ABMA
American
Boiler Manufacturers
Association
1500 Wilson Boulevard
Arlington VA 22209
Do I
United States
Department
of Energy
Division of Power Systems
Energy Technology Branch
Washington DC 20545
EPA
U.S. Environmental Protection Agency
Office of Research and Development
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA 600 7 80 065b
April 1980
Field Tests of Industrial
Stoker Coal-fired Boilers
for Emissions Control and
Efficiency Improvement —
Site F (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-600/7-80-065b
April 1980
Field Tests of Industrial Stoker Coal-fired
Boilers for Emissions Control and
Efficiency Improvement — Site F
(Data Supplement)
by
R.J. Tidona, H.L Stix, J E Cook,
and M G Gabriel
KVB. Inc
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
IAG/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, 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, SC>2 and 803 data, particle
size distribution data, chemical analysis of the coal and coal size
consistency data.
KVB 15900-535
11
-------
TABLE OF CONTENTS
Section Page
FOREWORD iv
CONVERSION FACTORS v
1.0 PANEL BOARD DATA 1
1.1 Control Room Data Sheets 2
2.0 PARTICULATE DATA 73
2.1 Particulate Data Summary 74
2.2 Particulate Data Sheets 76
2.3 Particulate Lab Worksheets 96
3.0 GASEOUS DATA 116
3.1 Gaseous Emission Summary 117
3.2 Gaseous Emission Data Sheets 120
3.3 SOx Data Sheets 141
4.0 PARTICLE SIZE DISTRIBUTION 145
4.1 Brink 146
4.2 SASS 158
4.3 Banco 159
5.0 FUEL AND ASH ANALYSIS 161
5.1 Commercial Testing Analysis 162
5.2 Combustibles Analysis 196
5.3 Coal Sieve Analysis 198
iii
-------
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 F; as it is the sixth 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 F."
KVB 15900-535
IV
-------
CONVERSION FACTORS
ENGLISH AND METRIC UNITS TO SI UNITS
To Convert From
in
ft
ftj
Ib
Ib/hr
lb/l06BTU
g/Mcal
BTU
BTU/lb
BTUAr
J/sec
JAr
BTU/ftAr
BTU/ftAr
BTU/ft2Ar
BTU/ft2Ar
BTU/ft3/hr
BTU/ft3/hr
psia
"H20
Rankine
Fahrenheit
Celsius
Rankine
FOR TYPICAL COAL FUEL
ppm @ 3% O2 (S02)
3% 02
3% 00
(S03)
02 (NO)*
02 (N02)
02 (CO)
ppm @ 3% 02 (CH4)
ppm (?
ppm @
ppm @ 3%
ppm @ 3%
To
cm
cm2
m
m-1
Kg
Mg/s
ng/J
ng/J
J
JAg
w
w
w
W/m
JAr/m
W/m2
JAr/m2
W/m3
JAr/m3
Pa
Pa
Celsius
Celsius
Kelvin
Kelvin
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
(lb/!06Btu)
(Ib/lO^Btu)
(lb/106Btu)
(lb/106Btu)
(lb/106Btu)
(lb/l06Btu)
Multiply By
2.540
6.452
0.3048
0.09290
0.02832
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 = 5/9R-273
C = 5/9(F-32)
K = C+273
K = 5/9R
0.851
(1.98xlO~3)
1.063
0.399
0.611
0.372
0.213
(2. 47x10- 3)
(9.28xlO~4)
(1.42xlO~3}
(8.65xlO"4)
(4.95xlO~4)
*Federal environmental regulations express NOx in terms of N02;
thus NO units should be converted using the NO2 conversion factor.
KVB 15900-535
-------
CONVERSION FACTORS
SI UNITS TO ENGLISH AND METRIC UNITS
To Convert From
cm
cm2
m
m3
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
FOR TYPICAL COAL FUEL
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
To
in
in2
ft
ftj
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
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
ppm @ 3% 02 (S02)
ppm @ 3% 02 (S03)
ppm @ 3% 02 (NO)
ppm @ 3% 02 (NO2)
ppm @ 3% 02 (CO)
ppm @ 3% O2 (CH4)
1.18
0.941
2.51
1.64
2.69
4.69
KVB 15900-535
VI
-------
SI PREFIXES
Multiplication
Factor Prefix SI Symbol
1018 exa E
1015 peta
1012 tera T
10;! giga G
10 mega M
103 kilo k
10 hecto* h
101 deka* da
10 deci* d
10"2 centi* c
10~3 milli m
10"^ micro y
10~9 nano h
10~12 pico p
10~15 femto f
10"18 atto a
*Not recommended but occasionally used
KVB 15900-535
Vll
-------
EMISSION UNITS CONVERSION FACTORS
FOR TYPICAL COAL FUEL (HV = 13,320 BTU/LB)
Multiply
To ^-\ By
Obtain
% Weight
In Fuol
lbs/106Btu
SO-
NO-
% Weight in Fuel
S N
1.50
2.47
lbs/l06Btu
SO2 N02
0.666
0.405
grams/106Cal
SO 2 NO2
0.370
(.556)
13.2x10
0.225
19.8xlO~4
(.556)
PPM
(Dry @ 3% O2)
SOx NOx
-4
5.76xlO"4
14.2xlO~4
Grains/SCF .
(Dry "?
SO 2
N'O
1.48
.903
(2.23)
(2.23)
SO-
2.70
grams/106Cal
(1.8)
NO-
4.44
sox
PPM
(Dry @ 3% O2)
NOx
758
505
1736
35.6x10
-4
(4.01)
(1.8)
25.6x10
-4
281
704
1127
391
(4.01)
1566
SO-
Grains/SCF
(Dry@12% CO2)
NO-
.676
(.448)
(.249)
8.87x10
-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 15900-535
-------
SECTION 1,0
PANEL BOARD DATA
1,1 CONTROL ROOM DATA SHEETS PAGE 2
-------
Sheet 1 of 4
KVB
Coal Flow, Ib/hr
PANEL BOARD DATA SHEET
ABMA TEST SITE F
--Steam Flow, Ib/hr & Q
FW Flow, Ib/hr £a
Design Capacity 7.5T1
Evaporation . if. 2
TEST NUMBER
DATE
DESCRIPTION
^fi»«» / 4?&>j/j>i*er/'tr'+
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "1^0
Windbox Pressure, "H2O
Furnace Pressure, "H20
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "HpO
'•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
/
/+•/ '^
1&4U*.H<.^i
racit
8ff£ 43
/0 :&,8
\-6.t
/s&
•f 3.4
-"-3
~<£
-/./
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-7.4
/**"
StJ~
/^
3
/^-/^-^
U< o+
^3^
W.IH
Wtfrf
^- tf?' ^.
M'K
+ 1.1
+ \-5
-o^
-I-H
-3.1
-S.3
iH<
L^3
I
-------
i \
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, CF
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Fec-dwater Header Press, nsig
Opacity, % C> -r /o&
CONTROLS
Boiler Master /Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
F-:-ecv;ater Flow
Conoensate Flow
Feedwater Pr^rsure
/
£3.&
6/.&
7S~
S48
3/<5
37-7
£4.e>
/4J~
*es
/?7
s _._._
<£&
5~e
6
^
£/.s~~
7-f,
£3-
51
50
-0,1-
o
LI
.__.??....
^)
_ _ — - ._
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press, "H20
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H20
Rear Lower OFA Press , "H20
Boiler Hopper Reinjection
Pressure, "H2O
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure , "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
1
/
,ifc »
A*-?
sag
''^
^'* _,
6.t
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34,6
y £.6
"* 3*.',
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5
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Sf.1
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Vo
Xl/^
A^(9
^)
i
-------
KV3
KOTES
TEST KO:
I'SST NO:
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr •
LOW. Ib/hr •'-' •:- i •
--Steam Flo
'.+-WW.
FW Flow, Ib/hr
(J™~ <-l*+r4-)
% Design Capacity
Evaporation
TEST NUMBER
DATE
DE SCRIPT ION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "I^O
Windbox Pressure, "HsO
Furnace Pressure, "I^O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "H2O
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
jr
/'*> f
/*tfS>'f- /*>/
ffcnHt ff/ CS.
S**/
gj'ffza
/o/o
&4V027
0.0.3.
/0£><9
/.
-------
1\
vs
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °E
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Kaster/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
^~~
44,
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press, "HjO
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H2O
Boiler Hopper Rein ject ion
Pressure r "HjO
Econ Hopper Reinjection
Pressure . "H2O
Over fire Air Fan
Static Pressure, "HjO
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
1
JT
•**> IP
•*' h.f>
."* in
-*•- G, i
•••* u
•* tb
" 36.0
re*
y*<
£.s~-. s
A/0
4/*
8
-------
\ ' O
« D
PANEL BOARD DATS SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr 34 / 1
-Steam Flow, Ib/hr
, FW Flow, Ib/hr
% Design Capacity £2 ,°l
Evaporation ] / >~7 I
.TEST NUMBER
DATE
DESCRIPTION
- 20-7?
to
/2.-Z8- Vg
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
! FD Fan Pressure, "H9O
i *-
Wiiidbox Pressure, "h"20
_0_.OiJL
10 '
1
78
13 /fc
._!_
-10-
LO
'-1JL
15 v-7
Furnace Pressure, "J^O
Boiler Outlet Pressure, "I^O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, ^HjjQ
PRESSURE GAUGES
Boiler St-iam Pressure, psig
Jt€-\7n Header Pressure, psig
Feedwater Header Pressure, psig
-O.SS
ll£—.
0,55
A.L
fit
__±JX3_
^-777
_O_, j^
If.:-:-,
LHi_
Mr
\ IP
-------
i \
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
j CONTROLS
I Boiler Master/Stoker
Fuel Air Ratio
V3,o
13
S.
HD
2,2-
_.__7
11(9
Forced Draft
Furnace Draft
j Furnace Draft Bias
Economizer By-Pass
Fc-edwater Flow
Condensate Flow
Feedwater Pressure
0
f£_
0
0
300
33.0
fl
~H
—I
0
':/ ..._.
10
-------
KV3
TEST NUMBER
-
STOKER
Front Upper OFA Press , "H20
Front Lower OFA Press, "H2O
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H20
Boiler Hopper Reinjection
Pressure, "H->O
Econ Hopper Reinjection
Pressure, "H2O
Overfire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
!
FURNACE
Ash Bed Thickness, inches
i. Clinker Formation, YES/NO
i
Visible Smoke?
h
H^,/3<3
o.X
1-7
,0\0
/•I
O.l">
l,.H
tf.vH
M
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$•1
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0.35
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11
-------
'•'
V
PANEL BOARD DATA SHEET
A3MA TEST SITE F
Coal Flow, lb/hr__702
-Steam Flow, lb/hr
FW Flow, lb/hr .
% Design Capacity ^ 7> "7
Evaporation //O 7 rz
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
•
i
DRAFT GAUGES
FD Tan Pressure, "K20
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "I^O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H20
*
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Fcedvater Header Pressure, psig
* sKo« U rv.A ~0.lfl
10
\'^-~>el
Btetu^z
0Mi01
\l:&,
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~J.3^
_^ta_—
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1^6
2L3I
-------
t\
TFFT \T: '.'•"? FF
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, ~f
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Fe&dvater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
F&edvater Flow
Condensate Flow
Feedwater Pressure
10
^0,0
J«
Hoo
$1
113-
_^>30
113-
^>
70 .. _
5?
^
._ .S7.
-a oo
0_
7^f
^
^/
JO
J7SQ_
J^t9
7-^L_
^05-
320
^00
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J<
9K
^05
J.s
..70.
^
?^
£«
-d-PO
5
7^
3^L
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.
I
'i
T
_
13
-------
KV3
TEST NUMBER
STOKER
[0
if
\o
O
Front Upper OFA Press, "H20
Front Lower OFA Press, "H20
Mo
9-V
Rear Upper OFA Press , "H2O
.»$
I,*-)
I-H
Rear Lower OFA Press , "H2O
(,.(*
,1.1-
Boiler Hopper Reinjection
Pressure. "H2O
Econ Hopper Reinjection
pressure. "H20
Overfire Air Fan
Static Pressure, "H2O
JL*1
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
FURNACE
Ash Bed Thickness, inches
31
Clinker Formation, YES/NO
Visible Smoke?
W
W
MO
14
-------
KV3
NO: /O
^a^^-^ff^^
TZST K'O:
•j'EST NO:
15
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr
-Steam Flow, li>/hr_
FW Flow, Ib/hr
% Design Capacity /^» i
Evaporation /O,7
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
'D fan Pressure, "H20
Windbox Pressure, "H->O
Furnace Pressure, "H^O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H2O
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
t
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-------
" \' Q
v V D
iv
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, CF
Feedwater Flow x 1000 Ib/hr
Stearr, Pressure, psig
Feedwater Temp, °F
Feecwater Header Press, psig
Opacity, %
f.D. FAiJ /Mter Ai£.TcHP °/r
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By -Pass
Fe&dwater Flow
Condensate Flow
Feedv:ater Pressure
r "
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-------
1.' M
i\ V
TEST NUMBER
STOKER
Front Upper OFA Press , "H20
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H20
Rear Lower OFA Press, "H20
Boiler Hopper Reinjection
_?ressure. "H2O
Econ Hopper Reinjection
._ Pressure. "H20 ....
Overfire Air Fan
__st.atic Pressure, "H20
Boiler Hopper Reinjection,
_ _ YES/NO
Fconomizer Hopper
R-2 injection, YES/NO
JL.
1.1
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/*/•/
u
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
A)0
-7.6
X9
3
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NO
3_
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18
-------
KV3
KOTES
rEST NO:
TEST NO:
/» < g ^ - ^ y )
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TEST NO:
TEST NO:
TEST NO:
19
-------
Shi-tt 1 of 4
KV3
PANEL BOARD DATA SHEET
AB.MA TEST SITE F
? 7_3
Coal Flow, lb/hr_ "73 ,
--Steam Flow, Ib/hr
FW Flow, Ib/hr
% Design Capacity
Evaporation /^. 9
TEST NUMBER
r __.
i DATE
DESCRIPTION
j
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "r^O
Windbox Pressure , "H2O
Furnace Pressure, "t^O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
i Dust Collector
Outlet Pressure, "H20
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Fr-odvkater Header Pressure, psig
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_
-------
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, DF
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, c
Feecwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Heaaer Press, psig
Opacity, % **"
CONTROLS
j Boiler Master/Stoker
i
Fuel Air Ratio
rorcec Draft
I ~
! Furnace Draft
i
r~
i
Furnace Draft Bias
Economizer By-Pass
F&ecwater Flow
Concierssate Flow
Fe?dwater Pressure
t^Qi.
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400
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0
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21
-------
TEST NUMBER
STOKER
Front Upper OFA Press, "t
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H20
Rear Lower OFA Press, "H20
Boiler Hopper Reinjection
J'EoQ —-
Econ Hopper Reinjection
Pressure. "H20
Overfire Air Fan
Static Pressure, "H20
Boiler Hopper Reinjection,
YES/NO
economize r Hopper
Reinjection, YES/NO
P
FURNACE
Ash Fed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
3
Oo
13-2
.71
5
j
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1
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA. SHEET
ABMA TEST SITE F
,S
Coal Flow, Ib/hr ~
-Steam Flow, IbAr "7
FW Flow, Ib/hr
% Design Capacity
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "^O
Windbox Pressure, "H2O
Furnace Pressure, "H2O '
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "H2O
»
PRESSURE GAUGES
Boiler Steam Pressure, psig
3team Header Pressure, psig
Feedwater Header Pressure, psig
/fra.
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-------
Sheet 2 of 4
KVB
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °B
Economizer FW Temp Outlet, °E
Economizer Gas Temp Outlet, °E
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, pslg
Opacity, % ^^ ^^J^,
c£ fff\p.-t"^or\
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By -Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
i
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-------
Sheet 3 of 4
KVB
TEST NUMBER
-
STOKER
Front Upper OFA Press , "H2O
Front Lower OFA Press , "H20
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure , "^30
Econ Hopper Reinjection
Pressure, "H20
Overfire Air Fan
Static Pressure , "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
f.1?.f4^ |r»ttf Aift- TkMP. rP
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
lu.
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m /?.fe
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MD
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA- SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr
-Steam Flow, Ib/hr 7^333
FW Flow, Ib/hr
% Design Capacity ft- °^
Evaporation //• 3
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "I^O
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H2O
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
3team Header Pressure, psig
Feedwater Header Pressure, psig
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-
-
-------
Sheet 2 of 4
KVB
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet , °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity , %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By -Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
n
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27
-------
Sheet
of _ 4
KVB
TEST NUMBER
STOKER
Front Upper OFA Press , "HjO
Front Lower OFA Press/ "I^O
Rear Upper OFA Press, "H^O
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure , "Tt^O
Econ Hopper Reinjection
Pressure. "HjO
Overfire Air Fan
Static Pressure. "HjO
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Rein j ection , YES/NO
£D F*«J iiJLer Att TmP. . */-
/
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
1
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J3.fe
iiu
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10
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-------
Sheet 1 of 4
KVB
PANEL BOARD DATA. SHEET
ABMA TEST SITE F
Coal Flow, lb/hr_
-Steam Flow, Ib/hr
FW Flow, Ib/hr
% Design Capacity_
Evaporation
79 3-? 3
//. 0
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H2O
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "^0
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H20
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
Iff
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- -
-------
Sheet 2 of 4
KVB
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °E
Economizer Gas Temp Outlet, °E
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity , %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
11
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30
-------
Sheet 3 of 4
KVB
TEST NUMBER
STOKER
Front Upper OFA Press , "H2O
Front Lower OFA Press, "H2O
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure. "H2O
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure. "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
f.Q. FA* 2.*><.{J A i *- -Tt™ P- . 6F
FURNACE
Ash Bed Thickness , inches
Clinker Formation, YES/NO
Visible Smoke?
- -
n
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5,0
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yes
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00
31
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA. SHEET
ABMA TEST SITE F
Coal Plow, Ib/hr "75 '
-Steam Flow, Ib/hr
FW Flow, Ib/hr
% Design Capacity_
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "I^O
Windbox Pressure, "H2O
Furnace Pressure, "I^O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H?0
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
"5team Header Pressure, psig
Feedwater Header Pressure, psig
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-3.3
-13
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3vt)>
—
-------
Sheet 2 of 4
KVB
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °B
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °E
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
h
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33
-------
Sheet 3 of 4
KVB
TEST NUMBER
STOKER
Front Upper OFA Press, "H2O
Front Lower OFA Press, "H2O
Rear Upper OFA Press , "H20
Rear Lower OFA Press, "H20
Boiler Hopper Reinjection
Pressure , nK-jp
Econ Hopper Reinjection
Pressure. "HsO
Overf ire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
/,E>. fA»o //o^r /^ f^P.^p
FURNACE
Ash Bed Thickness , inches
Clinker Formation, YES/NO
Visible Smoke?
. ._
11
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34
-------
Sheet 4 of 4
KVB
TEST NO:
NOTES
/) A / C
TEST NO:
TEST NO:
TEST NO:
TEST NO:
35
-------
S:,e.:-t 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, lb/hr_
-Steam Flow, Ib/hr
FW Flow, Ib/hr
% Design Capacity "7 */. "7
Evaporation /'•*/
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H2O
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "HpO
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H20
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feodwater Header Pressure, psig
30
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-
36
-------
KV3
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Eoonomirer Gas Temp Inlet, °F
Econoirdzer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedvater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
For ceo Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedvater Pressure
c9o
W.O
Jfl*
lo
_£3tf .
-.3.LO .
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fe»(5
__13r _
&0
\
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press, "HjO
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "HjO
Boiler Hopper Reinjection
Pressure. "H2O
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
Ai/L
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
ao
IF
16-0
5-0
4'A
•ou
-'?
•30
t'O
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H
1
38
-------
KV3
NOTES
^fl
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TEST NO:
7EET ?;0:
:-S£T NO:
39
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA. SHEET
ABMA TEST SITE F
Coal Flow, lb/hr_
-Steam Flow, Ib/hr 6 / 11 (a
FW Flow, Ib/hr
% Design Capacity_
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "f^O
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H?O
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
^/
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\
-------
Sheet 2 of 4
KVB
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °I
Economizer FW Temp Outlet, °B
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master /Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
31
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41
-------
Sheet 3 of 4
KVB
TEST NUMBER
-
STOKER
Front Upper OFA Press , "t^O
Front Lower OFA Press, "H2O
Rear Upper OFA Press, "H20
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure , "HaQ
Econ Hopper Reinjection
Pressure. "H2O
Overf ire Air Fan
Static Pressure r "H20
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
F#. fy/j IUI&T ftta. Tvwf *>?•
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
1\
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I2A
0/5 C,
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1-7
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-------
Sheet 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr ^, ? J 7. 5
-Steam Flow, Ib/hr 7 ? V 7 3
FW Flow, Ib/hr __
% Design Capacity
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H2O
Windbox Pressure, "H2O
Furnace Pressure, "H20
Boiler Outlet Pressure, "I^O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "H2O
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
~team Header Pressure, psig
Feedwater Header Pressure, psig
3*
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43
-------
Sheet 2 of 4
KVB
TEST NUMBER
-
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
i
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44
-------
Sheet 3
of
KVB
TEST NUMBER
-
STOKER
Front Upper OFA Press , "H20
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H2O
Rear Lower OFA Press , "H2O
Boiler Hopper Reinjection
Pressure. "H^O
Econ Hopper Reinjection
Pressure. "H?0
Overfire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
{,V ^ i^ieT AifL ~twp , '>p
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
,5 a.
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"* 7.7
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45
-------
Sr.c-et 1 of 4
KV3
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr J" '-j^
- - Steam Flow,
FW Flow, Ib/hr
% Design Capacity I()0>Q
Evaporation / /,'/
£.(-6^,
TEST NUMBER
DATE
DLSCRlrrlON
•
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H20
Windbox Pressure, "H2O
Furnace Pressure, "H2O
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "H20
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
23
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46
-------
f' \ >
I \ V
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
I""
L
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
r
1 Fieawater Flow
Coridensate Flow
Feedwater Pressure
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I
47
-------
KVB
TEST NUMBER
-
STOKER
Front Upper OFA Press , "H^O
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H20
Boiler Hopper Reinjection
Pressure, "HjO
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
£'&•?**) wuT w Tf*Pf'?
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
/?£/*/ jftT/d'O AifL. To £co*JOW
fill t>**fiC*frll>
1 fa>» 0M*CIS t'<*U'l> U»fi
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'
-------
KVS
NOTES
TEST NO:
'JEST NO:
J
I TEST NO:
49
-------
Sheet 1 of 4
KV3
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, lb/hr_
- Steam Flow, Ib/hr
FW Flow, Ib/hr
% Design Capacity
Evaporation
/
TEST NUMBER
DATE
DESCRIPTION
w^
9H
3-r-
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
0:30
I£HX
0
rt.fl-S.
O.o. S-
!
-------
:VB
TEST NUMBER
-
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
_^1__
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SI
-------
KVB
TEST NUMBER
STOKER
Front Upper OFA Press , "H^O
Front Lower OFA Press, "H2O
Rear Upper OFA Press, "H2O
Rear Lower OFA Press , "H2O
Boiler Hopper Reinjection
Pressure, "H2O
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure, "H20
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
«.f*0 /wtc^T /^d T£*f ^
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
1
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XI /I
-------
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal. Flow, Ib/hr 7c? 3ff. /
--Steam Flow, Ib/hr
FW Flow, Ib/hr _
% Design Capacity_
Evaporation
TEST NUMBER
DATE
a-*-
DESCRIPTION
4 of A
INTEGRATORS
Ccal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Fet?dwater Flow x 100 Ibs
Time of Reading I 2 11 J I 3'I
tfO/J
Q
DRAFT GAUGES
FD Fan Pressure, "H20
Windbox Pressure, "H20
Furnace Pressure, "H20
4-91,0
I
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Boiler Outlet Pressure, "H2O | _ |,Qn
Economizer Outlet Pressure, "H20
Dust Collector
Outlet^ Pres_sure,_"H2O
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
MP...
S3
-------
t\
VB
TEST NUMBER
...
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, DP
Economizer FW Temp Outlet, °P
Economizer Gas Temp Outlet, °f
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
?&
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1
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
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70
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0
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54
-------
KV8
TEST NUMBER
STOKER
Front Upper OFA Press , "H^O
Front Lower OFA Press, "I^O
Rear Upper OFA Press, "H20
Rear Lower OFA Press, "H20
Boiler Hopper Rein ject ion
Pressure, "HoO
Econ Hopper Rein ject ion
Pressure. "H20
Overfire Air Fan
Static Pressure, "H2O
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
t$jl^ J^^f.M^ T^P; "?
T~
|_
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
31A _
O.qo ;| ,
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4.1c
OAI - . ,j
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i
-------
Sro-i-t 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow,
Steam Flow, Ib/hr 7^7 0B
FW Flow, Ib/hr
% Design Capacity /?•*/
Evaporation j / . t^
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ubs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "I^O
Windbox Pressure, "H20
Furnace Pressure, "I^O
1
j Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H2O
Dust Collector
Outlet Pressure, "HpO
•
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
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202.
— —
-------
KVR
t\ * ?j
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °1
Economizer FW Temp Outlet,
Economizer Gas Temp Outlet, °f
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, osia
Opacity, %
r
CONTROLS
.
I
j Boiler Master/Stoker
I Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Conder.sate Flow
Feedwater Pressure
__3l.o_
OO
-31
J17__
-DM
._.J2
r
7.0
_Jii
wo
&4&L.
73
L^
0.0 S-
n$L
£>•<).$
60
10
-O.Zo
a
S
-i—
-ft
sr
57
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press, "H2O
Front Lower OFA Press, "I^O
Rear Upper OFA Press , "H2O
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure, "H2O
Econ Hopper Reinjection
Pressure. "H20
Overfire Air Fan
Static Pressure, "HpO
Boiler Hopper Reinjection,
YES/NO
Economizer Hopper
Reinjection, YES/NO
f,D-fiM-> (KittT *t/t. T?M'. *?
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
__. .„ _J
;?
"" IM,
'•'" «.P
_ .
24,
"" /**
••* •?,/
'* /.7
°'" ffO
e.i^
^
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7.®
\,X
3V./
Ve3
Y«S
131
3
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NO
— -
31
4.ifl
13-6
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li_
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31
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wo
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d.>4
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1.7
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w.(
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— ' —
—
— —
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~ '
-
- — - —
' — —
~ "
56
-------
Sheet 1 of 4
KV3
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, Ib/hr
-Ftaain Flow, lb/'hr
FW Flow, Ib/'hr
•o Design Capacity
Evaporation
/»?.3
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
I Time of Reading
0-0 S.
00-S.
DRAFT GAUGES
FD Fan Pressure, "H20
i
! Kindbox Pressure, "H2O
; Furnace Pressure, "f^O
i Boiler Outlet Pressure, "i
-Ll-A
-l.oo
I
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "H20
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Fee-water Header Pressure, psig
__-_L£^
Nl
P-J-33
0 ft.S.
I.O
59
-------
KVB
TEST NUMBER
-
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Air Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, °F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity, %
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias
Economizer By-Pass
Feedwater Flow
Condensate Flow
Feedwater Pressure
I
Aci
^.o
(.6,0
£&
s™
T*>0
1X0
160
13*. J
tee
(K J
o.&.S.
7^
60
tf
10
-0.30
0
^
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*?
w.o
(0.0
£,0
r?o
3oo
3S*
«0
1^
^00
«?OJL^
o.o, s,
7'
$0
ko
10
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0
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ID
M
^
lo.t
uo
$.$
51*1
30S"
7 A f^
^ o ^
^S ^1
/3^
^50
P«5-
0-o.S-
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£0
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10
-0.20
0
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ft
~"
- -.
'
"
_
—
~~
- .
"
~~~
"
"~~"
' •
"—
__
60
-------
KVB
TSST DUMBER
Front Upper OFA Press, "H20
Front Lower OFA Press, "f^O
Rear Upper OFA Press, "H20
I Rear Lower OFA Press , "H2O
Boiler Hopper Reinjection
Econ Hopper Reinjeerion
_Press_uire_, "H.2.Q
Overfire Air Fan
_Static. . Pressure.,... "K^O
Boiler Hopper Reinjection,
YE_S/NO_
"Economizer Hopper
Reinjection, YES/NO
10.0
C.I?
i
FURNACE
r^
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Srroke?
AJO.
D
o-n
-J_'.;..
"7
r.o
21
-~\
61
-------
KVB
NOTES
TEST NO:
TEST NO:
TEST NO:
TEST ?JO:
TEST NO:
-------
' •' \ / i3
i\ * O
PANEL BOARD DATA SHLET
AEMA TEST SITE F
Coal r . ow, IL/hr
- Stsarr. Flow, Ib/hr
FN Flow, Ib/hr
ci D.'-pign Capacity
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
I Feedwater Flow x 100 Ibs
I Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H20
Windbox Pressure, "H2O
\(:o\
0.0.5 •
P-
-79 ?
5A 55
0.0.}
j Furnace Pressure, "H20
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
bust Collector
Outlet Pressure, "H_20
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
-A*>_
.J-M_.
__rl3
^-00
r
.3 PJ. (*L.lOoJ_3fi_L^j
__CL0:-^_
/(>
\ ±2=3—4
3- ,
" °.^Q L
<3. j.
__,_: .ia__
-(*.?
63
-------
KVB
-------
KVB
TEST NUMBER
STOKER
Front Upper OFA Press, "H20
Front Lower OFA Press, "f^O
Rear Upper OFA Press, "H20
Rear Lower OFA Press, "f^O
Boiler Hopper Reinjection
Procure, "HoO
Econ Hopper Reinjection
Pressure. "H2O
Overfire Air Fan
Static Pressure, "H2O
Boiler Kor>per Reinjection,
YES/NO
~ Economizer Hopper
Reinjection, YES/NO
Cr\ T'W It^L-fT /|j|L Tk^Pg *t~
FURNACE
Ash Bed Thickness , inches
Clinker Formation, YES/NO
Visible Smoke?
00
°' 10 <
''* n
*'* S.T.
*'* t.o
*''* r,o
'A 5.0
"^ 3«/./
VA5
^s
7^
3
K>0
NO
>.
'
t
i
\
';
\
i
j
y
1
j
/
/. -
... / .
1
|
/
\
\
W
°'* fo,f
™ *!•!
°'IS 5.3
"'^ f.O
O.I?
M* 1>d
I1/./
Jfe
%&-
^3
5
Wfe
f)»
r
/OS
°*t ^
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011/1 ?,o
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o.ig c
|fl* J3^
Vo
U
3
uo
f\c>
50
!^_4.o.s
A53
"° 5-.J-
tf'M «.o
Ol'* s-.d?
C ^P
'^ 33^
/T5
^3
^
3*L
/oo
MO
65
-------
KV3
TEST NO:
TEST NO:
TEST NO:
7EST NO:
66
-------
S':.-rC-t I cf
KV3
PANEL BOARD DATA SHEET
A3MA TEST SITE F
Coal Flow, Ib/hr _ _5"_3 j£j?, 7
- - Steam Flow , Ib./hr $ ^'^ 7O
FW Flow, Ib/hr —;—
% Design Capacity /S»O
Evaporation //•<*-
TEST NUMBER
DATE
DESCRIPTION
-
OF*
5
11.
. to
LO
INTEGRATORS
Coal Scale x 200 Ibs
130 «|f 3.
U
Time of Reading
13-13
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
6.0 5
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "H2O
Windbox Pressure, "H2O
j Furnace Pressure, "H20
Boiler Outlet Pressure, "H2O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "HsO
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
__ikL
__±I.L_..J
0-7
14$
-u
230
1-0
njf__
D.
A&
— 0&Q—
67
-------
KVB
TEST NUMBER
31
•33
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
(,0.0
Air Flow, %
l. o
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
$10
55-0
Economizer FW Temp Outlet,
Economizer Gas Temp Outlet, °]
310
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
HO
Feedwater Temp, °F
3*0
Feedwater Header Press, psig
Opacity, %
0.0, S.
fl.0-3.
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
68
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press, "H20
Front Lower OFA Press, "H20
Rear Upper OFA Press, "H20
Rear Lower OFA Press , "H2O
Boiler Hopper Reinjection
U__!lHaQ
Econ Hopper Reinjection
_pressure. "H?0 ,
Overfire Air Fan
.qtgtic_Pressure, "H?0 .
Boiler Hopper Reinjection,
YES/NO
'Economizer Hopper
Reinjection, YES/NO
___ 31
6.0$
1.1
i-i i i-
1.1
00
i - - -
11
0.0
1.1
4 oT~
J^
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
AJt)
/u »k^j
MO
_^_
A>0
7
o.or
•Jo
0.35-
o.oj
'•V
MO
1
1
AJQ
69
-------
Sheet 1 of 4
KVB
PANEL BOARD DATA SHEET
ABMA TEST SITE F
Coal Flow, lb/hr_5_3_V J.
-Steam Flow, lb/hr
FW Flow, Ib/hr
% Design Capacity
Evaporation
TEST NUMBER
DATE
DESCRIPTION
INTEGRATORS
Coal Scale x 200 Ibs
Time of Reading
Steam Flow x 100 Ibs
Feedwater Flow x 100 Ibs
Time of Reading
DRAFT GAUGES
FD Fan Pressure, "I^O
Windbox Pressure, "F^O
i
Furnace Pressure, "H2O
Boiler Outlet Pressure, "t^O
Economizer Outlet Pressure, "H20
Dust Collector
Outlet Pressure, "H7O
^
PRESSURE GAUGES
Boiler Steam Pressure, psig
Steam Header Pressure, psig
Feedwater Header Pressure, psig
.
35
-P-XV'7?
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uom OFA
O » o ^r" 1 *>
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L_i!iiL
P I3L
35-
y-iv-^]_
_I^UV3^
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3o-j«f«?i1?
(?.ft,5'
I -7-^
o.£
^ I.
^La_
-0-^
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PIP
_ 3^
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uijn
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+ l.i
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jt£_
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—
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1 •
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- —
" .
~ • —
— _
.
. — »,
— _ i
1
— !
— —
^_ i
70
-------
:vs
TEST NUMBER
CHART RECORDINGS
Steam Flow x 1000 Ib/hr
Mr Flow, %
Excess Oxygen, %
Economizer Gas Temp Inlet, °F
Economizer FW Temp Outlet, °F
Economizer Gas Temp Outlet, "F
Feedwater Flow x 1000 Ib/hr
Steam Pressure, psig
if
T
111
1ST)
ۥ40
ST
J 5/fl_
__!?£
Feedwater Temp, °F
Feedwater Header Press, psig
Opacity,
CONTROLS
Boiler Master/Stoker
Fuel Air Ratio
Forced Draft
Furnace Draft
Furnace Draft Bias I ^-A/g* I
Economizer By-Pass
Feedwater Flow
Conder.sate Flow
Feedwater Pressure
0
0
to
•70
71
-------
KV3
TEST NUMBER
STOKER
Front Upper OFA Press , "H2O
Front Lower OFA Press , "H2O
Rear Upper OFA Press, "H2O
Rear Lower OFA Press, "H2O
Boiler Hopper Reinjection
Pressure. "H2O
Econ Hopper Reinjection
Pressure, "H20
Overfire Air Fan
Static Pressure, "H^O
Boiler Hopper Reinjection,
YES /NO
Economizer Hopper
Reinjection, YES/NO
f ,\) ?K^ /MUT ffllL T€HP op
FURNACE
Ash Bed Thickness, inches
Clinker Formation, YES/NO
Visible Smoke?
\<
°* 1 1,1*
** 1,1
/,
l^° 3(,.0
y^s
y^5
10
3/is
W
iO(?
%
°'Mt1 /J.A
«.^
(>'0$ A V
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''VV ^?
°'31 fcfc
JC^7
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\J^^
7o
2Y^
VO
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—
~~
i
•
,
'
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•
~
~~ • -~
— ~ —
72
-------
SECTION 2,0
PARTICULATE DATA
PAGE
2.1 PARTICULATE DATA SUMMARY 74
2,2 PARTICULATE DATA SHEETS 76
2,3 PARTICULATE LAB WORKSHEETS 96
73
-------
"
LOCATION: AtS/ilA
PARTICULATE DATA SUMMARY
PART I
TEST
NO.
Total
Mass
mgm.
Dry Gas
Volume
ft3
Liquid
Coll.
ml.
Baro.
Press.
"Hg
Static
Press.
"H20
Pitot
AP
"H20
Orifice
AH
"H2O
Stack Gas
Temp.
°R
Excess
02
Sampling
Time
min .
Nozzle
Dia.
in.
Pitot
Factor
n.d.
Fuel
Factor
SCF/10%TU
Flue Gas
MW
g/g mole
30,0
-2 *
lt.1l
77^
521
-ft
88
zfr?
757
21*7
77
21Z-T-
» 7
777*
ff I*
sans
-34.
6,
831
ft
2f.
nzff
33-^4
j /c t •>
2.W4
24. V
-2 b
zi&e.
zy .t
7Z-
12ZI7
21
Z-7-I2-
32 I
72-
44-1
,-zr
-8*7
21
611
feo
-837
-3-fc
283
72-
ff-ulz.
77i
63
Z1 /
71.71,
-3.0
77-
1*7.7
21-74
#15900
rev.
-------
Location
PABTICULATE DATA SUMMARY
PART II
TEST
NO.
LOAD
02
CONDITION
EMISSIONS
lb/10°BTU GR/SCF
LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin.
20,18
6*4
/oo
1*8
/JS
•T-7/
f?-'
>" f' 0
fOO
f-?-/
L.I
&•>'}*>
5&.81
0 ?
21, 1\
H<
44-1
Zt 61.?-
571*
6-17
/.ztz
JO
//*-
ffc'i) V>
(SI+
•37*
17
?v 0
24
fo
7 '53
-5'
r
5.1?
P
HI
•1.7/fe
U-7
91
#15900 Rev.
-------
? AKT1CGL.-.TE
DATA
Sample
Point
/
2-
3
V
5
£
7
r
1 ^
/a
II
/O-
Time
(0*
\
/ **
f
i
i
;
V
72
Averag
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SAMPLE
S = tot
,£J7J
^ « • cent
Leak Check Rate 1SOKIKETICS - ^* "-'l
Sampling Time
Per Point , Mm
Before
After
Vac
in. He
/s
C
TEST KUMEER "*
DATE
OPERATOR
FUEL
SITE
/l-t^-Tr
# ffl407,Hc.
rv.fi n A~*
F
PROBE LOCATION £lC*r, . 01, )
^ETER CONDITIONS
A PS
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Total -2 (3^
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76
tal Vol. H-,0 O(f r.i
-------
F.Z--RTICULATE
DATA
LeaX Check Kj^te
Safnpljno Tiwe j
^er r-cint . f.ir. j Before
vac
in. HQ
s5 1 After
ISOKIKETICS
• ^
\ TEST
Kl'MBtt. '^
OPERATOR
FUEL
SITE
ATII A
jr"
PRQEE LOCATION ''''V'- & '•"
Sample
Point
;
2,
L/
^
6,
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Time
5~
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^TER CONDITIONS
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METES VOL. 1 ;— rd 'Wter
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77
_£ f_^i^r^? /-.crains_
'•/^~T_ . jr^_
<<-/< 4.,
'otaJ Vcl. H-.O '-^. /"T.J
-------
F .VKTI CUL.-.TE
DATA
Leak Chec^ Rate
-------
PART1CULATE
DATA
ftk Check Rate
Vac
in. Ho ft3/
ISOKINTTJCS -
TEST N'.'MBEK / /
Before / 5. /
DATE
OPERATOR
F~
PROBE LOCATION
-------
F.-RTICliLATE
DATA
LeaV Check Rate
1SOK1NETJCS -
Vac
in. Hg
/5
ftVmin
o
,5
TEST
DATE _/
OPERATOR
FUEL
SITE
PROBE
Sample
Point
Time
METER CONDITIONS
A Ps I AH |Heter Reading
,2-7
7775:75
'F
Stack
Probe
Oven
Ir.oinaer!
/JLT
Meter
V»c.
2% 5
3
- 7/
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7
31*
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7V
Cl-
7V
to
£2,
52.
.74
76
72.
fr
Average
1
ETAKT^U
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Vol.. IEric» Vcl. (Start) flVol.(ml)
Stack t'x«ss.
L . __ _J.-~—^-- f-
barometric
Jr £
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otal to--^
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f
&t: 15-
80
Total Vol. H-,0 '_' r!
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hg «t3/"in
JSOKINETICS
TEST NUMBER
DATE >
OPERATOR
FUEL
SITE f_
PROBE LOCATION
Sample
oint
Time
METER CONDITIONS
& H |Meter Reading
Stack.
Probe
Oven
Imoinaers
In Out
Meter
ac.
2.6-
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33
,/J
26'
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t.o
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700
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5
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7-0
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35-
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3/6'
40
3.0
//
If
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3.00
2-0
Average
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HETEK VOL.
Nomograph Setup
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4Hg - Nozdde*!)-
« HjO • ^. j Noz(Actual)-
jmo. Vol. (End) Vol. (start) £,Vol.(ml)
«1
12
• 3
i.
Percent O2 *
o(Start)
Silica
Gel
81
/5^ ? . 5; 7
Total Vol. HjO ^ »«:
-------
PARTICULATE
DATA
Sampling Time
»er Point, Min
Leak Check Rate
Vac
in. Hq ft3
Before
After
1SOKINETICS
/min
» TEST KUMBEB / T
DATE
/./;?^?^
OPERATOR
FUEL
SITE
sVr)f\ Sf
F
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Sample
Point
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3
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7
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f
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Time
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v
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METER CONDITIONS
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-35
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ART
SAMPLE VOL.
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-fc37
Percent
AH
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3*2t> &£
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335
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25$
2.KO
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205
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2-2^
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76
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70
7cJ
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7V
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76
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Inc. Vol.CEnd) Vol. (start) iVol.(ml)
11
13
14
// 2- _ /L>U m / 2_
//7 . /^o
V . O
i^i
Total
olstart)
/£/. £
V
33
^grains
•y. /
Vac.
3.2L
'
'
Total Vol. H,o
-------
PARTI CULATE
DATA
Sampling Time
Leak Check Rate
V
in
-5 After /_
ISOKINETJCS
ac
. Hq ft3/min
f •!,'-
) . £• i-
» TEST
DATE
KUMBEK / /
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OPERATOR
FUEL
SITE
/<-^7x7 /f
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PROBE LOCATION tv'-" <^t ^
Sample
Point
/
2-
3
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£
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7
1
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Average
METER VOL.
METER CONDITIONS •
APS
./-*
Jl
,/J
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END
START
SAMPLE VOL:
cpjtot
,f37
Fei cent
Stack
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AH
.7^
L'2^
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X
TEMPERATURES, 'F
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Press. barometric xwter
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Vol. (End) Vol. (Start) ivol.(ml)
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Total
o(Start>
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^T7
Vac.
/;^
/5
/^
/,e>
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^-tf
2 5
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/f
2^
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1-0
63
Total Vol. H,O ' nl
-------
PARTICULATE
DATA
Sample
Point
/
Z
3
Ll
5
£
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fr
(0
H
11-
Time
*!/•.
i
/
i
^'
Av€rage
HETCD VOL.
Leak Check Rate ISOKINET1CS - % TEST KUMBEB /^
Sampling Time
Per Point, Min
1
;
^ETER CONDITIONS
APS
,u
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,57
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6. 600
END
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SAMPLE VOL,
Cpitot
0 637
Percent
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3* 5?2-/"
335?. 73
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2-35
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65
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^(End)
Total
a (Start)
Total Vol. H.n
>?5
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5=-^
3i-9 .,
Vac.
_
' —
84
-------
DATA
Same-line T:me
Per Point,Mir
Leak Check Rate
Vac
in. tig it^/
JSOKINTTICS -
Before
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PRDEE LOCUTION
F
85
J-*-*-*.
-------
PARTICULATE
DATA
Chech Rate
in. He ft /mm
ISOKK.TTICS -
Sample
Point
Time
METER CONDITIONS
s [ A H |Heter Reading
.25"
'F
Stack
Probe
32 c
Oven
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7"
Meter
PHOEE LOCATION ^r«-"'»'^_ *
Vac.
/ 0
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251
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76
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Stack Vress.
.F37
fcaiomctric
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86
Total Vol. H-,0 tl__
\,
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-------
FARTICULATE
DATA
Leak Check Rate
v«c
in. He ft /ir.in
i so>:: NTT: cs
FUEL f fnn
SITE F~
PROEE LOCATION /^'''
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Sample
Point
Time
METER CONDITIONS
APS
0.13
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2-31
330
75
20
326
75
32-5
75
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-------
FAKTICULATE
DATA
Sample
Point
/
I
3
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5"
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7
f-
f
V
II
t^
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Time
2--* 7
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3-/y
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before
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3
24>o
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35^
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2-7<>
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MTE
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OPER,
FUEL
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12
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-------
FAKTIGUILTS
DATA
al* Cneck Kate
V»c
Sami;l i no 1 jme
^ e r I'o int., .V j r
DATE
OPERATOR
FUEL
PHOEE LOCATION
u. 0.>5
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Meter
^ "}$-/,?$
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57
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•'
3 f ?t,/o
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2- •'
2-- So
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.33
T 5$ 3 "-/i.
TW^TW
12
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Average
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t;c!*.ournph Setui-
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89
Total Vol. H-,0 ._J
-------
Stack I'ress. faaiofnctnc
411. l!a Gauae \ Pressure
TW
iH,
IL'C-
90
Total vol. HjO •3J^'1iS+
-------
DATA
Leak C.'.pck KAte
FUT1. / ,J
SITE
PROEE LOCATION
Sample
Point
Time
METER CONDITIONS
5?
A H JMeter Reading
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Stack
tfaoj.
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I Ir.oinaers
£2-
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7L.
J/0
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2-3
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30*
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76
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02
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91
Total Vol. H,o
-------
I ARTICULATE
DATA
Ltak Check RJle
vac
in. Hq ft'/min
ISOKIKETICS -
TEST KmttEE
DATE
OPERATOR
FUEL /
SITE
PROEE LOCATION
Sample
Point
Time
METER CONDITIONS
APS A"
Meter Reading
Stack
Probe
Oven
Imoinaers
In
Out
Meter
-------
DATA
Sample
Point
/
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\ 1
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ft}
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t^
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Time
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ISOKIf.TTlCE
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in. KG ft /rr.in
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Reading
^'co?- '-'-v
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DATA
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-------
PARTICULATE
DATA
Sampling
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Time
Leak check Rate
JSOKINETJCS •
Vac
in. Hg Jt'/min
After
'<••' J
% TEST
DATE
NUMBER ' J
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KETER VOL.
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75
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*4 3(Endl
Silica y .
Gel 7i- 6 ''
7 >
A~- '-
. 6 . 5'
Tot*]
o(Start)
'- . /5c .
Agrams
/6
Vac.
/,U
J.5
<-/.*-
3.o
5-L/
->.^
/.5
V>
<-' •-/
'.a
2.0
$-0
95
Total Vol. H,O
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
Test Description_
, Outlet)
Box No.
LOCATION
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
100. $(*
HI .(^>
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
Final
Initial
A Vic
ACETONE
RINSE
/
/
/£?-/
M.&/C
CC trtf^C/n
^hSr
FILTER
NO.
/
/
&-'*-*£
.£<&$-
.ff*J-&
,0*S&
.3^7
4eejcffc
ff**»t{
*/*?
f*>o *./
6
&-'&-;»
S=>e>-<&0^
/*« *ffe>y
**?, 4ff/s
J££L31*9
POST TEST WTS.
•jo.// 91
AVG.
A WT.
o. rW
0./7/6
A Vic =
A DgV =
A Mn
36
ml
LOAD
klb/hr
REMARKS:
96
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO.
1
Date //;•' / V'7
Box No.
Test Description_
LOG ATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final _
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2 j
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
ACETONE
RINSE
JT
/*-/#- 7g
•;£
9*7. U&
9-7g
/6o. 7«C^
/(&. ~>ei£l
fvo.l'ltj
,M.'/M
FILTER
NO.
J
/ on t3
o.oV^
ml
ft3
mgm
AOi'.y VJ
-D<. :;-?-'-5
y^r. ^^^
4.46X2
LOAD
0,
REMARKS:
o/ ^j^-y
0/036?
01. OIL!
_Q/.Q363
O.////
^
7^
klb/hr
%
97
3830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date l/g f 7
Test Description_
Box No.
LOCATION F"
Eng.
Dry Gas Meter Vol (ft3)
Fi na 1 _
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
ACETONE
RINSE
2
/- 4- 7?
/M. (,033
/QO. t,052
DRY
FLASK
2L
/-y- 7?
7«.r^»
7>.^J/J'
?? *.?/6
7f 0//
FILTER
NO.
?
//-/r- 7/
.f/^7
. ^7<>3
.HO/
• K02
BLANK
NO.
POST TEST WTS.
1
2
3
4
AVG.
A WT.
/nn.9J7?
sao. 9372
/*>. 9372
JM.K72
0.332/
79.3971
79.3971
79.4973
79.W72
o. 7tfy
0/.2473
o/.wn
QI.IW
o/ if 11
o.v/69
-
A Vic =
A DgV =
A Mn
ml
ft3
mgm
LOAD
02_
klb/hr
f.f
REMARKS:
98
-------
PARTICULATE LAB WORKSHEET
TEST NO./7-r/
Date
Box No-
Test Description
LOCATION^
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
ACETONE
, RINSE
• S 1
//.'
91. ~'M
9Y. •*-•;>?
9.7 ,<
9f. /VJ-y
DRY
FLASK
-•> i; V IQ
.'OO.VT/8
FILTER
NO.
/c
y. ,/-:-
. ';<•• ;>i
*'/. <
• 5 ' -• 1
.?w
BLANK
NO.
POST TEST WTS.
AVG.
A WT.
A Vic
A DgV
A Mn
1
2
3
4
=
?/ *
M77
W>2. 9
9/? fw
9$ MM
9!?. 8^3
9f.n«
OJOI
ml
ft3
mgm
SM au
/M&39
/W.&40
;M. 413$
v.ovt
LOAD
Op
REMARKS:
/. OVM)
/.o^z/
/ WZ2
/.OM
0./9W
xo
L.1
klb/hr
%
99
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date /////
Test Description
Box No.
LOCATION_
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
ACETONE
RINSE
/<
;62.*/m
/a/. *'3t,
•£/. 4''.V.F
Jf)/. 4236>
DRY
FLASK
7
0.1731
ml
ft3
mgm
ST WTS.
99. 7/hr
%
100
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
(Inlet, Outlet)
Box No.
LOCATION_
Eng.
''//'
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
ACETONE
RINSE
&.M
/-;*-?>
/,-£•./'<:<:•
.vj ;...',:>•<>"
/&. >J)>*%
/n?.//on
DRY
FLASK
^r
/-/3-7f
9*. *W
<:*/ <->"*..^'
O-f -f/1
99.92K
FILTER
NO.
^
S-/3-79
.?19f)
.K'\°
. f/90
,xm
BLANK
NO.
POST TEST WTS.
AVG.
A WT.
A Vic
A DgV
A Mn
1
2
3
4
r =
11.7
0&.3V
*f5"3'l.<9
A--. '/:•:';•>
,,-.•.<••",'
Ar-:y :•
/ffl.
-------
PARTICULATE LAB WORKSHEET
TEST NO .
Date
- 79
(Inlet, Outlet)
Box No.
Test Description
LOCATI 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
ACETONE
RINSE
&/0
S-/3-W
/M. 9KQ
/M. 9M't>
/no. 93W
/M.V3V7
DRY
FLASK
#J
S-/.2-79
/Of). 07V3
/M>. 0-?*/t>
/OO. 07&
/M,f)Mt>
FILTER
NO.
9
/ y.r- 79
-*467
. rux
wu
. M67.
BLANK
NO.
POST TEST WTS.
- -,
i. L _ v
AVG.
/ 00-1021
A WT.
.327X\ .321?
A Vic =
A DgV =
A Mn
ml
LOAD
1,1.10
klb/hr
%
mgrn
REMARKS:
102
883°-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO.
i •' •'• / ">'-,
Date // / j.; ' •
Test Description
Box No.
/r /' /
LOCATION " y, ' '
Eng.
Dry Gas Meter vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
'
TARE WT.
1
2
3
4
AVG.
H20 RINSE
ACETONE
RINSE
/tf
/-/7- "f
ft'. />"j
CA K'u \
?>..KM
fS.736 X
DRY
FLASK
-*•
i ' rf
ICC. ( . O
/:\ . (:. '
IOO.LOZO
FILTER
NO.
2-
P-M-IS
.ZVS^T
. 9 V
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Sniet,r0utlet)
\ /
Box No.
Test Description
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.
H2O RINSE
ACETONE
RINSE
X
/-/7-W
99.3339
99.K17
9?.sm
99.3K9
DRY
FLASK
O/
/-/&'7?
/(*. ?.--;r
jy.-/':^
y0i-. ?,V:-'
y^s.^y
FILTER
NO.
'/
.%;?M2
/ 2 > s»'o
11*1
.t&O
BLANK
. NO.
POST TEST WTS.
/flV.'m?
AVG.
A WT.
A Vic =
A DgV =
A Mn
33.9
ml
ft3
mgnv
LOAD
7*2
REMARKS:
104
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. y.J
Date _/• .. .LI.
Test Description_
Box No.
LOCATION --J, '
En9- Jj.V'
Dry Gas Meter Vol (ft3)
Fi na 1__
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.
H20 RINSE
ACETONE
RINSE
¥ 30
\-<1-1°l
10}, III?
/01.IOW
101. I Off
/Q3.lo
/o;.3»57
FILTER
NO.^
.. . >
.5^vr
. Vr'?/,
. ,7-5'X
b.wi
BLANK
NO.
POST TEST WTS.
AVG.
A WT.
A Vic =
A DgV =
A Mn
ml
ft3
mgm
REMARKS :
klb/hr
%
105
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. e?/
Date /'5V- 7^
Test Description
Unlofe, Outlet)
Box No.
7S*% LA**. fiJ'f-
LOCATION
Eng.
•** ', »!,' ft
fl-VW/L /=•
"T; //"V^L-
riFA
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
Final
Initial
A Vic
ACETONE
RINSE
4 £3
/-22-->*
/P2. 101*1
/&';..-&?
/03.1016
kn.Wl<
DRY
FLASK
/^
/- )1 - ^
G r. ">:fg
^!Y^'^
2cr
It.-nsn
FILTER
NO.
to
l'11-Ti
at/92
o. $/i2
0- t/9/
6. «/?tf
BLANK
NO.
POST TEST WTS.
/ 0 ^ . «-/ tf 3
/
AVG.
10),
1-0153
A WT.
A Vic =
A DgV =
A Mn
d.
ml
ft3
mgm
LOAD
REMARKS:
106
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
___ (Inlo*, Outlet)
71 Box No.
LOG ATI ON
Test Description
sJt)/lf)
Eng.
/•?
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
Final
Initial
A Vic
ACETONE
RINSE
#2-
i/3ini
100 &Q51
loo £or?
/oo. COS •)
/M. mr>'
DRY
FLASK
&ZI
//?) h<^
JOZ.^H")
/O >.*>?!/;
/ajP7'/7
/^,?7«Y7
FILTER
NO.
7
\-n-Ti
fl.f&>3
o. 9 ±01
P,\
t±0t>
O.KOZ
BLANK
NO.
_2_
3
POST TEST WTS.
l&L.
AVG.
101.
A WT.
. - -"
A Vic =
A DgV =
A Mn
0,
ml
- 7
LOAD_
°2_
REMARKS:
107
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. c/J
Date 3/ IJTf
Test Description
fcSBSBfcr-Outlet)
Box No.
OPT T.
O'*y
LOCATION /r&tyfl f~
Eng.
^6 £"td »J . ££"> *Jf.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV :
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
.
Final
Initial
A Vic
ACETONE
RINSE
lb
\-w-y*
IOO. ?£ 7J
}i*. Htf
/O0.^56f
/OO. 937A
DRY
FLASK
?
f-^H-T?
97. $3 f /
^.5^27
^9.^74
99. 927 S
FILTER
NO.
73 i
i -JP-->I_
^W«/H
^?. ?5V«L
0.
tov\
&M43
BLANK
. NO.
POST TEST WTS.
SOI. 0236
/Q/.023V
362?
S.07M
J. 0204
AVG.
4 WT.
A Vic
A DgV
A Mn
4.
0.
ml
LOAD
klb/hr
%
REMARKS:
108
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO. <3 3.
Date J - / -
'iff M • d . c .
(Inlet, Outlet)
Box No.
Test Description_
LOCATION_
Eng.
.
A-$ /*) A
Dry Gas Meter Vol (ft3)
Fi na1
Initial_
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO
.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
ACETONE
RINSE
*
;->/--??
ft #£*
^?. 336/5
t7-3S&/
9? ?j? J.
AVG.
A WT.
A Vic =
A DgV =
A Mn
ml
LOAD_
°2_
rngm
REMARKS:
klb/hr
103
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 3 V (Inlet, Outlet)
Date J— H f t»*1tc*iA)(S- Jfi/tTel***
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (mp
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
RINSE
^
2-J-7?
saojm
/ao. y :><'*:
//n '••>••'
100.7 H.*!
DRY
FLASK
//
2 S-7?
99. f to 3
99. MX
?9.ruj*
fy.9o&t
FILTER
NO.
c?
^-S-7«i
/•«9/
/.5a
-------
PARTICULATE LAB WORKSHEET
TEST
Date
Test
Dry
NO. t?V (iiilert, Outlet)
*2--77 Box No.
Description £>V7\ &s QPT DrA
Gas Meter Vol (ft3)
Final
Initial
A DgV
LOCATI ON fl gWA
Eng.
i
~ nRlniH 1 n#s>*><:ui,A*>£-j"
P
- /WkieAj)
Impinger Water Vol (ml)
1 2
Final
Initial
A Vic
3 Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
ACETONE
RINSE
* /9
2-f- 79
9b-iZ?>
98. If7~
9j', <\
O.lLrlO
tf.Tfeoi
0.7fe.3i
^.7t3/
BLANK
NO.
POST TEST WTS.
/• t/
AVG.
A WT.
A Vic =
A DgV =
A Mn
37,
ml
ingm
LOAD_
°2_
REMARKS:
klb/hr
111
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
t, Outlet)
Box No.
LOCATION
Eng.
Test Description
Dry Gas Meter Vol (ft3.)
Final
Initial
A DgV
Final
Initial
A Vic
Inpinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
ACETONE
RINSE
*J
2//I / 71
<7i.&> ~> -r
W. ^7lL
^c?. ff ? 7 Z
%1a-7^
DRY
FLASK
J?
i(\\n\
ibi ,6>6<>' )
, 76V/
, 76 yf
dSKn
BLANK
NO.
POST TEST WTS.
AVG.
A WT.
A Vic
A DgV
A Mn
1
2
3
4
.
.
10
py.12-
s^/V.7
79.W/
.'-,-, c?.V - ,
"-'< *'<' -,-•• t
fy.mt
0,t>~PS
ml
ft3
mgm
/r>6.r3*o
>of-JJ-. ^
16^.^3^
H. $17)
LOAD
0,
REMARKS:
: v-/
/.o /»/
/.o/O
1.0)02
O.Wfl
to >
s.o
klb/hr
%
112
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST
Date
Test
._ ~~
• i -
Dry
folk- DC
NO. - (&OKL, Outlet) LOCATION fi QMfr
^
£.~ /I-79 Box No. Eng. l,'dn*&.
Description
Gas Meter Vol (ft3) Impinger Water Vol (ml)
Final 1 2
Initial Final
A DgV Initial
A Vic
3 Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
ACETONE
RINSE
$
.'.'ii ;-'-.'
vT '"'S 1 1
'',%
9f.?3'0
DRY
FLASK
;r
-•/ii/><
l_^l m '. :'i
if} 1 il)Cn
:0 ! .'7 \(,°
/oi.fn,o
FILTER
NO.
C^"7
?////??
.7^?^
/ 7^ -\^
, ^ 6 3 ,2
^7t3i
BLANK
NO.
POST TEST WTS.
AVG.
ml
mgm
LOAD_
02_
REMARKS:
Xlb/hr
%
113
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. ^ S W
Date 2//T/7?
•>luL, Outlet)
Box No.
LOCATION r C^
Eng.
>A r/f, F
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.
E2O RINSE
Final
Initial
A Vic
ACETONE
RINSE
)*^
2//i n<\
/po. r/i-ttf
/#<>• ^"?>
/ ^~,
JOO,*)!,*) 1
DRY
FLASK
^1
?/"' / "1
," • S '
ft. fry/I
/ o / > O *|
IV.Kto
FILTER
NO.
(a
-/n ; /i
7^/-7
//:./?
/'../ 7
0. ~>(ol~?
BLANK
NO.
-.
POST TEST WTS.
AVG.
A WT.
71 ft.tbW
A Vic =
A DgV =
A Mn
Aid.
ml
LOAD
mgm
REMARKS:
114
8830-5
rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 3^> *
Date 2 / ' ^"(7^
£>£.
Jutefc, Outlet)
Box No.
LOCATION -'/r'/^A '"'' .f
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
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
ACETONE
RINSE
3|
rV/i/^
/>.•'/';->
' " .. "I
/ ••>./
/0?.9?*0
DRY
FLASK
/o -
7 M'/71
"• -•>--'. v .
/<.'-c).^?v •: •/
• '. riS
/fl0.^3«,
FILTER
NO.
7
*s \\f-i
• ics ;
n&si
. 76 -T /
^..7tri
BLANK
NO.
POST TEST WTS.
AVG.
A WT.
0.
A Vic =
A DgV =
A Mn
ml
LOAD
lO.Q
REMARKS:
115
8830-5 rev.
-------
SECTION 3,0
GASEOUS DATA
PAGE
3,1 GASEOUS EMISSION SUMMARY n/
3,2 GASEOUS EMISSION DATA SHEETS 120
3,3 SOx DATA SHEETS
116
-------
GASEOUS EMISSION SUMMARY
Location:_
Fuel:
S'%
fit
It
//Z
O
11-20-1%
It
n
/2-r
77
2? 7
12 7
4+
//Jo
(V
// 1
It
fat fat _ vb»'/j
iz.
2-21.
/-•$•- 7?
IT-
ff/
li
1*6
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
Of'/
-------
GASEOUS EMISSION SUMMARY
Location;_ "Tg&T SITT^ F
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
%
Dry
C0
Dry
CO
ppm
Dry
NO
ppm
Dry
N02
ppm
Wet
HC
ppm
Wet
02
%
Dry
CO 2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
SO2
ppm
Dry
so3
ppm
Dry
NOTES
fFA
7-6
III!
226
J-1-71
7.2-
II X
til
a*-
&*>
17
n/
6*1
/7-
/3-V
/f/c
1°}
OF*
3*1
r
n*
/W
/r
-Z.I
7*4
per* t>2 4
to
110
22
6.0
ft
i/2.6
2 -/-?
-------
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
CO2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
SO2
ppm
Dry
SO3
ppm
Dry
NOTES
-2*1
5"
f-*
/J?
r
2.2-
•5A-S.-S
5i
frijt
319
?s
//r
2*7
7*3.
//Y
tfo
6*7
12*
10
pA-iTTit u
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900-
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NOS._
DATE
f
FUEL
DtC 1 o 1978
LOAD_
CONDITIONS
J, *
,,.r, , * -,
NOTE: Parts per million (p?m) figures are corrected to 3% 02
nc^ r/>nftif^ iff tjry b* $,'
120
15900
-------
KV3
TEST
TEST NO
DATE
GASEOUS EMISSIONS DATA
FUEL
LOAD
K/fe/A
Off 1 197H
CONDITIONS
i./«)t
i C '-' t
DATA TAKEN BY
million f::.m) fiures are corrected to 3%
121
-------
KV3
GASEOUS EMISSIONS DATA
TEST SITE
TEST NOS.
DATE
rjEL &• B-'^-J
LOAD ~ V
CONDITIONS 10
DATA TAKEN BY
NOTE: Parts pen. million (npn) figures are corrected to 3% O2
15900
-------
KVB
TEST SITE
TEST NO.
DATE
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS
DATA TAKEN BY
: Parts per million (ppm) figures are corrected to 3% 02
123
15900
-------
KVB
TEST SITE A2>AA F
TEST NQS 11 ~
DATE JAM. OS
CASEOUS EMISSIONS DATA
FUEL \ Q
LOAD
CONDITIONS
DATA TAKEN BY
3,
T>cU>*& I A
1TE: Farts per million (ppm) figures are corrected to 3% 02
124
15900
-------
KV3
GASEOUS EMISSIONS DATA
TEST SITE A L. K^/A E
TEST NO. VQ .
DATE _10Ai^_Jia^_132a.
FUEL (g V, i ; 4 U !/M ( c* ^ -J I C *
LOAD \Qo~U
COND ITI ONS
ff,
DATA TAKEN BY I uJputx / £fi<
I n-r^ ' r ._ ' e \ a S
4PTP' • Parts per million (ppm) figures are corrected to 3% 02
125
15900
-------
KVB
GASEOUS EMISSIONS DATA
- F"
TEST SITE
TEST NO. \& A ~ 8 - C-_
DATE ~
FUEL
fe. Trvlu
LOAD
CONDITIONS 0?A
f 5 VJC \.~WNJ •
DATA TAKEN BY
NOTE: Parts per million (ppm) figures are corrected to 3% 02
126
159QQ
-------
KVB
TEST SITE
TEST NO.
DATE
/ 1
GASEOUS EMIS5IONS DA..-A
FUEL
LOAD_
CONDITIONS
/5 • 'QI i/n • rt a '< ^ '
DATA TAKEN BY Cj^
NOTE: Parts per million (ppm) figures are corrected to 3% 02
127
15900
-------
KVB
TEST
TEST NO.
DATE
GASEOUS EMISSIONS DATA
FUEL /<. £*•'
LOAD
CONDITIONS
DATA TAKEN BY "j jdoUc..
Frobe
Position
hi
P f«S
H
H
? I'S"
u
*
* •,/ /£
Time
13.2,5
1405
1110
is 15
\S20
IfefS
AVG.
AVG.
AVG.
°2
% :
(dry)
(pj
1.0
s.4
M.8
t-3
5-1
4.^
co2
%
(dry)
12.8
12.0
13-4
lf.2-
iz.g
13. 1
M
CO
ppm(dry)
unc
Ito
105
220
880
b2o
22o
N
'Wll
:',!in
cor
lit.
136
25H
'////,
'///I,
///It,
cor
/2
(J?
O
/i
(=
JC?a.
Remarks
fr»ye»< /C**e4
^^7~^^~
930 /f07J
~B2S4-* \6 "
/ ^720/1 133
_
i^Zi^ir
•
^.r
( \\6
NOTE: Parts per million (ppm) figures are corrected to 3% O2
128
15900
-------
KV8
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO.
DATE
FUEL |l fr. %fiuL*.-:*0uS
LOAD
CONDITIONS 6fr7/»iu<"l
DATA TAKEN BY
HOT LINE SAMPLES, PPM(WET)
-OTE • Parts
million (ppm) figures are corrected to 3%
129
15900
-------
GASEOUS EMISSIONS DATA
TEST SITE A£MA
TEST NO.
DATE
20
Ol - 17- "7^
FUEL
LOAD
CONDITIONS
^ -?-,l^,;.,.,c .^i
7S %
t f\r? • ^\
Noir^'1! .) " Mrt«n/a( TA tu*^/^^'
DATA TAKEN BY S4i"<
Probe
Position
H
94* 5
VI
\i
?4 » 5
U
P M <-
•
<<"• ,
Time
|6fS
bzr
(630
!7fS
17£S
1815"
\8z.o
AVG.
AVG.
AVG.
02
(dry)
7-S!
i^
7g9
IW
in
StVi
2,7>0
115
3100
1%
3143,
i2>2.
^35
32C
!
j
' "V4" JL
• ••'.•/
' t
HOT LINE SAKPLES , PPM(WET)
NOx
unc cor
110 \VQ>
228
122
221
III
sm
34
1
I
i
i
. '••/] 390
•.../'
/ /
NO
unc
2/0
ZZ8
Z2o
cor
Wl
Sl^
3>n
i
220301
!
I
\
i
^
t ' '1
N02
unc cor
z.
o
3
?
w
i
o
4
L|
!
•^•/ '
••' /•'/
-3.
'////'
HC
unc
I***
10
IO
to
-'''/ •/.
'/Jll
cor
Zo
/S"
IS
l!f
—• — .-
1$
'l/ll/\
Remarks
CWCO££/ Cofit
-------
KV3
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO. _
DATE
- r
FUEL tcu >', '4
u «/.'.» .-to t
oo^
02J
LOAD 7S
2.M-
CONDITIONS |j
DATA TAKEN BY
NOTE: Parts per million (ppm) figures are corrected to 3%
131
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A#MAr F
TEST NO. 2lZ / -I-Ar: f -SO%
DATE
JAN 3 1 1979
FUEL
LOAD
CONDITIONS
FA ^jljJKAJ
MQJu;
\oo •/,
OFA •
DATA TAKEN BY
NOTE: Parts per million (ppm) figures are corrected to 3%
132
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST siTE_Afe>AA F
r> •?.
FUEL *?A .
,' H-V.T. loot. I
TEST NO.
DATE
AfcTi C UH c-'i?
LOAD
11979
CONDITIONS QtjL
Of A 'W. ~.-*. -^ *
I >
DATA TAKEN BY £;JU i
ft-* nJTf.tr>
Parts per million (ppm) figures are corrected to 3%
133
15900
-------
KV3
GASEOUS EMISSjrONS.JjATA
TEST SITE
TEST NO.
DATE
/&"
p
FUEL
/"<.,./_
•* I* ff
LOAD &£>10t>t> Xi
COND ITI QMS jyr 0*. Of 7
DATA TAKEN BY
NOTE
: Parts per million (ppm)' figures are corrected to 3% O2
134
15900
-------
KV3
TEST SITE fT^M/T /-
TEST NO.
DATE
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS
>. W. Ct>
£u>«0.
DATA TAKEN BY // &
Probe
Position
Time
> TV, ,piu(dry)
unc cor
V
HOT LINE SAMPLES, PPM (WET)
NOX
unc cor
2/7
NO
unc | cor
oo
N02
unc cor
HC
unc cor
Remarks
tit a / /is:
O
//2\/13
2/01
AVG.
AVG.
NOTE: Parts per million (ppm) figures are corrected to 3% 02
135
15900
-------
KVB
TEST SITE
TEST NOS.
DATE
GASEOUS EMISSIONS DATA
FUEL
FEB 12 1979
LOAD
CONDITIONS
DATA TAKEN BY /fl ft.
Probe
Position
H
Time
02
% :
(dry)
(drv)
/a. 2
CO
ppm (dry)
unc cor
no
NO
ppm(dryj
unc cor
Xinc I cor
HOT LINE SAMPLES, PPM (WET)
NOX
NO
unc
'AM
cor
N02
unc cor
unc
1.0.
/n.2
/70
/20
ni
^££
MJL
znn
? '/ s ^
710
/in
MO
MX
-JOL
4
jLO.
II.Q
/70
222
Ml
3LAJCA.
NOTE: Parts per million (ppm) figures are corrected to 3% O2
136
15900
-------
KVS
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO.
DATE
FUEL R . fr'
(W K**/
- O
LOAD
CONDITIONS
DATA TAKEN BY f '
NCrr*E :
per million (ppm) figures are corrected to 3%
137
L5900
-------
KVB
GASEOUS EMISSIONS DATA
NOTE: Parts per million (ppm) figures are corrected to 3%
138
159QQ
-------
KVB
TEST SITE
n
GASEOUS EMISSIONS DATA
FUEL )
TEST NO. JJ / —
DATE .-> //*•/
LOAD
CONDITIONS !
DATA TAKEN BY /\
NOTE: Parts per million (ppm) figures are corrected to 3% 02
139
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO.
DATE
f?./-
CONDITIONS //•-•/;•'*"' ' }
::>"X-
DATA TAKEN BY ,
-i.
10
/06
171
to
AVG.
AVG.
AVG.
'1 HI
Hill
NOTE: Parts per million (ppm) figures are corrected to 3%
140
15900
-------
SOX DATA SHEET (GOKSOYR-ROSS METHOD)
Test No.
Unit No.
Capacity
Engr.
I'i/t<
Date
?<
Location resrr
Fuel TeA.'d A
Unit Type *?<: pc «•» «• '
* <-
-»-h? fcr* ,
Conditions
. e>pj 6S.
i)f-ft
Meter Finish
Meter Start
Sanple Volume Collected
start Time
ADCF X
Stop Time
Elapsed Time (minutes)
/ 3i
Total Sampling Time =
Meter
7-?
'>*/
min.
Temperatures (°F)
Coil In
n.l
in
Coil Out
Water Bath
Stack
Sample Flow
Rate (ADCFM)
C-
*1?*/
NOTES: (1) Sample flow rate at meter should be 0.075 ADCFM
or 0.01 cf/8 sees.
(2) Total sample volume collected should be M..5 cf (*• 20 minutes sampling time)
141
A Research-Cottrell Company Data Sheet KVB 6015-37
-------
Date
K VB. INC.
Test No.
TEST NO.
UNIT N0.
SOx DATA SHEET
FUEL O>' <— LOAD
_klb/hr
JLocation f.<~_f'f. -
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Calculation- ^ «r fi« FI™ (A - B) x N x F x (460 + T) x 24
Excess 0, ^>£> %
so2
N = Normality of lead perchlorate titrant = -1 -j \c n
F = Dilution factor =
T = Average temp, in gas meter =
V = Volume of gas sample ft3 =
P = Barometric pressure =
p = Pressure in gas meter ;>,. '-.-, =
Concentration, C, ppm =
,qm/dscn =
Emission ,E, g/Mcal =
E = CF{ 2090 1 Ib/MBtu =
bo.s-xcu
where L J ng/J =
so3
o
o
d.'^L '•>
\.o
'?? *-
/ * J ' &
2^> t>»_
tf>'*^-
o
o
o
o
0
S0x
— _
1 •
_
C = pollutant concentration, g/dscm
F, volume factor = dscm/10 cal
dscf/104
Btu
142
from Fed. Reg. 9/11/74 p 32856
60-14
rev. 1/2/75
-------
SOX DATA SHEET (GOKSOYR-ROSS METHOD)
Test No.
Unit No.
Capacity
Engr.
Date /*•*£
Fuel
Location Tes>7~
Unit Type
Conditions
Meter Finish
Meter Start
Sanple Volume Collected =
ADCF
71-,
Start Time
//-iL
Stop Time
//•' Y3
Elapsed Time (minutes)
«?/
Total Sampling Time
21
min.
Time
// ZT-
IJjU
ii-yj
K Y'»
— - —
Meter Vac.
<"Hg)
r
5
v.r
¥<-
Temperatures (°F)
Meter
Zi
is
*5
?i
Coil In I Coil Out
W
4<
H
11
HI
H3
n 3
Hi
Water Bath
/v«
It*
,^
ity
Stack
?*?
?jsr
3*f
~U1>
Sample Flow
Rate (ADCFM)
^.^7^5-
6 O7f^
f-flf*
f^Jff
NOTES: (1) Sample flow rate at meter should be 0.075 ADCFM
or 0.01 cf/8 sees.
(2) Total sample volume collected should be ^1.
143
A Research-Cottrell Company
cf (^ 20 minutes sampling time)
Data Sheet KVB 6015-37
-------
Date
7/3/7
K V B. INC.
Test No.
TEST NO. 32> UNIT NO.
SOx DATA SHEET
LOAD
_klb/hr
Location
Box No.
Time
Temp, in Gas Meter
Press, in Gas Meter
Meter Reading
Barom. Press.
Percent Oxygen
N2 Purge Time
Calculation: SO^ or SO^, ppm =
Excess 0-> C'D %
- B) x N x F x (460 + T) x 24
V (P + p)
—
B =
N =
F —
T —
V =
P =
P =
E =
whei
C =
F,
f roro
Ml of J:ead perchloratc used for
Ml of -lead perehlorato- used for
so2
sample — fiO -* &.
blank - loi-^flf.
Normality of lead perchlorate titrant = -j~alt.ey\
Dilution factor
Average temp, in gas meter , °F
Volume of gas sample ft3
Barometric pressure
Pressure in gas meter /^ l\,
' d
Concentration
Emission -/E,
CF 2090
20.9-xo, 1
:e L •*
pollutant concentration, g/dscm
volume factor = dscm/10 (
dscf/104 j
Fed. Reg. 9/11/74 p 32856
=
=
=
=
=
.C, ppm =
mn/dscm =
a/Meal =
Ib/MBtu =
ng/J =
so3
^* * C^.
^9 fy
D.">3?^
I.Q
Zt
l>s*44
^?3'/7
n 4 /
/ 22
S0x
, * >.
:al
144
3tu 60-14
rev. 1/2/75
-------
SECTION 4,0
PARTICIPATE SIZE DISTRIBUTION
PAGE
4,1 BRINK 146
4,2 SASS 158
4,3 BAHCO 159
145
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
LOAD
% 02
FUEL
SPECIAL CONDITIONS ^QU/ c^U
g;t-.__
Pp - Density of particles £
y - Viscosity of flue gas •
MWs - Molecular wt. flue gas
g/cm3
X #>~¥
poise
g/g mole
Vm - Dry gas volume
SCF
Mn - Total particulate mass
AP - Pressure drop across impactor ^. / in.H70 I - Percent isokinetics
Ps - Absolute stack pressure
Ts - Absolute stack temperature
Qs - Actual flow rate at stack conditions
in. Hg
R
Vs - Gas velocity
Dn - Nozzle diameter
t /min
Cn - Total concentration _/^
-
SCT*
ft/sec.
Stage Number
Dj - Jet Diameter, cm
Fj - Press, factor, n.d.
Ds,£; Stokes diameter, ym
D, •=- Aerodynamic
'V^jo
diameter, ym
A^^ Aerodynamic impac-
tion diameter, ym
Mn - Particulate mass, mgm
% - Percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grains-'SCF
CYCLONE
Z.S*
0.
3.0 1.
+.B&
0.3
2.3
O.OO2.
a/775"
0.02.73
2.67
0.7
J.I 7
A95"
Z..I2-
/ 2.
A
0.7
0.32.7 7
0.7
o. /
o.ocxr
FINAL
FILTER
146
#15900
-------
TEST NO.
KVB
BRINK CASCADE IMPACTOR DATA SHEET
LOAD ®Q, OOQ
TEST SITE /ftM/A Afte. F
TEST
DATE £. // / 7 <3
SAMPLE LOCATION £,C.GY). £>
7.
FUEL
- ^
J
Ivan i
-------
KVB
TEST No.
TEST DATE
TEST DESCRIPTION
BRINK CASCADE IMPACTOR LAB WORKSHEET
LOCATION ^-/JMA F
ENGINEER
M MM 6 FA } **> fca** &r/*JTgCTVO
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
CYCLONE
FINAL
FILTER
DATE WT.
TARE WT.
0.
AVERAGE
POST TEST WEIGHTS (GRAMS)
DATE WT.
GROSS WT.
v, Vv- ?
.?."?; 77
AVERAGE
. 66 If
.7.
3-tftf
7.7S97
NET TEST RESULTS (MILLIGRAMS)
NET WT.
o, ooi y-
0,
0,
PERCENT
o.n
0.3? I P. 11
TOTAL NET WEIGHT
mgm
148
#15900
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
•3 A
LOAD
% 02
FUEL
/DO
SPECIAL CONDITIONS
KM
pp - Density of particles £
y - Viscosity of flue gas ^, V
g/cm^
^ 'poise
Vm - Dry gas volume 3.0^7 SCF
Mn - Total particulate mass £33.9 '
- Molecular wt. flue gas £.*), H~ 9/9 mole Cn - Total concentration
\-p - pressure drop across impactor .5"". ^ inH20 I - Percent isokinetics
JT-J
ps - Absolute stack pressure £3-3^" in. Hg Vs - Gas velocity ^ 9. *Jt ft/sec.
Ts - Absolute stack temperature &30 CR Dn ~ Nozzle diameter C^.O*?^ in.
Os _ Actual flow rate at stack conditions Q, £> (-, Q&ft /min
Stage Number
Dj _ jet Diameter, cm
pj - Press, factor, n.d.
Ds _ stokes diameter, ym
— Aerodynamic
diameter, urn
Aerodynamic impac-
tion diameter, ym
.1 _ particulate mass, mgm
% _ percent of Total
Cumulative percent
rn - Concentration,
C grains/SCF
Cumulative concen-
tration, grains/SCF
CYCLONE
AT. 7
£.00
6.*)
3.8
O.OW&
3.2.
0.6131
0.66
0,0
0.017
J./8O
FINAL
FILTER
0.0
0.0
a 000
/-/££>
149
#15900
-------
KVB
BRINK CASCADE IMPACTOR DATA SHEET
TEST NO.
TEST SITE
TEST DATE
x> ^ A.
/-. O /T
^/e/79
LOAD / O O **/$->
% o2 \5~. ^
£> \ ' -o " .1 '
FUEL r&jjn -SM l^^/ijc^ £5 / T./y ^)/ >intf 5
SAMPLE LOCATION
SPECIAL CONDITIONS O
ft)
GAS VELOCITY DETERMINATION
PITOT TUBE AP
£).
GAS TEMP. °R, Ts
BAROMETRIC PRESS in. Hg, Pj->ar
GAS STATIC PRESS in. H20
PITOT CORRECTION FACTOR, Cp
Vs = 85-48
Ts
ft/sec
GA£ STATIC PRESS in. Hg abs./Ps ^ ^ .
MOLECULAR WT. FLUE GAS , MWS g. 9
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn O ~ O
NOZZLE AREA ft2. An 3. *t b H~
I O
Qn = Vs An 60
Qc = Qs
O
An = TT(Dn/24) 2
at nozzle
ft3/min corrected to calibration conditions
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE
OPERATING VACUUM (corrected for static pressure of duct) Q , \5~
ISOKINETICS DETERMINATION
in. HO
INITIAL
FINAL
A
SAMPLE
TIME (6)
/Z:/0
/3!//
£1
METER
READING (Vm)
33/7- B30
^^0- &9(^>
3,e>6
METER
TEMP (Tin)
8:3
ee>
S£
%H20 =
1.667 Ts Vm Pbar
6 Tm Vs Ps
150
#15900
-------
KVB
TEST No.
TEST DATE
BRINK CASCADE IMPACTOR LAB WORKSHEET
LOCATI ON
ENGINEER ~T"»
TEST DESCRIPTION
fajL I t? 7" '"''••' 3
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
CYCLONE
7*- 13
FINAL
FILTER
DATE WT.
TARE WT.
-./-,«
•?'•-••'
/or ;; <
>/
J •)
0.03^1
AVERAGE
/ £ 1 36
-3.2^/77
POST TEST WEIGHTS (GRAMS)
DATE WT.
- / -v
,'/:•-'
GROSS WT.
» 7 .' - •
AVERAGE
/03.I607
Si
NET TEST RESULTS (MILLIGRAMS)
NET WT.
PERCENT
J373-
«^,3
,'^07^
3.^r
.0^9?
lfl«
. oo ^f!
3.^0
.oc?r
3.Xo
.OCi^
I4S~
0
o
TOTAL NET WEIGHT
3,
mgm
151
#15900
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
Z.H-
St'-k^. F"
LOAD
% 0,
J0G *?*
FUEL
**
SPECIAL CONDITIONS
^
Pp - Density of particles
y - Viscosity of flue gas
VMs
9/cm3
Vm - Dry gas volume >&.
SCF
Mn - Total particulate mass S.Of.
AP - Pressure drop across impactor
PS - Absolute stack pressure
inH20 I - Percent isokinetics
in. Hg Vs - Gas velocity
*
Ts - Absolute stack temperature QSD °R Dn - Nozzle diameter
Qs - Actual flow rate at stack conditions Q. Qf> 3$ f t /min
ft/sec.
in.
Stage Number
Dj - Jet Diameter, cm
Fj - Press, factor, n.d.
Ds,j^ Stokes diameter, ym
D, r^ Aerodynamic
diameter, ym
'AI,5> Aerodynamic impac-
tion diameter, ym
I^n - Particulate mass, mgm
% - Percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grains/SCF
CYCLONE
6.O
Q.02.10
&.OI
2.8
AO
<$:&
O.OZ7S
£.86
3.6Z-
3.7
A3
0.0*8
0.03*5" tt
/3
o. 8
006
A/7
A*.
O'OOS O.
0.^*71
FINAL
FILTER
o.o
#15900
-------
KVB
BRINK CASCADE IMPACTOR DATA SHEET
TEST NO.
TEST SITE v5
TEST DATE ;
SAMPLE LOCATION
2, 4-
5i>e_ pr
a /6 /?^
Eton. OLfb
LOAD
% 02
FUEL /^
SPECIAL
/£>£> ^o
6-^5
^^ssi/^nm JK',4:.
CONDITIONS j/^&uy O^ H-iall &F,
GAS VELOCITY DETERMINATION
PI TOT TUBE AP
GAS TEMP. °R, Ts
PITOT CORRECTION FACTOR, Cp &,
BAROMETRIC PRESS in. Hg, Pbar
GAS STATIC PRESS in. H2O —
GAS STATIC PRESS in. Hg absyPs
MOLECULAR WT. FLUE GAS , MWs
8£>
Vs
85.48 Cp
Ps MWs
-3 O
ft/sec
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn
NOZZLE AREA ft2, An *
X JQ
An = Tr(Dn/24)2
On = Vs An 60
. ,PsMWs
at nozzle
QC =
. .3Ts
>, (Qv5~/ "7 ^ ft3/min corrected to calibration conditions
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE
OPERATING VACUUM (corrected for static pressure of duct)
ISOKINETICS DETERMINATION
Q
_in. H20
_in. H20
INITIAL
FINAL
SAMPLE
TIME (9)
/3 : 3 o
METER
READING (Vm)
METER
TEMP (Tm)
88
%H2O =
I =
1.667 Ts Vm Pbar
6 Tm Vs Ps
153
#15900
-------
KVB
BRINK CASCADE IMPACTOR LAB WORKSHEET
TEST No.
LOCATION
£/*
TEST DATE
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
^^
^r)-/^.
f
LOAD
% 0,
FUEL
100 !
6,^
?7
&
SPECIAL CONDITIONS
Pp - Density of particles^*. \^~_
y - Viscosity of flue gas £.Q
MWS - Molecular wt. flue gas_
-y
Vm - Dry gas volume
SCF
mole
Mn - Total particulate mass
Cn - Total concentration L
- Pressure drop across iirpactor \S^ 6 in H?0 I - Percent isokinetics
Ps - Absolute stack pressure
Ts - Absolute stack temperature
Qs - Actual flow rate at stack conditions
in. Hg
°R
Vs - Gas velocity
Dn - Nozzle diameter
Stage Number
Dj - Jet Diameter, cm
Fj - Press, factor, n.d.
Ds— Stokes diameter, "um
p — Aerodynamic
diameter, ym
impac-
tion diameter, ym
jin - Particulate mass, mgm
% - percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grain^SCF
CYCLONE
D.02.JO
i.
//.
3. Z.
A//
A V
/. 8
FINAL
FILTER
A/
0.3
a
155
#15900
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA SHEET
LOAD
% 02
FUEL
.0-
SPECIAL CONDITIONS
PITOT TUBE AP
GAS VELOCITY DETERMINATION
GAS TEMP. °R, Ts P *7 <•>
PITOT CORRECTION FACTOR, Cp F>")
VS = 85.48CP
Ps MWs
BAROMETRIC PRESS in. Hg,.Pbar ^
GAS STATIC PRESS in. H2O —- '3.
GAS STATIC PRESS in. Hg absyPs 2rt. G. V
MOLECULAR WT. FLUE GAS , MWS ^ *?. •-/
. Po
ft/sec
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn . O "? °
NOZZLE AREA ft2, An T, Vo *> X ' O " ^
P^j = Vs An 60
Qc = QS
-------
KV3
TEST No.
BRINK CASCADE IMPACTOR LAB WORKSHEET
LOCATI ON /•_"/'''
TEST DATE J? / / 2 / ?'-'(*
TEST DESCRIPTION t>PT
ENGINEER •
PRE TEST WEIGHTS (GRAMS)
PLATE N
DATE WT.
TARE WT.
AVERAGE
0.
1
2
3
4
CYCLONE
?/u /?*
<"( f.- •> 5 c-if
.."•'. '-!-•• 7
"" '/?
2
-V'l/7--
7.?osn
?•?*!>
3 ? v i /
7 • ' ' )
3
- /M/?>
~: •> --/c
J. 7^ A/ 7
s^ v^-
?!/'*
- -^ i"2 v
?.7A26
?• 2S-2J'
_| ^
?. ^r?A-
5
^ /.-,-/>
3" >j-j-?
3. 7JV3
•'. ? r"X^
"
?,7s-r
157
#15900
-------
SITE F
SASS GRAVIMETRICS
Test 22 10U 89.4199 9.81% Passing
3y 6.3749 3.38% Passing
ly 0.9482 2.42% Passing
Filter 2.4037
TOTAL 99.1467
Test 30 10U 74.9933 12.86% Passing
3V 7.1511 4.55% Passing
1U 1.2138 3.14% Passing
Filter 2.7016
TOTAL 86.0598
153
-------
KVB
6990-01
July 12, 1979
Sample No.
Sample Description
Bahco Particle
Size Determination
% Through //100
(149 Microns)
K-23138
Fly Ash
F-5
12/19/78
33.8
Results:
Terminal
Velocity
112.
79.
31.
12.3
4.15
0.96
0.35
Diameter
(Microns)
26.
22.
14.
8.8
5.1
2.4
1.5
. %Smaller
19.7
17.4
12.7
7.4
3.6
1.3
0.3
K-23139
Fly Ash
F-21
1/24/79
18.2
Diameter
(Microns) %Smaller
K-23140
Fly Ash
F-23
2/1/79
17.3
Diameter
(Microns) %Smaller
Density, gms/cc
(On //100 mesh
Material Only)
Screen Sizing
% Through #10
16
30
50
100
200
325
2.23
100.0
98.5
79.6
54.3
33.8
16.3
8.3
24.
21.
13.
8.1
4.7
2.3
1.4
5.6
4.7
3.2
2.0
1.3
0.8
0.4
24.
20.
13.
8.0
4.7
2.2
1.4
5.5
4.8
3.4
2.4
1.7
1.0
0.5
2.61
100.0
97.8
67.7
37.6
18.2
5.1
2.4
2.64
100.0
95.8
60.
34,
17.3
5.3
2.6
.4
.3
159
-------
KVB
6990-01
July 12, 1979
Sample No.
Description
K-23141
Fly Ash
F-24
2/6/79
K-23142
Fly Ash
F-29
2/12/79
Bahco Particle
Size Determination
% Through MOO
(149 Microns)
Results: Terminal
Velocity
112.
79.
31.
12.3
16.1
4.15
0.96
0.35
Density, gms/cc (On #100
Mesh Material Only)
.Screen Sizing
% Through #10
16
30
50
100
200
325
Diameter
(Microns)
25.
21.
13.
8.4
4.9
2.3
1.4
%Smaller
6.1
5.3
3.4
2.6
1.7
1.0
0.6
2.44
100.0
97.8
64.
33.
16.
5.
.1
.1
.1
.0
16.0
Diameter
(Microns) %Smaller
26.
22.
14.
8.8
5.1
2.4
1.5
6.8
6.0
4.5
3.1
2.1
1.1
0.5
2.4
2.23
100.0
98.2
68.8
35.4
16.0
4.7
2.8
160
-------
SECTION 5,0
FUEL AND ASH ANALYSIS
PAGE
5,1 COMMERCIAL TESTING ANALYSES 162
5,2 COMBUSTIBLES ANALYSES 196
5,3 COAL SIEVE ANALYSES 198
161
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-8434
^MMR WMkt
KVB, INC.
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
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Coal
Sample taken at
Sample taken by KVB, Inc.
Date sampled 12/19/78
Date received 2/22/79
ABMA Test Site "F1
Test #5
Analysis report
no 71- 28163
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed CarDon
Btu/!b
% Sulfur
Initial Deformation
Softening (H = W)
Softening (H - lAVi
Flu:d
Ap ht'CPivpri
4.80
10.80
14.03
70.37
100.00
13145
1.34
FUSION "•r-!/':Cr. •'-
Reducing
xxx r
XXX r
xxx ''f
xxx F
Dry Basis
xxxxx
11.34
14.74
73.92
100.00
13808
1.41
;UF
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
QENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80601
AREA CODE 312 726-8434
Ztk
KVB, INC.
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
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc
1/8/79
2/22/79
ABMA Test Site
Test #15
Analysis report no. ~j.]_- 28165
PROXIMATE ANALYSIS
As Received Dry Basis
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/lb.
% Sulfur
5.69
10.96
22.86
60.49
100.00
12975
1.20
xxxxx
11.62
24.24
64.14
100.00
13758
1.27
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H = W)
Softening (H = VzW)
Fluid
RAH/ br
Copy Watermarked
For Your Protection
Reducing
Oxidizing
XXX
XXX
XXX
XXX
°F
°F
°F
°F
XXX
XXX
XXX
XXX
°F
°F
°F
°F
H = Cone Height
W = Con» Width
Respectfully submitted,
COMMERCIALJESTING & ENGINEERING CO.
163
R. A. HOUSER, Manager,
SO. HOLLAND. IL • BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER, CO • GOLDEN CO
HENDERSON, K V • MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA > NORFOLK. VA • PIKEVILLE, KV • VANCOUVER. B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
PLEASE ADDRESS ALL CORRESPONDENCE TO"
16130 VAN DRUNEN RD., SOUTH HOLLAND, 1L 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc.
1/10/79
2/22/79
ABMA Test Site "F1
Test #17
Analysis report no. 71- 28167
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
5.26
9.69
23.86
61.19
100.00
13223
1.24
xxxxx
10.23
25.18
64.59
100.00
13957
1.31
Initial Deformation
Softening (H = W)
Softening
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-6434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc.
1/15/79
2/22/79
ABMA Test Site "F1
Test #18
Analysis report no. y^_ 28169
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/ib.
% Sulfur
Initial Deformation
Softening (H^W)
Softening (H--''?W>
RAH/ br
Original Copy Watermarked
" for Your Protection
5.58
12.50
22.66
59.26
xxxxx
13.24
24.00
62.76
100.00
12649
1.43
100.00
13396
1.51
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
XXX
XXX
XXX
XXX
• F
XXX
XXX
XXX
XXX
H -•-- Cone Height
W .-. Cone Width
Respectfully submitted,
COMMERCIALIZING & ENGINEERING CO.
165
R. A. HOUSER, Manager, Midwest Division
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO > GOLDEN CO
HENDERSON, KY • MIOOLES8ORO. KV • MOBILE. AL • NEW ORLEANS, LA > NORFOLK, VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN.
Charter Member
-------
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, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc,
1/16/79
2/22/79
ABMA Test Site "F1
Test #19
Analysis report no. 71- 28171
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
Fixed Carbon
Btu/lb.
% Sulfur
Initial Deformation
Softening (H = W)
Softening (H^VzW)
Fluid
RAH/ br
Original Copy Watermarked
For Your Protection
As Received
Dry Basis
7.76
11.08
22.45
58.71
100.00
12501
1.35
xxxxx
12.01
24.34
63.65
100.00
13553
1.46
FUSION TEMPERATURE OF ASH
Reducing
xxx °^
xxx F
xxx °F
xxx "F
Oxidizing
xxx
xxx
xxx
xxx
•F
F
•-F
T
H
W
Cone
Cone
Respectfully submitted, , .
COMMERCIAteTESTING & ENGINEERING CO!
166
. HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. «VV • CLARKSBURG. WV • CLEVELAND. OH . DENVER. CO • GOLDEN. CO
HENDERSON. KY •MIDDLESBORO KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK. VA • P.KEV.LLE KV . VANCOUVER. B.C. CAN
-------
F 462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
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
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc
1/17/79
2/22/79
ABMA Test Site "F1
Test #20
Analysis report no. 71- 28173
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.26
8.43
25.22
64.09
100.00
13813
1.61
xxxxx
8.62
25.80
65.58
100.00
14132
1.65
Initial Deformation
Softening (H = W)
Softening (H = VaW)
Fluid
RAH/ br
Original Copy Watermarked
For Your Protection
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
XXX
XXX
XXX
XXX
°F
°F
°F
°F
XXX
XXX
XXX
XXX
°F
°F
°F
°F
H = Cone Height
W = Cona Width
Respectfully submitted,
COMMERCIA/tfcSTING & JNGINEERING CO.
167
R. A. HOUSER, Manager, Midwest Division
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM, AL • CHARLESTON, WV • CLARKSBURG. VW 'CLEVELAND.OH • DENVER. CO • GOLDEN. CO
HENDERSON. KY . MIOOLESSORO. KY > MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN.
;•*«*'•.
Charter Member
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 221 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80601
AREA CODE 312 726-8434
KVB, INC.
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
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc,
1/24/79
2/22/79
ABMA Test Site
Test #21
Analysis report no. 71- 28175
PROXIMATE ANALYSIS
As Received Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
Initial Deformation
Softening (H = W)
Softening (HnVzW)
Fluid
RAH/ br
Jriginal Copy Watermarked
For Your Protection
1.99
11.15
62.87*
23.99^
100.00
13347
1.85
xxxxx
11.38
64.15
24.47
100.00
13618
1.89
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
XXX
XXX
XXX
XXX
°F
°F
°F
°F
XXX
XXX
XXX
XXX
°F
°F
°F
°F
H «- Cone Height
W ^ Cone Width
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING c'65
168
SO HOLLAND IL • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER, CO • OOLOfN. CO
HENDERSON. KY . MIDDLESBORO. KV • MOBILE. AL • NEW ORLEANS. LA . NORFOLK. VA • PIKtVILLE. KV • VANCOUVER. B.C. CAN.
-------
F-467
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, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Coal
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site
Test #22
KVB, Inc.
1/31/79
2/22/79
'.,01 :-'J
^Strontium oxide, SrO
%Barium oxide, BaO
%Manganese oxide, Mn.,0
Analysis report no.
'•lii'i Ai received
3.13
• A:;II 9.44
' • ° 23.58
63.85
100.00
13627
'"' 1.51
a ° xxxxx
u1- ; .
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
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
March 7, 1979
Samole identification
°y KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal ABMA Test Site "F"
Test #23
KVB, Inc.
2/1/79
2/22/79
Analysis report no. 7]__ 28177
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Sti.v'ib.
% Sulfur
Initial Deformation
Softening (H - W)
Softening (H--. V'W)
RAH/ br
Original Copy Watermarked
For Your Protection
As Received
2.28
9.45
24.20
64.07
100.00
13750
1.66
Dry Basis
xxxxx
9.67
24.76
65.57
100.00
14071
1.70
FUSION ""cMPERATURE OF ASH
Redijcing
XXX F
XXX P
xxx f
XXX
Oxidizing
xxx
XXX
xxx
xxx
-F
"F
•F
p
Respectfully submitted,
COMMERCIAL/PBSTING &
Cone
GINEERING CO.
170
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS MT • 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
•*= vre-
Charter Member
-------
F-462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-6434
KVB, INC.
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
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc
2/8/79
2/22/79
ABMA Test Site "F1
Test #23A
Analysis report no. y^_ 28181
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
2.51
11.01
23.92
62.56
100.00
13467
1.67
xxxxx
11.29
24.54
64.17
100.00
13814
1.71
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
Initial Deformation
Softening (H=W)
Softening (H = y2W)
Fluid
RAH/ br
Original Copy Watermarked
For Your Protection
XXX
XXX
XXX
XXX
°F
°F
°F
°F
XXX
XXX
XXX
XXX
°F
°F
°F
°F
H --• Cone Height
W - Cone Width
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
171
R. A1
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. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
Charter Member
-------
-467
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-9434
zfc.
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sarrp'o
reported to us Coal
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
bV KVB, Inc.
Sample taken at
Sample taken by KVB, Inc.
Date sampled 2/7/79
Date received 2/22/79
ABMA Test Site "F"
Test #24
Analysis report no.
PROXIMATE ANALYSIS As received Dry basis
% Moisture
% Ash
% Volatile
% ~>xed Carbon
Btu/lb.
% Sulfur
°.c Alk. as Na,O
3.42
11.59
23.32
61.67
100.00
13164
1.32
xxxxx
xxxxx
12.00
24.15
63.85
100.00
13630
1.37
0.20
71- 28189 % Weight
ULTIMATE ANALYSIS As received Dry basis
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff)
3.42
73.70
4.53
1.20
0.14
1.32
11.59
4.10
xxxxx
76.31
4 69
1.24
0.15
1.37
12.00
4.24
SULFUR FORMS
•o Pvritic Sulfur
-'o Su.'fate Sulfur
°o Organic Sulfur
A'ArLi:. SOLUBLE ALKALIES
% K O -
0.52
0.08
0.72
xxxxx
xxxxx
MINERAL ANALYSIS OF ASH
0.54 Silica, SiO,,
0 QQ Alumina, AI,O ,
0 75 Titania, TiO,
IH -_- Wl
Reducing
2700+ '
2700+ '
:• "e: -y 'M-. 'rW) 2700+ '
_ np!>'!d 2700+ '
" ''' '""'; "'' ''''''' ' ' v XXXX
•'• -.:••• •,.-ri iu^-x 89
. -L -r. i'-.i"X .. 9
*These ignited basis results were used
to calculate undetermined value above
%Strontium oxide, SrO
%Barium oxide, BaO ,
^Manganese oxide, Mn.,0. ,
xxxx
xxxx
Oxidizing
xxxx
xxxx
xxxx
xxxx
0.04
0.10
0.01
Ferric oxide, l-c o
Lirno CaO
Magnesia, MgO
Potassium oxide. K O
Sodium oxide, Na.O
Sulfur trioxioe. SO
Phos. pentoxiae. P.O
Undetermined
SILICA VALUE ..-
BASE. ACID RATiO
J?,r Temperature ..
Respectfully submitted,
COMMERCIM9TESTING & ENGINEERING CO.
°F
°F
°F
°F
V Watermarked
For Your Protection
172
R. A HOUSER, Manager, Midwest Division
SO HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CH
HENDERSON. KV • MIODLESBORO. XV • MOBILE. AL
ARLESTON WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER, CO- GOLDEN. CO
NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE, KV • VANCOUVER. B.C. CAN.
Charter Member
-------
F-467
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601
AREA CODE 312 726-8434
zlk
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Coal
March 8, 1979
by KVB, Inc.
KVB, Inc.
2/12/79
2/22/79
ABMA Test Site "F"
Test #29
Anj
•• •• -•••• ^'*:^«
3.54
8.79
26.10
61.57
100.00
13623
1.00
'.•-'••• ' ' '
:,::.". K. rWS
'-'' 0.00
0.67
•'i V:.'L'_ ' • './'-I .;• ';
«._«
—— '—
. • ; ' • . -M Pt.'cucing
. — — -
2700+
2700+
2700+
: 2700+
81
f\
9
*These Ignited basis results were used
to calculate undetermined value above
ilysis report no. y^_ £8192 '
Dry basis ULT !$.-"> Yi /.< •>. v : : '• - . -r,'-
xxxxx ''•'' " ' 3 54
9.11 -;-lt:" •'• 76.62
27.06 H;;' •-" 4.70
63.83 ;;••••--• Ia5
100.00 ^•-•••v"1 0.17
1*123 ••"'. V 1.00
1.04 ^ ^; 8.79
0.14 ^>'K--:iM A>03
MINERAL ANALYSit CF ASH 100"°9v
0.34 ' " S.!.ra.f,0.
0.00 Alumina. A: O
_ __ 1 itani.i. ! u
0.70
Forric cxide. t:o t '
i irn , ,- u--j
Wagnesi;- ^^;O
Potassium oxioc-> ;\ v)
Oxidising Sodium oxi-Jc \
P " °P
^^^v>
F C'F SuHur tnox' v ^ '~
,,c ~S Pfen T!! '•'. -•
SILIC/ v/-1. i.1.
BASC A,,'i. .'• .•":
i i '.;|IV- • ' '"•''•
Respectfully submitted,
0 • 10 COMMERCIAL TESTING & ENGINEERING CO.
0.1? Si *
^* j f ^F
o.oo W^V3/7 '"
xxxxx
79.43
4.87
1.19
0.18
1.04
9.11
4.18
,,oh, 10,0,90
47.74
34.17
1.38
9.21
1.32
0.57
1.74
0.37
1.43
0.30
1.55*
100.00
81.14
0.16
2805 °F
,- ..' '* "':
u 4 ..'-,
pv Watermarked
orYour Protection
173
R. A HOUSER, Manager, Midwest Division
SO HOLLAND. IL • BILLtNCS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. VW • CLEVELAND. OH • DENVER. CO • GOLDEN CO
HENDERSON. KV • MIOOLESBORO KV • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
Charter Mambtr
-------
F-467
COMMERCIAL TESTING & ENGINEERING CO.
•'V
GENERAL OFFICES: 2J8 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 Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Coal
March 7, 1979
Sample ide-nt!?... •••
by KVB, Inc.
KVB, Inc.
2/13/79
2/22/79
ABMA Test Site "F"
Test #30
Analysis report no. 7^- 28194
A^recen/ed P[V_b3sis ULTIMATE AH
Ash
3.84
9.12
25.39
61.65
100.00
13568
0.99
xxxxx
0.44
0.00
0.55
°0 Weight
As received Dfy basis
0.46
0.00
0.57
c no -
MINERAL ANAL
3.84
76.09
4.68
1.09
0.17
0.99
9.12
4.02
100. Op
xxxxx
79.13
4.87
1.13
0.18
1.03
9.48
4.18
iop. 00
47.95
32.66
1.46
xxxxx
xxxxx
r'_oducjrig
2700+
2700+
2700+
2700+
xxxx
xxxx
XXXX
xxxx
xxxx
xxxx
xxxx
84
9
*These ignited basis results were used
to calculate undetermined value above
%Strontium oxide, SrO 0.10
%Barium oxide, BaO 0.17
^Manganese oxide, Mn 0, 0.01
Respectfully submitted,
COMMERCIAL TJSTING & ENGINEERING CO.
Watermarked
For Your Protection
174
R. A
IOUSER, Manager, Midwest Division
SO HOLLAND IL-BILLINGS MT • BIRMINGHAM AL • CHARLESTON. WV CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. KY • MIDDLESBORO. KV • MOBILE. AL • NEW ORLEANS LA • NORFOLK, tf A • PIKEVILLE. KY • VANCOUVER. B.C CAN
2730 °F
Charter Membtr
-------
F 462
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Ztb.
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Coal
KVB, Inc.
2/14/79
2/22/79
ABMA Test Site "¥'
Test #35
Analysis report no. 71- 28184
PROXIMATE ANALYSIS
As Received
Dry Basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu/lb.
% Sulfur
Initial Deformation
Softening (H = W)
Softening (H = V2W)
Fluid
RAH/ br
Original Copy Watermarked
For Your Protection
4.17
10.25
25.54
60.04
xxxxx
10.70
26.65
62.65
100.00
13315
1.01
100.00
13894
1.05
FUSION TEMPERATURE OF ASH
Reducing
Oxidizing
XXX
XXX
XXX
XXX
°F
°F
°F
°F
XXX
XXX
xxx
XXX
°F
°F
°F
°F
H Cone Height
W - Cone Width
Respectfully submitted,
COMMERCIA>*ESTING ^ENGINEERING CO.
175
R. A. HOUSER, Manager, Midwest Division
SO. HOLLAND, IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER CO • GOLDEN CO
HENDERSON. KY • MIDDLES8ORO. KV • MOBILE, AL • NEW ORLEANS. LA • NORFOLK, VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN. '
Charter Mambtr
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
12/19/78
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO'
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "F1
Test #5
Analysis report no. 71— 28164
%Ash
%Combus tible
DRY BASIS
89.38
10.62
Respectfully submitted,
COMMERCIAl/TJSTING 4
GINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
176
,lfM
R. A HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG, WV • CLEVELAND. OH • DENVER, CO • OOLDEN. CO
HENDERSON. KY • MIOOLESBORO. KY • MOBILE. AL • NEW ORLEANS, LA • NORFOLK, VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN.
Charter Member
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
«**.
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/8/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
ilo ieer»i!i(-a', ,.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/10/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO"
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample iuO';'"'i.a>..-.>:,
hy
V KVB, Inc.
ABMA Test Site "F1
Test #17
Analysis report no.
71- 28168
%Ash
%Combustible,
DRY BASIS
82.66
17.34
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING.
RAH/ br
Original Copy Watermarked
For Your Protection
178
SO. HOLLAND, IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN, CO
HENDERSON. KY • MIODLESBORO, KY • MOBILE, AL • NEW ORLEANS, LA • NORFOLK, VA • PIKEVILLE, KY • VANCOUVER. B.C. CAN
Charur M«mb«r
-------
F-464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
ztt.
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/15/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "F1
Test #18
Analysis report no.
71- 28170
ZAsh ,
^Combustible
DRY BASIS
91.79
8.21
Respectfully submitted,
COMMERCIALJESTING & ENGINEERING
RAH/ br
Original Copy Watermarked
For Your Protection
179
R. A. HOUSER, Manager, Midwest Division
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER CO • GOLDEN CO
HENDERSON, KY • MIDOLESBORO. KY • MOBILE, AL • NEW ORLEANS, LA • NORFOLK. VA • PIKEVILLE, KY • VANCOUVER BC CAN
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO, ILLINOIS 60601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/16/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "F"
Test #19
Analysis report no.
71- 28172
%Ash
%Combustible
DRY BASIS
86.21
13.79
Respectfully submitted,
COMMERCIAtiTESTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
180
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON, WV -CLARKSBURG, WV • CLEVELAND, OH • DENVER, CO • GOLDEN. CO
HENDERSON KY • MIODLESBORO. KV • MOBILE, AL • NEW ORLEANS LA • NORFOLK. VA • PIKEVILLE, KV • VANCOUVER, B.C. CAN
Chirt.r M.tnb.r
-------
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 Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/17/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN ORUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample- iCie-ptifrcst-o"'
!:y KVB, Inc.
ABMA Test Site
Test #20
Analysis report no.
71- 28174
%Ash ,
^Combustible,
DRY BASIS
93.95
6.05
RAH/ br
Original Copy Watermarked
For Your Protection
181
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A.'
anager, Midwest Division
SO. HOLLAND, IL • BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON. WV -CLARKSBURG. VW -CLEVELAND. OH • DENVER, CO • GOLDEN CO
HENDERSON, KV • MIDOLES8ORO. KV -MOBILE. AL • NEW ORLEANS. LA • NORFOLK, VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN
Charter Member
-------
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 Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
1/24/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
KVB, Inc.
ABMA Test Site "f
Test #21
Analysis report no. 7, 28176
%Ash
^Combustible,
DRY BASIS
90.10
9.90
Respectfully submitted,
COMMERCIAUKSTINQ & ENGINEERING CO.
RAH/ br
Original COPY Watermarked
For Your Protection
182
R. A. HOUSER, Manager, Midwest Division
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, LA • NORFOLK, VA • PIKEVILLE, KY • VANCOUVER, B.C. CAN.
Ch«rt,r Mwntwr
-------
F-464
It'
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-8434
zlk
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Fly Ash (Cyclone Hopper)
KVB, Inc.
1/31/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 8, 1979
Sample identification
by KVB, Inc.
ABMA Test Site F
Test #22
Analysis report no.
71- 28188
%Ash.........
^Combustible ,
XSulf ur ,
Dry Basis
34.10
65.90
0.71
Respectfully submitted,
COMMERC>*1TESTINGA ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
183
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND, IL • BILLINGS, MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER. CO • GOLDEN CO
HENDERSON. KY • MIDOLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK, VA • PIKEVILLE, KY • VANCOUVER. B.C. CAN.
Charter Member
-------
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 Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash
KVB, Inc.
1/31/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 8, 1979
Sample identification
by
KVB, Inc.
ABMA Test Site F
Test #22
Analysis report no.
_ 28187
%Aeh
^Combustible
ZSulfur ,
Dry Basis
91.38
8.62
0.09
Respectfully submitted,
COMMERCIAWSTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
184
R. A. HOUSER, Manager, Midwest Division
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, LA • NORFOLK, VA • PIKEVILLE, KY • VANCOUVER. B.C. CAN.
Charter
-------
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, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
March 7, 1979
KVB, Inc.
Kind ot sample
reported to ,:•.
Sample taken at
Sample taken b«
Date sampled
Date received
Bottom Ash Sample
ABMA Test Site
Test #23
KVB, Inc.
2/1/79
2/22/79
Analysis repc-1 no
71- 28178
%Ash ,
^Combustible,
PRY BASIS
90.40
9.60
RAH/ br
Original Copy Watermarked
For Your Protection
185
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. VW • CLEVELAND. OH -DENVER CO • GOLDEN CO
HENDERSON. KY • MIOOLESBORO, KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B C. CAN
Charter Member
-------
F 464
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO. ILLINOIS 60601
AREA CODE 312 726-8434
V
PLEASE ADDRESS ALL CORRESPONDENCE TO"
16130 VAN DRUNEN RD., SOUTH HOLLAND IL 60473
OFFICE TEL. (312) 264-1173
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
March 7, 1979
Sample ident>!ic?.i:or:
ty KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Flyash Sample (Cyclone
Hopper)
KVB, Inc.
2/1/79
2/22/79
ABMA Test Site "F1
Test #23
Analysis report no.
_ £8179
%Ash ,
^Combustible,
DRY BASIS
43.37
56.63
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
186
R.
ton
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM, AL • CHARLESTON. (VV • CLARKSBURG, VW • CLEVELAND, OH • DENVER, CO • GOLDEN, CO
HENDERSON. KV • MIDDLESBORO, KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER. B.C. CAN.
Ch.rt.r Mtmlxr
-------
COMMERCIAL TESTING & ENGINEEft//VG co.
GENERAL OFFICES: 228 NORTH LA SALLE STREET. CHICAGO^JLLINOIS_60601_____AREACODEJJ12 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Ash Sample (Econ. Hopper)
KVB, Inc.
2/1/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312)264-1173
March 7, 1979
Sample irtc-
KVB, Inc.
ABMA Test Site "
Test #23
Analysis report no.
71- 28180
%Ash ,
%Combustible,
DRY BASIS
29.65
70.35
Respectfully submitted,
COMMERCIAL-NESTING ENGINEERING CO.
RAH/ br
Original Copv Watermarked
For Your Protection
187
R, A. HOUSER, Manager, Midwest Division
SO HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHABL6STON, WV • CLARKSBURG. VW • CLEVELAND. OH • DENVER CO • GOLDEM rn
HENDERSON. KV • MIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER B C CAN
Charter Member
-------
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, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
March 7, 1979
Sample identification
by KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
2/8/79
2/22/79
ABMA Test Site
Test #23A
Analysis report no.
71- 28182
%Ash ,
%Combustible,
DRY BASIS
88.58
11.42
Respectfully submitted,
COMMERCIAUWSTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
188
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND 1L • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG, WV • CLEVELAND. OH • DENVER,CO • QOLOEM.CO
HENDERSON, KY • MIDDLESBORO. K V • MOBILE. AL • NEW ORLEANS, LA • NORFOLK. VA • PIKEVILLE. KY . VANCOUVER. B.C. CAN.
Crurt.r M«mb«r
-------
F-4B4
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH IA SAUE 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 Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
March 7, 1979
Sample identification
b>' KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Flyash Sample (Cyclone
Hopper)
KVB, Inc.
2/8/79
2/22/79
ABMA Test Site "F1
Test #23A
Analysis report no. J±- 28183
%Ash ,
^Combustible ,
DRY BASIS
36.73
63.27
Respectfully submitted,
COMMERCIAX1ESTING & ENGINEERING
RAH/ br
' Copy Watermarked
for Your Protection
189
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER CO • GOLDEN Co
HENDERSON. KV • MIOOLESBORO. KV • MOBILE. AL • NEW ORLEANS, LA • NORFOLK. VA • PIKEVILLE. KV • VANCOUVER, B.C. CAN '
Charter Member
-------
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 Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
2/6/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "F1
Test #24
Analysis report no. -,-._ 28190
%Ash ,
^Combustible,
DRY BASIS
86.19
13.81
Respectfully submitted,
COMMERCIA^TESTING ^ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
190
R A. HOUSER, Manager, Midwest Division
SO. HOLLAND IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG, VW • CLEVELAND. OH • DENVER. CO • GOLDEN, CO
HENDERSON, KY • MIDDLESBORO. KY • MOBILE. AL • NEW ORLEANS, LA • NORFOLK. VA • PIKEVILLE, KV • VANCOUVER. B.C. CAN.
Charier Member
-------
F-404
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 226 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60801 • AREA CODE 312 726-8434
KVB, INC.
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
March 7, 1979
Sample identification
by
KVB, Inc.
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Fly Ash Sample (Cyclone
Hopper)
KVB, Inc.
2/6/79
2/22/79
ABMA Test Site "¥'
Test #24
Analysis report no.
71- 28191
ZAsh ,
XCombustible,
DRY BASIS
36.55
63.45
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
191
SO. HOLLAND. IL • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER CO • GOLDEN CO
HENDERSON, KV • MIDDLESBORO. KV • 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 «0601
AREA CODE 312 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
2/12/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "¥'
Test #29
Analysis report no. 7l_
%Ash ,
^Combustible,
DRY BASIS
86.93
13.07
Respectfully submitted,
COMMERCIAL TKTING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
192
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG. WV • CLEVELAND. OH • DENVER. CO • GOLDEN. CO
HENDERSON. KV • MIDDLESBORO, K V • 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 60601
AREA CODE 31Z 726-8434
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reponed to js
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash
KVB, Inc.
2/13/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 8, 1979
KVB, Inc.
ABMA Test Site F
Test #30
Analysis repori no
71- 28195
%Ash. ,
%Combustible ,
%Sulfur ,
Dry Basis
89.81
10.19
0.09
RAH/ br
Original Copy Watermarked
For Your Protection
193
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A
Charter Member
SO. 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. KY • VANCOUVER, B.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 Company
6176 Olson Memorial Highway
Minneapolis, MN 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Fly Ash (Cyclone Hopper)
KVB, Inc.
2/13/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO-
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 8, 1979
Sample ider'.'ica'.ic.
-'' KVB, Inc.
ABMA Test Site F
Test #30
Analysis report no.
- 28196
ZAsh ,
ZCombustible,
ZSulfur ,
Dry Basis
35.49
64.51
0.43
Respectfully submitted,
COMMERCI/CfTESTING ^ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
194
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND IL • BILLINGS. MT • BIRMINGHAM, AL • CHARLESTON. *VV • CLARKSBURG. WV • CLEVELAND, OH • DENVER. CO • GOLDEN, CO
HENDERSON, KY • MIDOLESBORO. KY • MOBILE. AL • NEW ORLEANS. LA • NORFOLK. VA • PIKEVILLE. KY • VANCOUVER, B.C. CAN.
Charter Member
-------
F-464
tj
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601
AREA CODE 312 726-8434
ztk
KVB, INC.
A Research-Cottrell Company
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
Date received
Bottom Ash Sample
KVB, Inc.
2/14/79
2/22/79
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN RD., SOUTH HOLLAND, IL 60473
OFFICE TEL. (312) 264-1173
March 7, 1979
Sample identification
by KVB, Inc.
ABMA Test Site "f
Test #35
Analysis report no. _._ 2 ft 18 5
%Ash. ,
^Combustible,
DRY BASIS
86.18
13.82
Respectfully submitted,
COMMERCIALJ53TING & ENGINEERING CO.
RAH/ br
Original Copy Watermarked
For Your Protection
195
R. A. HOUSER, Manager, Midwest Division
SO HOLLAND. IL' 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.
Charter Member
-------
COMBUSTIBLES DATA SHEET
SITE
Crucible
Number
Sample
Origin
Crucible
Weight
grams
Crucible &
Sample Weight
Post 110°C gms
Sample
Weight
grams
Post 750°C
grams
A Weight
grams
Combus
tibles
6 &41**f'*
A<
7.9UT
7V
/1 . 4-63?,
-72-73,
AVG .
7* -7,5
l-l>
AVG.
/». a » 0
/.
AVG.
J7.474T3
77
_tt
-------
rucible
Number
Sample
Origin
Crucible
Weight
grams
Crucible &
Sanple Weight
Post 110CC grr.s
Sample
Weight
ar ams
Post 750°C
grams
A Weight
grams
Combus
tibles
0***
AVG.
/*. //if
33
s>.
Of
AVG.
71
ft.
If- U -O
AVG.
/e.
77
AVG .
H
AVG.
l-lrt-7
AVG.
AVG.
AVG .
187
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
SAMPLE IDENTIFICATION P/j.
DATE SAMPLE TAKEN /
TEST PERFORMED BY "p^
Screen
Sire
Passing
0) W
M -H
id «
H *
4i -*4 £
« V O>
2 * "
0) ^-
U *
W *•*
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O.
Cumulati
Weight
Passing
(gm)
ulative
t
cen
sing
r
s
(
C
Per
Pas
US-
*•§«•!!
o) 18 w e
-n £ -
w w
Du
(
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3200.^
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P.S7
yv
Ma. Mo. No. No. Mo.
4' J'IH'7* 1H' f *' H- V V 4 t W 14 20 30
IK'
V
Mo. Mo. No. Mo.Mo.No. MB. Mo. No. No.
4 (10 W20W40M M 100
SIEVE OPENING
No.
200
198
No.
325
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
DATE SAMPLE TAKEN_
TEST PERFORMED BY
11C I'
SAMPLE IDENTIFICATION
Screen
Size
Passing
Trf?
1"
j."
^
•4"
M».^
^ '(,
*J
01 C7>"
S «) §>
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4-1
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41
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7.0
13.2
11-1
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J-1
10.1
Cumulative
Weight
Passing
(gm)
ot^oS.)
A 70J, 1
n(,(,.°i
^3.7
39/. <
3/6.*>
Cumulative
Percent
Passing
(%)
JOO.0
93.S
(,0.1
<* 3.3"
y3.7
/A?
Sieve
Shaker
Duration
(min)
/
^
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k
100.
100
V
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in
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4
No. No.
t 10
No. No. No. No. No.
It 20 30 40 SO
M 100
Me.
200
\
4'
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M- V
X- No. NO.NO. No. No. No. No. No. No. No.
4 I 10 1C 20 30 40 M M 100
SIEVE OPENING
» O
C
o
m
X
M -«
to
10
100
200 321
199
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
SAMPLE IDENTIFICATION
DATE SAMPLE TAKEN / \ fb(~)el
TEST PERFORMED BY
C C
0) -H
0) d> 0)
M H »
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9 « «
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01 0) 4J "c
w w o
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100-0
No.
4' 3'W2* IH" 1* *' H' V V 4
No. No. No. No. No. No. No.
8 10 W 20 30 40 SO
80 100
200 33
4"
K- V
V No. No. No. No. No. No. No. No. No. No.
4 8 10 16 20 30 40 SO 80 100
SIEVE OPENING
No.
200
200
No.
32S
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
DATE SAMPLE TAKEN
TEST PERFORMED BY
) t I
SAMPLE IDENTIFICATION
een
e
sing
Scr
Siz
Pas
4J
0) O>^
(3 4) &
t* s —
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to 01
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01 01 &
0) ^~~
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^4 ^»
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cu
Cumulati
Weight
Passing
(gm)
tive
t
g
a
n
in
Cumu
Perce
Pass
Sieve
Shaker
Duration
(min)
32L
0
311
36-0
JL
I3I&.3
We.f
- 3s)
4" 3"2>4'2" IK' 1
No.
4
No. No. No. No. No. No. No. No. No.
8 10 16 20 30 40 60 80 100
No. No.
200 325
V
No.
No. No. No. No. No. No. No.
4 8 10 16 20 30 40 50
SIEVE OPENING
No. No.
BO 100
No.
200
No.
325
100
201
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE F
SAMPLE IDENTIFICATION
DATE SAMPLE TAKEN )
TEST PERFORMED BY
7-7«/
O<
0) -^
0)0)0!
M M W
o •* 8
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H * —
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£
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0) 4) 5>
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K) 4J C
•j J2 -H
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3 0) «
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HI
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1A2_
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14* I
r
£77, /
3-9
it.
No.
4' 3'2H'2' 1»* .V *' H- V V 4
No. No. No. No. No. No. No. No. No.
8 10 U 20 30 40 SO 80 100
No. No.
200 32S
4' J-2H-Z' IH' V
'<.- No. No. No. No. No. No. No. No. No. No.
4 8 10 18 20 30 40 SO 80 100
SIEVE OPENING
No.
200
No.
325
100
202
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
SAMPLE IDENTIFICATION
. l>>'/
DATE SAMPLE TAKEN_ /
TEST PERFORMED BY
o>
c c
0> -H
a) 0) m
M N W
o -H id
w w o<
TOP
\
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£"•
''4"
&.9
/•o* /(.
t)
0)01 —
3 'i
V 01 &
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l£tf
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4J CJ>
(0 4J C
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e -H to o»
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o s a.
y^<»j /
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3302,*
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100
4- 3'2H'2' 1»' T
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No.
4
No.No. No. No. No. No. No.
8 10 IS 20 30 40 SO
No.
100
No. No.
200 325
4- 3-2H-2- IK-
V
'(.' No. No. No. No. No. No. No. No. No. No.
4 8 10 16 20 30 40 SO 80 100
SIEVE OPENING
No.
200
No.
32S
100
203
15900
-------
KVB
SIEVE ANALYSIS TEST REPORT
TEST NO.
TEST SITE
SAMPLE IDENTIFICATION
V* • %'~t-
DATE SAMPLE TAXEN_
TEST PERFORMED BY
/ "
Screen
Size
Passing
01 "i^
a « a>
m j:
o> w 5»
z » —
4J
0)
o
M
V
ve
Cumulati
Weight
Passing
(gm)
Cumulati
Percent
Passing
(%)
Sieve
Shaker
Duration
(min)
. 0
ft,*
/a*ff.3
II S"l.f
. 1
ins
13,7
I
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KVB
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-------
KVB
SIEVE ANALYSIS TEST REPORT
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-------
KVB
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-------
KVB
SIEVE ANALYSIS TEST REPORT
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210
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325
15900
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing)
REPORT NO.
EPA-600/7-80-065b
3. RECIPIENT'S ACCESSION NO.
. TITLE ANOSUBTITLE
Field Tests of Industrial Stoker Coal-fired Boilers for
Emissions Control and Efficiency Improvement--Site
F (Data Supplement)
5. REPORT DATE
April 1980
6. PERFORMING ORGANIZATION CODE
AUTHOR(S)
R.J.Tidona,H.L.Stix,J.E.Cook, and M.G.Gabriel
8. PERFORMING ORGANIZATION REPORT NO.
. PERFORMING ORGANIZATION NAME AND AOORESS
KVB, Inc.
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
10. PROGRAM ELEMENT NO.
EHE624
11. CONTRACT/GRANT NO.
EPA-IAG-D7-E681 and
DOE-EF-77-C-01-2609
2. SPONSORING AGENCY NAME AND AOORESS
EPA, Office of Research and Development*
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AN.O PERIOD COVERED
Supplement; 12/78-2/79
14. SPONSORING AGENCY CODE
EPA/600/13
15. SUPPLEMENTARY NOTES (*)Cosponsors are DOE and the American Boiler Manufacturers
Assoc. Project officers are R. Hall (EPA) and W. Harvey Jr. (DOE). The final tech-
nical report is EPA-600/7-80-065a.
16. 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 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, and coal size consistency data.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.IDENTIFIERS/OPEN ENDED TERMS
c. COSATI Field/Croup
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
Fly ash Re injection
13 B
13A
21B
21D
14B
11G
07B
13. DISTRIBUTION STATEMENT
Release to Public
19. SECURITY CLASS (This Report)
Unclassified
21. NO. OF PAGES
219
20. SECURITY CLASS (This page)
Unclassified
22. PRICE
EPA Form 2220-1 (9-73)
211
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