ABMA
DoE
EPA
American
Boiler Manufacturers
Association
1 500 Wilson Boulevard
Arlington VA 22209
United States
Department
of Energy
Division of Power Systems
Energy Technology Branch
Washington DC 20545
US Environmental Protection Agency
Office of Research and Development
Industrial Environmental Research EPA-600/7-79-1 30b
Laboratory July 1979
Research Triangle Park NC 27711
Field Tests of Industrial
Stoker Coal-fired Boilers
for Emissions Control
and Efficiency
Improvement - Site C
(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-600/7-79-130b
July 1979
Field Tests of Industrial Stoker
Coal-fired Bolters for Emissions
Control and Efficiency Improvement
Site C (Data Supplement)
by
J. 0. Burlingame, R. A. Parker, J. Cook,
W. M. Jackson, and J. D. Demont
KVB, Inc.
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
lAG/Contract Nos. IAG-D7-E681 (EPA), EF-77-C-01-2609 (DoE)
Program Element No. EHE624
Project Officers: Robert E. Hall (EPA) and William T. Harvey, Jr. (DoE)
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
U.S. DEPARTMENT OF ENERGY
Division of Power Systems/Energy Technology Branch
Washington, DC 20545
and
AMERICAN BOILER MANUFACTURERS ASSOCIATION
1500 Wilson Boulevard
Arlington, VA 22209
-------
ABSTRACT
The Data Supplement is a compilation of test data presented in greater
detail than was practical in the Final Technical Report. 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, description of facility
tested and coals fired, test equipment and procedures, interpretations
and conclusions. The Final Technical Report also contains data summaries
not found in this volume. The Supplement contains panel board data for
each test, detailed particulate, 02, CC>2, NO, SO2 and 803 data, overfire
air velocity traverse data, flyash reinjection mass flow rate data,
particle size distribution data, modified smoke spot data, chemical analysis
of the coal and coal size consistency data.
11
-------
TABLE OF CONTENTS
Section Page
FOREWORD iv
CCiWERSION FACTORS V
1.0 P/-"
-------
FOREWORD
The purpose of this Data Supplement Volume is to document
data in greater detail than was practical in the Final Technical Report.
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, description
of facility tested and coals fired, test equipment and procedures, inter-
pretations and conclusions. The Final Technical Report also contains data
summaries not found in this volume.
The data in this volume are arranged by type (i.e., Panel Board
Data, Particulate Data, etc.) and within each type by test number. Data
summaries where they exist are at the front of each section. The boiler
tested is referred to as Boiler C; as it is the third boiler tested under
the program entitled, "A Testing Program to Update Equipment Specifications
and Design Criteria for Stoker Fired Boilers."
Gabrielson, J. E., et al., "Field Tests of Industrial Stoker
Coal-Fired Boilers for Emissions Control and Efficiency Improvement - Site C",
EPA-600/7-79-130a, May 1979.
IV
-------
CONVERSION FACTORS
ENGLISH AND METRIC UNITS TO SI UNITS
To Convert From
in
in
ft
ft
Ib
Ib/hr
lb/106BTU
9/Mcal
BTU
BTU/lb
BTU/hr
J/sec
J/hr
BTU/ftAr
BTU/ft/hr
BTU/ft2/hr
BTU/ft2/hr
BTU/ft3/hr
BTU/ft3/hr
To
cm
cm2
m
m^
m3
Kg
Mg/s
ng/J
ng/J
J
JAg
W
W
W
W/m
J/hr/m
W/m2
J/hr/m2
W/m3
J/hr/m3
Multiply By
2.540
6.452
0.3048
0.09290
0.02832
0.4536
0.1260
430
239
1054
0.002324
0.2929
1.000
3600
0.9609
3459
3.152
11349
10.34
37234
psia
"H20
Rankine
Fahrenheit
Celsius
Rankine
COAL FUEL ONLY
ppm @ 3% O2 (S02)
ppm @ 3% 02 (303)
(NO)
(NO2)
ppm @ 3% O2
ppm @ 3%
ppm @ 3% O2 (CO)
ppm @ 3% 02 (CH4)
Pa
Pa
Celsius
Celsius
Kelvin
Kelvin
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
6895
249.1
C
C
K
K
5/9R-273
5/9(F-32)
C+273
5/9R
0.851
1.063
0.399
0.611
0.372
0.213
-------
CONVERSION FACTORS
SI UNITS TO ENGLISH AND METRIC UNITS
To Convert From
cm
cm2
m
Kg
Mg/s
ng/J
ng/J
JAg
J/hr/m
J/hr/m2
J/hr/m3
W
W
W/ra
W/m2
Pa
Pa
Kelvin
Celsius
Fahrenheit
Kelvin
COAL FUEL ONLY
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
To
in
in2
ft
ft2
ft3
Ib
Ib/hr
lb/106BTU
g/Mcal
BTU
BTU/lb
BTU/ft/hr
BTU/ft2/hr
BTU/ft3/hr
BTU/hr
J/hr
BTU/ft/hr
BTU/ft2/hr
BTU/ft3/hr
psia
"H20
Fahrenheit
Fahrenheit
Rankine
Rankine
Multiply By
0.3937
0.1550
3.281
10.764
35.315
2.205
7.937
0.00233
0.00418
0.000948
4.303
0.000289
O.0000881
0.0000269
3.414
0.000278
1.041
0.317
0.0967
0.000145
0.004014
F = 1.8K-460
F = 1.8C+32
R = F+460
R = 1.8K
ppm (
ppm (
ppm ^
ppm 3% 02 (CH4)
1.18
0.941
2.51
1.64
2.69
4.69
-------
SI PREFIXES
Multiplication
Factor Prefix SI Symbol
1012 tera T
109 giga G
10^ mega M
103 kilo k
102 hecto* h
101 deka* da
10~1 deci* d
10~2 centi* c
10~3 milli m
10~6 micro V1
10"^ nano n
10~12 pico P
10~15 femto f
1CT18 atto a
*Not recommended but occasionally used
vii
-------
EMISSION UNITS CONVERSION FACTORS
FOR TYPICAL COAL FUEL (HV = 13,320 BTU/LB)
Multiply
To "~\^ By
Obtain
% Weight in Fuel
S N
lbs/106Btu
SO2 NO2
grams/106Cal
SO2 NO2
PPM
(Dry @ 3% O2)
SOx NOx
Grains/SCF.
(Dry @12% CO2)
SO? NO?
% Weight
In Fuel
0.666
N
0.370
0.405
13.2xlO~4
0.225
1.48
5.76xlO~4
.903
lbs/106Btu
SO-
1.50
(.556)
19.8x10
-4
(2.23)
2.47
(.556)
14. 2x10
,-4
(2.23)
SO-
2.70
H-
H-
H-
grams/106Cal
(1.8)
f j
NO-
4.44
35.6x10
,-4
(4.01)
(1.8)
25.6x10"
(4.01)
SOx
PPM
(Dry @ 3% O2)
NOx
758
505
281
1736
704
1127
391
1566
SO,
.676
Grains/SCF
(Dry @ 12% C02)
(.448)
(.249)
8.87x10
,-4
NO-
1.11
(.448)
(.249)
6.39x10"
NOTE: 1. Values in parenthesis can be used for all flue gas constituents such as oxides of carbon,
oxides of nitrogen, oxides of sulfur, hydrocarbons, particulates, etc.
2. Standard reference temperature of 530°R was used.
-------
SECTION 1.0
PANEL BOARD DATA
PAGE
1,1 CONTROL ROOM DATA 2
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
_,< Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "J^O
Boiler Out. Pressure, "f^O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "^O
1 Fan Out Pressure, "I^O
Precip Out. Pressure, "H20
Overfire Air Press, "l^O
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-------
Sheet 2 of 4
KVB
| TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2 -Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9 -Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Ceil Air Heater In, °F
13-Air Heater Air Out, °F
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-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Danger
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H20
Front Lower OFA Press "H2O
Rear Upper OFA Press "H20
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. P.ress "H20
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers '
OFA Fan Static Pressure "H2O
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-------
Sheet 4 of 1_
KVB
I
• TEST NO:
NOTES
- P**
TEST NO:
TEST NO:
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ub/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
..rf Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H20
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
"» Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2o
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
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TEMP RECORDER ^ ^
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2-Grate Thermocouple, °F °
3-Grate Thermocouple, °F ^ |,
4 -Grate Thermocouple, °F 0|f
5-Grate Thermocouple, °F HMf
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
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KVB
TEST NO.
CONTROLS
Plant Master
fv«~-T
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
Crfr
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
LtL
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H20
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H20
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H20
8
-------
Sheet 4 of 4
KVB
NOTES
I TEST NOs/ /S'ap.fl. HtfLil fa** "fit f*.
TEST NO; 5 /r ^ F.A"
r"t ^o\U ^- i -
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TEST NO:
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
/ 7/
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
rW Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O .
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "^O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
'D Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F Cred)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F '
13-Air Heater Air Out, °F
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-------
Sheet
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KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front tapper OFA Press "H20
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "^O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers '
OFA Fan Static Pressure "H2O
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-------
Sheet 4 of 4
KVB
NOTES
TEST NO: y t?r *" p
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TEST
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Lb/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
**? Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red).
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
lie
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-------
Sheet
of 4
KVB
TEST NO.
CONTROLS
Plant Master
V*
Feedwater
Attemper ator
1*
SF/AF Ratio
FD Damper
ID Damper
SL
Overfire Air
1*
1°
FD Set Point
a
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "l^O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H^O
Blr Hopper Reinj. yes/no
^
Mech Hopper Reinj. Prass "H2O
Mech Hopper Reinj, yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
r
Clinkers
OFA Fan Static Pressure "H2O
1.6
-------
Sheet 4 of 4
KVB
TEST NO:
NOTES
h
TEST NO:
TEST NO:
TEST NO:
TEST NO:
•
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: j_2,
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
. rf Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H20
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
> Fan Out Pressure, "H20
Precip Out. Pressure, "^O
Overfire Air Press, "H2O
3
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure , psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F '
13-Air Heater Air Out, °F
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-------
Sheet
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H20
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H20
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea:
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
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-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: 17pi
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
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-------
Sheet
of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, IbAr * 1000 (red)
Air Plow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
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-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
It
Feedwater
Attemperator
SF/AF Ratio
f/
FD Damper
ID Damper
1
Overfire Air
60
(oO
FD Set Point
AMPS
FD Fan Amps
III
ID Fan Amps
OFA Fan Amps
"
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
1",
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
r
3"
Clinkers
?-?•'
r*-*
OFA Fan Static Pressure "H2O
14.
It
2*1,0
0
-------
Sheet l_of JL
KVB
TEST NO; a #5* F"
NOTES
TEST NO:
TEST NO:
TEST NO:
TEST NO:
*"•
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
i-rf Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H^O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "l^O
Air Heater Out Pressure, "H2O
) Fan Out Pressure , "I^O
Precip Out. Pressure, "H2O
Overfire Air Pi-ess, "H2°
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stin Flow, lb/hr x 1000 (red)
Air Flow, % Cblue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig tredl
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, 8F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
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11
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-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overf ire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/**'"'-)
Front Upper OFA Press "H2O
Front Lower OFA Press "H20
Rear Upper OFA Press "^O
Rear Lower OFA Press "H2O
•* Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj, yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers i
OFA Fan Static Pressure "H2O
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-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr: jj Fan Out Pressure, "H2O
Precip Out. Pressure, "H20
Overfire Air Press, "H2o
II
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, ppig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
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-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Araps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H20
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
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-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
-0%
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
.W Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "^0
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "^O
Economizer Out Pressure, "f^O
Air Heater Out Pressure, "H20
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 {.red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig Uedl
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
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-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
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-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, lb/hr:
Stm Flow, lb/hr:
FW Flow, lb/hr:
% Design Capacity:
fe~5<-/-
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
*ri Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H20
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H20
D Fan Out Pressure , "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
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-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, ?sig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % Cblue)
FW Flow, IbAr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig Cred)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
fo
m
<\ot>
rt^
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btf
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fit
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7(»
(^l^
(,iy
IA[
Ll»
W
K
/•'
V
/ot
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H20
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
?!
$"»
n
f"
it
5«
4
f)
111
ff
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-------
Sheet 4 of 4
KVB
NOTES
TEST NO: fa, £ - 7^ ~ ?3
TEST NO:
TEST NO:
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: / 7
Stm Flow, Ib/hr: /
/J: v&
?7/ ?
3- ^
/•tr
l.tT
/.o
-• c,
-2 o
--*.;
-'/•£
K /
O
22 .r
/^ > r
f7/^i S
?
^/jrsy ^
^7/^j'Vo^
?^?^j.
/?,
/^^. ^y^
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F Cred)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, "F
5-Grate Thermocouple, "F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F-
12-Stm Coil Air Heater In, CF '
13-Air Heater Air Out, °F
<77^
£<£>
*7eo
/£<>'
/3>o
/(o
/y
$7^
?^
/^s^
^X
y^
^Jo
7/A
^5"^
/Jo
7*6
7^o
7/7
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^^r
/.?d?
^
/^r ?
^
/^j>
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f/
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T-^O
g-4/.?
^A
^??
*1t
^z
^^
/^?
/.^^
//^
/.?j? ?
^
/*r
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
i
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "I^O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H20
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers '
OFA Fan Static Pressure "H2O
31
5&
<76
ST°
9o
JT*.*
'•%,'
*'•%*.*
c"/t.o
»*A*.*
TVs
(
5.6/
/t'f.
2"^ ±'
Ok
?*,r
3 /
5^
£%
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//^
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/s-.(*
3"-S<
ok
40
-------
Sheet 4 of 4
KVB
TEST NO:
NOTES
TEST NO:
TEST NO:
TEST NO:
TEST NO:
"A*
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: /7, ^' (,
Stm Flow, Ib/hr: /^
^ rifA
/^•^
?7^7J
fl/J/J
^231 <-/&
fffl/
7-^ 7o
-O.i -o.j.
2.1 /•*
/.±~ AJ
/•tr /• 3
/d? -?0
-&.(, - f>.$-
-l-L -1-8
-V,°-*^
-^>> -yy
g.o W
o 0
/7 « / ?, o
./O-v
A>:z?
9?70?
9 S3 y j
(7^.3?y?
yyjo^
'7^7
-O.^L
/•?
/-J
/^
, »o
— o- 1
-x?.0
-J7
'/i'
g,J
0
/?.J'
/'>¥
9-??? > '
?JJ^J
^y^?p
VJ-75-7
7^
.^ . 1
•
___
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
••
STRIP CHARTS
Stm Flow, lb/hr x 1000 (.red)
Air Plow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,cF
12-Stm Coil Air Heater In, °F '
13-Air Heater Air Out, °F
'//iT
ff?r
%±
/(I
£1
/9e
&3-5~
7/6
Ko
77*
77*
Cxf
7?r>
77-5
6\f
/3i"
//?
/&
/S>0
/&&
V*
$70 %
/3r
//^"
?i
/*
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers '
OFA Fan Static Pressure "H2O
3;
56
&
Jrs
9$
<:/
?°
*7
/V?
2r
//*
^/^
'*-*/,**
s.*s
f±i 0
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9e ?
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'
t 8.&/
/ /8-0
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f«i
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3*~S"
ok-
—
44
-------
Sheet.4 of 4
KVB
NOTES
TEST NO: /&- ^ / ?; oo ^ ^ c fi^, „-/- ^ ^7
/ !••»< f (. ~T~&r- <*
d- /7cr> kll>< A
TEST NO:
^ L- d^ £ /
A
TEST NO:
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, lb/hr: /7
Stm Flow, lb/hr:
FW Flow, lb/hr: / cy /
% Design Capacity : (j y
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
Fw Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H20
FD Fan Outlet Press, "H20
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H20
Air Heater Out Pressure, "H20
Fan Out Pressure, "H2O
Precip Out. Pressure, "HjO
Overfire Air Press, "H20
/£•
f-H-lf
£. vV,-H £
??,«.< ^
/?:**
??/??
9SPnr>
?3*/A//
S~(,e*-l
- . c
- 7.0
-a.s>
- V-r
f.3
t>
n
o JA
4sy¥J
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure . psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (.red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple , °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F '
13-Air Heater Air Out, °F
Ito
«ijr
;xo
£?-s
7o~?
&ST>
7 2r->
f
7zo
6'l'o
700
6fs-
6>(°
/.!>
//<<
/3~r
for
/of
7/o
S?o
^^5'
/?0
s-^
/9o
Z2S-
7o")
$SO
{£*
6?
7 oo
2/J~
«^<3^
7jo
7-2o
?i?c>
72»
toS-
/3S-
/J-"
/S-sf
/f/
/*r
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
"
OFA Fan Static Pressure "H2O
3/
SU
/1- ^
&*/ ^
""S/iK-
c-
/o?
'*''% :*
^'%-0
/ S'lO
*-f/s.0
'^7,7 <-
/«
^i
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*'
c-k
2 fc? r
.J/
&
9?
^/
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//<
J2,c-
/&*
/S:%'0
//S'.o
S~. <^> y/
/ £. O
J J/j'.o
/;
-------
She.et4 of 4
KVB
TEST NO:
NOTES
x_ *V f i C* ""\-i_- / '' ) r*
c?
TEST NO:
-- -70*
TEST NO:
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: /'/,
Stm Flow, Ib/hr: yj/;
FW Flow, Ib/hr: /S2 ,
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
i .1 Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H20
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2o
/?
5~- 12 - ? y
f-Al-i-'r*
/y, **>,
//«* <.
fc:o 7
-+c
2.2.
0
2<*>£
/<=• <~, /-- <->j
/
/,. l/*~r
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t
6* 2.**
7.7 t.V
/^
IC>M_
o^
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s-o
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/JT
/•/
/J
.(,
*-.r
-/-/
-3.0
- 7./
^'C.
C1 f6tss^>
/^.^
j> /7
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (.red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple , °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, "F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
-o
loo
&r&
&ST?
4
5'2c?
/•>«*
4?
^
^/
•93
i
•/o 3*.
: -kfrf-^)
7&o
&*>
frVo
Mo
I/O
/•s-sr
<$*&&
£/&
%z^
e^r
S9o
?*r
X
/J-°
9?
^r
?^
rr
51
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
''/
s&
K<-
/.
to
i7
Si
(.*
//f
!
**-*
M-°/,
' />& • o
i^
**Y*<.
3"
olc
27.o
1*
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76
2&
7°
s*
5-7
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X*
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(,.y/
/&.0
"/{.r
*•'/«,
£ .&/
/£o
ny
/ 2-0,0
y«
**•/*.
-i«*
js:c/
/s.<*
**'
ok
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: /
Stm Flow, Ib/hr: Jti$ toe
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
FW Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "f^O
FD Fan Outlet Press, "H20
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "I^O
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "I^O
Air Heater Out Pressure, "I^O
Fan Out Pressure, "I^O
Precip Out. Pressure, "I^O
Overfire Air Press, "H2O
ff
C-t2'7Z
&*£&>->-
OkC, £5**>-^
1^
*K<»t
ei^ctiX
^ffo-T^
^45*0
1*
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ts
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-*i
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n
17
^•^•
&• */(.*
*tf>3?&
If /f8f
lyj fsT6
6*7 7to
7/
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple , °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
4*
3&>
6\is
itf
<<
i*<
^
fr
fa
•&*
v*
to*
tf,
H*
^
^
hf
tf
4<
/
DRY
FLASK
•
67
3~v./£oJ
$v./6°3
S&- /6°3
— •
3-0. Jbo?-
FILTER
NO.
3*
.t>-737
. ^737
,6738
.^>73-7
BLANK
NO.
\
\
\
\
A
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
_3_
4
A
7\
AVG.
\
A WT.
\
-2-1 t>O
b vie =
t^ DgV =
£^ Mn
ml
mgro
LOAD_
°2_
REMARKS:
klbAr
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Ii>let-f Outlet)
Box No.
LOCATION
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
H20 RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
\
39
\
z
DATE WT.
I
TARE WT.
7
\SL
5
\
X
s
AVG.
69.
.67*8
POST TEST WTS.
\
¥
. -2-811
/i.
\
\
2
\
AVG.
\
. 74S-7
A WT.
\
0.
0.
A Vic
A DgV
A Mn
. 3
ml
mc[in
LOAD_
02
REMARKS:
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
(Inlaf, Outlet)
Box No.
Test Description
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ 1
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
-Tf
.
t?. 5*4(>
6. 43^
4». 4332-
61. 7^?
0. /4S&
ml
ft3
mgm
*-&> &£.
J9 • 3/&2»
S3. z
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Illlef, OuLlH.)
Box No.
LOG ATI ON
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Fi na1
Initial
Impinger Water Vol (ml)
A DgV_
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
X
BEAKER NO.
I
\
DATE WT.
i
TARE WT.
N»Z
5
X
\
£
. 3*77
\
S
AVG.
3° ~78
X
POST TEST WTS.
5
A
te.
AVG.
A WT.
A Vic
A DgV
A Mn
X
\
.***1
0. "2418
0.
X
ml
mgm
LOAD_
°2_
REMARKS:
klb/hr
230
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Iftlef, Outlet)
Box No.
Test Description^
LOG ATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
v
A
/ \
/ V,
/ \
ACETONE
RINSE
.
77
•77.034°
17, 032.7
17 &3>?4
17> oZ2°
DRY
FLASK
-
•7*
— —
o j . *^«^5 C? *f
£*^7 tfP^?^?2?
^7. &3?3
67. ffSfZ.
FILTER
NO.
4?~
^7J5V
. 675-2.
.675-2.
— —
,*7S-2
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
AVG.
A
f 7
3S~*/7
.0/33'
4/35-
A WT.
//,
A Vic
A DgV
A Mn
ml
LOAD
mgm
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet-', Outlet)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fi nal_
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
BEAKER NO.
s
Go
DATE WT.
\
TARE WT.
V
^z:
A
X
s
S
AVG.
/02 .
POST TEST WTS.
\
\
*
.3ffVS~5*
. -S3Z1
\
\
AVG.
\
\.
A WT.
\
0, 034?-
N
A Vic
A DgV
A Mn
ml
LOAD
°2_
REMARKS:
klb/hr
8830-5
rev.
-------
PARTICULATE LAB WORKSHEET
^/./Pw^r
TEST NO. 42, CbfrSLef, Outlet)
Date Box No.
Test Desert
LOCATION jSr'Je C
Eng.
iption ,_
Dry Gas Meter Vol ,ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
AVG.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ \i
/ \
1
2
3
4
A WT.
\ /
\ /
\/
A
/ \
/ \
-
Impinger Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
#/
<95~. yess
<^^^"~" ^&^2^^1D
^^?J ~/ v^*O
f55T W/7
fglfJSV
A Vic
3 Total
DRY
FLASK
. .
•77
•
f~) * &^) &*J
^^^~ /£^~^/
/^? » r^^--^
•
9S: L&.3
FILTER
NO.
•
44
•
, £?/£
, 67/7
* ^ f f f
w9 **7 f^J '
BLANK
NO.
\
\
\
\
/
/
/
|/
/
/
/
/
\
\
\
\
POST TEST WTS.
^» 2S7/
l6.-z&>1
jb. 24- 2,t£l
/2-1. 0333
/^?, ^^"55
/^^ 5iT^
—
/2f ^^SS"
^.2^/2-
s-Jptef-
- .
-------
PARTICUIATE LAB WORKSHEET
TEST NO. 4/2- (Inlefc-, Outlet)
Date Box No.
Test Descr
LOCATION ,5/^T C
Eng.
iption
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
Y
A
/ \
/ V
f \
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
\ /
\ /
v
A
/ \
/ \
Impinoer Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
k
g*J
. .
64, *W?
£*J* 0t4o
&*[• 06 fa
£<{. 064s
A Vic
3 Total
DRY
FLASK
-78
"
^>. 3Z.13
S9. 3294
^9.3ZfS
,5». 3213
POST TEST WTS.
//. 32/1
64. 3z/3
64. 3z&
64. 32/5
^. 25"7«>
SJ< 2£fJ
St. 2*S*
s/.tts*}
— -
sf.afst
*.f£~l3
FILTER
NO.
*J6*
•
,^7f^
./7^5*
, /7^T"
•
• 67?£~
-. fjff
< 9153
•
•
* U&&
&< 3/£°8
BLANK
NO.
\
\
\
\
/
/
/
/
\
\
\
/
/
/
- ml LOAD klVhr
^ ft Oo ^
* J^**m ^ i , „ DPMUPVC •
J4^ ^r ^Wm t InCJUi x\Etnn*\r^& •
/
/
/
/
\
\
\
\
s
/
/
\
X-
X,
8830-5
rev.
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
(Inl-ef, Outlet)
Box No.
Test Description_
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
85-
•
7 643^
—
41. 6433
FILTER
NO.
4*>
'
.U17
.Ul*
,&(>?€
- — '
,U
ml
mgm
LOAD
klb/hr
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 4*3 <
&.*
Date Box No.
LOCATION ^fsJt C
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
-
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
$£>
.
£ /. && c/ 2-
6J.00&/
67. fft>7£~
6J. -77
A Vic
DRY
FLASK
03
&>.3o9l
S&. 3*05-
St>-3o?3
. —
sv. 3083
FILTER
NO.
^7
— -
, 6>&zg~
. 6Cz(>
. 6&-2J
f&t-zl?
BLANK
NO.
\
\
\
\
/
/
/
/
7
_^/_
—7—
\
\ _
X
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
Y
A
/ \
/ \
W.Z344
&1- 234 <
£*. 6/41
JV, 6/tfz
S#- &/.2^»*~
\
\
\
/
/
A Vic = " ml LOAD klb/hr
A DgV = ft3 O2 %
y
A Mn 7v2.& mgm REMARKS:
s
/
<
\
\
\
8830-5 rev
-------
SECTION 3,0
GASEOUS DATA
PAGE
3,1 GASEOUS EMISSION SUMMARY 238
3.2 GASEOUS EMISSIONS DATA 243
3,3 SOx DATA SUMMARY 288
3,4 SOx DATA SHEET 289
-------
Location:_
Fuel:
TEST
NO.
DATE
LOAD
GASEOUS EMISSION SUMMARY
CONDITIONS
02
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
ppm
Wet
HC
ppm
Wet
02
%
Dry
CO 2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
SO3
ppm
Dry
NOTES
4,0.
7-3
f-5
f-7
7-2.
//.*
337
//f
-20-7 a
/e.2,
303
8,2.
1.1
373
00
7"
7A
1.1
/*.!
5-7
3/6
32$
1.2,
X',2.
/0.1
322-
57
&9T
e
V-.2T-7I?
42.0
fe>.2.
$.8
253
10
/*.!
n
1.1
/0.0
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
CO
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry
NOTES
2.73
9.1
/o. e
13
~- 4 -7*
91
231
/V
/a. o
3*3
~-/*- 79
S>'4£>
S3
6.7
337
is; as f=hm-f- e^A
37
3o
17 A
- 7*
37
ZffT,
ne
f.V
ow
I/.*
Z/
//-V
25"
32
233
2/Z
//f
£--12. -7$
*J?ea.*
/*.£
33.6
8.1
33/
9.L
333
-/b- 7*
44.7
1.*
26°
319
*$«.&«**£.
/lied. OT
p.o
/te
•2,1
47*
NOTE: All parts per million (ppm) figures are corrected to a 3% O2 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:_
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
Dry
co2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
C02
%
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry
NOTES
$.9
ff.V
//.v
5"32^
72
12.
//v
•2ZC
361
377
23
/'.I
3/1
3*7
/A/
2&S 383
2V
S-7
43V
372.
2£T
- 7*
/73
/33
33
-------
Location:_
Fuel:
(.32.-
TEST
NO.
DATE
LOAD
GASEOUS EMISSION SUMMARY
CONDITIONS
02
%
Dry
co2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
N02
ppm
Wet
HC
ppm
Wet
02
%
Dry
C02
%
Dry
CO
ppm
Dry
NO
ppm
Dry
so2
ppm
Dry
S03
ppm
Dry
NOTES
32,
7.2
3*1
7.
ff.3
241
341
//.*
02,
33
£--30-76
ff.l
/o.l,
322
v.v
3*7
1.*
/o.o
43.1
393
364
0a-
4-il
££
471
34
e.l,
32-7
357
/1. 2.
3&£ 3**
fl.o
all
ad.
25*
*.
(>-/- 78
3S-7
ff.*
//.£-
6-7-70
It. 3,
9*
/I. -3
6.3
£"7
.3*5-
1.4
z&l
Tfy-+B/r+DC.
L-/3-76
I*
374
40
NOTE: All parts per million (ppm) figxires are corrected to a 3% O2 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
so2
ppm
Dry
so3
ppm
Dry
NOTES
-/5-- 78
243
4t
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
c.
1
4-/3-7*
FUEL £A£,r£f,c>.
f&S, 0-2.
DATA TAKEN BY "PLL
Probe
Posi tion
Time
\
(dry)
(dry)
CO •
ppm(dry)
NO
ppm ( dry )
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
fi.o
346
f.ZS
0.2.
31
/. 3
70
2JSI
1.1
/OS
7.3
281
e -7
Z&T 32.1
/e
23
235-30Z.
•7.3
25-
3.=?
275-
=?».<
AVERAGES
12
2*3
NOTE:
Parts per million (ppm) figures are corrected to 3%
•"> '•• • •?
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
0-2_
Probe
Position
/-£
7
/-£
7
l-L
•7
Time
*V2.<
/»;¥»
//:z°
#38
/z:z*
iz:.z
02
t
(dry)
?.3
*f
ff.l
e.f
7.Z-
L.1
C02
\
(dry)
y.7
/tf.2.
//.*
/•P.?
//»
//•f
CO •
ppm(dry)
unc
4o
3S-
35"
3o
3S~
4$-
cor
62.
5~2
v#
V2.
V5-
5-7
NO
ppjn ( drv )
unc
24^5"
z.*l
Ike
.ZSf
ZS-8
Z4°
cor
57»
431
3^o
36 2.
3J7
«Je6
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO -3
unc
cor
HC
unc
cor
REMARKS
r**Sf*
t>77. "
s&?» "
S-f?T "
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
4-20-78
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
/-*
7
/-£
7
;-£,
7
Time
/y;v*
/s:*t>
/5-/2/
/s-,y?
/l;a$
#>:&
02
%
(dry)^
8.8
9.2-
/o.l
1.J
//.$"
/^.«
C02
t
(dry)
/O.2.
/*.<}
1.1
?.*
7.*
1.0
CO •
ppm(dry)
unc
33
4*
go
4s-
f"
4*
cor
4s
*r&
/3-2.
-?*>
>-7i
7o
NO
ppm(dry)
unc
2*5-
24t>
Z^
23*
ZZe>
Z.Zt>
cor
3<>3
3
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
£ei*s
LOAD_
CONDITIONS_
DATA TAKEN BY
/fl>
Probe
Position
Time
02
t
(dry
C02
t
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
REMARKS
27.5
3-7
ofA
1.2-
32.
1-2-
Z/o
1.3-
/p. a
3-2.
23"
JSV
•or, i
53T
7 B4#
&fA
35-
2*7
of*
37.S
Zot*r
**?A
/-*
f.er
7"
Z&
AVERAGES
NOTE: Parts per million (ppm) f jures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C
TEST NO
DATE
&
FUEL eA*r*<* ±*~ M*»
LOAD /2 5" /(sn..
V~25"-7* CONDITIONS /V+tfMs&t 07
DATA TAKEN BY O~» 13
Probe
Position
/-£>
/— 5~
/ — 5"
/-3~
/H£c*l
/-5~
/— 5*"
Time
,*r>c
/5"/i.
/^;^
/*/^i
/7/^
/5T;?0
/7-'5S
02
(dry)
/*».3
/*-3
/».*>
/"-3
/0.3
/a-3
/*.c>
C02
t
(dry
e-7
ff.t>
f-l
8. 7
?.£>
9.5
f-»
CO •
ppm(dry)
33-
3«
55
5^"
35"
55"
3S~
^•7
^4^
7419
57
3*5
5~?
^7
NO
ppra ( drv )
/J'o
/?s-
2/o
2»S"
2/0
22$-
zy»
•
cor
:?z/
32^
3^5-
3^
3S2f
5^'
s^y
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
HC
REMARKS
•V&trf&UArG
•&L*,*>
f.e
tt.t>
^^
^%%
;^^
%M
fi>
£*?
%%%>.
v//y/s;
w/wfy
W/6
5S3
^SS
WM
'MM,
W///>
WM
v%%
WM
W%
'W//,.
Wflfr
WM.
m?/,
WM
Wffifr
w/%fr
V///S&
%//////
?»*?,>
NOTE: Parts per million (ppm) figures are corrected to 3%
02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
02
*
(dry)
C02
%
(dry)
CO •
ppra(dry)
NO
ppm ( dry )
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NOo
unc cor
unc cor
REMARKS
2-*
rs:/*
37
SB
37
2-
37
/
2e-&
AVERAGES
2#9
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
coNDiTior:s_
DATA TAKEN BY
Probe
Position
.2-^
2-£
2,-t
2--6
2.-1?
Time
?;
/»,~n
fc:3S
V',/2.
n.tB
°2
%
(dry)
*.9
1.*
4.1
i..
CO -
ppm(dry)
unc
*e>
sr
26
3f
44
cor
*r
s-3
31
^
*>i
NO
ppm(dry)
unc
2S»
?7°
ZS*
&>s-
2*T>
cor
37»
tfot*
372
«?/f
J/y
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
AVERAGES
T2^~ S/
NOTE: Parts per million (ppra) figures are corrected to 3% o?
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
2-6
2-k
z-£
2-6
2-4
Tine
A'.-A
#:s*
/z>
n:*s
/fizz
02
%
(dry
0.f
ff.fS
Vr
**
C02
1
(dry
/*.2.
/»,»
t.e
<*•*
/*,»
CO •
ppm(dry)
unc
3S~
37
3f
as
32-
cor
5~2.
S-S-
^S
^f
49
NO
ppm(dry)
unc
23f
238
27,«T
&n>
Z'J
cor
33*
^tr6
jar*
^/3
^62
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
.
AVERAGES
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
il'l
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
*
s-
4
3
2.
/
Time
13:39
t3:<&
'3'.41
wsj
tyff*
'4*7
02
\
(dry)
.6>
7,°*
S-SS
f.z
1*t
C02
\
(dry)
1.1
/Z.o
//Si
/*./
t.8
1.*
CO •
jgpin(cJry)
unc
32.
B2.
(1
32-
3?
W
cor
5-2.
^
2^~
^
5^
^f
NO
ppm(dry)
unc
/fV
264
25"
2Z&
225
2*>t>
cor
3/3
3S<=>
323
S*>
^V
S2S-
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO 7
unc
cor
HC
unc
cor
REMARKS
AVERAGES
/o.
3*
NOTE :
Parts per million (ppm) figures are corrected to 3% O2
15900
-------
TEST SITE £
TEST NO /2.
DATE S~-tJ-
.2-6 - ~BLf
Probe
Position
Time
02
*
C02
co -
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
unc cor
unc cor
REMARKS
32
'7?
37
/I'.&r
f-/*
%
27
272
7
8.36
33
/*•
274
7
12:4
35
,84
//* ~Ju£>t '-O
a;**
e.g
37
53-
2/V
$.1
35"
AVERAGES
ff'1
NOTE: Parts per million (ppm) figvires are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
OF*
Probe
Position
2-*
2-£
2-t>
z-(>
7 _
2-t>
7
Time
OJ'«>
/JT/r
/7/5S
^•27
«,y»
f*/53
/f»»
02
%
(dry)
^3
tf'.i'
tf./
^/^
^*
f.^.
7.7
C02
%
(dry)
f.ff
/*.*
//.«
/»./
//s
/p.»^
//v
CO •
ppmtdry)
unc
49
48
/z*
&0
isr
^r
^5"
cor
7V
£7
/*7
/^2
fff
*4
08
NO
ppm(dry)
unc
/52T
XT3
/^V
/5V
/:*•
/5»
/7<
'
cor
^?8
2Z«
229
23V
23f
22?
2.37
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO-j
unc
cor
HC
unc
cor
REMARKS
AVERAGES
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE_
TEST NO
DATE
£--
3
7
Z-t>
Z-6
•7
Time
H.'ev
'4/08
<4:'-2.
A/IZZ
^.'32
rt;4
—
&:*7
/£•:/»
/f.X.
#'./o
/t'.Zf
02
%
(dry
?.*
9-1
8.6
7.&
/*.
.
/o.2
/».y
//2
1.°
/e.i
/»,0
i.e
/o.e)
1-*
/O.2.
/o.
*
VV
NO
ppm(dry)
unc
/?*
Z3°
ZZf
22T
/ffo
2*Jo
S*r*
22°
22.0
2ft>
2Zo
Z3S
cor
Z9t>
3
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
%
(dry)
C02
\
(dry)
CO •
ppm(dry)
unc cor
NO
ppm(dry)
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO-)
unc cor
HC
unc cor
REMARKS
>,
3/y
4^/*.2
4*
3417
30
f.7
4°
•2/0
3"
44
3*
23*
332
V*
/f.o
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332
tf.o
22*
3*
2,-b
if.-}
40
322
2-
22f>
A/7
36 /
7.7 //-V 3o
AVERAGES
1.1
wm
63
328
w///,
NOTE: Parts per million (ppm) figures are corrected to 3% Oo
-
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C
TEST NO /£
DATE £~—
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
X=fctg ?crA/
Probe
Position
Tim
02
\
(dry
C0
(dry
CO •
ppm(dry)
unc cor
NO
pptn(drv)
unc cor
HOT LINE SAMPLES, PPM (WET)
NO
NO-j
HC
REMARKS
7.V
#5
/'.*
er/o
Zo
25
7.5
2LS
/o.
25
3°
+*
48
AVERAGES
'.7
NOTE: Parts per million (ppm) figures are^corrected to 3% 02
* . t'\
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
/7
LOAD
fur
CONDITIONS —_
DATA TAKEN BY
-7 —
Probe
Position
Time
02
(dry
C02
\
(dry
CO •
ppm(dry)
NO
ppm(dry)
HOT LINE SAMPLES. PPM (WET)
NOx
NO
NO?
REMARKS
2-
32.
2*2.
8.
35
/«.*>
ft*
3V
2/3
/&•!
?.*
/*
/-?*
-2*
•298
286
/t
ss-
2.S
2-1
22.7
7
2V/
AVERAGES
2*2,
w///,.
ma
W//6
w///,
W///,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
Position
2-t.
7
Z--£
7
2-£
r
Time
/2',n
fZ.I
tXZ
f2.'.£
'2.4
fZ.Sl
02
%
(dry
7.
ff.4
1.x>
?.s
C02
%
(dry
/?.<*
'(•1
//.*
///
/O.O
/e.a
CO •
ppm(dry)
unc
2o
B7
47
NO
ppm(dry)
unc
/**>
/7*
/t*
'7o
/t°
/•7S
cor
Z/2.
2/7
233
2*3
^*z>
275
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO 7
unc
cor
HC
unc
cor
-
REMARKS
^
AVERAGES
NOTE: Parts per million (ppm) figxires are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
— 7
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
firn.nO
Probe
Position
Time
°2
i
(dry
C02
t
_(dry)
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (MET)
unc cor
NO?
unc cor
HC
REMARKS
7
41
336
V/s
2*
A.
22°
V//
AVERAGES
VV
NOTE: Parts per million (ppm) figures are corrected to 3%
o,
2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
£.
2-0
<~-/3--?8
FUEL &*ton L*, ***><«
LOAD /*& ^^/JV).
" /
CONDITIONS //,&*?» ^2. — Aft>4Sls&£.
DATA TAKEN BY J~Q
Probe
Position
2-£
2
3
4
f
6
7
2-(e
2.
— »
3
Time
?;/2
r^
?/y*
7/35
'»;//
'»;ja
/*••<*•
///o*
//,/<•
///3«>
02
«
(dry
/*,7
//"
/*.'/
/».7
/».?
It-9
A*7
//.»
/?.•
//.7
C02
«
(dry
tf.S
y.y
*.z
«r.2
tf-2.
^'^
£>.<
8.4
7.y
7>
c
ppm
unc
^«
3S~
^>
Z<»
3*
4°
4*
3°
ts-
ST>
o •
(dry)
cor
5-3
63
SB
33
f3
72
70
JV
/3I
17
N
ppm
unc
/7T
/#5~
/y*
^"4T
2/tf
2n>
H»
{to
/&>
/7°
0
dry)
cor
3o7
334
333
31°
sts
&l
333
as
IO
cor
NC
unc
>•>
t
C
REMARKS
^V= vy«.
AVE RAGES
/f.ff
9.1
33L
NOTE
: Parts per million (ppm) figures are corrected to 3% 02
'
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
•Bi.% OUT - 2-4 -Pt
/tfM./^ic/one-*•?- f^t>e£
LOAD /4°
CONDITIONS
DATA TAKElM BY
Probe
Position
;?-£
7
2-6
7
2-6
7
Time
/A32
//irz
/^.'J"
/2,'5l
/3:/V
^;./
02
%
(dry)
/*•?
f.^
f-2
?•*
9.1
*>./
C02
%
(dry)
7.2
y.*
/».»
/•/.«»
//.&
/0. 6
c
ppra_
une
1-75
S±°
//»
/^z
//«
?2
3 •
dry)
cor
2??*
ii*"
/^*
/*V
/3-V
#3
N
ppm
unc
2/o
245-
Z3°
Z6>o
2S*>
26?
D
dry)
cor
$?s
371
352
3T/
^Sz>
V^
•
HOT LINE SAMPLES, PPM (WET)
N
unc
3x
cor
^
O
NO
•)
h
C
REMARKS
AVERAGES
W///A
w////,
wm
w///,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
2-2-
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
Position
2-6
-
7
2-6
•7
2-6
7
Time
*;»
/5T*
/5-/5S
/£,*
fat
*;sr
02
«
(dry
r.e
*<1
7.1
f.4
/O.o
V*
CO?
«
(dry
//*
//v
/2.«
/AV
^
/p. i
-
CO •
ppm(dry)
unc
/^r
/5*
//*
/£*
ZZ*
rt°
cor
«7
^/i'
/W
2/5
S6/
2^«
NO
ppm(dry)
unc
2/o
2So
•Zle
ZZo
ZZ°
2^0
'
cor
3/1
3Z1
2&a
3/f
3tl
377
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO-)
unc
cor
HC
unc
-
cor
REMARKS
AVERAGES
NOTE- Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C.
TEST NO
DATE
•BL*
/*)HI
Probe
Position
..
7
•z
3
4
5"
6
7
2.-t>
•&-tf*r
Time
~#3
f& ,2
XOV3*
fo.s*t
x/; /V
'2,'c6
/2-/6
—
23
V--/7--7S
rt
3«06&
\r£_ .
C02
%
(dry)
"^2
XX. 2
/*•. 2
y.v
/6».W
//'^
/ii.ti
/A*
//-£
••
/*-f
5 2-^
7
c
ppm
"XT?
/f<7
2tf*
35>
22tf>
/22.
/S*
2e^"
/6*>
^^
^^
2M2
o -
(dry)
25"?
^72
4^ZS
67*
3^5'
/^5
^•9
2-f*
2Xfe
JX/
FUEL (>ir£sr&{/v
LOAD /*t<4/(
CONDITIONS /^/4l4 <>xi'* — f.S~7»-O-2_
DATA TAKEN BY ^«
K
ppm
unc
^
^tfo
^Oo
^toe7
26*0
i»o
27"
25^
2//o
*
^^
mtm,
fff/f*/f
^^
o
(dry)
cor
£fOt
^Jy jg
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
(dry
C02
I
(dry
ppm(dry)
unc cor
NO
ppjn(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
/#:*»
330
-71
9-
//•*
433
1.*
22*
35*
23"
*•!>
31*
//,*
7.1
1.9
$3
23°
24°
377
AVERAGES
•Btftur
468
377-
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
1
Probe
Position
Z-£
6
f
4 \
3
2.
7
*-*
-
Time
/o;s*
ll'.fo
11'^
it:y£\
fZ,&
I2,&
1
•
ppm(dry)
unc
/2.Z-
n-
t$-
12.
/to
t?f
iv-
Ht>
cor
/ff
-------
KVB
GASEOUS EMISSIONS DATA
TEST SI'
TEST NO
DATE
TSJ-4 fM*
/Uu/t)clt
Probe
2-*
2-£
7
2.~t>
7
2
3
*f
5-
6
sofrttr
nu»ta*#6
tif'fft
/yv'
^vn*
*-.V»
>r«
/^y^
*.*»
^•v*
/P « 25
/4 *VC
_—
re C,
5--2S-7*
" ^/fotfes - 2-6
>*£ TK»&£. — 7
02
f. /
r<
f./'
f'f
*F £
*> f>
/fl-K
f.6
f' 1
1-1
+ 4
f f
C02
fo.*
/»•!
/e ,o
fO.o
/o.o
1'2-
4 ?
77
^.7
1.7
--
1 *
fr> o
CO -
ppm(dry)
2-fo
27°
/1o
2.7*
227
^S»
ggo
/TST
220
24$
W%%
^^
^y
Vz-T
ff2.tJ-
3»/
34&
3St
4^V
^V
2-T?
3t£
3K
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
NO
jppm(dry)
2J£~
27"
2-*»
2S*
zs»
25»
^SS"
•24°
7ZS
23°
•
5"2^
V^
W^
.?^2
J72
4/?V
/a^ff
^m&
373
^7V
•
^^r^f/u ^x«L
x^/ - 7* ^fCtfSSfi^
ff/^6 4/xv'ff^ <5^v4.
x*;j-
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
AVERAGES
5*^
3«t
Wtfr
w%%
wm
.^I'v
^/^
'4%%%
%jjjj%
Vssssss
*SS/Ssss
#?%;xx$
^^
gg^JS;
^J
cor
NO->
unc
plil
^^
^^^
^^^
cor
HC
unc
Wflk
Mtfjb
\&MA
cor
REMARKS
^Jftfar-estr
"^•^ = 7
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
-2V- 78
LOAD_
CONDITIONS_
DATA TAKEN BY
/?? J"
Probe
Position
Time
02
t
C02
%
(dry
co
ppm(dry)
unc cor
ppm(dry)
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
un c cor
HC
unc cor
REMARKS
» 57"
2.70
V/7
7-3
il.t,
/SO
•2.96
9.1
2^4
/O.I.
22T
1-
•27°
443
v//
'1$ /•>!
1,*
ff.e
2J6-)
25Z>
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ff.3
24°
fo.b
12.1.
f.2.
/o.e
11°
/SIS-
ZSS 3Sl
AVERAGES
e.es
38-?
NOTE: Parts per million (ppm) figures are corrected to 3%
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
f-2S~-
LOAD__ /a
CONDITIONS
DATA TAKEN BY
Probe
Time
02
%
(dry
C02
«
(dry
CO •
ppmtdry)
unc cor
NO
ppmtdry)
HOT LINE SAMPLES^ PPM (WET)
NOX
NO
NO?
HC
REMARXS
//a
= 93
* -71
6-
3/S
itrt- =
//•V
*f*t
3
/O.I
72?
II.2S
Vf*
27*
f.
AVERAGES
'tern
W///S.
W//4
NOTE
- Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
TEST SITE_
TEST NO
DATE
2,1
~-2(,- 7&
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
2-£
•7
6
5~
4
3
2.
4
7 _
S~
6
7
l-*>
Time
#*»
7/2$
##
1:$$
/•:K>
't>:z$
ft>;&
*:<&
tl.-*»
2,7*
i'.Zf
±
*•'!
14
4.}
7.3
^•7
7-7
$.6
&.7
ff.7
CO2
t
(dry
^*.y
ll.o
(6.k
/M
/o.$
/e.o
fO.O
(l.t>
/9.B
rl.*>
7/2,
/A*
II,"
CO •
ppm(dry)
unc
2/o
2Z»
2
/SS"
ff*
/s*
280
/»fo
•2S*>
/v*
38"
Z»o
24*
cor
3 06
2/3
42g
203
2.71
241
43-2.
;e4
3*7
25*
sis-s
/
V2S
5^2
V//
4&>
44*
4*1
437
393
4*7
4
-------
TEST SITE
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
3o
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Z-b
7
2-6
t~(f
~j
Time
///«
//:¥
f2.'
f2',3l
02
(dry
fl.5
//•7
f/,0
/e.»
/o.o
C02
(dry
9.7
7.9
e.t>
y,6
1.6
-
CO-
ppn(dry)
unc
m-
/<(»
fto
fZ
*?2
cor
^?z
272-
/•?«
/5~/
/5~/
NO
ppm(dry)
unc
2y»
2Je>
ZJ°
ZZ°
Z3*
cor
£f(Tt>
4/6^
37J
3LI
377
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
,
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
AVERAGES
NOTE
: Parts per million (PPm) figures are ^corrected to 3% O2
15' JO
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE LI-
TEST NO 3 /
DATE
FUEL /5V^5r^/f/l/
LOAD /
/Z2.
?2-
//°
f/°
/4°
0 •
(dry)
f7
/2/
/fz
/5V
/^y
/ff
253
N
ppm
/»^
//*>
/
K
REMARKS
AVERAGES
WM
Wtfc
'»
W/A
^^
^
«%%
g^^
«
^
^%%
W^
w%
m%
mzt
mz
%m.
mz
mat
sy/ss/Y
WM
W///,
ss/y///
'?/////'
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE
TEST NO
DATE
32-
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
%
(dry
C02
t
(dry)
CO
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOX
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
2-t
//.£.
/?*r
34
3S-/
/*.?
230
//. 6
1-1
/#. <•
2Z*
22*
MffP
22<=
AVERAGES
NOTE- Parts per million (ppm) figures are corrected to 3% 02
-
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
33
LOAD
-3°- 79
CONDITION5 /Hir>
DATA TAKEN BY
Probe
Position
"?
2--*
7
2. -6
7
Tine
//;/7
tr-&
H.S»
rz:/S
ft:&
02
%
(dry
it. A
9-1
7'5-
/*-?
1-s-
C02
\
(dry
/*-4
f*.t>
//y
e.t>
1.2.
-
CO-
ppn(dry)
unc
270
/?*
/*'
4rt>
3»S
cor
3V3
ZU
-2S*/
•7*1
V77
I
NO
ppn(dry)
unc
*£&B
22-
23"
24-
27'
• •
cor
36
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE t—
TEST NO -3-4
DATE $~-3*
FUEL
LOAD
CONDITIONS_
DATA TAKEN BY
Probe
(dry
C02
%
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPUX, PPM (WET)
NOX
unc cor
NO
unc cor
NO 9
unc cor
HC
unc cor
REMARKS
fl.*
32S
Stff
e.s
S7S
&:?.
an?
2-*
2*f
23S-337
9.*
f.f
Z.9I
f.8
//z
/if
2**
S64S
AVERAGES
WM
W#m
W%&
•'//////>
w%
mm
W%k
v/////,
WM
^P
Wfm
\mta
^^
Vwmi
vzzA
ma
W%
\z&A
NOTE- Parts per million (ppm) figures are corrected to 3% O2
274
159; >•
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
. -/£>.
_ 3 14
Probe
Position
Tim
02
(dry
C02
t
(dry
CO •
ppm(dry)
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
XT*
Z13
7
//;/.*
•2JTV
s/t
//*
/••
/t>0
iz-.sl
+
A 7
/to
/e.ti
ff.e
cl
0.
AVERAGES
1.*
vim
w%
tte.$2m,-22Z.s
m//,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
~ •
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
(dry
C02
\
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
f.
32/7
61
7.3
255
- 43 V
/&>
.2*5
3
-52SS
38
•2-
e.i
Aisr
ZJS
-7
MS
7
ZSS-3&
AVERAGES
8.06
mat.
2V7
NOTE: Parts per million (ppm) figiores axe corrected to 3% 02
4 . VN
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE__ £•
TEST NO
DATE
FUEL_
LOAD
6-2-1*
CONDITIONS ۥ 3
DATA TAKEN BY
„-.. /^^g>f
fiiettjeeJf^
-------
KVB
GASEOUS EMISSIONS DATA
TEST SI1
TEST NO
DATE
Probe
2-&
2.
3
4
g-
6
7
2-6
•2.
3
4
/*•#
/0:4a
(9.S&
ff./3
M'.3o
//•5?
f2',3l
/2'.53
t3'*\
13'. 2'
DE C-
6-7-70
02
/y.z
//7
//^
/o.-?
/o.7S
//•V
/2.o
://,*
7/2<
// *
C02
1
(dry)
*-2
^^
^."
9.6
4-4
e.9
9.&
7.*
* & A
8.3
CO •
ppm(dry)
unc
3S"
t£
4*
3o
3>*
40
4*
3f
3£
3o
f7-4*"
cor
t*J
/33
78
5f
5T2
To.S
"75:4
7°
t(>
sit
4
2Z°
22.o
&SV
/IT
/jo
/?*
Jfs
2jo
cor
4/0*
4zl
s»*
4°$
39^
3fB
3f^
38 'z
3S*Z
3^1
36*
/44"9^ f-Us/tO)
/f& Jf jJoJ jts) •
Afyd 0&4. — ^SfccSS Oy //• 2,
C7-^>^
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
AVERAGES
1LKW
SfefrffM
—
— -
//3
^V
g.Zb
(f.<
w%%.
'///////,
'///////,
vvm
in
75
W%P>>383
wmn
w%?//
mm
£>$
yftvfc
'W%.
$Mt
'mA
%%%/.
HH
^^
\%&A
%%$%.
'jfttffr,
^HH
\&&A
mwfc
^^
W%k
\6ZOA
cor
REMARKS
NOTE
- Parts per million (ppm) figures are corrected to 3% 02
1590C
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
J~. 7~.
Probe
Position
2-1,
7
2.-6
7
•z--t>
7
Time
/
W,2£
M43
02
%
(dry
1,»
1-7
1-5
t.3
1*
T4
CO2
\
(dry
/". ^
1.*
/'•/
/0.3
/*.6
//.o
CO •
ppm(dry)
unc
*£
t/o
/f&
/fft>
/ft>
-/3
X57
/5V
*7
'4
NO
ppm(drv)
/v*
'16
/*»
/go
/*s~
/1*
cor
zs
3J2-
283
2.76
2?*
2?*>
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
NO-j
HC
REMARKS
AVERAGES
/Si
/*>.*.
/s-e
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SX1
TEST NO
DATE
Probe
•> — -^
•7
2-t>
2
3
4
g-
£
7
2—6
*>••*(•
fr-tt
if**
H'.l*
/f',
(t;
/e,1
CO •
ppm (dry)
^,<
^<
p-r
3f
3-
2°
^5 O
_^?^
^S"
25"
A//
ijp
41 1
£g~
•f*/
s$-
42-
4°
*{r>
38
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
NO
ppm ( dry )
unc
-?**>
225"
2.2$
22*>
2Z£
Z2S
26o
2&0
^^^O
^^JQ
•
cor
7-70
3!S*
«*?
4/09
4*7
3f7
.5^^
34/7
PI-7/
32/
•
£K*J.*.£.
sWJ
HOT LINE SAMPLES, PPM (WET)
NOX
unc
cor
NO
unc
cor
NO?
unc
AVERAGES
fi£/p$$>>$$
W/A
'5
NOTE:
Parts per million (ppm) figures are corrected to 1\ O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD
CONDITIONS
*,.— fr*?- ~
DATA TAKEN BY _ ^
Probe
Position
Time
02
I
(dry
COj
(dry
ppm(dry)
NO
ppm(dry)
NOx
HOT LINE SAMPLES,_ PPM (WET!
NO
NO?
HC
REMARKS
Z-3V
#,1
73
Z-K 3ti
//-Z
237
280
V/V
+5
/SS
242
22g 3S3T
AVERAGES
16.
w////,
W///,,
w///,
WM
m?/,
v/v
w////.
w///,
W////,
NOTE: Parts per million (ppm) figures are corrected to 3%
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SIT
TEST NO
DATE
Probe
2*J~b
-7
tj
z.
g-
£
2 *J-£>
7
2 V-4
/f/5j
•&>'&
Z».'3£
y)-,lo
z/:4c
22;*
ZZ'.(7
Z£:n
23'.9
CE ^
^ j^j •y ^y
C^ f f ^ g ^
02
^.2.
^0 <9^
?/*~
zt°
3*f,
N(
ppm(
^
Z65
273
23s'
^&£0
?SX
T^^^^
^7T
7>Mo
2Lo
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
)
dry)
v-/
374
3Z*}
36 /
423
^43
*<&
37"
4/1
Tff
•
ȣ*&** &>+<-
/0o f^/M •
ff.S^o &K3SS&&
ij-Jl ~ *
2. K/XfA. Of,&*
^r»e>
HOT LINE SAMPliS. PPM (WET)
NC
2/0
)x.
223
N
2/7
AVERAGES
'BLKtw*
Mcc.4-
-,
f 3
if, 4
^./
// ^
vffifw
YS/fflSfr
-------
TEST SITE_
TEST NO
DATE
6-2.0-78
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
£*<£&>
£>. ^
Probe
Position
Time
02
\
(dry
C02
\
(dry
CO •
ppm(dry)
NO
ppm ( dry )
NOx
HOT LINE SAMPLES, PPM (WET)
NO
REMARKS
1.2
3°
~7
1.1
/o.
277
f-/
70
Z8S-
A 2
42-
^-.-25
4*
&**>
-7
AVERAGES
/tf. 2
W///,
1-1
/e./
w///,
w////,
W////,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
TEST SITE
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL f.
- 21 ~ -78
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
2.-t>
6
sr
4
3
2
a-4
#:&>
*&
02
%
(dry)
?.?
9.6
.•$
//.»
/*.$
1.&
C02
\
(dry)
1>L
/e.&>
/e.2.
3f
27
3"
cor
V?
3t>
33
3V
^
V^
V^
NO
ppw(dry)
unc
2.4°
*7sr
ztf
z*&-
23S
2S5
?41
cor
3^/
^<«>
3
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE 48 C
TEST NO
DATE
4*
FUEL £"&£•&')') £ot*s fltS'**!
LOAD f?0 tfft&/fr).
f-Z-J-je CONDITIONS t/*2y O.f? A
I/
DATA TAKEN BY SIT.
Probe
Position
2-^
2-6
2-t
2.-C,
2.-1*
•2.-L
2-£
z-t
z-f>
Time
/y;*»
/V/3C
#•4*
/y:*
/S'2*
&4S
• —
—
02
t
(dry
-
1.3
'/:3
1.3S
'*•
A3
#•3
f.s
fyts
C02
(dry
f.f
/tf.
/ff.f
/O.I
1.4
/*>.e
2&>
2&
•2tS~
cor
ijtfb
^Oi
3*/
3«a<-
^575
syi>
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO?
unc
cor
HC
unc
cor
REMARKS
Zf"e>fz#.
/£" &=&
^T** ^^C* >*-
«-* %9r^^^
/S"* «4
^^•"o^A-
f"o^A-
AVERAGES
^^
»
W/6
*w<
B79
317
39*
'wffm
'jtftffi
W///S.
W///,
I^P
^^
^^
#%^
x!v5>5^
YSSSsft
w//,.
w///,
^^
^^J
^^
^%^
s- " *&
XS-" o/tr^.
2^-/' o^^
NOTE: Parts per million (ppm) figures are corrected to 3%
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
f^ttSfffT)
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
2-4
7
•Z-L
2-t>
7
Z-t>
•7
Time
//*>
//:*£
//:<&
//:*&
I-Z'.Z
as*.
te',s>
02
\
(dry)
fZ.f
t/.-»
'/).*
/o.<,
/o.6
-9-*
<*.*
CO2
\
(dry)
7*
7.3
7-V
s.t.
e.t>
1.*
1-9
CO •
ppm(dry)
unc
^5-
5&
S»
3*
2£~
•z*
/9
cor
/3«7
1*
74
S-2.
4Z
3^
27
NO
ppm(di-y)
unc
1-7*
/I*
/<*>
J<&
2*T
2?£
2/"
cor
373
372
3*2
33t>
3S3
3°8
3/6
•
HOT LINE SAMPIJES, PPM (WET)
NOX
unc
cor
NO
unc
cor
NOT
unc
cor
HC
unc
cor
REMARKS
AVERAGES
mm
vm.
NOTE
- Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
•z-l>
-7
2-4
1
7,-L
7
Time
/V:i«
W3S
it:s&
/t:t°
><+:&
/y.'a
02
«
(dry)
•/».?
/f>.S
*A
*.»
1.2.
-7,1
C02
%
(dry)
ff.9
0.8
/*3
/».v
r/.6>
il,1
CO •
ppm(dry)
unc
4*
cor
72
4* 7/~\
4*
^t>
42
?2
4-7
74
tz*
111
NO
ppm ( dry )
unc
2^rr
•2/0
W
??£
/*>
-------
SOx DATA SUMMARY
Test
No.
Load
02
S02
(unc ppm)
SOl
(unc ppm)
SOx
(unc ppm)
S02
(corr ppm)
SO 3
(corr ppm)
SOx
(corr ppm)
Test Description
9.
6-73 .
674.S
. o
7,6
-7.3
USA
1.3
3.0
0f3
781
-712.°
V5-C
4-70
. -2.
/go. 7
ri
1.
• y
/e/z.
. f
/f/7.3
G.-2-
/•Z
/06Z.6
7.s
r
-------
Local
Date
Unit #
-S;Je C.
SOx DATA SHEET
Probe Location & Probe Length
Fuel
Load /*>
Test Description;
Test
No.
44*
44&
44 c-
Box
No.
/
3
Z
Sample
Time
23: lo
:z3 : 22.
- —
23 :s»
— '
Meter
Temp .(f)
//5~
//5-
/2-<>
/Z*
/£*-
/2-2-
Meter
^)press.
— ^> -^
{-
Meter
Reading
tf>. tfTrjp
/»^y?>
^» ^yp
/. <»?r2>
^#. tf>P
/,*&>
(p^'Baro.
Press.
^^3^
/
I
Port
|
'
Purge
Time
^*
«S»
&>
1
02
SI
x
CO
Q
U
Test #
Test # */*/&
Test #
Normality N
Dilution
Factor F
5pife
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + P
A - B
SO2
,/e>7
2
^•5?
^.7
SO 3
— '
/
2. 2.
^. /
2. •
?-/
3.2.
• —
__
3. 2-
/, / .
SOx
S02
2»
6.9
6.-?
&.
*r.<*
1T.1
^•l
£.°
£-«*-
6.°
SO3 ,
/
3.1
-
f.o
SOx
*7~
>!
SO2
SO2
(A-B)(N)(F)(460+T)(24)
V(P+p)
(/
SOS =
SO3 =
)24
SO2 @ 3% 02 =_
SO3 @ 3% 02 =
SOX @ 3% 02 =
>-7
)( )24
SO2
SO3 =
SO2 @ 3% 02 =
SO3 @ 3% 02 =
SOx @ 3% 02 =
/9IZ.O
t'1
,•'1
)24
SO2 =
SO3
803 =
SO2 @ 3% 02 =
S03 @ 3% 02 =
SOx @ 3% 02 =
-------
Local
SOx DATA SHEET
jf- '
Date 6- /7- "7& Probe Location & Probe Length "T2*-/- 2 • 2' •*"
unit f 6 -$;kc Fuel we&fan £*&J
Load /*° *lts*/hr.
Test Description:
Test
No.
?
*£
Box
No.
'
3
Z
Sample
Time
7.'2«r
714*
e:*g
ff'./f
013*
ff'.fS'
Meter
Temp.(T)
X2^
___
/2£
/^^
Meter
(f)press.
-0-
)
\
r
Meter
Reading
o.sr*
/.sr*
+.
/.**»
ff.*V»
7,evt>
Press.
C .
,1
1
Port
*
/
*^
Purge
Time •
e:e*
S!3o
ff f ,3^^
^y * £"£
£?* ' &fr
7:30
\
02
&.3
\
<
/
Test # Test # Test #
«
Q
W
Normality N
Dilution
Factor F
&i*C
Blank B
Averages
Ml. of
Titrant A
Averages
'SO + T
ample
Jol. V
+ P
A - B
SO2
,0/07
2"
2.2.
^-2-
•Z.2.
f.6
s:t
^' 7
f.t>3
S-7&
/.**»*
21.38
$*.(.3
SO3
• •
/
2.*
. —
—
2.*
.*
SOx
~
S02
—
2.e>
^7-T
f. f
S~.£~
Jif
S~?<>
£-.5-
SO3
/
2-f
z.f
.7
SOx
S02
•££>
&•?
-57^
^ 7
^^
jr.^
S03 ..
/
2.*
— ™'-
^. *
.^
SOx
^
»•
^
SO2 =
(A-B)(N)(F)(460+T)(24)
S02 =
S03 =
@ 3% 02
@ 3% 02
(3 3% 02
SO2 =
SO2 =
SO3 =-
SO3 =
S02 @ 3% 02 =
SO3 @ 3% 02 =
SOx @ 3% 02 =
•7^1
.o
(•fe)(" ) (' )(5)24
SO3 =
SO3
SO2 @ 3% 02 =
S03 @ 3% 02 =
SOx @ 3% 02 =
-------
Local
Date
Unit #
& - St
SOx DATA SHEET
Probe Location & Probe Length
Fuel <£0u>
Load
Test Description^
41*
Sample
Time
Meter
Meter
Meter
Reading
Press.
Port
Purge
Time
02
. /
V.1
Q
W
. a~pt>
4:2*5"
46 c
Test #
Test # "B
Test #
•
Normality N
Dilution
Factor F
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
+ P
A - B
S02
. ^>/0 7
2«
_ _
1
/
//. 3~
//. 7
//, 5T
//. ^
A /It*"
7- 7-v6
//.*
SO 3
/
/. *
—
—
/.*
/. «
SOx
S02
25-
f-7
/£>. *
f. f
f.jr<
^r^^
SO3
/
. *
—
. ^
. #
SOx
'
SO2
25-
?.*
4.6
4.L
f.6£
f.U
S03 .
/
/. /
• —
—
A/
„.- —
/. /
SOx
^
• ?"
^,
— "^
ffi
Q
E-
l-l
EH
SO2 =
S02 -
(A-B)(N)(F)(460+T)(24)
V(P+p)
•''
<**
5
503
)24
S02 @ 3% 02 =_
SO3 @ 3% 02 =
SOx @ 3% 02 =
7,
r
-------
BLANK PAGE
232
-------
SECTION 4,0
SPECIAL TEST DATA
PAGE
4,1 OVERFIRE AIR DUCT DIMENSIONS & SAMPLE
GEOMETRY 294
4,2 OVERFIRE AIR DUCT VELOCITY TRAVERSES 296
4,3 FLYASH RE INJECTION MASS FLOW RATES 333
4,4 MODIFIED SMOKE SPOT DATA SHEET 335
4,5 PARTICLE SIZE DISTRIBUTION - BRINK 337
- SASS 343
- BAHCO 344
-------
FRONT OVERFIRE AIR
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
FRONT OVERFIRE AIR
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
BACK OVERFIRE AIR -
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
- MAIN PIPE
INCHES
.250
.795
1.40
2.10
2.96
4.21
7.65
8.90
9.77
10.47
11.07
11.62
- TOP - ID PORT
INCHES
.120
.380
.678
1.01
1.43
2.04
3.70
4.31
4.73
5.07
5.36
5.62
MAIN PIPE ID
INCHES
.200
.653
1.15
1.72
2.43
3.46
6.28
7.31
6.02
8.60
9.09
9.54
14 - 2.125 =
% DIA"
+ PORT
2.37
2.92
3.52
4.22
5.09
6.34
9.78
11.00
11.89
12.59
13.20
13.75
7.75 - 2.0
% DIA"
+ PORT
2.12
2.38
2.678
3.01
3.43
4.04
5.70
6.31
6.73
7.07
7.36
7.62
PORT 11.875
% DIA"
+ PORT
2.329
2.77
3.275
3.85
4.56
5.58
8.41
9.43
10.14
10.72
11.22
11.67
11.875 "DIA OF DUCT
5.75
- 2.125 = 9.75
-------
BACK OVERFIRE AIR - TOP DUCT ID PORT 9.75-2 = 7.75
SAME MEASUREMENTS AS REINJECTION
REINJECTION - ID PORT 10.0 - 2.125 = 7.875 ID
% DIA"
% DIA INCHES + PORT
.021 .165 2.29
.067 .527 2.65
.118 .929 3.05
.177 1.393 3.52
.250 1.968 4.09
.355 2.79 4.92
.645 5.07 7.20
.750 5.90 8.03
.823 6.48 8.60
.882 6.94 9.07
.933 7.34 9.47
.979 7.71 9.83
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
C.
SAMPLING LOCATION ;
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE '
NEAREST DOWNSTREAM DISTURBANCE
e>\i.
BARAMETRIC PRESS, in.Hg
_STACK PRESS., Ps , iwg
STK. GAS SP. GRAVITY,Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
1G.
17.
18.
Average
% OF STACK
DIAMETER
.
. d>"
. 2^S-o
,'77
, 11^
. eio'l
.oil
STACK GAS,VS = 174 Fg
SPEED
DISTANCE
FROM
INSIDE WALL
//.**
//• e 7
/o . 47
1.77
0. fo
^y, 6s
^. 2-1
2-. ?fr
2. 1
/ ^J
. Zi
VELOCITY
HEAD
( Aps) , in. HS0
—
•—
fi*4
i.?r
fi^
/. t>
1. f
2. 1
2 . 1
/. #
—
• —
—
/.
/. 7
/. «9
X •
/.
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO _
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE '_
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
STACK PRESS.
iwg_
JSTK. GAS SP. GRAVITY, Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
; 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
a,Yrr,-iOf>
% OF STACK
DIAMETER
.^7f
. 933
,002.
, $23
•7S*
. &4S'
• 3S£
. ZS-o
.f7-7
. u&
.Olel
, 02-1
DISTANCE
FROM
INSIDE WALL
//. ft?-
//. "-7
/0.141
f. 77
0. -
i£ - 76 • f ° &L/$e c .
OXYGEN
Si
STACK GAS
SPEED, Vs
ft/mi n
1
2l/° - / 2i~25~
7J- = S-=S-:T
7^ - 30. *
-------
Table C-ll-
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
BARAMETRIC PRESS, in.Hg_
J5TACK PRESS., Ps, iwg
STK. GAS SP. GRAVITY",GC
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Avcrnpe
% OF STACK
DIAMETER
, *J£~
. 355"
. 25"»
"77
. 067
,0-2-1
STACK GAS , Vs = 174 FS
SPEED
DISTANCE
FROM
INSIDE WALL
•
STACK •
TEMPERATURE
(Ts, °F
K
<**
*
I
(
}
i
I
&
/flu
OXYGEN
STACK GAS
SPEED, Vs
f t/min
x 3<>.ll
-------
Table C-ll. '
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)_
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS,in.Hg
_STACK PRESS., Ps, i wg
_STK. GAS SP. GRAVITY,Gg_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6-
7.
8.
9.
10.
11.
12.
13.
IS.
16.
17.
% OF STACK
DIAMETER
. m
, 1 33
, 882.
.82.3
. 7SV
. t>4£'
, 3S5~
. -Z.S~o
"77
. // &
. e-67
r O^l
- •-•
DISTANCE
FROM
INSIDE WALL
5", £2-
-S^.36
J"7 c?7
V- 7.3
-^/. 3/
-?. 70
21. ^V
/• V-3
/• e>/
< 67^
< 3 &
. /Z--,q «3 ^
1.00 ^
GS
STACK . •
TEI-1PERATURE
(Ts, °F
is-*
(
\
\
OXYGEN
STACK GAS
SPEED, Vs
ft/min
*.r C ^- /
f
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
, A c,
*/_/fc?_
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO "
OUTSIDE OF NIPPLE, (DISTANCE B)_
STACK I.D. (DISTANCE A - DISTANCE*
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
_STACK PRESS. , Ps , i wg
B)
_STK. GAS SP. GRAVITY, Gs_
-r*A
TRAVERSE
POINT
NUMBER
1.
2 .
3.
4.
5.
i 6.
7 .
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Average
1
STACK (
SPEED
f
% OF STACK
DIAMETER
.77?
,
, 6*/6
• 3S£~
• ~ZS*>
• IT?
. tie
•. 7
. P2.I
1AS,VS = 174 Fs
DISTANCE
FROM
INSIDE WALL
?.s*/
7/ ®9
€. t>
8>e>2.
-7.BI
b, 2.V
3> ¥&
2.^3
(• I'Z
1 1 /5~
. 6±3
. "ZJ>
Average
// A P(T + 46
V s
- 43. 77 &/£
VELOC:
HEAI
( APs)
. 3S~
' 3~7
• Z*?
. 36
, tJ'Z-
* 44
jj * 1
/I i
- —
0) 407
S
[TY
)
in. HS0
, •?.£"
- 42-
. *s4
* 44
i *{£~
f 4±T
' 4^
. 41
-——
—
1.00 '
5
STACK
TEMPERATURE
(T£, °F
*<* * *'
r*, — ~
OXYGEN
-5V
"*/
*1
STACK GAS
SPEED, Vs
ft/min
*
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
IXXTATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
_STACK PRESS.,Ps, iwg
_STK. GAS SP. GRAVITY ,GS
-rtft
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
IB.
i 6-
7.
8.
9.
icT.
11.
12.
13.
14.
15.
1 (,.
17.
1FT
hvfrrinP
% OF STACK
DIAMETER
.*7f
. ^ss
; ^6E-
. &7.Z
. 75P
,
.3SZT
>*zs*>
• /77
• /I8
i (^fa 7
« ^2- /
DISTANCE
FROM
INSIDE WALL
y.5^
"f, «>^
^. 6
8.02.
7,31
6. 2-V
3,46
2.43
/. 72-
/, /*"".
. 6&3
. 2-«>
VELOCITY
HEAD
( Ap_), in. HO
^> s
^c- ^
•
/. 2.
/ 2-
J.2-
/• /
/• /
/* /
/• /
•
IvBAr- &
/' •2-
/- 2-
/- 2-
/. 2.
/. /
/• /
/ /
/ 0
Average
STACK :•
TEr-lPERATURE
(Ts, °F
W/=
l
OXYGEN
STACK GAS
SPEED, Vs
f t/min
%> - /. /V-zf
STACK GAS,VS = 174 Fg A! A P (Tg* 460) 407 1.00 ' '» " ~' "^
SPEED " S Ps G^ - *P* = -5"'
?3 := 71. ** ""> ~ *-* °
-------
• Table C-ll. !
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
*/ -
SAMPLING LOCATION
INSIDE.OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE_
BARAMETRIC PRESS,in.Hg_
_STACK PRESS. ,Ps , iwg
_STK. GAS SP. GRAVITY,GC
NEAREST DOWNSTREAM DISTURBANCE_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
~ .
.
' .
eranp
% OF STACK
DIAMETER
.171
. 333
. B$2.
, 'S'iS
. 7SV
, 64£"
. 3S£~
. 2s&
•'77
.IIS
4 16&
I, 343
• ^2-1
. 5-2-7
VELOCITY
HEAD
( A p ) , in. HO
&(&r- A
—
— •
- —
. Z2.
i 2^>
* 24
.2.2.
.2-b
•
&fer-B
. 22
, 2^
. 2-3
.^5-
2_/cY
y//
•
Average
STACK GAS,VS = 174 F£ J A P (T + 460) 407 1.00 <
(/ S \n I lp / -
SPEED v *s ^s
STACK •
TEI4PERATURE
(Ts, °F
f'
/
_., . _ . ._
4-f*
*
OXYGEN
STACK GAS
SPEED, Vs
f t/min
/Mi*'., - 2,<7
3^x
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
c
£ -
SAMPLING LOCATION
INSIDE.OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO "
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE"
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
7J.4C/T roP - of. 4.
BARAMETRIC PRESS, in.Hg_
STACK PRESS.,Ps , iwg_
B) STK. GAS SP. GRAVITY'Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
1 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
(iyprnpe
% OF STACK
DIAMETER
, 77?
, 133
, eez
, &2-3
• 7S~D
. 64s
.355"
, 2s*>
• /77
./IS
.067
. C2-\
STACK GAS,V£ = 174 F£
SPEED
DISTANCE
FROM
INSIDE WALL
7-7/
*7 **? ^ /
h tf * I
£. *(•&
6~. 3°
-------
• Table C-ll-
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO _]
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO_
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
BARAMETRIC PRESS,in.Hg_
_STACK PRESS.,Ps , iwg
~STK. GAS SP. GRAVITY,Gc
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE^
TRAVERSE
POINT
NUMBER
1.
2.
3.
4 .
c
i 6-
7
8.
9.
10.
11.
12.
13.
14.
15.
16
17
18
STACK
SPEED
% OF STACK
DIAMETER
171
. 133
g$2
923
7SV
645"
35-T
25TP
• /77
1 ,118
.obi
02-1
GAS,VS = 174 F,
•S :
DISTANCE
FROM
INSIDE WALL
7-7/
7. 3 4
6 14
6. tf-S
£~ 3°
S.°~l
z.7<7 I
/, 3^3
, £~
VELOCITY
HEAD
( A ps) , in. HS0
3 */
'3, 3
3. 2.
3 . 2-
3 1
"3. /
Average
- —
—
~
3. 1
3 . 3
3- 2-
3. 2-
3. 3
3, 3
!• • 1 1 IliMTM
- 1 2.1. 1 4 £^~/st<- .
STACK •
TEMPERATURE
(Ts, °F
^
t 1
\
1
A- ^
^ - 3
OXYGEN
STACK GAS
SPEED, Vs
f t/min
r. 22-43
0. if
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
BARAMETRIC PRESS, in.Hq
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE _ ~
NEAREST DOWNSTREAM DISTURBANCE _
J5TACK PRESS. ,Ps , iwg
STK. GAS SP. GRAVITY^GC
— -T/TB
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
; 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
(^yprnpp
% OF STACK
DIAMETER
.1*1
. 433
. 6^2
. 'SIS
- 7$T>
. 64s-
. 3S£~
. 2S*>
• 111
. 118
. ok>1
>02-l
STACK GAS,VS = 174 F£
SPEED ^
DISTANCE
FROM
INSIDE WALL
7-7/
7,34
6. f*/
6. 48
6~. 3°
/. ^63
1, 343
, ^2-^.
. 5"z-7
« it>£~
VELOCITY
HEAD
( Aps), in. HgO
tfit-fl
,61
>tt
, (,£•
. -71
. 71
.
W&>r- (3
—
• 63
. ^5"
• t>7
• b11-]
• k^
, 63,
—
—
. —
Average
VA P(T * 460) 407 1.00 '
^ s l?T"^ •
STACK
TEMPERATURE
(Ts, °F
M
1
V
f
^
/
-7
/
/*
OXYGEN
I
STACK GAS
SPEED, Vs
f t/min
it &4*?3
tr-trd
'^ •• _ ij~j T
% -= 3e-<=l
7^ - ^ f , o
305
-------
•• Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL T0_
OUTSIDE OF NIPPLE,
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE_
BARAMETRIC PRESS, in.Hg_
(DISTANCE B)
_STACK PRESS. ,Ps , iwg
~STK. GAS SP. GRAVITY, Gc
NEAREST DOWNSTREAM DISTURBANCE_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
• fc
7
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Averape
% OF STACK
DIAMETER
. *7?
. 962-
. €2-9
. -73-0
. <**/3~
• 3SS~
Z&o
./-77
.//*
.02.)
DISTANCE
FROM
f3. 73T"
/3 2.
/2 . 3~1
it.gr
tl.c
1.76
.5-. «> ^4 |