ABMA
American
Boiler Manufacturers
Association
1500 Wilson Boulevard
Arlington VA 22209
DoE
United States
Department
of Energy
Division of Power Systems
Energy Technology Branch
Washington DC 20545
EPA
US. Environmental Protection Agency
Office of Research and Development
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
EPA-600/7-79-0416
February 1979
Field Tests of Industrial
Stoker Coal-fired Boilers
for Emissions Control
and Efficiency
Improvement-
Site B (Data Supplement)
Interagency
Energy/Environment
R&D Program Report
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the INTERAGENCY ENERGY-ENVIRONMENT
RESEARCH AND DEVELOPMENT series. Reports in this series result from the
effort funded under the 17-agency Federal Energy/Environment Research and
Development Program. These studies relate to EPA's mission to protect the public
health and welfare from adverse effects of pollutants associated with energy sys-
tems. The goal of the Program is to assure the rapid development of domestic
energy supplies in an environmentally-compatible manner by providing the nec-
essary environmental data and control technology. Investigations include analy-
ses of the transport of energy-related pollutants and their health and ecological
effects; assessments of, and development of, control technologies for energy
systems; and integrated assessments of a wide'range of energy-related environ-
mental issues.
EPA REVIEW NOTICE
This report has been reviewed by the participating Federal Agencies, and approved
for publication. Approval does not signify that the contents necessarily reflect
the views and policies of the Government, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/7-79-041b
February 1979
Field Tests of Industrial Stoker
Coal-fired Boilers for Emissions
Control and Efficiency Improvement
Site B (Data Supplement)
by
J.E. Gabrielson, P.L. Langsjoen, and T.C. Kosvic
KVB, Inc.
6176 Olson Memorial Highway
Minneapolis, Minnesota 55422
lAG/Contract Nos. IAG-D7-E681 (EPA), EF-77-C-01-2609 (DoE)
Program Element No. EHE624
Project Officers: Robert E. Hall (EPA) and William T. Harvey, Jr. (DoE)
Industrial Environmental Research Laboratory
Office of Energy, Minerals, and Industry
Research Triangle Park, NC 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, DC 20460
U.S. DEPARTMENT OF ENERGY
Division of Power Systems/Energy Technology Branch
Washington, DC 20545
and
AMERICAN BOILER MANUFACTURERS ASSOCIATION
1500 Wilson Boulevard
Arlington, VA 22209
-------
ABSTRACT
The Data Supplement is a compilation of test data presented in greater
detail than was practical in the Final Technical Report. It is intended
to provide the necessary details to other researchers who are interested
in performing their own analysis. Readers are referred to the contract
final report for information as to objectives , description of facility
tested and coals fired, test equipment and procedures, interpretations
and conclusions. The Final Technical Report also contains data summaries
not found in this volume. The Supplement contains panel board data for
each test, detailed particulate, 62, CC>2, NO, SO2 and 803 data, particle
size distribution data, modified smoke spot data, chemical analysis of
the coal and coal size consistency data.
11
-------
TABLE OF CONTENTS
Section Page
FOREWORD iv
CONVERSION FACTORS v
1.0 PANEL BOARD DATA 1
1.1 Control Room Data Sheets 2
2.0 PARTICULATE DATA 77
2.1 Particulate Data Summary 78
2.2 Particulate Data Sheets 84
2.3 Particulate Lab Worksheets 129
3.0 GASEOUS DATA 176
3.1 Gaseous Emission Summary 177
3.2 Gaseous Emission Data Sheets 180
3.3 SOx Data Summary 213
3.4 SOx Data Sheets 216
4.0 SPECIAL TESTS DATA 227
4.1 Modified Smoke Spot Data Sheet 228
4.2 Particle Size Distribution - Brink 230
- SASS 242
- BAHCO 262
5.0 FUEL AND ASH ANALYSIS 269
5.1 Commercial Testing Analysis 270
5.2 Combustibles Analysis 310
5.3 Coal Sieve Analysis 316
111
-------
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 B; as it is the second boiler tested under
the program entitled, "A Testing Program to Update Equipment Specifications
and Design Criteria for Stoker Fired Boilers."
1Gabrielson, J. E., et al., "Field Tests of Industrial Stoker
Coal-Fired Boilers for Emissions Control and Efficiency Improvement - Site B",
EPA-600/7-79-041b, February, 1979.
IV
-------
CONVERSION FACTORS
ENGLISH AND METRIC UNITS TO SI UNITS
To Convert From
in
ft
ft2
To
cm
m
m2
m-
Multiply By
2.540
6.452
0.3048
0.09290
0.02832
Ib
lb/hr
lb/106BTU
g/Mcal
BTU
BTU/lb
BTU/hr
J/sec
J/hr
BTU/ft/hr
BTU/ft/hr
BTU/ft2/hr
BTU/ft2/hr
BTU/ft3/hr
BTU/ft3/hr
psia
"H20
Rankine
Fahrenheit
Celsius
Rankine
Kg
Mg/s
ng/J
ng/J
J
JAg
w
w
w
W/m
J/hr/m
W/m2
J/hr/m2
W/m3
J/hr/m3
Pa
Pa
Celsius
Celsius
Kelvin
KeIvin
0.4536
0.1260 _
430
239
1054
0.002324
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
COAL FUEL ONLY
ppm @ 3% O2 (S02)
ppm @ 3% O2
ppm @ 3% O2
ppm @ 3% O2
(S03)
(NO)
(N02)
ppm @ 3% O2 (.CO)
ppm @ 3% O2 (CH4)
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
0.851
1.063
0.399
0.611
0.372
0.213
KVB 15900-521
-------
CONVERSION FACTORS
SI UNITS TO ENGLISH AND METRIC UNITS
To Convert From
cm
cm
m
m
TO
in
ft
ft2
Multiply By
0.3937
0.1550
3.281
10.764
35.315
Kg
Mg/s
ng/J
ng/J
J
J/kg
J/hr/m
J/hr/m2
J/hr/m3
W
W
W/m
W/m2
W/m3
Pa
Pa
Kelvin
Celsius
Fahrenheit
Kelvin
Ib
lb/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
2.205
7.937
0.00233
0.00418
0.000948
4.303
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
COAL FUEL ONLY
ng/J
ng/J
ng/J
ng/J
ng/J
ng/J
ppm @ 3% O2 (SO2)
ppm @ 3% 02 (S03)
ppm @ 3% O2 (NO)
ppm @ 3% 02 (NO2)
ppm @ 3% O2 (CO)
ppm @ 3% O2 (CH4)
1.18
0.941
2.51
1.64
2.69
4.69
KVB 15900-521
-------
SI PREFIXES
Multiplication Factor Prefix SI Symbol
1012 tera T
109 giga G
106 mega M
103 kilo k
102 hecto* h
101 deka* da
10-1 deci* d
10~2 centi* c
10-3 milli m
10"6 micro y
10-9
nano n
10"12 pico p
ID'15 femto f
10"18 atto a
*Not recommended but occasionally used
vii KVB 15900-521
-------
EMISSIONS UNITS CONVERSION FACTORS
FOR TYPICAL COAL FUEL (HV = 13,320 BTU/LB)
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 15900-521
-------
SECTION 1,0
PANEL BOARD DATA
I.I CONTROL ROOM DATA SHEETS PAGE 2
-------
Coal Designation:
Ib/hr Steam:
Ib/hr Coal:
Ib/hr Feedwater:?
5 , •} 4
PANEL BOARD DATA
ABMA TEST SITE B
Test No. /
Date: __[•> /
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
//- 2 -
Wo**r
Hi- o 5^0
6£~-cj yj
_rVxZ>'/
2 to
.S^l °
2^0
-> '/^
/ 2 •'•-• )
t/'S&.-.JLI
V^^sv.s-
6rj/ s<-?
s'^^ > ?^
.?VV
o-e
- o.j_
-o>
~.og
-p 4-
. —
—
/ f.c~
^5j"
/^-r
rr~
S^r
H*
->6o
i'^o
?-<{<->
^<-Vo
/^ /^
VV^-o'v' ?
V^^Sv?
<^.s-j»s'
3'^J ^£-0
3V-J~
O.S7
-o. /
o. r
- , 07
-2.
—
- —
/?S"
^?J^
/^s'
^ - /CTO
S'S-
Vo
-'Co
.r1/''5
^t/o
^•y.:>
A Research-Cottrell
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
?r
o
O - ^~o
3 -<;
31-
~ 0.2
W
«•//
,5r
-6
^b
/ ?£>
~) &
<~l.r
? 3
a s~~
y
S •
,',••>• r
c>
C- • S^=>
, i"
;?•/
-<^\3
S7
*/ J-
3<,
*
V?
/ ?,v
•7o-
Vo"
^^>,r-
O-i- -T
6". c^
i". c7
/£••. '-"
c-
r- s~c:>
, V
JV
-0.3
r.3
-7i-'
^
'/7
?y
/yc
'<'• T
He.r,
_Z'2 -T
2r. ,s"
-i'-i"
i'li"
REMARKS;
A Research-Cottrell
-------
Coal Designation:
Steam: ST
Ib/hr Coal: >•')-
Ib/hr Feedwater :
PANEL BOARD DATA
ABMA TEST SITE B
Test No. ^~
Date: I?/' 2*1 /
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
| FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
1 FD FAN IN TEMP °F
1 ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/^~0
i/<-tO'ior
L<2 O <=i<-/J
&r JVi ;
ryj/"/^
n(
.?
- . i
-.LI
-.£,
- /• y
- —
/ PS-
2 7J'
y~ac>
$& - i w
£'!T
9-c.
3F&
f 3 ^
3 Y 0
J^^'
/
—
/ S c-
27J"
no
G^
-s-i-
21
?C"O
^"'4-?
3- >-fd
J~< ~JC
iVJ^i-?,
^/
. r"
/
^ /j-
-. ?j"
-/9
—
/^j-
P77
/
/r
60
2.J?
^rs>
rv^
cz Vo
->?o
A Research-Cottrell
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
Co n c
0
o - -i'°
• y
P-o
,-i i~
j~/
?l
1)
-c/o
J.-T'
/?2
~7 • i"
^/J"
2-2. J-
3-i". ±T
S'."
/". i~"
. '
/ 2.
dJ
Jc-5
/
21/
— AT
JV
PA
JLJ"
-3S7
a 7
/^
7-s"
y.j-
? > • s"
?C~. i"
^".-s"
^-.>"
/J~
C^
o -r~o
/
J2t/
— . .?,->
J~V
y-q
^&
-^"c-i
3-y
/**-
7t>"
*-l.^~
^2.J"
^2 r. y
^ .^~
-r.r
REMARKS:
/'<-...
A Research-Cottrell C^ipany
-------
Coal Designation:
Ib/hr Steam: -ST^'i 333
Ib/hr Coal: £ ^Oc3
Ib/hr Feedwater: _<>'>>,
PANEL BOARD DATA
ABMA TEST SITE B
Test No. ^
Date: _/_X_S / 7
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
PD PAN TM T"PMP °"P
ECON OUT -GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
// & 6
W?9'7
4 I I^IC
bl^Xi?
^(f y <-/ 2./
^H
o. ?
- , >
-. 5
—. 1
-2.0
""
/8^>
D.^0
/&&
'•fs"
s~o
2^
?S^
5-J o
2 ^ ,^
^70
/I • ' 7
im-ft(38
//^?cf'S.'J
£v?g?£
S~t>J <4fG
V-(
0. &
- . 1
_, -V
_ -j>
-/•?
— —
/gs'
^0
/ez>
•C&
^i~
^±'
3fZ>
5VO
^ ^iT
^ZO
//•^^
i/L/^^70
y,2 ->Cffl~
bivr??
±~i>^ $-*<-/
^
o.5>
— . /
- . ^~
-, 7
'/-7
/fo
^^/cb
/^c9
-Cs"
^"0
2^'
_crr>
-3-"Y<£>
?'r^
a?r")
A Research-Cqttrell Corftany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR. HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
ii.sr
A?
0 ST^
~ /
P*
-. 3
Xiar
31
31
-/e
3^?
/gs~
7,0
-/•s-
2-2-tJS
J2.i-o
H-S-
5"c>
/'-?.6
r
O - iT£>
O
^2-
— . J-l*
S3
2^
3-S-
- 3S"
Pa
/
S" jT"
/>.e>
£>
<5> -20
-2.
21
~. 3.0
J~«/
.2 2
y-f
-Hi
?->
/?£'
-------
Coal Designation:
Ib/hr Steam: tfi) ,
Ib/hr Coal: ( O , •$
Ib/hr Feedwater: 9^,73/
„>^if
PANEL BOARD DATA
ABMA TEST SITE B
Test
Date
Page
No.
/
1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR X 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H20
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/o '/'
V> B ^-)
^ Lffg, ?6
6 %•/??<-/
tfrWl
2 Y
^. /
~. ?
- ?
-2-1
6±
/O &•
ftr
^ x&
//2>
/A"
9s-
4*'
3?y
i'i"^
-2SZ>
S~&
//-//
«*?*•&
•>
/qo
22 j-
/gs-~
//o
f&v
<-/?
-3*0
J>~^
2Jf
Sb
, /A ://
US-tot
y-fe v//
^J~
- 2./
6 a-
/^»?
/e*~
2S^
&0
9s-
9^
c/S'
f^j"
^~Y5—
^V7
y?
/2.-y?
Y i/ftf
V
•
A Research-Cottrell C^ipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
t.r
/O
10
2.
*-/:>-
-•3
&/
^
^
~ ~. c>
I ~ —
^'o
X-S-
o - Jo
1
Hi
— . 3
Cl
S~?L
V/
-/o
H*~
/&-±-~
~7.±'
"-f-S-
? J ^ 0
^ J'.o"
3T-0
-TO
g'.o
^0
f^f'f* I' 0>
y. j-^ti- -
£~
Y^
—.3
^J-
vr
*o
-?
Y$r
/££>
~>. £•"
V.JT-
^-?. J-
•2 J-70
v~s:cJ>
>r:o
F.a
f
^•/-&>
-/
V/
-• Jj~
ry
v/
y/-
-/a
iz
/#>j-
7-J-
^24 :0
/^-o
XJ.'
REMARKS;
A Research-CottrellHimpany
-------
Coal Designation: fJ
Ib/hr Steam: q^ jj-,
Ib/hr Coal: /O} $o 3
Ib/hr Feedwater?
PANEL BOARD DATA
ABMA TEST SITE B
Test No . S .A- ~ Jb
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H20
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
fr'/3
i/2ia. 73
WfJi-7
&WP>7;
jT?/?/0
s*
^
&.?
- a ?
_ 0.2.
~o.s
-2-t-.
/of
.& 2.
/« ?
?$$~
/?&
fo
9s~
//&
??e>
-S3T.*
2 VJ"
^v^"
P-£CJ
/^•^6
^^9JCP
<-( W ci
£~?3 fr X 'Z.
^B
33
o.£
— O 2.
~ 0 . _J
-0. >
-/. *•
/o-f
^ 1
/^i
~>SC
ff-3.
Sfrc^r
^60
J~"ro
^ vj
^o
^c, f
/d"//a_
Vi H- 3 9 7
Wf '/f ?
/i -?r-jsy
•-i "'J' ?JCj"
-2.J-
o.S"
~ O-Jt
- o.C
-o.7i'
— -2-0
<"=?&
Q ^7
/r?
j .f^c
A Research-Cottrell
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No: J
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR RE INJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
So
H 60)
O^rot- £t,-u
57 **
yj m,
n
O/L*.
y-ttr-
is>jrA-
7*c>
H--f
^2,
2- •-/. ^
JT.o
?-°X?.s-
S'.o
//-Jo
&oj;
0^-
ZfA-
-.zs-4
d^C? frl
7C/K
4T%
O t1\
v? A-
/yjA-
si'.o
1-Z~
-^2.
^*~
$ -0
REMARKS;
A Research-Cottrell Jijpany
-------
Sheet & of
KVB
NOTES
TEST NO;
Lrs
..«..- «~*
-V •—-U.T
oF A*.
-- J ~'
'tJ
4,
TEST NOr K.r
A.
"-•—j<
-<». I~.^
TEST NO:
"
~~«.Se.
Urf SiSt- ) >
^.. . \ •Ji^.
TEST NO;
f/'*
* P
tn>
/^5 ' /%5 V-^-*^— >-**<^ -1-
o-ff'
TEST NO: ^
JLf~
:£
-------
Coal Designation:
Ib/hr Steam: i^'o/ c\$i
Ib/hr Coal: /£j >3.J
Ib/hr Feedwater: / sTt?j oot>
Test No
. t
PANEL BOARD DATA
ABMA TEST SITE B
Date: / / / / / ?&
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H20
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
( o . • ) 3
Lp-^gl &
y/?9 ?
//O
i~nr
2 7JT
/S^>
A/._r
fcv
/ &*o
YO/
syo
2^s~
P?o
//•*i
yj±
vyffy?
6t? on
3'VJ-Vo ^"
2j-
'- ^
-. /
fo.J.
-O.q
-3.S-
67
//o
177
{
P?J,~
/S-3.
/7s-
/s-^T
/ i~o
J*?£
^Vi~
^ yy
270
j |-r»-.ar. ^-.
&'-l°t
<-/•)-*( 9/0
ys~c*o*4 *•
£ S '??-£,-}
-i'~tss-*i a.
3.i —
s.v
-. /
i-o.-s
-/ i-
-H.G
6J
//O
/7J~
274'
/(O
"• /^"&
/•ri,~
/J^"
^^
.s- ^J>
7 Vj
^70
/!>' 03
*/2ooc= e.
tJ>-&/Yf
6 5?«j-^>
•>-;_ryvo
20
/a
— /
-•-o. X
-/A
'-* 3
//J
2c?J~
2 7J~
f&~>
/
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR RE INJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
1-2-
/O
O O j
O
61
-- . i
ss-.s-
6+
JTY. J-
s~o
? 2
/es-
£><J-'/s.r
/o
7
OO i
oA-
6i> A
- z.A
y-^-A-
S"^-i"A
s-y fr
~s.b n\
?•?- 4
/^J>
8. «
r-o
27 0
26. J"
s. .r
i~ o
/o. j—
7
O> S5 J.
c3
^
- 2
J^s-
6~J-
yv
>S^>
dT-
/c5i-
/o
7
O o s
o
6 3"
— . ^
7S>
-------
Coal Designation:
IbAr Steam: /S(t
Ib/hr Coal: /gj*,
Ib/hr Feedwater: I
\
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
(0'- **(
L(2o-i^
6&
12 '-&J>
130. 72.
^ros^vj—
6*3 Co?
i~?7
7o
$»
^o\~
37 ST~
/to
/6-^k
/J'3'
/fsr
V'CTO
^^
it^i-
J-3 Oo S
A Research-CoKrell
any
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
S02 , PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
^ • 5>
7
O& i
o
6^
— G. i
7z
^
&r-r
3 $,~~
7
/!3
2T.o
>~-0
6-0
12.£>
S, O
6". 0
3-o/j. c
So
f
OGL
e>
6S
-O i
-?±r
^ 7
Ci-
^3~
<^0
(23
l\
Tt< t-e -
/ D , SO
//
o
A Research-CottreH|C)gnpany
-------
Coal Designation:
lb/hr Steam: /
G
-0. 1
-/•^
-3.J
~7o
/OJT
1 13
26>o
no
I2o
/**.-
7o
10
L{C>&
^ iO
1 7
y^>(? 5-fff 2 i-&
29
y.s
«3
-o.j
-^
- V- ?
?3
/Of
no
'1 6 o
/?«?
AT?
/6>o
J'-sTo-
p. \-<;
(Soi
/^:37
yj-iS_r^^
V3^ yy6
7//^3i
•Ty^^^-
•s/
"?.o
-o.x
~/J>
-/•3
- * y
;^
/o?
11°
2-<*O
/3
A Research-CottreUlCempany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02 , PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
K/^-.i <4 *
£ fo~f,l frfi
1*-
. 7
5". 0
?'3~
J'V/^^
&t>.^
IV
c>o ^
c->
C->^"
- 3
Cr-
s>y
<£s-
,S,-£>
VG
Sg&
7S~
j;~ o
'21
•77
j>; j-
3-&
•f <--> /?to
C^._3
/ °
c;L^
/
j-
£o
^'8
9o
/^^
2^
-JT,
5"r-
27
^"-.r
3.0
^ °/?*0
REMARKS:
ft f-
r?c*2>
//t-,
./fr
A Research-tottreljfgipany
-------
Coal Designation:
Ib/hr Steam:
Ib/hr Coal: / £,
IbAr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No._
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 IbAr
STEAM FLOW x 1000 IbAr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/6 :/Cf
VJTG 7a.
~o.?
-2.X
6«
A?J-
/4v
P- 6 o
/^
//«?
-2-&CP
/fi3
7 o
J?O
JTSX;
^.^r
Oo ±>
/?./?
V^rc-i6
- /. c,
- J? o
<5J^
/o6
/*}*-
2-co
2 oo
/^
2^,0
J?oO
7'
TCo
CSTi—
P«-/t~
00 -S
/r.v?
V-^6 5"09
-X,o
-/.o
^i-
/C3 €
;r$—
?-t,6
/-&
2-
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR RE INJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
?.<*
V
£>o3
c?
£2
- 3
^^.
67
^r
<:y
//
/<*?£-•>
7.s"
<£-•&
"i —i
3-<<
6-0
Sf-c?
4 / sr
£,o
/O -30
r*>o J>
/
<£5-
— 3.
~~?<^>
&t
6Y
?c>
I*.
/*r
7.S~
5~0
76
2 X
J>~0.3
0
2<-~
-3,
?0
tr 1
6£-
Yo
/2
/ &o
?• y
iT O
^?<^
^>S
J~^"
^:o
•//r
REMARKS :
X
A Research-Cottrel
pang
-------
Coal Designation:
Ib/hr Steam: 6,i,.
- o •/
-o.-/
-0. 7
' P.t?
63
/o?
/£c
^6cJ
/1&
y*-
60
2 7
J^^
^(, 7
-/. -f
// ^4-
<-/j?-r-?
-0-^
2.?
<^ */^
XXc3
/£
^^
£&
V'f
.? £o
J~J?J"
^<-/(D
oo-S
A Research-CottrellJgjnpany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No: /Q
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
(0
3
-1
-?o
- o . o
^-o
s~&
y-f
-Ho
YA
/yi-
7.o
-J~
^^. O
29.0
^-s—
7.0
REMARKS;
\L
A Research-CottrelSSipany
-------
Coal Designation:
Ib/hr Steam:
Ib/hr Coal:
PANEL BOARD DATA
ABMA TEST SITE B
Test No. //
Date: / /I.
Page: 1 of 2
' ' j J**~?
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
fy'-37
( -J ^^?O/
f ^ f ^^? \ "™ '
""7 / /" /* **3 if
f O a Of
Joscs-j
2^
o, ?
-02
-O./
- 1-0
-2.P
6*
//o
/*i-
i«/r-
/?o
/£>&
/^d>
J,-^
&>
7>s>-
Oo
2^0
OoS
/o :i •)
y-S-fa a •/d'"
?fl
0,?
o
- 0.-?
-o. 7
-2.-?
&>•(
/>0
tfo
2<-S*
sr&
/Oo
?
yj-«»6 f
V^'.^VS
7/6 /;«?
6&W//
09
O. 9
-0.5-
-O.i-
-/•o
- *.'/^
V'fTf^J
/J<>--
//O
/8s~
2-Jf'
Xs-c-
/^>o
9s-
-To
7Pi-
-rvo
^Yo
I2 7J —
A Research-CottreJEQmpany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
\f(# •>-<.'. O^ £>Ca,'g>f!> -/& 7 i"2
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
?.o
<7~/2
£*>£
fyf fLrtc-t*.
£>
V.s
- O. -t !>~~
6r
.ya
Cl3
-3
6*?
/ So
l,c-
< <.-•
^7
^2-Cj
C-
H
2 r/_i
9.0
-
<^-A
0
-//
— . -o~
^,?
r?
^/^
^
72
/fc>
?-->'
-£':a
.?->. J^
arr
(.,,
3
J'-i'/j.j'
Jo
/o -/*
o&s^
-/
'A
' ij~
r?
j"?
J5^
~" j'^
j"^,~
/~
.A~.^>
J?7 i"
2-r
c.
•3.
~3-i~/j.x'
REMARXS:
1^4^
,/r
5 /to i/
A Research:Cottre
pang
-------
Coal Designation:
IbAr Steam:
Ib/hr Coal: /
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No./2
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR X 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H20
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/TT'^o
ysy/-?*?
Kiss**.
7f7/^f
6<=>.
/8-f
7-70
if
~o.f
-&.\
~0.
/a^
47
— - —
2 To
r-Jo
? «/o
2-&0
/£• r?
yj-f2j/
fJ*S78
7i ->3rif
ga'S^to*
jr~
.S
-o./
_o./
-/.o
-2.J"
^/
J'?
/ftf
2-10
/
A Research-Cottrelljgwipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
£.s-
Z^z*
OO.S
o
. 2
£.*~
?.o
^AO i
£~C>
P-/0
<3<=> 3
/
Y2
~O. "2. 3~~
^CJf
«/r
^0
o
3.0
2.0/7.0
^^
S-'3
cio-S
/
.«»
REMARKS:
A Research-CoHrel
pany
-------
Coal Designation:
Lb/hr Steam: /^
Ib/hr Coal: /<•(<{, 9 PL /
Ib/hr Feedwater: / 5~j 3 2. 7
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date :
/
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H20
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
Pn PAN TN TPMP °P
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
H- *3
V-V-^7ii"
c/39&/0
7.22.r<2, *•
£0?j-3a
:? V
fr
-0.1
-o.^f
-/,/
~4
/S~5~
/S~&
TO
?VO>~
^'30
"210
OO f
/J~/0«~
VS~>7^?
VJTC30
'~~? -~J
(^O^S 1 S
?^~
/.&
- 0. i
O
-/.&
- 3. r-
^re>
/
/•s^o
O
y?sr
S~GO
2-^&
Ooj,
ts-.-*.3
y.s.^- ?£-? ?^?
V^f^j-v
-7-2> 7^-y
tSb
/s*-
(£c2
^ ?0
i~?J-
-^ <-/r"
0(5 ^
/£••/•/
^'V^oi~
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No: />
Page 2 of 2
OXYGEN, % (jV<< "^ '• -\» &o-^ O
J?o
7i
/7r~
~t.-?T
^•&"
T.-z-.C-
£.0
?-0
L^zk^'
i-i
//- f<*
OO-J
+3
to
- . J
?0
6*^
€>G '
VD
"7?
/?7
?.*r
>S~o
;?2..f-
7?j-
£.0
l-c>
V-J-/^-.o
V.7
/2--fG
fsc^s.
Cj
£/
-. is'-
£Y
t^^
S
J3-f~
rV. o
d 0
_?. o
^^y^-o
?..<-
f-/2_
O»J
0
JT^
-.2^-
76
?o
& O
J"o
72-
^cPO
7,0
V.j"
?JTO
5_rr^-
<£-C3
J"-0
^0^7^
^-/J
<5C,^
y
^v
- . ^J-
^J-
?r-
G;0
. o
& ° /
-------
Coal Designation: /Cr/cXi.o
lb/hr Steam: / ^ft&.'C,s."
lb/hr Coal: £>?
^602.60
L( ^00 7 /
-?;>y-*ey
£l°9K±
^
3-1
-O. 2-
~o.->
-l.t
-.1T.V
81-
//v
.2- o'
^2-70
3 00
2c*;>
2&o
s-^f
i/(0
2&o>
/^?J~
,2oo
/
X?
- &. ?
- 0, a
-/ V
-<^.J
7*S
,/
> YJ—
(5~C>S.
ss'.n
ytoSZS-
Wo/Je
?^/j-.p^
<C,
^9
2-o
- o. /
-o. /
-AC
-^.o
^J
///
2-ie?
^?O
/Vr-
/9-j"
W^
If?
T"
00^
A Research- Cottrell
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, % tvo-1" "/"-"oct
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
A" ?
/?-*!
Oo_i
-2
£0
~ - 2.
*
/ ? (,. 0/6 . Z
t.jT
?-/3
C50J
+ ^
e^
-. zs-
^
^~
Po-
rv
^-~
/£>o
&0
V-J~
^a -&
2/&. i
3 sr
?-/*
00 \
6
-?v>
". 3
teo1-
7^
^0
¥V
/&<=>
7-j-
3- <=>
^c-a
3-Cf.O
&-r~
-C-« o
^^>^,x
"T.-^r-
0(^ %
r--
-?
2o
A Research-Cottrell30pany
-------
Coal Designation: (
IbAr Steam: /7t/,
Ib/hr Coal: I
Ib/hr Feedwater: i
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date :
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR X 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
"/Vf lfl->
V//J-67
•l^ifi-'f
7*4*03
6/rfcoj
ii i>
/." l-i
-O.i. - 0. 1
O.I O. \.
•I-* -/.o
-3J ~?3
6t 62
III t'3-
2 of- 2.06
i7»' 2">.J
115 /9V
/&>" / *?
Ife /dK>
rs s-s
^ 5 ee
src$ <>~*>°
? 2W
ISW It, •'I1
2? 21
/;0 //
-O.2. "O.I,
O- 1 O.i.
•l.o -l>
-Si ~f-°
62 70
til //*
2O <~ JLoL
27O i?i'
/fP /<5W
te& tvo
f&- ffO
Sf 67
. —
7
2 Y«f 3 Vb
IfeS' 27
>7 30 If.k
3? *g
f. V / .->'
-a.i -o.t~
0. / &.1-
'/.t -/.i
->/.o -». o
T/ ?;
"•e ///
2-o£~ OoX
ZVf pli"
/0? /^<^
/?i~ //<5
/^5" /5J'
^J £1
<-{&} '•(00
y<^> ^&<3
^^V i^/jr
^ ?C> 2Jo
ft: Oi
^fS(,l
t6n&>*~
7>?z-
W.i
-Ml.
?a
f/ i
2.I&
27 S-
/qc.
(T&>
(&<>~
£7
<-t£>/
i"70
2-
A Research-Cottrell
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL,
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
!.<•' /o
77 70
-0,j -&,l
/af ?o
i ^ &o
7<{ 1*
•{£ t
V /
^L__2L
o^- o:-r
7i" 7J
-&. 2- -o.f
72- £>5
J^- 6i'
?S~ 7^
^ ^
^/ e?
//^ /^
S5 V
£.
J-TJT ^
^r" PJ-
^/ *y
<> 6
JT S~
f-ty Sf*,
XJ-fc xfis.
o
?£>
&
.\-s~
J-S~~
?J
4
r"
^-^
REMARKS;
A Research-Cottrell3wJpany
-------
Coal Designation:
Ib/hr Steam: 177,
Ib/hr Coal: /
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No. fr
Date: 2- /I /
Page:
1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR X 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H20
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H20
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
r\) Fn-n Awf^
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
//i'*n TV
6/fV -7J
/n X/-2
tfo ///
3e># 1 lo
2?i- 2??
/VP (US'
IW //T
/JU /fi.
S5 SV
c/ Q
ifo -(la
5"6O ^"to
;v? JY?
?X6-> z*:~
/tf/«3 /£*
?T- ?2
^.6 2-t-
-07 -o./
£7.^ O.i
-/4~ -l.t>
-£6 -IX
•7V 7?
^ y/^
/// //?
^/£? 2/0
2 A- 2- ?,i~
Syo ne
/*& /ff
iZf /yj
<& SJ
t/^o V/o
i"60 y>0
2^/3 2^0
57i" -?A"
/ 7 ." Jc. / .4>.'/t
3/ ^i
zf z.y
-0,2. '^2
^'^- 0. X
-/J' -/tf
-^r< -v?
? 3-/0
2?r 2?y
/*J-" /S't?
//O /^
'^i" / 7?
57 ^
V^ ^'^
3"6^ Xti"
7Vi" ^/i
?fc> 275T
/P.Jte /?%
V*irj-t
mtimi
Tiivyc
^•/^/p^
JA ?i
-U? 2-6-
-<2i -c?- 1
o.\. 0-i
-U -!•<*
-S~? -%
72> 14
tt* ///
IN /U
20& 3 I*
2 ? V -2 7j-
;^s ' ^ /§^
/8J /Si.
S> Jj-
V J"6o
2 *J 2 i-o
^7s~ 2fs-
A Research-Cottrell
any
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
cr\o PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR RE INJECT ION PRESS, "H20
GRATE SPEED SETTING (left/right
(, r
—
-0.3 o
?^ 12.
-o.2-i- -0,3
fr- fr-
52f C7
?Y K-
Jnr j-fe
£/ ev
tte ts-i
g S>
r.s- JTJT
•2"£>
f/ F/
>^J /7>
^ s
r.o s.f
•2
& o
^ ?3
-o,j -c>.i
f? ^
fi> a
_r
/? ^o
L'-v vfy
/s.l / -i'>
7J 72
5"fe J^6
?/) >&
/ S-.D
2? S"?
3/ ?;
^ 7
^ ^
v-v ^
x^,o Xro
REMARKS:
our
A Research-Cottre
pany
-------
Coal Designation:
Ib/hr Steam: l~> 6j £(,
Ib/hr Coal: 1 ?j fr^f
Ib/hr Feedwater: /i-
PANEL BOARD DATA
ABMA TEST SITE B
Test No. / 7
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/<=> ' l(*
163s-±,
'-1432.11
??(, r.
2*1
2.1
-0.3
» 0 3
-/.7
-tf.a
w
i/n
"2*0
2 ?O
/
£?T
$-}
<-{(0
^•&s~
2^$—
00 S
/
f&JS-fyg
VV2J70
?3£ S?J
6 2.2.Cr H iT
2
-6.2
5?^
///
2fO
s'r o
/f£3
^r
/?s~
°f/
^3
'-/&(.
S-2f
l2iT&
OC5 V,
/^; OJ
V6 j^ v sr
VV-?V/6
? J ? 0
/?JT
/*•<>
so
Vof
S'^'
p-.r<>
ooj,
A Research-Cottreggmpany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, % (TO* ~YVx?c^
OPACITY, %
SO2 , PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
£.r
/i.
©04,
— 3
?«r
-&-3
7.o
2^.0
C'O
•S.LX?
%1
6- •)
f-/
o&_s
/
2-^,^
60
(5,o
-fo/e-.i.
^
2 r- 30
G&S
- /
Qo
— &5
o
?2L
- , 2
J?£
py
?o
t&>
-?^
/jfj-
g"/rt
-------
Coal Designation:
Ib/hr Steam: /y -/
Ib/hr Coal: ,S~j^
Ib/hr Feedwater: /_p_j/ j 7^
^ . ^&L^^-^^~—
Ja^pJ
v-—- ,«_jfes-To
AVJ-
3 j>
//-To
^?776
V/7 H^>
7S~3- 07?
<&J?V 76
2?
/-J
-6,/
£>
-/./
-t/.o
^f
/0?
^?oo>
2^d>
^00
/^3"
Xrz>
6j-
>T7
^0.5
J^~0
^^6"
C-^i^
/5L -• JJ
y^^o-/
^?V-ro
7i~i ' re
<^^? j^r^
P^?
/-^
- 0.7
/3-~c?
£*-
S~x
Z^~
-TX-D
2^r
o _S
IS 'of
<-!(, 7 y u-
'•/
-O.i
<2>
-o.t
- y-r
£j-
i"i?
:79-^&
•STS-O
^^->-
oo r
^7 ', jr>
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No
: /e
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
y.-r
?-/!
Ooi
- 2
^f
-°-J-
W
?J>
^ '
if
~7I
/ &•<->
&.->
r.o
2-k . r~
2t-o
£o
?.o
) *&
&2-
L-
^7
' 9^
?,e>
V-c3
^6,
±~.j~
8-//
00 J>
f- /
6l
-a. x
7S>
^-S~
^2
0
^C'
r &0
7,o
<-/. <3
-?6.e.
?V.O
i^.O
?.^
H.J-/
/ -/,G
^-0
*-/i -^
C>o3
'2.
C-c>
— o.^?_
74'
^i~
^2?
cJ
^/
S*/
X.o
i~4 AJ"
^XO
?<^.C3
^S"
V-a _
REMARKS:
A Research-Cottrel
hOmtpany
-------
Coal Designation: rc tw-t-yct y
Ib/hr Steam: /So,
Ib/hr Coal: / j~ Qo 7
Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date :
Page : 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
^.-?y
ytfj"i?(
£/V?f/6
~}f^iO
£3
1*1
(^03
10'. I)
y&XlOo
Vt/???2-
7rVo ij—
/r>^?3 & r-
2>sTo
/.a
-oo
-o./
-o. V
" J. O
^?
/<>•?
•2-&0
2c&
'*&
/J~J-
/So
S'Zf
&>
?
5-^Y?
OOJ
//:«•-?
V6^i_?i"
•/V~<-fl-^f,
& if'/f/
-2vT. cJ
/.*
- a
/o?
^50
2.s-y~
'?0
(GV
f*s~S-
^/
?J>~V2S^3
& ?9J~?A-
2ST.O
/a
-&,/
O
'//
-J-V
*9
/?
/
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
? Xl
X-/2
<5>O.S
/
60
-. 3
-7?
£j~
&C
^1
77
/ te>
2.™
-^o
?i,o
>~?.o
<£•*-
7-5~
) L'i/ll*-
Y-4 3j'
{o - /i.
<5><3-S.
C2
£^
-.2-
?x
r9
<£>3
vr
?ji
/yo
C.e.
Jr.i"
^y.o
J-l .0
&. jt-
c?.o
<{.<-/ __
/ tl.S
<-lJ S'.o
/& - fj
Oo4
2-
^^
-, 2.
?/
^7
<^^'
V^>
?3
/
-------
Coal Designation:
Ib/hr Steam: ,/*/-*
Ib/hr Coal: , j-;
Ib/hr Feed-water: /
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/J;i&
(Ft-j
K'O
/.2
- .1
O
-I./
-3.G,
?0
M
/9o
-2C,X~
/xt-
2oo
fafj
u?£
s~y
?s~>
J, -(&_«, —
^Y^
/^-'^-i
Ytjrytf,
<-/
~/J
-3.)
-71
(*?
//t/3
~J.r»-/ 7o y
£,*/ ooil
?i"~
A-3
r">
o
-Xc>
--?.C
^^
/&£
/^s-
?c>&
We
/ji->
^0"
_
:?^o-
A~?-~i"
^Y?
fPOi
'^''j«?
y&s^trf
LA/4J/6'0
74V 7 70
?
2-S-
/.i
c>
&
-l.o
-?Pany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR RE INJECT ION PRESS, "H20
GRATE SPEED SETTING (left/right
L'.O
/
^7
f^.7
<<<
&?
( ?s
/
^2-
-. -J.
Si
~?n
&?
SG
?€,
/£>&
52 -.0
$>\D
2T 0
•2 ?C0
^0
-Tc?
^i-iy. -
/^-*
-- ?
f* -/OJ>
;
i'-i-
-. 2_r-
^f
-?o
&&
j~~0
7-/
/S>°
£.0
^TtO
-2'2-o'
27,0
&.&
S o
*•*/<,.*-
•±--.1
?-/3
00 Z>
/
6&
^,0
^;°
^j- j"
P?*o
<<. 0
JC<3
*-r^
REMARKS:
A Research-Cottrell^pSpany
-------
Coal Designation:
lb/hr Steam:
Ib/hr Coal:
lb/hr Feedwater: / -T/,7
PANEL BOARD DATA
ABMA TEST SITE B
Test No. 2 (
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H20
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 lb/hr
STEAM FLOW x 1000 IbAr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
(* '-<*J
469 •?*£
Wqott*.
7
2 V
/?&
/to
fS~o
7o
/*
v&«?
J "i^"
2^--
??o
//'•Jo
i./6c/V° 7
^yL:J'
V^-7 Y-Tf
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
xV
OXYGEN, %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
c
/sr
oos
/
i"?
-M
VI
77
£Y
79
2t
/?!
2-°
5-0
PP.J-"
7-C.^f—
6?
v.<—
//T.r-
c.tr
>*
<£>ft J.
6
*Y
-.2.
?r
^> 2.
?C
<^^
s&
/ X2-
S.o
-£.
->s~
^~?
£v
S1
/yo
,F,0
^. o
^f-J-
IL-T
^^ <=?
^r-r 0
*/.f/ ^
Aci
REMARKS:
A Research-Cottreli4klfipany
-------
Coal Designation: /j
lb/hr Steam: //J, fe C'>
lb/hr Coal: /^ /J/
Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No._
Date:
/?.?
Page: 1 of 2
TIME OF READING .
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 lb/hr
STEAM FLOW x 1000 IbAr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
A/ 0
".O
2 . I
- /
/-.3
-/. 2
-Ac?
7/
» 7
/^
'2 73'
/^
/ SO
/JV
72
3•-•/.>"
y^.^rjo
''I ti*? 3-20
7 $-*'(, 6 >r
e--ti ?
?x
^4
/9/
2 #0
/fr
AA"-^
/_S-<:.'
7^
SC
J^»-
3-ry
P- ^ ^
•^ '••<-1
; y • "/-?
L/6<7.i-jr?
vy? >y?
~?f£-?l, ?
a V.; * x&
t>~.o
/• ?
- . i
— ,2.
-f.-l
-4-3
£1
27
/^•A
^^^
/7&
/S-v
/ <.-<=>
72
5-g
- —
i"S'<->
P V3
S^C'1^
//.' /o~"
V6f -TV/
^<-lcfy.(s2-
~7$j>y) ,?
6 VJ"?-.**
A Research-Cottrelt^^ipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No: ~ --
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H20
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
V-.i"
V - 0.
Cc<
f •'
~,v
- )~'
7^
73
f, c .
3~>
71
/ yj
to
r.o
s. y"
/r r-
<:'.c-
-5.", o
C/-i/V. s-
^~.r
i-./y
Oo .i
o
^
— . i"
'^ 'o
li
C2
9+
-^ <:-,
/n
?T,D
S", <^
i". C'1
/o. O
f, ^
$"0
V-J-//-S-
-i . i •
>•' /r
c-^s
^j
5"V
- 7
?/
7jT
££
X£>
r .>
/^
^,0
.C' o
-V.O
/o ..<-
^•.0
-f ^
^-//.,
REMARKS; /;
0,
A Research-
-------
Coal Designation:
Ib/hr Steam: /f 7j
Ib/hr Coal : .2 ^ £ /
Ib/hr Feedwater:
( ' o
PANEL BOARD DATA
ABMA TEST SITE B
Test No. 2?
Date : ,
/7.P
Page : 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
'/./*
£ VO
?tv
3o r
i?://
(/ 70 T-^L 0
yj~0 '21 i/
7s± ?<^j—
^V?-?jV
-3
.^ C-J
?3L
'-/
-0,?
-/•?
^.G
32
//*
tf^
}<0
-L 6 c?
^Vo
3/^
/^ J /
V?0 J"Z
V-ro 2 6 i
7^ 2 yv 7
S-<{ ?j?s>
.?<=,
3.2.
-, -i
-o.C
-!•*
-£.2
ey
//2
no
^0
/9&
T^oG
2-0 S~
?•
-T/
<-(<^
^"feo
r-^o
'/ J.C
/.? ->17
/ 7c-;'.T3pr,
^//"OA^
7 A P j->?
^y^y ?o
A Research-CottreH^fiipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H20
BLR HPR RE INJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
3~o
/
(
#0
- "(
/oo y~
f
/??
r.r
-T.o
"? ?, ST
2/. f
/
o
^
-T. s.~~
^
f^o^
/
7^
/- 9 '
^ +-
9l>
32.
F7
5L?
/^
cT. ^~
4TO
^F.r-
?/<• o
~?
o
f S
^^S^'
REMARKS:
; fc-
A Research-ConreliJQipany
-------
Coal Designation: S "
;7i J.-IQ
/<~ ±->o
)H* )^-
f'c1 •> J '-
1 2:*-?
?r
7. *
.i
t-. C
-!•(,
- r.z
7?
"3
2 |6—
?->f
/??
? Tc>
>rc,
«r?
y?
-
1lS
/'/* 33
-?J~
?.J-
O
^ r
-/•V
-^ ^
7 7
//i
2r ^
?^*'
/?i
?C?C>
i e y~
2 /J^
^?yj
/?'?
?.*>
.?«/
2.^-
— ,2.
y . j
-/. j~
-vT. ^
7?
//a
•3--1-0
2^3
/
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR RE INJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
5 , K : 1
c ?
fio } \ '
-, •? -, }
?*
< ? « ->
4v
7 < j •--•
7< S- ?
fS> / s )
S\ v
y" V
2/
T? .Vi"
V H T-tf
' 9
\^y ~ >-/
' X 7 _J.C
7. y
__
->
c-(
\ 0
T
?/ ^
^r?.0
?. V
^''
/". * .' /
' X' ?
i"
72
. *.)-
/,,,,
c"/^
i''--
«.' c.)
?J
'' ,V.
^; o
3
?/
^j
/.-.', r-
>'. c •
/C^/,£:
' !• : >
<. -1
F-o
— 3
/•''
,c,- \ ~
J';-
^o
S'/J
//ft^
^. CO
<>"
Pf r "
^^ , S~
/f. 0
-? c
^'^.0
?-7
-— -
0
6J
-v
rj'
,5^
i^--
^c. .?
7i
/^o
,-
^
_.
— --
REMARKS:
A Research-Cottrell
-------
Sheet * of 4
KVB
NOTES
TEST NO; /O:3Lf r^^fj /».J .-.»r«^«
L4. R
a. ----
TEST
>•»» «./ *«,»«. L *.
TEST NO:
TEST NOs
51
-------
Coal Designation: / • - I •• '• / < i
Ib/hr Steam: ,7' •'','A''t-'
Ib/hr Coal: , > j <^'c'
Ib/hr Feedwater: yo(, o< •< •
PANEL BOARD DATA
ABMA TEST SITE B
Test No. 2_f
Date: •„'/ ')'
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H20
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H20
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW F_LOVil__xJ-OOq_lb_/hr_
STJ-'AM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
KCON OUT GAS TEMP, °F
STEAM TEMP, °F S
ECON IN WATER TEMP, °F .' Y'
1-X'ON OUT WATER TEMP, °F
•/7^'.U-
? y
6U Ji
3?
/. i
••'7
— ),
• ^ ..' 7 7
-/.£
•r.
7 6,
A Research-CottrefjC^npany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No: 2)
Page 2 of 2
OXYGEN, %
OPAL. 1 1 1 , %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
1 0
—
. i~
76
- . _> 5~
/„„*
?J~
£j
2 &
7\-
/F&
(
V
?r,r
l2.*-~
£-^
r.a~
) 7/0
3. a
—
/
sr/
~ j?.r
I&0
Stf
<£(,
•3-0
S'J
/?J"
^
5"
?o
22.
7.0
~s~. v~
*y/ / o
<-/.(,->
—~
. —
. s~~
ro
- 3
?y
ef
C?
/o
&?r
> -?v
Z
•r
2?.j~
.?/
"?. o
£
9/r
Z&
-2
^7
^0
7K
/ >*o
F
^r
?^
2-3
7
^5>
V.' 6-
3^""
—
0
P<
— - 3
fj-
P/
S'.^
Zo
?-»-
/7J'
?
S"
?J
5- /• i~
?.o
?,r
REMARKS:
C-
21
A Research-Cottre{J@npany
-------
Sheet & of
KVB
NOTES
TEST NO:
iLJ?
l/^/h
^ VV, «rc, 3F j:?
/-v^.
O
******
TEST NO:
a—£
K+-^& «^i- t*^-<*tJr
su.
TEST NO:
JL
1
\
gsv>
TEST NO;
(-
A
I Jliw cJL^j/ ,^j r>x-eK
-------
Coal Designation:
Ib/hr Steam: /?#,
Ib/hr Coal: 21, J <*
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date:
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/O: /v .// ^Icj
yr& 3 ^ i,
Hjtfl^
Tf<^
j"jj J7^
. /^- -/ir1
72.
^6,
-, 2
r. V
-/.J>~
- 5". \T~
77
//2
?m
?7$
itfo
~2~C>
200
*3
rsp
t/ro
rfc
^l^
J/3>
/4*TJ/
31
?^y'
-, 2
v ,3
-/.J-
- i. J~
77
//2
} /i -
^77
/?«
20-s-
^^N-
^i
62-
YO/
j";o
2^4-
-?/i"
?/
7i"
- . z
t .-?
- / .T"
o: '/
77
/M
3/S~
2 ?7
/ f£-
^cs-5~
2-0^-
^>
tz.
yeo
(~6?
7VV
?/V.
/S. /o
<-/^~c c ><.>
il 77<^J'?>
7<^C't:3j-
(
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , %
OPACITY, %
S02, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H20
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H20
BLR HPR RE INJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
C- H ^
-
O ^
fT fo
-.-I -.2
ffot fop*
/0C V )
?/ S-3
C*-)
2o- 10
6,0 <^
/yv /yo
i'r S
%- K-
?/.<,- :?*\r
3* y ?' ,"
7 7
af ^.J"
)C->>,^ — ^
,Ci'
-
...
(->
yo
- j
S}"t-
rr
yo
'*
^
Vj'
^
7/^"
7
[ //
/ 7-0
r.-r-
r~
¥1
^.fT_
rfa^
W
£1
<^«
w
/$o
&>
^7s-
ys'.j-
3l.s-
->
#,3
£ //?,-&
lf-
0
O
~ *i
T*»*
Si
—
REMARKS:
-*t~
JT
: J / -/2_ : >/y
- / ' ?.'
A Research:CottrefiUnpany
-------
Sheet J^_of 4
KVB
NOTES
TEST NO:
)e,So
™*~* •
fr
J^^ *~+~~uO
UdlX
,t b»
-------
Coal Designation: /Ci-~TO"(<:>
Ib/hr Steam:/^y", 76<7
Ib/hr Coal: //; ~ i~i-
Ib/hr Feedwater:
. N
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date :
Page: I of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H20
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT .GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
*?• r-p)
G/
Vt/V^^
?^i^Y
6 16 ?&/
?r~
J.r
i
r.3.
-1. x
~3.?
71
/£','
//io
7c?o
/?(>
/iO
/6°
•70
fs-
J?j-
<.'<<<>
7^"~
-'ic-
/o'.~-l
V7V^?/
VJ3-V JrJ
"1^3 >cr*=>
£. 1&2& r
~3 -,
j <->
/ S'
-. JL
/•^
~/.3-
~^-±
7^
/^
J^O
^fY"
/gy
/*.r~
/ 6 V ? o
I?c;
/s*
-. i
^-J
/- L
h>-2
~?3
//£>
#6
.?&>?
/^J"
/6o
//J ~
~i^
//^
A^o
>^7
/f&
M^
y^c~
?a
^j-
p?^>-
3"C c3
T Vf
7/ -7
/^;fj?
7 -? ? c 'Y ?
{???io£r
A Research-CottrelWJQipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
y~.y
U ~2a
?oo ?
- £
£?
-V
vy
7J
Sr
2/
£&
/7f
&,o
%-
?? 0
D.&
7+2-
r.o
I fa/**
r. ^—
so //
•?oo
{.£-
£j~~
-2^
5.1?
7^
<££
L/O
66
/ £>O
?.o
9^
? 7.0
'7&.O
7 ft
tf.^
Wf.f
>r,o-
P /6
2- c'1 c>
>l
6?c>
-.J
5>J
7y
£
*y+*
REMARKS;
P:X! .
!>,
•/•& .2
A Research-Con
mpany
-------
Coal Designation: frs
Ib/hr Steam: i('"/l ~fZc',
Ib/hr Coal:
Ib/hr Feedwater:
Test No.j2lJ2
PANEL BOARD DATA
ABMA TEST SITE B
Date: 3/9/7?
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H?0
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OF A FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/,
^y/rvb'
7 U 7 ~~
/ /
-+o»±
7^,3
-l.o
-<-/>
/V
//
/-Ts"
/££'
7+
76
2cfO
fee
? YS
^'J-
/^~->/
«/ 74- ~
/, >
-. z
-^.-2.
-/A
"/.X
7J
//'/
/YV
2^0
/^/^
/{-r-
/(- s~~
7i
7o
_^^o
f'S~^'
2T^>
->V ?
/^-.'^D
V7^«?/
/i-*^ Y?
~/ 4 3 1*10
677 S-3?
^6
I>o
-•/
y j
-/:?
-fO
?y
//*/
/^
^^j-~
/p-?-
te?
/*?
^
£
J'^D
-2/7
?/-2
/^/r
y/?^ /?
wscft.
7ci"/^^
6??co±
^6
2-6
-. JL
/-./
-//
-//
7^/
J/V
/^'2.
?9f
/9s
/^<^~~
/^/
?*-
£7
3?o
^S^->
^y"7
-"//
/C-33
'/?7J.<7C
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
_S^~~
7
;>.>"»
0
7.3'
£5
60
?•/
/7y
V.o
*"/*»
i-r.&
n-r
1 + 1
1«>
"«/•<«
V- f
7
-*f-&
o
SJ>
- Jr~
i'^
?y
3i<5 /
/t^
zy.o
27.0
7^^
7.0
s c-'/7r
V. Y
'7
^2-&~O
-. /
6?
--J.J"
^3
7^~
£?
S?
g°
/*/
^0
*%«
^L/0
2 ?.C
7t1-
?.£>
r-Tr.j-
-/J-
7
>JC>
^5
6 ?
-3°
S3
75
£7
-------
Coal Designation:
IbAr Steam: K'V ,
Ib/hr Coal:
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No. /•*- I
Date : ?//?
t . J~
-/.£
- J , J
-]s-
/^7
/to
? &>o
/fr
fffO
/S-V
?
<-/{> ^ j-f
&01-/6 i-
£ ?'!>-£ i.
JX 7
/7
- -/
i- . 7.
-//
L/-°
•72-
/0f
/*?&
•z-tfo
/?<>
/6o
^0
/^
G7>
232
-STi
"2 Vf
v- 7
>3:*f~
Yf jor/
^/^ ;Z-
s-'o?<:,o^
^f
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO 'CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR. HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
7.0
K-/o
?
O
7&
- -J
11
-ytf
tf
K)
$6
/??
C.o
V-c-
2 <~<-
1-t.O
or
X .0
^'"7^-
J.o
1-3
3 GO-
I
G^
••>
6L/
c-r
6?~
So
t"$~
/X0
6.*
%-
-2^-r
2 t;0
1
£.€>
r-*Ysr-
-1&
/
*?
"1
?o
72-
61
9?
<7^
/*/
REMARKS;
D<
O \AL,L>
-------
Coal Designation: :
lb/hr Steam: /S~~>;
lb/hr Coal: /<-} $ VJ
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date:
//?
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H20
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 lb/hr
STEAM FLOW x 1000 lb/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
// -S2.
^zym
1 te<5?s
8»""
J ~-i~S"
> -n
A?V
11- • * °
(f^J-S^fl.
l/f^(^73
i'0
/c'0
h~<-
/* r -
^7£>
&v
Hoj.,
i"«foo
^v f
Tt^j"
/-?-vTV
^/tl^c/'3c/
L/£-3 ?* 1
?loo/3
£ 91 Ccr>
^2*
/.'
— 2
1~]
-/•o
- 7-?
72.
//*
/^z
2
/s, 3
7c3
^^
y^ j-
j^^-j-
^.N1 )
3\'! 7
/fc :^
•/^^j-f
/^'a'i;
J/6^ '/Y1/
s?
•* ^
//
-/
^-2
-/o
-^f
Cf
/(?>f
^
2?j-
/?)-
AA^
/~J"3'
^Z
£/
Y^^
JTV3'
2YJ
_1^2_—
A Research-Cottrel
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
>U->
7-7
-23d
, 5~
a
— - "}
' -O
£7
70
££
7f
*y
/ x°
jr
.r/.r
'2f.
?*
7t^
X
> *•*%*-
x.f
7-/o
2 zv
,r
&
- 3
&-)
7A
^7
76
fj
y #2-
8
V*'
a«$-
/y
7 £2.
^
*-^J-
<^c>-^>
7 - 7
.? JfO
, 7
<£?
"~ • ^3
£5
62
6)
•?r
/•j
/ *3
t$
Vs-
7-G
^>>
-?
7
2- 3 .r"
,3
^J-
-.3
^7
?/
/^
7-?
#3
/go
S
r/r
2t
^2?
7
^
6-^"/^.J"
«?. i~
~)
^2^0
._?
J~J~
-,3
J^P
£y
£3
r~c
73
/ 3~>
V
*/sr
^c
2-^f
~7
^
&-£~^7>o
/^
REMARKS:
A Research-Cottrefwhipany
-------
Sheet ^ of
KVB
NOTES
30
TEST NO:
UP
TEST NO:
TEST NO:
TEST NO:
TEST NO:
-------
Coal Designation:
Ib/hr Steam:
Ib/hr Coal:
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No. '-V
Date : f // f )
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "^2°
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
n^0
&IJ I*;
6 fS~o y°
-2*
7 1
-.1
1- T~
-/,^
/^
/^^
As-
66
^
^?«-
-i-j-i"
2.VV
3/t
M:*-*
<-/6? J"?y
Yf/??K
f/2. •/>•!
^/^?^-2
2j~"
/.2.
~ 1
-./
-/*
-J-/
;&&
/
2-£>
ay
^^
P^J-
_s~-i-^—
^v?
Ill
fry/
^61 £}-/
/*v y^ /
y/p^j^-
^VjVf/
?i^
/. 7
-./
o
-/./
-
7^
/6€
/9o
2~
-/J
y^O
-?/
A>£
/To
^^i.
/sy
/<££>
/J'J-
£J?
7o
^^
JT^~&-
7 VJ>"~
5V_S-
A Research-Cottrell€5Jfipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN , % O
OPACITY, % /
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H20
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
''2
1*
7 ^
o
-. 1.T
i~-'
$,c>
y^-
-33. &
,?&.£>
<^- j"
p
_i:j//;ir
/^
^^//
Tc^o
•^-.J.-
?/
-J
d
SS>
^
x±
J?
/7/
cf,0
W
?3.0
? 6>. O
7
6
lev
M-
73, 0
•3-6,0
^
-------
Sheet ^ of -1
KVB
TEST NO:
NOTES
st 31 - S,/* 8
TEST NO;
~~f i^ }
-------
Coal Designation: /-/&•/-/,
Lb/hr Steam: /_y frj ooo
Ib/hr Coal: /^ j?j r~
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date :
Page: 1 of 2
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H20
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H20
GRATE DRAFT, "H20
BOILER OUTLET PRESS, "H20
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
//:o
IXf
//<-
/-?s~~~
/±~<>~
~?0
7^
V^O
~$r<^&
2 <- o
5>0
//' ^
i& ^((,21
/«ry»y
(jf r-02.
&90
2-i X
7/0
X2-V7
Y^V^
Xi— '
/•J"
-/
^ 3
-/.O
-^ j-
^^
/^>c/
/-r
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 2 of 2
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR 'RATIO CONTROL
OVEKFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H2O
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
6ftJ
~7-7
?
- J
3^
k-1.
£^
^^
^c>
(r?
/ s/
REMARKS:
A Research:Conrel¥uunpany
-------
Coal Designation:
Ib/hr Steam: f ^
Ib/hr Coal: /£j 5~
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date: ^/-2 / /7^>
Page: 1 of
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H20
FD FAN DISCHARGE PRESS, "H20
FURNACE PRESSURE, "H20
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
/2.' //
^6^T/3(,
V*6 03V
x/e'j?^
7o / o ej
?s~
;.y
-./
£>
^/./
- 7, g
7o
/oc,
/to
2^6-
fr^
/^£>
/&C>
6?
<£'2
-3*0
^6,&
2S^>
.7-2 ^,-
/? .'/ <•/
^tsrnt
H xt <5§;
Ifl ?6 /J ~
?0 / 'i I -J
^y
/' r~
- /
7./
//
~T £-
?/
So6
HO
29i-
/^o
/£&
S<~&
6
7i
S3
YOO
0^4 '-7
7 s"~e>
^?.i—
/vi~' /^
y^-^j->
i-/f6;?D
£'/ #
/?<=>
29-£> —
/ X?
/^O
/<^<^
^>0
^ J-
J^J —
J~J~?
2 ve
?^j"
/^//i
fsyjff,
Yt^Zl?
&l j
?jT
/.6
0
+•/'
/•2
-«<€>
V
/>o<:
/90
29S- _
/?0
/<£>o
6)
^2
3r
A Research'Cottrefljt/i$npany
-------
Coal Designation:
Ib/hr Steam:
Ib/hr Coal:
Ib/hr Feedwater:
PANEL BOARD DATA
ABMA TEST SITE B
Test No.
Date:
Page:
/;>
TIME OF READING
COAL SCALE A COUNTER x 200 Ibs
COAL SCALE B COUNTER x 200 Ibs
FW FLOW INTEGRATOR x 1000 Ibs
STM FLOW INTEGRATOR x 1000 Ibs
OVERFIRE AIR PRESS, "H2O
FD FAN DISCHARGE PRESS, "H2O
FURNACE PRESSURE, "H2O
GRATE DRAFT, "H2O
BOILER OUTLET PRESS, "H2O
ECONOMIZER INLET PRESS, "H2O
FD FAN AMPS
OFA FAN AMPS
DRUM PRESSURE, psig
FW PRESSURE, psig
STEAM HEADER PRESSURE, psig
FW FLOW x 1000 Ib/hr
STEAM FLOW x 1000 Ib/hr
AIR FLOW, %
FD FAN IN TEMP, °F
ECON OUT GAS TEMP, °F
STEAM TEMP, °F
ECON IN WATER TEMP, °F
ECON OUT WATER TEMP, °F
17-13
t{Cs"s?i
v/ V6>i"&
Xlliicl
7oiJVf>
2 -r
/<>
-. /
f./
-I.I
~L/.o
7/
(o<-
/ID
}
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page '21 uf
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H20
REAR LOWER OFA PRESS, "H2O
BLR HPR REINJECTION PRESS, "K20
MECH HPR REINJECTION PRESS, "H2O
GRATE SPEED SETTING (left/right
* J~
7
^C
7 «-
^
-•3
^7
/7
£3
X?
50
/ y$—
/£/
+y*>
li.i
7~y./
S.o
-7. J"
*/6
~
X,o
/,
•2i~D
, y
^
- 3
to
6?
£2
^
257
/ yo
t~y
^-/J.J
1./.J
ZV. -2-
V->£-
<^ ^
^•-£p/ ..
/0-fO
8,0
6-1
2?o
W-o
72
-. Jj^
7i
7f
^y
/
/??
26-2
Y \ —
G C
^•J7r0'
7- j-
vT-6
77 j—
^/.4'
(oO
-. 3
7V
76
£7
70
te
'~?6
^-4-
V'^^
7/a
-?^.&
*-{•)
&.£
v- 'x<.^
^^i-
J>~
7?^0
X. 0
£>
— J
?/
7?
f?
IV
?r
/7f
£.f~
v^v
a/.o
2-y.i_
v- ;
e> '~i
^•^-^
REMARKS:
A Research-CottrellCwipany
-------
PANEL BOARD DATA
ABMA TEST SITE B
Test No:
Page 3 joi 2
1
OXYGEN, %
OPACITY, %
SO2, PPM
DRUM LEVEL CONTROL
FEEDWATER CONTROL
FURNACE PRESSURE CONTROL
FD FAN DAMPER CONTROL
AIR FLOW CONTROL
STEAM/AIR RATIO CONTROL
OVERFIRE AIR VANCE CONTROL
BOILER SUBMASTER
PLANT MASTER
FRONT UPPER OFA PRESS, "H2O
FRONT LOWER OFA PRESS, "H20
REAR UPPER OFA PRESS, "H2O
REAR LOWER OFA PRESS, "H2O
BLR. HPR REINJECTION PRESS, "H2O
MECH HPR REINJECTION PRESS, "H20
GRATE SPEED SETTING (left/right
l.o
7.C
3&o
l.o
6V
-•?
Cc,
1?
£7
if
?/
/*?
C~
l(-*A.*
a/./
aW
^.^
tf.j"
^-/*.r
REMARKS:
A Research-CottrelfJf&pany
-------
Sheet ^ of 4_
KVB
/
NOTES
TEST NO:
. r»<^
'uAu
. -/-"t
TEST NO:
TEST NO:
TEST NO:
76
-------
SECTION 2,0
PARTICULATE DATA
PAGE
2,1 PARTICULATE DATA SUMMARY 78
2,2 PARTICULATE DATA SHEETS 84
2,3 PARTICULATE LAB WORKSHEETS 129
77
-------
PARTICULATE DATA SUMMARY
PART I
LOCATION: /\ 17/HA
TEST
NO.
Total
Mass
mgm.
Dry Gas
Volume
ft3
Liquid
Coll.
ml.
Baro.
Press .
"Hg
Static
Press .
"H2O
Pitot
AP
"H2O
Orifice
AH
"H20
Stack Gas
Temp.
°R
Excess
02
ampling
Time
Nozzle
Dia.
in.
Pitot
Factor
n.d.
Fuel
Factor
SCF/10%TU
lue Gas
MW
g/g mole
7
O OS 2.
$65
0 79
JO V fc
/ */ JV
,3)6
.£"'37
.(.-Ct
,'. 5
3.1. fe'o
-.70
0. X6
(• V
/''• 779
V/.r
Jo
-376
O. 7/1
c- ^ ?.
O,
/ /w
t r/
£<•>
/r
-/-Jo
L/
/
O. DC ?
o. 71/?
S'.O
to
VO 7
-fas.o
77
SO
Kl . J
-/. 2-
o
v- j
JLL.
/si
.'/C
V iG.
f gs-7. i
d-O
#15900
-------
PARTICULATE DATA SUMMARY
PART I
LOCATION:
TEST
NO.
Total
Mass
mgm.
Dry Gas
Volume
ft3
Liquid
Coll.
ml.
Baro.
Press.
"Hg
Static
Press .
"H20
Pitot
AP
"H20
Orifice
AH
"H20
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
fli-
O.S2:??
/
37.7^
j." J.
3 7
Zf.Co
•*-
-f. 61
O:
0.99.8
2?.
6-336
-"Ts-
to
0.
a.
60
O-Jfc.
6, 6 03
(T1. S.1
#15900 rev.
-------
LOCATION:
PARTICULATE DATA SUMMARY
PART I
TEST
NO.
^?«
f?l>
^
-Lib
00
C
Total
Mass
mgm.
/jT-'Uo
10&.1
f*,W3,\
-/<>?.J
Dry Gas
Volume
ft3
Ll/ C /?
2. V-?.
' 2. ^ S'
??,_ 3
pt/.'i'J-O
i 2f J-iJ-
«
,
Liquid
Coll.
ml.
-TS-i
4T7.o
J"^. J
V2-/
Baro.
Press .
"Hg.
^T- 9*
,
1
/
Static
Press .
"H20
~/.l
-f.o
-/-/
-o
Pitot
AP
"H20
o./j-y
o-i rt,
o m $~
0,f 7
a.^ it
O 2.^.1~
Orifice
AH
"H20
O.S^J
ev6f ?
e. /(S
o - * ^'
0. S/3
Pitot
Factor
n.d.
^o
\
,
Flue Gas
MW
g/g mole
2v J3~
2
-------
PARTICULATE DATA SUMMARY
PART II
Location \ fT-
^. out- c .- £sf
TEST
NO.
LOAD
02
CONDITIONS
EMISSIONS
lb/106BTU GR/SCF
LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin.
a ?. 2.
r^-t.-^-. C o
y
£" 3
7. -3-
//ft
Sb
71
75.0
C
//a
. OF? A. Sau
A'.?
H-3.
*/-«/
33 f I
0 . 1 r&~
, 0 6
5k
0.
6.31
$.0?
0.263
7.**
7 ^
S'-C'S
/«.
/c-r
V.J
7-
7.
//•s*
1 1
7.C7
7.0% Q,
O.Oog
^
-------
Location ^ TTE
PARTICULATE DATA SUMMARY
PART II
TEST
NO.
LOAD
CONDITIONS
EMISSIONS
lb/106BTU GR/SCF
LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin .
, oo
3 y. 7
ZL
73-?
13.
7.1 f i
sr ><-//
(o,
/It,
o. 3 / /
/o.
let/
0 .
33.
. ?
{ C ff i'
<$: . 77
'( i i
. g* y
o-Hll
b
0, 2
7.
«//
Jtlty
-------
Location
\ , )~, K
PARTICULATE DATA SUMMARY
PART II
TEST
NO.
LOAD
02
CONDITIONS
EMISSIONS
Ib/lO^BTU GR/SCF
LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin.
(I.
/.2 ->-<£>
n?
ft*.
& PA,
JO.
H
71
#15900 Rev.
-------
PARTICULATE
DATA
Leak Chec* Rate
in. Hq ftj/rain
ISOXINETICS =
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEriPER/itURES , " F
ample
Point
Time
METER CONDITIONS
(\ H Meter Reading
Stack
Probe
Oven
Irr.oinaers
I n ' Out
Meter
Vac.
•?£>
7,0
/,2 *?.*%>'•
62.
.42-
62.
7.8
.38
7/
36s-
3?-°
3.3,
3/0
62-
/•z -70 .
42
0
75
.3-3
€6, 08
• 73
80 .
3/0
6$
. 73
33°
fo
Wf///
, 43
33°
33°
7°
6°
#. 0*
Avera
ge
/'2~bb
Nomograph Setup
7/3
ft3
meter
Pstack
Imp. Vol. (End) Vol. (Start)
5tock t-ress.
__L
No2(Ideal)=
Noz(Actual)=
£>
g(End!
Total __
_a.(Klart)_ _i2iams_
//-V = 'Z
64
Total Vol. H20 e"
-------
PARTICULATE
DATA
Sampling Time
Per Point, Mm
2-
Leak Check Rate
Vac
,. 3
Before
ISOKINE
'min
After
rics = '?/ • 1 \ TEST
DATE
NUMBER O'
OPERATOR V C -f-ff. d/^
FUEL
SITE
rs: /• K
PROBE LOCATION 3i./? - 0~lf J~
Sample
Point
/
#
2
3
V
to
//
/z.
>3
/V
*T
/^
V
/B
/?
2*
2/
i"3 "^
^5
zy
Time
.Average
METER VOL .
W:TER c
APS A"
@&
. .ffV
, 072
. ef
.
. 6l>
, f*
.£&
•
//
,7V
,^eT
, z?~
.s*1
END /3/ / &
START /*
SAMPLE VOI.fl 2'
cr i tot
.^37
F-ercenc
/2.4. ^
/3*iT.&£>
— .
A5e»6, i?3
/3*>7 f/
/ *^y j>. ^TI X?
/ _"j C* c^ * *^G
/ ••-? / ^^ ^^ /
/5// . 03.
/B/2-. //
/3/3. £.J
/3/4 . &^
;3/<* . /$'
/3/7- e3
- - -
.j.
"t# ,?t
•j, *"rft3
Stack F'ress. liar
In. ,Hc-Gauae ?r
-. 7 '^z^l ^
02
=
ensure
9
7-"'
/ ,
^
" m
Tm
Ail
Stack
4ff*
*y ' /£'
4-Vz?
4 00
4ct>
*J/&
4ff&
^ ' C7V
4/0
4 ' fft?
4tsr
dj / &
^J &*&
Probe
2t>0
3*v
33 f
320
•2-70
-
Z€c
??o
3*V
^70
S$
3*0
Jj £1? "2Z. &o
4*e
git 0T?
^> #
•2-4°
2S^
3
.-'"L'te
^"
_J
(^
?.v
ft J
V-t.er - C
i-stack •= Tst
7J771 T-"ctor ir
?f:77J ^
/
(
% H-,0 = *oz
.OL
(^-' P/?L^t - /^66 \
// - ef^&G - • 327)
Imp.
»1
ck
t*2
Tdeal)= "3
Actual)= -t>/'°
Silica
Vol.
(End) Vol. (Start) AVol.(ml)
y^t?
^^.r
tJ-
/ , 2.3
' -^
i'T
/7
Total
Total Vol. H,o
4
37
Aarams
100
-------
PARTICULATE
DATA
Leak Check Rate
3
ISOKINETICS -
Vac
in. Hg
ft /min
TEST NUMBER /^
DATE
OPERATOR
FUEL •~Re,/04.d
SITE £3
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
AH
Meter Reading
EMPERATURES, " F
Stack
Probe
Oven
Imoinqers
In i OuF
Meter
o2.%
Vac.
,77
2-
32.°
. 72-
2.
°
,02.
5?
A 5
./t
7°
7
-7°
7°
./
-70
f
7
-------
102
-------
FARTICULATE
DATA
*.. f^t"
Leak Check Bate
•2- » TEST N"«PF
Of
Before
P ROB E LCO.r:DN /y£ P C?«-^
Sample
Point
Time
METER CONDITIONS
.27
AH
Meter Reading
Stack
Probe
Oven
n ' Out
H Meter
o,%
Vac.
7s'
70
7
\
-
/. 7
£70
230
:?/g>
(0
.IS"
3.26
(1
O,
.11
///?,
230
.00 -
J'/o
A/3-
,33 /.)
{00
- -r-
7
•72
|o_
! /-
, io
70
.-?§'
.Average
7o
Imr. Vol. (End) Vol. (Start/ TA'ol. (nl)
F =
m^ter
Fer cer.t 0-> = I
«2
»3
3
T^al 7,
.c f /.
103
-------
FARTICULATE
DATA
Leak Check Rate
in. Hg ft /mm
ISCKIN'ETICS
/C2 i%
TEST NUMBER
OPERATOR
FUEL
SITE
PROEE
R /G
Sample I .
^TEP CONDITIONS
Tt..^-^ URES , F
A Ps I AH 'Meter Reading Stack
J_
Probe
Oven
I .T.D i r. o e r s
In Out
Meter
Vac,
At-
r
57
r
ST
.s-r
/•I?
/oo
/3
J ?0
p/f I I,
! 2^
£
JT
/ *-o
//o
.A
ve -age
/.r
S02.
7
^_J
Irar. Vol - (End) Vol. fSTiar^; iVol. {ml)_
7. VVJ>1 ;rJ
SZ'
S3
o
5- r
104
-------
PARTICULATE
DATA
Leak Check _Ra_te_
Vac
in. Ho ft3 'ra
ISOKINETICS =
TEST NUMBER
OPERATOR
s
SITE '£>
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
AH i Meter Reading
TEMPERATURES, 'F
Stack
Probe
Oven
Irr.oir.aers
In Out
Meter
Vac.
. A3
-470
70
7?
/<<
7o
/o_
/.c,
6s-
o
,24
—4.......
I-
,£0
JL
.4,
70
^2^
.?0
70
/on
.Average
A/Vp
Imp. Vol._[_En^)_ Vcl. 'Start)
fl
, 3 if'f
105
-------
TEET w&zi. / /
START /g?AC? .
In. Hc-r.auqe
Nomng r a ph S e rup
p r
*meter ^
^stack Tstack
"-"meter &*
AHg Noz(Ideal)=
% ri2O ^ Noz(Acrual)=^J
.6^
laip. Vol. (End) Vol. (Start) AVol . I
O
/
-------
PARTICULATE
DATA
Leah D-ieck Rate
Vac
ISOK:NETICS
TEST N-.-fcEP /,9
Furl-
SITE
_
iOKE LOCATION gift C\J\
Sample
Point
Time
/'•'07
l-^TER CONDITIONS
AH
Meter Reading
Stack
Probe
Oven
Irr.Dinaers I
; Out '
70
Meter
0 ,\ Vac.
7?
7*
.7?
. iff
3?
4?
X Jo
: (.{
6
-/O
7
0,00
70
: o
fo
n
no. ? >
71 >.
.00
}.£>&
?o
-/o
30
'. /f
A
verae
/ 7 ^ J-
/(*?•
EAMPLE VOLfi
1C
Iir.r. Vol. (End) Vpi •_!^.-^.:"t
P"~
I Puck J-rsss. r,:i .^..trie
! In. Ho-3auije_ ! *Z*-:"-T.!L-
fercent Oj = I J
mtter
Pstack
-meter
Dig
'stack
Lf
Hc,:(Iiea:; =
NonActjall'.J-f/
T-.^
mL" ^
c .' 51 ar 11 .Gorans
AT)./ . //o
^"^ri
107
-------
Imp. Vol. iEndl Vol. (Start) £Vol. lu
Noz(Actuall= . J 7 7
•*r , , •<
. <^~r
108
TctaL Vci. n-,0
-------
PARTICULATE
DATA
Leak Check Race
ISOKINTTICS -
fOZ
TEST NUMBER
DATE
OPERATOR
FUEL Iff* foe Iff C J *--!.- r&~1
SITE
cfSicr-) Icrams
//f
Total Vol. rioO
109
-------
NozCcealia
Nol(Acri.al)= ^??
110
-------
PARTICULATE
DATA
Leak Check Rate
£c?JT
111
Total vol. H,o /'• a ™*
-------
112
-------
PARTICULATE
DATA
ISOKINETICS •
TEST NUMBER
A/
Vac
in. Hg
R fi
PROBE LOCATION
ample
oint
Time
^ETER CONDITIONS
AP
AH
Meter Reading
TEMPERATURES. °F
Stack
Probe
Oven
n I Out
Meter
Vac.
/TO
70
70
We
10
Y/
ffo
/**
70
y
.yo
79-
£30
/SO
to
^Q_
U
.so
3~.cc>
12.
/3
I?. 3f
Hi^_
2-00
?0
h£.
/fO
Average
.1
sm, »OL. -5°!^Jfe-|e
METER VOL.
meter
f'stack
,-
'-'rcer.t u; = I I
IIT-. Vol. (End! Vol. (Start) AVol. I ml)
.2 /O
S3 J
:«!,- ^//
* >Z S silica I / t^ C*
113
Total
Q (Start) .Larams
Total Vcl.
-------
DATA
L-eak Check Rate
ISIKIN'ETICS I I. A \ TEST !.".'^,EK
114
-------
PARTICULATE
iTA
Leak Check fete
3 ,,
ISOKINETTCS
Vac
in. Hq
ftj/nun
FUEL (Je^fa eft
SITE B
PROEE LOCATION
ample
oint
Time
METER CONDITIONS
APS I AH
JHeter Reading
TE.nPERATURES, ' F
Stack
Probe
Oven
Imcinaers
I n ' Out
Meter
Vac.
S>o
•A*
/JTO
I/*.
S
y
?£>
8
3&0
to
O-Oo
Average
SAMPLE VOL|«?7.73>
ft3 Co«>.
,W>| -/.
Stack ?ress.
In. Hc-Gauqe
Percent Oj
baronotnc
Nomouraph Setup
p ~ C -
Pstack - Tstack
rmeter - iP -
iHg - NozlIdeal)=
» H20 - Noz(Actual)- /4
Imp. Vol.lEndJ^ Vol. (Start) AVol. (mil
- ~3?
/oo
s
«3 _& 0 - 0
,y Total y fe?
P4 g(£nd) c(Start) ^.ararr-s
Core.
Total Vol. H,0 O-J nl
115
-------
mr. Vol. (End) Vol. (Start) tvol. (ml)
116
-------
FARTICUIATE
117
-------
DATA
-Sarrlino Time I
Per Point , Ki*1 Before
DATE
OPERATOR
-0
PKOEE LOCATTilll
Sair.ple _.
T .' Tine
:?cint
t-^TER CONDITIONS
A PC
Meter Reading
.33
Stack Probe
Oven
In : Out
Meter
for
3-
_3_
JL
_r
(y
1*
.11 \ A?°
.sv
/_?^/.
.5-0
r/o
T
£t
74
-P
(0.0
II
. 57
j/2.
12
/3
/3
l/v
KA_
7- V
3/R
xr
1 2 ^
k?./*
//*
/, .37?
.373 ;.oo
7-
Average e
23, j-oo
=T=
Noz(!deal)=
Irar. Vol. lEnii) Vcl. !Srarti ;,vc»:. (ml'
" /I? /oo ^2_S__
f; / 31 _/_0_Q _ J /
~T,--.! __14_
118
-------
PARTICULATE
Leak Check Rate
Vac
ISOKIN'ETICS
Sampling Time |
Per Point, Kin [ Before
SATE
OiLU.TOR
Ircr. Vol.(End) Vol. (Star-) AVol.lral
/I, f\^r Corf-
119
-------
TEST \"JMEER 2 ^
OPEPJ\T9R
Imp. Vol.(End) Vol. (Start) gvol.lull
120
Total Vcl. H,o g^ J?i
-------
Leak Ch"jck__Rat£
Vac
JSOKINETICS «
~:.liriy Tine
Ter Point, y.:n
TEST f^'M^EF
DATE 'SfJ/Ti
OrEKATOR ^ £°C
FUEL /^ty. £W
SITE g
PROBE LOCATION gZ/? C> «T"
ISarople
Point
Time
APS
>
AH ,Meter Reading] Stack
.SO
Probe
/7o
Oven
Tfo
.TDir.aers
I n ; Out
Meter
Vac.
^_
ft S3. o-/
/Jo
• /r
1.
-Go
^^^
T'c?
.Jo
9r>
s-
10
/GO
(1
--20
17
i?
/£>
y
C)-c?o
_\ i
~
I 20 I
•2.0 .y
—r -| -|
.2 V
22
i oo
lift. 23
.A
verae
y
Imp^ Vol. (Lndl Vcl_^ __ !3^t_a_£O_ .'VcO . (-all
/ti ~> _
O
JO
O
.
'-trct-r.t 02 = |
121
-------
I.ATA
122
-------
FrtRTICULATE
S~^~"i—: r \ in. hi
Per Point, Kin I Be fore
DATE
Gf'Kt.ATOF
FUEL
SITE
PRr?r: LOCATION tsCR O
Sample
Point
Time
METER CONDITIONS
AH
Meter Reading
. ;* ?y
Stack
Probe
210
Oven
Irr.nir.aers \
Out_
\ Meter i 2
0 ,\ Vac.
72.
2-10
r
/ff;?, 9/r
?/*
CT
Xff7.
/70
/O
9-000 6 / <=
(Jffo
J/o
Co
,1*
2 <&o /,
S/o
4,0
/2
O.co
^L
2.00.
/1/
.2-0
/r
.*-
n
•2.60*. -i
/
2oie>. Q£-±~
'
62
91-
2?
.JB
?0
. (Xs
.Average
X1TES VOL.
.
/
-------
Nomoaraph Setup
Imr. Vol. (End) Vcl. (Start) Avcl . (ml)
:z™i '::
o
Total J "
c'r-,,rtj_ _-'lr*I:
/r / / _ ..9- f
Cf
124
Total Vol. HoO lf "•'-.
-------
PARTICULATE
DATA
Leak Check _Ra_t£
ISOKIXETICS = f'-) JL t
j'er Point, Mini
Before
After
TEST N"MBEP
DATE
Or-ERATOR
FUEL
SITE
PROEE LOCATION
ample
oint
Time
M^TER CONDITIONS
A H jMeter Reading
.2 c? f/ . I ic?
Stack
Probe
Oven
I.T.oiraers
In ; Out
Meter
fry
Vac.
'II
S'J-o
S>S>
,13
r
'3-027.
3/j-
,/JS
2/0
/Y
7
o.oo
to
J?
P,00
13,
XJF
./!> V
C
/C
6.0&
n
/?
^L
.3 Jo
, FO
.S"U o
2i£_
6?
Average
O.oo
S/6
2.0 IT-
^^o^/L
mr-ter
^stack
^"nc-ter
AHa
Imp. Vol.(End) Vol. !Start)
n /3S~ /OO
Noz(Iaeal)=
tJcz (Actual) =
o
0
O
fll'izr Cc'rr fn<-H»--/.
OiXQ,
Total y^
c 'Srcirt) Ac raj P
'r-/. o /g, -z
125
-------
Leat Check kate
ISOKZ HETICS - f J *
SITE £j
PROHE LOCATION ,
fSarr.ple
IPcint
'Time
METER CONDITIONS
APS
A H iMeter Reading
Stack
Probe i Oven
Iroinaers
7 60
2.0
I n Out
/O
i Vac.
.JTO
• 3S-
&
1,0
. Av e r a q e
•-"j/^/nr
Imp. Vol. (End) Vol. (Start.) AVol- (
^
I -^ W,o) T
J,;
/.?,
!ioz (Act ual) =
126
-------
PARTICULATE
DATA
Leak Check Bate
ISOKINETICS -
Vac
in. Hq
ffVmin
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
C^
Sample
Point
Time
METER CONDITIONS
A H Meter Reading
Stack
TEWERAlURES. °F
Probe
Oven
Impingers
-la.
ifot:
Meter
oa.%
Vac.
s-(o
JO
y
. /
/£*>
vy
f
26 ?l.
(0
? -T7
2/0
/©D
/I
-17
X3
7>.
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS
- 9<
Vac
in. Hg
ft3/min
Before
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
M
TEMPERATURES, "F
Sample
Point
Time
METER CONDITIONS
A H Meter Reading
Stack
Probe
Oven
imoinqers
In
Out
Meter
o2,%
Vac.
24 "Z>
z.
£ZJ
Sfeo
//o
ttL
YJT
57)5-
.c?
. O/o
(O
• 23
r?
.23
• 3V
y. 750
230
/Y
oyo
2.?
/-2-0
Average
SAMPLE VOL|
RT / *
CplCOt
Percent
Stack Press.
In. Hq'Gauge
- c/.o'X?0
0, -
Barometric
Pressure
z^f.q ^
Nomograph Setup
pmeter " C
'stack • *.
''meter "
AHg - Noz(Ideal)-
% HjO - Noz(Actual)-
'stack
OP
Imp. Vol. (End) Vol. (Start) AVol.(ml)
•i y 2- y - /e><3 - ?s
O - 0.0
13
Silica
Ccl .
To
,tal 3fo
g(Start)
Total Vol. H2O
-------
PARTICULATE LAB WORKSHEET
TEST NO. ^ filler (^V (Inlet, Outlet) LOCATION lft,l$,'/f /V
Date /V'2/" 77 BOX No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
\ /
V
A
/ \
/ \
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
a
—
6 V, HI?L
£Y>//£/
£ V
/ 7^^^
—
,7V^ 6
BLANK
NO.
\
\
\
\
\
/
/
/"'
/
/
/
/
Y
\
\
^-^
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
\ /
\/
A
/ \
t^ / i * i (£> /
V"> / . J / (& f
/ ^ y , """ *^ >* -"^
—
£V. f 7_4^
, /
^-^
A Vic = ml LOAD klb/hr
A DgV = ft3 0? %
A Mn ^/ 0%2-,'ti' mgm REMARKS:
/
/
/
/
^
129
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. JV) I'oi/erfo Inlet,
Outlet) LOCATION 77
-------
PARTICULATE LAB WORKSHEET
TEST NO. Oft /y\4//^^7Tlnlet ,
Outlet) LOCATION /^ /~ 5, /^ l~2>
Date 1- H. d/i i 7
£ H. Ok It
— -
£v, otii
A Vic
DRY
FLASK
\ /
\ /
\ /
\ '/
\ /
Y
/\
_/ \^
FILTER
NO.
^
— -
7<-! LOL 1
^1.1017
(*<-!, 10 L 7
^/.WIH
im L~
^ /
\ /
V /
\/
A
// \^
I.U7L
l,/(o(,g
{./£& 4
—
.^11 1
\
\
\
X
\
_^^
A Vic = ml LOAD klb/hr
A DgV = ft3 O? %
A Mn mgm REMARKS:
/
/
/
/
<
^^~~^_
131
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. Ll /3 at' Iff fy/llnlet ,
Outlet) LOCATION 77* / ^ 'Tf. [H?
Date /-<£' 7S7 Box No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H2O RINSE
I /
\ /
\ /
\ /
\ /
V
/\
/ \
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
—
6
—
£ 7. £/ 0 /
&q,oo?c,
dy.noil
—
by.ooiry
A Vic
DRY
FLASK
—
3
— —
£lfT7V
^ ?,
^^
/
/
/
/
/
/
\
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
\ /
\/
A
X
(,CfJ070
Cq,iO(?"t
—
^.1070
/~) C/ <•? 1
t L/ i y I
7i. v/?r
7/,V/J^
—
—
~7/.V(5G
7.7(011
, PY / s^
.?cfl7
• 9C1I
-------
PARTICULATE LAB WORKSHEET
TEST NO. Y^/A-^rdnlet,
"/"""* ~r~ <~ -r~ ^?
Outlet) LOCATION (?-, I Jile l~~>
Date /-(•>- 7? Box No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
\ /
w
X
/ \
/ \
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
—
7
. —
f-S.^X}*/
^'l^Z'L'-l
& v, 5"^ / r
—
^1,^16
A Vic
DRV
FLASK
\ /
\ /
\ /
\ /
\ /
V
A
/ \^
FILTER
NO.
—
y
—
. 1*10
,7-T/V
—
/ If IL
BLANK
NO.
\
\
\
\
\
\
___ — •"
/
/
/
/
/
/
/
V
\^__
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
\ /
\ /
X
^/ ^^
Cy.to1?^
6<-l.M20
k-l.tf ?;?
—
&<-/. b^VI
, 05T5'
\ i
\ i
\ /
X
/, I'1 ^2
Li-z^n
i nm,
—
/ jfig
,3?}^
V
\
\
\
s
A Vic = ml LOAD klb/hr
A DgV = ft3 Op %
A Mn *-/ T-^ . I rogm REMARKS:
/
/
/
/
/
"^^~^^
133
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO. (Q - /30l'/tf ^/Tlnlet, Outlet)
LOCATION f,(
Date 1 - 1 I ~ ?& Box No- Enc?-
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.
H2O RINSE
\ /
\ /
\ /
I /
\ /
\ /
y
/ ^^^
Final
Initial
A Vic
ACETONE
RINSE
—
/ >
I- 10-1?
6V.V/51
— —
6 "-/>// ? v
Impinger Water Vol
1 2
3
(ml)
Total
DRY
FLASK
/ /
/- /£?-7*
5~^, 5"t'/
70.WZ
—
^a Y3f6
FILTER
NO.
—
#
— •
,760V
.76/t
.76/5
,7 (,10
BLANK
NO.
\
\
\
\
\
\
s
^~^
/
/
/
/
-\
^\
POST TEST WTS.
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
\ /
\ /
\ /
\ /
X
^•-' X^
6C/S'Y5'2
^ ^ ^YC /
6V, CVs'O
—
6 *-(, r*/r /
,/'>/?
ml
(J.U1L
^
L? It hi? I 1
&L (if
;^
I/. in?
,^273
.Ctl7<
, 41 If
—
, <^Z7V
/ /66V
\
\
\
\
\x
^^~^
LOAD
J
/
/
/
^-^-^_
klb/hr
ft3 0, %
/ / ) 3 /. £r mgm
REMARKS:
134
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST
Date
Test
Dry
NO. O >H4/n-d2f^Inlet' Outlet) LOCATION I c$ ( <
I- 11- 7*? Box No. Eng.
Description
?:r ft
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.
H20 RINSE
\ /
\ /
\ /
\ /
\ /
V /
A
y ^_
ACETONE
RINSE
/ <-l
1-10-7%
6*f. oo H 7
£4.00^2-
f<,y.(yOHf
M.OOff
DRY
FLASK
\ /
\ /
\ /
\ /
\ /
\/
/\
y \
FILTER
NO.
<-/
—
, ? <
, tt 3
,7^33
BLANK
NO.
\
\
\
\
\
\
\
/
_^^
i
/
/
/
/
/
/
\
POST TEST WTS.
AVG.
A WT.
A Vic =
A DgV =
A Mn
ml
mgm
LOAD_
°2_
REMARKS:
klb/hr
135
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. b r^u /r.-fl-jQ
Date /- If - /"
Eng.
Test Description 5/ ?//-?«. f- S~ ^*, h ^s Tsrblrs 5/^\55 **"*/• a t r^
Dry Gas Meter Vol (ft3)
Fi na 1
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
—^~
Z-Z-
( G"
DATE WT.
/-it-??
/- 10
TARE WT.
it>(jQ
00
<-/<(,
AVG.
POST TEST WTS.
AVG.
A WT.
A Vic =
A DgV =
A Mn
ml
ft3
rngm
LOAD_
°2_
REMARKS:
klb/hr
136
8830-5 rev.
-------
PARTICIPATE LAB WORKSHEET
TEST NO. -
Date -
, Outlet)
Box No.
Test Description
LOCATION Test
Eng.
/
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
to
\
DATE WT.
- 10-7?
X
TARE WT.
\z
if
/\
\
AVG-
POST TEST WTS.
*
L
AVG.
.
A WT.
10. £7 it,
A Vic
A DgV
A Mn
ml
LOAD
REMARKS:
klb/hr
%
137
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date / - /2. -
, Outlet)
Box No.
LOG ATI ON /A T 5, / <•
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
Total
CONTENT
H2O RINSE
V
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
\
DATE WT.
X
¥
X
TARE WT.
. 7V.5P7
/\
\
\
AVG.
\
POST TEST WTS.
X
\
\
C<-f. 77^^
l.^///
A 1110
x
\
AVG.
\
'.V -7793
f: ^///J-
s
A WT.
h Vic =
A DgV =
A Mn
ml
ft3
mgm
LOAD_
°2_
REMARKS:
klb/hr
138
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /t^^/r.-O^f^Inlet, Outlet)
Date /- //- 75? Box No.
Test Description
LOCATION
Eng.
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO
BEAKER .NO
DATE WT.
TARE WT.
AVG.
B
.
1
2
3
4
H2O RINSE
tO^ C*Ja«f
*2.6
I- 1*1- 7?
£7.¥'Wfo
67,^?7
£7, ^>3^C^L^
(
/-/7-7fP
&/£f £ £*•//*)?
w.£c//
•3^^-Z
3/-?r, /
*>OC,I
-~r
V)£ /
3
BLANK
NO.
T
otal
POST TEST WTS.
AVG.
A WT.
A Vic
A DgV
A Mn
1
2
f
3
4
=
£7?£<^X
^7,^2^7
/* "7 ^/ ^ ^y /
Lo ( f ( Z* / (a
£7
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet-, Outlet)
Box No.
Test Description
LOCATI ON
Eng.
R^r .9,7?
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
Total
CONTENT
H2O RINSE
s
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
X
BOTTLE NO.
s
BEAKER NO.
s
DATE WT.
I -1C,
/-1 1-78
TARE WT.
\
\
X
\
AVG.
.77 r 7
POST TEST WTS.
A Vic =
A DgV =
A Mn
ml
LOAD_
°2_
mgm
REMARKS :
klb/hr
140
8830-5 rev.
-------
WORKSHEET
TEST NO.
Date
Test Description
-, Outlet)
Box No.
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
Total
CONTENT
H2O RINSE
X
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
\
BEAKER NO.
\
DATE WT.
TARE WT.
7
7
\
K
AVG.
POST TEST WTS.
A Vic =
A DgV =
A Mn
ff C 7.
ml
LOAD
mgm
REMARKS:
kli/hr
%
141
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST NO.
( Inlet", Outlet)
LOCATI ON /X 7"
/.J?
Date Box No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/\
/ Y
/ \
1
2
3
4
AVG.
A WT.
\ /
\ /
V
A
/ \
/ \
Impinger Water Vol (ml)
123 Total
Final — - J__ _. '
Initial J^T^-CCH^
ACETONE
RINSE
3
A Vic | •--— ^_
'
DRY
FLASK
—
£ 6
/~2T'7?T
f.7.^77
£-7.7
,171?
, f-73 ^
—
,^75^
.ZO,'>,/ mgm REMARKS :
/
/
x
\
\
\
8830-5 rev.
-------
PARTTCUL.ATE 1AB WORKSHEET
TEST NO.
Date
', 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)
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
S
BEAKER NO.
J_Z_
£ -7
s
DATE WT.
t-i6~TV
TARE WT.
& V,
^
\
AVG.
POST TEST WTS.
5
\
s
_^£A.
i.&c-oo
X
AVG.
X
\
A WT.
12.70
A Vic =
A DgV =
A Mn
ml
LOAD
jngm
REMARKS:
143
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TES
T NO. ///} -fyltr fi r(Inlet", Outlet) LOCATION //'>/' f
e /~ °^ 7V7 Box No. Eng.
-,;r. (\
Test Description 1 &O t^ AVcry CD 1c S\>
Dry
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
\ /
\ /
\ /
V
A
/ \
/ Y
/ \
ACETONE
RINSE
—
7?.
-------
F ART! C'JI ATE LA3 WOPKSHEET
TEST NO.///?, yylfl,/, ^/7-dnlef, Outlet)
LOG ATI ON T .5;,r.
Date /- "tf- 7V7 Bo* No. Eng.
Test Description
/V\et<. n P /\. JOOK
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
\ /
\ /
\ /
V
A
/ \
/ \
/ \
1
2
3
4
AVG.
A WT.
\ /
YY
A
/ \
/ \
Impinger Water Vol (ml)
1 2 3 Total
Final • _ _.— - — "^
Initial ^l!^*-1^^!!!
ACETONE
RINSE
"?r
1-29- if
£?.<-/(,*,-&
CZ-^t^t '
6<< ^(,^1
—
c ?. -/(, r-r
A Vic " ^_
DRY
FLASK
S,^
/- ^&~?3'
^C/ ^^t//
6^/. tit, ?>*f
—
t,*/, &£ VO
FILTER
NO.
/£
/"2^-^
t ?c,/£r
. ?(-(£>
—
—
. 7^ i^
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
£^^/-/
,
-------
PARTICULATE LAB WORKSHEET
TEST NO-
Date /-
Test Description
-, Outlet)
Box No.
/H/V r
LOCATION
Eng.
inn k
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
s
BOTTLE NO.
s
BEAKER NO.
1-7
V
DATE WT.
TARE WT.
\
76-5 C.
76 -9 &
X
X
AVG.
POST TEST WTS.
\
\
C'-f.
7(.
AVG.
\
7f.
A WT.
\
A Vic =
A DgV =
A Mn
ml
LOAD
klb/hr
'~7 mgm
REMARKS:
146
8830-5 rev.
-------
PARTICIPATE LAB WORKSHEET
TEST NO.
Date
Test Description
^,/IInlet-, Outlet)
Box No.
/n,^ r>
LOCATION
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
Total
CONTENT
H2O RINSE
\
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
w
A
\
DATE WT.
TARE WT.
X
\z
/\
\~
AVG.
POST TEST WTS.
X
X
_i2_2
, mic
,2910
AVG.
, %?£/
L/
A WT.
h Vic =
h DgV =
h Mn
ml
mgm
LOAD_
°2_
REMARKS:
klb/hr
147
8830-5 rev.
-------
?ARTICULATE LAB WORKSHEET
TEST NO. /
Date £
r pjp pyj- (Inlet', Outlet) LOCATION ,
'-/T-/7^ Box No. Eng.
tecT 7
~Tf> L/
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.
H2O RINSE
\ /
\ /
\ /
Y
A
/ \
/ \
/ \
Final
Initial
A Vic
ACETONE
RINSE
•
^/ •>
1 _ ^_ 7;^
(.<-/. nr*-)
7V 7O
7L/<$$>
,-7^
/
/
/ \
/ \
BLANK
NO.
\
\
\
\
/
/
/
, 777^
7^/
—
. —
f 77<^0
,03-^0-
/
/
/
\
\
\
\
^\
\
/
/
/
/
/
/
\^
\
\
LOAD klb/hr
0
2
%
REMARKS:
148
8830-5 rev.
-------
PAP.TJC'JL-ATE T..5.? WO'RI'SHTET
TEST NO.
(Inlet', Outlet)
LOCATION 77} / J?,'/'7(' /31
Date /: ' 6 7^ Box No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ \
/ \
1
2
3
4
AVG.
A WT.
\ /
\ /
V
A
7\
/ \
Impinger Water Vol (ml)
123 Total
Final ' — _ _ ._- ' '
Initial T^->~'::::^IZ
ACETONE
RINSE
V 2-
2- 7- 7-9'
C^^L^O
£C1.^£L«)
CC1.
Date '2." /- /5f Box No. Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/\
/ \
/ \
1
2
3
4
AVG.
A WT.
V^ /
\ /
V
A
/ \
/ \
Impinger Water Vol (ml)
123 Total
Final — —^ . ~~~
Initial ^^^^^-^L
ACETONE
RINSE
vr
2- ^-7^'
£&,H^O
C-?,^5^
C% , t-tb^y
- —
£^ %f/
A Vic __ — - — T^ -~^_
DRY
FLASK
\ /
\ /
\ /
y
A
/ \
/ \
/ \
FILTER
NO.
' —
2 -^
^ - S~- 79
•?<"*£
, -7f*}O
. 7
-------
PARTICLE-ATE LAB WORKSHEET
TEST
Date
Test
NO- /7 nAse,!* ^/tlnlet', Outlet) LOCATION T^<,T~
"J-"^-?'?5 Box No. Eng.
Description
?.r,n
Dry 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
\ /
\ /
\ /
V
A
/ \
/ \
/ \
ACETONE
RINSE
•
TO
•Z- 4- ?
£) <>'K
FILTER
NO.
—
2-Y
z-. r- j^
.75- 1-/
.?•&!.
t1CGl.
—
,7. 2$ re,
A Vic =
A DgV =
A Mn
ml
ft3
mgm
LOAD_
°2_
klb/hr
REMARKS:
153
8830-5 rev.
-------
FARTICULATE LAB WORKSHEET
TEST NO . ($ /5h,'
Date
1 - I 7
Test Description
, Outlet)
Box No.
LOCATI ON /V'., / S*<
Eng.
<
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
CONTENT
H2O RINSE
5
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
S
BOTTLE NO.
S
BEAKER NO.
2,-
\
DATE WT.
TARE WT.
i~Ot 30 -7O
X
AVG.
TO,
POST TEST WTS.
\
\
\
5D,
£&.<-/? tO
I ,
AVG.
^
A WT.
A Vic =
A DgV =
A Mn
ml
LOAD
ingm
REMARKS:
kLb/hr
%
154
8830-5 rev.
-------
FA31ICUIATE IAE KCHSr.'iL
,„
T£ST NO.JJ
(Inlet, Outlet)
Test Description
LOCATION
--''9-
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Irnrinqr-r Water Vol (mi;
2
.
155
-------
£
-------
ATS LAB WG?_K£HEET
TEST N0./f /
D3te o./ / g / 7 /
Test Description
, Outlet)
Box No.
LOCATION /_
En c.
. ft R
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Irnpinger Water Vol (ml)
A Vic
A DgV
A Kn
ml
LOAD
02
klb/hr
%
157
-------
TEST NO .,2-0 Bid £>cJ( (Inlet, Outlet)
Date D-/l-g. I 18, Box No.
Test Description
LOCAT: OK 5 iTe.
£ng.
Dry Gas Meter Vol (ft3)
Final
Initi al
A DgV
Iir.oinger Water Vol
Final
Initial
A Vic
Total
A Vic =
A DgV =
A Mn
ml
•r- 3
LOAD
klb/hr
158
-------
PARTICULATE LAB WORKSHEET
TEST N0.2O
Date
f>JT'(Inlet, Outlet)
7* Box No.
Test Description
LOCATION 5 I
End.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A Vic
A DgV
A Mn
ml
ft3
LOAD
kUb/Tir
^-ARKS :
159
-------
?ARTICULATE LAB WORKSHEET
TEST NO.P; g<.(?£X?T~ (Inlet, Outlet)
Bate _ 2. / ,?£> / 7 S Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Ini ti a 1
A DgV
Impinger Water Vol (ml)
A Vic =
A DgV =
A l-ti
ml
LOAD
/^/ OO y. 9
REMARKS:
160
&530-5.. rev.
-------
PARTICIPATE LAB WORKSHEET
TEST
Date
_ P/po/7g
Test Description
oJTTCnlet, Outlet)
Box No.
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final
initial
Impinger Water Vol (ml)
A DgV
CONTENT
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO
BEAKER NO
A
V
DATE WT;
TARE WT.
X
\
\
s
AVG.
POST TEST WTS.
5
x
5
3- ?
AVG.
_£L
^
A WT.
,2 CO 7
A Vic
A DgV
A Mn
ml
ft3
mgin
LOAD
REMARKS :
kli/hr
161
-------
NO-Z2. glR. O^T (Inlet, Outlet)
/7X 3cx No.
LOG ATI ON /
Test Description
Dry Gas Meter Vol (ft3)
Fi r, a 1
Initial
A DgV
IiTipiuger Water Vol (ml)
/ \
77.7'94 /.Q'/e?
~Z.
V
A Vic =
A DgV =
A Mn
ml
LOAD
klb/hr
%
-------
PARTICIPATE LAB WORKSHEET
TEST NO.pL2. fatt\AOJC~(Inlet, Outlet)
Date 1^lm/?X Box No.
Test Description_
LOCATI ON
Eng.
5
Dry Gas Meter Vol (ft3)
Final
Ini ti a 1
A DgV
Impinger Water Vol (ml)
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
•72.
2?
\
DATE
\
TARE WT.
X
So.
X
P.VG.
A Vic
A DgV
A Mn
POST TEST WTS.
ml
mgm
LOAD
02.
RERARKS:
klb/hr
163
.SS3C-5 rev.
-------
'A?.TIC'_TATE LAB WORKSHEET
TEST NO . 2 j-g<~* j 7£ Bex NO-
Test Description
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final
Initi al
A DaV
Impinger Water Vol (ml)
Final
Initial
A Vic
3 |Total
A Vic =
L DgV =
ml
ft3
mam
klb/hr
%
EE FA PICS :
164
-------
PARTICULATE LAB WORKSHEET
TEST N0,2> /If^UCbTTlnlet, Outlet)
Date _ g-/^3 / 7 t Box No.
Test Description
LOCATION_
Eng.
^s,^ g
Dry Gas Meter Vol (ft3)
Final
initial
ipinger Water Vol (ml)
POST TEST VvTS.
s
v
SO.
/O£/o I >^
X
K
SI
AVG.
X
A WT.
S
NJ
A Vic
A DgV
A Mn
/ o
-------
No.
LCCATI DK
En c.
Test Descri-otion
Jry Gas Meter Vol (ft3)
Final
Initial
A DcV
iir.oir;aer Wa^er Vol (ml)
Zi X7lc =
A DgV =
A Mn
I,OAD
klb/hr
%
166
-------
PARTICIPATE LAB WORKSHEET
TEST NO/lW
Date
Test Description
, Outlet)
Box No.
LOCATION
Eng.
2
Dry Gas Meter Vol (ft3)
Final
Initial
Imoinger Water Vol (ml)
A DgV
Final
Initial
A Vic
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
ILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
?<£
3X
\
DATE WT. .
TARE WT.
\
s;
AVG.
A Vic =
A DgV =
A Mn
POET TEST WTS.
ml
mgm
LOAD
JREKARKS:
klb/hr
%
167
SZB^-S re-,
-------
FXRTICURATE u^=. WC?J;S:-:EET
TEST N0.^5ll2kR_0^r"(Inlet, Outlet)
Date 3ox No.
LOG A Ti ON
Eng.
S,y-
Test Description
Pry Gas Meter Vol (ft3)
F i - a 1
Ini ti a 1
A DgV
Water Vol (ml)
A Vic
i DqV
ml
•r- 3
LOAD
kUb/hr
%
168
-------
PARTICULATE LAB VCO?_r;5HEET
TEST
Test Descriction
, Cutlet)
OCATION S
Dry Gas Meter Vol
Fir.a 1
Initial
Iirrpiriger Water Vol (ml)
A DgV
Final
Initial
A Vic
A Vj c
A DgV
A Mn
Klb/hr
169
-------
•TT5T NO..P-6 j?^ OJT~(Inlet, Outlet)
Date _3X_£~/ 7 ? Bex No.
Test Descrio-cion
Pry Gas Meter Vol (ft3)
Final
Jni ti al
A DgV
Iirrpiriger Water Vol (ml)
A Vic =
A DgV =
ml
LOAD
klb/hr
%
170
-------
PARTICIPATE LAB WORKSHEET
TEST NO..2.6 fllft.l< oJTTlnlet, Outlet)
-ete 3/£~/?£ Box No.
Test Description
LOCATION_
Eno.
Dry Gas Meter Vol (ft3)
Final
Initial
!__3_
i 4
POST TEST WTS .
K 7\ZL
///r/
J
_Lj*T_._
A vie =
A lev =
A Mn
/
ml
ft3
itigm
LOAD
02_
klb/nr
REMARKS :
171
-------
rARTICl
TEST NO.J2')
tJb "(Inlet, Outlet)
Box No.
Test uescriotion
LOG ATI ON
En g.
Dry Gas Meter Vol (ft3)
Fi r. a 1
Initial
Invpinger Water Vol (ml)
Vic =
DqV =
ml
klb/hr
172
-------
?ARTICULATE LAB vOrJ'JTHEET
TEST NO.,3.7/1, ^ r,JfiTlnlet, Outlet)
r>:>; No.
Test Description
LOCATION
En a.
Dry Gas Meter Vol (ft3)
Final
Ini t i a 1
A DgV
Inn-inger Water Vol (ml)
Total
Final
Initial
A Vic
L Vic =
A DgV =
A Mn
ml
-n-3
LOAD
REMARKS :
>,Ib/'hr
%
173
-------
?ARTICULATE LAB WORKSHEET
TEST NO.jZy &LI* O'-TTlnlet, Outlet)
Date Bo>: No.
Test Description
LOCAT! ON S"/
En a.
Dry Gas Meter Vol (ft3)
Fi n a 1
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
I
Total
A Vic =
A DgV =
A Mn
ml
LOAD
klb/hr
%
REMARKS:
174
8£30-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST N0.2ff/f
-------
SECTION 3,0
GASEOUS DATA
PAGE
3,1 GASEOUS EMISSION SUMMARY 177
3,2 GASEOUS EMISSION DATA SHEETS 180
3,3 SOx DATA SUMMARY 213
3,4 SOx DATA SHEETS 216
176
-------
GASEOUS EMISSION SUMMARY
Location:_
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
Sei/
er
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
N02
ppm
Wet
HC
ppm
Wet
D.
Dry
C02
%
Dry
CO
Ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry.
NOTES
-pou
no
301
OQS
28
low le>4c|
5.0
00.5
333
l/X/78
£7
Jov load
a. 2.
292.
47
. Jb/r
l/B/76
6-6
fc.03
fair
l/il/78
75-
norm OF A
32.
blr
mech ,
lie,
76
reduced OFA
/2.&/16
73-
25-
306
loir*.
I/2.6/78
73
237
, blr,
4- <*vfi« M _
/Oq
I/2-7/78
//.-a
35-1
peo'uceol
31}
8-8
/o.y
^73
5". 8
norm OF/
8.8
/0-6
96
cart" blr
I/26/7&
rec/«cee/ OF/I
36
260
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
Bol Un Outlet
02
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
N02
ppm
Wet
HC
ppm
Wet
Q. C.
02
%
Dry
C02
%
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry.
NOTES
72.
//.fc
a.sw
£7
b//~
88
320
20
a//
73
6.8
35"
332.
73
DFn
3/0
bit", cut
22.
redueW (3FA
. A ,
2L3
•Z./22./7&
rem
r\ C
NOTE
: All parts per million (ppm) figures are corrected to a 3% O2 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
Dry
CO2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
SO2
ppm
Dry
SO3
ppm
Dry
NOTES
3/Z/78
•SW
part, felr ot(t-
, oat,
2.5-
3/3/76
5.3
13.7
4,0
2.6
99
5:3
83
£87
ouir
2.7
79
W\&t
L
2.8
3/^/76
8/
norm or>\
305
79
as
30
3//T/76
78
6.0
£32.
3/16/78
77
a-S -found
6.0
13-0
2,
3/20/7Q
76
JS.I
3)
33
79
a. 5 -foancj
6J
T^
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
PC./
-------
KVB
TEST SITE A 5/A A-5/fc
TEST NO /
DATE
GASEOUS EMISSIONS DATA
P> FUEL Kt^Tuc. /\f V Cfrr^hc
LOAD ^-/ /. /
II
CONDITIONS
DATA TAKEN BY J.&.fo.
Probe
Position
/ - c,
/- c
Ec,oiV,
£ £. t>/v.
ff /
pl
1*7 i/
^C
*<>
EfsfiN
(~0
l-b
FCOtf
Time
V-'.^
02
t
(dry
/'•^
(0.1
10. %_
in. q
e,*f
4,y
<*.o
4.0
d'G
&.C
ll->
(0$
*W
C02
\
(dry
&-t,
I't
t.k
#.(„
I (?."!>
10.1
10.1.
10.1
IO.1-
t.O
$.(*
11 -0
CO -
ppm(dry)
unc
—
—
_
—
^
.-
—
-
-
-
-
cor
NO
ppm(dry)
unc
16$
ier
no
i~?
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE /-. £?/V\/V- ".'iff P)
TEST NO 2-
DATE
12.- 2 1-7-7
FUEL ^ nTttc- ky ^- t^i^ bes /&!"&(
LOAD 2 7 x7
CONDITIONS /O ^ *
#2
* l~H
* J**/
*hc,
•* 1
* 7
*7-C
te/'/r/t a,/l
>V\*T.' .
SfjIISl o«/
Time
Id:*
IV*
'3ilL
fj-^-Tj
If,! t£
fc,2Q
lk&?
17*
02
(dry
(l.o
It, '1
/a
//,&
(0.5
//,$
//?/s
//.^
//.^
ti-^
((<(
-
C02
(dry
^.2.
X / (
9.0
?.£(
&.L
7-0
T,0
9.7
I
U3
•J*- -
2*0.1
z-^;;
/
/
CO •
ppm(dry)
UJ1C
—
-
-
-
*-
-
—
-
~
-
-
• '
».
W
w%
cor
NO
ppm(dry)
unc
flo
t9(
Itff
/f S"
/•9T
/6/
/VO
/<%(?
I7t>
Iff
cor
?VA)
?yy
1%>/
jra,-?
33^
*1 **L
"7 ^2
^7^
<37-y
3^V
127
•
HOT LINE SAMPLES, PPM (WTT)
NOx
unc
cor
*
NO
unc
cor
NO-j
unc
cor
HC
unc
cor
REMARKS
•
AVERAGES
W-
m
'm
w%,
^n r
L«— '— y-- ;
7 7 '
^
m.
WA
'vm
»
'
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A /3 /V\ A- 5, to B
TEST NO V2>
DATE
FUEL
LOAD_ <-/ "7. 3
CONDITIONS_
DATA TAKEN BY
Probe
Posi tion
Tim
02
t
(dry
C02
(di-y
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAKPIXS, PPM (WET)
unc cor
NO
unc cor
NO7
unc cor
HC
unc cor
REKARKS
to
I-LOO
»
lO
lap
lo
•
Lid
-pn?
&a
LL
362-
u±
^Zi
IbO
I_100_
13C
2£I
z-fu
JJc>l IfT (,*
r^O IT,
NOTE
1&3L
(O-f^
±LL
^M
9'\*
2Vi
^M/^
f/« /
?«
Parts per million (ppm) figures ar
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE AP>M\J\-£iTt
TEST NO
DATE
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
7.
Probe
Position
Tim
02
%
(dry
C02
CO •
ppra{<3ry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
NO
NO-j
HC
REKARXS
OffT'tr
*~&
360
£13.
'/•>:&
7,
2
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE /\ /> /V\ A- 5;Tc
TEST NO
DATE
/ " §* - 7
FUEL fi#Tfl
LOAD_
CONDITIONS
DATA TAKEN BY c). E.
Probe
Positip
Time
02
%
(dr
CO2 | CO -
ppm(dry)
fdry)|
unc cor
NO
ppin(dry)
HOT LINE SAMPLES, PPH (WET)
NOx
unc cor
NO
unc cor
unc cor
HC
unc cor
REMARKS
fi I
IQ'irt
fo
L^o
IO'.K -?,
II.O
1<2. «o
t
/Z/
170
GL
C.
10
22.2
_.?4.
C-JjLL
AVERAGES
/m
-------
KVB
GASEOUS EMISSIONS DATA
TEST S3
TEST NC
DATE
TE /U3/V\A-5ir, f
> C
1 - ll~ 7<5>
^ FUE]
LOAI
L
*'l.b-C,
K'/
P '£
*/-2 ?(>
*%£ '
£/lT/
p^
*/-£
" '/-£
* (-&
Tim
IfiM
t<;c
//••&
/2.!f
12$L
Hte
fi:i r
/?•'?
F/'H
/4" '(JC
02
(dry
(«,"/
c,t^
£O
2/ff
•2?, > '.
^
m%
Wk
m%
•17 '
Iffl -' :
v
-------
TEST SITE /I £? /W A - "S '{Tf f1)
TEST NO "7
DATE I - II
FUEL 5o.^/A £CPLES, PPM (WET)
unc cor
NO
unc cor
NO->
unc cor
HC
unc cor
REMARKS
£23.
Co
nt,,-
L2JL
-£l£±
/v, ?
10
70
r i
*7h
22_l
;JC/J'E: Parts per million (ppm) figures are
to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE/\ /^ /\/\
TEST NO Q
DATE /- 26-
FUEL f\
i / U C k\
CONDITIONS /-/,
DATA TAKEN BY
f /?. C?
Probe
Fositio
Tim
02
%
tflry
C02
(dry
CO •
ppm(dry)
unc cor
NO
ppiti(dry)
HOT LINE SAMPLES, PPM (WET)
NO
unc cor
NO?
unc cor
unc cor
REMARKS
T^T
2-4
f/'X
H£L
7.1
m.
LC
(A£i
1&&.
NOTE: Parts per million (ppm) f icrures • are IS/ected to 3% Q2
15900
-------
KVB
TEST SITE /I IJ> /V\ /\-6;ic
TEST NO ^
DATE
/ - f
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS
DATA TAKEN BY , ). &
Probe
Posi t io
Time
02
%
(dr
(dry
CO •
ppra(dry)
unc cor
NO
ppm (dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
unc cor
unc cor
REKARXS
r,*?
* /- s
2.0
2/
7.2
U/
.
M
t2_Q_
l£L
l£.
NOTE: Farts per mil] ion (ppm) figures aTe1' corrected to 3% 02
15900
-------
TEST SITE
TEST NO / {)
DATE
2 7-
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Tim
02
t
(dry
C02
%
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO-5
unc cor
HC
REMARKS
unc cor
10:
160
M.'l
®£
UL
'4&
It*
//r
22^
'•J=A.
KG
Ft-a iv
m
AVERAGES
m
NOTE: Parts per million (ppm) figures are d?ir?itted to 3% 02
15900
-------
KVB
TEST SITE_
TEST NO
DATE
GASEOUS EMISSIONS DATA
fc /3 FUEL_ /"I e
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Pos itio
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
2^
7JO
^£
10.53
V
111
~~%
NOTE: Parts per million (ppm) figrores areLJIH-ected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE /\ /3 AA A -•£"//? &
TEST NO
DATE
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
Q F A
Probe
*^
*;?-£
*?-£
FS-oiV
vfrt,
n-t,
*'!-(>
&Q
ty2
Itl
/(,'•<&
M%
/W
l?-'(l
02
%
(dry
#.%
T>,L
&.f
?#
^b
£,n
W
CO2
»
(dry
H'i
I/. 4
ax
M.?
//-I
/in
ac,
CO •
ppm(dry)
1(1
2f
K
in
?n
£C
^0
2%
1\"
t^
y
i\
^
NO
ppmtdry)
lift
1((
1(0
MO
170
WJ
Mo
?,Q6
716
2-r
^>?-
^
7-61
^Vf
•
HOT LINE SAMPLES, PPM (WET)
N
Ox
\
1
1O
NC
3?
}
1C
REMARKS
it.it
AVERAGES
lay
!H
NOTE: Parts per million (ppm) figures are4*#4ected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A /3 /V\ A ' Jiff I
TEST NO / 3
DATE
J FUEL ^5 /£ ^ d
LOAD ^7A b
*2 - 9 - X7^ CONDITIONS '2<^^l/ (^2
' ' ^ l s,
DATA TAKEN BY ( ) E C ^
Probe
Positio
* /-£
£Ctf/l/
*l'(o
EC^O l\i
fhc.Hfr
E^-OIM
Time
W
W
PC
02
(dry
'7,^
"2^
6/-7
c^^
\
~L
C02
(dry
' //,£
/3.6
/^/!
'/^
'/U
CO •
ppm(dry)
unc
40
rft
-tf
1$
3f
cor
n ^
Ct7
3C
•^Cf
L9
36>
NO
ppm(dry)
unc
2O"
/?/
110
170
190
160
cor
7
unc
cor
*
NO
unc
cor
NO •?
unc
cor
HC
unc
cor
REMARKS
AVEPAGES -,
/
/
/
'/
's
y
/
W%
'»
^
m;
/
/
'/
/
•'m.
-
-------
KVB
TEST SITE /•
TEST NO ,
DATE >
TfT
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
71
Probe
Position
Time
02
t
{dry
C02
(dry
ppjn(dry)
NO
ppm(dry)
unc cor
NOx
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
IV-l
llo
12-
7-
10
££>
122.
t;oo
2V
lo_
-fftr
AVERAGES
•2.—
L-^Hi
•m
It
iM
'^
y/m
NOTE: Parts per million (ppm)_ figures aral*c
-------
KV3
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO /_
DATE 2^.
IT, P)
FUEL / \ g /
LOAD S 7
CONDITIONS >o n
DATA TAKEN BY
-------
KVB
TEST SITE /-\
TEST NO l_
DATE 2
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
r\
Probe
Position
Tim
02
*
(dry
COi
(dry
CO •
ppm(dry)
unc cor
NO
ppro(dry)
unc cor
HOT LIKE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
PXKARXS
11L
(,.
ItJ*
10
IXL
11
it-
7.0
tff
rr
20
I2.fi
to
Ay
^Y
it*
TJL
TL
£Z
42
ftr
£i
wo
7,0
/ C
Om.
11,0
U-
TL%-
(£L
UL
2J-
tgr
&L
LL2.
m,
^M
Jl
A£.
NOTE: Parts per million (ppm) figures are cd»?&ed to 3% 62
15900
-------
KV3
TEST SITE /•
TEST NO / 7
DATE
2-1-7B
GASEOUS EMISSIONS DATA
TT/p FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
d
Probe
Positdo
Pre Te. ST
(L 0/v\p
*I-X
*i- CT
*y- v
*/- v
*!-£
•i-s
*/-f
fau/r/
F c ON
*i-s-
Time
I0:'
/O-'K
/l-'Ot
I/-T<
nuo
11:10
ft!3l
I2'i(
02
%
(dry)
?i6.-f
i 6,7
i (?,6
7 (,,«
^.3
6.8
1^
>().$
MiAS.b
IZ-K
I1): 10
-7.1
6,7
C02
\
(dry)
/?.->"
/^ ?
lift
n.,i
v.z
n.?
IIH
IK
m
ntf
n.i
CO -
ppm(dry)
unc
to
37
17
V2
VO
W
?7
.30
40
1%
3.5"
cor
62
*/7
V/7
fV
<7^
?8
^r
37
Y7
W
w
NO
ppm f dry )
unc
W(
2V
^r^
ICO
uo
16,0
1-60
1^(\
250
?do
itf
cor
2W
,^(72
T/>
-712
7^
7)^?
"?/^
?/7
2
7. 1
/2.V
02.
>W
^7
-------
KVB
TEST SITE A P) M/N - 5'fr
TEST NO / Q
DATE
GASEOUS EMISSIONS DATA
/3 FUEL_
LOAD
2-11-78
CONDITIONS /V\c*X
DATA TAKEN BY C/ °. /^.
Probe
Position
n-t>
*2-b
*2-6
*2-t>
*2-6
*2-6
*<2-b
*2-6
*2-6
*2-6
*2-
12.1
12.6,
4.5
izfi
CO •
ppm(dry)
unc
HO
HO
$0
bQ
/OO
HO
/y^
160
IbQ
170
IftO
l$5
}<*0
its
195
cor
na
<-t$
si
Bo
13*
132
172
142.
m
ao2
2.4-r
w
MO
2«2
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
t
NO
unc
cor
NO?
unc
cor
HC
unc
cor
REMARKS
•
AVERAGES
NOTE: Parts per million (ppm)_ figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A QAAA-Sffr 6
TEST NO /
/Y.9
/V.6
/Yff
/?*?
/v./
/^,T
I3A
11 A
(i,Z
H,fi
n.
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A/3/YlA-S'fr £
TEST NO % O
DATE
FUEL Kt>r,t,jt.ky-£.umb(>rla net
LOAD "7 P £?
2 - /ft ' ~7fi CONDITIONS
DATA TAKEN BY fl O P\
Probe
Position
Pfl'f
ft }-£
*/- 5*
*/-5"
*/- 5"
"7-5"
*l-S
"1- *•)
*/-5~
•7-S"
Time
/«/•'
2^^
25"
•
cor
77*^
P'J'V
33S
?7/
3/y
36'
3/3
3/2
302,
3^2
•
•
HOT LINE SAMPLES. PPM (WET)
NOx
unc
cor
,
NO
unc
cor
NO?
unc
cor
HC
unc
cor
REMARKS
'
AVERAGES -,
firt//C/>
6 #
12 '•I '•
/
vs/sfa
m#,
ma
^
^%^
%^
ywjffi/
«
31?
^^^
w///,
w///,
«
'///////.
*/////s
mz.
mt,
m&,
V//S%s
WW%/
^m
Wm>/
W///,
W///,
WM
NOTE: Parts per million (ppm) figures ara.SS!rected to 3%
159PQL.
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE ABMA-SiT y^.^
CONDITIONS AA^* C/!/^~/A,
DATA TAKEN BY cJ.°/^.
Probe
Posi tio
*!-$
*/- .5"
^/-f
*/-5"
A/_ 5"
*V - 5
*/ ~^T
•*/-5~
*"/-$"
fr/_5~
"Y-fT
Time
l(ri<
win
lO:3&
IO."ii
iO:5d
1/!00
l/'/Q
W10
//'"TO
12'VO
/;2,'/f
02
I
(dry
>7Y
L? /
6-ff
<,7
("7
0--7
7.o
COj
(dry
/?,
/a
/-2,^
/2,<-
/2,^
///6
/2.
J2-
5y
?r
NO
ppm(dry)
unc
2v;
210
11&
2.1$
WO
2}o
2
^^
"*?I^^C
*7 n s
•
.
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
,
NO
unc
cor
NO?
unc
cor
HC
unc
cor
'
REMARKS
•
AVFRAfTPS — ,
foo'iler
(O.G"
«
g^
M.
»
3V
'9^^'°'
m
w%
'///M
m
wa
w///,
•
•L
^^
Y//$//
W%
^k
vVyyVW
'///////.
WP,.
m.
NOTE: Parts per million (ppnO figures .are ^SUlJected to 3% O2
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE y4 P>A/\A"SiTf R
TEST NO "2J 2
DATE
5-- £O-7^
FUEL H<*Tfi'JsS
LOAD ~7 /, 8
CONDITIONS A/\ in H F A
DATA TAKEN BY (J. °. f~2>.
Probe
Position
'2-6
*2-£
'£-<£
'2-6
*!-<£
*2^&
MV /
'3.- £
*2-£
Time
/V'>
/?/fl
('V/^
#-;/}
/j;-%
/j"^5
/6''/
CO -
ppm(dry)
unc
f-(0
%o
£f
*)f
^5"
#T
$^f
13
107
cor
57?
b (
C*5/
Fd?.?
1/G]
ioi
too
113
m*
NO
ppm(dry)
unc
170
1?$
/ ^^C
j cr/**
ifZ
2.00
200
U0
liif
ic,f
cor
*//
2.^7
^7
/vy
^z^
2.1?
ffi
2oy
[•£>&
•
HOT LINE SAMPLES, PPH (WET)
NOx
unc
cor
\
NO
unc
cor
NO?
unc
cor
HC
unc
cor
REMARKS
•
AVERAGES
0&//V
C.*}
urn
^^
^
^
103
»
m.
»
'.
w%.
w&
%%>%'!•
//%%t>.
m%.
w%.
'mt.
w%.
mm
ym,
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE A&fi\A-5,re A
TEST NO ^2 3
DATE 2 - 2 2 ~
FUEL
LOAD
CONDITIONS
DATA TAXEN BY
'
fS
. f\< ;^j*,.T.'
Probe
Fosi tio
Time
02
I
(dry)
C02
I
(dry)
CO •
ppin(dry)
unc cor
NO
ppm ( dry )
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
mi£L$j*
l
-------
TEST SITE
TEST NO ^
DATE
3-2-73
KVB
GASEOUS EMISSIONS DATA
t P> FUEL Southeast
LOAD
. fl
CONDITIONS /\ s
DATA TAKEN BY
Probe
Position
Ti
02
«
(dry
COJ
«
(dry
CO-
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (WET)
NOx
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
i in
•
IS'
/i
/££
IVl
rr
r
£J.
i^i
1X
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
k<
LOAD
CONDITIONS
DATA TAKEN BY
n*
Probe
Position
Tim
02
t
(dry
C02
«
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
-C
6.0
v
rv
±1
Yo
11,°°
u.tf
_£_
sir
-fct
a
114.
ft?
3/P
log
HJL
yj_
70
j-U-
AVERAGES
NOTE: Parts per million (ppm) figures ar
acted to 3%
15900
-------
KVB
TEST SITE /3
TEST NO 2
DATE
GASEOUS EMISSIONS DATA
FUEL
JAY?*
LOAD_
CONDITIONS_
DATA TAKEN BY
T£c?Md
Probe
Position
Time
02
%
(dry
C02
%
(dry
CO •
ppm(dry)
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO •>
unc cor
HC
unc • cor
REMARKS
2*0
if ft!?
C,k a.,r
po
i't'i
2-t
13
7
l-2"/» S
73
> i U»c t
2-6,
r:0
I'i-o
2 JO
7?
f s.
77
^r
li". Jo
-220
V-V
AVERAGES
S,z,.
TJ
NOTE: Parts per million (ppm)_ figures are'
to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE Lf
TEST NO Q.
DATE
FUEL
-bcr kJS
LOAD
. V
3/9 / ?
CONDITIONS
. Art. — \A o/• i--wc./
DATA TAKEN BY
Probe
Position
Time
02
t
(dry
C02
(dry
CO •
ppm(dry)
NO
ppm(dry)^
unc cor
HOT LINE SAMPLES, PPM (WTT)
NOX
NO?
HC
REMARKS
2-4
13-0
YJ-
J/fc
2- -
/.
^ S3
iz.
AVERAGES
NOTE: Parts per million (ppm)_ figrures •are^^Drrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
3
2&
z /*?/??
FUEL
LOAD
CONDITIONS
/'"ft-,/, ScH.J^
("o f ^
"2/. „ <0/CA
DATA TAKEN BY Jb fe
Probe
Position
o-c
1-0
a -6
a-C
a-C.
i-C
*~c
T.-C.
L<
Time
/V.iyi
rt'.Gp
/i'/i
ci-<-
/£:to
02
%
(dry
tf
t-r
6Y
6t
(•t
t-i
(.V
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Positio
tji.t-t
'jf-C
/.W
'/. y-6
',V*
'
Time
//•
02
%
(dry
7^
7-^
6-)
£*
<^.c
C02
%
(dry)
/Z.^
/-irO
(1-7
I-*-?
\3--i
CO-
ppro(dry)
unc
-??
}*-
P-*7
^0
,?"
.cor
if
i*-
?*
3~t
if
NO
ppm(dry)
unc
7*>l
Ho
ioo
•£.
-------
KVB
TEST SITE_
TEST NO
DATE
GASEOUS EMISSIONS DATA
FUEL
50
LOAD_
CONDITIONS_
DATA TAKEN BY
•7*. 1
Probe
Position
Time
(dry
C02
%
(dry
CO-
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
>}:*>
C-/
ff
//'JO
£./
/i-9
/if-1
H- 10
C-2.
'Y-'ib
/"?•*
1. H-L
ft
c?
A7.50
C-l
ff
ng
>*•'(
VJ
so
/fo
U.f
1 <<-(-
IT-iO
fli
37
AVERAGES
10..
6"!
NOTE
: Parts per million (ppm) figures ar*joe»r
ected to 3%
15900
-------
TEST SITE 16
TEST NO 3/
DATE 2 I /
KVB
GASEOUS EMISSIONS DATA
FUEL
If
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Tim
02
(dry
C02
(dry
CO -
ppm(dry)
NO
ppm(dry)
HOT LINE SAMPLES. PPM (WET)
NOx
NO
NO-)
REMARKS
/, y
9-2
/r?
I.V-C
Ys
/V.-/T
'1 ' 2\
s, i
SO
i. V-6
/?. j
f. i
•> 1 1'
<&'£*
Z£_
NOTE: Parts per million (ppm) figures are
to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE /?
TEST NO
DATE
FUEL
LOAD
CONDITIONS_
DATA TAKEN BY
Probe
Position
I/S-C
Ijt-t
/,]-(,
2.
Ijl-l.
ij ?-6
i
/,?-£
•)i?-6
Tim
ff
IK
r*>f
K.3
CO-
ppm(dry)
unc
?6
£•*
«i?
,?i
3J~
JL3,
^-5'
33
^3.
cor
3?
S3
?i
JJ'
Jc.
^u;
P-9
26
l_f
NO
ppm(dry)
unc
'?.?
/f-o
A>v-
220
/?}
p_qr
A/»S~
/fo
XOS"
•
cor
2-0
J-^6
i'/C.
•ZV"?
20fr
2-V/
^rz>
^y
3-fl
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
*
NO
unc
cor
NO-)
unc
cor
HC
unc
cor
REMARKS
NOTE: Parts per million (ppm) figures are^TOPrected to 3%
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE ^
TES_T NO
DATE
LOAD_
CONDITIONS^
DATA TAKEN BY
Probe
Positio
Time
02
(dry)
C02
(dry)
CO •
ppm(dry)
NO
ppm(dry)
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO-)
unc cor
unc cor
REMARKS
L^c
11.
?r
/fo
13-00
Si
LLS_
Vo
6^L
Vi V-£
•/.'Vo
i&l
1 f-6
iS~:<9o
/2.C
3±.
?o.s-
32.
n-
l.^-f.
£.[
n£_
Y3
m
m%
NOl'E: Farts per million (ppm) figures are^WrTected to 3% 02
-------
SOx DATA SUMMARY
Test
No.
Load
02 (%)
SO2
(unc ppm)
SO3
(unc ppm)
SOx
(unc ppm)
sol
(corr ppm)
SO3
(corr ppm)
SOx
(corr ppm)
Test Description
1 a
/
385".
38^.3
0
port 7^3
82.- /
8.75*
fc/r.
c.
82. 1
9. /
. 6
avj.
370-3
. 8
, 0
35* /.O
. 8
o
. O
39-/.0
0
. 2.
386-2.
o
- kin
, B
. o
/A5-.0
o
out
. o
o
/AT.
. 0
o
out
j
o
. «t"
-------
SOx DATA SUMMARY
I Test
No.
Load
02 (%)
S02
(unc ppm)
(unc ppm)
SOx
(unc ppm)
S02
(corr ppm)
SO3
(corr ppm)
SOx
(corr ppm)
Test Description
6.1
_Z£_
4*1
576
6.1
37/
441
C..2.
84
322.
22^
127
472-
85-
za
C.
37
•8-1
-241
52
7.t
-£L
357.
7
277
31
5.4,
31 £
^5-7
3'F
/r
37Z
63
-------
SOX DATA SUMMARY
Test
No.
Load
02 (%)
SO2
(unc ppm)
(unc ppm)
SOx
(unc ppm)
(corr ppm)
SO3
(corr ppm)
SOx
(corr ppm)
Test Description
32 Q
35*7
2.8
Bo/
r
33
68
3?
383
H-
39V
8830-7
-------
Unit %
->
Pi:o:>? Location & Probe Length __ -f
FuelJL/J_^.&^ __________ . Load 7p /<
Description:
Test
No.
//v
/o
/-
Box
No.
z
J
1
Sample
Time
//.'If
M : u/ o
—
/2;oi
—
Meter
Tcmp.(l')
77
?2
sv
§>?
&4
f1
Meter
(/^Press.
- 0 —
C
<
j
Meter
Reading
0 ooo
y.oc^o
0.000
l.ooo
O . ooo
/.0<5«?
Press.
*»>/
i
Port
V
2
Purge
Time
//••J3L
/3ic?>
/a:ojr
/:?;.?_r
/^ • J r
• —
02
V.4-/
—
*w
— -
q. /
?. /
>1
m
Q
w
Test #
Test # I
Test #
Konr.ality N
Dilution
5P/^
l«M*k B
.'.versycs
Ml. of
Tit rant A
7-.vi5 rages
/ '^o + T
Vol . V
? !- p
A - B
SO2
,o*wr
/o
"7 °7 7 / •
f.o
S03
1
<-!.(,
^•L.
0 -
SOx
SO2
/O
T 9
g>. £
r. S"
V.i
J-Yd
c^ "7
SO3
/
V-c
ti. (e
O
SOx
SO2
/O
f?.o
7.7
JL-O
C.o
W3
2.o
SO3
/
y:^
Y< J"
'
^>
SOx
\
- — >
>
Q
H
H
EH
(A-1?) (N) (F) (/;6Ci-T)J24)
""""'
S02
)24
S02
S02
24
SO2 = ^—^p >,
.rt>° ^u.»l
)24
SO 3
- [77:3
S02 @ 3% 02 - JT2JL-J1_
SO3 @ 3% 02 =
SOx @ 3% 02 = "l?>3Zy,"
-------
SOX DATA SHEET
Local
Date
-£- 7?
Unit #
Probe
Fuel
»~ J*>J sT*r
~
Load
Test
No.
is*
is-e
IS'C
Box
No.
3
i
2.
Sample
Time
17 = 01
17: ll
17 :i3
17:37
17:17
IS: to
Meter
Temp. (7?
SV -F
SV
1o
12.
12.
12.
Meter
ft)Press.
o —
/
Meter
Reading
O.ooo
1 . 060
O. too
1. 000
o. aa, o
l.ofo
Press.
3*
,
>..,
Port
Purge
Time
17: 17
IT- 17
17:17
IS": i7
i
O2
v,/
v.*
v.'
V.o
J.t
Test f IS~A
Test # IS"8
Test #
Normality N
Dilution
Factor F
5r,t«.
Uaiyt B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + p
A - B
SO2
0.0100$
lo
9.1
S.3
ff.3
S.33
vTVV
I.G36
30.61
£.33
SO3
'O.aiotS
1
V.o
^^ ( " J lflr/) 24
(MO (*'0
S02 = \ 3S1 \
oUJ * | '*«
217
f
„...-, _ (»"/•) (.*'*) (/» ) (55T} 24
(W) (iMO
SO2 = ^g,^
?
„_- (»J5) (.«^1 ( / ) («i) 24
"""* (/^Virt (M4l
cn^ — 0» o
8830-6
-------
SOx DATA SHEET
Local
Date
Probe -Longth
Unit #
Fuel
Load
Test
No.
/TP
*e
is-?
Box
No.
/
Z
3
Sample
Time
11 '.60
It: 13
ft. 27
/? -• v/
11 -.H
I1-./3*
SOx
(A-B) (N) (F) (460+T) (24)
"°" V(P-fp)
y-* ,*A?
^_^ (^) (.w/r) ( '" ) (s)f ) 24
™ ^I^V^ ^- /./»
U/=*J (&•*')
SO o — 1 //V 1 SO3 — O / \
A*
(>•*) (."'* ( / ) (rr?)24
&UJ — /. ,A / \
&°
OQO (5.7^) (.*|e) (r*)(S-V7)24
(;/y) {»'")
S02 - f ns- \
\ "° 1
,** 1
o03 _ ("-'/) (."' ) ( / ) (-rV) 24
\ww \>°-fja
SO 3 — 1 ex* 6 J
218
__„ (2.-!3)(X('")(^7)24
7)24_
" //.-.» f-*aA
\I4>6I \}'ST>
SOS — ^?- o
R810-6
-------
Local /gy-/- g,/^
SOx DATA SHEET
nit f
/Y
Fuel
Probe Langth Lec-a-i,** : £3F*
lijad
Test
No.
UA
Ki
Kt
BOX
No.
2.
-
3
Sample
Time
/V.-*s~
n-s-s
is-.- of
lS-:i*
/S-.-&
is--.lt
Meter
Temp.Cr;
51/
ss-
8f-
SS~
?S~
8S-
Meter
^Press.
-.—
/
Meter
Reading
0.OOO
l.OZo
O.000
J.Goo
O.aoo
l.ooo
Press.
3.
*-
y
Port
*
i
•i
i
Purge
Time
tfto-L
JS-.-3L.
>S-:3Z
/t.-el.
O2
&f
f.z.
V.f
9.2-
9.3
Test # ///^
Test #
Test
Normality N
Dilution
Factor F
Split,
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + p
A- B
SO2
O.aioog .
10
v.z.
f.r
•f.l
V./J
j-v/
LOS"?
Jo.af-
VJ3
SOS
O.otoeg
I
t.o
V. o
J.*t
J.^7
t.t
'f.l
V.y
V,o7
j-^rr*
A«-J/
Itf.tfJ-
S-TJ-
f.»3/
3o.OS~
>r:vo
SO3 .
O,6 (4of
1
1.0
f.O
3.1
3.1?
f.T-
V.Z
s-fr'
1.034
30.0 f
0.&
SOx
S02
(A-B) (N) (F) (460+T) (24)
V(P-lp)
173, I S03
S03
(.6.1% ($) ( i
24
S02 =
SO2 =
SO3 =-
SO3
219
?
SO2 =
S02 = j ^z.
( to) (J*T24
S03
S03 =
24
8830-6
-------
Date
"> — 7-
Unit
SOx DATA SHEET
Probe Langth_
Fuel RJaaJ ^^ )e.*.) s^
Local
Load
Test
No.
MP
Hf
Uf
Box
No.
2
1
?
Sample
Time
16 : S-Q
17: 67
17. If
17:2>
I7:<,0
I7.-S-3
Meter
Temp.(T,)
?3
?J-
99
2?
ll
0.13
SOx
SO2
0,c/aof
la
1.°
ff.1
1.0
&.17
S~J~S~~
i.o J/
3 0,0 *-/
$.17
SO3 .,
0. o/6o£
1
f.o
V.a
3.1
•3.11
Lf.t
1.1
jrs-f
I.03J
36.01
O.tf
SOx
SO2
SO2 -
SO 9 =
(A-B)(N)(F)(460+T)(24)
V(P-tp)
S03
SO2
S02
S03 =—^
(ww)
; / ) (SiS) 24
S03 = I O.t \
S02
SO3 =
220
8830-6
-------
Frobe Location & Frobe Length
Unit 3
/*/
Load /^O
Description:
Test
No.
M
-? - /O
O-0°°
/. tfftf
(»Baro.
Press.
^.srs-
)
i
Port
/
/
/
Piu-ije
Time
/^.'^/
^/,Y
/^-«rs-
/; ^ s-
/-•2-C
/- i'?
f
02
(TV
6,0
6, (
6-z
.
G,2
m
Q
H
Test #
Tost
Test #
Normality N
Dilution
Factor F
Sf '<«
Averages
Ml . Ot
/ivc-rages
-560 + T
Sanple
Vol . V
P + p
A - B
S02
.0 0
5 Ox
•7
S02
.c3o^
/->
Ll.Cr
t-s'
tj.G
4-6
SVf
/.ojc.
2<<.fS-
/.02 @ 3% 02 = t^c\i
•;03 ;3 y-, 02 == £<-f
302 " ^ u^
SO2 - [ 3£^ g- "T
LJ£ 1
v7 ^ -?-'
^-•--Vj/r^;^--
SO3 = /f §*/i J
S02 @ 3% 02 = J / ^
SCx (9 J% 02 = i/Tr»
(^'S (' )(l°)(^7?24
^~" — / \/ \
SO2 '- 1 / C ^ 7 1
,V1 ^ ,
c03 = -(:._)J_-pJ_L )(S.7..)JA_
S03 = [ /^^^ 1
S02 @ 3% 02 = P-36
S03 @ 3% 02 =-- (C ^'L(
•}0x @ 3% 02 ---- l-eQv I
-------
'/-/? I
V, it if
e s t n. .^ c r i pt i on :
Loo-; i-.i on S Frobe T.c-iioth s ^ f C> o
Ti.st
Wo.
3°l>
SO ll
30 r
T1>ox
No.
Sample
Time
3-o-t
3 : /?
j. -^
J : ^o
3' ±~o
H:oS
Kcter
Tr-rr,p.('//
/(Dlo
/oG
/ol
/o?
|0 1
(07
•loter
fr) Press.
— O-
1
\
XX
!•;, rer
Rending
O- o o o
/. €>(."•>
f> 6 u ^
/. oo/
0. ooo
/.dV>0
Press.
1
/.
Port
Purge
Time
;'.'iO
H-oo
i.f_:^i.
Y- 31
V'jy
7
>H
m
§
Tost
Test
fir
Test If
T7oi::iality N
Dilution
F,;cl.or F
.Avc vaaes
M -i r f
'.vr-rr- gcs
/60 + T
Carnple
Vol . V
P + p
A - B
SO2
.00^
fO
O-^C ^
J,1? ^-^
/x?. ^'
/7.0
IU3-
n.6
m
l.o^
zW
7.C7
SO3
/
{ct^£
Si^itj^
/H-<*'
H.5-
/^.r
SOx
SO2
,007
/^
3±%__n t
•-
S".<2
^-4
^?
^^
/.*J6
*
-------
SOx DATA t7Hii>:T
Hate "^ I .(J? I .2— . ______ Probe Location & Probe Length
Unit!
Fuel
(f) 0^7 /
Load f £ Q
Test Description:
Test
No.
«.*
3(5
31-
Box
No.
,
a
3
Sample
Time
//: JO
// :«>
//: 50
/a '/•/
!?'.**
Meter
Temp .(T,)
/o/
/0«.r
(6l.r
/o-^
/«?x
/6^
Meter
6s) Press.
- 0-
(
Motei-
Reading
0.00C?
1 ,000
O- ooo
/ ^ ^ ^
c^' (J cyc^
/•GOO
'VV- »r'o "
Press.
?»./»
/
/
Port
Pxirye
Time
i(:s-o
/2^0
;0^
lo*^
02
^- /
? L
7.^-
m
Q
w
Test
Test #
Test #
Normality N
Dilution
Factor F
ti±a«* B
ai^^t •
Averages
Ml r^-p
7-iverages
460 +-T
Sample
Vol . V
P + p
A - B
S02
.o/(
/o
0*-_L
i". 6
r. •>
i*.")
5:7
r6/
.
/.O 3&
Jo. /-J -
S--7
SO 3
/
3.^H^
H-l
±4f
0.2.
SOx
S02
-°l(
/^
£>v»—t-
z^~
{..C
dT-J"
^"42.
^.JT
S03
^L
J.-P--C
[_£/••»"
y.j-
0.6
SOx
SO2
.0 II
(*
O *4—
S~.i
j-j
3'J
^"'
S-62.
^Tj
SO3
/
1.1 »Jl.
^.0
^r.O
//
SOx
- - . -=t
.. __ >
CQ
Q
H
EH
S02 = ----
~""
S02 - (Vl)
~ "
(24)
502 =
S03 =
( .)( )
S02 @ 3% 02 =
503 @ 3% 02 =
SCx @ 3% 02 -
SO2
502
S03 ^-~
^£_
|7o
-------
•i V
Unit #
Tost Description:
Tost
srx ::Y'\A :-::^'^T_
Probe Location & Frobe Length
Fuel /Sf '-/Vet- v ( o^,L,
f~3 r j~
Load
Q
W
J
§
Test
Test
Test #
Normality N
Dilution
Factor F
'c
Jo. 1 i
^."C
SO3
- —
21-3
3I.J
?(.3
SOx
SO2
.oil
0^~£
7. y
1. 7
7.7
7-6
7'~-L
6-3
6.?- f
(,, 3
£.P
4-i-8-
^.^r
SO3
p. 9
7.^-
7.3"
7.t
SOx-
n
w
r^
H
E-i
S02
(A-3HN) (F) (4501-T) i
V(rfp)
/-^C ^^\ ^f
-C3 -
% 0,2
% 02
S02 =
S03
( / )
.(1°
502 =
o% 02
3% 02
3% 02
S03 =
.SO2 i5 3% 02
S03 @ 3% 02
EOx @ 3% 02
-------
•a
~\\~a 3/3-iJ / 7 f Frobo Local'ion & Probe I.c-nuth "
Unit f /V
Tost Description:
".-Jft
Tost
No.
M
•?2g
33LC
Box
No.
;
^
z
Sainple
Time
I/HI
//:•/£> '
ll-fl
/i.oy
fr'.ty-
a:>r
Ke i.or
Teiiip.CT<)
/or
^of
/of
/of
/^
Sol
(fa
- (.
cter
CCS S .
'J —
Meter
Reading
a ooo
/. C 00
C' O<^0
/.<*>/
O. OQO
/. ooo
,).t
Prc
X?
(
^
.ro.
;GS .
7^
Port
Purge
Time
///n.
12.01
ll'.of
13 '• ^
/i •' 3?
/ ? . <---*.
02
^7
-Tj-
rV
en
Q
w
Test # Ji A-
Test #
Test #
Normality N
Dilution
Factor F
x- j ^^*
S("> «t — ^^
Blank B
Averages
Ml . or
Titrant A
Averages
460 + T
Sample
Vol . V
P + p
A - B
S02
&\/
(0
V- f *(
O>^c
~7.rt
^. ^
~7<0*
~ — -
—
W
SOx
S02
,0(1
( o
'J.^
l.f
•~7 ^
l.f
&1
1-1
S03
/
Ho S,f'te
?.'*-_
3
C- 1
a.?
6.lr
^
£-<*$
_
£.t
503
/
Ylfi, Cplkz
-tf-
//
SOx
^
n
w
E-"
H
EH
V(P+p)
302
)24_
7.3J
SQ3 = -
< Jf I
i.o* >.,.<<''
S02 @ 3% 02 -- J'J "X
;:03 3 ;a r;.o - -j V
SCx 3 3% 02 =
S02 =
S02 =
S03 =-(
(7?)
S02 @ 3% 02 - 7 J
^O3 «| 3% 02. --=
POx i? 3% 02 -
S02 =
(^)(,,irf
"ill
SOS =
SO2 @ 3% 02 •-= 3^S
SO3 (? 3% 02 = 7"-".'
-------
-T
-:te 3/,L/ /?/_
I' jit S_._1L_(_
Tost Description:
/ / AY /? rj Jsp
Probe Location & Prcbe T.i:-ngth _5 //'LI C
Fuel Soofii >?£-v> 1 Load /6
Test
:;o.
2^A-
Box
No.
/
.
Sample
Time
/*'. -?1-/
/-? -' V -a.
Keter
Tcir,p.(T,)
^?3
?3-
. -
'•Jeter
Oppress.
- o-
(
Meter
Roisding
O, c9oO
/. C7c?o
tx>i^ O^"""
_..
. . -.
(^)Baro.
Press .
-2^. i <*
/Kfk'- (
Port
Wi lu.t, -
•
Purge
Time
/2;vc-
/•/O
- -. . .
—
02
&'. /
. .
CQ
Q
Test
Test #
Test
Normality N
Dilution
Factor F
^P / ^c C
Blank B
Averages
Averages
460 + T
Sample
Vol . V
? + p
A - B
SO2
/oM
/o
O **u.
^r1?
7-o
7.0$'
l.o
sw
1,0 3(,
^.n,
7.G
SO3
y
14.0 **.
i-*
»?
SOx
SO2
S03
SOx
SO2
S03
SOx
(A-3) (N) (F)
^ .^. -~-~-
(24)
en?
S02 - - - -
1 ) J (O )
-- -
SO2 =
^03
S03 =
)24
"J
S02 =
SO3 -
SO 3 =
( ) ( ) ( ) ( )24_
( ) ( )
-------
SECTION 4,0
SPECIAL TESTS DATA
PAGE
4',1 MODIFIED SMOKE SPOT DATA SHEET 228
4','2 PARTICLE SIZE DISTRIBUTION - BRINK 230
- SASS 242
- BAKCO 262
227
-------
KVB
SMOKE SPOT DATA SHEET
TEST SITE
TEST NO.
NO. PUMPS
READING
PARTICULATES
lb/106BTU
COMBUSTIBLES
COMBUSTIBLES
lb/106BTU
3
8
V-V77
44
,6, To
4
//.
4
fa
\o
14
$17
it
n
7-21 4
/Z
IL
2
17
1.2-
n
11
Uz-g
ts
z.
15900
-------
KVB
SMOKE SPOT DATA SHEET
TEST SITE
TEST NO.
NO. PUMPS
READING
PARTICULATES
lb/106BTU
COMBUSTIBLES
COMBUSTIBLES
lb/106BTU
ft
£.$•3.8
2*
7.03S-
Zl
21
Sf.2.
22
S3. 3
23
to.'l
V 3
J
4 A
7.47*
xr. 7,5-y
^ 6
V7.0
7.2ft
7.288
27
2,2-
£.730
27
£.730
2*
7o.
7.0IS
7.0 //
15900
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
S~ LOAD %5~O ^To
g
//&/
/ /
X7fi
Out fcort
% o?
FUEL
.^^ SPECIAL
£*-£*>
Hn^-fie.
CONDITIONS
/J
/>owe-
Pp - Density of particles £j.-5~ g/cm3
y - Viscosity of flue gas £..5^/0 poise
Vm - Dry gas volume
SCF
Mn - Total particulate mass
MWs - Molecular wt. flue gas 2 *? . H- f g/g mole Cn "- Total concentration /.($£./
"~
AP - Pressure drop across impactor /3. £. in H2O I - Percent isokinetics #£.. 0 *
-L ~ L "*"
Ps - Absolute stack pressure £<) . / °) in. Hg Vs - Gas velocity /S,<5~£> ft/sec.
Ts - Absolute stack temperature 8^6 °R Dn - Nozzle diameter ^>, //^" in.
Qs - Actual flow rate at stack conditions Q. Ob 73 f t3/min
Stage Number
Dj - Jet Diameter, cm
Fj - Press, factor, n.d.
Ds,^ Stokes diameter, ym
Dj — Aerodynamic
diameter, ym
'-'Also Aerodynamic impac-
tion diameter, ym
Mn - Particulate mass, mgm
% - Percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grains/SCF
CYCLONE
£/8.<5-
8517^.
/^.28
AS-6J
A^T6/
i
0.2L*fQO
O.O2-IO
2.92.
^.7S
H-.0)^
2.1. ^f
8.^0
5:88
a/ 5-3
/. 7//
2
o.ms-
0.02.73
;.fe7
2.. 67
3.00
8-8
3.V4-
E.¥3
a 06 3
I-???
3
0./396
o. 03^5-
I.IO
/.86
£. 0^
3.7
J.H-&
0.98
0.026
/.S03
4
O.09¥6
O.O9O3
O.v53
O.^^f
1.1?
0.9
0-3^
O-63
O-O06
A 80^
5
O.O73/
0.32.77
O.<3f
0.^8
0.79
o.-f
a.it>
0. + T
O.003
/.BIZ.
FINAL
FILTER
J.2.
0.^7
o
a 009
/. 8^1
230
#15900
-------
KVB
BRINK CASCADE IMPACTOR DATA SHEET
TEST NO.
TEST SITE
TEST DATE / / & / "7 &
t -f
SAMPLE LOCATION Qlr~ Out"
LOAD
% 02
FUEL
SPECIAL CONDITIONS
GAS VELOCITY DETERMINATION
PITOT TUBE AP
GAS TEMP. °R, Ts & 9 Q
"
PITOT CORRECTION FACTOR, Cp f). fi 3 *7
BAROMETRIC PRESS in. Hg, Pbar
_GAS STATIC PRESS in. H2O — Q^
GAS STATIC PRESS in. Hg absyPs
MOLECULAR WT. FLUE GAS , MWS
ft/sec
. /
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn
NOZZLE AREA ft2, An
. Z./3 AC
An = 7T(Dn/24)2
Qn. = Vs An 60
Qc = Qs (PsMWs
^
O»
ft-Vmin at nozzle
ft3/min corrected to calibration conditions
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE
OPERATING VACUUM (corrected for static pressure of duct)
ISOKINETICS DETERMINATION
INITIAL
FINAL
A
SAMPLE
TIME (6)
o
7^
72.
METER
READING (Vm)
O. OO<5
2.^3^
^.3/9*
METER
TEMP (Tm)
96
96
—
%H2O =
1.667 Ts Vm
-factor-
^.036
231
in. H20
6 Tm Vs Ps And
#15900
-------
KVB
BRINK CASCADE IMPACTOR LAB WORKSHEET
TEST No. .V R
TEST DATE / / 's / 7 &
LOCATION ^^"t-G. fi b/r O£/ZT AOrT. ^
ENGINEER
TEST DESCRIPTION
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
DATE WT.
TARE WT.
1
2
3
4
AVERAGE
CYCLONE
O-3933
0.3933
i
3.*/*<)
3.W3I
3.V/3/
3.^/30
2
3.^m
3,2.7/<$
3^7/e
^3.^7/a
3
3.^81
3.^80
3,V«?t5/
3.^981
4
3. ^^6
3-^Vfc
o.^y?
a.^v^
5
3.30/7
3.30/fi
e-30y«
3.3d>/&
FINAL
FILTER
0.0W
ao-^^
0-0^^
a 0^7
POST TEST WEIGHTS (GRAMS)
DATE WT.
GROSS WT.
3.3022.
AVERAGE
0.6//&
NET TEST RESULTS (MILLIGRAMS)
NET WT.
PERCENT
TOTAL NET
0.2.I&5T
8
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
a
LOAD
% 02
FUEL
SPECIAL CONDITIONS
Pp - Density of particles j
V - Viscosity of flue gas t
MWs - Molecular wt, flue gas
9/cm3
Vm - Dry gas volume
I SCF
AP - Pressure drop across impactor £
Ps - Absolute stack pressure
Ts - Absolute stack temperature lOQO °R
Qs - Actual flow rate at stack conditions
Mn - Total particulate mass
g/g mole Cn -- Total concentration 0.^^*3
in. H^O I - Percent isokinetics <^,S^
in. Hg Vs - Gas velocity "V,2..£L3 ft/sec.
~ Dn - Nozzle diameter P.P^fc. in.
ft^/min
Stage Number
Dj - Jet Diameter, cm
Fj -Press, factor, n.d.
Ds/5 Stokes diameter, ym
D» ^ Aerodynamic
diameter, ym
DAIs> Aerodynamic impac-
tion diameter, ym
Mn - Particulate mass, mgm
%-Percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grain^SCF!
CYCLONE
. 86
0-/-T7
O.O2.IO
/AO
X9.93
a. 02.73
A
>,3 OB
J.O7
X5I03
0.0905
0.9Z.
A/ 8
3.<5~
(D.02.7
FINAL
FILTER
2L.7
o
(9-OA.I
#15900
-------
KVB
BRINK CASCADE IMPACTOR DATA SHEET
TEST NO. ^.y
TEST SITE Q
TEST DATE •3/2-//'6
LOAD /GO 9/^G
% O? v^~ °^^>
FUEL vSS%^ L,
SAMPLE LOCATION Mil ltteLt>H<2-,
SPECIAL CONDITIONS
GAS VELOCITY DETERMINATION
PITOT TUBE AP
GAS TEMP. "R, Ts
PITOT CORRECTION FACTOR, Cp
Vs
85.48CP
BAROMETRIC PRESS in. Hg, Pbar ^ 9>
_GAS STATIC PRESS in. H2O ~v5"l
GAS STATIC PRESS in. Hg absyPs
MOLECULAR WT. FLUE GAS , MWS
MWs
ft/sec
. $ 7
9-
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn
NOZZLE AREA ft2. An /
An = TT(Dn/24)2
Qn = Vs An 60
QC = QS (PsMWS)
1.3Ts'
ft3/min at nozzle
ftvmin corrected to calibration conditions
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE
OPERATING VACUUM (corrected for static pressure of duct)
ISOKINETICS DETERMINATION
in. H_O
-b in. HO
INITIAL
FINAL
A
SAMPLE
TIME (6)
/*:
234 •-
#15900
-------
TEST No.
TEST DATE
2. ~ 2. -
KVB
BRINK CASCADE IMPACTOR LAB WORKSHEET
LOCATION_
ENGINEER
TEST DESCRIPTION
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
CYCLONE
FINAL
FILTER
DATE WT.
2-4-7*
2.-Z-78
TARE WT.
3 . 2J/2.
^
3.
AVERAGE
3.
POST TEST WEIGHTS '(GRAMS)
DATE WT.
3-4-78
-4- 7S
3-4-73
GROSS WT.
3,
3.
3.
3
AVERAGE
-3.^673
3-3031
NET TEST RESULTS (WHUBBGRAMS)
NET WT.
00 £1
,00^7
PERCENT
TOTAL NET WEIGHT
S ^ *
FIGURE
TM S15900-511
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
S
3-3-78
rtetL**,cJ O*H*.f
LOAD
FUEL
SPECIAL CONDITIONS
Pp - Density of particles
y - Viscosity of flue gas
MWs - Molecular wt. flue gas
g/cm3
poise
Vm - Dry gas volume
SCF
Mn - Total particulate mass
g/g mole Cn - Total concentration
AP - Pressure drop across impactor jg.Zf inH^O I - Percent isokinetics \
Ps - Absolute stack pressure tajdEf? in. Hg Vs - Gas velocity ft/sec.
Ts - Absolute stack temperature 1ft? °R Dn - Nozzle diameter in.
Qs - Actual flow rate at stack conditions .O7fT\ ft3/min
mgm
grains
SCF
Stage Number
Dj - Jet Diameter, cm
Fj - Press, factor, n.d.
Ds,j- Stokes diameter, ym
T Aerodynamic
diameter, ym
Aerodynamic impac-
tion diameter, ym
rfn - Particulate mass, mgm
% - Percent of Total
Cumulativepercent
Cn - Concentration, "^
grains/SCF
Cumulative concen-
tration, grains'SCF
CYCLONE
It. 3
36.1
£3.S
1
o.aVfo
0.0 11 0
2.78
V..JV
•f-ff
7.1
3.0.1
13.S-
2
0. )7?f
0.07.73
i.s-?
2.SV
2.K
1.?
3.S-.Z.
If. 3
3
0./3?/
0.031J-
J.03
l*7£
2.03
3.V
y-7
5.7
4
o.ollt
o.otoZ
o.'ff
0.8V
A/3
2.<
t.t
3.1
5
0.0731
0.33.77
0.2.7
o.s-z
0.7£r
1.2
3.1
o.o
FINAL
FILTER
O.O
0.6
__
236
#15900
-------
SAMPLE LOCATION
KVB
BRINK CASCADE IMPAGTOR DATA SHEET
TEST NO. £lv^)
TEST SITE JB
TEST DATE ^2> / 3 / "7<^
LOAD
% 02
^> FUEL
SPECIAL CONDITIONS
PITOT TUBE AP
GAS VELOCITY DETERMINATION
GAS TEMP. °R, Ts
PITOT CORRECTION FACTOR, Cp
BAROMETRIC PRESS in. Hg , Pbar £. ^. -fy-
_GAS STATIC PRESS in. H2O — \5~» "7
GAS STATIC PRESS in. Hg absyPs
MOLECULAR WT. FLUE GAS , MWS
ft/sec
- O
<3 -
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn
NOZZLE AREA ft2, An
O.
Qn = Vs An 60
Qc = Qs (PsMWs
l
„ Q
10
An = ir(Dn/24)2
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE /& .
ft3/min at nozzle
in corrected to calibration conditions
in- H2°
OPERATING VACUUM (corrected for static pressure of duct) £.3 - ^v5 in- H2°
ISOKINETICS DETERMINATION
INITIAL
FINAL
A
SAMPLE
TIME (6)
•39 A7//1
2>& ^ee.
METER
READING (Vm)
O-OOO
/l
B°>
^sro "ft
%H20 =
= 1-667 Ts Vm Pbar
6 Tm Vs Ps An
237
#15900
-------
KVB
BRINK CASCADE IMPACTOR LAB WORKSHEET
TEST No. ? fa
1 /
TEST DATE ^ /<^ /*7&>
LOCATION \5 f u^L. L^> *^ />ie.c_/1 o/^T
ENGINEER
TEST DESCRIPTION
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
DATE WT.
TARE WT.
1
2
3
4
AVERAGE
CYCLONE
3/sfie
.367^
i
i^y ^Li / ^? *^
^O • /"/ *-J ^~
5.^/t3/
3-^/3/
2
s, 2.7(^9
z.ttfo
3^7^
3
3-^976
S-^^7S
3.^975
4
3,y^£
6-^f^-
3.Y6^
5
3.3C*/
3.?>o^
3,302.1
FINAL
FILTER
.(^37^
^0376
.0^7vT
POST TEST WEIGHTS (GRAMS)
DATE WT.
GROSS WT.
3.28/5-
.0387
AVERAGE
NET TEST RESULTS (MILLIGRAMS)
NET WT.
PERCENT
^9. -7
^5^, g
&.V
/^ 0
/a ^5-
/^7
V.O
7-f
/.£
^. 8
^>. 9
/. 6
/^-
2.-/
TOTAL NET WEIGHT
mgm
238
#15900
-------
TEST NO.
TEST SITE
TEST DATE
SAMPLE LOCATION
R
KVB
BRINK CASCADE IMPACTOR DATA REDUCTION
LOAD -
% °2
FUEL
SPECIAL CONDITIONS
Pp - Density of particles_
y - Viscosity of flue gas
MWs - Molecular wt. flue
g/cm3
poise
g/g mole
Vm - Dry gas volume
SCF
Mn - Total particulate mass
Cn '- Total concentration
mgm
AP - Pressure drop across impactor/<9^x5^i^ H2O I - Percent isokinetics i
Ps - Absolute stack pressure £.°)* W7 in. Hg Vs - Gas velocity ft/sec.
Ts - Absolute stack temperature ^ gQ °R Dn - Nozzle diameter in.
Qs - Actual flow rate at stack conditions g), Q^f, *7 f tVmin
Stage Number
Dj - Jet Diameter , cm
F j - Press, factor , n.d.
Ds/io stokes diameter, ym
diameter, ym
» Aerodynamic impac-
tion diameter, ym
Mn - Particulate mass, mgm
% - Percent of Total
Cumulative percent
Cn - Concentration,
grains/SCF
Cumulative concen-
tration, grains/SCF
CYCLONE
0.
S.D&.
0.761
FINAL
FILTER
239
#15900
-------
KVB
BRINK CASCADE IMPACTOR DATA SHEET
TEST NO.
TEST SITE
TEST DATE
,3 AT fo&
LOAD
% O2
FUEL
SAMPLE LOCATION
SPECIAL CONDITIONS
GAS VELOCITY DETERMINATION
PITOT TUBE AP
o
GAS TEMP. °R, Ts
PITOT CORRECTION FACTOR, Cp (Qx gfcgS)
Vs = 85.48CP
BAROMETRIC PRESS in. Hg,
_GAS STATIC PRESS in. H2O
GAS STATIC PRESS in. Hg abs^Ps — ,£.
MOLECULAR WT. FLUE GAS , MWS £-*-*>-
ft/sec
"{L
IMPACTOR FLOW RATE DETERMINATION
NOZZLE DIAMETER inches, Dn
NOZZLE AREA ft*, An
Qn = Vs An 60
3 - C>fe
X / O
An = TT(Dn/24) 2
ft3/min at nozzle
ft3/min corrected to calibration conditions
PRESSURE DROP ACROSS IMPACTOR FROM CALIBRATION CURVE
in. H20
OPERATING VACUUM (corrected for static pressure of duct) xL*
ISOKINETICS DETERMINATION
in. HO
INITIAL
FINAL
A
SAMPLE
TIME (6)
/
-------
KVB
BRINK CASCADE IMPACTOR LAB WORKSHEET
TEST No. £.^>
TEST DATE 3 / ^> / *? A
LOCATION
ENGINEER
TEST DESCRIPTION
PRE TEST WEIGHTS (GRAMS)
PLATE NO.
CYCLONE
FINAL
FILTER
DATE WT.
TARE WT.
3^0/6
AVERAGE
POST TEST WEIGHTS (GRAMS)
DATE WT.
GROSS WT.
338%
3JOZ&,
AVERAGE
'3*702.'?
3,90^9
NET TEST RESULTS (MILLIGRAMS)
NET WT.
PERCENT
'0/K3
.oon
*oow
.ot>*y
-OOZ&
.ovrz.
,0000
TOTAL NET WEIGHT
mqm
241
#15900
-------
PARTICULATE LAB WORKSHEET
TEST NO. ;>/r-~ ""• (Inlet, Outlet)
Date /-//~7# Box No.
LOCATION_
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
'l
2
3
4
AVG.
H2O RINSE
^fc'^tW
II
/-/3-7B
/#. 6* 4 £/
/G.4/43
/&.6S43
/ ^^ f / s J ^c
/ C' * tf7 * i ^y
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
?/«/ »
ij?acc ».-j / i? ^—
A Vic
DRY
FLASK
cJsJfiiJL
CRucreLt
/- 13- 78
3. 3724
3. <}7Z3
3. £77Z±~
•
3 97^
FILTER
NO.
-
/, z^-?6
1 2*rt1
- —
— -
^_
/. ZS") $
BLANK
NO.
POST TEST WTS.
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
2.1. S27/
Z-/. 52.72,
2,1-32.7^
.
2-/.^7^
Z,7/2^
/f . 5tf 7/
/1.S-C73
/ tf *\~~l> "7^
—
/ ^ ^T^ *7 ^
1,05^10
4. 44/6
4 -44' 7
V- yy/7
—
/7€^V/7
4M5
/v 4?,~2,£,
) . *-}2.Z.&
/ sj —i ?•'?
/• rf ZU /
/. -V^Z7
./*&
\
/ P^f
J '
\
J
'
= ml LOAD klb/hr
ft3 0? %
mgm REMARKS :
1l°~C ..
^M*
242
8830-5 rev.
-------
TEST NO. /- //- 7ff (Inlet, Outlet)
Date Box No.
PARTICULATE LAB WORKSHEET
LOCATION^
Eng.
Test Description
Dry Gas Meter Vol (ft 3)
Final _
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1 •
2
3
Total
CONTENT
ACETOME
•"DRY"
FILTER
NOr
BLAWK
•we-.
BOTTLE NO.
BEAKER NO.
/7
DATE WT.
S-/3-78
/-/S-78
TARE WT.
, 6311
• AVG.
POST TEST WTS.
63.6619
41.8281
AVG. .
^4.£5^7
A WT.
A Vic
A DgV
A Mn
ml
LOAD_
0,
mgm
REMARKS:
£43
8830-5 rev.
-------
RATION -^^^^•^••-£-.
TEST NUMBER
DATE
*^» Paoe ..
/-ft- 78
nppp^Tvip, "^A.A AMBIENT TEMPERATURE, «F
Laak Check Rate
Vao
Before fl£ f 7(7!>T~^ \^? j i , ^
v ./V.-1
1 11 21
Sampling Time
Per Point, Hin.
1 11
ample
oint
? //,d
•Z^J.P
,
1 '
•
Time
r , *
Average
Particulate
. Wt . , • mg
"
Nomograph Setup
meter" a •
P 1 •* ~
tack Press.
[n.Hg-Gauge
Barometric :
Pressure '
i
TEST RESULTS
'est Averages!
^H =
• . Tmeter " F
51 61. Sample Vol." Ft"
TEI1PERATURES, °F
Stack
:5YST
&\t>
.
Probe
3&3
*& &f t
"2 tS f J*
. '
1S~> b
Ovei
i
^H
'33 *i
q *) "i
•z
W'
Impingers
In
1 -
Out
•
•
•
•
Meter
*7?-\7*t
3i>
i
*
7X
tit
-
..
oa,%
Vac.
7. 2-
t0i2-
Percent 0, - _____
""stack gas ' l~28
Velocity, " ft*ee
Total Sample
Time » min.
ISOKINETICS - %
. Particulate Emissions
6
COMMENTS «
15900
-------
PARTICIPATE LAB WORKSHEET
TEST. NO.
Date
(Inlet, Outlet)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
- AVG.
2%£l££*-
1
3 b&&tj
3.&#o3
S (? &o -3
3. t$°3
Final
Initial
A Vic
""jSSf/
wuarae*^
3.ti$l
3. U>*l
B. U&I
—
3 i>y&\
i
-ess-
j r^MSK. /
J M e^( Wui
WcrBLe* ^
3.7/£"-J
3. 710-5
3.7/°?-
-.
3 1\o3
2
FILTER
NO.
.•'
f.
-------
PARTI CU1ATE LAB WORKSHEET
TEST NO._
Date
(Inlet, Outlet)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final _
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
DATE WT.
/-/ I
AVG.
1 7*30
A WT.
,001*1
A Vic =
A DgV =
A Mn
ml
LOAD
mgm
REMARKS:
8830-5 rev.
-------
r
^^»oLii.
y
Befo
Afte
Sw1
W'7
PERAT
CMS
Leak Check Rate /,
Vao , jtf"
in.Hg ft3/mirfr>
re fe'xTF
r IAJ VjXfl / ')•'
1 .AM
Sampling TUirie
Per Point, Hin.
1 11
Sample
Point
/0 '
/X**
.
1 '
5 '
Time
. ••
Average
t- ^ 21
Particulate
Wt. , -mg
(C.»/"«5M.
FUI
i
"Ii ii..
i
T
meter-
* HO -
No^raph
S/ !to*-*r««i
TEST NUMBER
DATE
~7 Paq* g _
AMBZEHT TEMPERATURE, «F
Sptun
C . •
T«tack"
AP
Noz(
Nozt
T
METER VOL. (START/END) .
.Imp.
J2 .
'"13
//^.V7/
Vol. (End) 'Vol. (Start) Avol.(ml) Filter!)
- _ _
_ • _ . Particulate Wtt
. — - ' rs • • • • Filter ' ms
" ' ' Total ; ._'_
Ideal)-
^ctu&U *
It"'"* g(End) . g (Start)
(Sili
Gel)
A grams •
ca ^ . __ Total mg
Total Vol. H?0 . ml
31 41 51 61 71
Condensate
Vol., ml
21 ' 31
Fuel Flow
gal/hr
41
METER CONDITIONS
A Ps
• f^
••
AH
3. "7
Meter Reading
j3&* 7o
/*/*?• £>y
•
.
•
} . '
(
Load
MW
. 1
*
Cpitot S
'. i
tack Press.
Cn.Hg-Gauge
Barometric
Pressure
i
TEST RESULTS
Pest Averages!
^H a
51 61. Sample
TEliPEHATORES, "F
Stack
£~2£~
.
-
Probe
ggg"
•
. ' ' .
Oven
^fffZ
Impingers
In
•
•
p
!
t ••
Out
•
*
'
•
.
Meter
75"
,
ffft
i
V*
Vac.
fe ^
, ^. Tmeter'" ^."F
Vol.- 1 Ft*
Percent. 0, - ^^^____
Velocity; - fbfeee
Total Sample
• Time " min.
ISOKINETICS - \
Particulate Emissions
COMMENTS t
15900
-------
OK/ S
TVt
a
T-
i \ -r> \ •
c\a -I••?> v-V \c. r\"V'. oT
Uje.\c
-------
f
"Or-fW
c.c.
. \ .p) \ •
J A e_v\i \-V\c. rx V i o v
,'J
* U>as,C.,.,.._....-
4^±uj
II M ,— / -^
"-S*. .-
c rf-
r©
0.
tf'
A 0/0 #9
.J&J?d>aniLCfiJ?,..ll&39/a
t 10.
""
-.-
3
.CMI
-Pi Hers
C I oA l^
249
0
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, Outlet)
Box No.
Test Description
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
/£, ~/£>M
—
S - V- 76
^/. tf'ZJ* ~7
^/- ^f~2 ob
r
*-/. *jt~2e(z
123 Total
Final
Initial
ACETONE
RINSE
"2s- .5^
^5 / / (5
4.1 60 ^
*/.
BLANK
NO.
POST TEST WTS.
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
12.. 733^
f2-733/hr
ft3 0? %
mgm REMARKS :
250
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
Test Description
(Inlet, Outlet)
Box No.
1_2
LOCATION^
Eng.
Dry Gas Meter Vol (ft3)
Final _
Initial '
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
#7
DATE WT.
3-6 - 70
TARE WT.
44. 641 s
AVG.
. 6413.
POST TEST WTS.
AVG.
A WT.
-------
(.1.4.
J7l * o x_
.2-8. .
LOG AT I
UNIT -
0
PERAT
Hi
np<;
Leak Check Rate
Vac
in. Hg ft3/min
Before _^
1 f> 6>'Z-'
After , L &&
1 11 21
Sampling Time
Per Point, Min.
1 11
Sample
Point
^.3^1*
yft
2fS>/vti"1'
• •
•
'ime
• ••
Average
Particulate
Wt. , 'mg
'
:
FU1
~ti
TI-'
Nomograph Setup
P
meter- C -
P T -
stack- stack
T • A P •
meter- ,
. „ Nozlldeal)-
Noz (Actual)-
*H2°- :T -r .
TEST NUI-EER
DATE
AMBIENT TEMPERATURE, °F
hETER VOL. (START/END)
Imp.
01
Vol. (End) 'Vol.
—
—
— ..
2^r "5^ i^f] Paqe
n f
Hft+'iW /
(Start) AVol.(ml) Filterlt
,
—
Particulate Wtt
=S • • '• • . • •-• Filter mg
Total .: . _„.
#4 g (End) g (Start)
Gel)
31 41 51
Condensate
Vol., ml
21 ' 31
Fuel Flow
gal/hr'
41
METER CONDITIONS
APS
C7' 1_
'
^ /
/ r-f
AH
//'
- 77
^^ ./ C
Meter Reading
/7?,X
SL,12>^5^
^ ^ •
\g(y\<\
( % .
-f^c
_^
•
^ /- /
«. • '
^6
Cpit
ca __
. • Total
61 71
ot S
tack Press.
Cn.Hg-Gauge
Vol.
Barometric
Pressure
•z?.?7
51 61 ;
TEMPERATURES ; °F
Stack
*H0
SSD
•"e>~?]/ /,
.# *n (
~*
.
Probe
tf-a®
..
• '•' '\ j
2GC7 U
Oven
UD^-
2- f ^( "?
0~3)CbMi
•'
?ers
Out
•
•
'•%«}
(us#&T
/TV
.
,
%7
\
I
A grams .
. — . Total m9
H?0 . ml
TEST RESULTS
Test Averages:
Ap= ™ T^ •.,«!, = *F
/
\ H °
Sample
oa,%
Vac.
Tmpt-p^1- . °F
Percent 0- - .
Velocity - ft^feee
Total Sample
• Time «• min.
ISOKINETICS - _\
Particulate Emissions
ihs/in BTU
COMMENTS :
15900
*
-------
PARTICULATE LAB WORKSHEET
TEST NO. 2iS~.
Date 3-^
(Inlet, Outlet)
Box No.
LOCATION
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
4$-/OS4
3-^-76
4.1 st~?
<4. -ftr/7
.
—
^f5~/7
Final
Initial
A Vic
ACETONE
RINSE
5^— ^^
S-4--72
4. 9 2f> 4
<4. ?Z* $
tf.q-Zeb
i
DRY
FLASK
6$ — /si
3-4-
78
4, 143&
^ 7
Total
BLANK
NO.
^_
POST TEST WTS.
1^±
AVG.
-7.
A WT.
A Vic
A DgV
A Mn
ml
LOAD_
°2_
klb/hr
mgm
REMARKS:
253
8830-5 re-<
-------
PARTICULATE LAB WORKSHEET
TEST NO. 2£~ (Inlet, Outlet)
Date 3-3-78 Box No.
LOG ATI ON
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
*
1
2
1
3
4
AVG.
H2O RINSE
/4u i*J/te>t+
&-*,
3- 4- 78
63. #o-?g~
£-73
6J- &? -72.
. .
/?. 0T?~)3
Final
Initial
A Vic
ACETONE
RINSE
"3^ WA6H-
84
3-^-y€
£<9.st?*
6/6
•
^^.£%/S
i
2
3
DRY
FLASK
f'JJ /J f -^^ /&-
f yvf C^V^T^ r T
X'
^2
•T7 ^ — 7tf?
»^ fr? / &
&V.2-3-76
53.25
?7f
3^,Zf77
^ra-2/hr
mgm
REMARKS:
254
8830-5 rev.
-------
Jx^
IkfirJ
Si
V - 1
• L
U
0
DCATI
HIT -
PERATi
ORS ^
/>«/
\<~ !•.<* ,-,
r? S"
T2U
'ft^lc :
Leak Check Rate
Vac ;
in. Hg ftVmin
Before ^.U ~ . GSfS
After
^~ *l / f J T ..
v -fr.t \> -9 J, O
1 11
Sampling Time
Per Point, Min.
1 11
ample
Point
1 ~
•
" f
•
•
Time
&M44
le?"-
•p
2-O
_. ,07
1-O
2>^
^7 -
Y. / '
Average
21
Particulate
Wt. , -mg
21
'•^/D
" i**'
FUI
•T -/Scfr-tWcJ
~>.
*°>r ,Crfv*Av
Nomograph Setup
meter™ C , •
P ' T "
stack" stack
^
T . • AP
meter- ,
AH.- Noz (Ideal)-
: ' Noz (Actual) -
2 T "
rU.
TEST NUMBER
JjfcTE
AMBIENT TEMPERATURE, *I
METER VOL, (START/END)
Imp
til
^5 7^^CiJKV-4 Page _
, . ., nf
•»
i3*-?ej^M. r>7
Vol. (End) 'Vol. (§RSt>— £jvol.(ml) Filter*
••• .•• TTo^
j|2 — ; _ Particulate Wti
•#3
— .. » — .
Total -.. : .;;_..
(Si
Ge
31 41 51
Condensate
Vol., ml
' 31
Fuel Flpw
gal/hr
41
METER CONDITIONS
A PS
^
(I, I
'( y^i,
~
If
AH
){?7
^^? jj
(
r p
^j
^?
Meter Reading
^i-JLf ^~cs>
'^^iSV.'C
0-7,3^5-
3-xp1' *-/
^ffi^ . S"
3O^ 'S'
t>l$ >S~2?
\ '*
t>li. €-if \(( &
. 6 >• 10-3^1^
— >
Load
: MW
; .
Cpitot
li<
1)
g(End) g (Start)
A grams . , . .
:a _ p . = . Total _•_
. ! total Vol. H50 . ' ml
61 71
S
]
TEliPERATURES ,
Stack •
S^CTP
VWc?
^-//o
sf/c?
^? C"~
[T4^
5^^
•\
oo yd
/^•yfe"
Probe
^ %^y
3*7/
"?'2-
H&.'i-
uc>l
*/oa.
£{&t
yj-'f- ^
tack Press.
[n.Hg-Gauge
2*/.JM.
Barometric
Pressure
TEST RESULTS
me,
«9
!"S
rest Averages:
^Ps = T.^ u " *F
\H a
v; ]± Tmeter " _
51 61. Sample Vol.- (^ (j
Vac.
* *
'
Percent 0_ »
• 2 . ^-~
"Wstack gas "
Velocity -
Total Sample
• Time "
ISOKINETICS -
•Particulate Emi
iv
COMMENTS:
*F
Ft3
••••V
(-28 ;
ftyfeee
min.
%
ssiohs
s/10 BTU
15900
-% .,.x ' ^ (¥5*
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, Outlet)
Box No.
Test Description_
LOG ATI ON
Eng.
£>
Dry Gas Meter Vol (ft3)
Impinger Water Vol (ml)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
/4# 45 //
7*
—
*r. 0zr//
jsr. c^i/
S~.es-f/
,
123 Total
Final
Initial
ACETONE
RINSE
34t-C^6*
$£>'
-5"7 ot-/&&
g~; cx^gj
- —
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet, Outlet)
Box No.
LOCATION
Eng.
B-
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.
H2O RINSE
WM - At4£/*
73
«•"> /" -~9/2
__^ ~~'C? """ f ^
t>3. sz-zs
63-5523
^3. 35*22
'
/ "2 £*~^^f*?2.
f? ^ ' *—'*—' 4*^
Impinger Water Vol (ml)
1 2 3 Total
Final
Initial
ACETONE
RINSE
^Ai-fo^S'tJ'
*3£j
3-£-7&
£7. 03?6
£7.£3?6
£7. esjt?
- '
t7. $37^
A Vic
"
DRY
FLASK
//t1—U.>j&S>ri
3.£7£z
i /2-J3 /
£3.0706
68 07/3
;'>6>.c7/6
'
£tf, °7/Z
,-Z3lt>
£
-------
KVB, INC, TRACE SPECIL AND ORGANICS SAMPLING DATA
C,' O I
Project:
Date: /
Location
Unit: I
Personnel: J"£C.
\«.r. s- V 14 7 ? ,
/
Barometric Press :
M Probe Nozzle Diameter (inches) :
Test: ^~ f-^
Fuel: . T~[ uTT(-~e\ O C
VW-W
Traverse
Point
Depth
\Ku
'
J
t
?>
f . #"7
(Dn)
Absolute Static Press, in Stack (in. Hg) :
Pitot Tube Coefficient: . *&
Pitot
AP
(in H20)
,/7
\
\
|
^o^
-^ 1
|.^7'
Orifice
AP
(in H20)
,/
2.1
(/>**
(t.y*
Cum.
Meter
Volume
(ft3)
*&&*
3 jo < o
"Z£/5 c —
33^,5-
;^S
^0^.3^]
7)(t-*>'n
,!
?.«•?)
9 v/ 73C?\,* S
Probe
3^1
5*?Y
?^^
i
^oo
6/OC>
CfOO
— _
)^-/4?
(Ps)
(Cp)
T U R E
XAD-2
\
)
('
\
\
/
/
(
\
i
( ° F )
Impinger
Out
(
N
/
/
\
\
/
/
(
\
^
Oven
LfO A
4^O 2
vo;*
L(Cr2-
£fo2^
1/C52,
y0^
Meter
In/Out
/o,
A*>
/^
73
//G
//^
(2(
(^ ' c
lo~
/O;
Av
roy
/qr
^d?
7>
Cone.
% dry
1
1
1
-------
CD
//A
. -3 #4 ZL
. 3843
23-
"73.
67.
. 7V7/
73.
67 <
- /&t.03t>8
- $4. Ml
3./7<>3
&-
i-Z6
-------
*- 1
. 36/7
,4^ ~ £
.2*2.
62 .ff 771
62.
62-
7/32
A 3S-70
B
93. 6 6 /£"
'-3/i
27,
»t*,
IV -
»
-------
- Akresr
23.2336
&33C]
233*1
23
<4n/- ^/s: 66g-y
£0 3/A0ycl
-------
KVB Company
ES-0596
5364-01
July 31, 1978
Sample No.
Sample Description
K-22483
Fly Ash
Site B
Test 4
K-22484
Fly Ash
Site B
Test 23
K-22485
Fly Ash
Site B
Test 24
Bahco Particle
Size Determination
% Through #100
(149 Microns)
Results: Terminal
Velocity
112.
79.0
31.0
12.3
4.15
0.96
0.35
Density, gms/cc (On #100
Mesh Material Only)
Screen Sizing
% Through #10
#16
#30
#50
#100
#200
#3?5
51.8
Diameter
(Microns)
27.
22.
14.
8.8
5.1
2.5
1.5
27.3
% Smaller
29.5
26.0
17.9
10.3
5.7
2.6
0.9
2.20
99.9
98.5
86.7
69.0
51.8
32.8
29.6
Diameter
(Microns)
27.
22.
14.
8.8
5.1
2.4
1.5
28.3
% Smaller
18.6
16.9
11.8
7.0
3.5
1.3
0.6
2.21
99.7
94.8
54.9
35.8
27.3
20.3
18.3
Diameter
(Microns)
27.
23.
14.
9.0
5.2
2.5
1.5
% Smaller
14.9
13.1
8.8
5.1
2.7
1.2
0.6
2.12
99.8
95.8
60.
39.
28.
18.6
17.5
.9
,1
.3
-------
KVB Company
ES-0596
5364-01
July 31, 1978
Sample No.
Sample Description
K-22486
Fly Ash
Site B
Test 25
K-22487
Fly Ash
Site B
Test 26
Bahco Particle
Size Determination
% Through #100
(149 Microns)
Results: Terminal
Velocity
112.
79.0
31.0
12.3
4.15
0.96
0.35
Density, gms/cc (On #100
Mesh Material Only)
Screen Sizing
% Through #10
#16
#30
#50
#100
#200
#325
33.8
Diameter
(Microns)
27.
23.
14.
8.9
5.2
2.5
1.5
99.9
96.8
66.3
45.5
33.8
22.2
21.5
37.2
% Smaller
.5
.3
16.
14.
9.0
5.1
2.7
1.1
0.5
2.16
Diameter
(Microns)
27.
23.
14.
8.9
5.2
2.5
1.5
Smaller
17.2
15.0
9.8
5.5
2.8
1.2
0.5
2.14
99.7
97.2
70.9
49.8
37.2
24.0
23.4
-------
LO
Q
UJ
I
99.9
99.8
99
98
95
90
80
70
60
50
40
30
20
10
5
1
0.5
0.1
.05
.01
SAMPLE IDENTIFICATION
^r 1
^
^
-
^
- I
6.
K Vo C.OAI/*/i/W
f
BAHCO SIZE DISTRIBUTION
I
w
-
c
^
0
i
**
^
x
r-
'*'
^
S
*
SAMPLE NO.
CHARGE NO.
.
^ 4
^
^
/
.
I
/
f-3*V?J
&36 V-o/
x
sy.
^
i/
'
v<
^«
y
X
1.5 2
6 8 10 15 20 30 40 60 80 100
EQUIVALENT PARTICLE DIAMETER - MICRONS
200 300
500
1000
DENSITY 3. 3 O g/cc
-------
SAMPLE IDENTIFICATION KVB
99.9
99.8
99
98
£
SAMPLE NO.
CHARGE NO.
95
90
80
70
60
50
40
30
20
10
5
BAt'co
i
0.5
0.1
.05
.01
1.5 2
6 8 10 15 20 30 40 60 80 100
EQUIVALENT PARTICLE DIAMETER - MICRONS
200 300
500
1000
DENSITY 3. 3 / g/cc
-------
SAMPLE NO. K- aa
99.9
99.8
99
98
95
90
80
70
60
50
40
30
20
10
c
0 5
05
.01
4
^
i
••^
-*
X^
X-
Piy As* s*»*ie 'sin e TfsTi
BAHCO SIZE DISTRIBUTION
0
9
X
X
1
I"
x^
^^
^^^
.^
•
•
>-
X"
^^
^^
*
**
^ CHARGE NO.
f
x-^«
x^
X*
-**
I
x-^
S/
JTJIV-O/
^>
Z.I
t
x
v,
X*
«
r
1.5 2
8 10 15 20 30 40 60 80 100
EQUIVALENT PARTICLE DIAMETER - MICRONS
200 300
500
1000
- / 00^, DENSITY a. JJL g/cc
-------
SAMPLE IDENTIFICATION
99.8
99
98
95
90
80
70
60
50
40
30
20
10
5
1
0.5
0.1
.05
.01
SAMPLE NO. Xr-ajygfe
CHARGE NO. S36V"O/
BAHOO SIZE DISTRIBUTION
V
1.5 2
6 8 10 15 20 30 40 60 80 100
EQUrVALBTT PARTICLE DIAMETER - MICRONS
200 300
500
DENSITY
1000
g/cc
-------
LO
Q
PJ
99.9
99.8
99
98
95
90
80
70
60
50
40
30
20
10
5
1
0.5
0.1
.05
.01
SAMPLE IDENTIFICATION A" V 6
+
s/T£6
SAMPLE NO.
CHARGE NO.
BAHCOSIZE DISTRIBUTION
•:
:o
Mf
1.5 2
6 8 10 15 20 30 40 60. 80 100
EQUIVALENT PARTICLE DIAMETER - MICRONS
200 300
500
1000
DENSITY
g/cc
-------
SECTION 5,0
FUEL AND ASH ANALYSIS
PAGE
5,1 COMMERCIAL TESTING ANALYSIS 270
5,2 COMBUSTIBLES ANALYSIS 310
5,3 COAL SIEVE ANALYSIS 316
269
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 338 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 313 736-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DBUNEN ROAD. SOUTH HOLLAND. ILLINOIS 60473
SINCE I9OB
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
Kind of sample
reported to us Coal
Sample taken at
Sample taken by KVB, Inc.
Date sampled
OFFICE TEL (312)»J.H7j
March 24, 1978
Sample identification
by
KVB, Inc.
Site B
Test 1
Analysis report no. 71-12749
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
2.99
7.58
34.82
54.61
100.00
13426
0.80
xxxxx
7.81
35.89
56.30
100.00
13840
0.82
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H=W)
Softening (H=%W)
Fluid
Reducing
XXX
XXX
XXX
XXX
Oxidizing
XXX
XXX
XXX
XXX
H li Con* Heljht
W in Con* Width
RAH:ljd
Respectfully submitted,
COMMERCIAL/TESTING & ^IGINEERING CO.
R. A. HouSER. Manager.Midwest Division
4~yr**f\ Charter Memoer
CHICAGO, ILLINOI* • CHARLESTON. W V* • CLARKSBURG, W VA • CLEVELAND. OHIO • NORFOLK VA • HEHO&faltf&J TOLEDO, OHIO • DENVER, COLORADO • BIRMINGHAM ALABAMA • VANCOUVER. B
-------
COMMERCIAL TESTING & ENGINEERING CO.
QENERAL OFFICES: 33S NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60S01 • AREA CODE 312 756-9434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 6047]
OFFICE TEL. (312) 214-111
SINCE I90B
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 2, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12750
PROXIMATE ANALYSIS
As received
Initial Deformation
Softening (H-W)
Softening (H-V4W)
Fluid
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
3.45
7.15
34.94
54.46
100.00
13367
0.91
xxxxx
7.41
36.19
56.40
100.00
13845
0.94
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
XXX
XXX
XXX
XXX
XXX
XXX
XXX
XXX
H It Com Height
W It Con* Width
RAH:ljd
Respectfully submitted,
COMMERCIAL/TtSTING &^NGINEERING CO.
CHICAOO, ILUNOII ' CHARLESTON, W.VA. • CLABKStURO. W.VA. • CLEVELAND. OHIO • NORFOLK. V,
R. A. HOUSER. Manager.Midwest Division
271
'A • HENDERSON f^f ~K>\
Charter Metntmr
iLEDO. OHIO • DENVER, COLORADO • BIRMINGHAM, ALABAMA • VANCOUVER, 8C
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312)264-1173
March 29, 1978
Kind of sample
reported to us
Sample identification
by
KVB, Inc.
Test 3, Site B, Coal
Sample taken at
Sample taken by KVB, Inc.
Date sampled
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% F. Carbon
Btu
% Sulfur
As Rec'd
1.90
11.38
34.44
52.28
100.00
12960
0.98
Analysis report no. 71-12751
ULTIMATE ANALYSIS
100.00
13211
1.00
xxxxx
73.55
5.07
1.51
0.08
1.00
11.60
7.19
100.00 100.00
FUSION TEMPERATURE OF ASH
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen (diff. )
1.90
72.15
4.97
1.48
0.08
0.98
11.38
7.06
Initial Def.
Soft. (H=W)
Soft. (H=1/2W)
Fluid
Reducing
2400°F
2700+°F
2700+°F
2700+°F
MINERAL ANALYSIS
Silica, SiO2
Alumina, Al,,O,
Titania, Ti02
Ferric Oxide, Fe2O,
Lime, CaO
Magnesia, MgO
Potassium Oxide, K-0
Sodium Oxide, Na2O
Sulfur Trioxide, SO,
Phos. Pentoxide, P20,
Undetermined
% Weight, Ignited
53.99
27.85
1.21
8.26
1.85
1.32
2.20
0.42
1.18
0.40
1.32
100.00
Alk. as Na 0, Dry Coal=0.22
SILICA VALUE = 82.53
Base/Acid = 0.17
"250 Poises:
2800°F
Respectfully
COMMERCIAL
NGINEERING CO.
R. A. Houser, Manager, Midwest Division
Charter Member
CHICMO. IL • BILLINGS, MT . BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER. CO . GOLDEN. CO • HENDERSON. KY •
MIDDLESBORO. KY • MOBILE, AL • NEW ORLEANS. LA • NORFOL0!QI'CTiEVILLE, KY • VANCOUVER, B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 998 NORTH LA 3ALLE STREET, CHICAGO, ILLINOIS 80601 • AREA CODE 311 738-6434
PLEASE ADDRESS ALL CORRESPONDENCE TO
KIM VAN ORUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-11
March 24, 1978
Sample identification
by
KVB , Inc .
Kind of sample
reported to us coal
Test 4, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12752
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H=W)
Softening (H-V4W)
Fluid
1.60
8.85
34.92
54.63
100.00
13485
0.84
FUSION TEMPERATURE
Reducing
XXX
XXX
XXX
XXX
xxxxx
8.99
35.49
55.52
100.00
13704
0.85
OF ASH
Oxidizing
XXX
XXX
XXX
XXX
H >• Com Might
w '• Con* Width
RAHrljd
Respectfully submitted.
ENGINEERING CO.
R. A. HOUSER. Manager.Midwest Division
xjajrj r* cnener Member
CHICAGO. ILLIHOII • CHARLESTON, W.VA. • CLARKSBURG. W.VA. • CLEVELAND. OHIO • NORFOLK. V* • HENOEHSON^^Te^JDO. OHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. B C
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 338 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 313 736-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN BOAD, SOUTH HOLLAND, ILLINOIS 6CM73
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
Kind of sample
reported to us coal
OFFICE TEL. (312) 2S4-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Test 5, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12753
PROXIMATE ANALYSIS
As received
Initial Deformation
Softening (H=W)
Softening (H=V4W)
Fluid
RAH:ljd
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.66
8.78
34.22
55.34
100.00
13472
0.89
xxxxx
8.93
34.80
56.27
100.00
13699
0.91
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
XXX
XXX
XXX
XXX
H It Corw H.lghl
W I* Con. Wldlh
XXX
XXX
XXX
XXX
Respectfully submitted,
COMMERCIAL/TESTING & £NGINEERING CO.
R. A HouSER. Manager,Midwest Division
CHICAGO. ILLINOII • CHARLESTON. W VA • CLARKSBURG. W VA • CLEVELAND. OHIO • NORFOLK. VA • HEND
Charter Member
LEDO OMI° * °ENVER. COLORADO • BIRMINGHAM ALABAMA • VANCOUVER. B C
-------
COMMERCIAL TESTING & ENGINEERING CO.
QCNERAl OFFICES: 99* NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 813 796-8434
PLEASE ADDRESS All CORRESPONDENCE TO
111)0 VAN DRUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN 54426
Kind of sample
reported to us
OFFICE TEL. (312) 264-1173
March 24, 1978
Sample taken at
Sample identification
by
KVB, Inc.
Coal
Site B
Test 6
Sample taken by RVB, Inc.
Date sampled
Analysis report no. 71-12754
PROXIMATE ANALYSIS
As received
Initial Deformation
Softening (H-W)
Softening (H-V4W)
Fluid
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.99
9.41
33.95
54.65
100.00
13011
0.83
xxxxx
9.60
34.64
55.76
100.00
13275
0.85
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H to COM Height
W IB Cone Width
Respectfully submitted,
COMMERCIAL TESTING 4 ENGINEERING CO.
RAH:lf
' CWCA80, IUINOW . CHARLESTON. W.VA. • CLARKSBURG. W.VA. • CLCVEIAND. OHIO • NORFOLK. VA. • HENDERI
. Manager, Midwest Division
I, OHIO • DENVER. COLORADO • BIR
ChBrt«r M«mb«r
ABAMA • VANCOUVER. B.C.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
Kind of sample
reported to us
Coal
March. 29, 1978
Sample identification
by
KVB, Inc.
Test 7, Site B
Sample taken at
Sample taken by
KVB, Inc.
Date sampled
PROXIMATE ANALYSIS
Analysis report no
% Moisture
% Ash
% Volatile
% F. Carbon
Btu
% Sulfur
As Rec'd
1.08
6.48
35.60
56.84
100.00
13981
0.82
ULTIMATE ANALYSIS
100.00
14134
0.83
xxxxx
78.93
5.31
1.39
0.13
0.83
6.55
6.86
100.00 100.00
FUSION TEMPERATURE OF ASH
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen (dif f . )
1.08
78.08
5.25
1.37
0.13
0.82
6.48
6.79
Initial Def.
Soft. (H=W)
Soft. (H=1/2W)
Fluid
RAH:ljd
Reducing
2700+°F
2700+°F
2700+°F
2700+°F
71-12755
MINERAL ANALYSIS
% Weight, Ignited
Silica, SiO_
Alumina,
Titania,
Ferric Oxide, Fe_O-
Lime, CaO
Magnesia, MgO
Potassium Oxide, K_0
Sodium Oxide, Na,,O
Sulfur Trioxide, SO,
Phos. Pentoxide, P2 5
Undetermined
53.39
30.71
1.54
6.. 41
1.90
0.75
1.15
0.62
1.13
0.50
1.90
100.00
Alk. as Na O, Dry Coal =0.09
SILICA VALUE = 85.49
Base/Acid = 0.13
"250 Poises:
2900+°F
Respectfully submitted,
COMMERCXL/ESJING
NGINEERING CO.
R A. Houser, Manager, Midwest Division
CHICAGO, II • BIUINGS. MT • BIRMINGHAM, AL . CHARLESTON. WV • CLARKSBURG,
MIDDLESBORO. KY • MOBILE, AL • NEW ORLEANS. LA « NORFOLK,
."2316;
AND, OH
HUE. KY •
DENVER. CO • GOIDEN, CO •
VANCOUVER. B.C. CAN.
Charter Member
HENDERSON, KY •
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60801 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
March 29, 1978
Kind of sample
reported to us Coal
Sample identification
by
KVB , Inc .
Test 8, Site B
Sample taken at
Sample taken by KVB/ Inc,
Date sampled
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% F. Carbon
Btu
% Sulfur
As Rec ' d
4.39
8.83
33.97
52.81
100.00
13111
1.05
ULTIMATE ANALYSIS
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen (diff)
4.39
72.66
4.96
0.85
0.15
1.05
8.83
7.11
Analysis report no. 71-12756
100.00
13713
1.10
xxxxx
75.99
,19
.89
5.
0,
0,
1.
9,
16
10
24
7.43
100.00 100.00
'FUSION TEMPERATURE OF ASH
Initial Def.
Soft. (H=W)
Soft. (H=1/2W)
Fluid
RAH:ljd
Reducing
2320°F
2570°F
2620°F
2700+°F
MINERAL ANALYSIS
Silica, SiO,
Alumina, Al-O,
Titania, TiO-
% Weight, Ignited
54.44
26.78
0.99
Ferric Oxide, ^^2°3 ' 9-29
Lime, CaO 2.02
Magnesia, MgO 1.43
Potassium Oxide, K_O 2.50
Sodium Oxide, Na2O 0.52
Sulfur Trioxide, SO, 1.42
Phos. Pentoxide, P2°5 0.23
Undetermined 0.38
100.00
Alk. as Na-O, Dry Coal =0.20
SILICA VALUE = 81.04
Base/Acid =0.19
250 Poises:
Respectfully s
COMMERCI
IGINEERING CO.
R. A. Houser, Manager, Midwest Division
Charter Member
CHICAGO, 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, <»S»»lllE. KY • VANCOUVER, B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 398 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601 • AREA CODE 312 726-8*341
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
SINCE 19OB
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN 55426
Kind of sample
reported to us
Sample taken at
Sample taken by KVB, Inc.
OFFICE TEL (312) 264-1173
March 27, 1978
Sample identification
by
KVB, Inc.
P.O. 321-15900
Coal
Site B
Test 9
Date sampled
Analysis report no. 71-12757
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
5.05
5.92
34.90
54.13
100.00
13434
0.93
XXXXX
6,23
36.76
57.01
100.00
14149
0.98
Initial Deformation
Softening (H=W)
Softening (H-V4W)
Fluid
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
XXXXX
XXXXX
XXXXX
XXXXX
XXXXX
XXXXX
XXXXX
XXXXX
H Is COIN Height
W It Con* Width
RAH:If
Respectfully submitted,
COMMERCIAL TESTING
ENGINEERING CO.
CHICAOO. ILLINOU • CHARLESTON. W VA • CLARKSBURG. W VA • CLEVELAND. OHIO • NORFOLK. VA
USER. Manager. Midwest Division
Charier Member
KY . TOLEDO. OHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. B C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 998 NORTH LA 8ALLE STREET, CHICAGO, ILLINOIS 60001 • AREA CODE 913 716-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
HIM VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
OFFICE TEL. (312) 2(4-1173
March 24, 1978
Minneapolis, MN 54426
Kind of sample
reported to us ~
• Sample taken at
Sample taken by KVB, Inc.
Date sampled '-
Sample identification
by
KVB, Inc.
Coal
Site B
Test 11
Analysis report no. 71-12758
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.99
5.08
35.44
57.49
100.00
14077
0.75
xxxxx
5.18
36.16
58.66
100.00
14363
0.77
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
Initial Deformation
Softening (H-W)
Softening (H-ViW)
Fluid
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H n CofW Ht)l0ht
W !• Con* Width
RAH:If
Respectfully submitted,
COMMERCIAL TESTING 4 ENGINEERING CO.
R. A1
CHICAGO. ILLINOU . CHARLESTON. W.VA. • CLARKS6UHO. W.VA. • CLEVELAND. OHIO • NORFOLK. VA .
Ch«rt«f M«mb«r
. TOLEDO. OHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. B C
-------
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 OBUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 2M-117J
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 12, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12759
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H=W)
Softening (H=%W)
Fluid
4.76
6.50
34.88
53.86
100.00
13368
0.85
FUSION TEMPERATURE
Reducing
XXX
XXX
XXX
XXX
xxxxx
6.83
36.62
56.55
100.00
14036
0.89
OF ASH
Oxidizing
XXX
XXX
XXX
XXX
H It Com Height
W It Con* Width
RAH:ljd
Respectfully submitted,
COMMERCIA«OESTING ^ENGINEERING co.
R. A. HOUSER, Manager,Midwest Di"mon
CHICAGO ILLINOU • CHARLESTON. W VA • CLARKSBURG. W VA • CLEVELAND. OHIO • NORFOLK VJk • HEI
Charter M«mt>«r
• TOLEDO, OHIO • DENVER, COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER, BC
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 226 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 726-6434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
March 29, 1978
Kind of sample
reported to us Coal
Sample identification
by
KVB, Inc.
Test 15, Site B
Sample taken at
Sample taken by
f Inc
Date sampled
PROXIMATE ANALYSIS
As
% Moisture
% Ash
% Volatile
% F. Carbon
T
Btu
% Sulfur
ULTIMATE ANALYSIS
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
* Sulfur
% Ash
% Oxygen (diff.)
Rec'd
5.48
6.47
34 . 21
53.84
00.00
13181
0.71
5.48
74.11
4.99
1.44
0.12
0.71
6.47
6.68
Analysis re\
Dry
xxxxx
6.84
36.19
56.97
100.00
13946
0.75
xxxxx
78.41
5.28
1.52
0.13
0.75
6.84
7.07
port no. 71-12760
MINERAL ANALYSIS
Silica, SiO_
Alumina, Al.O,
Titania, Ti02
Ferric Oxide, Fe
Lime , CaO
Magnesia, MgO
Potassium Oxide,
Sodium Oxide, Na
Sulfur Trioxide,
Phos. Pentoxide,
Undetermined
% Weight, Ignited
54.14
30.00
1.43
2°3 6i;39o
0*81
K-0 1.55
_0^ 0.47
SO, 1.43
P,6, 0.28
2 5 1.64
100.00
100.00 100.00
FUSION TEMPERATURE OF ASH
Initial Def.
Soft. (H=W)
Soft. (H=1/2W)
Fluid
RAHrljd
Reducing
2700+°F
2700+°F
2700+°F
2700+°F
Alk. as Na.O, Dry Coal
SILICA VALUE = 85.66
Base/Acid =0.13
T
250 Poises:
= 0.10
2900+°F
Respectfully submitted,
COMMERCIAL TESTING ytNGINEERING CO.
R. A. Houser. Manager, Midwest Division
CHICAGO, II • BILLINGS, MT • BIRMINGHAM, Al • CHARLESTON. WV • CLARKSBI
MIODLESBORO. KV • MOBILE, AL • NEW ORLEANS. LA •
Charter Member
CLEVELAND, OH • DENVER, CO • GOLDEN, CO • HENDERSON. KY •
PIKEVILLE, KY • VANCOUVER, B.C. CAN.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
March 29, 1978
Kind of sample
reported to us Coal
Sample identification
by
KVB, Inc.
Test 16, Site B
Sam p le taken at
Sample taken by KVB, Inc.
Date sampled
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% F. Carbon
As Rec ' d
6.46
6.96
33.73
52.85
100.00
Btu 13001
% Sulfur 0.75
ULTIMATE ANALYSIS
% Moisture
% Carbon
% Hydrogen
% Nitrogen
% Chlorine
% Sulfur
% Ash
% Oxygen (diff.
6.46
72.78
4.88
1.45
0.11
0.75
6.96
) 6.61
Analysis report no. 71-12761
Dry MINERAL ANALYSIS
xxxxx
7.44
36.06
56.50
100.00
13899
0.80
xxxxx
77.81
5.22
1.55
0.12
0.80
7.44
7.06
Silica, SiO-
Alumina, Al.O-
Titania, Tio_
Ferric Oxide, Fe
Lime, Ca,0
Magnesia, MgO
Potassium Oxide,
Sodium Oxide, Na
Sulfur Trioxide,
Phos. Pentoxide,
Undetermined
A 1 TJ- ^ ^ M-» r\ r\*.
% Weight, Ignited
53.39
30.71
1.32
.0, 7.22
2 3 1.97
0.90
K 0 1.85
20^ 0.42
SO, 1.43.
P.Or 0.31
^ 5 * 0.48
100.00
•,* f~*r* -.1 — f\ TO
100.00 100.00
FUSION TEMPERATURE OF ASH
Initial Def.
Soft. (H=W)
Soft. (H=1/2W)
Fluid
RAH:ljd
Reducing
2700+°F
2700+°F
2700+°F
2700+°F
f±^*Jl. • W* t*t &* *-fc f. \w• f •!_/J- V VirV^d
SILICA VALUE = 81.20
Base/Acid = 0.14
250 Poises:
2850°F
Respectfully submitted,
GINEERING CO.
R. A. Houser, Manager, Midwest Division
Charter Member
CHICAGO, II • BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON, WV • CLARKSBURG. WV • CLEVELAND, OH • DENVER, CO • GOLDEN, CO • HENDERSON, KY •
MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK. VAMPWMILLE, KY • VANCOUVER. B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 22S NORTH LA SALLE STREET, CHICAQO, ILLINOIS «0601 • AREA CODE 112 756-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
KtNVANDRUMEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
SINCE 19O8
OFFICE TEL. (312) 2(4-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us coal
Test 17, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12762
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H-W)
Softening (H-fcW)
Fluid
As received
3.20
6.99
35.28
54.53
100.00
13535
0.77
FUSION TEMPERATURE
Reducing
XXX
XXX
XXX
XXX
Dry basis
xxxxx
7.22
36.45
56.33
100.00
13982
0.80
OF ASH
Oxidizing
XXX H '• Co"* H»'»M
XXX w '• Con« widlh
XXX
XXX
RAH:ljd
Respectfully submitted,
COMMERCIAL/T6STING S^/NGINEERING CO.
R. A. HOUSER, Manager.Midwest Division
CHICAGO, ILLINOII • CHARLESTON. W.VA. • CLARKSaURO. W.VA • CLEVELAND. OHIO • NORFOLK. V.
'A • HEHOEHCTI
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 238 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80801 • AREA CODE 312 728-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DBUNEN HOAD, SOUTH HOLLAND. ILLINOIS 60473
SINCE 19O8
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL (312)214.1173
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 18, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12763
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
3.64
5.66
35.24
55.46
100.00
13696
0.71
xxxxx
5.87
36.57
57.56
100.00
14214
0.74
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H=W)
Softening (H=ttW)
Fluid
Reducing
XXX
XXX
XXX
XXX
Oxidizing
XXX
XXX
XXX
XXX
H It Con. H«lght
w It Com Width
RAH:ljd
Respectfully submitted,
COMMERCIA^TfeSTING
NGINEERING CO.
R. A. HOUSER, Manager.Midwest Division
OlD/f Ch«n«r Member
CMICAOO. ILLINOIS • CHARLESTON. W VA • CLARKSBURG W VA . CLEVELAND. OHIO • NORFOLK. VA . II III I idbflfj J[llll I III OHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. B C
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 328 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 91» 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN. 54426
Kind of sample
reported to us
Sample taken at
OFFICE TEL. (312) 264-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Coal
Site B
Test 19
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12764
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H=W)
Softening (H-V4W)
Fluid
4.75
8.00
32.53
54.72
100.00
13115
0.87
FUSION TEMPERATURE
Reducing
XXXXX
xxxxx
XXXXX
xxxxx
xxxxx
8.40
34.15
57.45
100.00
13768
0.91
OF ASH
Oxidizing
XXXXX H 1. Con, H.lghl
XXXXX W ll Con* Width
XXXXX
XXXXX
RAH:lf
Respectfully submitted,
COMMERCIAtVTESTING 1 ENGINEERING CO.
R. A. HOUSER Manager Midwest Division
CHICAHO. ILLINOIS • CHARLESTON. W.VA. • CLARKSBURG. * VA. • CLEVELAND, OHIO • NORFOLK. VA • HENDERSON,
Charier Member
. OHIO • DENVER. COLORADO • BIRMINGHAM, ALABAMA • VANCOUVER. B C
-------
COMMERCIAL TESTING & ENGINEERING CO.
QENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80601 • AREA CODE 312 728-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD. SOUTH HOLLAND. ILLINOIS 60473
OFFICE TEL (312) 2M-1171
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
Kind of sample
reported to us Coal
March 24, 1978
Sample identification
by
KVB, Inc.
Test 20, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12765
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
4.95
8.22
33.81
53.02
100.00
12972
1.06
xxxxx
8.65
35.57
55.78
100.00
13647
1.12
Initial Deformation
Softening (H=W)
Softening (H=%W)
Fluid
I-USION IfcMPfcRATURfc OF ASH
Reducing Oxidizing
XXX
XXX
XXX
XXX
XXX
XXX
XXX
XXX
H li Con* Height
W ts Con* Width
RAHiljd
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R A HouSER, Manager, Midwest Division
OJDC* Charter Member
CHICAGO. ILLINOIS • CHARLESTON, W VA • CLARKSBURG. W VA • CLEVELAND. OHIO • NORFOLK, VA • HENOERS*W^»lObLEDO, OHIO • DENVER, COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. 6 C
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 918 NORTH LA SALLE STREET, CHPCAOO, ILLINOIS S0«0t • AREA CODE 81» 796-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND. ILLINOIS 6047]
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN 54426
Kind of sample
reported to us
Sample taken at
Sample taken by KVB' Inc<
Date sampled
SINCt I9O8
OFFICE TEL. (312) 214-117}
March 24, 1978
Sample identification
by
KVB, Inc.
Coal
Site B
Test 21
Analysis report no. 71-12766
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
4.81
8.42
33.42
53.35
100.00
13097
0.89
xxxxx
8.85
35.11
56.04
100.00
13759
0.94
Initial Deformation
Softening (H-W)
Softening (H-VfeW)
Fluid
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
xxxxx xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H It COM HaloM
W la Con* Width
RAH:If
Respectfully submitted,
COMMERCIAL-NESTING & ENGINEERING CO.
R. A. HOUSER. Managar.Midwait Division
^^ Charter Member
CHICAGO, IUINOII - CHARLESTON, W.VA. • CLARKSBURG, W.VA. • CLEVELAND. OHIO • NORFOLK. VA • HENDERSOrQlQWfcDO, OHIO • DENVER, COLORADO • BIRMINGHAM, ALABAMA • VANCOUVCR. B.C
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 328 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 313 736-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUN6N ROAD, SOUTH HOLLAND. ILLINOIS 60473
SINCE 19O8
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (J1J) 2M-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 22, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12767
PROXIMATE ANALYSIS
As received
Initial Deformation
Softening (H=W)
Softening (H=ViW)
Fluid
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
5.89
8.26
33.05
52.80
100.00
12926
0.91
xxxxx
8.78
35.12
56.10
100.00
13734
0.97
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
XXX
XXX
XXX
XXX
XXX
XXX
XXX
XXX
H It COM Height
W ll Con* Width
RAH:ljd
Respectfully submitted,
COMMERCIAL TESTING SyENGINEERING CO.
R. A. HOUSER. Manager,Midwest
CHICAGO, ILLINOII • CHARLESTON, W VA .CLARKSBURG W VA - CLEVELAND, OHIO • NORFOLK, VA • RENDERS'
Charter Member
. OHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER, BC
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 338 NORTH LA SACLE STREET, CHICAGO. ILLINOIS 60001 • AREA CODE 311 738-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD. SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN 5426
Kind of sample
reported to us
Sample taken at
OFFICE TEL. (312) 264-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Coal
Site B
Test 23
Sample taken by KVB , Inc
Date sampled
Analysis report no. 71-12768
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H=W)
Softening (H-%W)
Fluid
5.56
7.60
33.31
53.53
100.00
13077
0.91
FUSION TEMPERATURE
Reducing
xxxxx
XXX XX
xxxxx
xxxxx
xxxxx
8.05
35.27
56.68
100.00
13847
0.96
OF ASH
Oxidizing
XXXXX H !• Con* Height
XXXXX W It Con* Width
XXXXX
xxxxx
RAH:If
Respectfully submitted,
COMMERCIAL TESTING i ENGINEERING CO.
CHICAGO. ILLINOIS • CHARLESTON. W V* • CLARKSBURG. WVA • CLEVELAND, OHIO . NORFOLK. v» . HENDERSON. KY • TOI
289
Charier Mamber
DENVER, COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. BC
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO. ILLINOIS 60601 • AREA CODE 312 726-84M
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
March 29, 1978
Kind of sample
reported to us Coal
Sample identification
by
KVB, Inc.
Test 24, Site B
Sample taken at
Sam pie taken by KVB, Inc.
Date sampled
PROXIMATE ANALYSIS
%
%
%
%
%
Moisture
Ash
Volatile
F. Carbon
Btu
Sulfur
As Rec ' d
5.03
16.79
30.97
47.21
100.00
11667
0.75
Analysis report no. 71—12769
Dry
xxxxx
17.68
32.61
49.71
100.00
12284
0.79
ULTIMATE ANALYSIS
%
%
%
%
%
%
%
%
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff.
5.03
65.56
4.44
1.30
0.10
0.75
16.79
) 6.03
100.00
xxxxx
69.03
4.68
1.37
0.11
0.79
17.68
6.34
100.00
MINERAL ANALYSIS
Silica, SiO-
Alumina, Alfo,
Titania, Ti02
Ferric Oxide, Fe
Lime , CaO
Magnesia, MgO
Potassium Oxide,
Sodium Oxide, Na
Sulfur Trioxide,
Phos. Pentoxide,
Undetermined
Alk. as Na_0, Dr
% Weight,
54.
28.
1.
2°3 7-
^ J 1.
1.
K,0 1.
2o o.
SO., 1.
P-0. 0.
25 0.
100.
y Coal = 0
Ignited
90
56
21
74
95
08
95
42
17
23
79
00
.30
FUSION TEMPERATURE OF ASH
Reducing
Initial Def. 2520°F
Soft. (H=W) 2700+°F
Soft. (H=1/2W) 2700+°F
Fluid 2700+°F
RAH:ljd
Base/Acid = 0.16
250 Poises:
2830°F
Respectfully
COMMERCI
GINEERING CO.
R. A. Houser, Manager, Midwest Division
CHICAGO, II
BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV '
MIDDLESBORO. Kr • MOBIL£, AL • NEW ORLEANS. LA • NORFOLK, VA
Charter Member
, OH • DENVER. CO • GOLDEN, CO • HENDERSON, KY •
, KV • VANCOUVER. B.C. CAN.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
OFFICE TEL. (312) 264-1173
March 29, 1978
Kind of sample
reported to us Coal
Sample identification
by
KVB, Inc.
Test 25, Site B
Sample taken at
Sample taken by KVB, Inc,
Date sampled
PROXIMATE ANALYSIS Analysis report no. 71 -1 5770
As Rec'd Dry
% Moisture 2.90 xxxxx
% Ash 10.66 10.98
% Volatile 35.38 36.44
% F. Carbon 51.06 52.58
100.00 100.00
Btu 12923 13309
% Sulfur 0.91 0.94
ULTIMATE ANALYSIS
% Moisture 2.90 xxxxx
% Carbon 72.27 74.43
% Hydrogen 4.98 5.13
% Nitrogen 1.19 1.23
% Chlorine 0.07 0.07
% Sulfur 0.91 0.94
% Ash 10.66 10.98
% Oxygen (diff.) 7.02 7.22
100.00 100.00
FUSION TEMPERATURE OF ASH
Reducing
MINERAL ANALYSIS
%
Silica, SiO2
Alumina, Al-O,
Titania, Ti02
Ferric Oxide, Fe-0,
Lime , CaO
Magnesia, MgO
Potassium Oxide, K?O
Sodium Oxide, Na20
Sulfur Trioxide, SO,
Phos. Pentoxide, P.,0
Undetermined
Alk. as Na_0, Dry Co
SILICA VALUE = 82.88
Base/Acid - 0.17
T . 2Rin°F
Weight, Ignited
54.90
27.14
1.10
7.22
2.80
1.32
1.95
0.52
1.71
0.17
b 1.17
100.00
OO f\
. zu
Initial Def.
Soft. (H=W)
Soft. (H-1/2W)
Fluid
RAH:ljd
2450°F
2660°F
2700+°F
2700+°F
ncn _ .
250 Poises:
Respectfully submitted,
COMMERCIATTiSTING & MRGINEERING CO.
R. A. Houaer, Manager, Midwest Division
CHICAGO, II • BILLINGS. MT • BIRMINGHAM. Al • CHARLESTON, WV • CLARKSBURG WV • c
MIDDLESBORO. KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK, VA •
Charter Member
I, OH • DENVER. CO • GOLDEN, CO • HENDERSON, KY •
f*KY • VANCOUVER, B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 226 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 80801 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN OHUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
OFFICE TEL (312) M4-1173
March 24, 1978
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 26, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12771
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
3.25
8.53
34.35
53.87
100.00
13235
0.95
xxxxx
8.82
35.50
55.68
100.00
13679
0.98
Initial Deformation
Softening (H=W)
Softening (H=ttW)
Fluid
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
XXX
XXX
XXX
XXX
XXX
XXX
XXX
XXX
H It Com Height
W I* Con* Width
Respectfully submitted,
COMMERCIA^ESTING ^/ENGINEERING co.
R. A. HOUSER. Manager,Midwest Division
RAHrljd
CHICAGO, ILLINOIS • CHARLESTON. W VA. • CLARKSBURG. W VA • CLEVELAND, OHIO • NORFOLK. VA • HENDERSON. KY*« TOLEDoloHIO • OEi
Charter Member
ABA MA • VANCOUVER, B C
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 911 NORTH LA SALLE STREET, CHICAOO, ILLINOIS 60601 • AREA CODE S13 736-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
1(130 VAN DRUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
r
KVB, INC.
600 South County Road 18
Shelard Tower, Ste. 1375
Minneapolis, MN 54426
Kind of sample
reported to us
Sample taken at
SINCE 19O8
OFFICE TEL. (312) 204-1173
March 24, 1978
Sample identification
by
KVB, Inc.
Coal
Site B
Test 27
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12772
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H-W)
Softening (H-ViW)
Fluid
5.30
5.83
33.97
54.90
100.00
13266
0.68
FUSION TEMPERATURE
Reducing
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
6.16
35.87
57.97
100.00
14008
0.72
OF ASH
Oxidizing
XXXXX H It Con. H.lght
xxxxx w '• Con* wldlh
xxxxx
xxxxx
RAH:lf
Respectfully submitted,
COMMERCIAL JESTING & ENGINEERING CO.
R. A. HOUSER. Manager.Midwest Division
CHICAOO, ILLINOII . CHARLESTON. W V*. • CLARKSBURG. W.VA. • CLEVELAND. OHIO • NORFOLK. VA • HENDERSON.
"10 ' D6NVEB- COLORADO • BIF
Charter Member
-------
COMMERCIAL TESTING & ENGINEERING CO.
OFFICES: »M MOBTM LA SALLE STBEET. CHICAGO. ILLINOIS MMOI A>EA CODE 9f> 7IS-«<»*
PIEASE AOOBESS ALL COMRESPOMOEMCE TO
ICO* *«• OHtMEH MMO. SOU1H HOUJWD. UJMOIS «H73
SINCE 19O8
KVB, INC.
600 South County Road 18
Minneapolis, Minnesota 55426
TEL rnjj s*-nn
March 24, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us Coal
Test 28, Site B
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-12773
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
As received
5.98
, 5.81
33.88
54.33
100.00
13318
0.87
Dry basis
xxxxx
6.18
36.03
57.79
100.00
14165
0.93
FUSiON TEiviPERATURE OF ASH
Initial Deformation
Softening (H=W)
Softening (H=ttW)
Fluid
Reducing
XXX
XXX
XXX
XXX
Oxidizing
XXX H It Com Height
XXX w It Cent Width
XXX
XXX
RAH:ljd
Respectfully submitted,
GINEERING CO.
R. A. HOUSER. Manager.Midwest Division
CHICAGO, ILLINOIS • CHARLESTON. W.VA. • CLARKSBURG. W.VA. • CLEVELAND. OHIO • NORFOLK. VA • HENDERSON. KV
Charter MvmtMr
DENVER. COLORADO - BIRMINGHAM. ALABAMA • VANCOUVER. • C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
flENERAL OFFICE*: 818 NORTH LA SALLE STREET, CHICAOO, ILLINOIS 60601 • AREA CODE S19 756-R4S4
«SE ADDRESS ALL CORRESPONDENCE TO
10 VAN ORUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
f KVB, INC.
600 S. County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
Kind of sample
reported tout —-—
Simple taken at
Sample taken by KVB, Inc.
Date sampled
SINCE I9OB
OFFICE TEL. (312) M4-1173
April 17, 1978
Sample identification
by
KVB, inc.
Coal Test 30 Site B Old
No Purchase Order Received
As of 4/17/78.
Analysis report no. 71-13761
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.51
10.35
32.91
55.23
100.00
13271
0.95
xxxxx
10.51
33.41
56.08
100.00
13474
0.96
Initial Deformation
Softening (H-W)
Softening (H-ViW)
Fluid
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H l« COM Hclgfrt
W It Con« width
RAH:lau
Respectfully submitted,
COMMERCIAJoTESTING & ENGINEERING CO.
R. A. HOUSER. ManagerMidwett.Diy
SWAM, IlLMOII . CHARLESTON. W.VA. • CUARKSBUHO. W.VA. • CLEVELAND. OHIO • NORFOLK. VA. . HENDEBBON.
J29S
Charter M«mb*r
I. OHIO • DENVER. COLORADO • BIRMINGHAM, ALABAMA • VANCOUVER. B.C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 6O801 • AREA CODE 312 720-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD. SOUTH HOLLAND, ILLINOIS 60473
OFFICE TEL. (312) ZM-1173
April 19, 1978
KVB, INC.
Shelard Tower, Ste. 1375
600 S. County Road 18
Minneapolis, MN 54426
Kind of sample
reported to us
Sample Identification
by
KVB, Inc.
Sample taken at
Sample taken by KVB, Inc.
Date sampled
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
% Alk. as Na,O
SULFUR FORMS
% Pyritic Sulfur
% Sulfate Sulfur
% Organic Sulfur
WATER SOLUBLE ALKALIES
% Na,O =
% K,0 -
FUSION TEMPERATURE OF ASH
Initial Deformation
H !• con. Height Softening (H = W)
w i> cone width Softening (H = Vz W)
Fiuiu
% EQUILIBRIUM MOISTURE =
HARDGROVE GRINDABILITY INDEX =
FREE SWELLING INDEX =
Coal
Test 30 Site B
J3e*w
Analysis report no. 71-13758 % weight
As received Dry basis ULTIMATE ANALYSIS As received Dry basis
4.71
8.35
32.73
54.21
100.00
13222
0.87
xxxxx
0.18
0.03
0.66
xxxxx
xxxxx
Reducing
2700+°F
2700+°F
2700+°F
2700+°F
xxxxx
8.76
34.35
56.89
100.00
13875
0.91
0.19
0.19
0.03
0.69
xxxxx
xxxxx
Oxidizing
2700+°F
2700+°F
2700+°F
2700+°F
xxxxx
xxxxx
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff)
MINERAL ANALYSIS OF ASH
Silica; SiO?
Alumina, AUO,
Titania, TiO2
Ferric oxide, Fe,O3
Lime, CaO
Magnesia, MgO
Potassium oxide, K,O
Sodium oxide, Na,O
Sulfur trioxide, SO,
Phos. pentoxide, P,O5
Undetermined
SILICA VALUE - 86.60
BASE : ACID RATIO 0.13
T250 Temperature = 2900+
4.71
73.61
4 .79
1.38
0.11
0.87
8.35
6.18
100.00
xxxxx
77
5
1
0
0
8
6
100
.25
.03
.45
.12
.91
.76
.48
.00
% Weight Ignited Basis
55.
29.
1.
6.
1.
0.
2.
0.
0
\j •
n
\J .
f)
\J .
100 .
op
65
30
76
34
40
87
15
"7 *7
77
Rfi
O U
38
J L>
5?
~J £-
00
xxxxx
Respectfully submitted,
COMMERQJ*U TESTING^ ENGINEERING CO.
RAH:If
R A HOUSER. Manager Ml .1 Division
CHICAGO. ILUNOn • CHARLESTON. W VA. ' CLARKUUIKi. W.VA. • CLEVELAND. OHIO • NORFOLK. VA
296
Charter Member
HENDERSON. KV • TOLEDO. OHIO • OENVER. COLORADO • »RMINQHAM. ALABAMA • VANCOUVER. 1C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
OENEIWL OFFICES: 99S NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 912 726-8434.
PLEASE ADDRESS ALL CORRESPONDENCE TO
1S1NVAN OHUNEN ROAD, SOUTH HOLLAND. ILLINOIS 60473
KVB, INC.
600 S. County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
SINCE 19CJ8
OFFICE TEL. (312) 264-1173
April 17, 1978
Sample identification
by
KVB, Inc.
Kind of sample
reported to us
Coal Test 31 Site B Old
Sample taken at
No Purchase Order Received
As of 4/17/78.
Sample taken by KVB, Inc.
Date sampled
Analysis report no. 71-13762
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.50
9.24
34.34
54.92
100.00
13371
0.98
xxxxx
9.38
34.86
55.76
100.00
13575
0.99
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
Initial Deformation
Softening (H=W)
Softening (H=%W)
Fluid
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx'
xxxxx
H li COM Height
W It Con* Width
RAHrlau
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R A. HOUSER. Manager,Midwest Division
^yfyt**! Charter Member
CHICAGO. ILLINOIS • CHARLESTON, W.VA. • Cl-ARKSBURO. W.VA. • CLEVELAND, OHIO • NORFOLK. VA • HENDERSON, KY • W^JO. tjHIO • DENVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER. B C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: fae NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 311 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN ORUNEN ROAD. SOUTH HOLLAND. ILLINOIS 60473
SINCE I9O0
April 18, 1978
OFFICE TEL (312) 2M-1173
r KVB, INC.
600 S. County Road 18
Minneapolis, MN 54426
Kind of sample
reported to us
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Sample Identification
by
KVB, Inc.
Coal Test 31 Site B New
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
% Alk. as Na,O
SULFUR FORMS
% Pyritic Sulfur
% Sulfate Sulfur
% Organic Sulfur
WATER SOLUBLE ALKALIES
% Na,O =
%K,0 =
FUSION TEMPERATURE OF ASH
Initial Deformation
H u con. H.iflnt Softening (H = W)
w i. con. width Softening (H - Vz W)
Fluid
% EQUILIBRIUM MOISTURE =
HARDGROVE GRINDABILITY INDEX =
FREE SWELLING INDEX =
Analysis
As received
4.36
8.18
34.43
53.03
100.00
13150
0.93
xxxxx
0.20
0.00
0.73
xxxxx
xxxxx
Reducing
2700+°F
2700+°F
2700+°F
2700+°F
report no.
Dry basis
xxxxx
8.55
36.00
55.45
100.00
13750
0.97
0.18
0.21
0.00
0.76
xxxxx
xxxxx
Oxidizing
2700+°F
2700+°F
2700+°F
2700+°F
xxxxx
xxxxx
71-13759
ULTIMATE ANALYSIS
Moisture
Carbon
Hydrogen
Nitrogen
Chlorine
Sulfur
Ash
Oxygen (diff)
MINERAL ANALYSIS OF ASH
Silica; SiO,
Alumina, AI,O,
Titania, TiO,
Ferric oxide, Fe,Oj
Lime, CaO
Magnesia, MgO
Potassium oxide, K,O
Sodium oxide, Na,O
Sulfur trioxide, SO,
Phos. pentoxide, P,O5
Undetermined
SiLiCA v'ALUE - 84 .
BASE: ACID RATIO 0.
T250 Temperature = 2870
% Weight
As received
4
73
4
1
0
0
8
7
100
.36
.29
.81
.10
.07
.93
.18
.26
.00
Dry basis
xxxxx
76.
5.
1.
0.
0.
8.
7.
100.
63
03
15
07
97
55
60
00
% Weight Ignited Basis
86
14
op
52
31
1
6
1
1
2
0
1
0
0
i no
j, \j \j
.64
.40
.54
.44
.90
.05
.30
.63
.05
.44
.61
00
• \J \J
xxxxx
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
RAHrlau
__ Charter Mtmbcr
CHICAGO, ILUHOn • CHARLESTON, W VA. • CLARKUURQ. W.VA. • CLEVELAND, OHIO * NORFOLK. VA. • HENDERSON. KY • TOLEDO. OHIO * DENVER. COLORADO • BIRMINGHAM, ALABAMA • VANCOUVER, B.C.
298
-------
COMMERCIAL TESTING & ENGINEERING CO.
ttCNERAL OFFICES: *9S WORTH LA SALLE STREET, CHICAOO, ILLINOIS 80601 • AREA CODE 119 T9S-S434
MUt ADDRESS ALL CCWWIESPONOSNCE TO
HIM VAN MUMCN "OAO, SOUTH HOLLAND. ILLINOIS 60473
r
KVB, INC.
600 S. County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
OFFICE TEL. (312) 264-1173
April 17, 1978
Sample identification
by
Kind of sample
reported to us
Sample taken at
Sample taken by
KVB, Inc.
Coal Test 32 Site B Old
No Purchase Order Received
As of 4/17/78.
KVB, Inc.
Date sampled
Analysis report no. 71-13764
PROXIMATE ANALYSIS
As received
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
Initial Deformation
Softening (H-W)
Softening (H-titW)
Fluid
5.65
8.62
32.84
52.89
100.00
12860
0.92
xxxxx
9.14
34.81
56.05
100.00
13630
0.98
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H It Com Hclgtil
W It Com Width
RAHzlau
Respectfully, submitted,
& ENGINEERING CO.
R. A. HOUSER. Manager, Midwest Division
CHICAGO, ILUMOII • CHARLESTON, W.VA. • CLARKSBURG. W.VA. * CLEVELAND. OHIO • NORFOLK. VA. • HENDERSON. KY •
Charter Member
• DENVER. COLORADO • BIRMINGHAM ALABAMA • VANCOUVER. B.C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 812 736-843*
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD. SOUTH HOLLAND. ILLINOIS 60473
SINCE I9O8
KVB, INC.
600 S. County Road 18
Minneapolis, "ill] 54426
Att: Jim Burlinjam
Kind of sample
reported to us
April 17, 1978
Sample identification
by
KVB, Inc.
Site B
OFFICE TSL. (31J) 264-117J
Sample taken at _____
No Purchase Order Received
As of 4/17/78.
Sample taken by KVB , Inc
Date sampled
Analysis report no. 71-13763
PROXIMATE ANALYSIS
As received
Initial Deformation
Softening (H=W)
Softening (H-V4W)
Fluid
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
5.31
7.79
33.35
53.55
100.00
13049
0.99
xxxxx
8.23
35.22
56.55
100.00
13781
1.05
FUSION TEMPERATURE OF ASH
Reducing Oxidizing
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
xxxxx
H It Cora Hilght
W li Con* Width
RAH:lau
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R A. HOUSE
CHICAOO. ILLINOIS • CHARLESTON. W VA • CLARKSBURG. W VA • CLEVELAND. OHIO • NORFOLK. VA • HENDERSON. KY • TOLED
Charter M*mb«r
•NVER. COLORADO • BIRMINGHAM. ALABAMA • VANCOUVER, e.c
-------
COMMERCIAL TESTING & ENGINEERING CO.
OENERAL OFFICES: 99* NORTH LA SALLE STREET, CHICAOO, ILLINOIS 90801 • AREA CODE 819 7a»-B4.34
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS (0473
KVB, INC.
600 S. County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
OFFICE TEL. (312) 284-1173
April 17, 1978
Sample identification
by
Kind of sample
reported to us
Sample taken at
Sample taken by KVB, Inc.
Date sampled
KVB, Inc.
Coal Test 33 Site B Old
No Purchase Order Received
As of 4/17/78.
Analysis report no. 71-13755
PROXIMATE ANALYSIS
As received
RAH:lau
Dry basis
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
1.31
8.03
34.56
56.10
100.00
13666
0.67
xxxxx
8.14
35.02
56.84
100.00
13847
0.68
FUSION TEMPERATURE OF ASH
Initial Deformation
Softening (H-W)
Softening (H-VzW)
Fluid
Reducing
xxxxx
xxxxx
xxxxx
xxxxx
Oxidizing
XXXXX H 1. Con, Might
XXXXX w " Col» wwth
XXXXX
xxxxx
Respectfully submitted,
COMMERCIAL TEST/G & ENGINEERING CO.
R. A. HOUSER. Manager, Midw««t Division
CHICAGO, ILLINOIS • CHARLESTON, W.VA. • CLARKSBURG, W.VA. • CLEVELAND. OHIO • NORFOLK, VA • HENDERSON. KV • TOLEDO.*
301
I Charier Member
VER, COLORADO • BIRMINGHAM, ALABAMA * VANCOUVER. B C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES-. »»8 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60801 • AREA CODE 312 716-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
' KVB, INC.
Shelard Tower, Ste. 1375
600 S. County Road 18
Minneapolis, MN 54426
Kind of sample
reported to us
zk
SINCE 19O8
OFFICE TEL, (312)264-1173
April 19, 1978
Sample Identification
by
KVB, Inc.
Sample taken at
Sample taken by KVB , Inc .
Date sampled
PROXIMATE ANALYSIS
% Moisture
% Ash
% Volatile
% Fixed Carbon
Btu
% Sulfur
% Alk. as Na,O
SULFUR FORMS
% Pyritic Sulfur
% Sulfate Sulfur
% Organic Sulfur
WATER SOLUBLE ALKALIES
% Na3O =
% K3O =
FUSION TEMPERATURE OF ASH
Initial Deformation
H n con« Height Softening (H = W)
w i> con. width Softening (H = VzW)
Fluid
% EQUILIBRIUM MOISTURE =
HARDGROVE GRINDABILITY INDEX =
FREE SWELLING INDEX =
Analysis
As received
2.75
6.77
35.17
55.31
100.00
13649
0.79
xxxxx
0.17
0.02
0.60
xxxxx
xxxxx
Reducing
2600°F
2700+°F
2700+°F
2700+°F
report no.
Dry basis
xxxxx
6.96
36.17
56.87
100.00
14035
0.81
0.09
0.17
0.02
0.62
xxxxx
xxxxx
Oxidizing
2700+°F
2700+°F
2700+°F
2700+°F
xxxxx
xxxxx
xxxxx
Coal
Test 33 Site B
New
71-13760
% Weight
ULTIMATE ANALYSIS As received Dry basis
Moisture 2 .
Carbon 7 6 .
Hydrogen 5 .
Nitrogen 1 .
Chlorine 0 .
Sulfur 0 .
Ash 6.
Oxygen (diff) 7 .
100.
MINERAL ANALYSIS OF ASH %
Silica; SiO,
Alumina, AUO,
Titania, TiO3
Ferric oxide, Fe,O3
Lime, CaO
Magnesia, MgO
Potassium oxide, K,O
Sodium oxide, Na,O
Sulfur trioxide, SO,
Phos. pentoxide, P3O5
Undetermined
SiLiCA vALUE — 85.37
BASE : ACID RATIO 0.13
T250 Temperature = 2900+°F
7 5 xxxxx
37 78.53
06 5.20
11 1.14
15 0.15
79 0.81
77 6.96
00 7.21
00 100.00
Weight Ignited Basis
54.14
29.99
1.65
6.60
2.00
0.68
1.23
0.47
1.15
0.62
1.47
100.00
Respectfully submitted,
ENGINEERING CO.
RAH:If
R A HOUSER. Manager Midwest Division
CHICAGO. .U.IMOW . CHARLESTON. W.VA. • CLARKSHURQ. W.VA . CLEVELAND. OHIO • HOBFOLK. VA . HENDERSON. KY . Ti
Charter M*mb*r
p DENVER. COLORADO • BIRMINGHAM ALABAMA • VANCOUVER. I.C.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA 8ALLE STREET, CHICAGO, ILLINOIS 80601 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO'
16130 VAN DHUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
f KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 55426
Kind of sample
reported to us
OFFICE TEL. (312) 264-1173
March 27, 1970
Sample taken at
Sample identification
by
KVB, Inc.
P- O. 321-15900
See Below for Identification
Sample taken by KVB, Inc.
Date sampled
Analysis report no. See Below
LAB NUMBER
71-12793
IDENTIFICATION
Multiclone Ash Site B Test 1
%SULFUR (DRY)
0.31
RAH:If
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
CHICAGO II • BILLINGS MT • BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG*WV • £££!*• OH '
MIODUSBORO. KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK. VA •**«*»*, KY •
Charter Member
DENVER. CO • GOLDEN, CO • HENDERSON. KY •
VANCOUVER. B.C. CAN.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 55426
Kind of sample
reported to us
OFFICE TEL. (312) 264-1173
March 27, 1978
Sample taken at
Sample taken by KVB, Inc.
Date sampled
Sample identification
by
KVB, Inc.
P. O. 321-15900
See Below for Identification
Analysis report no.
See Below
LAB NUMBER
71-12794
71-12795
71-12796
71-12797
71-12798
71-12800
71-12801
71-12802
71-12803
71-12804
71-12805
71-12806
71-12807
71-12808
71-12809
71-12810
71-12811
71-12812
71-12813
71-12814
RAH:If
IDENTIFICATION
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Multiclone
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
Test
Test
Test
Test
Test
Test
Test
Tests
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
2
3
4
6
7
8
9
11
17
18
19
20
21
22
23
24
25
26
27
28
& 12
Respectfully submitted,
COMMERCIAL-NESTING & ENGINEERING CO.
R. A Houser, Manager. Midwest Division
%ASH
36
51
49
31
34
68
44
46
34
34
37
23
47
26
20
38
43
52
52
39
(DRY)
.97
.37
.13
.97
.15
.36
.66
.11
.02
.76
.06
.36
.11
.07
.52
.02
.32
.28
.79
.83
m
Ml
Charter Member
CHICACO, II • BILLINGS. MT . BIRMINGHAM, AL • CHARLESTON. WV • CLARKSBURG, WV • CL
MIDDLESBORO. KY . MOBILE, AL • NEW ORLEANS. LA • NORFOLK, VA ',
AND, OH • DENVER. CO • GOLDEN, CO • HENDERSON
KY • VANCOUVER, B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAGO, ILLINOIS 60601 • AREA CODE 312 728-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 55426
Kind of sample
reported to us
Sample taken at
Sample taken by KVB, Inc.
Date sampled
OFFICE TEL. (312)264-1173
March 27, 1978
Sample identification
by
KVB, Inc.
P- 0. 321-15900
See Below for Identification
Analysis report no. See Below
LAB NUMBER
71-12799
IDENTIFICATION %ASH (DRY)
Boiler Outlet Ash Site B Test 7 21.91
RAH:If
Respectfully submitted,
COMMERCIAL TESTING & ENGINEERING CO.
R. A.
CHICAGO, II • BILLINGS, MT • BIRMINGHAM. AL « CHARLESTON, WV • CLARKSBURG WV •
MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK. VA •
'Midwest Division
Charter Member
OH • DENVER. CO • GOLDEN, CO • HENDERSON, KY •
UTT, KY • VANCOUVER. B.C. CAN.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 55426
Kind of sample
reported to us
OFFICE TEL. (312) 264-1173
March 27, 1978
Sample taken at
Sample identification
by
KVB, Inc.
P. O. 321-15900
See Below for Identification
Sample taken by KVB, Inc.
Date sampled
Analysis report no. See Below
LAB NUMBER
71-12774
IDENTIFICATION
Bottom Ash Site B Test 1
%SULFUR (DRY)
0.01
Respectfully submitted,
COMMERCIALIfiSTING & ENGINEERING CO.
RAH:If
CHICAGO, II • BILLINGS. MT • BIRMINGHAM. AL • CHARLESTON, WV • CLARKSBURG. WV
MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK, Vj
R. A. WouW. Manager. Midwest Division
Charter Member
, OH • DENVER. CO • GOLDEN, CO • HENDERSON. KY •
IE, KY • VANCOUVER. B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES: 228 NORTH LA SALLE STREET, CHICAQO, ILLINOIS 60001 • AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 55426
Kind of sample
reported to us
Sample taken at
OFFICE TEL. (312) 264-1173
March 27, 1978
Sample identification
by KVB, Inc.
P. O. 321-15900
See Below for Identification
Sample taken by
KVB, Inc.
Date sampled
Analysis report no.
See Below
LAB NUMBER
71-12775
71-12776
71-12777
71-12778
71-12779
71-12780
71-12781
71-12782
71-12783
71-12784
71-12785
71-12786
71-12787
71-12788
71-12789
71-12790
71-12791
71-12792
RAH:If
IDENTIFICATION
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Bottom
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Ash
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
Site
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
B
Test
Test
Test
Test
Tests
Tests
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
Test
2
3
4
6
8 & 9
11 & 12
17
18
19
20
21
22
23
24
25
26
27
28
%ASH (DRY)
91.79
94.60
80.94
90.31
75.82
96.01
94.34
91.10
90.00
93.54
93.31
74.24
85.78
86.44
90.11
82.43
93.56
76.61
Respectfully submitted,
COMMEROfffl TESTING .
ENGINEERING CO.
R. A. Houser, Manager, Midwest Division
Charter Member
CHICAGO, II
> BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON. WV > CLARKSBURG, WV •
MIDDLESBORO. KY ' MOBILE, AL • NEW ORLEANS. LA • NORFOLK. VA <
DENVER, CO • GOLDEN, CO • HENDERSON. KY <
', KY • VANCOUVER. B.C. CAN.
-------
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 ROAD, SOUTH HOLLAND, ILLINOIS 60473
OFFICE TEL. (312) 264-1173
April 18, 1978
KVB, INC.
Shelard Tower, Ste. 1375
600 S. County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
Kind of sample
reported to us
Sample Identification
by
KVB, Inc.
See Below for Identification
Sample taken at
Sample taken by KVBf Inc_
Date sampled
No Purchase Order Received
As of 4/18/78.
Analysis report no. See Below
LAB HO.
71-13766
71-13770
IDENTIFICATION
Bottom Ash
Test 32 Site B
Multiclone Ash
Test 32 Site B
SULFUR (DRY)
0.04%
0.08%
RAH:If
Respectfully submitted,
COMMERCIAL/TESTING & ENGINEERING CO.
R. A. Houser, Manager, Midwest Division—.,
Charter Member
CHICAGO, II . BILLINGS, MT - BIRMINGHAM. AL • CHARLESTON. WV • CLARKSBURG, WV • :LE
MIDDLESBORO, KY • MOBILE, AL • NEW ORLEANS. LA • NORFOLK VA • PIKI
• DENVER, CO • GOLDEN, CO • HENDERSON. KY •
• VANCOUVER. B.C. CAN.
-------
COMMERCIAL TESTING & ENGINEERING CO.
GENERAL OFFICES; 228 NOHTH LA SALLE STREET, CHICAQO, ILLINOIS 60601 » AREA CODE 312 726-8434
PLEASE ADDRESS ALL CORRESPONDENCE TO:
16130 VAN DRUNEN ROAD, SOUTH HOLLAND, ILLINOIS 60473
KVB, INC.
Shelard Tower, Ste. 1375
600 County Road 18
Minneapolis, MN 54426
Att: Jim Burlinjam
Kind of sample
reported to us
Sample taken at
Sample taken by
Date sampled
KVB, Inc
OFFICE TEL. (312) 264-1173
April 18, 1978
Sample identification
by
KVB, Inc.
See Below for Identification
No Purchase Order Received
As of 4/18/78.
Analysis report no.
See Below
LAB NO.
71-13767
71-13768
71-13769
71-13771
71-13772
71-13773
RAH:lf
IDENTIFICATION
Bottom Ash
Test 30 Site B
Bottom Ash
Test 31 Site B
Bottom Ash
Test 33 Site B
Multiclone Ash
Test 30 Site B
Multiclone Ash
Test 31 Test B
Multiclone Ash
Test 33 Site B
ASH (DRY)
83.51%
86.41%
91.29%
45.84%
23.90%
25.22%
SULFUR (DRY)
0.08%
0.03%
0.03%
0.07%
0.07%
0.08%
Respectfully submitted,
COMMERCIAL TESTING bENGINEERING CO.
R. A. Houser, Manager, Midwest Division
Charter Member
CHICAGO, It • BILLINGS, MT • BIRMINGHAM, AL • CHARLESTON, WV • CLARKSBURG, WV • CLE«MJ2|! • DENVER, CO • GOLDEN, CO • HENDERSON, KY •
MIDDLESBORO. KY • MOBILE, AL • NEW ORLEANS, LA • NORFOLK, VA • PIKEVILLE, KY • VANCOUVER, B.C. CAN.
-------
COMBUSTIBLES DATA SHEET
SITE
e- B>
Crucible
Number
Sample
Origin
Crucible
Weight
grams
Crucible S
Sample Weight
Post 110°C gms
Sample
Weight
grams
Post 750°C
grams
A Weight
grams
Combus
tibles
AVG.
/'f
fcfc
1 8- 0
AVG.
0-34.14.
13iR our
AVG.
\°\.
AVG.
IS-
I 8.
40,4
our
AVG.
IS
I8TT5&
1-1.
AVG.
n-
54-0
-rest * 4
AVG.
2. fa 4-2-3
C)
oo r
AVG.
AVG.
ISV/z-
^441
77 1
3
oo
AVG.
310
-------
COMBUSTIBLES DATA SHEET
SITE Agfa ft
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
AVG.
21-
t3.o
1
l«
AVG.
I^ClfcZ.
34,1
AVG.
1 '7
24.
AVG.
3-7^40-
3-7771
3.777Z
3.7773
3.7772-
8-7
resr »*7
AVG.
3. SfeZT-
SftSS
lp
AVG.
3 €3 76
243
ou-r
\«
V?
AVG.
IS
lS.ti7.sT
DOT
3,
AVG.
3.^233
3
oo r
i?
AVG.
Ide^ OUT
3
AVG.
3. 477. 4
4-
-------
SITE
COMBUSTIBLES DATA SHEET
Crucible
Number
Sample
Origin
Crucible
Weight
grains
Crucible &
Sample Weight
Post 110°C gms
Sample
Weight
grams
Post 750°C
grams
A Weight
grams
Combus
tibles
5"
AVG.
o.
,
-------
COMBUSTIBLES DATA SHEET
SITE ASfti* TEST-
Crucible
Number
Sample
Origin
Crucible
Weight
grams
Crucible &
Sample Weight
Post 110°C gms
Sample
Weight
grams
Post 750°C
grains
A Weight
grams
Combus
tibles
(I
cur
\8-ti4l
AVG.
20 .
\3m)
MfrtZ.
ovir
TEST
AVG.
IS
/g.9/fe7
.
2- /IS"/
1-6.
AVG.
I8.44/H
2C2
our
AVG.
. -7431
2Q -743T,
.!&
AVG.
|«.
D-4^1-l
AVG.
II
AVG.
AVG.
) 1-0*1*
/^^^
.113
2^7
-------
COMBUSTIBLES DATA SHEET
SITE A15tyft- T€ |