ABMA
American
Boiler Manufacturers
Association
1500 Wilson Boulevard
Arlington VA 22209
DoE
United States
Department
of Energy
Division of Power Systems
Energy Technology Branch
Washington DC 20545
EPA
United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA-600/7-80-136b
May 1980
Field Tests of Industrial
Stoker Coal-fired Boilers
for Emissions Control and
Efficiency Improvement —
Site I (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-600/7-80-136b
May 1980
Field Tests of Industrial Stoker Coal-fired
Boilers for Emissions Control and
Efficiency Improvement — Site I
(Data Supplement)
by
J.O. Burlingame, R.A. Parker, J.E. 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: R. Hall (EPA) and W. Harvey, Jr. (DoE)
Industrial Environmental Research Laboratory
Office of Environmental Engineering and Technology
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, descriptions 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, SC>2, and 303 data, particle
size distribution data, chemical analysis of the coal, coal size con-
sistency data, combustible analysis and overfire air traverse data.
KVB 4-15900-544
-------
TABLE OF CONTENTS
SECTION P.AGE
FOREWORD iv
CONVERSION FACTORS • v
1.0 PANEL BOARD DATA 1
1.1 Control Room Data Sheets , 2
2.0 PARTICULATE DATA 31
2.1 Particulate Data Summary 32
2.2 Particulate Data Sheets 34
2.3 Particulate Lab Worksheets 42
3.0 GASEOUS DATA 50
3.1 Gaseous Emission Summary 51
3.2 Gaseous Emission Data Sheets 53
3.3 SOx Data Sheets 67
4.0 PARTICLE SIZE DISTRIBUTION 69
4.1 SASS 70
5.0 FUEL AND ASH ANALYSIS 71
5.1 Commercial Testing Analysis 72
5.2 Combustibles Analysis 93
5.3 Coal Sieve Analysis 94
6.0 OVERFIRE AIR TRAVERSES 107
6.1 Overfire Air Data Sheets 108
111
-------
FOREWORD
The purpose of this Data Supplement Volume is to document data
in greater detail than was practical in the Final Technical Report.1 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 J; as it is the ninth boiler tested under
the program entitled, "A Testing Program to Update Equipment Specifications
and Design Criteria for Stoker Fired Boilers."
Langsjoen, P. L., et al., "Field Tests of Industrial Stoker Coal-
Fired Boilers for Emissions Control and Efficiency Improvement - Site I."
KVB 4-15900-544
-------
CONVERSION FACTORS
ENGLISH AND METRIC UNITS TO SI UNITS
To Convert From
To
Multiply By
in
ft
ft
cm
cm2
m
m2
m3
2.540
6.452
0.3048
0.09290
0.02832
lb
lb/hr
lb/106BTU
g/Mcal
BTU
BTU/lb
BTU/hr
J/sec
J/hr
BTU/ft/hr
BTU/ftAr
BTU/ft2/hr
BTU/ft2/hr
BTU/ft3/hr
BTU/ft3/hr
psia
"H20
Rankine
Fahrenheit
Celsius
Rankine
FOR TYPICAL COAL FUEL
(NO)*
(N02)
(CO)
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
Pa
Pa
Celsius
Celsius
Kelvin
Kelvin
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
(lb/106Btu)
(Ib/lO^Btu)
(lb/106Btu)
(lb/106Btu)
(lb/106Btu)
(lb/106Btu)
0.4536
0.1260
430
239
1054
2324
0.2929
1.000
3600
0.9609
3459
3.152
11349
10.34
37234
6895
249.1
C
C
K
K
5/9R-273
5/9(F-32)
C+273
5/9 R
0.851
(1.98xlO~3)
1.063
0.399
0.611
0.372
0.213
(2.47xlO~3)
(9.28xlO~4)
(1.42xlO~3)
(8.65xlO~4)
(4.95xlO~4)
ppm @ 3% 02 (SO2)
ppm @ 3% 02 (S03)
ppm @ 3% 02
ppm @ 3% O2
ppm @ 3% 02
ppm @ 3% 02 (CH4)
g/kg of fuel**
*Federal environmental regulations express NOx in terms of NO2;
thus NO units should be converted using the NO2 conversion factor.
**Based on higher heating value of 10,000 Btu/lb. For a heating value
other than 10,000 Btu/lb, multiply the conversion factor by
10,OOO/(Btu/lb).
KVB 4-15900-544
-------
CONVERSION FACTORS
SI UNITS TO ENGLISH AND METRIC UNITS
To Convert From
To
Multiply By
cm
cm
m
m
Kg
Mg/s
ng/J
ng/J
J
JAg
J/hr/m
J/hr/m2
J/hr/m3
W
W
W/m
W/m2
W/m3
Pa
Pa
Kelvin
Celsius
Fahrenheit
Kelvin
in
in2
ft
ft2
ft3
Ib
Ib/hr
lb/106BTU
g/Mcal
BTU
BTU/lb
BTU/ftAr
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
0.3937
0.1550
3.281
10.764
35.315
2.205
7.937
0.00233
0.00418
0.000948
0.000430
0.000289
0.0000881
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
FOR TYPICAL COAL FUEL
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
ppm @ 3% O2 (SO2)
ppm @ 3% O2 (SO3)
ppm @ 3% O2 (NO)
ppm @ 3% O2 (N02)
ppm @ 3% O2 (CO)
ppm @ 3% O2 (CH4)
g/kg of fuel
1.18
0.941
2.51
1.64
2.69
4.69
0.000233
KVB 4-15900-544
VI
-------
SI PREFIXES
Multiplication
Factor Prefix SI Symbol
1018 exa E
1015 peta P
1012 tera T
10^ giga G
10 mega M
1Q3 kilo k
10 hecto* h
101 deka* da
10 deci* d
_2
10 centi* c
10"3 milli m
10~6 micro ]l
10~9 nano n
10~12 pico p
10~15 -femto f
10~18 atto a
*Not recommended but occasionally used
KVB 4-15900-544
vn
-------
EMISSION UNITS CONVERSION FACTORS
FOR TYPICAL COAL FUEL (HV = 13,320 BTU/LB)
% Weight
In Fuel
% Weight in Fuel
S N
lbs/106Btu
S02 N02
0.666
0.405
grams/106Cal
SOj N02
0.370
0.225
PPM
(Dry e 3V 02)
SOX NOX
13.2X10"4
5.76X10'4
Grains/SCF.
(Dry @ 12% C02)
SO2 NO,
1.48
.903
lbs/106Btu
SO,
1.50
N02
(.556)
19.8xlO~4
(2.23)
2.47
(.556)
14.2xlO"4
(2.23)
SO,
2.70
grams/106Cal
(1.8)
NO,
4.44
35.6xlO"4
(4.01)
(1.8)
25.6xlO~
(4.01)
sox
758
PPM
505
281
(Dry @ 3% O2)
NOX
1736
704
1127
391
1566
SO,
.676
Grains/SCF
(Dry? 12* CO2>
NO2
(.448)
(.249)
8.87xlO"4
1.11
(.448)
(.249)
6.39xlO"4
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.
KVB 4-15900-544
vin
-------
SECTION 1,0
PANEL BOARD DATA
PAGE
1,1 CONTROL ROOM DATA 2
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, lbs/hr s^y
Coal Flow, lbs/hr *fi
% Design Capacity
Ib steam/lb coal
f"' -*
?•?
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
/
4-?^7^
CL\40
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I
flow
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/a
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-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H20
2 "H20
3 "H20
4 "H2O
5 "H20
6 "H2O
FURNACE DRAFT "H2O
FD FAN "H2O
OFA "H20
BOILER OUT "H20
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
/
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6
37
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-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
Coal Flow, Ibs/hr
% Design Capacity
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
2
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-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H2O
2 "H20
. 3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H20
FD FAN "H20
OFA "H2O
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
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r>
,
-------
KVB
NOTES
TE5T N0:
-irtrif
TEST NO; 2.
TEST NO:
TEST NO:
TEST NO:
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, lbs/hr 72-.I &%
Coal Flow, lbs/hr
% Design Capacity
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
3
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.
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "HjO
2 "H2O
3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H2O
FD FAN "H2O
OF A "H20
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
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-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr 7t'.-C't'":''
Coal Flow, lbs/hr_
% Design Capacity
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
+
^-c,~W
£>ho
/O^ Oi.
/*
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "HjO
2 "H2O
3 "H20
4 "H2O
5 "H20
6 "H2O
FURNACE DRAFT "H2O
FD FAN "H2O
OFA "H20
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5 i
#6
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-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr 57.
Coal Flow, Ibs/hr
% Design Capacity
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
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-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H20
2 "H20
3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H20
FD FAN "H2O
OFA "H2O
BOILER OUT "H20
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
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12
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
Coal Flow, lbs/hr_
% Design Capacity
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Kits Air
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
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13
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "HjO
2 "H2O
3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H2O
FD FAN "H2O
OF A "H2O
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
&
i
1°
H
D
0
0
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14
-------
TEST NO.- {,..'2
KVB
NOTES
TEST NO:
TEST NO:
TEST NO:
TEST NO:
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
£i2?7
Coal Flow, Ibs/hr f>Tl
% Design Capacity /65f
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, KlbsAr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
7fc
r-*?-7?
<9k*v
7o,ooo
ifrrj dz_
lOOo
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/
MW
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fr
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tff
r~>ei.
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16
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H-O
2 "H2O
3 "H20
4 "H20
5 "H20
6 "H2O
FURNACE DRAFT "H2O
FD FAN "H2O
OFA "H20
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5 i
#6
1
-7
0
I'D
D(.
o
o
-o I
av
},°
-»..
«»
"A
'^4.
^}
*••
tf
0
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^
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r
p
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tr
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0
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^
2--
c
f
17
-------
TEST NO: 7 '
KVB
NOTES
51
TEST NO:
TEST NO:
TEST NO:
TEST NO:
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, lbs/hr_
Coal Flow, U>s/hr_
% Design Capacity
Ib steam/lb coal
fO.O
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
?
5>-7 \rf
14 V
1i/
V
\,90
H<
I*
tf
w
\
|i^ ^/r»C
1»<>\fyZ.
i ( /»
19
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "HjO
2 "H2O
3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H2O
FD FAN "H2O
OFA "H20
BOILER OUT "H20
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5 '
#6
^
a
\v
1."
$
0
a
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I*
le-o
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l\
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0
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0
a
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0
0
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1-4
K
- 1 0
'X
>JX/-
'7yt- -
1\
fr'
>
t<
4«
?--
2<
?
i
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, lbs/hr_
Coal Flow, lbs/hr_
% Design Capacity _
Ib steam/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY , %
/o
<"-/2-9f
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V
i f-t^>
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Zoi<"7(,
ti
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H20
2 "H2O
3 "H20
4 "H2O
5 "H20
6 "H20
FURNACE DRAFT "H2O
FD FAN "H2O
OF A "H20
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
/
l%<
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0
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1?
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<
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rj
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t
.
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
Coal Flow, Ibs/hr
% Design Capacity 7/ V
Ib steam/lb coal l_L'^L
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
i4
*r-<4-7J
&rtk,a
g'O.Gtxifi'/tu-
AC -L«. J
to ft
JU
Mi
fan
fr
M
W
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m
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fb
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ift
n<
u<6
J-^K
1* 2t4o
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^
u
ft
#
IW
Ifr
*1
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "HjO
2 "H20
3 "H20
4 "H20
5 "H20
6 "H20
FURNACE DRAFT "H2O
FD FAN "H20
OFA "H2O
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
IS
#6
i4
0
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A*
D
C
U
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V.
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*-
fi>
a
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— • ~~.
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
Coal Flow, Ibs/hr fat
% Design Capacity /oc
Ib steanv/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
IS
5-n-iU/tlS
foot,
t* lft<
filUl
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III
lit
• n^
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1C
il
tl*
no
no
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rfo
tcui7^
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H°
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE 11 "HjO
2 "H20
3 "H2O
4 "H20
5 "HaO
6 "H20
FURNACE DRAFT "H2O
FD FAN "H2O
OFA "H2O
BOILER OUT "H20
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5 i
#6
0
l<
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0-1
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-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, lbs/hr_
Coal Flow, lbs/hr_
% Design Capacity _
Ib steain/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART_RECORDER_
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
It*
S--1-*>-~7^<
^
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ul
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27
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H2O
2 "H20
3 "H20
4 "H20
5 "H2O
6 "H20
FURNACE DRAFT "H20
FD FAN "H2O
OF A "H2O
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
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//
p'
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J
-------
KVB
PANEL BOARD DATA
ABMA TEST SITE I
Steam Flow, Ibs/hr
Coal Flow, Ibs/hr (?2dc>
% Design Capacity /*V *{•
Ib steain/lb coal
TEST NO.
TEST DATE
TEST COAL
TEST CONDITIONS
COAL
TIME
POUNDS ADDED
STEAM
INTEGRATOR READING
TIME
CHART RECORDER
STEAM FLOW, Klbs/hr
AIR FLOW, RELATIVE
FLUE GAS TEMP, °F
STEAM PRESSURE, PSIG
WATER TEMPERATURE, °F
STEAM PRESSURE, PSIG
FEEDWATER TEMP, °F
TEMP FD FAN, °F
RELATIVE HUMIDITY, %
J3
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/
-------
KVB
TEST NO.
DRAFT GAUGES
WINDBOX PRESSURE #1 "H20
2 "H20
3 "H20
4 "H20
5 "H20
6 "H2O
FURJiACE DRAFT "H2O
FD FAN "H2O
OF A "H2O
BOILER OUT "H2O
CONTROLS
OFA
FORCED DRAFT FAN
STOKER SPEED
STEAM FLOW/AIR FLOW
STOKER
COAL GATE POSITION
GRATE SPEED, %
WINDBOX CONTROL POSITION #1
#2
#3
#4
#5
#6
0
11
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n
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30
-------
SECTION 2,0
PARTICIPATE DATA
PAGE
2,1 PARTICULATE DATA SUMMARY 32
2,2 PARTICULATE DATA 34
2,3 PARTICULATE LAB WORKSHEETS 42
31
-------
LOCATION:
PARTICULATE DATA SUMMARY
PART I
TEST
NO.
O<
Dl
*$
^
If
/"
H
i?
:
V
1
->
1
5
10
ii
15
Total
Mass
mgm.
vrv.'
Zf'l e>
flits'
i?;«c
/oZ-Ctt
6
t;. ^^
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r^^«
^.CtlO
•H.tf*
85IyAS
Liquid
Coll.
ml.
5«
tfe
^
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5-7
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Baro.
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"Hg
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Press .
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fr^JfO
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021
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£>.27
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Orifice
AH
"H2O
tf-fcr
0-5T-
d-^
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0-^
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7,3-3
Stack; Gas
Temp.
"R
&
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t&3
4?$:
/OC£
/o W
Excess
02
%
ilB
gl
25
^
*1
lit
Pi
7(>
Sampling
Time
min .
7-Z
^
ft
W
72
%
fZ-
9^
Nozzle
Dia.
in.
£>.3<4>
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0 31 &
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Pitot
Factor
n.d.
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0 *}7
£>8S7
O.V3>7
Fuel
Factor
SCF/10%TU
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fgzo
032.0
4&c
ff32.o
9S20
132.0
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MW
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2.9.X3)
>2^.£6
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C'X I4/
2 ^."3 7
#15900 rev.
-------
Location
PARTICULATE DATA SUMMARY
PART II
TEST
NO.
LOAD
02
CONDITIONS
EMISSIONS
lb/100BTU GR/SCF
LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin.
//-a
17,8
-found
IO&- 1
OF/4
/, 0/9
/OD
3JL
ft
/O
/oo
~founc)
4 OF A-
1.71,1
It
6.1S1
73
/O
1 'CO
f>-
-------
PARTICULATE
DATA
Leak Check Rate
Percent Oj
-------
PARTICULATE
DATA
Leak Check RJte
vac
in. Hg ft3/min
ISOKINETICS •
TEST NUMBER 2~
DATE
OPERATOR
FUEL
SITE
PROBE UDCA'
TEPlPERAtURES , "F
Sample
Poinc
Time
METER CONDITIONS
A H Heter Reading
Stack
Probe
Oven
Imointjers
In
Out
Meter
Vac.
, ^
. 63-
•2.20
•79
,/7
7
. 85"
-70
£Z< O
2.7°
23°
2.3?
-7°
•2.0
412° .
ZS&
4132
4123.
-2.4,0
/Z
24°
•71
71
72
76
w?. o
•z z
ftf-l
4130.
2/5"
2". 7
t/o
265"
75"
z.
,32-
41*3.6*.
-2.es*
2.7
. 77
2.70
4146'. 77
•77
27
. 27
00
37
. f f
33
3**-
2.?
It
33
8°
252T
Aver 096
METER VOL.
SAMPLE VOL
*V7
Nomcxiraph Setup
p»eter c
Pttack • Tstack
cpitot
.037 ~
percent O2 •
Pressure
» HjO -
Noz(Ideal)- ,
Noz(Actual)*
Vol.(End) Vol. (Start) avol.lml)
«i /S2^ - / . c? . o
Total
35
*
e
*
Total Vol. H,o c'° ml
-------
PARTICULATE
DATA
Leak Check Hate
vac
in. Hq ftV
ISOKIHETICS " /0O-~
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
Sampl
Point
Time
METER CONDITIONS
A H Meter Readin
TEPIPERATURES, "F
Stack
Probe
Oven
Imoinqers
In
Out
Meter
Vac.
e-l
2.20
2. e
.23
f/o
4*
7.47
3.2.
,*/
33*
2.2-
3.3T
418* .
62°
2/7
• 76
77
1,26
62,
/V
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2*
37
4167. Jo
ff
37
49*1. -f?
2.7*
//*>
4113 -S3
ft*
//*
• 11
S3"
2.60
2.*
60
. f »
60
38
3£
4°
243-
6*
34
m
II
ZfS~
,36
62.
Average
f*
1,26
KCTER VOL.
SAMPLE
431 -.
Oj •
Pressure
iH,
Monograph Setup
C
T«tack '
. AP -
Noil Ideal).
^ Vol.(End) Vol. (Start) avol.(ml)
«i /"7° - /**> _ . 70
.2 //(> - /**> . /f>
• 3 ° - ° . O
\ H^O • Hoz(Actual).
Tot.l
30
14
Silica
g (Start)
/fz . S3
Total Vol. H2o '• _r
-------
PARTICULATE
DATA
Leah Check Rate
vac
in. Hq ftVniln
isoKiorrics
TEST NUMBER_
DATE
OPERATOR
FUEL
SITE X
PROBE LOCATION
TEWERAtURES , °F
ample
oint
Time
e-l
METER CONDITIONS
APS
./I
A"
Meter Reading
47
Stack
Probe
2-70
Oven
ImDiriaers
In , Out
Meter
/0V
Vac.
.4*
2-4°
3
V
5*3°
.11
3/c
3.7
.24
36
2-?
,**
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. 92,
2-7°
Ll.°
£•3
//2-
.34
3,2*
72.
J^L
//*
,54
6/0
./*
.47
2-8*
.32-
f.ff
-2-8*
6f°
.4*
7 3 • 46
t.1
,3*
Average
METER VOL.
START
SAMPLE VOLJ
sozz
Setup
V*
pl tot
ite?
StacK Press.
In. Hq-Cauqe
Percent O2 •
fiHq
Tstack •
CP 1
Noz (Ideal; =
Noz (Actual) *
tup. Vol.I End) Vol. (Start) &Vo1.(mil
»i f7^ - / 0t) > 7^
.2 /I2, -
Total
gfStart) Aqrams
Silica
Gel
/2.6 .
otal Vol. H,0 *•** ^'•1
-------
PARTICULATE
DATA
ISOKINETICS •
Vac
in. Hq
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATI
Sample
Poinc
Time
METER CONDITIONS
A PS AH Meter Reading
TE«PERATUR£S.
Stack
Probe
Oven
I momqer s
I n j Out.
Meter
Vac.
•70
-7-2.
• 43
'2.70
A
.43
-zto
(0
.64
sser
11
.44
a-
.2°
2*7°
fz
fz
56'
2.7
7
•2.70
37/sr.
-2,7°
-2-70
f. of
Average
METER VOL.
START
Setup
meter
PstacK
In. H9-Gau«|e
Pressure
2*70-
NazddeaJ)^
Ho.lXctu,!,. .3/6
'"P- Vol. (End) Vol. (Start! AVol. (mlj^
,1 /42> - /so
*-**~-
12
• 3
Total
- qlStartl Agrams
38
Total vol. H2o
-------
PARTICULATE
DATA
Leak Check Jtete
J/
Vac
in. Hq
ISOKINETICS
TEST NUMBER
OPERATOR
FUEL
SITE
PROBE LOCATIOH
TEftPERAtORES , "F
Sample
Point
Time
METER CONDITIONS
A^s AM Meter Reading
Stack
Probe
Oven
Imoinqers
In Out
Meter
oa,%
Vac.
£-j
.32-
£717.31
./v
e-z
.n
1.2,
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7
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e
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2-2
£7°
27°
\
z.e
II
• 1*
.82.
Average
SAMPLE VOL
Homograph Setup
C
-pitot
Stack Press.
Barometric
Pressure
Pstack •
Tn»ter *
AHg
Imp. Vol. (End) VoU (start) AVol. Imll
II
iP «
Noz( Ideal}-
Nozl Actual) -
39
«4
Silica
Gel
/^«> -
Total Vol. H20
figrams
-------
PARTICULATE
DATA
Leak Check Rate
vac
in. Hg ftj/
ISOKINETICS
/*•••*.
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TErtPERAlURES
Sampl
Point
£-1
Time
METER CONDITIONS
A H Meter Readin
Stack
Probe
Oven
Imoinaers
In Out
Meter
Vac.
Z/D
62.
BO
32*
32*
3.7
/*
3770.41
^
£704.
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II
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. 32
2,2*
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2.0
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& 94-33
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£202 .02-
A
260
//e
/xsr
Average
.1*1
START
SW1PLE VOl.
?*7
^^71 -
Pressure
mo
Total Vol. H,O ^T ml
-------
PARTICULATE
DATA
Leak Check Rate
METER VOL
jiAHPLE VOL
/**/
<
~*»6
CpiCOt
StjcK fress.
_In;H2^au,
Percent O2 * I
Barometric
Pressure
meter
Pstack - Tstack
T t >r ™ ^ *
AHg - NozddeaD-
% H2O * NOZfActual) = ,
Imp. Vol.I End 1 Vol. (Start) flVol.(ml)
•1 /»*_. -
*4 _g(Endi
Sjlica
Ctl
Total vol. H,0
-------
PARTICULATE LAB WORKSHEET
TEST NO. /_
Date
(Inlet, Outlet)
Box No.
Test Description
LOGATION
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
H2O RINSE
RINSE
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
BEAKER NO.
V
\
DATE WT.
\>
TARE WT.
X
\
\
AVG.
s
/a.
\
POST TEST WTS.
\
A
s
~. 0033
/o . 47/6
0S-7-2-
\
AVG.
\
\
A WT.
\
t>. 2JVZ
A Vic =
A ogv =
A Mn
. 3
ml
mgm
LOAD
klb/hr
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, Outlet)
Box No.
Test Description_
LOCATION
Eng.
Dry Gas Meter Vol (ft3)
Final
Impinger Water Vol (ml)
Initial
A Dgv"
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
\
BLANK
NO.
BOTTLE NO.
/
\
BEAKER NO.
\
\
DATE WT.
Y-27-7JT
-2? - 77
TARE WT.
,7-732-
^.\
\
-7^2.
V
\
S
S
AVG.
SB.
POST TEST WTS.
^
V
*
/• *^ Jtyii
AVG.
\
A WT.
\
A Vic =
A DgV =
A Mn
ml
LOAD
mgm
REMARKS:
43
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, 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.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ \
f \
RINSE
•
7
y-2f-?7
9 7. -7637
17- 7&3t>
17. 763t
f 7- 7(>3t>
FLASK
4
&
6*f.sifosr
•
t>
FILTER
NO.
3
-------
PARTICULATE LAB WORKSHEET
TEST NO. *[_
Date
(Inlet, Outlet)
Box No.
Test Description_
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG. _,
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ \
/ \
Final
Initial
A Vic
ACETONE
RINSE
e
3~-1-7l
/e
i
DRY
FLASK
2-
£~~l-7l
S*. 3043
' £&• "2>04 1
S&- 3o*JO
S0.3°4/
2
FILTER
NO.
^
4-25-7^
^7&?l O
^^£}*y &
.T?3<>
•
"7 ^^-3^
3
Total
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
X
/. o 75-2.
\
AVG.
\
10
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, Outlet)
Box No.
LOG ATI ON
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Iropinger Water Vol (ml)
1
2
3
Total
CONTENT
H20 RINSE
7
RINSE
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
X
X
BEAKER NO.
V
\
DATE WT.
\
TARE WT.
\7
5
S
s
\
\
AVG.
POST TEST WTS.
V 7
\
/of. 47o I
\
AVG.
S
A WT.
S
0.61*8
J83I
A Vic
A DgV
A Mn
ml
mgin
LOAD
REMARKS:
klb/hr
%
46
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /
Date
Test Description_
(Inlet, Outlet)
Box No.
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
AVG.
__ A WT.
A Vic
A DgV
A Mn
H2O RINSE
Impinger Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
/"=/
,-z-/&>
/02../43&
/e> 7. • /&(>
.
/o2,/'J3^
A Vic
3 Total
DRY
FLASK
.
/^
•
9f. 17*&
tt 17*0
?S~. ?773
•
^5". ^777*
FILTER
NO.
^P
•
dffj 49 1
.941*
.04?°
. .
.636>
^f> . Zt>*fl
1*>. 2i>4t,
*
1l.'2.W4
0. 2,&6>£~
. 1702.
. 1 702
- ^*77
. 1 16*
p. Wt* 1
= ml LOAD klb/hr
ft3 0? %
b 04- 9 mgm REMARKS :
47
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. S*f (Inlet,
Outlet) LOCATION ^St'/C JT - *3 OCJP
Date &Z- /V~^7 Box No. Eng.
Test Description
Dry Gas M«
Fina]
Initia]
A Dg\
ster Vol (ft3)
L
L
/
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ \
/ \
Impinger Water Vol
Final
Initial
A Vic
RINSE
2J<=>
7^5-72°
#5": 37/6
7^:5-7/6
1G. sin
1
FLASK
'
JS~
^&.'3°£l:>
«5^- Zotf*>
%SB>. 3°^
5"*- so 41
2
NO.
7
.e&ei
,es€*f
.ese*l
—
. 9$ '6Z
3
(ml)
Total
BLANK
NO.
\
\
\
\
/
/
/
/
7
/
/
/
\
\
\
\
POST TEST WTS.
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
\ /
\ /
V
/\
/ \
/ \
7*57 7ob 7
ffP. ~?t>7l
1&. -7°? 4
•
^,7*73
o.i$yt>
ml
&i. 4449
&-/. 4448
^/- 445~l
5-/, 44^
/. 140^
/. &/3&
f. o/jj"7
/.o/ZS~
J,0/Z'£
tf. /$-
-------
PARTICULATE LAB WORKSHEET
TEST NO._
Date
Test Description_
(Inlet, Outlet)
Box No.
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final .
Impinger Water Vol (ml)
Initial_
A DgV~
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
\
Z/
\
DATE WT.
\
\
TARE WT.
X
A
\
V
X
X
AVG.
POST TEST WTS.
\
s
y
A
-. 1486
AVG.
/.
A WT.
\| ff. 577f\ Z.*°2,<]
A Vic
A DgV
A Mn
ml
LOAD
REMARKS:
klb/hr
8830-5 rev.
-------
SECTION 3.0
GASEOUS DATA
PAGE
3.1 GASEOUS EMISSION SUMMARY 51
3,2 GASEOUS EMISSION DATA 53
3.3 SOx DATA SHEETS 67
50
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
%
Dry
co2
Dry
CO
ppro
Dry
NO
ppm
Dry
ppm
Wet
HC
ppro
Wet
Dry
C0
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
SO 3
ppm
Dry
NOTES
01
G2-
8-3.
II
tt-L
to Z
/2-r
/«T
72
12 -1
to; 1
6.1
'*•?
/? r
02
84
/« 8
DgC
oul
z-t
/£>
as.
/f
•7/.V
or J -f c>t4t> cf
10. 1
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
5-t &'.
Fuel : f\ &h~t*j D
/=.£
/^;
DATE
4T/*2,M
^.^^
>r/X^y?J
LOAD
/To
100
/^a
CONDITIONS
6f&»*~ C* <+*FA
Y
7.8
co2
Dry
/z.7
/A3,6
11.0
CO
ppm
Dry
NO
ppm
Dry
fW
^»
160
/6f
/Jfc
/^
^ed
NO2
ppm
Wet
HC
PP">
Wet
02
Dry
C02
Dry
CO
ppm
Dry
NO
ppm
Dry
so2
ppm
Dry
^L-i-
S03
ppm
Dry
L
NOTES
v _. C. •' y
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO J,
DATE
FUEL £) /•// Q
LOAD
CONDITIONS
5s.
DATA TAKEN BY Q Ef
Probe
Time
02
«
(dry!
C02
(dry)
CO -
ppm(dry)
unc cor
NO
ppraldry)
HOT LINE EAXPLES. PPM (WET)
NOx
unc cor
NO
unc cor
NOi
unc cor
HC
unc cor
RE HARKS
OC
Vr
7.o
2s-
Iff?
to
NOTE: Parts per million (ppm) figures are corrected to 3% 02
53
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE ^\ DM A- S\fg
TEST NO
DATE
FUEL
CONDITIONS
DATA TAKEN BY
Probe
Position
Tim
02
t
(dry
C02
t
(dry
ppm(dry)
unc cor
NO
pprc(dry)
unc cor
HOT LINE SAMPLES. PPM rWETl
NO
NO 7
REMARKS
-go
2
no
/o
'.0
3,'JC
A
AVERAGES
4L__
U7
II"
m&
%%%•
NOTE: Parts per million (ppm) figures are corrected to 3% 03
54
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE Jr
TEST NO
DATE
Probe
5/s.ck^
Ste*tfe
CLri'i*
Mr-iL
S52
S_!f±t—
frteJt
J
V///7*»
02
%
(dry)
/>
^A
/A»?
f.V
o^
7.V
7*
*o
C02
\
(dry)
//(?
W
7-t»
/£?JT
y/.^
/i6
H*
//.i
CO
ppint
unc
/
"s
1
1
)
/
(
}
t
I
\
•
iry)
V
/
\
NC
ppral
unc
/>
•+:w
V-To
?JO
tw
I/O
Wo
(<4e>
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
flry)
cor
?35
^l/
^
^
»i-
»(.
/^3
O^'O Cec* I
/00c/t 7o^^//,r.
i^<^ a/^A
^^-C^
HOT LINE SAMPLES, PPM (WET)
NC
unc
)x
cor
N
unc
0
cor
NO
unc
^
cor
,
H
unc
c
REMARKS
JL«-
*#. zv
npifM" -^^j-
I*r V7'/=
.yct-vj'/*
AVERAGES
£
|J
T*i*^
tJ'l
«•«
W
m
»*
H.O
0m
W/tf<
w///,
WM
wm
w<#,
w///,
m,.
V?
251
144
w///<,
wm
wm
•mnk
^%
%^?
'#m,
%%%.
^
W6
wm
^/////,
w
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE jfX!L']rvA- £(.Y"C _J_,
TEST NO
DATE
/Y
S~/| / ? ^
FUE
LOA
CONDITION
L Ok;o
D /00?b
s /0uJ ft. /y,toc ^p^-
DATA TAKEN BY ^ Ec^
Probe
Positjo
Mettle
£ fc*c\ctfJL
St&tL
£feclc
(•KtAtM-
jf7.dk
Time
f'V
fc
r.3o
.
7'V.i
IS-oo
S»:K»
b.Ja
i.**1
(dry
\\
> -$
*/
•i
C-*»
fcO
*r-=
*,*«;.}
— —
— L_
C02
\
(dry)
fL£) _|
|^-?-_ ^
\M-
\
^/•d
a«>
W.3-
/'•6
\
— V"
1 ( f 1
4.1
JtLL
/?•• > w^
U* %jz
UL^
CO •
ppm(dry)
unc coi
-4-
\,
444
.
/44
\ —
»r-
NO
ppra(dry)
^0
7o
10
w>
1^Q
cor
r/y
2ol
?-^1
H>l
3.T1
93-e>U£tl
. 1
v^^\
[.._
HOT LINE SAMPLES. PPH (WET)
NOx
r
NO
NO 5
unc
CO
HC
unc
REMARKS
•"^r/.
Pr> Gl^ "~
urt~ Sp/-^-'
PhcC
2C( td
—
AVERAGES ~ "-*
1
^^
I It '
',
th\
'/////\
^
/
%jj&-
w%.
Ji^/j
$
^^
?%i"
^P
*/S/S?
NOTE: Parts per million (ppm) figures are corrected to 3% 02
56
15900
-------
TEST SITE_
TEST NO <*>
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
',(J C
o. <»
01
•*
ft
fo.1
fit
WM
o
AVERAGES
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE £_
TEST NO <£_
DATE f-
unc
cor
HC
unc
cor
REMARKS
K«—-r«?^7
IK
NOTE: Parts per million (ppm) figures are corrected to 3% 02
58
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SH
TEST NO
DATE
Probe
fltt__
-St*cH_
tfft*JV^
Mi'to
toWt" '
i^SiJ-
lay^r i.
L.W -31-
tSJi— -^~
^w<./ i
^.Uc< ^
t£V**_L
/^U.f L
Time
/a«
/ 10
1 lo
//}«
«JV
II Vo
HHi
\lf°
nJr
^.or
-B ^
ft-?
/ri^- ^-^^
02
I
(dry)
f<5
7A
7.X
7A
/-1/
M
SIS
i.o
11
4-0
7-1
C02
%
(dryl
M-i
!^/
!i-°
a.o
«A.i
U*
«1.1
«.i
n.6
i/.o
11.1
FUEL <£*oe
LOAD "?<^ K
CONDITIONS Gcvfioc,r P° 'W 2
DATA TAKEN BY Vj\"
CO •
ppn(dry)
unc
cor
NO
pp»(dry>
unc
Ho
IV
J?°
IK
ir
I>S
IW
18S-
|«i
f80
\**
cor
z*<
«r
22-Z-
»f
>/
2rt-
2>l
*»*
2'/
2't
4A
*
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
^v *.^4 w*
AVERAGES
__£££_
_£*£_
tfu*-
7-'«
H
^f
n-i
•i-1
Mi
'W#
Wt
WM
W/ti
W//J
WM
W//t
wm
ilX
7>o
l*>£
^^
^^
^^
M^
^^
^^
m<
Wfa
W/&
ym
W^'
Y/m
W///S
W//«
'^m
w%
W^i.
^^
L*^
NOTE: Parts per million (ppm) figures are corrected to 3%
S9
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE X.
TEST NO **8
DATE r>l->s
FUEL
LOAD
CONDITIONS Gi
DATA TAKEN BY
Probe
Posi t ion
ALL
-St^H
*/"/JV,
Tim
*u
k-H
U.SO
l/t-
01
13°
ns
1Mb
02
*
(dry
1-1
8.'
8.5
8.tt
7-8
7.-A
?.fl
A.fc
CO2
t
(dry
i.r
t
/to
ISC
l*a
Iflo
fRO
cor
Z-5Z-
243
l4f
&l
T-^
111
Z?T-
12\
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO-)
unc
cor
HC
unc
cor
REMARKS
OL MOVX^
OC.WK
Hv*iL.a^
•4-jUwU
L<.^'^ +f
TV/ ;<-«.
^ si«.rr
. » '— f-1
AVERAGES
7-fr
NOTE: Parts per million (ppm) figures are corrected to 3% 02
60
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LORD
CONDITIONS
DATA TAKEN BY
Probe
*ff*t.K.
Time
//-%?
1t~S-
art
7. to
ii.^1
i/nf
|f&3
^•Zo
02
(dry)
6£
srr
/•M
£t>
j.S~
III"
cor
/c&
^2«4.
^€
2*7
WZ-
iyi
Zt-t
'
HOT LINE SAMPLES. PPM (WET)
NOX
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
£0K «*•! ^*2.
5»y ** _?
^
AVERAGES
217
UOTE- Parts per million (ppm) figures are corrected to 3% 02
61
15900
-------
TEST SITE__
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
H-
HT
LOAD_3^ K
CONDITIONS
DATA TAKEN BY
Probe
St^K
*
Time
/«*>
JOff
Jl ofl
M
;/Jo
iff!
II .Hd
a.
unc
cor
HC
unc
cor
REMARKS
AVERAGES
if.i
l-K
gill
w////,.
w?//,
W///S
NOTE: Parts, per million (ppm) figures are corrected to 3% 02
62
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE _/
FUEL
LOAD
^
11
CONDITIONS g£
DATA TAKEN BY
t
Probe
Time
02
%
(dry!
C02
%
(dry)
CO •
ppm(dry)
unc cor
NO
ppn(dry)
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO-)
unc cor
HC
REMMWS
unc cor
Uo
l.a
II 10
ins
217
lil
Cst.
KU
10.
)0
M.O
AVERAGES
/a i
NOTE: Parts per million (ppm) figures are corrected to 3% 03
63
15900
-------
KVB
GASEOUS EMISSIONS. DATA
TEST SITE ~f.
TEST NO ^* 1 f*
DATE fff)c\~) J^L ' • 1
1
FUEL Ktdutle^
LOAD % 0oc>
CONDITIONS ffjT/tiu^u- Ot ~-J at&
"~~ — ^
HOT LINE SAMPLES. PPM (WFI
AVERAGES
3r*c«
/•*
//•7
W%ffi
'#m
»Z%M%
yftaa.
jfffpfi'.
ma
vm/fa
zzz&
\l?f
tfjfjjz
'#m
'##&
%%%%•
yffi/%.
'WM
W#&
wmff',
mffim
m<&
&/%%
y/ssffl'
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
FUEL_
LOAD
:?-?•)
CONDITIONS
-±=v
0*"
DATA TAKEN BY ]\>
3-
Probe
Tine
02
%
(dry)
C02
t
idrjr).
CO •
ppm(dry)
unc cor
NO
ppra(dry)
HOT LINE SAMPLES, PPM (WET)
NOx
NO
NO->
HC
REMARKS
l.o
IXZ.S
B.i
195
m
M-A
1*$"
O |6^(
10,1
hi
AVERAGES
'am.
ma
WM
Parts per million (ppm) figures are corrected to 3% 02
65
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
02
(dry
CO;
I
(dry
CO •
ppm(dry)
unc cor
NO
ppm ( dry J
HC3T LINE SAMPLES, PPM (WET)
NO
HC
REMARKS
/v,r
Z2
tt
HI
7
r/.w
7.4
30
8,6
/If
3ii
ll.Ol
NOTE: Parts per million (ppm) figures are corrected to 3%
66
15900
-------
Local
Date
Unit * 3
SOx DRTft SHEET
Probe Location fi Probe Length
Fuel /^UD
Load
Test Description: Tfes.T ** - O*3t" Mio
Test
No.
1A
It
K
Box
NO.
^
t>
-2.
3
Sample
Time
t6'-it'
/3-'o
Wf
Meter
Temp.(T)
/** *>r
/j;/dC~
/d^
/fc>f, /or
of
Meter
ft>)press.
• d
o
£>
Meter
Reading
O,o
//oo
tf.o
/.to
to
1-00
(f^B&ro.
Press.
rrr*.
>
^
Port
ffcrtt
/
\
1
Purge
Time -
2a+v^
ZGrtJuv*
*2o*u^
(
02
5T*
5^^
7^
ffl
Test
Test
Test
Normality N
Dilution
Factor F
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + P
A - B
SO2
DGlW
\?*r
A
23. r
£3-7
2->.4
Z5-6
5if
/,oo
SO3
fe./
SOx
SO2
i?^>/5«/
2«>
A
fat
*•*
n*
/(,*
fur
{,00
SO3
^.r
ir
SOx
S02
0-etO'J-
/»
<2>
34.7
5r»
5T*-
3tfo
^4
S03 .
*4-r
4.r
SOx
CO
O
w
(A-B)(N) (FH460+T) (24)
502 - V(P4p)
502 - ( )( )( )( )24
cr\*5 1 / "?7it- 1 c^dl —
qo, ( ) ( ) ( ) (
S03 ( )( )
S02 @ 3% 02 = /6*>7
S03 @ 3% 02 = Jo
SOx @ 3% 02 = /6S7
Z$b
>24
S02 =
*?(*•)•> *
on^
S02 @ 3%
SO3 @ 3%
SOx @ 3%
)( )( )
( )(
iff "3
)( ) ( )
( )(
2H4-
02 = ($
02 =
02 "= ft
( )24
)
( )24
)
3f
^5^
^4i
S02 =
SOS =
SO2 @ 3%
SO3 @ 3%
SOx @ 3%
)( ) ( )
( )(
/K?
}( ) ( )
( )(
z/.4
02 = 2/'(
02 - <2
o? = .2-1 '
( )24
)
( )24
)
/^
«
74*
-------
Local
Date
Jnit
/ 8
Fuel
SOx DATA SHEET
Probe Length_
k \)
Tt
S:
Load
Test
No.
tf/4
tf£
//<*•
{6(-
Box
No.
^
hft
3
Sample
Time
/^,07
/1.00
;•£*/'?
Meter
Temp.(T>
6^~
62-
&J
Meter
ft^Press.
0
0
0
Meter
Reading
.6
f.OO
.0
/.QO
.0
I- 00
(f) Baro .
Press.
;r^r
i'
i,
Port
Nc^k
Po^-
Purge
Time
-2-0
2~&
5L&
i
02
^-/
^•^
<7.^
Test #
Test #
Test #
Normality N
Dilution
Factor F
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + p
A - B
SO2
.0/of
?LO
0
'fcy
-7, V
7. cr
S7X
/<70
SO 3
/
1. 7
SOx
S02
>0/02,
^5~
0
t3#vA~
•sfi.4
3f?-
-------
SECTION 4,0
PARTICLE SIZE DISTRIBUTION
PAGE
4.1 SASS GRAVIMETRICS 70
69
-------
SITE I
SAS3 GRAVIMETRICS
Test #9
Ohio Coal
10 y
3U
1U
Filter
TOTAL
9.7104
1.3858
0.3880
1.1981
12.6823
76.57
10.93
3.06
9.45
100.01
% Passing
23.43
12.50
9.44
0
Test #18
Kentucky Coal
10U
3U
Filters
TOTAL
10.5443
1.2289
0.4275
0.6164
0.4853
0.5507
13.8531
76.12
8.87
3.09
11.93
100.01
23.88
15.01
11.92
0
70
A Research-Cottrell Company
-------
SECTION 5.0
FUEL AND ASH ANALYSIS
PAGE
5,1 COMMERCIAL TESTING ANALYSIS 72
5,2 COMBUSTIBLE ANALYSIS ' 93
5,3 COAL SIEVE ANALYSIS 94
71
-------
F 462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-843*
ztt
PLEASE ADDRESS ALL CORRESPONDENCE TO'
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal Test No. -1
Sample: Ohio Coal
Test Site: I
KVB
4/28/79
6/23/79
Analysis report no. 71-34524
PROXIMATE ANALYSIS
As Received Dry Basis
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/lb.
% Sulfur
4.08
10.09
37.43
48.40
100.00
12634
3.50
xxxxx
10.52
39.02
50.46
100.00
13171
3.65
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
Initial Deformation
Softening (H = W)
Softening (H = VZW)
Fluid
Original Copy Watermarked
For Your Protection
xxxx
xxxx
•xxx
xxxx
xxxx r
op
XXXX r H -. Conehe.qht
xxxx °F
°c
xxxx •"
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A.
tdWtK^^y^-
RAH/ br
SO HOLLAND, IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG, WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDtBSOM. KV •MIDDLESBORO.KV -MOBILE. AL -NEW ORLEANS. LA • NORFOLK. VA - PIKEVILLE. KY • VANCOUVER. B.C CAN.
'-.5 i
Charter M.mber
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-M34
SlNCI t«0ft
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal Test No. 2
Sample: Ohio Coal
Test Site: I
KVB
4/30/79
6/23/79
Analysis report no. 71-34528
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
3.76
9.05
38.10
49.09
100.00
xxxxx
9.40
39.59
51.01
100.00
Btu/lb.
% Sulfur
12757
3.14
13255
3.26
FUSION TEMPERATURE OF ASH
Oxidizing
Initial Deformation
Softening (H = W)
Softening (H = ViW)
Fluid
Original Copy Watermarked
For Your Proteclion
XXXX °F
xxxx °F
XXXX "F
XXXX °F
73
XXXX
xxxx
xxxx
xxxx
H — Cone, Height
A — Cone Width
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
V '"v •'"' V
Charter Member
RAH/ br
SO HOLLAND. IL • 81LLINGS. MT • BIRMINGHAM, AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER.CO • GOLDEN. CO
HENDERSON. KV • MIDDLESBORO, KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 22S NORTH LA SALLE STREET. CHICAGO, ILLINOIS M«01 • AREA CODE 312 726-1434
jiif^
PLEASE ADDRESS ALL CORRESPONDENCE T*v
16130 VAN DRUNEN RD.. SOUTH HOLLAND IL804S
OFFICE TEL. (312) 204-1178
RVB
A Research-Cottrell Co.
6176 Olson Memorial Highway
Minneapolis, MN 55422
July 3, 1979
Sample identification
by RVB
K r- at
Sample taken by
Date sampled
Date received
Coal
KVB
5/1/79
6/23/79
Test No.;
Sample:
Test Site;
3
Ohio coal
I
Analysis report no. 71-34533
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
3.28
9.15
37.96
49.61
100.00
12881
2.81
xxxxx
9.46
39.25
51.29
100.00
13318
2.91
FUSION TEMPERATURE OF At
Reducing
Oxiaumg
Origin*! Copy W«t»rm»rked
For Your Protection
>. Dc'o:mation
,'too.ng (H--W)
xxxx
xxxx '"
xxxx F
xxxx F
74
xxxx r
XXXX 'f » Con»H,.9h,
xxxx i?
xxxx F
Rwpecttulty submltMd.
COMMERCIAL TgSTING A ENGINEERING CO.
R. A
«0. HOLLAND. IL • MLLINOl. MT • limNNOHAM. AL • CHAKLiSTOH.MV • CUM
I.WV •CLEVELAND. OH •OCMVEH, CO'OOlDtN. CO
<»*nit Mtmtatr
RAH/ br
Ml NOEMON. K V • MOOLCIKMO. KV • MOWLE. Al • NEW OMLfAM. LA • NOKfOLK. VA -HKSVILLE. KV - VANCOUVER. •£. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 22S NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60W1
AREA CODE 312 726-6434
KVB
A Researoh-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB
5/1/79
6/23/79
Test No. 4
Sample: Ohio Coal
Test Site: I
Analysis report no. 71-34535
PROXIMATE ANALYSIS
As Received Dry Basis
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/lb.
% Sulfur
3.50
10.37
38.61
47.52
100.00
12660
2.83
xxxxx
10.75
40.01
49.24
100.00
13119
2.93
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H = W)
Softening (H = %W)
Fluid
Original Copv Watt rmarked
For Your Protection
XXXX °F
xxxx °F
XXXX °F
XXXX "F
xxxx °F
XXXX °F
xxxx °F
XXXX °F
75
H = Con* HdgM
W « Con* Width
Respectfully submitted.
COMMERCIAL TESTING & ENGINEERING CO.
Charter Mambar
RAH/ br
SO HOLLAND. IL . KILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. KV • MIDOLES8ORO. KV • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • HKEVILLE. KV • VANCOUVER. B£. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601 AREA CODE 312 726-9434 \j
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND IL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal Test No. 5
Sample: Ohio Coal
Test Site: I
— — — —
KVB
5/2/79
6/23/79
Analysis report no. 71-34536
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.69
10.58
38.05
48.68
100.00
12739
2.98
xxxxx
10.87
39.10
50.03
100.00
13091
3.06
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
Initial Deformation
Softening (H = W)
Softening (H = VzW)
Fluid
Original Copy Watermarked
For Your Protecnon
xxxx °P
XXXX r
XXXX °F
XXXX °F
XXXX "F
f£
xxxx F
xxxx °F
xxxx °F
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
V
a A
RAH/ br
SO HOLLAND IL • Bl LLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. KY -MIDOLESBORO. KY • MOBILE AL • NEW ORLEANS, LA • NORFOLK. V» • PIKEVILLE. KY • VANCOUVER. B£. CAN.
Charter M«mb«r
-------
F 462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-S434
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB
5/8/79
6/23/79
Test No. 6
Sample: Ohio Coal
Test Site: I
Analysis report no. 71—34538
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.67
9.38
37.84
50.11
100.00
13024
2.28
xxxxx
9.64
38.88
51.48
100.00
13381
2.34
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
Initial Deformation
Softening (H = W)
Softening (H = V2W)
Fluid
Original Copy Watermarked
For Your Protection
XXXX °F
XXXX °F
XXXX °F
XXXX °F
77
XXXX F
XXXX F
XXXX F
XXXX CF
Respectfully subrtn
COMMERCIAL TfS
R. A HOUSER, Manager. Midwest Division
Charter Member
RAH/ br
SO. HOLLAND. IL • BILLINGS, MT* BIRMINGHAM, AL • CHARLESTON. WV - CLARKSBURG. WV - CLEVELAND. OH - DENVER. CO- GOLDEN. CO
HENDERSON, KY-MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS, IA • NORFOLK, VA • PIKCVILLE. KY - VANCOUVER, B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60601 • AREA CODE 31Z 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND. IL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research-Cottrell Co.
6176 Olson Memorial Highway
Minneapolis, MN 55422
July 25, 1979
Sample identification
bV KVB
Kind of sample Coal
reported to us
Sample taken at
Sample taken by KVB
Date sampled ——
Date received 6/23/79
Sample
Test Site: I
Test 19
Analysis report no. 71-34539
PROXIMATE ANALYSIS
As Rec'dDry Basis
ULTIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.96
8.37
38.15
50.52
100.00
13308
1.88
xxxxx
8.63
39.31
52.06
100.00
13714
1.94
As Rec1?^ Dry Basis
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen(diff)
2.96
72.62
.97
4,
1,
26
0.40
1.88
8.37
7.54
100.00
xxxxx
74.83
5.12
1.30
0.41
1.94
8.63
7.77
100.00
Original Copy Watermarked
For Your Protection
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
78
R. A. HOUSER, Manager, Midwest Division
Charter Member
RAH/br
CO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. KV • MIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KV • VANCOUVER. §C CAN.
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Co.
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
August 13, 1979
Sample identification
by KVB, Inc.
Kind of sample Coal
reported to us
Sample taken at Site I
Sample taken by KVB, Inc.
Date sampled
Date received
Kentucky Coal
Site I
Test #10
Analysis report no. 71- 34541
PROXIMATE ANALYSIS
ULTIMATE ANALYSIS
As Rec'd Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.47
5.23
39.38
52.92
100.00
14053
1.43
xxxxx
5.36
40.38
54.26
100.00
14409
1.47
As Rec'd Dry Basis
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen(diff)
2.47
76.57
5.34
1.51
0.13
1.43
5.23
7.32
100.00
xxxxx
78.51
5.48
1.55
0.13
1.47
5.36
7.50
100.00
Original Copy Watermarked
For Your Protection
79
Respectfully submitted,
COMMERCIAlXtSTING & W4GINEERING CO.
R. A. HOUSER, Manager, Midwest Division
RAH/dh
SO. HOLLAND, IL -BILLINGS, MT • BIRMINGHAM, A L • CHARLESTON, WV • CLARKSBURG, WV * CLEVE LAND. OH • DENVER, CO 'GOLDEN, CO
HENDERSON, KY • MlDOLESBORO, KY * MOBILE, A.L • NEW ORLEANS, LA * NORFOLK. VA - P1KEVILLE, KY • VANCOUVER. B.C. CAN.
Charter Member
-------
F 462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 221 NORTH LA SALLE STREET. CHICAGO, ILLINOIS «0601
AREA CODE 312 728-M34
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD.. SOUTH HOLLAND IL 60473
OFFICE TEL (312)264-1173
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
t>V KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal Test No. -14
Sample: Kentucky Coal
Test Site: I
«»_«-»
KVB
5/14/79
6/23/79
Analysis report no. 71-34542
PROXIMATE ANALYSIS
As Received Dry Baals
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.10
7.32
37.87
52.71
100.00
13558
1.75
xxxxx
7.48
38.68
53.84
100.00
13849
1.79
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H a W)
Softening (H = ViW)
Fluid
Original Copy WiMrnwrktd
For Your Protection
Oxidizing
XXXX °F
°C
xxxx p
xxxx °F
xxxx Of
Respectfully submitted.
COMMERCIAL TKTINQ &
H = Con* Height
W = Con* Widlti
INEERINQ CO.
80
R. A. HOUSER, Manager, Midwest Division
RAH/ br
10. HOIUMO. II • WLLINO*. MT • KHWNOHAM. AL • CHARLEITOM. «V • CLAHKMIMO. WV • CLEVCLAMD. OH • DENVER. CO • OOtOtN. CO
HINOfMON. KV • MIOOliSWNIO. KV • MOWLE. At . NCWOHCEANt. LA • NORFOLK. V* • MKCVILLC. KV • VAMCOUVEM.«JC.CAM.
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES; J28 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB
5/22/79
6/23/79
Test No. 15
Sample: Kentucky Coal
Test Site: I
Analysis report no. 71—34544
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/lb.
% Sulfur
2.50
6.14
38.38
52.98
TOO.00
13687
1.46
xxxxx
6.30
39.36
54.34
100.00
14038
1.50
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
Initial Deformation
Softening (H = W)
Softening (H = ¥2W)
Fluid
Original COPY W»e'marked
For Your Protection
xxxx °F
XXXX CF
XXXX °F
XXXX °F
81
XXXX CF
XXXX °F
XXXX °F
XXXX CF
Respectfully submitted,
COMMERCIAL TBiTING & ENGINEERING CO.
R. A. HOUSER, Manager, Midwest Division
Charter M«mt»r
RAH/ br
SO HOLLAND IL • BILLINGS Ml • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV -CLEVELAND. OH • DENVER.CO • GOLDEN. CO
HENDERSON. KY • MIDDLESBORO. KV • MOBILE. AL • NEW ORLEANS, LA • NORFOLK. VA . PIKEVILLE KV • VANCOUVER. B.C.CAN.
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60W1 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
July 3, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB
5/24/79
6/23/79
Kentucky Coal
is
PROXIMATE ANALYSIS
Analysis repo rtno. 71-34549
MINERAL ANALYSIS
As Received Dry Basis
%Moistore
%Ash
%Volatile
%Fixed Carbon
Btu/lb.
%Sulfur
1.97
5.45
39.53
53.OS
100.00
13995
1.33
5.56
40.32
54.12
100.00
14276
1.36
ULTIMATE ANALYSIS
As Received
Moisture 1.97
Carbon 77.88
Hydrogen 5.22
Nitrogen 1.49
Chlorine 0.13
Sulfur 1.33
Ash 5.45
Oxygen (diff) 6.53
100.00
SULFUR FORMS % We
As Received
%Pyritic Sulfur 0.55
%Sulfate Sulfur 0.02
%0rganic Sul . (dif ) 0.76
Fouling Index = 0.35
Slagging Index = 0.49
Original COPY Wit«rm»rk«d
For Your Protection
Dry Basis
xxxxx
79.44
5.33
1.52
0.13
1.36
5.56
6.66
100.00
ight
Dry Basis
0.56
0.02
0.78
Silica,
Alumina, I
Titania,
Sio-
% Weight
Ignited Basis
Ferric
oxide,
Lime
Magnesia,
Potassium oxide.
Sodium oxide, Na
23
CaO
MgO
K20
Sulfur trioxide, SO-j
Phos. pentoxide, Po°5
Strontium, SrO
Barium, BaO
Manganese oxide, Mn.,0.
Undetermined
42.
25.
1.
18.
2.
0.
1.
0.
3.
0,
0.
0,
0.
57
24
59
87
99
75
,48
96
08
26
18
36
02
Na2O
Alkalies as
Dry Coal Basis
Sixica Value =
Base:Acid Ratio =
T250 Temperature =
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
r 1.65
100.00
0.11
65.31
0.36
2460°F
82
R. A.
R, Manager, Midwest Division
RAH/ br
SO. HOLLAND. IL • BlLLINOt, MT • BIRMINGHAM. AL • CHARLESTON. IW • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO• GOLDEN. CO
HENDERSON. K V •MIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA - NORFOLK. VA • MKEVILLE. KY • VANCOUVER. BjC. CAN.
Ch«rt«r Memoir
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL (312) 264-1173
KVB
A Research Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
July 24, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB
5/24/79
6/23/79
Kentucky Coal
COMPLETED REPORT
Analysis report no. 71-34549 (Page 2 of 2)
FUSION TEMPERATURES OF ASH
Reducing
Initial Def., IT 2065°F
Softening, ST 2235°F
Softening, HT 2415°F
Fluid, FT 2575°F
Ofioinal Copy Watermarked
For Your Protection
Respectfully submitted,
COMMERCIALj£9riNG & ENGINEERING CO.
83
R. A. HOUSER, Manager, Midwest Division
RAH/bl?0. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. IW •CLEVELAND,OH • DENVER. CO • GOLDEN. CO
' HENDERSON. KY • MIDOLESBORO. KY • MOBILE. AL • NEW ORLEANS, LA • NORFOLK.VA • PIKEVILLE. KY • VANCOUVER. B.C.CAN.
-------
F-46V
>v
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: ZZ» NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB, INC.
A Hesearch-Cottrell Co.
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us Ohio Coal Composite
Sample taken at Test Site I
Sample taken by KVB
Date sampled -
Date received 6/23/79
July 17, 1979
Sample identification
by KVB
Smr
Analysis report no.
PROXIMATE ANALYSIS As received Dry basis
71- 34547 % Weight
ULTIMATE ANALYSIS As received Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
% Alk. as Na2O
SULFUR FORMS
% Pyritic Sulfur
% Sulfate Sulfur
% Organic Sulfur
WATER SOLUBLE ALKALIES
% Na2O =
% K20 =
FUSION TEMPERATURE OF ASH
3.08
10.07
38.16
48.69
100.00
12718
2.95
xxxxx
1.70
0.06
1.19
xxxxx
xxxxx
Initial Deformation
H is cone Height Softening (H = W)
wiiccnew.dth Softening (H= ViW)
Fluid
°i EQUILIBRIUM MOISTURE =
HARDGROVE GRINDABILITY INDEX =
FREE SWELLING INDEX =
*7hese ignited basis results were used
to calculate undetermined value above
%Strontium oxide, SrO
%Bariura oxide, BaO
xxxxx
10.39
39.37
50.24
100.00
13122
3.04
0.17
1.75
0.06
1.23
Ixidizing
°F
°F
°F
°F
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff)
MINERAL ANALYSIS OF ASH
Silica, SiO2
Alumina, AI2O,
Titania, TiOs
Ferric oxide, Fe2O3
Lime, CaO
Magnesia, MgO
Potassium oxide, K20
Sodium oxide, Na2O
Sulfur trioxide, S03
Phos. pentoxide, P;O5
Undetermined
SILICA VALUE =
BASE: ACID RATiO
T250 Temperature =
3.08 xxxxx
70.30 72.53
4.88 5.04
1.76 1.82
0.16 0.16
2.95 3.04
10.07 10.39
6.80 7.02
100.00 100. Off
% Weight Ignited Basis
38.94
23.04
1.22
27.22
2.39
0.81
1.93
0.33
1.55
034
* ""*^t
2.14*
100.00
56.14
0. 52
2295 °P
%Manganese oxide,
/.....,
index.
Original Copy Watermarked
For Your Protection
Fouli
Slagging index.
0.00
0.04
0.05
0.17
1.52
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
'SER, Manager, Midwest Division
RAH/dh
K>. HOLLAND IL • BILLINGS MT • llflMIMGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV -CLEVELAND. OH • DENVER.CO • GOLDEN. CO
HENDEHKW. KV . MIDOLISBORO. KV • MOBILE AL • Mf*ORLEANS. I* • NORFOLK. VA • P1KEVIU.E. KV • VANCOUVER. B.C. CAN.
Charter M«rnb«r
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 221 NORTH LA SALLE STREET, CHICAGO. ILLINOIS MM1
AREA CODE 312 72«-*434
KVB, INC.
A Research-Cottrell Company
6176 Olson Manorial Highway
Minneapolis, VK 55422
Kind of sample
reported to us Coal
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
July 13, 1979
Sample taken at
Sample taken by
Site I
KVB, me.
Sample! dentifjcation
by KVB, Inc..
Kentucky Coal Composite
Site I
Date sampled -
Date received 6/23/79
Analysis report no.
PROXIMATE ANALYSIS As received Dry basis
xxxxx
6.61
38.69
54.70
100.00
14034
1.46
0.12
0.66
0.03
0.77
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
% Alk. as NasO
SULFUR FORMS
% Pyritlc Sulfur
% Sulfate Sulfur
% Organic Sulfur
2.32
6.46
37.79
53.43
100.00
13708
1.43
xXXXX
0.65
0.03
0.75
71- 34546 % Weight
ULTIMATE ANALYSIS As received Dr
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff)
MINERAL ANALYSIS OF ASH
Silica, SiO,
Alumina, AI3O,
Titania, TiO,
2.32
76.05
5.15
1.40
0.14
1.43
6.46
7.05
100.00
xxxxx
77.86
5.27
1.43
0.14
1.46
6.61
7.23
100.00
% Weight Ignited Basis
43.98
23.64
1.42
WATER SOLUBLE ALKALIES
% Na,0 = xxxxx
% K30 = xXXXX
FUSION TEMPERATURE OF ASH
Initial Deformation
H u cone H«K)hi Softening (H = W)
w ii con. widih Softening (H = Vi W)
Fluid
% EQUILIBRIUM MOISTURE =
HARDGROVE GRINDABILITY INDEX =
FREE SWELLING INDEX =
*These ignited basis results were used
to calculate undetermined value above
%Strontium oxide, SrO
%Barium oxide, BaO
SjManganese oxide,
Original Copy Watermarked
Fof Your Protection
0.05
0.25
0.02
Ferric oxide, Fe,O,
Lime, CaO
Magnesia, MgO
Potassium oxide, KSO
Sodium oxide, Na2O
F
F Sulfur trioxide, SO3
F Phos. pentoxide, P2OS
F Undetermined
SILICA VALUE =
BASE: ACID RATIO
TJJO Temperature =
Respectfully submitted,
COMMERCIAMEESTING &£NGMEERING CO.
17.78
3.44
0.79
1.75
0.73
R. A. HOUSER, Manager, Midwest Division
RAH/dh
SO. HOLLAND. IL-BH.LINCS.MT.«1BMINGH»M.«,L-CHAI11.ESTON.WVCL*RKSBUBG WV • CLEVELAND OH • DENVER CO-GOLDEN CO
HENDERSON. KV .MIDDLESeORO. KV • MOBILE, Al • NEW ORLEANS, LA • NORFOLK. VA • FIKEVILLE. KY • VANCOUVER. B.C.CAN. '
Charter Membar
-------
F 464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60601 • AREA CODE 31Z 726-8434
PLEASE ADDRESS ALL CORRESPONDENf-F TO.
16130 VAN DRUNEN RD., SOUTH HOLLANDIL 60473
OFFICE TEL. (312) 264-1173
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash
KVB
4/28/79
6/23/79
Test No. 1
Sample: Bottom Ash
Site: I
Analysis report no. 71-34525
Dry Basis
%Ash 55.31
%Combustible 44.69
Original Copy Watermarkad
For Your Protection
Respectfully submitted,
COMMERCIAL TfigTING & ENGINEERING CO.
R. A.
R, Manager, Midwest Division
RAH/ br
SO. HOLLAND, II • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKS81MG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN CO
HCNMRSON, Kr 'MIOOLESaORO. Hf • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKCVILLE. KY • VANCOUVER. •£. CAN.
CHartar Mwnbw
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS BOW1
AREA CODE 312 726-8434
SIMCC l»0«
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
June 28, 1979
Sample identification
fay KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash
KVB
4/30/79
6/23/79
Test No. 2
Sample: Bottom Ash
Site: I
Analysis report no. 71—34529
%Ash
%Combustible.
Dry Basis
75.73
24.27
Respectfully submitted,
COMMERCIALJSSTING & ENGINEERING CO.
Oriainal CoPV Watermarked
for Your Protection
R. A. HOUSER, Manager, Midwest Division
Charter Mcmtwr
RAH/ br
SO HOLLAND It • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV -CLARKSBURG. WV -CLEVELAND. OH • DENVER. CO • GOLDEN, CO
HENDERSON. KY • MIOOLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 80601 • AREA CODE 312 728-6434
PLEASE ADDRESS ALL CORRESPONDENCE
16130 VAN DRUNEN RD.. SOUTH HOLLAND llf
OFFICE TEL. (312)
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash Test No.. 3
Sample: Bottom Ash
Site: I
— — — —
KVB
5/1/79
6/23/79
Analysis report no. 71-34534
%Ash ,
%Combustible,
Dry Basis
64.11
35.89
Original Copy Watsrmarked
For Your Protection
Respectfully submitted,
COMMERCIAL-JESTING & ENGINEERING CO.
R. A. HOUSER. Manager, Midwest Division
RAH/ br
SO HOLLAND. IL • BILLINGS. MT • BIRMINGHAM AL • CHARLESTON. WV > CLARKSBUHO. IW • CLEVELAND. OH • DENVER. CO • GOLDEN, CO
HENDERSON. KY • MIOOLESBORO. KY • MOBILE, AL • NEW ORLEANS, LA • NORFOLK, VA • PIKEVILLE. KV • VANCOUVER. B.C. CAN.
Ch«rt.r M«mb«r
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD.. SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
SINCE HOB
m KVB June 28, 1979
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422 Sample identification
by KVB
Kind of sample Ash Test No. 5
reported to us Sample: Bottom Ash
Site: I
Sample taken at
Sample taken by KVB
Date sampled 5/22/79
Date received 6/23/79
Analysis report no. 71-34537
Dry Basis
%Ash 69.18
%Combustible 30.82
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
89
_ .„,-,. copy Watermarked f \~*^ *^f *"* •" "*r~ ^ ^
<£r Your Protection R. A. HOUSER, Manager, Midwest Division
>"Or T u Charter Member
SO. HOLLAND, IL- BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG WV • CLEVELAND OH • DENVER CO • GOLDEN CO
HENDERSON. KY • MIDOLESBOHO. KY • MOBILE. AL-NEW ORLEANS. LA-NORFOLK VA • CIKEVILLE KV • VANCOUVER BC CAN
RAH/ br
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60601 • AREA CODE 312 728-8434*
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND IL 60473
OFFICE TEL. (312) ™
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash
KVB
6/23/79
Test No. 9
Sample: Bottom Ash
Site: I
Analysis report no. 71-34540
%Ash ,
%Combustible.
Dry Basis
64.49
35.51
Original Copy Watermarked
For Your Protection
Respectfully submitted.
COMMERCIAWESTINQ i^NGINEERING CO.
90
R. A. HOUSER. Manager. Midwest Division
RAH/ br
SO HOLLAND. IL • BILLINGS,MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV 'CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. K Y • MIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
Charter M«mbir
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80601
AREA CODE 312 726-8434
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
June 28, 1979
Sample identification
by
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash
KVB
6/23/79
Test No. 15
Sample: Bottom Ash
Test Site: I
Analysis report no. 71-34545
%Ash ,
%Combustible,
Dry Basis
85.86
14.14
Respectfully submitted,
COMMERCIAL TifiTING & ENGINEERING CO.
91
Original Copy Watermarked
For Your Protection
R. A. HOUSER, Manager, Midwest Division
Chtrter Mimbtr
RAH/ br
SO HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLABKS8JJRG. WV • CLEVELAND OH • OENVEB CO • GOLDEN CO
HENDERSON, KY • HIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK, VA • HKEVILLE. KY . VANCOUVER B.C CAN. '
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 80801 • AREA CODE 312 726-1434
PLEASE ADDRESS ALL CORRESPONDENCE Try
16130 VAN DRUNEN RD.. SOUTH HOLLANDIL 604%
OFFICE TEL. (312) 264-1173
SintCf i»0»
KVB
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
June 28, 1979
Sample identification
by KVB
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash
KVB
6/23/79
Test No. 18
Sample: Bottom Ash
Analysis report no. 71-34543
%Ash
%Combustible.
Dry Basis
81.61
18.39
Original Copy Watermarked
For Your Protection
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A
RAH/ br
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM, Al • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. K V . MIDDLESBORO K V • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA > HKEVILI.E. K Y • VANCOUVER. B.C. CAN.
.
Charter Member
-------
SITE
COMBUSTIBLES DATA SHEET
rucible
Number
Sample
Origin
Crucible
Weight
grains
Crucible &
Sample Weight
Post 110°C gms
Sample
Weight
grams
Post 750°C
crams
A Weight
grams
Combus
tibles
TB6T*/
/». 3674
J6. W 72.2-
AVG.
J,
f. 64
AVG.
1, 7V7*
AVG.
/ff. 4o to
/».
A\
AVG.
n
2Ti>
it
AVG.
AVG.
AVG.
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KVB
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DATE SAMPLE TAKEN
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-------
SECTION 6,0
OVERFIRE AIR TRAVERSES
PAGE
6,1 OVERFIRE AIR DATA SHEETS 108
107
-------
SMOKESTACK FLOW PROFILE
TEST NO. //
LOCATION N0._
DATE
si-re-
SAMPLING LOCATION f=Kt,nr
INSIDE OF FAR WALL TO /? '/% "
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE,
BAROMETRIC PRESS, in.H
(DISTANCE B)
STACK PRESS.,Ps , iwg
STACK I.D. (DISTANCE A - DISTANCE B) /fr'/fr STK. GAS SP.
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
GRAVITY,G
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
6.
7.
8.
9.
10. SrtH-lC.
11.
12.
13.
14.
15.
16.
17.
18.
fty^rave
* OF STACK
DIAMETER
3:^
/*.«-
tf'-f
Si-*
tr?
J0>t
«ir
-«r
STACK GAS , Vs - 174 Ffi
SPEED
DISTANCE
FROM
INSIDE WALL
o.^<6-v 3% = i«
/.i^S+^-1 *S--*44
J.MSr+3^- 6-88
5". 2«-ff «-?*A|« S^
/0^-T*-S»/i(«r/V'fi7
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VELOCITY
HEAD
( Aps), in. HS0
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^'T1 <>.//
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tn ».n
'tZ*
^/4* 4"
Average
VA P(T + 460) 407 1.00 *
-------
SMOKESTACK FLOW PROFILE
TEST NO. _/l
LOCATION NO.
DATE _
SAMPLING LOCATION FBofST
.?,-
"*/*/'*.
OUTSIDE OF NIPPLE, (DISTANCE B)_
STACK I.D. (DISTANCE A - DISTANCE*
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BAROMETRIC PRESS. in.Hg 21 &
B)
J5TACK PRESS.,Ps, iwg_
GAS SP. GRAVITY, GS
~
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
16.
7.
8.
9.
10. SfiftTV^
11.
12.
13.
14.
15.
16.
17.
18.
ftYprflv
STACK
SPEED
% OF STACK
DIAMETER
5.^
/*v5T
/*4
523
^7-7
ffcif
fftr
#».s-
GAS,VS - 174 F
DISTANCE
FROM
INSIDE WALL
4*7
S'44
*#g
g
«.4I «>-^o
e--z^ oa«-
// " //Xi"
>0) 407 l.OQ. ^
f ' '••% / ' \
(pp (Q—)
STACK
TEMPERATURE
(Ts, °F
>/
/
s
{
I
)
j
y
OXYGEN
%
STACK GAS
SPEED, Vs
ft/min
109
60-23
rev. 11/74
-------
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
/5
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO 3*A "
OUTSIDE OF NIPPLE, (DISTANCE B)_
STACK I.D. (DISTANCE A - DISTANCE"
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BAROMETRIC PRESS,in.H
B)/gffi STK
STACK PRESS.,Ps, iwg
GAS SP. GRAVITY,G
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
f>.
7.
8.
9.
10. •y*rx-.
11.
12.
13.
L4.
L5.
16.
L7.
18.
Average
STACK
SPEED
% OF STACK
DIAMETER
31
»r
H"t
3Z3
6*7
;fi»-6
itff
Ce>
060 C£e>
0 tf <9{>3
0.67 <>-63
0^1 d-i^
d'Sr ^> 'S"i
• ^J a4t
6.2/>> 0-42-
/(^ /e>
0) 407 1.00 ~*
(^P <5T~)
STACK
TEMPERATURE
(Ts, °F
&
(.
/
s
/
i
V
V
OXYGEN
t
STACK GAS
SPEED, Vs
ft/min
~~
11 -
110
60-23
rev. 11/74
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
REPORT NO. ,
EPA-600/7-80-136b
3. RECIPIENT'S ACCESSION NO.
TITLE AND SUBTITLE
Field Tests of Industrial Stoker Coal-fired Boilers for
Emissions Control and Efficiency Improvement--
Site I (Data Supplement)
5 REPORT DATE
May 1980
6. PERFORMING ORGANIZATION CODE
AUTHOR(S)
J.O.Burlingame, R.A.Parker, J.E.Cook,
W.M.Jackson, and J.D.Demont
8. PERFORMING ORGANIZATION REPORT NO
PERFORMING ORGANIZATION NAME AND ADDRESS
KVB, Inc.
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
1O. PROGRAM ELEMENT NO.
EHE-624
11. CONTRACT/GRANT NO.
EPA-IAG-D7-E681 and
DoE-EF-77-C-01-2609
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development*
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT A
Supplement; 4-
IOD COVERED
14. SPONSORING AGENCY CODE
EPA/600/13
is. SUPPLEMENTARY NOTES (*)Cosponsors are DoE and the American Boiler Manufacturers
Assn. Project officers are R.Hall (EPA) and W. Harvey Jr. (DoE). The final tech-
nical report is "a" of this same series.
16. ABSTRACT Tne pata Supplement is a compilation of test data presented in greater de-
tail than was practical in the fir-1 technical report. It is intended to provide the
necessary details to other researchers who are interested in performing the'r 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 proce-
dures, interpretations, and conclusions. The final technical report also contains
data summaries not found in this Supplement. The Supplement contains panel board
data for each test, detailed particulate, O2, CO2, NO, SO2, and SOS
data, particle size distribution data, chemical analysis of the coal, coal size consis-
tency data, and combustible analysis and overfire air traverse data.
17.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.IDENTIFIERS/OPEN ENDED TERMS
COSATl Field/Group
Air Pollution
Boilers
Combustion
Coal
Field Tests
Dust
Stokers
Improvement
Efficiency
Flue Gases
Fly Ash
Particle Size
Nitrogen Oxides
Sulfur Oxides
Air Pollution Control
Stationary Sources
Combustion Modification
Spreader Stokers
Particulate
Overfire Air
13B
13A
21B
21D
14B
11G
07B
'13. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS {This Report,
Unclassified
21. NO. OF PAGES
119
20 SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
111
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