
2?X
2,t
285
2S5
0
2&
ft,*?
S^
SI
4,7
1^
220
777
26 122 I It
2of-}2.
ISS 1.55
232
232-
0
3.^5
23S
23*
0
227
15.0
hrfi
SI
>2f-fJ
f-7
ta,7
fft
"^"*
3-21
/ '*
\
.
202-1
2fS
2,6
2S1
w-l
6,2.
2*0
1
*.£?
30
—••«•. i '
202'ij
2.&
/?f
I&
O
23 o
2-7
2^0
2*0
O
2*6
W
-------
Test No._
Unit No.
Unit Type
Date
Fuel
MOBILE LABORATORY DATA
Location
Test No.
fingr.
Capacity
V$-
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) ttOf /G0L9
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%) &>H£R fX/T
14. Carbon Monoxide (ppm) uncor/cor
it
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C) WY/V£T
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.Jf4cK 4u
23. WATfA ero*>rfA>r fa\joi)
24. tfO (.STACK)
25.
26.
27.
28.
29.
30.
200-2 f
277
2-1
2&
6.F
22.7
211
201-13
3.5-0
t,t
232-
/f
ft
S2.
36.G&
s-.f
I1f
211
2.01- fi
Zlf
U
2*1
IS"
6.0$
(1?
23S
2*2 -f
2.S5
Z3S
22-0
f
23S
z&
2fZ
&7
5"
*y-f
H.i
,
*7
ft
3
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
Date f(2-7/76 Location
Test No._
Engr.
Fuel MO, £ Capacity
Unit Type C, £,
Burner Type
I. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) H&TI COI-D
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%) Sn/t-f # fXlT
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C) ^/CX/1*^7"
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
23 vS*rf& Cofttff/^r (% V0L )
24. uo (STACK)
25.
26.
27.
28
29
30.
200 17
2.J
175
172.
3
2.10
2.3
JS5
/82.
3
2.71
M.£
6 2-f
10.3
I3f
MT
2fl- IS"
I.SS
220
22^
0
270
/•£
224
22.4
0
2SJ
ir.e
£f
f7
je>,t£>
?. $5
10.7
2*1
7.1*
}03-27
3.3
/ss
)Sf
0
1?*
3.35-
173
175
0
/si
13.2-
75
SO
30-16
7-0
1,$
/i7
tri
• III
—
.•_•» —
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
293
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No.
test No -2 0 1 G " 1,2-f 3 Date & ~02- f£ Location
?$
Engr. W^ , T,P.
Unit No. Fuel <£/f 5 Capacity V^ K&/kr
Unit Type £.£• VE^T^^L- Burner Type P£Ap&0Y~r\lfl\3
1. Test No.
2. Date
3. Time
4. Load (k1*/Ar)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) 6010 ttM '£ '/#£ '/irfff HUE
9. NOx (hot) read/ 3% 03 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A tiros. Temp. (°F/°C) &M/VET
19. Dew Point Temp. (0F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. STACK, e,.
23. tf0 CsTAc-K)
24. Co ceumve/ftoT L/ve/srA<&
25. Co* a,u> we /HOT true, STAC*
26.
27.
28.
29.
30.
2#>6-t
H/4
It!
/62-
O
171
I'f
tel
10, 3~
srs
ss
3* '&1
6.2-
131
tas
/j^
1*5
7.9
2*16-1
fo.O
1.0
HI
(1?
O
It*
*'t
/£
-------
MOBILE LABORATORY DATA
Test KQ.20l6-1.5~, 6 Date 6-2 ~ 76 Location 5
Unit No.__ Fuel G>A 5 Capacity
Test No._
Engr.
Unit Type
C~,£-
Burner Type
1. Test No.
2. Date
3. Time
4. Load (k#/Ar)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)^P U*>£/tK>T */V£
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (eF/°C) P^/Ufff
19. Dew Point Temp. (°P/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. SrjcK Oa_
23. M* (srAtK)
24. co cam £.M£ /HOT tjv£
25. co CsrAt-Z)
26. £°3- £.OI~J> 1./HE H&T L(fi)£
27. C£>^ CsrAcXj
28.
29.
30.
ZoiG-y
H0-0
2.?
/«
156
0
166
2<l G-5~
11,2-
1.2*
152
131
t0.f
&Z5
l/i
2.00O
I3f
JL00&
/AS"
g
2olG-6
ID.?
I-HS
Ht
HS
O
M
IJ&
151
n.0
4.0
/a
2X0
M
ISO-
ISO
300
11.0
n.o
7,3
\
-
1
,
Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
295
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
Fuel
Unit Tvoc C.f-
MOBILE LABORATORY DATA
Location
Capacity
Burner Type
Test No._
Engr.
k
1. Test No.
2. Date
3. Time
4. Load \ K*^/nf'J
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen <%)*""' LW6/Hor LiME
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Baoharaoh> #OftfF&
18. Atitos. Temp. (°F/°C) P£f/U£T
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. 5fjCK 0y-
23. STACK NO
24. C0 COt-p Lj/*)£ /for L(#£
2s.srAc-K co
26.^i *«^ A/**/Wi/y*
2T.sr/f^K c0?_
28. /b/f/3" 0Pf/J
29.
30.
2006-3
3f,0
2,7
Ifl
151
0
\U
2.7
163
J0
o
S~3
f2-
30, 2 i
£.
24?
I/2
112-
0
I2S
2>fr
I2f
J2-6
I
fr.S
SJ*
30.2 H
7.0
1S
/?
122
/£
It
I2.£
/2-t
1.9
pwrs il+ts
201-2
3Z.0
2*£
lit
/(I
0
I3o
2.6
127
J2. 6
0
£7
?7
34.21
£,Z
#3
f
131
II
7
/++* b
f,f
ff»XB IH&
201-3
3X.3
2-1
I3£
IM
0
/f2
3,0?
Ifl
12.'
0
74
<1
30.21
7.0
l/g
£
/S2
1
i
12- *
12. £
1.?
icA
201-1
3f.$
3.0 2.U
136
131
3-
161 M
I2> £
o
7f\ft
3*. 2 3
(.If
116 \ 161
\7\1L
3
fcf&f.
£-
MTS^L^S.
• — • — •
_— —
*Correction to 3% 02 should not be performed if
the value is measured on a
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location f %
Fuel
Capacity V 5" k tf/j,
Test No._
Engr.
Onit Type
Burner Type
£ ) tf f-,
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) £~OiV t-/fJ£/ffoT l-ffl£
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. {°F/CC) PW/WfT
19. Dew Point Temp. (°F/°C)
20. Atroos. Pressure (in. Hg)
21. Relative Humidity (%)
i*'57~A£K A/0
24. gg tow utte/ifar ujj£
25 SfACK CO
26 CQ± £*l-P t-/fl&/#0r Ut>&
27 SfAC-K £&?~
28 POA.TS 0/*£/t
29.
30.
20 y-r
Z7S
&Z
/*?
I
131
2.7$
131
12, {
41
fz
$0,3-3
£75'
{0^
n
(10
{2.
/0
(Zj
n.{
to
** 6+7
20i-t
2-7
/a
/VZ
10
w
S2.
30.23
£,7^
lie
2£
PI
ZS'
10
71
fc*iz +13
• ... * •
2.006 - i
2-7
136
J36
0
171
2.r
174
10
£•7
I3X
6
j
/o
171
£
/&
7,6
pAseuse
,m ""
•
-
'•"
•"
*Correction to 3% 02 should not be performed if
the value is measured on a wet
Data Sheet 6002-2
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
Date £ ~ y ~ 7£ Location _ 2 0
Test No.
Engr.
Fuel
Capacity
V5"
Burner Type_
1. Test No.
2. Date
3. Time
4. Load **/nr
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) CoL* "^/ff&rrep WK
9. NOx (hot) read/ 3% 03 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
18. A trass. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. 5r4cj< 0*.
23. #0 (#OOF) / CO#&.
24. £o ce>"> ^*/ttor u#£
is. CO [#ooF LI#£)
26. C0y. C01* ""*/fH>T US*6
n.C°2. (froF (./#£)
28. Wtrex. c0MT£fiJT fa vo**)
29.
30.
2.0o~,500
2.7S
15%
m
X
/ft
2.53
jgl
t7Z
q
/ft
/e.f
/y
fS'
30.37
f.f
HI
3~
/si
£
3
/o.S"
/o.f
g.o
tt.Z
20/-G-!
fO, 060
?.1 M?
Ii2. 172-
itt m
0
176 /SO
/a.0
£6
5-7
30.37
7.2
137 //f
t f'
^
J0.0 /O.O
7-1
/S,&
2*i-7
j
2.7
no
/og
2-
J3i
2.7
13-1
13-6
3
02.
/o.Zf
75~
£6
30.37
f.1
^
135
g
i
0.3S
7.
10.33
f
It. I
2.0^-1
31, 5~«o
2.&
"1
W
3
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3.**
130
lif
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IO.06
7f
£0
30.37]
7,
J0t
z*.
— •• '
^ .4
01.
2-2
2.2-
19.00
/AM
Z/_!
JS^^
1
•
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
298
Data Sheet 6002-1
-------
Test Ho._
Unit No.
Date
HOBILE LABORATORY DATA
Location 3
Test No.
Engr.
Fuel
5
Capacity
Unit Type
T / C- A L
Burner Type
1. Test No.
2. Date
3. Time
4. Load i*VV7/V/
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) *"* A/A*/W i./*£
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% 03 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/eor
16. Sulfur Dioxide Cppra) uncor/cor
17. Smoke Spot (Baeha»agh$M#/7#^t
18. fttnos. Temp. (°F/eC)
19. Dew Point Tesnp. CeF/sC)
20. Atmos, Pressure (in. Hg)
21. Relative Humidity (%)
22. 5T4 CK 0*.
23. W4T££ Cfs/^TS^T (%&!*.}
24. ttO (%®t>f) /£0AR.
25 £0 £»l.j? t.t&£ /H0T t-/*/£
26 co #00 f we
27 C^j*. C&**& t~l#£ /tffff~ t~/At£
28 £0* *eef L///£
29.
30.
X>*-6-6
31 K
2.3
($"2
isrz
o
/?£>
2.3
17*
I7S
&
161
I0,£
/3X
41-0
30,00
&ts~
If' 1
W
6
/oS
171
/2
/*
t»,r
7-Z
201-1
3?K
2,25
HI
III
to.f
£1
f3
jp ti
a t jT
//
/Z2~
/61
/£>0
/A^j
p.s
7f
w-,0
31 K
2.$\
11
11
2.
r/f
2.6
110
ie>7
3
III
/^2.f
/
O
s*t
£3
£g
16. 1
Z?
39
*»
I0.3S
//&
12-
?
16, OO
7-r
**i-ii
31K
j2,y
///
///
o
/if
2.tS
121
W
O
137
/0.0
Y
0
7S
sz
21 >>f0
(.$"
}(,
/It
It
£
lo.o
3
139
/o
r- •-
10. 0
7.*
**Y-/*
3Z,fK
2.3S
11
13
1
llf
2,3?
101
Ifff
/
HI
/0.0
%
£>
fl
ts
21*10
6.£
li.
11
/
^
10,0
1
II?
6
\i».e
7-?
*Correction to 3% O, should not be performed if
the value is measured on a wet basis.
299
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
V "6 Location -^ u
Test No.
Fuel
Unit Type £,£ ' '
? / C 4 L
Engr. W, . V,
Capacity
Burner Type_
1. Test No.
2. Date
3. Time
4 . Load *Tfhr
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) 'GOLD Ufȣ / tfffT ting
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (PF™)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spet — (Daehngaeh) HOfi£f^
18. Atmos. Temp. (°F/8C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. 2T/ICK
23. Mr£~A corf TMT (f0 I/OLJ
24. #0 (RO°F} CORK,
25. CO Cffl-ff *-//(>£ /for t//J£
26. £& &OOF L/fi/B
n.COji. COLO LM£//f&T L/fl£
2&.£0i AooF t/Atf
29.
30.
201'tf
&K.
1.7
to?
fol
/
135-
(.7
Iff
117
I
f26
10.$"
7
0
?3
6 %
-2f-f
{.0
16.1
lo i
11
?'
I0-f
fr
fr*f
2-1
f
/6.5"
?
Zfi-fr1
31X.
1.2S
1/6
116
0
US'
/.fS
13-1
X2f
0
/3l
J/.0
7
0
?3
6*
21.1
f'7
17*3-
Hi
1/6
i
//.o
132
TIT
9
ll.o
f.3
2.01-1?
31 /£
y./
(OS"
(03
2.
&1
f./f
132.
/2-1
3
137
1-1
2.
0
7.?
/ i * **
/fit
6
13*
g
3
LI
1-\
7,1
20'H~ If
3fSoo
3.0
lot
1*6
0
Jlf
3,0
f*6
12.6
0
/*r
__
-
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
300
Data Sheet 6002-2
-------
Test NO._
Unit No.
MOBILE LABORATORY DATA
Date _£-?- 76 Location
Fuel 6> '* g" Capacity
Test No.
Engr.fr: V 2.•'-*.•,/- ^
Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load #//ir
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) &>U> UM6//fOT Iff)*
9. NOx (hot) read/ 3% 02 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppn»*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Cpot (Daehaifteh)^^^^
18. Atuos. Temp. (T/°C)
19. Dew Point Temp. (°F/°C)
20. Atinos. Pressure (in. Hg)
21. Relative Humidity (%)
22. srAck a^.% i
23. WAnR cp+iredT fa> voL~2__
24 A/0 [&.QOF) / Co&K.,,
25 co COLO UN£ tfeT Lttte
26 £D #e>0p LlfilB
27 £-0%. C-&L& t-ipe HOT *JA>£
28. <^^a- ^tf/1 M/V&
30.
2o?-l
*/0fff0a
2.3S
ffl
/Vf
3,
tfe>
2..5S
ITS'
/72
2.
/ts-
/0.7&
f
0
71
/^
30.02.
£.?5T
/4*2.
IH1
II
tu
11
/e>
lo.7f
1937
Z.3 j
Zof-l
¥0,006
2,2.
&7
tf&
/
2oS
2..3S
tfl
It*
/
W
/a.f
f
i
£,2.5-
I6>f
Itf
to
m
/e
10
10,4
toS
frfi
20S--3
*/0,000
**S
Uf
/**
0
toff
2-if
W
ni
0
111
/e.f
i
?3
££
30,0o
,£.3?
' i&3
/£0
I3~
m
12-
It
I9.S
/AS
*•*_!
^i • - "
2.05- -i
90,006
2
It.?
1*
16
HX
V
t
JO.f
JC.6
f.3
_... - -
2af-$~
fCjffoo
Z.SS
f*3-
1/9
6.2.
16
*
4>
16.5
1/7
f.3
*Correction to 3% O., should not be performed if
the value is measured on a wet basis.
30 1
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA Test No.
Test No. Date 6f&t 6/3 Location ** Engr. 1*
', MAZWoutt
Unit No. Fuel U> 4 5 Capacity
Unit Type Burner Type
1. Test No.
2. Date
3 . Time
4. Load \™/nr)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) £°i-D L/*J£/t/er LfNE
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spat (Bachnirneh) fi/Vtl6£%
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. srAcx 0* j?0
23. &4r£A ero*JT£*rr fa VOL)
24. A/0 (Aoof) / eofi£.
25. £e COLD L/Af£/#tr i^^e
1f>. C.0 Roof L/0£
27. £°2- cou> u#e/ffort,/te
28. C£>3. #0*£ tJj/£
29.
30.
205"" £
If 6 £00
l»7
/&f
Pi
0
IIS
1-7
117
II 7
0
in
lt>>7?
1
-2 7- 7V
Frff
j6.q
f
21.37
4.5
i s it
/ Q* ^J
/Y
f
/e>y
f
2-
faf
fo.f
Z.o
W# *•
SCA &7
f/1
200G-Z
10,000
2.3
If2
1*2.
^
170
23S
)7£
176
0
141
/e.S'
*£
63
21.17
£.15*
/6-i
[30
/?
l*(
/I
/*.
/9.f /AS
7.*
SA%W£
zaoG-1
16, 300
2.3f 2,1$
12-6 M
1*4 /16
0 0
/if /&
lo.f
61
61
Zf.ll
t.f
/£.3
HO m^
/? 20
l^Ts
7.t
Jtf6iSTe£
ftii.L epfii
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
302
Data Sheet 6002-2
-------
Test No.
Unit No,
Unit Type £ t
Date & /? ,
Fuel <£/f
e/ffor LfN£
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)* '
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°P/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. STACK 03, %
23 Mfra? coMret/r fa VOL.')
24. fiiO C/?OOP) / CO&t..
25 , £T^ &&&-P ^^^/ffOT Lffil£
26 £•& fooF {-/#£
27 C* &2, £0LD i-/^£/tfoT l-/fl£
28. ^"^3. &60f- £-/fll£
29.
30.
2M&-/0
3g.0
J**>
110
ft
q, 7
2W>
£
&00
1.7
l/X fov
2*€>G-ll
3f.5
1*35
126
Hf
/o.f
2»0t»
£
2,3.*?'?
2&o®>
fo>5
l//f /cw/
200G-/1
ft>.£
2>s:
tft
/Zl
/e.J-S'
Zl
6
2-3
/0.25
3*o<$-/3
Vo.7
l.tt
l?g
/tr
/0.7S'
256
&
mq
Zfo
lAjy
***6-M
fG.7
i.r i,t
UQ /fo
t6e> n*
O 0
20S fqz
/&* r ^7
ft £9 £3 £}
6.2-*
(6.7
157 /fZ
2* 2?
2-2
/0.7S /0.75
&• &
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA Test No.
Test No.
Unit No.
Unit Type £ £
Date ^/Y
Fuel £?// S
V£fi T ' }£ rf L-
Location ^ t> Engr. W- }JA2!M$W
Capacity 7-^ #"/#/•
Burner Type
1. Test No.
2. Date
3 . Time
4. Load fk#Ar)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)'*"* **** JHCfiTa *&
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.STAC-K ** %
23 . wrf* COM re*tr fa VOL.)
24. #0 (toe?) /co*R.
25. CO Ct>LQ Wt/tiffT UAT&
26. £0 £00? L/#£
27. CO^ COLO W6/HOTLII06
28. G°3- AW? Ufle
29.
30.
ZOOG-tf
to,?
23$
I7g
/*c>
0
2/2
z.iS-
2CJ
2*1
e
2o5
l£.f
f
71
tz
W.It
£.7?
16,3
165
11
20Z
2-6
U
/o.S
10, ZS
%0
200G-/6
10.*
2.1
(Si
&7
o
/1Z
2.1
176
/tz
0
W2
/0,&
i
*7
70
27
2.3*
102.
103-
f>
103
l*.5
2-
to
71
2W3
6-i
16.1
?e>
2tt
11
2e>o
3*00
lo.f
p.?
f.o
Zel-ft
3?,g
W*
1/2
112.
O
/ft>
3'5S
137
137
O
/W
1.7S
2-
*/
70
21,12
7.3*
15-3
M
/2-
wi
12.
10
1.75
t.7f
7.1
2*1-20
10.0
2.9
16
1*
O
)2t>
2.X
113
f!3
O
111
/0'2-f
^
13
70
21.1^
6.t
151 .
n
21
2
io*s
m
2±-
6
l«,tf
-Jj—
__ —
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
304
Data Sheet 6002-2
-------
Test No.
Unit No.
Date * /
Fuel O?.
f/o
45
Dnit Type <£ £ \/£$r'C4i.
MOBILE LABORATORY DATA
Location
Test No.
Capacity
Burner Type
1. Test No.
2. Date
3. Time
4. Load (K&/flr)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) C°L° «"f/#*r W£
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
1 ' - *
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Stroke Spot (Daeharaoh-)X#*ftfe/C
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. {°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. 5TA&K &z. % i
23. WAr£/Z cofire^r (% you)
24. NO (RQ6F)fCQ£& .
25. Co C6"* v** /wr w£
26 CO #O0F *•/#£
27 c<»z *** "^/Horwe
•&.Cf>3- #0QP t-/#£
29.
30.
2006-17
31,?
2-2.
tst
I5i
o
w
23
177
IT7
<£>
7^2
&'S~
2
I
72-
£1
30,07
&?
It.if
Ho
12-
/<<2
/O
10
io.r
K,
£.«£
rtf
10
i'7
/
f<7
t.e>
ZC06-I7&
3
te.2S
£
,...
6
{O.2.*
i ' •
laoG-trc
37. S-
2.2S
17*
171
M.S'
l&
10
ro.M
—
&JOG-17D
W?
2't
/S7
IfZ
IAS'
U>
i*>
io.it
*Correction to 3% O, should not be performed if
the value is measured on a wet basis.
305
Data Sheet 6002-2
-------
Test No.
Unit No.
Unit Type £ £
Date 0 ffU
Fuel (?n $
? tf/eT/cji~
MOBILE LABORATORY DATA
Location
Test No.
Engr. M/,
Capacity
Burner Type_
1. Test No.
2. Date
3 . Time
4. Load
31,6
31.0
31.*
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
2,93
9. NOx (hot) read/3% O? (ppm)
110
lie
71
10
11
12.
13_
ii
15
16_
17
18
19
20_
2!
22_
21
24,
25,
NO (hot) read/3% 02 (ppm)*
112.
71
NO? (hot) read/3% 02 (ppm)*
NO (cold) read/3% O2 (ppm)*
/57 in
lot
fj
n
71
Carbon Dioxide (%)
10.
Carbon Monoxide (ppm) uncor/cor
Hydrocarbon (ppm)
uncor/cor
Sulfur Dioxide (ppm) uncor/cor
Smoke Spot (Bacharach)
. Atmos. Temp. (°F/°C)
7X
12.
Dew Point Temp. (°F/°C)
£L
7/.S-
71
Atmos. Pressure (in. Hg)
30,00
Relative Humidity (%)
JTAcK
£.5"
s.
It
15.1
(too/*) Scot*..
11°
IX
z±
75
35-
1*L
6
21. co*.
<=***
It.ff
10,
10,0
7,6
f.OO
29.
30.
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
306
Data Sheet 6002-2
-------
Test No._
Unit No.
Onit Type
Date
MOBILE LABORATORY DATA
*//£> Location J g
Fuel
S
Test No.
Engr. W/, /
Capacity
Burner Type
1. Test No.
2. Date
3. Time
4. Load (k &/hlr)
5. Process Rate
6. Flue Diaro. or Size, ft
7. Probe Position
4?oiQ LJ1&£ /
8. Oxygen (%) *" " ^ /H*r t-INf
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
" *
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Cpot (Sagharaoh)//i-^j
24. A/Q (#&0f) /eoRR.,
25 C O cot-* Lt*^Su0T~ ±j#£
ze to &MF LW£
27 C"6/ftffT LJUZ
28 C01. tOOF l~lf£
29.
30.
39.0
2.6
76
71
10,0
1
1
10
71
21.81
£,f£~
fl
31
7f
11
fr 0
7-g J
mi "•
3-°1/S~2&
31,1
2.3f
If
17
10^0
i
#6
71
21. n
/JS
^/
Sic
1A
170
(0.0
g>0
,m I . li
W/S-27
31.0
2S2.
11
yr
10,0
1
*1
7^
21. ?f
t.Sf
37
"^!B»
j
16,0
t 9
^73"
2.0
.. •• •
2o't/r-2.g
31 f0
2,3
1Z
13,
O
#2.
2-1
ua
U0
f)
&0
lt>,e>
3
71'f~
^6%
21. ?/
f^S"
Mi
1o
*hz
ffC
H1
lit
VI
twj
f,0
.
***£-&
31.0
i-3
fe
ft
te.y.S'
71
£7
21.??
6.3?
il
J.*
^
w.j.i>
31
35
tf.0
- ~
*Correction to 3% O2 should not be performed if
the value is measured on a wet. basis.
307
Data Sheet 6002-2
-------
Test No._
Unit No.
x A yWJBILE LABORATORY DATA
Date & //f/ft Location J?
Fuel <5/4'5 Capacity
Test No.
Engr. W,
Dnit Type C ' £ VEP T/ C/4 L- Burner Type
\. Test No.
2. Date
3 . Time
4. Load C^# /hr)
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%) COLD /fffAffP
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke SpuU (DaUiaoiauh) #VM8£&
18. AtJios. Temp. (°F/eC)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. ST^C-K O-* %>
23. #0 fXoef) /co fa.
.f, -» sct-o z/A/ey
24. &-& /Her i.iti£
25. £& KM? L/AJE
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27. <^^ t»»f *-ltie
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_ — - —
Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
308
Data Sheet 6002-2
-------
Test No.
Unit No.
Unit Type C £
Date
Fuel
V£ff "
MOBILE LABORATORY DATA Test No
€/'•' /7<^ Location ? f Engr_ u£ rJA2m0
G * $ Capaci ty V 5" ,1 ' •#• / 'fo ^
/C A I— Burner Type
1. Test No.
2. Date
3. Time
4. Load (k &/hr)
5. Process Rate
6. Flue Diam. or Size, ft
1* Probe Position
8. Oxygen (%) Ce>t-° /HEATE&
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
- • — *
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
IT. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Pow Point- Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22. STACK &JL %
23. U//?7"/# COfJTEtfT &» fat-.)
24 W faeef) /eoHR
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28 C& K0aP Ufi>£
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the value is measured on a wet basis.
309
Data Sheet 6002-2
-------
KVB
CONTROL ROOM DATA
!•«.«=«: Niimhpr 2 0 2 1 3- O 2 Date ^//f/?
Unit Number Owner
Fuel Tp £ Location
Capacity (KK/hr) Y^"
Test
Engr.
NO.
**>
'f
3*
Furnace Type Burner Type
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5- STACK, e,.
6. Oxygen/Air Level WFM.fXiT jnrjoti
t.ltlf Oraai Pressure (psig)
8. Final Steam Press/Temp(psig/°F)
9. Fuel-Air Ratio Setting \OH. t-o/u>/t>£
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Sscondary (
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (fe/-hiH* GtyfauJ
16. Fuel Press/Temp (psig/"F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke «star SfoT
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23f*^ir Heater Inlet Temp. (°F)
24. Air Heater Outlet Temp. (°F) 1 1*6
25. Windbox Temperature (°F) 123
26. f 5 \»S.
27. Msren
28 • MO FUHjiAee fxir fa>u) rm
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-------
Test Number
Unit Number_
Fuel
KVB
CONTROL ROOM DATA
Date 5~f2lf76
Test No.
Engr. U/.M,
Owner
Location
Capacity (K*/hr)
Furnace Type £ £ VfAT I^^L Burner
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7,^DiUB Pressure (psig)
8. Final Steam Press/Temp(psig/°F)
9. Fuel-Air Ratio Setting /fft L0*f
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Pr imary /Secondary { )
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (Ib/hr)*
16. Fuel Press/Temp Spsig/eF)
17. Fuel Atomization Press (psig)
18. Pressure Furnaee/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet Temp. (°F)//iw
25. Windbox Temperature (°F) / / f
26.
27 MASTfA. Ca^rX.e>l~
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27S/212-
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-------
KVB
Test No
Engr.
CONTROL ROOM DATA
Test Number
Unit Number_
Fuel
'*.***.
Date
Owner
Location
Capacity (K#/hr)
Furnace Type C £ V£AT/c4i
Burner Type
ST*H>
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7 .''"' Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( )
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet Temp. (°F)
25. Windbox Temperature ("F) 1 / *f
26.
27. gc/l-££ tfAsrfK,
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4/76
60-33
3 1 2
-------
Test No.
Engr.
KVB
CONTROL ROOM DATA
Test Number 2-Q ^Zo^ 2.C>1 ^ 2o3 Date f/2-(/7{ f/2 7/7f
Unit Number_
Fuel
Owner
Location
Capacity (K#/hr)
Furnace Type C £ Vffl.riC.jL Burner Type PfAfOPY -
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. -oi- OBI Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting Jon. ioAO&t
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Pr imary /Secondary ( )
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/"F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (CF)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet Temp. ("F)
25. Windbox Temperature (°F) 1 / *f
26. I/ 2. /I
27 HAITI.*. CeA>TK0t~
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3 1 3
-------
KVB
Test No.
Engr. IV. X.
CONTROL ROOM DATA
Test Number
Unit Number
Fuel
Date
Owner
Location
Capacity (K»/hr)
Furnace Type £.E. V££r/CJL- Burner Type
1. Test Number
2. Load (Kft/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7 f^*rc pi mil Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( )
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Teaip. (eF)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet Tamp . ( 'r^fltfgfi'wj)
25. Windbox Temperature (°F) J / V
26.
27 • GAS S£rrM/6$ MTO/MJHJ
28 • cartel. Svfft-Y MESS f*'J
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4/76
60-33
3 1 4
-------
KVB
CONTROL ROOM DATA
Test No.
Engr.
Test Number
Unit Number
Fuel
Date
Owner
£4$
Location
Capacity (K*/hr) V$~ K
Furnace Type £, £,
Burner Type_
»/^./ /e — •?• t/ 1 t/J
1. Test Number
2. Load (K#/hr)
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4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( )
12. Air Temp Pr imary /Secondary (°Fj
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow /#Z.
31
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2 £
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60-33
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-------
KVB
CONTROL ROOM DATA
Test Mo.
Engr.
Test Number
Unit Number
Date
Owner
Location
Capacity (K*/hr)
Furnace Type C./.
Burner Type K ttf G
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Drum Pressure (psig)
8. Final Steam Press/Temp(psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( )/V?
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (Ib/hr)*
16. Fuel Press/Temp (psig/'F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. ("F)
23. Air Heater Inlet Tcmp.(°F)
25. Windbox Temperature ("F) 1 / <•/
26.
27- G>tis CONTROL. jfrrw&/f)eess
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4/76
60-33
3 1 6
-------
KVB
CONTROL ROOM DATA
Test No.
Engr. W'A/
Test Number
Unit Number
Fuel
Date
Owner
6/45
Location
Capacity (Ktt/hr)
Furnace Type C. f. \JEftTjCAi- Burner
Type
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp. (°F)
24. Air Heater Outlet Temp,. (*V)f/tffS
25. Windbox Temperature (°F) / / Y
26.
27. £/ff S/rj-jA/g/eQfjfKC'l' P/tf$S
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27S/M1
31/f. 7
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4/76
60-33
31 7
-------
KVB
Test No.
Engr.
Test Number
Unit Number
Fuel ^
- 7
CONTROL ROOM DATA
Date £~~ ' ' ^6
Owner
Location
Capacity (K*/hr)
Furnace Type C. £ - \/f*T}<;4l Burner
Type
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( ) *u.'
/ +7
Sc4
1.7
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tff\
M6
3-f
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7
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3,£
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71
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f£3
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3i/$.q
20t-r
3f.f
MSP
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Sc*
Z.qg-
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3.7
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2.3
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91
£{0
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30S/J23.
31/t.S
\
*Fuel flow in Ib/hr needed for efficiency calculation.
4/76
60-33
3 1 8
-------
KVB
Test No.
Engr.
Test Number
Unit Number
Fuel
CONTROL ROOM DATA
Date6~ 7-
Owner
Location
Capacity (K»/hr)
Furnace Type
\j£ fi T ) C 4 L
Burner Type
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. v' arum Pressure (psig) <
8. Final Steam Press/Temp(psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11 . Air Flow Primary /Secondary ( ) /Vy
12. Air Temp Primary /Secondary (°F>
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/'F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.CT)
24. Air Heater Outlet Tamp. (BF) ptfss
25. Windbox Temperature (°F) \ / H
26.
28.
3.6-£
31.0
KAM0
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KVB
Test NO.
Engr. W.A/.
Test Number
Unit Number
Fuel
CONTROL ROOM DATA
Date ° ~ ''
Owner
Location
Capacity jK*/hr> L
Furnace Type Cf
Burner Type
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( )
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
25. Windbox Temperature (°F) //3~
201-/S
}g.r
HAtfP
S* 7
S£A
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271
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15~
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'71
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3/S/33S-
33.r
-------
JVY
KVB
CONTROL ROOM DATA
Test No.
Engr.
Test Number
Unit Number
Date
Owner
Fuel
Location
Capacity (K#/hr)
Furnace Type_
Burner Type
-> fall
1. Test Number
2. Load (Kt/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7.t/A' Bram Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( )
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)* ]
16. Fuel Press/Temp lpsig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbax (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp. (°F)
24. Air Heater Outlet fumy. (T) ?K£ $5.
25. Windbox Temperature (°F) / / 1
26. 2-/3/5~
27 gAs f/rrMf /S^irfCt PttSJf*
28.
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4/76
60-33
32 1
-------
KVB
Test No.
Engr.
CONTROL ROOM DATA
Test Number
Unit Number
Fuel
Date
Owner
Location
Capacity (K*/hr)
H S"
Furnace Type C.f.
Burner Type AItf G
foil
1. Test Number
2. Load (Ktt/hr)
3. Control Method Auto /Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
1 L. '"' Bw»- Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( ) !<*j
12. Air Temp Pr ijnary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (»open C.C.)
15. Fuel Flow (lb/hr)«
16. Fuel Press/Temp (psig/eF)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. ("F)
23. Air Heater Inlet Temp. (°F)
24. Air Heater Outlet Temp. (*V)/>fffs.
25. Windbox Temperature (°F) ; J y
26- 2 / r
27. G*s SF-rvjc /re^TFei. '(f^ff
28.
205--S-
31. (
HJM>
J!oȣ
tfffi
2.SS'
l?f
HH
271
2-1
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7<
73
16
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/9
3.1
71
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2.S-
-.75-
£?{
-I>15~
Vf/HC
110/152
32.S~/T. 2
205--*
10.&
HAM
ftode
Vf>H
1-7
/3f
111
271
1£
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3.7
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at
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2*F-7
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2.3*
134
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27f
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71
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271
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-20\3.,2
1*7
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££0
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210/3*0
2i»/2lt
33/f.f
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4/76
60-33
322
-------
KVB
Test No. 200 & - ? G-r
H0.0
HAUD
t/tue
eta£t./M£
23
US'
/IH
27f
1-6
33
72
g2
73.2.%
3.?
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1
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H31
-,f&
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271/213
Zt3/3of
31 r/f. 7
2*>6-f/
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HA#D
ttott*
13?
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271
f.o
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72
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211/310
31>'g.7
*Fuel flow in lb/hr needed for efficiency calculation.
4/76
60-33
323
-------
KVB «»•
CONTROL ROOM DATA
Test Number Date o '
Unit Number Owner
Fuel 6>A 5 Location 3*
Capacity (K#/hr) 'i 5
Furnace Type C-f. \/E*T/CAl- Burner Type K lH G
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
_, t/v/ .
7. s«» Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( ) 'i~a
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp. (°F)
25. Windbox Temperature (°F) 1 / */
26 • 2,/5~
27. '„-*<; f/r7/MC/fc>u~(ei ffffS
28.
3.&G-13
H0. 7
H/tfJO
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27i
r,7
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17 ft
1£-ife
3.6- 72
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WJ
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££/
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215/300
m/3ffg
3i /Kf
2006 -/i
V0'7
HMO
ftoiJf
).f
/3S~
in
271
£"8
4/76
60-33
324
-------
KVB
CONTROL ROOM DATA
Test No.
Engr.
Test Number
Unit Number
Fuel
Date
Owner
5
Location
J,
Capacity (K»/hr)
Furnace Type C.f, VffT/CJi Burner
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7.i/v Orum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( )'*'?
12. Air Temp Primary/Secondary (°F)
13. Fan Setting FD/ID
'14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Tamp. (°F)
24. Air Heater Outlet Temp; — t^ftptffS.
25. Windbox Temperature (°F) / / Y
26. 3- / ?
28.
6-1
Type P)NG
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77.2
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31.?
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73.2-
3-5 7f
-,/
-------
KVB
Test No.
Engr.
CONTROL ROOM DATA
Test Number
Unit Number
Fuel
Date
Owner
&AS
Location
Capacity (K»/hr)
Furnace Type C£
Burner Type r\t" C*
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Pfum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp(psig/"F)
11. Air Flow Primary /Secondary ( )iurf
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. ("F)
23. Air Heater Inlet Temp.("F)
25. Windbox Temperature (°F) / /'/
26. 2 / f
27- 6/4?
120 for
jy//. f
2<*/f-23
31.0
•/
12* >3
g,f.<' fill or
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2.1*
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11
73
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i
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tSI/'tr
1 12 //?2-
?1 /t.6?
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4/76
60-33
326
-------
Test Number
Unit Number
Fuel MAT- G$S
lf\IO Test No.
l\ V D
Engr .
CONTROL ROOM DATA
Date £-/0-7(
Owner
7 rf
Location y &
Capacity (K#/hr) *f$
Furnace Type £• £ V0 RT V«
— * *- Burner Type
vffi SLI&M
Bans*. if/ec^ifaf>
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
?t" Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Pr imary /Secondary ( )
12. Air Temp Pr imary /Secondary (CF)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomizatior, Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. <°F)
21. Boiler Outlet Press (iwg)
22. Boiler outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet Temp. (<>'e)fff^-}"
25. Windbox Temperature (°F) ) / ' <-/
26. 2- / 5~
27 . £,4 _r f£ r7"//t/£ /£GAl Tffi PA£& ORE
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136,5-
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4/76
60-33
327
-------
KVB
CONTROL ROOM DATA
Test No.
Engr.
Test Number
Unit Number
Fuel
Date
Owner
Location
Capacity (K#/hr)
Furnace Type C f VfAT/CAL Burner Type # IN //(
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7. Drum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary/Secondary ( )
12. Air Temp Primary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (lb/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (DF)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24 Air Heater Outlet -T-oiRp (ftF) ^f"~
25. Windbox Temperature (°F) j / t,[
26- 2 /r
27- £•/»; ^/'^/'.///v^r^ ftt(fv<£
28.
2ol/3 //32-
3i/ / ft *r
2M6 -/?
H.r
&fJD
/dcv£
2.0?
tff.f
/yy
273
1.5
21
76
7?
3-t
-.3-
1
73
'2.7
yzr
-.70
f/f
-/, $
•J ff ") /1&f
^ c'-f- / ^-f 5
2f?fal
3?S/f.f
200G-/1
31. f
HAtft
#6*lf
1.1*
/3£
115
a.£2
I'D
11
£t
/<$0
77
r»
3,t
-.22
73
+2.V
vzr
-.7f
f/2.
'/ f
3fJ~/2ffl
210/346
?}S//.f
2.6CG-2-0
31'f
HA**
/VWf
2.*?
ISf.S'
/If \
2f7
Hf
11
72 V2
/06%
J>¥ \7V
-,/&
torte
H.Q5'
(30S
HI
**1
S,o
?£
17 13
/6&7o
3'*j\
-2 ]?-1f
~.P5~
SS0
-2 -'7
2?S/W
W fat
13/f.f
•Fuel flow in lb/hr needed for efficiency calculation.
4/76
60-33
328
-------
Test Number
Unit Number
Fuel
KVB
CONTROL ROOM DATA
Date
Test No.
Engr.
Owner
Location
Capacity (Kt/hr)
Furnace Type £ f
Burner Tpe
s / ^ C
1. Test Number
2. Load (K#/hr)
3. Control Method Auto/Hand
4. Staged Air Port Open
5.
6. Oxygen/Air Level (%)
7."" -Brum Pressure (psig)
8. Final Steam Press/Temp (psig/°F)
9. Fuel-Air Ratio Setting
10. Feedwater Press/Temp (psig/°F)
11. Air Flow Primary /Secondary ( )
12. Air Temp Pr imary /Secondary (°F)
13. Fan Setting FD/ID
14. Register Setting (%open C.C.)
15. Fuel Flow (Ib/hr)*
16. Fuel Press/Temp (psig/°F)
17. Fuel Atomization Press (psig)
18. Pressure Furnace/Windbox (iwg)
19. Smoke Meter
20. Stack Temp. (°F)
21. Boiler Outlet Press (iwg)
22. Boiler Outlet Temp. (°F)
23. Air Heater Inlet Temp.(°F)
24. Air Heater Outlet gtmp. -f
le?/J11
s / ,/•
\
1
*Fuel flow in Ib/hr needed for efficiency calculation
4/76
60-33
329
-------
Location 38
Fuel Gas Analysis
Gas Concentration, 'c by Volume
Methane 96.99
Ethane 1.9"
Propane 0.1O
Butanes .0^
Pentanes • Ol
Hexanes -00
Carbon Dioxide .60
Oxygen .00
Nitrogen .28
•Water Vapor ..00
Higher Heating Value = 1,011 Btu/SCF
330
-------
Location 38
Fuel Oil Analysis
G*AVITY,API @ 60°F
FLASH, PM CC
Visc.,SU @ 160°F
Visc.SU § 220°F
SULFUR,ASTM
B.T.U. PER POUND
CARSON
HYDROGEN
NITROGEN
OXYGEN
ASK
NET
GROSS
G3393 LAB NO 031*30
15.2
2U°F
359SEC.
118SEC.
1.88*
17^25
18^9
86.21*
11.22*
0.32*
0.3^
0.03*
15.2
21 8° F
358sEc.
119SEC.
1.88*
lorn
86.26*
11.20*
0.30*
0.29*
0.07*
33 1
-------
PLANT
LOCATION
3g'
METHOD 5 CONTROL CONSOLE READINGS
UAifc.
RUN NO. -
SAMPLE BOX NO.
DIETER BOX NO.
1ETER H /. -
: FACTOR"?
0,9
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN.
PROBE HEATER SETTING
3/9
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
zo"
JAJ&lPf
£T#tt.
TOTAL
WERAGr
Sampling
Time
(e)Min.
;6^r3
/7£>Z
J720
173*>~
I %JO
/€3^
Static
Pressure
•V20
420
4&0
V20
4*0
yzo
V30
Velocity
Head
,^^
-^jr
. z^f
.ss
. 2S
. -?-£'
.£•>"
Pressure
Differen-
tial Acres
Orifice
Meter
(AH),
In. H2O
/./
/.I
/, /
/-/
A f
/./
J. I
s Gas
Sample
Volume
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
OF
7^
*z
«8
98
/eo
27
AVG .
AVC.
Sample
Box
remprta-
ture
op
2>20
3*O
320
330
330
32.0
AVG-
32o
Temperature
of Gas
Leaving
Condenser on
jast Impinger
OF
^"<5
£- O
S" 0
3-0
(, 0
.5-0
jrf>
CO
-------
Test No.
Box No.
Test Description
PARTI CULATE CALCULATION SHEET
Date 3-- 7 - 7 C. Location J g
Sample Probe Position jo " ,*,*.,&
Test Crew
Dry Gas Meter Vol. (ft )
Final
Initial
Total
Beaker No. £.
Date
Weighed
Tare 1 fff. ^6^9
wt. 2 «y . ^ 5-sa.
3 «V. £S*7/
4
5
6
Avq SV.^^C/
Bottle No.
Inpinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 t V. 27JV
Wt. 250 2 s?V. «•?«.-/
3
4
5
6
Avg 2V.g7.i-/
Residue wt _ Hif~D
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Comments:
Impinger Water Vol (ml)
1 2
Final 3 V-*~ ^"6
Initial /po /£C
A Vol ^^jf -*-x;
3 S. Gel Total
.2 tfi.2
& tV(..(.
•2 /^^ J?/7'
-------
PARTICULATE EMISSION CALCULATIONS
Test No. 2t>/- 7 Date .T- ?~ 7^- Location 3 g
Fuel * C
.89
Engr
. x.r.
Unit No.
Sampling Train and Method
Pitot Factor, Fs_
Barometric Pressure, P «? 7. 3 O in. Hg
Tot. Liquid Collected, V^J? t?. (* ml Total Particulate, MR
m gm
Velocity Head, AP 0 . 2 ** iwg Stack Temp., Ts___££O_°R Stack Area, As_/A£ - ft
Sample Volume, Vm C / ft3 Stack Press., Psg - fl.o/ iwg Excess Cy X02%_x^» - %
Orifice Press. Dif f. , H A / iwg Stack Gas Sp. Gravity, Gs /.£->" n.d.
Sample Time, 9 /£ / min Nozzle Dia. , Dn
in. Meter Temp., T
•1. Sample Gas Volume Vm = 0.0334 Vm (Pbar + H/13.6)
2. Water Vapor Vw = 0.0474 V
3. Moisture Content Bwo - Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C « 0.0154 Mn/Vm
std
b. C = 2.205 x 10~6 Mn/Vm ,
std
c. C - Eq. 4b x 16.018 x 103
5. Abs. Stack Press. Ps = P x 13.6 + Psg
6. Stack Gas Speed Vs - 174 Fs /APTs - x
x
L.OO
7. Stack Gas Flow a. Qsw = Eq. 6 x As x
Rate @ 70°F
b. Qsd «= Eq. 7a x (1. - Eq. 3}
8. Material Flow
9. XO factor
10. Emission
11. % Isokinetic
Ms - Eq. 7b x Eq. 4b x 60
XO f «= 2090/(20.9 - XO %}
a. E - Eq. 4b x Fe x Eq. 9
b. E - Eq. 4c x FBI x Eq. 9 x 1000
14077 x Ts(Vm . . + Vw . .)
std std
6 x Vs x Ps x Dn2
Fe SC Feet/104 Btu
4
Fm SC Meters/10 joules
Oil
92.2
0-002475
Gas
67.4
0.002346
Coal
98.2
0.002636
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
0. 3'r7(, grams/DSCM
in. w abs.
36
-------
PtANT
LOCATION
OPERATOR K P.
METHOD 5 CONTROL CONSOLE READINGS
13, fi76
RUN NO. 3-oo-ft
SAMPLE BOX NO. _
METER BOX NO . f /,
fVj
0,0^
^
/
Stack
Tempera-
ture
(TD)°F
5
^o
370
S75~
310
?1$-
312.
?%5~
JZZ'
MOTE: A
r
3
131. 6000
qi/.ywo
is/./ wo
160. 6 £*£
tl.GOW
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
°F
62
70
77
7$
72
73
-73
76
r~5 ARt
e.
7J.2?
Outlet
^mout'
op
^^
£0
{£
{?
67
*7
£t
67
13-0-
(t. *?
AVG.
AVO . £$
Sample
Box
Temprta-
ture
•F
?20
32-0
32*
3/o
320
520
320
320
vjo e/?f
AVG.
Temperature
of Gas
Leaving
Condenser on
jast Impinger
OF
?o
^$-
f*
6#
£&
£0
5"7
£0
CO
CO
en
-------
PARTICULATE CALCULATION SHEET
Test No. ^ f(' - /
Box No.
Date
Test Crew
Location
Sample Probe Position_
Test Description
Dry Gas Meter Vol. (
Final
Initial
Total
Beaker No. 7
Date
Weighed
Tare 1 Ic+.o^ff
Wt. 2 ]C2.0"^f
3
4
5
6
Avg tc2.z
Bottle No.
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 / '02. 2 / 7g
Wt. 250 2 /ffZ.s-l 78
3
4
5
6
Avg if 2. 2.1 1 (ml)
S. Gel 1
/
Filter
No. 2.
. 6?7 1
:£ 87 1
.6371
. 35"f '2.
.?5~S3
,gs~s~g
.165 7
total
36.5-
Blank
No.
Comments:
Data Sheet 6002-3
336
-------
Test Ho.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Location
Engr.
Fuel
** '£
Pitot Factor,
Sampling Train and Method
Barometric Pressure, P J2 ?, 2- 7 jn. Hg
ml
Total Particulate, M j 5 j ,
, n
m gm
Tot. Liquid Collected, V, 13 (.
ic
Velocity Head, AP _°R stack Area, As //. ^ ft2
Sample Volume, Vm__£V__ft Stack Press., Psg_j2_£_f__iwg Excess 0 , XO % J2- (T %
Orifice Press. Dif f. , H /. 2- $~ iwg Stack Gas Sp. Gravity, Gs I.&5 n.d.
Sample Time, 6 *f f min
*1. Sample Gas Volume Vm
Nozzle Dia., Dn
3/9
_in. Meter Temp., T
, = 0.0334 Vm(P. + H/13.6)
std bar
Vw , = 0.0474 V,
std 1
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
std
4. Concentration a. C = 0.0154 Mn/Vm
b. C = 2.205 x 10~6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps
std
3
P. x 13.6 + Psg
bar
00
6. Stack Gas Speed Vs = 174 Fs /APTs J^- x -^g
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x =— x ^y
Rate @ 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. XO^ factor X02f = 2090/(20.9 - X02%)
10. Emission a. E = Eq. 4b x Fe x Eq. 9
b. E » Eq. 4c x Fm x Eq. 9 x 1000
11. % Isokinetic
14077 x
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
4
Fm SC Meters/10 joules
Oil
92.2
0. 002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm . by 530/Tm(eR) if meter not temp, compensated.
0.
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
grams/DSCM
^^. 7_ in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
Data Sheet 6002-4
337
-------
PLANT
LOCATION
OPERATOR
DATE
RUN NO._ _
SAMPLE BOX NO.
METER BOX NO.
'1ETER H '
: FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
-2 T.
-LL
SCHEMATIC OF STACK CROSS SECTION <^Sc^Jf£ )Sffacr6*.
Traverse
Point
Number
TOTAL
Wr.RAOn
uampiing
Time
f n 1 M -i n
10 jmn .
/rvz
15*3L
1602.
Ift2-
Static
Pressure
'
In. 'Kg.
5.
Velocity
Head
.
—
•
Pressure
Differen-
tial Acres
Orifice
Meter
(AH) ,
In. H20
^ &
l.t
i. i
i.t
s Gas
Sample
Volume
-------
Test No.
CASCADE IMPACTOR DATA SHEET
TEST RUN NO. 2QQ-/*' LOCATION
IMP ACTOR NO. / CYCLONE NO.
SAMPLE POINT LOCATION
SUBSTRATE COATING
DATE
-// — 7 (,
_OPERATOR
FUEL
TEST LOAD
IMPACTOR ORIENTATION /JOZ-Z.££
FLOW THRU IMPACTOR
klb/hr
CFM
FLUE STATIC PRESSURE Q. O ? JnHpO, VELOCITY _
NOZZLE DIA. 3/2 /AfCff ••» IMPACTOR PRESSURE DROP - END TIME
GAS METER END
GAS METER START
GAS VOLUME
CF
START TIME
DURATION
CF
FLOW RATE
6.67
CFM
AMBIENT TEMPERATURE
FLUE GAS MOLECULAR WT.
*F PRESSURE
3
.7W*
.Wt
.00 ^Jt
O
.0f>
-------
PLAMT
LOCATION
OPERATOR"
DATE <-~
METHOD 5 CONTROL CONSOLE READINGS
NO.
SAMPLE BOX NO
METER BOX NO.
1ETER H
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING ~
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN.
PROBE HEATER SETTING
JLL
30.06
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
20"
j/j*i&f
ST4C.K.
-
TOTAL
fWERAOr
Sampling
Time
(e)Min.
/&00
/£/0
/£Zt>
/630
/t.
Pressure
Differen-
tial Acres
Orifice
Meter
(AH),
In. H20
,41
. .V?
.4*
.?S
.4>S
.?*
^
s Gas
Sample
Volume
co . Zoco
/oof. /ooo
/00&.O06V
^
17. 2 Of/
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
OF
77
12.
«?
?*
9?
9?
Outlet
(T )
* mout'
op
73-
77
to
S2
?^'
S3-
AVG.
Avn.
Sample
Box
Temprta-
ture
OF
AVR.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
°F
&o
CO
(,0
to
&o
6,0
CO
4^
O
-------
Test No.
~ /8
CASCADE .IMPACTOR DATA SHEET
TEST RUN NO. J2OO-
IMP ACTOR NO. /
SAMPLE POINT LOCATION
SUBSTRATE COATING /l
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
to LOCATION ^% DATE _5--y<
CYCLONE NO. SJQsJ£. OPERATOR yf /
£»*T *J/T££ for- . j?0* yx/^*
r/GS0u)"J FLOW THRU IMPACTOR
inH9O, VELOCITY
^-7£
•y
r klb/hr
CFM
NOZZLE DIA. ^~ /A>g.y/ •» IMPACTOR PRESSURE DROP
GAS METER END ^O^.OO^ CF
END TIME
GAS METER START
GAS VOLUME / "7. tjO3~/ QF
AMBIENT TEMPERATURE
START TIME
DURATION
FLUE GAS MOLECULAR WT.
FLOW RATE
*F PRESSURE IN Hg. HUMIDITY
, TEMP. .3 ^5" *F, DENSITY
CFM
g/cc,VISCOSITY
POISE
Foil + Sample, g
Unused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
Stage Number
1
.7*t7
.75?*
.tx&f
O
2
.7VC6
.7*8?
—
*
3
.7*y?
.7*09
.00/0
&
4
.7^
.7^ay
,^AT
o
5
.-7S03
. 75»V
—
0
<£.
~y/ *9 ^1
f\f 4%* t
.7*0
• —
0
Stage
Blank
,7tM
&
FILTER NO.
Sample Blank
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
J^NAL SAMPLE, g
./*'?
,/3^/
. <9 Sf/
O
.0*f/
,/3*0
J3>20
o
FULL CONTAINER, g _
EMPTY CONTAINER, g
CYCLONE CATCH, g _
34 1
60-20
-------
PLANT _
LOCATION
OPERATOR
METHOD 5 CONTROL CONSOLE READINGS
/> '
RUN NO- *0-2-
SAMPLE BOX N0.
METER BOX NO.
1ETER H
: FACTOR"!
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
/o
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
'lumber
//
/H/ AO
TOTAL
wr.UAGr
Sampling
Time
(e)Min.
//v-s"
,*>''
///(-
flTSt-T
f/jro
fZOO
If/0
1 2*3
IZ30
iZ'JO
IZ1*
Static
Pressure
,Z^
—
,3^
.3 if
, 3f
.3*'
.3^
.3^
.3*'
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
in. H20
/.O
1,0
f-0
V.o
*t.o
1.0
4.0
v.o
s Gas
Sample
Volume
e.
M
67
•71
7^
7C,
73
7S-
AVG.
AVG.
Sample
Box
Temprta-
ture
Op
[//»/' /!/
330
3*0
3-2.0
3^0
3'0
3?o
330
AVG.
Temperature
of Gas
Leaving
-ondenser on
Jast Impinger
OP
»/?.
arj**"
(.0
6>O
60
(*0
<*0
&0
CO
-------
Test So.
Box No.
Test Description
PARTICULATE CALCULATION SHEET
Date 3~- 3.0 - 7 C. Location_
Sample Probe Posi-tion
Test Crew
Dry Gas Meter Vol. (ft )
Final
Initial
Total
Inpinger Water Vol (ml)
1 2 3 S. Gel Total
Final JZO <»7 £ ^
Bottle No.
Impinger
Content (Water)
Rinse (ml )
Date Weighed
or 250 Bake
Final 1 /e2 . s-J~£O
Wt. 250 2 jo3. S~fC>3
3 tcf. ss~t>3~
4
5
e
Avg /£>£. S~ffD3
Residue wt .o<&3<)
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
c
6
Avg
Residue Wt
Comments:
/ oo. VSo2
ICO., Vg OS"
/oa. V?o i
Probe
(Acetone )
/GO. y 963
106.^^3
/DO •tfiV
/oe>.7/o
too, e ~)e>%
, ofi. 2
Cyclone
(Acetone)
Flask
(Dry)
Filter
N0.3
.&&<&
, £.£. rf*
,&L
O
343
-------
Test No.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date_J'- aP-7£ Location 3 %
Fuel Sampling Train and Method
Engr.
Pitot Factor, Fs 6. £3
Barometric Pressure,
Tot. Liquid Collected
Velocity Head, AP
_in. Hg
m gm
//3. (, _ml Total Particulate, MR
iwg Stack Temp., Ts IB & °R Stack Area, As 7- ? 7__f t
3 Stack Press., Psg_£j_s9__iwg Excess C X0% 3,J - %
Sample Volume, vm <£ / ft
Orifice Press. Dif f . , H__f-_£__iwg Stack Gas Sp. Gravity, Gs
Sample Time, 6 -S"? min Nozzle Dia. , Dn 3/% in. Meter Temp.
*1. Sample Gas Volume Vm . = 0.0334 VmfP + H/13.6) (*/.
sto bar
n.d.
2. Water Vapor
Vw
std
°-0474 v
ic
3. Moisture Content Bwo « Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 MnAm td
b. C = 2.205 x 10~6 Mn/Vra,
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P, x 13.6 + Psg
^
std
3
6. Stack Gas Speed Vs = 174 Fs /APTs
/:
407
Ps
530
1.00
Gs
Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x •^z-:- x
Rate @ 70°F TS *°'
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
X0,f = 2090/(20.9 - XO.%)
9. XO factor
10. Emission
11. % Isokinetic
a. E = Eq. 4b x Fe x Eq. 9
b. E • Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vm _, + Vw .)
StQ St-fl
2
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
F» SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
-. 32
SCF
SCF
N.D.
O. & ~?£ 9 grains/DSCF
I./3 * I0~ lb/DSCF
/. g/ X /^> ~X grams/DSCM
in. w abs.
ft/min
//, / 3 ^- wsCF/min
DSCF/min
lb/hr
N.D.
I.SZy 10 lb/MMBtu
/
T.Jt. V/« ng/joule
•Multiply
by SSO/T^fR) if meter not temp, compensated.
Data Sheet 6002-4
344
-------
METHOD 5 CONTROL CONSOLS READINGS
Z.OCATIOW
OPERATOR"
DATE ,-7
RUN NO. 3>03-£<.
SAMPLE BOX NO.
METER BOX NC
DIETER H
1 FACTO R~"@
AMBIENT .-_
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN. 3/*"
PROBE HEATER SETTING
SCHEMATIC OF STACK CROSS SECTION
CO
c-.
1
r averse .
oint
umber
* 3.0"
TOTAL
UVCRAGH
Sampling
Time
(e)Min.
/&*o
/&/O
/C.20
/^O
MO
JLSO
/(.&'
y*r
Static
ressure
n. 'Hg.
Stack
Tempera-
ture
(TS)°F
fi y tj
ft S <*"
W<*
y
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
S/
9&
/Of
/0&
/£>
op
7?
SO
*«
*&>
z&
O *^7
c3 •
AVG.
AVG.
Sample
Box
Temprta-
ture
op
B*0
3,3.0
-$30
3^0
320
2*0
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
60
60
t,o
6,0
to
6,0
-------
PARTICULftTE CALCULATION SHEET
Test No.
Box No.
Date
S-SO'7ta
Test Crew
Location_
Sample Probe Position
Test Description
Dry Gas Meter Vol. (
Final
Initial
Total
Beaker No. / O
Date
Weighed
Tare 1 /<»3./^6
Wt. 2 /e 3 ./£ 76.
3
4
5
6
Avtj /£ 3 • /b 7c-
Bottle No.
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 /"3. 3*1"0
Wt. 250 2 /c3. 3000
3 /e2.T>eo£
4
5
6
Avg /03. 3 ee /
Residue wt . /3.3£"
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4 "
5
6
Avg
Residue Wt
Final 650-Tare
fO
^
_?_?J<2o1 (ml)
S. Gel 1
I1-S2
l£'.5~O
V.02 1
Filter
No. ,1
. 6,7 Q(a
. (e"?O£^~
. f, ~7 O &
. g S~G /
.tS03
. 2i~o4
.&5""0_?
.1797
"otal
9. OZ
Blank
• StOJ1
^£~£ O
-------
Test No.
Unit No.
PARTICULATE EMISSION CALCULATIONS
Date tr-so-Jk Location 3 g
Fuel
Engr.
Pitot Factor, Fs_
Sampling Train and Method
Barometric Pressure, P 3 f. 7.2 in. Hg
bar
Tot. Liquid Collected, V //f.02 ml Total Particulate, M 37Q-t) m gm
Velocity Head, AP • 3 5" iwg Stack Temp., Ts ?o/> °R Stack Area, As 7.f7 ft2
Sample Volume, Vm ^/. c> ft3 Stack Press., Psg . 0 9 iwg Excess 0 , XO % 2-* %
Orifice Press. Dif f . , H */> O iwg Stack Gas Sp. Gravity, Gs / _ n.d.
Sample Time, 6
min Nozzle Dia., Dn
•*/%
in . Meter Temp., Tm
*1. Sample Gas Volume Vm __. = 0.0334 Vn{P,_ + H/13.6)
std bar
Vw . = 0.0474 V,
std Ic
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
!
~6
'std
b. C = 2.205 x 10 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
std
3
5. Abs. Stack Press. Ps
^
bar
x 13.6 + Psg
r. /407 1.00
6. Stack Gas Speed Vs - 174 Fs /APTs^— x -gj-
530 Ps
7. Stack Gas Flow a. Qsw = Eq. 6 x As x 7^— x -^j
Rate @ 70°F
b. Qsd = Eq. 7a x (1. - Eq. 3)
B. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. XO factor
10. Emission
11. % Isokinetic
XO f = 2090/(20.9 - X02%)
a. E = Eq. 4b x Fe x Eq. 9
b. E «= Eq. 4c x Fm x Eq. 9 x 1000
14077 x
I =
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
A
Fm sc Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal _
98.2
0.002636
•Multiply Vai , by 530/T (»R) if meter not temp, compensated.
std ni
SCF
N.D.
grains/DSCF
/O' grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
X ID~ lb/MMBtu
3. 3- ng/ joule
. 3
Data Sheet 6002-4
347
-------
PLANT 3"?
LOCATfdN" 3g"
OPERATOR Kf
DATE S~-f/^ 7
RUN NO. 3^
SAMPLE BOX NO.
METER BOX NO.
1ETER H
2 FACTOR"!
METHOD 5 CONTROL CONSOLE READINGS
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
STAtC. .
fsir-jt^zt
four
TOTAL
WERAGF
Sampling
Time
(e)Min.
///<
//-?£
//3&
//Vt
//s~£
/*o/
V-f*»>
Static
Pressure
'
In. 'Hg.
Stack
Tempera-
ture
(Tg)°F
y.2*
VZ7
92 1
?*7
V27
**•?
42-7
Velocity
Head
«Ps>
.2>y
.z^f
. 3s-
. 3-S-
,3-sr
. Jj-
, ^*"
Pressure
3if feren-
tial Acres
Orifice
Meter
(AH),
In. H20
.33
. S3
.93
. 83
.83
. £3
. 23
s Gas
Sample
Volume
.
oo
-------
Test No. £O3-
CASCADE -IMPACTOR DATA SHEET
TEST RON NO. 2O3- J27 'LOCATION 3° DATE /%,
TMPACTOR NO. CYCLONE NO. S/O *> £T~ OPERATOR J? f
SAMPLE POINT LOCATION ^TrfttC frf^T ^t>cu£'/C /~'0£'7~
SUBSTRATE COATING (^/€f /^S. *f FUEL TEST LOAD
IMPACTOR ORIENTATION ^£>% g. ^ £ litftt)^ FLOW THRU IMPACTOR
*Y ^/ /?;
klb/hr
CFM
FLUE STATIC PRESSURE inHjO, VELOCITY
NOZZLE DIA. 7*f /**CH *» IMPACTOR PRESSURE DROP END TIME
GAS METER END
CF
CF
GAS METER START _
GAS VOLUME 3%, 99? % CF
AMBIENT TEMPERATURE
START TIME
DURATION ^
FLOW RATE
CFM
PRESSURE
IN Hg. HUMIDITY
FLUE GAS MOLECULAR NT.
, TEMP.
F, DENSITY
g/cc,VISCOSITY
POISE
Foil + Sample, g
Dnused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
Stage Number
1
.7*/*
.7**?
.*«>7-
0
,*fl»09
2
.7^0
.7/^
,^y
O
.0*24
3
.?stf
+J^r/ 5
/iS 8^-^
.*>S*
O
.4)03^
4
,7f«a
*^£/ / t
I V I
.DO*/
O
.0021
5
.7*96
.1S90
.CMC,
&
QOb £•
(^
.1&3
,7.5-fS
.o*o*r
0
.000*
Stage
Blank
.7^7
.?«•/*
O
4 sT
_PILTER NO. Sample Blank
JUTER + SAMPLE , g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
.BLANK^ g
•I2£L_S_AMPLE, 9
./^/<^
./3.2S
.0^3
0
.0293
.t*¥3
./3*3
£>
FULL CONTAINER, g _
EMPTY CONTAINER, g
CYCLONE CATCH, g _
349
60-20
-------
PLANT
LOCATION
OPERATOR"
DATE <--
METHOD 5 CONTROL CONSOLE READINGS
RUN NO.
SAMPLE BOX NO.
METER BOX NO.
DIETER H _
2 FACTOR~1?
T?
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, %
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
3-rjCK.
**&r
XL4U>£X /o/tT
srv
e.fi-&>*.
TOTAL
\vcuAor
Sampling
Time
(e)Min.
/y/o
/y^jr
/?*£
r /1*r&
/*•//.
J3-2C-
/srs*
£-2.
Static
Pressure
^s''
In. 'Kg.
Stack
Tempera-
ture
(TS)°F
y^t
42$'
• —
yzf
yzS'
y^-i"
Velocity
Head
(P.)
.^«
.v«
,^-
.yj"
#*'
.v±"
Pressure
Differen-
tial Acres
Orifice
Meter
(AH) ,
In. H2O
s-.V
9o
Outlet
(T .)
mout'
OP
7V
7
AVG.
AVG.
Sample
Box
Temprta-
ture
op
3»o
320
—
330
3?o
3£o
AVR.
Temperature
of Gas
Leaving
-ondenser on
Last Impinger
"F
<£o
73"
6,0
•70
68
CO
-------
PARTICULATE CALCULATION SHEET
Test No.
BOX NO.
Test Description
Date
Sample Probe Position
Location
-3 8
Test Crew
Dry Gas Meter Vol. (
Final
Initial
Total 1 (ml)
S. Gel 1
Sii.6,?-
20. YS.
C. . s o //
Filter
No. _f
. j-*fl3
.5"«0^
,J-gi>*
,7ft"?
,?£?y
.7S1(-
.?a.ty
• SWO
\3tal
/•* 0
Blank
No. C
.S~iS~/
• -ftf/
,ft,<'/
.S-Sff
. s&s/
.ft*/
o
leet 6002-3
35 \
-------
PARTICULATE EMISSION CALCULATIONS
Test NO. 2&O-2? Date f- 2 Location
Unit No. Fuel Sampling Train and Method
Engr.
Pitot Factor, Fs
Barometric Pressure, P.
Tot. Liquid Collected,
Velocity Head, AP__L_^£[
bar
ml Total Particulate, M
_in. Hg
m gm
_iwg
Stack Temp., Ts S 83" °R Stack Area, As 7.
-------
FXsSl l-l T
ROL C7OMSOLE
OPERATOR
DATE _s-=-3
RUN NO. .
SAMPLE J3OX NO.
METER BOX NO.
METER H
z FACTOR"!
TVMGIENT TEJMITSI
BAROMETRIC PRESSURE
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
'At
SCHEMATIC OF STACK CROSS SECTION
Traverse 5
Point
Number
S9i7~
AxtT"
XOiOE*
t TOTAL
VERAGH
sampling
Time
(e)Min.
/^^7
tLS~7
/707
l-?>-7
I7Z7
/732
y^
Static
ressure
.*/*'
.**'
.1^
.I*'
.^
Pressure
Differen-
cial Acros
Orifice
Meter
(AH),
In. H20
.*«
.6«
.fe«
>g
./:»
s Gas
Sample
Volume
(vm) ft3
21*1,60° O
je.s.srt»
2-?o.*°°*
3~??./oe>e>
2_1c,S%
20.3f>S~S
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
°F
7?
7?
7?
7?
79
?*
Outlet
(T )
v mout'
op
73"
7Y
?y
?'~
3~^~
6. ^
6 0
CO
CJI
CO
-------
Test No.
TEST RUN NO.
IMPACTOR NO.
CASCADE IMPACTOR DATA SHEET
LOCATION
DATE
CYCLONE NO.
OPERATOR
SAMPLE POINT LOCATION
SUBSTRATE COATING
FUEL
TEST LOAD
_inH20,VELOCITY_
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
NOZZLE DIA. r*/ /*)CH •»• IMPACTOR PRESSURE DROP
GAS METER END CF
FLOW THRU IMPACTOR
.klb/hr
CFM
END TIME
GAS METER START
CF
START TIME
DURATION
GAS VOLUME £6. 3OS'S CF
AMBIENT TEMPERATURE *F PRESSURE
FLUE GAS MOLECULAR WT. , TEMP.
FLOW RATE
CFM
IN Hg. HUMIDITY
"F, DENSITY
g/cc , VISCOSITY POISE
Foil + Sample, g
Unused Foil, g
Sample , g
Correction
for Blank, g
Final Sample, g
Stage Number
1
.7*57
,7W
*«>?
O
.too?
2
.7V33.
.7^7
.000^
O
.OoeS-
3
.7m
.7^3-
poo^
O
.000-7
4
.7¥t*
.7*6,7
.Mif
o
.00,*-
5
,7^/0
.•?
-------
METHOD 5 CONTROL CONSOLE READINGS
cow
OPERATOR'
DATE .5-
RUN NO.
SAMPLE BOX NO.
METER BOX NO. "
1ETER H ~
- FACTORT
JVMDIENT TEMPERATURE
BAROMETRIC PRESSURE ~
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
JLOu)£t-
£A3.r
flZtK.
TOTAL
WE RAG
ampling
Time ]
e)Min.
//so
ItiO
HJtO
II ZO
HfO
Itfto
//s-1
^
Static
3ressure
(Ps),
Cn. 'Hg.
Stack
etnpera-
ure
T ) °F
s
y-?6
Vlt,
fst
V27
oo
35-4. ^ooo
3
-------
Test No.
Box No.
O/-
Test Description
PARTICIPATE CALCULATION SHEET
Test Crew
Date S~- 2?-
Location
Sample Probe Position_
Dry Gas Meter Vol. (
Final
Initial
Total
Beaker No. /"?
Date
Weighed
Tare 1 ?*r f« 7 V
Wt. 2 ^^'.9^'?
3
4
5
6
Avq g.S', 9 0 7£
Bottle No.
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 ts'.tt.tl
Wt. 250 2 £y: ££ g 5
3 £ .S". ? £ 8 V
4
5
6
Avg 2.i'. H23
Residue wt
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Final 650-Tare
ftJ)
/v
2 V. C, 1 2-£"
gV
77, y yo. ta.
69. ad
10 . 12 J
Filter
No. &
.^f.£-/
.S~gS~/
.7CZ-&
.7LP.I
.76. ?V
. •7&Z'?-
./•>•?/
Potal
?5". %Z
Blank
No. -7
. _s~?y9
.^-ZV-7
.^~6
Comments:
Data Sheet 6002-3
356
-------
PARTICULATE EMISSION CALCULATIONS
Test No. ,? ft Stack Press., Psg ^.^9 iwg Excess 0 , XO % /. iT-*' %
Orifice Press. Dif f . , H 3 - -S" iwg Stack Gas Sp. Gravity, Gs _ / _ n.d.
Sample Time, 6 .5^? min Nozzle Dia. , Dn •3/
jn. Meter Temp., T
*1. Sample Gas Volume Vm = 0.0334 Vm(P + H/13.6)
Vw . = 0.0474 V,
std lc
2. Water Vapor
3. Moisture Content Bwo = Eq. 2/{Eq. 1 + Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm ,
std
b. C = 2.205 x 10 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
std
3
5. Abs. Stack Press. Ps = P x 13.6 + Psg
bar
6. Stack Gas Speed Vs = 174 Fs /APTs f~- x ^j^-
V Ps Gs
530 Ps
7. Stack Gas Flow a. Osw = Eq. 6 x As x —— x -r^T
TQ Ai\t
Rate @ 70°F s
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. X02 factor
10. Emission
11. % Isokinetic
XO f = 2090/(20.9 - X02%)
a. E = Eq. 4b x Fe x Eg. 9
b. E = Eq. 4c X Fm x Eq. 9 X 1000
14077 x Ts(Vmgtd + Vwgtd)
j = j
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
•Multiply Vm . . by 530/T (°R) if meter not temp, compensated.
std in
SCF
SCF
O. Oft: N.D.
O. O77(e> grains/DSCF
/. // H /0~* Ib/DSCF
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
lb/hr
2. O N.D.
O • "O Ib/MMBtu
^ 7.C> ng/joule
Data Sheet 6002-4
357
-------
PLANT
LOCATION
OPERATOR"
DATE .g-t
RUN NO.
SAMPLE BOX ""NO.'
METER BOX NO.
DIETER H
METHOD 5 CONTROL CONSOLE READINGS
FACTOR"?
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
/.ou)E*
£/>&r
£,TffH K-
/V JtO"
TOTAL
WrUACr
Sampling
Time
(e)Min.
fx-/3~
/s-*^
^3^
S£-
s^e
^•jzo
Velocity
Head
(ps^
.*?
3
-------
PARTICULATE CALCULATION SHEET
Test No._
Box No.
Date -£~- ;?-iT-
Test Crew
Location
Sample Probe Position
Test Description
Dry Gas Meter Vol. (
Final
Initial
Total
Beaker No. £ &
Date
Weighed
Tare 1 fc>2 . D^v^
Wt. 2 /e>£ o yog
3
4
5
6
Avq /£>:?. 0^07
Bottle No.
Impinger
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 /OS./V37
Wt. 250 2 /eS. /MO
3 /e£. )VV>
4
5
6
Rv5 io£ ./c)
Residue wt
Final 250-Tare ' ^°2>£
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Comments:
ftJ)
/r
/£3. /2.Z7
/G 3 . /S33
/o3. /g K. f
Probe
(Acetone)
/o3. £e>&3
/Q 3r *t.Q*Z£
/OS .zop<4
/OZ. 20S«
.o/9?
Final 2£
Initial /e
A Vol /o
/9
$(.. 5"893
td.fS^y
&(, . 5~8?V
Probe
(Water)
ri.^Sji"
?t. £396
f i . C, 3 9^
,0ro2
Impinger
1 2
>
-------
PARTICULATE EMISSION CALCULATIONS
Test No. £C>2- */ Date S"-£!>- 7 (* Location
Unit No. _ Fuel
Engr.
Sampling Train and Method
Pitot Factor, Fs
.83
Barometric Pressure, P, % 9- 7 3 ' in. Hg
t>ai
ml Total Particulate, M 3 3# ?
m gm
Tot. Liquid Collected, V
Velocity Head, AP • 3V iwg Stack Temp., Ts /O'O °R Stack Area, As "?. fj ft
Sample Volume, Vm O ft3 Stack Press., Psq 0-6 7 iwg Excess Q^, XO2% ^*- U %
Orifice Press. Diff. , H 3-3 iwg Stack Gas Sp. Gravity, Gs / n.d.
Sample Time, 6 <» 3 min Nozzle Dia., Dn /% in. Meter Temp., T °R
*1. Sample Gas Volume Vm = 0.0334
2. Water Vapor Vw = 0.0474 V
3. Moisture Content Bwo = Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C «= 0.0154 Mn/Vm
sta
b. C = 2.205 x 10~6 Mn/Vm
c. C = Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P^ x 13.6 + Psg
bar
+ H/13.6)
_.
sta
3
6. Stack Gas Speed Vs = 174 Fs /APTs I
407 1.00
Ps X Gs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x ^- x -^-.
Rate e 70°F 1S 4U'
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
XO f = 2090/(20.9 - XO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Pm x Eq. 9 x 1000
9. XO factor
10. Emission
11. % Isokinetic
14077 x Ts(Vm + Vw )
6 x Vs x Ps x Dn2
Fe SC Feet/104 Btu
4
FBI SC Meters/10 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
SCF
£>.£>%
. /
0.09C, K.D.
grains/DSCF
'<•»
Ib/DSCF
/
grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr
N.D.
Ib/MMBtu
ng/joule
%
•Multiply Vm by 530/Tjn(<>R) if meter not temp, compensated.
Data Sheet 6002-4
36 U
-------
PI^M-JT
LOCATION
OPERATOR"
3 g
METHOD 5 CONTROL CONSOLE READINGS
.
RUN NO. 2o/ -73,
,
SAMPLE BOX NO.
METER BOX NO.
4ETER H
2 FACTOR"!
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, % "
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
jLex^if- "i
KitS.7~
&TJ9&K
/^/ ao"
TOTAL
WERAGH
ampling
Time
(e)Min.
////
/A*V
//3'
In. "Hg.
Stack
Tempera-
ture
(T )»F
o
y^3
y-?2
V-J/
/^/
vjy
V^V
Velocity
Head
(P.)
.32-
. 13
. 32
. J^
- 3 3-
/3»
Pressure
Differen-
tial Acros
Orifice
Meter
(AH) ,
In. H20
. 7?
,7
-------
Test No.
CASCADE .IMPACTOR DATA SHEET
TEST RUN NO.
IMPACTOR NO.
LOCATION
3%
DATE
CYCLONE NO.
OPERATOR
SAMPLE POINT LOCATION <,
SUBSTRATE COATING
FUEL
TEST LOAD
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
J>OU>*J FLOW THRU IMPACTOR
.klb/hr
CFM
_inH2O,VELOCITY_
NOZZLE DIA. Xy /AfCff •» IMPACTOR PRESSURE DROP
GAS METER END CF
END TIME
GAS METER START
GAS VOLUME
CF
START TIME
DURATION
CF
FLOW RATE
CFM
AMBIENT TEMPERATURE
PRESSURE
IN Hg. HUMIDITY
FLUE GAS MOLECULAR WT.
, TEMP.
F, DENSITY
g/CC ,VISCOSITY POISE
Foil + Sample, g
Unused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
Stage Number
1
• 7S/t
.74*76
.to**
o
.0°**
2
.7****
.7***
f ooSio
£>
,, (?£>£ o
3
.743-7
.75^3
.*orV
O
.005^
4
,7V^
.7VV/
. ••*<*-
o
.00^
5
7^/gO
.1^70
.06/0
O
.one
(e
.7 ft*
.If*
.000-7
0
.0*07
Stage
Blank
.75?jr
.?y*r
0
(* 7
FILTER NO. Sample Blank
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
BLANK, g
FINAL SAMPLE, g
,/£.3t
,/•&*
.ML
o
.?2l/(f
.AW
./3Vt
6^
FULL CONTAINER, g
EMPTY CONTAINER, g
CYCLONE CATCH, g
362
60-20
-------
PLANT
LOCATION 31£
OPERATOR
DATE 3-, y(_ _ 7£-
RUN NO. 1OT~-
SAMPLE BOX NO.
METER BOX N.O..
METER H
METHOD 5 CONTROL CONSOLE READZNGS
_
: FACTOR"?
AMDIENT TEMPERATURE
BAROMETRIC PRESSURE ~
ASSUMED MOISTURE, %
HEATER BOX SETTING _
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN.
PROBE HEATER SETTING
SCHEMATIC OF STACK CROSS SECTION
Traverse
'oint
Number
^"-*^7-
/UKjJfK.
a7>a K.
/*> ao"
TOTAL
WEKAGr
ampling
Time
(e)Min.
/£»o
/&/0
/6>£o
/L3o
/&VO
J&,
. 30
. 30
. 30
. 30
. -30
. 30
Pressure
Dif feren-
:ial Acres
Orifice
Meter
(AH) ,
In. H20
. 6
. 6
. £
. c.
.6
.6,'
s Gas
Sample
Volume
0
733. 3000
73-?,S~000
74 '/. 7£>oo
~?-t?
•T&
s-j."
srs"
-S'-i"
^"•-5"
CO
O5
-------
Test No.
TEST RUN HO. 3 O £ -
IMPACTOR NO. X
CASCADE IMPACTOR DATA SHEET
LOCATION
DATE £~~
CYCLONE NO.
OPERATOR
SAMPLE POINT LOCATION ^ 0 O ' / ' '
SUBSTRATE COATING X-7' ''•' r i-'
TV"" : '
J? 7"
FUEL
TEST LOAD
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
NOZZLE DIA. A/
FLOW THRU IMP ACTOR
_inH2O,VELOCITY
IMPACTOR PRESSURE DROP
END TIME
GAS METER END
CF
GAS METER START
CF
START TIME
DURATION
GAS VOLUME / 9, 3 9
CF
FLOW RATE
AMBIENT TEMPERATURE
PRESSURE
IN Hg. HUMIDITY
.klb/hr
CFM
CFM
FLUE GAS MOLECULAR WT.
, TEMP.
"F, DENSITY
_g/cc .VISCOSITY POISE
Foil + Sample, g
Unused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
Stage Number
1
,W7
.7y*y
.00 1 3
o
,0o/3
2
,7*-?-?
ns/{*>
•0027
0
.0027
3
.710%
.73??
.OOff
O
. 60/1
4
.7-fTO
-75"7/
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,-->
,001*
5
,-?y*3
.7yV8
. <3oa3."
ocoy
Stage
Blank
. ?.s*r
.7Jr^"
£)
7 €
FILTER NO. Sample Blank
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
BLANK, g
FINAL SAMPLE, g
.Mot
.JZtf*
.ox.*'
o
.£>&,*?
, /5,-ro
tzs-o
O
FULL CONTAINER, g _
EMPTY CONTAINER, g
CYCLONE CATCH, g
364
60-20
-------
PLAHT 3 g
LOCATION 3\
OPERATOR
METHOD 5 CONTnOL CONSOLE READINGS
RUN NO. -2ol, /
SAMPLE BOX NO.
METER BOX
DIETER H
: FACTOR"!
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE "
ASSUMED MOISTURE, %
HEATER BOX SETTING
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
J.OUJf /£
f^AT
STstf/C.
;* lo "
TOTAL
WCRAGI:
ampling
Time
(e)Min.
/O/£>
/ozO
So 30
/ovo
to^o
S/f>0
//£>-?
5~?
Static
Pressure
«v-
In. -Hg.
Stack
Tempera-
ture
(T )»F
o
V/7
• 3^
.3/
,*ooo
?gO, oooo
8?6. say?
^/. Of>e>o
Gas Sample
Temperature at
Dry Gas Meter
Inlet
/T
umin.)
op
?i>-
9/
97
/o/
/OA
9S
97
Outlet
(T )
v mout'
°p
SO
S3
8i>"
«S
V
9o
90
AVG.
AVG.
Sample
Box
Temprta-
ture
"F
3?0
32o
32#
3 50
350
3^tf
3 3
en
-------
Test No. J.0f-fi>'
Box No.
Date
PARTICULATE CALCUIATION SHEET
1-7-7 Iff Location
Test Crew
Sample Probe Position
Test Description
Dry Gas Meter Vol. (
Final
Initial
Total
Beaker No. "2- 3
Date
Weighed
Tare 1 /<»/. & 3 £ V
Wt. 2 jo/.tsm"
3
4
5
6
Avq /O/. (.Stf
Bottle No.
Impinge r
Content (Water)
Rinse (ml)
Date Weighed
or 250 Bake
Final 1 _/O/. ££<}(>
Wt. 250 2 to/, {.(fto
3 /o/.6t,9f
4
5
6
Avg /ff/. £.£ 9/
Residue wt . e3(2£
Final 250-Tare
Date Weighed
or 650 Bake
Final 1
Wt. 650 2
3
4
5
6
Avg
Residue Wt
Final 650- Tare
ftj)
21
gV,6.T£3
JV.i^s-i-
Sf. S.3, /oo
g ^c3
Cyclone
(Acetone)
Water Vc
3
x1 -??-
.£•-?•?>
,7^3-'i>
.-7S-S-V
.7SS&,
.-JfS-S'
. /76V1
total
!?,o.5~
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No. G
.ST6V3-
.S(c^*-
.s-cv/
.S-t,V3-
.S-&1//
. S-6,95-
. J-ti'T"l/
• SC.9 '2
C>
Connoents:
Data Sheet 6002-3
366
-------
PARTICULATE EMISSION CALCULATIONS
Test No. 2.O/-/'!>" Date -5"- S7-7& Location
Fuel
Engr.
Unit No.
Pitot Factor, Fs O.S3
Sampling Train and Method
Barometric Pressure, P 30.
Tot. Liquid Collected, V
ti.Q*'
Total Particulate, M 3. 8 a". .
n. Hg
_m gm
Velocity Head, AP • 3
-------
PLANT
LOCATION 3 g
OPERATOR
DATE
METHOD 5 CONTROL CONSOLE READINGS
--37-
RUN NO. 203,
SAMPLE DOX .
METER BOX NO. £
DIETER H "
3 FACTOR"? '
AMBIENT TEMPERATURE
BAROMETRIC PRESSURE '
ASSUMED MOISTURE, % '
HEATER BOX SETTING "
PROBE LENGTH, IN.
NOZZLE DIAMETER, IN."
PROBE HEATER SETTING"
J±.
SCHEMATIC OF STACK CROSS SECTION
Traverse
Point
Number
"?Jf
f*, 20"
TOTAL
\VERAGr
Sampling
Time
(e)Min.
/too
tf,o
l'
In. 'Hg.
Stack
Tempera-
ture
(T )oF
S
y/ <,*"^?
^3-0
VJTO
y 1 f~ ' f)
yy?
W9
Velocity
Head
(P.)
.33-
.3^
.**'
.zS
.3i"
.3i"
Pressure
Differen-
tial Acros
Orifice
Meter
(AH),
In. H2O
.79
,-76
,78
. 78
-78
,76
s Gas
Sample
Volume
t>%
Gas Sample
Temperature at
Dry Gas Meter
Inlet
(Tmin.)
op
1*
36
^
t<~
«•?
Outlet
(Tmout>
27
?6
rt i i
rt O
<33
AVG.
AVG.
Sample
Box
remprta-
ture
Op
AVG.
Temperature
of Gas
Leaving
Condenser on
Last Impinger
op
£<*"
&0
(& O
D C'
LO C-'
CO
o>
00
-------
Test No.
CASCADE IMPACTOR DATA SHEET
TEST RUN HO. X O <> ~ * S LOCATION J> 0 DATE S~ ' 3 7 - f <-
IMPACTOR NO. / CYCLONE NO. SJ & *V £ OPERATOR /f, f3. Sr .
SAMPLE POINT LOCATION <, 7~s*7 £?/-i
0
.00^
2
.-#**
. 7&1
,00*1
o
.00*1
3
.740*
.7S7S
.OOZ4
0
.oozV
4
.7S3I
.7S03
.oolS
C
.00/8
5
.7472
.74/67
. 000 £~
o
.000 £
(f>
.73S*
. 73 «»"
,0003
o
,000 3
Stage
Blank
*~jfQ S
*7 ^'^ ^
O
FILTER NO.
Sample
Blank
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
JilANK, g
JlKAL SAMPLE, g
,/O3
,/3st>
.oSSU
O
to*s*
/33y
.133 f
0
FULL CONTAINER, g _
EMPTY CONTAINER, g
CYCLONE CATCH, g _
369
60-20
-------
Proj ect:
Date r/*f/7(-
VELOCITY TRAVERSE
Test Description:
PJC
Location:_
Unit:
Stack Cross Section
-~5
Personnel:
Test: ..
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient:
rbtti
ft
Time
Traverse Point
Port Depth
e
1
2
<-/
6
9
10
•z
/W
>6
*t
n.r
/
-------
VELOCITY TRAVERSE
Test Description:
Personnel:
/ D 0!/'i.f '
\ I
Stack Cross Section
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):
Pitot Tube Coefficient:
|V2
?7
Time
Traverse Point
Port Depth
O
2-
'/ _,
4
?
10
IZ
!<•!
1C
>?
**>
21
2.4
3- 6
2- 3
30
Velocity
Head
(in. H.,0)
AP
.OS"
.05
,e*r
.ff
,*5
,CS
.e?
,e>f
• @5
/?$"
.£>?
,05
.05
,0f
.05
.05
Gas Temp.
("F)
.02f
,03
.
-------
Project:^
Date:
VELOCITY TRAVERSE
TeEt Description:
Location:_
Unit:
Stack Cross Section
Personnel:
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient:
(P.)
V = 85.4B Cp
1/2
1
1
1
1
I
1
1
1
1
i
Ml.
; 1 i 1
1 ! 1 1
1 ' !
1 ' ! 1
1 M '
• ' ' !
i '
: i i • i
Ei i
i lii
i III
1 1 '
! | ill
, ; .1
' I ' '
' • i
1 • i 1
|
j
i
i
1
I
Time
Traverse Point
Port Depth
ttf
/.r
5*0
7.e>
t^
f./
Ay*P
Velocity
Head
(in. H20)
f/7tS
.11 ,1?
.H3I
.21 .21
,21 .20
Jl .X
,15
*/e
.11 .It
.17 .11
•If -ft
•19 ft
J6>. It
jfJI
,Hf ,///
Gas Tec?3.
Gas Temp.
Ts
Molecular
Vt.
MS
Velocity
(ft/sec}
vs
02
Cone.
(% Dry)
6002-13
372
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: * / 5 / 7£
Location: 3> & Stack Cross Section
Unit:
Test: Z.fl-2- Personnel:
Fuel : - -
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg) : (Ps) ~-\
Pitot Tube Coefficient: (CXJ
_ 1/2
FT AP! '
V - BS 10 C S
s P P M ;:: —
L E SJ . .
:__ :_j_
: — -±jr
— L
'
p~
-i-r
4 j
1
___i_|
-)-
^
F
| |
i i , , i ' i j
^ -._+=}- -rjT
T
j
I !
--(-— — |-
-4
4-1
i
— 1-
— r
i
-T—
|
•
!
rn:-— H-H-
1
1 ' i i
i
— r
!
.
_i_
i
T
Time
Traverse Point
Port Depth
.-¥
/.5~
1°
7
t.f
1.1
SVG.
Velocity
Head
(in. H.,0)
fftf a./7
.21 ./f
.2? .2.0
.2-6 ,24
.2? ,2a
.21 .20
,17 .13
.22? -27
Gas Temp.
(°F)
Gas Temp.
(°R)
Ts
Molecular
Wt.
«S
Velocity
(ft/sec-)
vs
02
Cone.
(% Dry)
6002-13
373
-------
VELOCITY TRAVERSE
Project: Test Description:
Date : f/S r 7 f
Location: ' 2 Stack Cro3s Section
Unit:
Test: .2 & */- .7 Personnel:
Fuel:
Barometric Press, {in. Hg):
Absolute Static Press, in Stack (in. Hg) : (Pn) '
Pi tot Tube Coefficient: (C_) ^- -
[_._-, 1/2 -- -
TC^ 1
_ — 1
P M -
s sj .
1
_l_L
::::-::
j
1 M I
' 1
1 I i 1 1 i 1 ! | 1
' i
j | 'i
1 1 \
\
-i — L- 1 — ^~
i
I
1
!
J_J , , , , | [
i
I i
T
|
1 1
i 1 1
' ' i
1 1 ]
: • : I
Time
Traverse Point
Port Depth
,Y
1,?
1.0
7
1S
1,1
AVG.
Velocity
Head
(in. H2D)
<*/fAP f/7
-// ./J
.19 .15
.'1 .17
.17 .It
.17 .*
Jf .W
.172- .tVZ
Gas Temp.
(T)
Gas Temp.
(°R)
TS
Molecular
Wt.
HE
Velocity
(ft/sec^
vs
02
Cone.
(% Dry)
6002-13
374
-------
Project:
Date: 6/l/7f
Location:
Onit:
VELOCITY TRAVERSE
Test Descriptions
Stack Cross Section
'6
Personnel:
Test:
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):_ (PB)
Pitot Tube Coefficient: (c_)
V « 85.48 C
1/2
±f±t
Time
Traverse Point
Port Depth
1
5
5"
7
1
II
13
>5
17
H
2 1
21
2?
2 7
21
J I
Velocity
Head
(in. H70)
ylT ipj"
• £l .If
,i? .ie
,31 .12
Jf .3"
.if .27
jr .2?
.11 .2?
,20 ,/f
.2i .}?
.2( ,lo
,3£ .?/
,? .M
.2g .X
.2? Jf
.23 ,33
,2! .22.
Gas Tenrp.
t°F)
Gas Temp.
(°R)
Ts
Molecular
VJt.
«S
Velocity
(ft/sec}
vs
02
Cone.
(* Dry)
6002-13
376.
-------
Project:_
Date:
VELOCITY TRAVERSE
Test Description:
Location:_
Unit:
StacX Cross Section
Test: 2C"-I'
Fuel:
Personnel :
Barometric Press, (in. Ilg):
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient:
V «= 85.48 Cp
1/2
±±
-H-
Time
Traverse Point
Port Depth
.H
).?
1.0
7.0
i.r
1.1
AVG.
Velocity
Head
(in. H,0)
&<*~d2)
.ff . /4
.2? .2,1
.21 .21
,2} .21
.11 .2)
,'1 .11
,205 .20
Gas Temp.
t°F)
Gas Temp.
(°R)
TS
Molecular
Wt.
"s
Velocity
(ft/sec}
•vs
02
Cone.
(% Dry)
6002-13
376
-------
Project:_
Date:
VELOCITY TRAVERSE
Test Description:
-|
LVsJ
1/2
FD
Time
Traverse Point
Port Depth
/
^
jT
7
f
/ ;
/J
1C
17
>1
2 i
2?
25
27
3-1
31
Velocity
Head
(in. H,0)
/ AP 2-
.37 ,-j
.10 .i
.» .:
.0 .1
.r^ .1
,•// ,i
,Vf •$
.ft ,;
1 .70
?-,{(
c-.te
7-.K
' .ft
? .17
.V^
o .21
.^ .V .2?
.fa .15 Jg
.67 .50 -W
,f( .W .W
.ft .70 ,#
fi .11
-« . If
.(? .ge
Gas Temp.
rn
ii.r
Gas Temp.
<°R>
Ts
Molecular
Wt.
«S
Velocity
(ft/sec^
VS
02
Cone.
(% Dry)
6002-13
377
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: £f7f~?7
Location: X C
Unit:
Test: 2O1"! ~ 1 1 Personnel:
Fuel:
Barometric Press, (in. llg):
Absolute Static Press, in Stack (in. Hg): (P.)
Pitot Tube Coefficient: (CV,)
[_, Ats -i 1/2
T API
- . - - 1
P M
£ S J
Stack Cross Section
i
1
1
i
-J-
j
I
1
_L
i
i~
i
1
i j
1
1
1
_1_
1 1 !
I 1
1 | :
I !
j :
1 1 * '
i
1 ' ' !
' ' i '
i i
1 !
|
! i :
1 i |
i
1 ;
Time
Traverse Point
Port Depth
• i
l-5~
3
7
?,r
1.1
Velocity
Head
(in. H,0)
*/7AP */.?
./¥ ./f
,2t .1-1
.Zff -11
,21 .21
,/P .Zl
.'? .20
Gas Temp.
<°F)
Gas Temp.
(°R)
Ts
Molecular
V)t.
"s
Velocity
(ft/sec^
VS
02
Cone.
(% Dry)
6002-13
378
-------
VELOCITY TRAVERSE
Project^ Test Description:
Date: <£/ / / "76
Location: ,' ? Stack Cross Section
Unit: _ _
Test: 2&V-1I Personnel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg) : (P0) -j
Pitot Tube Coefficient: (r )
fT AP~] '
V •- 85 48 C 1 '^ • •- 1 '
s P I P_M 1 ; -
L s SJ
U._UI Mil
|l|j|l^ip35S3
_j ^4--r ' -•' i *-
"~4JJ-M^4--^-^-i+
4" | |" l( * j ; ! ' 1 L.
1 i ! i ! j
I " ' 1 ' ' 4-
-i i l I 1 1-|-| ' ; •' i | | 1 |
1 I i i ! • i
1 i ' 'i
i • i •..-(- l
Time
/"
Traverse Point
Port Depth
Ffon wit.
}
5~
3
'3
1?
21
>?r
**)
31"
Velocity
Head
(in. H_,O)
&<*'&>
.56 .W
J7 .33
,3i .?
-------
Proj ect:
Date 6/7/76
Location: > ?
Unit:
VELOCITY TRAVERSE
Test Description;
Stack Cross Section
- 13
Personnel :
Test:
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):_
Pitot Tube Coefficient:
<
VS ' 85-4B CF I P.
,1/2
*J
J h
Time
Traverse Point
Port Depth
. 1
f.f
3
7
r.r
1-1
Velocity
Head
(in. H20)
»/7AP at >g
,°7 . 1
.1 .11
./ .11
,01 .12
.) .13
,0$ .13
Gas Temp.
(°F) "
Gas Temp.
CR)
TS
Molecular
Wt.
»s
Velocity
(ft/sec^
VS
°2
Cone.
(% Dry)
6002-13
380
-------
Proj ect:
Date: 6/7/76
Location:
Unit:
J
-------
VELOCITY TRAVERSE
Project:
Test Description: _
Date : 6 1 7 / 7 '£
location: ' I
Unit:
,-} ^, (i / Lj
Test: y- e " " '"
Personnel:
Fuel:
Stack Cross Section
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg) ;_
Pitot Tube Coefficient:
(Cp)
V = 85.48 Cp
1/2
Time
Traverse Point
Port Depth
-V
h5-
3
7
r,r
?./
Velocity
Head
(in. H^O)
*/7 ts & /g
.£>(. .Cf
.07 ,&i
• 17 ,10
,07 .#1
.0? JD
.or ,ei
Gas Tenrp.
(°F)
Gas Temp.
(°R)
TS
Molecular
Wt.
"s
Velocity
(ft/seel
VS
02
Cone.
(% Dry)
6002-13
382
-------
Project:
Date -•
Location:_
Unit:
Test:_
Fuel:
VELOCITY TRAVERSE
Test Description:
Stack Cross Section
j2gy~/5-
Personnel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg):
Pitot Tube Coefficient:
±
1
i
(
\
(
\
ffj n
^•..
i
$~
1
13
'7
2- '
2$
2-1
?l
, f
><5~
?-0
•7
f.f
1-1
Velocity
Head
(in. H20)
Q ** ©
.<"? .f2
.Ft .11
,fj •!{
.3? M
.22 . ?(
,W .31
.31 .!t
.13 • 11
,'/f ///
«7 #!g
,>1 .'1
.'(, ,n
.if .11
.// -n
.15 -It
II. ' ./'/
-f1^-
_£-/
1f
Jif
.;/
."•7
Gas Temp.
(°R)
Ts
Molecular
Wt.
MS
Velocity
(ft/sec-J
vs
02
Cone.
{% Dry)
6002-13
383
-------
Proj ect:
VELOCITY TRAVERSE
Test Description:_
Date: £/ 7/7£
Location: EtecX Cross Section
Unit:
Test: ^J- P ' ' ' t Personnel :
Fuel:
Absolute Static Press, in Stack (in. Hg): (PD) >
. , , _ _ si
. ,_ . _ ff . . . i— \
T AP J
P M
S S J
j
1
i
i i
i
1
1
1
| •
i i
I >
i
i
4-
i
j ; i '
1 1
1 ' 1
1
_i
_u
T
_u
1 1 1
( !
i i
,
i
1
1
1
I 1 ; • i : '
Time
Traverse Point
Port Depth
(
}
FP\
1
1
1
\
'^
(
\
-------
VELOCITY TRAVERSE
Project: Test Description-
Date: £ /.7//Y
Location: stack Cro.= SprMftn
Unit: |^I}I|
Test: 2oH-'7 Personnel:
Fuel: - -
Barometric Press, (in. Hg): " ~
Absolute Static Press, in Stack (in. Hg): (PB) T~-
Pitot Tube Coefficient: (r )
rT&>-|1/2
V - 85. 48 C M—
s <;
|_ s sj
lijlll l-t-
"-l-'-ft"
--Lf£4-
%T
-"[I-
j 1 i
4-
+
i
F
-"-
---±u~ ^r
•j-j-
--L-U ' 1 I j
| :.j-prj_n!_i4l
RJ44-I i ' ! ittl
1
-"I'M--
in — TT~; — i —
-f—f-fM+f
B^fit]
1 i '
i
iii!'
- : j ;
Time
Traverse Paint
Port Depth
(
\
)
FD<
f
\
(
\
J
}
I
(
^.
/
5"
1
13
17
21
zr
21
31
,*/
;.f
J.e
7
?s
I'l
Velocity
Head
(in. H00)
(J) AP @
.// .3?
.17 ,3e>
31 .27
Jo .26
,2>t .26
.26 Ji
.25- . 3}
,2-1 .2?
.23 .25
#17
,l?
.It
,'f
,/f
x/7
./}
Gas Tenp.
(T)
Gas Temp.
fR)
Ts
Molecular
Wt.
«S
Velocity
(ft/sec^
VS
02
Cone.
(% Dry)
6002-13
385
-------
»roject:_
Date:
VELOCITY TRAVERSE
Test Description:
location:
Unit:
Stack Cross Section
,2. i
•12-
,72
.pr
.ft
.
CF)
(°R)
TS
Molecular
Wt.
«S
Velocity
(ft/sec-)
vs
02
Cone.
(t Dry)
6002-13
386
-------
VELOCITY TRAVERSE
Project: Test Description:
Date : Cf 8 / 76^
Location: Stack Cross Section
Unit:
Test: 3-$ — i
S S \ 7
irt-
1---M-
H — -p ' —
- \
r-i4
\ > , ' i
— i— j--i J — 1 j J-
1
; i
-_LL_1 1
1 U
1
i * i i i
1 t i ! j
--(-M-
— 1 — >-
I i i
n~H~-
— i — r
i
1 ! i ' ill
Time
~
Traverse Point
Port Depth
/
7
5~
7
f
//
l*>
/5~
17
//
Velocity
Head
(in. H20)
AP
e?
o
o
o
<*{
,3
,7?
/,?
/ 7
/.g
Gas Tenjj.
(°F)
Gas Temp.
CR)
Tc
Molecular
Wt.
MS
Velocity
(ft/sec^
vs
°2
Cone.
{% Dry)
6002-13
387
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: £/ f / ~7 £
location:
Unit:
Test: J 0 5~ ' 1 ~ & Personnel:
Fuel:
Barometric Press, (in. Hg) :
Absolute Static Press, in Stack (in. Hg) : (?„)
Pitot Tube Coefficient: (Cp)
[T AP ~1 1/'2
s s 1
•^
Stack Cross Section
I
i
-
—
r^
1
i
I
1
--, — -
1
-HTT
— i < i -
*
i
I
— P.^ -
i i
i
,
i
1 1
1 1
III '
1 1
i * ' i
i
i
1
1 !
Time
Traverse Point
Port Depth
/
/
jT
7
f
//
/3
If
/7
//
Velocity
Head
(in. H20)
AP
0
o
G>
V
,rt
,2Z
,?}
*.1f
1-2-
). 3
Gas Temp.
rn
Gas Temp.
("R)
TS
Molecular
Wt.
MS
Velocity
(ft/sec^
VE
02
Cone.
(% Dry)
6002-13
388
-------
VELOCITY TRAVERSE
Project: Test Description,
Date: £/ f / 7f
location: stac). Cro_E Section
Unit: 1 JJ j
Test: 2CT/'.'-f Personnel:
Fuel:
.
. |
r- — 1/2
TT APT '
s p ps"s :::::
L s aj
rrn j~
-4-H--
ft-K-
S:+i
i '
-L _ .;.
1 1
1 ; i -
— X 1_
i
i
- . i
- - i
i ;
1 1
_i
-+-i-i-
•j-H^f-
-1-I-4-, :
J 1 ; : '
T~!
~-~^-
i .
1
1 i
-y-^J-i-l-r-l-i-
1
-I -I
1
1
i ; i
i i i : i i
i n
;
1 I
1 1
1 1
J-J-
i
i
i
i
1 ! !
1
l
-
1
i
i l
1
: l ;
Tine
Traverse Point
Port Depth
.i
i.r
j
7
f-r
^/
Velocity
Head
(in. H20)
#/?&#/$
.H ,//
,// .3t
,// .21
.// . It
,'? ,/f
Jl ,//
Gas Tenp.
(T)
Gas Temp.
(°R)
TS
Molecular
Wt.
"s
Velocity
(ft/secl
vs
02
Cone.
(\ Dry)
6002-13
389
-------
Project:
VELOCITY TRAVERSE
Test Description:_
Date:
e--<7- 7f
location:
Unit:
Test: J
10C& - t?~
Personnel:
Fuel:
Barometric
Press, (in. Hg):
Absolute Static Press, in Stack
Pitot Tube Coefficient:
tin. Hg):
Stack Cross Section
(V
•= 85.48
K]
Time
Traverse Point
Port Depth
/
?
3
13
17
21
ZJ-
2-1
5Z
Velocity
Head
(in. H.,0)
O&&
•*r .HI
.?# ,rt>
.v .if
,1? . ti
» .27
.51 .10
S3 ,Lt?
•K .5?
•77 , 70
Gas Teinp.
(°F)
Gas Temp.
(°R>
Ts
Molecular
Wt.
MS
Velocity
(ft/sec-)
vs
02
Cone.
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: 6//C/7*
Location:
Unit:
Test: 2.0.?
3,0
7.£>
$.?-
1.t
Velocity
Head
(in. H20)
^//AP *"/f
Vf .20
~22 .25
.3-3 .3?
.27 ,?1
.22 .22
.15" ,20
Gas Temp.
(°F)
Gas Temp.
(°R)
Ts
Molecular
Wt.
"s
Velocity
(ft/sec^
VS
°2
Cone.
(% Dry)
6002-13
39 1
-------
VELOCITY TRAVERSE
Project: Test Description:
Date: 6/'G/7t
location:
Unit:
Test: 2<3i/'2.2- Personnel:
Fuel:
Barometric Press, (in. Hg) :
Absolute Static Press, in Stack (in. Hg) : (Pp)
Pitot Tube Coefficient: (CV,)
[n An-lVZ
T APT
-
P M
S S J
Stack Cross Section
_P
4\
l
j
_L
1
i
I
i
~
"
\
+
i
i
+1
~i
!! 1 ' '
! i i ;
-T+^-TTT
~ 1— -] — >— r-1-
i .' !
t-"-H H--
i
1
i
l
— L ' ' ; ' ' : ' ] '
1 ' i
j
• 1 • !
' . 1 i
' ' ' i
i ' i i
i i 1 1
Time
Traverse Point
Port Depth
r
\
)
FP •<
V,
, i
).^
3,f
7.e
f.r
i.(
l"
r
1
13
l?
2-1
zr
2-1
33
Velocity
Head
(in. H00)
3TI7L& * /$
.If ,2 >
.21 .2H
.2? ,1(
.2* .25
.21 .Zi
.n .22
0 (5)
.(1 .«7
.12 ,U
J( .11
3} ,3o
22 .)2
27 ,1V
10 ,37
.S3. .21
.3} .53
Gas Temp.
(°F)
Gas Temp.
(*R)
TS
^
Molecular
Ht.
MS
Velocity
(ft/sec^
vs
02
Cone.
(% Dry)
6002-13
392
-------
Project:_
Date:
Location:
Unit:_
Test:
Fuel:
VELOCITY TRAVERSE
Test Description:
Personnel:
StacX Cross Section
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Kg):
Pitot Tube Coefficient:
(p.) -fH-H-H-i-
Vg = 85.48 Cp
Time
\
^
Traverse Point
Port Depth
/
(
, \
*(\
^M
V ')
/
/
.i
!.?
J.t
?,G
9.r
Lf
i "
3"
r
7
1
//
!}
/r
/?
Velocity
Head
(in. H,O)
ir/^AP ft > ,f~^
.& . ?~3-
,'ff .^7
• 71-/ .3?
,rr
,fi
.£3
.Ft
.47
.((
,rf
,*1
,70
Gas Tenp.
(«F)
Gas Temp.
f°R)
TS
Molecular
Wt.
«S
Velocity
(ft/sec}
VS
02
Cone,
(^ Dry)
,(7
6002-13
393
-------
Project:
VELOCITY TRAVERSE
Test Description:
Date: £/te/7f
Location: Etack Cross Section
Unit:
Test: 2&^ /5~~3f Personnel:
Fuel:
Barometric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg): •? • 1 (Pa) ~r
' ' ' ' " .
, ^^ i. /••«*••*• fr*\
[_.„-. 1/2
T AP
_£
P K
S S 1
T 1
^~q
4_
±
_. _.
1
i 1
i i •
i
i
I
^
I
i
III III
II ! :
N 1 1 1 1 1 1 ! i 1 N
1 I 1 1
1 I ] . .
'I ' 1
1
1 ;
i i i •
i . , • , ,
i . . i ;
III:
1 • 1
Time
(
Traverse Point
Port Depth
/"
,\
^}
^±J
^ ^ \
1
I
I
3
*r
7
3
//
//
IT
i 7
Velocity
Head
(in. H.,0)
Gas Temp.
(°R>
TS
Molecular
Wt.
«S
Velocity
(ft/sec-)
VS
02
Cone.
(% Dry)
'f .(7
6002-13
394
-------
STAGED COMBUSTION AIR FLOW DATA
KVB Test No--
Test No.
20 3-
Date
_Test Type
Boiler No.
Location No
. j &
Capacity
_103 Ib/hr Burner Type
Test Fuel No G>
Test Load
10 Ib/hr
21,720"
(g //, <
f/27
Test No.
Windbox °F/iwg
T1/P1
T2/P2
T3/P3
T4/P4
Furnace °F/iwg
SC Ports °F/iwg
T6/P6
T7/P7
VP8
VP9
Tio/pio
T11/P11
T12/P12
T13/P13
T /t ^\
14v 14y ' k*?
T15^1§)
T16/P16
T17/P17
T18/P18
T19/P19
T20/P20
201-2.
f/f
'1
M
IP2
£
AV?e.
msr
tvrc
.'/"
l.f
l.f
7. a
S.5
f , /
r£i7
it .if
.16 .17
1$ J$
.it J7
.!( .16
.13 .12
few'
J*c.
.Iff
.Iff
.Iff
,l£
.125
.!£
)
,/$ ,21
.11 .21
11 .3.1
2e .23
./I .23
.15 .17
rr
,21 .30
.2
-------
STAGED COMBUSTION AIR FLOW DATA
KVB
Test Type
Test No.
Test No. HO3'3-7 Date
Boiler No. Location No. Capacity 103 Ib/hr Burner Type_
Test Fuel
Test Load
10 Ib/hr
Test No.
Windbox °F/iwg ^
Vpi i.f
T2/P2 9
T3/P3 7
VP4 If
Furnace °F/iwg 7. /
A**.
SC Ports °F/iwg
VP6
T7/P7 & JUO"
T8/'P8 C
.11
•If
,/r
v^
./y
.««
ff 17
.t*-
.!(>
./£>
./f
.If
JO
,115
•Iff
./&r
.iff
,/V
."?
.f3T
# I
A/>
,lt>
,17
, '1
•>1
• >'/
.13
3
./S
.17
,/f
./#
M
.12
.155-
.17
./(
.It?
,/f
.11?
Jtl
4/76
60-32
396
-------
STAGED COMBUSTION AIR FLOW DATA
KVB
Test No.
Test No. J2 I
Boiler No.
Test Fuel Xy,
' V- 2- Date
Location No.
£ 4 5 Test
e/i/7(
Load
, "V
Capacity
? f ,^3
f ? 10
Test
vr
lb/hr
Type
103 lb/hr Burner Type f ' 'J (,
Test No.
Windbox °F/iwg
T1/P1
T2/P2
T3/P3
T4/P4
Furnace °F/iwg
SC Ports eF/iwg
T6/P6
T7/P?
VP8
T9/P9
Tio/pio
T11/P11
T12/P12
T13/P13
T14/P14
T15/P15
T16/P16
T17/P17
T18/P18
T19/P19
T20/P20
SoH-l
20^-3.
**/&
ir
«6/z<
201.3
/1 7
'Oi/,?-
"*>/2\
-2«v-y
/tf
'7*.*
/*<
aov-r
K.7
»• ,?
2
-------
STAGED COMBUSTION AIR FLOW DATA
KVB
£ /7 're
Test No.
Boiler No.
Test Fuel
Location No. / Z Capacity ^ *~'
/J , (? . Test Load 10 Ib/hr
103 Ib/hr Burner Type f I'JC
Test No.
Windbox °F/iwg
T1/P1
T2/P2
T /P
y 3
T./P.
4 4
Furnace °F/iwg
SC Ports °F/iwg
T6/P6
T7/P?
T8/P8
VP9
Tio/pio
T11/P11
T /P
12/rl2
T /P
^is^ia
T14/P14
T15/P15
T16/P16 'F /i~}
T17/P17
T18/P18
T19/P19
T20/P20
iOH-IO
/cr
A?.r
ic^i
~zi- /i
15.0
If.O
ie&
2*.?
201- .'Z
15.0
2CV-1}
1.0
T.I
lef
12.2.
ioi-'i
7.^
7, £>
1/0
I0.C
2W-/f
15.^
15.0
101
2e.f
-/(
IF*?
/f.o
to
-------
Test No.
2&1 ?- 2
STAGED COMBUSTION AIR FLOW DATA
KVB
pate { /f - (//&/?{
Test No.
Boiler No.
Test Fuel fa 1
Location No. J/7
r £<* f Test Load
Capacity 103 Ib/hr Burner Type f ' 'J £
•X VS 103 Ib/hr
Test No.
Windbox °F/iwg
T1/P1
T2/P2
T /P
i3/ 3
T./P.
4 4
Furnace °F/iwg
;
SC Ports °F/iwg
T6/P6
VP7
T8/P8
T9/P9
' Tio/pio
TI:L/PU-
T12/P12
T13/P13
T!4/P14
T15/P15
T16/P16
T17/P17
T18/P16
T19/P19
T20/P20
X
^.r
/V.^7
'"^.T
2 P.?
^
,0
K.2-
V.2-
,*/
/zo.f
X
/57T
/J.i
'"//
2o.*-l
,/
IS.1
H.2
>H/
zeM
^
e. /
^-/
IF.ff
12.?
i/e/
HJ
S
H.O
>H.O
1. t
n.g
j
.^
o
-at
)5.0
13,0
in
2£>
.»«•
i.r
i.<~
?t.e
'2. 3
!if
>4
f
11.0
If. 0
>2.e>
->t,0
li f
H
4/76
60-32
399
-------
STAGED COMBUSTION AIR FLOW DATA
KVB
•6/7S
Test No.
Boiler No.
Test Fuel ^f'
Location No. x 0 Capacity
r- 6>A £ Test Load ^ V& 103 Ib/hr
103 Lb/hr Burner Type %!#£
Test No.
Windbox ° F/iwg
VP1
T2/P2
T3/P3
VP4
Furnace ° F/iwg
SC Ports "F/iwg
VP6 ^/v/
T7/P?
T8/P8
T9/P9
Tio/pio
T11/P11
T12/P12 >/i
T13/P13 '60W*
T14/P14 ^^'
T15'P15 /^/ t?f/j
T16/P16
T17/P17
T18/P18
T19/P19
T20/P20
ifi/r
-27
$ 1
i *
f
3
12.
ie>
»r
2e1/f
-2t
12.5
to.?
ill
/(,0
-23
It.?
IC.t
ti.r
w
in
if.0
~}C
•&-
-}/
!?
12-
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
REPORT N07.
PA-600/7-78-099b
2.
|3. RECIPIENT'S ACCESSION NO.
TITLE ANDSUBTITLE
mission Reduction on Two Industrial Boilers with
Major Combustion Modifications (Data Supplement)
|5. REPORT DATE
December 1978
6. PERFORMING ORGANIZATION CODE
AUTHOR(S)
S.T. Fisher, J.J.Buening, W. A. Carter, and
S.C. Hunter
8. PERFORMING ORGANIZATION REPORT NO.
KVB 6004-734a
PERFORMING ORGANIZATION NAME AND ADDRESS
KVB, Inc.
7332 Irvine Boulevard
Tustin, California 92680
10. PROGRAM ELEMENT NO.
EHE624A
11. CONTRACT/GRANT NO.
68-02-2144
2. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Supplement; 1/76 - 1/78
14. SPONSORING AGENCY CODE
EPA/600/13
5.SUPPLEMENTARY NOTESrERL-RTP project officer is Robert E. Hall, Mail Drop 65, 919/
541-2477. The supplement documents detailed test data reported in the final report,
"!PA-600/7-78-099a.
6-ABSTRACTThe report provides raw data from a study of the effects on air pollutant
emissions of extensive combustion modifications on two industrial boilers. The sup-
plement is intended for researchers who wish to perform their own detailed calcula-
tions.
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lDENTIFIERS/OPEN ENDED TERMS
COSATI Field/Group
Air Pollution
Combustion
Boilers
Burners
Nitrogen Oxides
Smoke
Fossil Fuels
Particle Size
Flue Gases
Circulation
Fuel Oil
Natural Gas
Trace Elements
Organic Compounds
Air Pollution Control
Stationary Sources
Combustion Modification
Industrial Boilers
Particulate; Excess Air
Staged Combustion
Trace Species
13 B
21B
13A
07B
21D
14B
06A
07C
18. DISTRIBUTION STATEMENT
Unlimited
19. SECURITY CLASS (ThisReport)
Unclassified
21. NO. OF PAGES
411
20. SECURITY CLASS (Thispage)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
401
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