-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
/
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
i .. Flow Integrator x 350 Ib
^Excess Oxygen, %
DRAFT GAUGES
4.
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H20
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H20
Economizer Out Pressure, "H20
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
_ — —
Precip Out. Pressure, "H2O
H)verfire Air Press, "H2O
n
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Vle»refcN
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/octer'
int*(
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31
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31
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/z*^z.o
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^
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^ A
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111 *>!>
/, 4*5-3
co?5V-
zc
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
^Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
W/6
fc*wp*l*
TEMP RECORDER pb,,fi»W
1-Grate Thermocouple, °F ^
2-Grate Thermocouple , °F f^
3-Grate Thermocouple, °F ^
4-Grate Thermocouple, °F f\.
5-Grate Thermocouple, °F ((*.
6-Grate Thermocouple , °F pfefft
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
n<
I*M>\
~^fe
iti^.
*=/*£.
*/\
W/1A
wi.
IS*
^
^
\'13,
*f
-------
Sheet
of
KVB
TEST NO.
CONTROLS /£
Plant Master £t«f»t Vr**fC"
j
Feedwater »t«t>«- t"fe»r-
Attemperator 9T«dV rtU->|S&*
o
SF/AF Ratio
FD Damper
ID Damper
* Overfire Air
FD Set Point
AMPS
FD Fan Amps
ZD Fan Amps
* OFA Fan Amps
STOKER (west/east)
Jf Front Upper OFA Press "H2O
* Front Lower OFA Press "H2O
^ Rear Upper OFA Press "H2O
**" Rear Lower OFA Press "H20
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
-<*• Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
% OFA Fan Static Pressure "H2O
^
«'/C
*^&
X
hi
I'S
<^'
«•%£
*+
Ho
if/nt
& P.
1*/v<
*/!*•
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f/w
ri
%
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l>y$* J
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y v
-£- -• ^ • - .
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4/«'
*-A<
7
/1--
»r~
-------
Sheet i_of ._4_
KVB
NOTES
TEST NO: 37
<-
t«»v^
TEST NO:
if
3^
TEST NO:
TEST NO:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
t,t Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H20
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
4*
fe-2-78
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-/••
-2-1
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k<
0
if
1X131
til 8o/L
/«C^«
-------
Sheet
2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER.
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
, 12-Stm Coil Air Heater In, °F
J 13-Air Heater Air Out, °F
°(\*
<*!*
V*-
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tf
7lo
fyo
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vn
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tf
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L1J
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^
1+
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~~
, — . — . — . —
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
1<*
*>
(
0
X
•K
w
s
I2o
*•?
no
*•/£
"a/6
-f '
•'%.
*&
"•%.
y*>
tfrrt-
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w
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-------
Sheet l_of J_
KVB
NOTES
/• &- JUj**
*t
-A
TEST NO:
TEST NO:
TEST NO:
TEST NO:
:
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr: //
Stm Flow, Ib/hr: /Oi
FW Flow, Ib/hr:
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
tn Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
*//
c /7/?y
£••*•_> -/I <-.—
/Colc&A
V //
/H&*&
(oil %2-
n3^i^
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/o
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-3.^
<4.3
o
>/<**> f
//,
//://
//ft* ?
iof><./
/7L/°
-------
Sheet 2 of
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple , °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple , °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
-;*r
S7o
f&>
/O 0
^/
I*--*
7X?
7 ao
^S'5-
&S*
/^/V
710
//
/(?
/*
/o±-
J"o-
/^o
7 *r
S?s~
KS-S-
fTVsST
/t?90
;&*/*
7*0
<76$r
7^
;jj-
/A?
77
//S~
/oj-
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H20
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj, yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
3?
S^>
7/
^C
*\~
L/^
i
7s"
-Tfe
/OC
2?
//^
"•*y,<»
/V/J/.
f H.o
I/..0/
//->'->'
*.«-/
//? .0
>'•%..
fc.
I'l-a/,.
sM*'
y^
fc ^
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f~V
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Vo
VO
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1"
/,*-•*
ft
^"0
7.c
?JT
S>5~
/6
7^
6~7
/W
^f
./A
/-/. *-/
// •/.-/-
^CT.«s>//
y?j-.o
//<..
"^3.,-
n.°s
/{*•*-
^^
I?.*'/
/I**
(J>
ffj
i-f/
A'°i
t"
', 3 + s-
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr: /yc> HO,
rA
// 0 0
IIS-G (G
loc(G Vt
/?/^C0
5^Y f/y
?.r
- 3
2.2
J-Y
/.3
.7
-l.o
-2.1
-y. 3
'6-
KJ-^^I
( OTtvi/
f93 /O^
Z^S-JtfS
?.•*
"•3
H.i
/.JT
/V
. ~ D
~(e>.04'
7-0
cr>
2i.^
/2.: /X
/ / or-^ 37
/0*77/i
/^^s-f;
av'J^-rpo
7-j
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, CF (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, DF
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, DF
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
| 12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, "F
1
7 07
<^t1
W*
(X>~
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760
n7
6n
?t*
7^1_
•?£>J
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71 1
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10*4
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,
70?
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ffrr
ta±
sv
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S5"o
7^>
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itr
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7*X
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^13
Ct-s
-?<*
rs±
rti
-?&
1/0
I*G>
f?
74T
/ox
?JT
114
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H20
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
ASh Bed Thickness
Clinkers
OFA Fan Static Pressure "I^O
'/••/
+ e
(60 +
-T7
n-
¥*
?*-
-T?
/3/
3i
/j-s-
'«*/**-
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A- -/
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/-$•*<
y
»1 e> ^ue_
0 t"
-------
Sheet 4 _ of 4
TEST NO: t/^ - I U
KVB
NOTES
TEST NO:
TEST NO:
TEST NO:
//-'-S
TEST NO:
TIP
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr: lift.
: 1&.
FW Flow, Ib/hr
% Design Capacity:
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
i.. Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H20
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H20
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
k
l-ff-1«
f*jT€.f* 4-\u
i4>*s('
10:11,
1 170^-
ntet
I-LVI +
3 9 te»^4
—
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7
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mr^/
I/I3*1-)
^««T2.rt-
*r7?^T—
—
-------
Shee
of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stan Flow, Ib/hr x 1000 (.red)
Air Flow, % (blue)
'FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (redl
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, "F
1
&
tf*
«4<
4*
itf
W
7'<
m
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logo
/0<|0
K<
i
657
10
17K
I4T
$*<7
1i<
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I*
n
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V
t»
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l«fv
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^
7^*
»<7
i*
v<
1*
&<
^
t?t
\*f
l*<
If
i«t
1<
— • —
• —
—
— _^_
118
-------
Shefc
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H20
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
, Clinkers
OFA Fan Static Pressure "H2O
3«
fi
&
yi
J-4
&
&
*<
60
!H
t<
M
•7<7/«-'
»
ii*
i<
W
»Vn-
n
*
1*
1fi
V
1(
V
Sf
(>o
\n
a<
w
<>*'/«<
"Sfa
!*•/*•
P/iy
IV* /,$••
/"
l^ fa
Y
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, lb/hr: 27,7*O
Stm Flow, lb/hr:
FW Flow, lb/hr: /f2.£.37
% Design Capacity:
-------
Sheet
2 of 4
KVB
TEST NO.
PRESSURE GAUGES
_Z., i '" '
Feedwater Pressure, psig
_ _ — —
Steam Pressure Header, psig^
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
—
Air Flow, %
(.blue)
FW Flow, Ib/hr x 1000 (red)
/*>
nf
SH Out Temp, °F
..
AH Out Temp, °F
tred)
(blue)
•7*7
ft*
it
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
_——• —
3-Grate Thermocouple, °F
4*
n«
it?
#7
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
—
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
Pf
H*
ft
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
in
13-Air Heater Air Out, °F
Vl
-------
Sheet
of 4
KVB
TEST NO.
CONTROLS
Plant Master
fl
Feedwater
f*
Attemperator
If
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
t*
FD Set Point
t»
AMPS
FD Fan Amps
II «
ID Fan Amps
li.
it
U
OFA Fan Amps
IH
/t!
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear lower OFA Press
"H2O
Blr Hopper Reinj, Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H20
*/*•<
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
Vf4
Clinkers
OFA Fan Static Pressure "H20
122
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, lb/hr:
Stm Flow, IbAr: /77
FW Flow, lb/hr:
% Design Capacity:
TEST NO.
DATE
COAL
—-
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
22. o>
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
17^720
,. Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H20
-J
-.1
FD Fan Outlet Press, "H2O
-2*
Air Inlet Air Heater, "H2O
2-*
Air Outlet Air Heater, "H20
It
M
Stoker Inlet Pressure, "H2O
f.v
1-1
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H20
-27
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
^t-o f
Fan Out Pressure, "H20
Precip Out. Pressure, "H2C
Overfire Air Press, "H2o
4<
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stan Flow, Ib/hr x 1000 (red)
Air Flow, % (blue)
FW Plow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, 8F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F '
13-Air Heater Air Out, °F
6f\t>
fc
fye
I*
*7
ni
K*
7L*
&
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w
M
1v>
w
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w
Iff
/M
/ft
M
0(\+
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^.•w
1-7-1
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VI'
It*
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tf
Ifi
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U
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i..
ii*
- H
**
t>
fo
57^
St7
5bt
ft
Ti*
**<
*(
II*
^
/7f
lol>
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
fl
Feedwater
Attemperator
SF/AF Ratio
ft
FD Damper
ID Damper
Overfire Air
JOCt
FD Set Point
4L
AMPS
FD Fan Amps
ID Fan Amps
-43-
1.1
17
22.
OFA Fan Amps
M*
STOKER (west/east)
Front Upper OFA Press "
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/eas
~^A»
Ash Bed Thickness
V
jii
r
Clinkers
OFA Fan Static Pressure "H20
13-S
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
_
lYt
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
1 • — —
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
tw Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H20
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H2O
Dust Collector Out Pressure, "H20
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "I^O
Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "^O
— • __— — — —
*
6-20-76
EWstviett 1
4,^W «>.f.,
/3-.
-tt
'^.4
-?•<
o
1>
0\4 VvjVo»»
l<^0
IZ»7»fc
liOfz-
7*T7«4e
^BiSf
-.1
74
2*
Z»
1.^
-.7
-2.^
^,S
-V-»
7-*
t
2*
lc-.fi
IZI7»
\\<*V
Z11932-
4^^^b
—
-.1
z-f
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t.$
J,V
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-it
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»
11
itm
itii««»
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^c.Vft
. •—
-;!
**
;..
/•t
)•*
-7
-2<
,*f
-U
?••
o
17
H:*^
12.1832.
lin#f
2^9/9«
«i^trrv*.
**~
-------
Sheet 2 °f_i_
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
4>
Steam Pressure Header, psig
Steam Pressure Drum, psig
<*%<
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
Air Flow, %
(blue)
•57
FW Flow, Ib/hr x 1000 (red)
n*
SH Out Temp, °F
(red)
AH Out Temp, °F
(blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4 -Grate Thermocouple, °F
(.fir
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
te
9-Flue Gas Boiler Out, °F
I5I
10-Flue Gas Economizer Out,°F
H7
I
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
44.
13-Air Heater Air Out, °F
1*7
108
(If
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Danger
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "HjO
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press "H2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
$•?
tf>
%
f v
•n
^
if
;»«»t
fe>
irt
74
/{1
«'/*•
»'A
!"%•<
,*'/*•
itXt.-
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^^
,
&
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V
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17
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r
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&
&
&
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k
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"y*.
1*
**/«•'
1"
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V
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r*
r»
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5?
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\oft-V
bo
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1"
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1**
"/'-
J"
IMTKA'
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stra Flow, Ib/hr: ~7
FW Flow, Ib/hr: 3£
% Design Capacity: '
TEST NO.
DATE
COAL
DESCRIPTION
TIME OF READING
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
^A Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace Draft, "H2O
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H20
Air Outlet Air Heater, "H2O
Stoker Inlet Pressure, "H2O
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
Economizer Out Pressure, "H2O
Air Heater Out Pressure, "H2O
1 Fan Out Pressure, "H2O
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
f»
^27-7*
&sfr** /,
6*sc«o«. \
to ».*>*.
&**
/2
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, lb/hr x 1000 (red)
Air Flow, % (blue)
FW Flow, lb/hr x 1000 (red)
SH Out Temp, °F Cred)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple , °F
2-Grate Thermocouple, °F
3-Grate Thermocouple , °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, 'F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,°F
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13-Air Heater Air Out, °F
1"
*\<
1"
nf
<«
iv*
W
7>
1$
l«7
>
U*
L
W
/r»
nf
i*
/»>
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,
ft
5f
V #
IH y
^
57
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gv»
-t?
&«
no
a
— 1^° —
^w^
•I?
1<°
l^
{V
•
130
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj. yes/no
Mech Hopper Reinj. Press MH2O
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H20
V*
r*
K
«
«
V
t&>
i>
frf
16
(Ik
— *-/=•
TM '
W. '
<*fa
% '
* i *
<+A~
1"
*fa
T"
' <«£•»
•>•
if.
2V<
!
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in
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X» %
**/ *X'
V/K V
%* */i'
%* +K-
% %-
Mt>
% %
T
^'^• u*
U
W
%
'%•
Wl
+4*
*A-
?•"
'%•
1"
i
?,$•
loo
|H
*/K*
^>
^if-
K5^,
^x<.
^
2?»
/•
^
-X /*•
*y^
*-/^<
v^,
'••/?..
V /(.>
<'/<•>
2V
-------
KVB
CONTROL ROOM DATA
TEST SITE C
Coal Flow, Ib/hr:
Stm Flow, Ib/hr:
FW Flow, Ib/hr:
% Design Capacity:
//
TEST NO.
f
DATE
COAL
p.t^»
DESCRIPTION
Uw
TIME OF READING
-*'
West Coal Counter x 400 Ib
East Coal Counter x 400 Ib
Stm Flow Integrator x 350 Ib
t.. Flow Integrator x 350 Ib
Excess Oxygen, %
DRAFT GAUGES
Furnace, Draft, "H2O
-.*-
FD Fan Outlet Press, "H2O
Air Inlet Air Heater, "H2O
Air Outlet Air Heater, "H2O
,1 4
Stoker Inlet Pressure, "H2O
•f
••f*
Boiler Out. Pressure, "H20
Dust Collector Out Pressure, "H2O
4?
Economizer Out Pressure, "H2O
-2o
Air Heater Out Pressure, "H2O
-21-
Fan Out Pressure, "H2O
41
Precip Out. Pressure, "H2O
Overfire Air Press, "H2O
-------
Sheet 2 of 4
KVB
TEST NO.
PRESSURE GAUGES
Feedwater Pressure, psig
Steam Pressure Header, psig
Steam Pressure Drum, psig
STRIP CHARTS
Stm Flow, Ib/hr x 1000 (red)
Air Flow, % Cblue)
FW Flow, Ib/hr x 1000 (red)
SH Out Temp, °F (red)
AH Out Temp, °F (blue)
Steam Pressure, psig (red)
TEMP RECORDER
1-Grate Thermocouple, °F
2-Grate Thermocouple, °F
3-Grate Thermocouple, °F
4-Grate Thermocouple, °F
5-Grate Thermocouple, °F
6-Grate Thermocouple, °F
9-Flue Gas Boiler Out, °F
10-Flue Gas Economizer Out,cF
11-Flue Gas Air Heater Out,°F
12-Stm Coil Air Heater In, °F
13- Air Heater Air Out, °F
»•
W
11<
[e>o
?*
lit'
>
1»o
tf
•?<•
f|i
*
Tfo
w
m
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l»<
V
II f
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si< 4t
»> 57*
ft» ^
1* I*'
1* )!
\V> \1*
Ifa Ttf
*< tf
& 1$
fy* 4*
» «^»
9 $
&fy tip
"* ^
&•
IX
**>
*
u
\\<
ii»
^
&
L6
v>*
•p
&
f
^b
5u<"
£?o
/Oo
2?
!/«?
77*
b^D
^^
^o
^
f^O
[) r»
ca
fT
-------
Sheet
of
KVB
TEST NO.
CONTROLS
Plant Master
Feedwater
Attemperator
SF/AF Ratio
FD Damper
ID Damper
Overfire Air
FD Set Point
AMPS
FD Fan Amps
ID Fan Amps
OFA Fan Amps
STOKER (west/east)
Front Upper OFA Press "H2O
Front Lower OFA Press "H2O
Rear Upper OFA Press "H2O
Rear Lower OFA Press "H2O
Blr Hopper Reinj. Press "H2O
Blr Hopper Reinj, yes/no
Mech Hopper Reinj. Press "H20
Mech Hopper Reinj. yes/no
Relative Grate Speed west/ea
Ash Bed Thickness
Clinkers
OFA Fan Static Pressure "H2O
i
<•
1<
K
tf
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1004
k
irt
1*
;*v
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/
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ttyrf.
•*'/<.'
V*
rtfa
y
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r f »
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2i-*
^
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^
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^
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to
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v<"
<2>
3^7
-------
SECTION 2,0
PARTICULATE DATA
PAGE
2,1 PARTiCULATE DATA SUMMARY 136
2,2 PARTiCULATE DATA 142
2,3 PARTICULATE LAB WORKSHEET 190
-------
PARTICULATE DATA SUMMARY
PART I
LOCATION
TEST
Tptal
Mass
ry Gas
Volume
ft3
Liquid
Coll.
ml.
Baro.
Press.
"Hg
Static
Press .
"H2O
Pitot
AP
"H20
Orifice
AH
"H2O
Stack Gas
Temp.
°R
Excess
02
ampling
Time
Nozzle
Dia.
in.
Factor
n.d.
Factor
SCF/10%TU
MW
g/g mole
/ D.r
- . 78
0.273
0.374
7.3
2-1. 4 '(
&&*
41
/». 2.
72
S-f. 39"
43
. 22-7
72
. s/z
. esi
fez*
O.C
. t>
84*
e.i
,3/Z
21.28
>; *
-. f «
>. 234.
0.
1.1
71
212.
037
toO.C. £2£.9
78
0. #47
1.1
.3/2
2-1.3°
21.17
643.
73.
LI
•72.
.312
9/7
2-1.30
fcj //&.*
r^
S-2£. 8
S»
>. 602
1.1
77,
3-17,
937
2.1. /I
21,3*7.4
&-241
0.6/7
e-1
72-
I2
<°
77
- .68
a. 0s*
.1
72.
.3,12-
.en
-.71
72.
.312.
,837
-. 7°
7.9
72.
.312-
. 9/7
44.ll>
?
a. 62.
72.
31?-
.037
98 '2
94.1
l.o
.312.
-.64.
0.32.
S.7
72-
,312.
24,0*6,
1 -2*
SI. 3
21.47
*.?./
72-
. 9*7
»/?
41.
9-7
72
.312.
/A/2.3
81
Z-1.17
0.3/4
9-1
7Z
3/2,
.8/7
767.°
'. Jig.
S-3
6.24S
8.7
7-2
312.
97
£-3*7
0.G/3
874
e.k
72.
.9/7
6.3-7-2.
1 1.*
317-
937
rev.
-------
LOCATION:
PARTICULATE DATA SUMMARY
PART I
TEST
NO.
Total
Mass
in gin.
Dry Gas
Volume
Liquid
Coll.
ml.
Baro.
Press.
"Hg
Static
Press.
"H2O
Pitot
AP
"H20
Orifice
AH
"H20
Stack Gas
Temp.
°R
Excess
Sampling
Time
min .
Nozzle
Dia.
in .
Pitot
Factor
n.d.
Fuel
Factor
SCF/IO^TU
Flue Gas
MW
g/g mole
4^7. /
-.79
#37
72-
£>. 3/2.
.8/7
8.6
72
.037
Zf.SB
~ ,61
/./&
7Z
.817
24614
37, /3J
0.326
0.762.
.7
72.
0- 3/2
2*8.72.
Z^D.C
32.4*7
- .71
tfVS
gV7
G. 3/Z
.817
2S.77
3T./73
37.1
-.69
0./1
9.6
-72
0.312
,837
. es~
61.7
23.70
-.66
032.
72.
0.241
3^,783
48.
- l.s
6.90
f-f
72.
0.212.
2.8. 79
2* C-C
. 7
38-
- .ft
72,
.0/7
- /. z
72.
0. 3/2
.037
27
1037.6
37.
f/
23.5S'
-.#2
0.4-2*
9.7
72.
0.241
. 47
o.sl
f./
72.
917
9*2-0
1 ffit
0. 35-
72.
.837
9SZQ
Z10.C.
733-9
'.*'
72
#17
9,9Z3.7
70. e
- .77
72.
.437
Z/o.Z
to
2-7.46
72.
9*2.°
26-7]
& 6K
10,3*7.7
Hi
2,1. 3t>
#•772.
7Z
.837
Ztf.fft
3bb.
-------
LOCATION:
PARTICULATE DATA SUMMARY
PART I
UQ
TEST
NO.
4I8IX
41 O.C.
4T.9¥tf
Liquid
Coll.
ml.
5-/-^
36
66.S-
08.2,
<&•&
73.4
Baro.
Press.
"Kg
2^.2^
Zf.^c
3^.5-7
21.57
•&.-H
2#*/
Static
Press.
"H20
-.77
--77
-/*
-.7^
-^6
-,W
Pitot
AP
"H20
^./^
^.2^3
*.J.Z&
Orifice
AH
"H20
^•te-7
0.2*2
o.W7
/,£•?
0-S73
0,723
Stack Gas
Temp.
°R
/(?tj&
«?S»
/& &/
9
/O&o
$3?
Excess
02
// 3
//V
y.v
^.5"
^ /P
^j 7
Sampling
Time
min .
72-
72-
72-
72-
72-
72-
Nozzle
Dia.
in.
*..*#
0.241
0. 3/3?
0. 3/ H
e. 3/ ۥ
6.3l#
Pitot
Factor
n.d.
*«*7
&.&i7
0. fef ;3 7
O.W7
e.Vtf
*.&7
Fuel
Factor
Flue Gas
MW
g/g mole
2*/'
.7^, ^
«2f. JJ
Pf. J^
S
-------
Location
PARTICULATE DATA SUMMARY
PART II
TEST
NO.
LOAD
02
CONDITIONS
EMISSIONS
lb/106BTU GR/SCF LB/HR
Moisture
Stack Gas
Velocity
Ft/sec
Stack Gas
Flow
SCF/sec
Isokin.
. 0
7-3
6
42.0
. 7&7
3*- $7
/I 77
11
#•?
/e. 2.4-8
4. 14
37. Vf
n
8.1
e.
. 31
-57.
f./
'in j e<,•&"*)
6-
3 If.
10
/e 2.
6-01
37.
// D.c.
/Ob
&-SI
1$
n
2.
jr. 6s
7. 77?
/23/
OC.
&• 6>&>-
13 0-t.
0.
7.(f
36.
1st
14
Upper
1, SI
122-i
D.C.
C,
7.41
£>. 32 7
31. 2 '£
17
22. &2 7
. (23
J3-32-
47
O.C.
6. f
It. B/«
9-7
/0.47
-------
Location ABM*
PARTICULATE DATA SUMMARY
PART II
#15900 Rev.
-------
Location
PARTICULATE DATA SUMMARY
PART II
TEST
NO.
41 Bl*
4/d.c.
42. 8//?
4? DC
4l&tf
43 /X
LOAD
3.-S*. 1
35-1
£c i
6c-./
41 4
474
•?
/1. 3
//.y
?^~
q &
f.7
CONDITIONS
/,
It
/'
//
II
EMISSIONS
Ib/lO^BTU
/6./14
0.S3&
27. ^7
7^72.
^c.206
0.60S-
GR/SCF
^3/7
e,/ 75"
//. w J
0,418
7. £f7
Q.2&2-
LB/HR
•2-7 &£~
7S~
6?//f
3i.^(?
47.°l
4S~.3«
3S~.
-------
PARTICULATE
DATA
Lea* Check Rate
ft3/min
Vac
in. Hg
ISOKINETICS -
TEST NUMBER /
DATE V-X
OPERATOR "^,/4,
FUEL
SITE
PROBE LOCATIOM
ample
oint
Time
METER CONDITIONS
A
AH
Meter Reading
TEMPERATURES , * F
Stack
Probe
Oven
Impingers
In
Out
Meter
o2.%
Vac.
/f*
3.8
39
31
29
32-
/?**-
/e
2.**
.21
27
ftl
3./0
73
/**
31
32*
e
.27
68
"2-3
63
27
•_01_
7?-
4.6
2.6
7-2.
Average
.273
.37
**•
Vol.(End) Vol. (Start) AVol.(ml)
Cpitot
Stack Presl.
Percent
fta. 22. °** p*tlck
^neter
Barometric
Pre»ure
H0 -
Noz(Ideal)-
Noz(Actual)-
11
12
Silica
Gel .
Total
g (Start)
Total Vol. H2O
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
Vac
in. Hg
ftj/min
Before
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATIOH
Stiff-
ample
oint
Time
METER CONDITIONS
&H Meter Reading
TEKPERATORES , °F
Stack
Probe
Oven
_ln_
;
Out
Meter
Vac.
2J3V-
3-2*
63
•*L
2/4*.
360
I
/e
33^
62-
3-3
.23
53
3- 9
/If.'/*
4-3
3-7
63
3.3
2./SD.
.2.3
34°
to
t
«4 qlEnd)
Silica
Gel
g(Start)
Total Vol. H2O
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
Vac
in. Hg
ftVmin
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TElVERAtURES . "F
ample
Point
Time
METER CONDITIONS
APS AH
Meter Reading
Stack
Probe
Oven
impinqers
In
Out
Mete*
o,%
Vac.
.21
.60
3-9
.60
2-70
f*
23
,5V
73
*/.*.
*31\~
Stack Press.
In. Hq-cauqa
rarcant Oj
B*rom«tric
Pressure
HOg
% H,0
T.tack '
AP
Noz(Ideal)-
Noz(Actual)
• 1
t2
13
-.3/2-
•V #IAe&tA#t£.
Vol.(End) Vol. (Start) flVol.(ml)
• 3£~
. - 3
O . G> . Cf
Total «38
*4 q(End)
Silica
Gel
g (Start)
Total Vol. H20
'43
-------
PARTICULATE
DATA
Leak Check Rate
Vic
in. Hq ft3/
ISOKINETICS
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
-/- 78
TElVERAtORES , *F
ample
oint
Time
METER CONDI"' CONS
APS
Meter Reading
Stack
Probe
Ovan
Impinqers
In
Out
Meter
oa.%
Vac.
-73
2*
. 92-
5
7.*
.92
1*
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b
/*Z
go
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/. oz.
38S~
7$
8
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33
. 13
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II
,27
. 33
90
7,7
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2.?*
. 73
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3*3
2-70
/'*
ff*
f.ol
39
/a. 0
/V
3?
•2-80
//.*
.37
390
ffe
. 0
-2.80
ffs
/O."
.3*
.2*
/62J. e f
3&_
.-27
39'
2,60
'I
t-i.
2-4*
fftr
f 3
.2.3
24°
95-
£
ff.e
Average
.9s?
30k
METER VOL.
START
SAMPLE VOL
ter
3^14,2/3 Pstack -
" Nomograph Setup
I1™*., - C
£._ Vol. (End) Vol. (Start) AVol.(ml)
11 /4* - /ff& . 6°
CpitOt
Stack Press.
In.Hg-Cauge
Percent Oj ™
Barometric
Pressure
Tmeter
AHg
Noz( Ideal)-
Noi (Actual)- « 9*
*3
o
3(End)
Total ~7&
g(Start) Agrams
SU^t /*°'7 - M&~
Total Vol. H20 *^-7«l
-------
PARTICIPATE
DATA
LeaX Check tote
vac
in. Hq ft3/»ln
I30KINETICS •
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES,
ample
Point
Time
METER CONDITIONS
&H Meter Reading
Stack
Probe
Oven
Impingers
In ^Mf
Meter
oa.%
Vac.
•zf
JT7
6.3
f
60
60
>2L
70
6*
6.3
t*
32.0
33*
•£23*-
?.*
7*
£3
. o
.11
69
33^
•70
3J_
36°
7°
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*?
7°
62.°
.41
73
. n
.•2.*
\
3**
•73
6.3
25*
±23-
2-°
6trt>
7,9
72-
*<>
2.1°
4*
90
.67.
33°
to
70
63-
7*
6.0
Average
,234
,/*
VOL.
JAMTLB VOl.1^ "'
7f
/f
%t3
Ho»oqr«ph S«tup
Iff. Vol. (ted) Vol. (Start)
cpitot
Stack Pr«i«.
In. H9-Gaug*
-.-fir
T«rc«nt 0? *
Barometric
Pra»»ure
P»t«ck -
AHg
Moi(Id.al)-
Noz(Actual)- t
•1
13
Sillc*
Gel .
/«*
/^j
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
TEST NUMBER
Sampling Time
Per Point, Min
Vac
in. Hg
ft3/min
Before
After
OPERATOR ff, X
FUEL
SITE C.
PROBE LOCATION^
F
ample
Point
ime
^^:TER CONDITIONS
Als
AH
Meter Reading
TEPlPERAtURES, °F
Stack
robe
Oven
Impxnqers
In
Out
Meter
oa.%
AL
*°
3
37
27*
72.
72
? 2.
9. :
73
e
.02-
. f 7
/2Z,
72
73
73
8°
7V
•°
27*
27
2-*°
'/e
S3?-
7S
77
2.?*
37°
/3S
3Z
. f
32
.13
.13
7°
32
1'
go
/°
.HI
H
Jtro
72
.2°
72
Average
.3*
.341
METER VOL.
START
SAMPLE VOL
Stack Press.
In. Hg-Gauqc
Barometric
/*&*«..
rmeter
COJ4 pstack
Tmeter
AHg
* H,0 »
lomograph Setup
C "
Tstack
AP
Noz(Ideal)-
Noz(Actual)"
Imp. vol.(End) Vol. (Start) AVol.(ml)
11
• 2
*3
Total t> fr
,(End) g(start) Agrams
Total Vol. H2O
-------
PARTICULAR
DATA
Check Bate
ISOKINETICS
V.c
In. H
PROBE LOCATION
TEMPERATURES, "F
ample
oint
Time
METER CONDITIONS
A H Meter Reading
Stack
Probe
Oven
imQinqers
In
Out
Meter
Vac.
.27
f*
.11
. 97
9*
.24
6/0
34°
62
12-
. 22
3s*
39
«*
.31
fo
.19
6*
2277- 77
4.9
,-77
2.4
78
±1
44
2-4
22,9*31
32^
7*
6/e
360
.3
39*
•9*
2.2-91.
3?
1-2.92
62*
39*
.-74
620
f'
63*
37"
.It
3**
35*
7*
7*
34°
6*0
3°.
. 73
76
75"
.26
6*0
32*
33S-
ffsT
S/*
32*
32*
7.9
Aver a 36
.to
t/3.7
VOL.
srwrr
SAMPLE VOL.
ffi
3
Monograph satup
* C
'•tack -
cpitot
,137
Stack Prea*.
In. Hq-G«ug«
Pwontt Oj • I
BaropMtric
Fnuur*
Zf.5*
£._ Vol.(End) Vol. (start) Avol.(»l)
ii /*So . /*e . t/o
« "3 -_
M / -
% B.O - Mo« (Actual)-
Total
M »(Endl q (Start)
Silica ^, «.
Gal .
g
Total Vol. BjO ^^ml
-------
PARTICULATE
DATA
Leak Check Bate
Vac
in. Hq ft3/min
ISOKINETICS
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
ample
oint
Time
METER CONDITIONS
A PS AH Meter Reading
TEMPERATURE S7~* F
Stack
Probe
Oven
In Out
Meter
Vac.
,2* .
3**
/Z*
. 77
3*+
TiT
6.0
T 7*
78
6.
. f f
-7.1.
-ff
/zs
7-5
38
/•7*2. . 2. 7
¥/*
3*+
ff.6
00
.33
ff
-------
PARTICULATE
DATA
Sampling Time
Per Point. Hln
Leak Cheek Rate
Vac
IP. Ho ft3/
1SOUBETXC8 -
rz-
Before
After
DATE
OPERATOR
FUEL
SITE
PROBE
Sample
Point
Time
METER CONDITIONS
s AH Meter Reading
TEMPERATURES , "F
Stack
Probe
Oven
Impinqers
In
OuV
Meter
v%
Vac.
\
.77
63-
7-0
.27
6*
6.3
33 »
60
6°
fi«i*3
.**
23/7.
£*&
2^0
62.
'•7
\
t*
63
.11
63
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.48
2322- 8S
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6*-
61
•31
71
6/0
62,
7.8
.2*
61
63
7.2
20
41
2320. 37
68
. 60
60
60
/I.'3S
.31
2,8°
;
•70
68
.30
2333. tf
61
«. z
.5V
62.
t.B
.22,
61
-71
.73
2338.
-71
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61-
73
2.9*
.11
2343.
2.40
e.7
Aver a 36
aph Setup
Si tot
Stack Press.
In. Bo-Gauge
Parent Of
• |
Barometric
Pressure
'meter
'stack
BjO -
Tataek
AP
HozddealJ- "
Meal Actual)-
150
lap. vol.(End) Vol. (Start! Aval.(nil
•i S*/0 - *** - *f°
6
»3
*4 q(Endl
. ___0_
Total V£
9 (Start) Aqram
- *•
ttetal Vol. H^ «3"«J»ftl
-------
PARTICULATE
DATA
Lea* Check Rate
ISOKINETICS -
Vac
in. Hg
ffvmin
TEST NUMBER / 2-
DATE jP-V
OPERATOR J~,
FUEl
SITE C
PROBE LOCATION
Sample
oint
Time
METER CONDITIONS
A Ps
.27
AH
.76
Meter Reading
TEf\PERAtURES ,
Stack
Probe
^ go
Oven
Impinqers
In
Out
•70
Meter
Vac.
.3*
7.
.41
3*
72,
,3*
-78
/,/2 , 75V.
e*
,32,
.f*
39
(Z*
6-7,
.9*
/2
Percent 02 *
Barometric
Pressure
%y. efl-
Pstack
AHq
Nomograph Setup
C
Tstack
AP
Imp. Vol.(End) Vol. (Start) AVol.(ml)
»1 /S"2- - /** - S~"3-
NozddeaD-
Noz(Actual)- « 3/2-
*4 g(End)
Silica
Gel _
a(Start)
otal O •
Total Vol. H,o
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
in. Hq ft-Vmin
Be fore
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES, 'F
I
ample
Point
Time
METER CONDITIONS
A?s AH Meter Reading
Stack
Probe
Oven
Impingers
In
Out
Meter
,«*
Vac.
. 61
77
(. 2.
23
.SB
23
STa
.bo
60
5-7
Z3 $7.
ffo
67,
**. 6
t?. 03
62,
7*1
67
. 22-
Z37/. S-3
$-#
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40
63
2373.37
2-70
ZZ74.1t
7.3
,37
77.
7°
6?
,_££
2371. 47
2.3*1.
,275-
270
7*
7
.42.
22 92 . 6**
•7*
7*
23*7- 92-
2.-?°
•7°
23 91.
3/0
70
-72
,•2.1
3/o
•72
te
Aver a 36
METER VOL.
SAMPLE VOL
3Z^
cpitot
Stack Pres«.
In. Hg-Gauge
Percent Oj
BAromctric
21.42.
Monograph Setup
p»et.r ' C
Iitack - T«t»ck
*««t«r - AP •
AHg - Nor(Ideal)-
% H,0 • Noi(Actuail)- • 3>^
Vol.(End) vol. (Start) flVol.lnl)
Total
14 g (End)
Silica
Gel ,
q (Start)
Total Vol. H20
-------
PARTICULATE
DATA
Leak Check Rate
ft3/min
ISOKINETICS -
Vac
in. Hq
Before
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
O.
Sample
Point
Time
METER CONtXTIONS
A PS
.22.
AH
£2.
Meter Reading
Stack
TEIVERATURES, *F
Probe
Oven
Impingers
JJL.
o^
Meter
Vac.
• IS
Ben?
75-
V
3*$-
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go
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7*
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go
/*.£'
it
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(2.
27
fo
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.26
39*
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7°
79
87
J/ffD
ffio
7 7
32-
13
27"
/3*
.7V
7. 60
ft
-/v
./f
9*
.2*7
.75-
Average
4/7.
METER VOL.
SAMPLE VOL
/*//.
Nomograph Setup
Vol.(End) Vol. (Start) AVol.(nl)
*;pi tot
,f/7
Stack Press.
In. Hg-Gauge
•".'J
Percent OT *
?*"#t,o
Barometric
Pressure
22*2
Tmeter -
AHg .
% H0 -
'stack
AP
NozlIdeal)-
Noz(Actual)- « 3/2-
Silica
3(End)
/^2
g(Start)
Total Vol. H2O
Agrams
7^7^
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Rg ft3/
ISOKINETICS = /O3. 2*
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCUTION
Sample
Point
Time
METER CONDITIONS
APfi
AH
Meter Reading
TEMPERATURES, °F
Stack
Probe
Oven
Impxnqers
In
Out
Meter
o2,%
Vac.
-74.
/21
3-3
27
.67
•3408.03
3/0
5-3
.-24
. 97
V.e
.26
. 93
,-ze
24/3.
270
62
,5-7
. 5V
62
.63
24/7.4-2.
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76
.26
.61
270
68
.49
.e 3
ts
68
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60
3.3
.33
.83
3/0
£.8
.68
62
5:9
243*
6/0
.32
2431. 39
3/S-
7/
. 8
.32
2433. 44
25*
7"
/. e
.2t>
.14
. 3/
•72
6.
.22-
2437. *4
.73
78
-244-2.se
270
7-8
t.-z.
2.*!
60
73
7,1
"2446 .
So
^78
Average
METER VOL.
SAMPLE
OS"
VfW
ft3
Nomograph Sotup
Tstack
In. Rg-Gauge
Percent
Barometric I *»>*•*
Pressure ^
» HjO
'nater °
'stack -
Tn»ter
Hoi(Ideal)= '
Icp, Vol. (End) Vol. (Start) AVol^dnlL
,ee .
12
«3
Noz(Actual)- • 3/2
Total
g (Start)
Silica
Gel .
/«?.$"
154
Total Vol. U20
-------
PARTICULATE
DATA
Leafc Check Rate ISOKINETICS - A^ l\
Vac
in. Hg
ft-Vmin
TEST NUMBER /
DATE .5"-
OPERATOR
FUEL
SITE
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
A P
,22-
AH
.12,
Meter Reading
Stack
TEltPERAlURES , "F
Probe
Oven
Impinqers
-In.
Outl
Meter
Vac.
,3*
39"
ff-z
,?*
. 36
270
70
/g
/,*/
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31
2,70
•73-
,38
ffo
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7.2
,38
77.24-
•7°
7?. 3 8
70
73-
. 71
39
12-
.72.
•79
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22
.62-
9°
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ffz
. 32.
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38o
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7.0
A/2
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.33
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38°
3V
. 73
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,32
: /?
38°
275"
go
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So
/3S-
28
/3S
;
2.2°
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70
Aver 096
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39°
METER VOL.
STftRT
SAMPLE VOL
\+t /. oS-/b
Nomograph Setup
ft
-s-J.
cpitot
.9n
Stack Press.
In. Hq-Gauqe
- , W*^«
percent 0? "
Barometric
Pressure
zf./z
Allg
Noz (Ideal )-
Noz (Actual)
r-r-
Imp. Vol.(End) Vol. (Start) AVol.(ml)
,1 /SV -
»3
/*T> -
e?
#4 g(End)
Silica
Gel .
Total
g(Start) &grams
Total Vol. H0 ' ' J»l
-------
PARTICUZATE
DATA
LeaX Check Rate
Vac
in. Hq ft3/min
ISOKINETICS =
TEST NUMBER_
DATE
OPERATOR
FUEL
SITE
-/*- 78
PROBE LOCATIOM &£./? fW
ample
oint
Time
METER CONDITIONS
APfi
AH
Meter Reading
TEMPERATURES, «F
Stack
Probe
Oven
Impinqers
In
Out
Meter
o2,%
Vac.
,32.
z4S3.ee
-70
.24
27*
257?
573
,23
68
-78
.-2-1
2,00
78
5:2.
.5-7
2.60
So
77
22
•270
77
S-.3
.-20
63
•73
.•20
63
76
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72.
73
£.8
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2461.* 2.
275-
73
6
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12.
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/yr/7
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2473.
73
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6.8
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2475. 37
3.70
72
6-3
•2476.
6-ov
68
72.
320
3f<>
72
5.2
36V
7..S-
. 41
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. 3"
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7/
578
$
7*_
3L
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7,2
.70
•Z488. 77
•260
4*
If
ZS"
Ztffo. SS
7°
-2412 .327
-7°
Average
.tl
METER VOL.
SAMPLE VOL,
2V5-A
cpitot
.937 -.
Stack Press.
In. Hg-Gauge
Percent 07 •
Barometric
Pressure
'meter
Pstack •
Tneter a
AHg =
% HjO -
Nocoqraph Setup
C
n
Tstac* "
AJ> = '
Hoz(l
d . «?
Total
Aval.(ml)
^tf
O
^r
«4
g(Start)
Gel
. /o- 3
Total Vol. BjO "^<^al
-------
PARTICULATE
DATA
Leah Check Rate
V.c
in. Hq ftvinin
ISOKINETICS -
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PRCBE LOCATION
ample
oint
Time
%isi
METER C0t> jITIONS
23
AH
Meter Reading
TEWERATORES , «F
Stack
Probe
Oven
Impinqers
In
Out
Meter
oa.%
Vac.
>1L
. 13.
90
3.?
88
7.
.32-
08
.32
/32.
8.3
38
1.2
39
83
'23
.38
96
8*
. 7/
7.9
n
86
/*/1 Pstack • Tstack
Tmeter "
AHg
AP
Noz(Ideal)-
Noz (Actual) -
Ei Vyl. (End) Vol. (Start) AVol.dnl)
•3
14 qlEnd)
Silica
Gel _?'
Total
q(Start) flgr
Total Vol. H2O ' •'
-------
PARTICUIATE
DATA
Leak Check Rate
Vac
In.
ISOXINETICS i
TEST NUMBER_
DATE
OPERATOR
FUEL
SITE
r
Sample
Point
Time
METER CONDITIONS
A PS
AH
Meter Reading
TEMPERATURES. »F
Stack Probe
Oven
impxnqers
In
Out
Meter
Vac.
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Pressure
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Gel .
9 (Start)
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-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hq ft3/
JSOKINETICS
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
—//- "79
Sample
Point
Time
METER CONDITIONS
A P
A H Meter Readin
.77
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13
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Total Vol. H2O ^ 7 ml
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
V»c
in. Hg
ft3/min
TEST NUMBER
BATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES , °F
ample
oint
Time
METER CONDITIONS
£ps A H Meter Reading
.-78
Stack
590
Probe
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In Out
68
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12
13
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g(Start)
Total Vol. H2O
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hq ft3/min
ISOKINETICS
TEST NUMBER
BUTE 3~~-/2~
OPERATOR J7 D,
FUEL
SITE C.
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
APS
AH
Meter Reading
TENPERAtURES . °F
Stack
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-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hq ftvnin
ISOKINETICS -
Before
After
TEST HUMBER_
DATE _.
OPERATOR _
FUEL _
SITE
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Stack
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Out
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70
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Percent O?
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11
12
13
0
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162
-------
PARTICULATE
DATA
Leak Check Rat«
Vac
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JSOKIKETICS -
* y\
After
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATIOM
ample
oint
Time
METER CONDITIONS
J^.
AH
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Stack
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START
SAMPLE VOL
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Uomoq^rjiph Setup
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f
q(End)
Total
q (Start)
Total Vol. H2O
-------
PARTICU1ATE
DATA
Leak Check Rate
Vac
in. Ho ft3/
ISOXIKETICS -
TEST NUMBER 2. 3
DATE
OPERATOR
FUEL
SITE
PROBE LOCATIOH
Sample
oint
Time
METER CONDITIONS
AH
Meter Reading
TEKPERAlURES . "F
Stack
Probe
Oven
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SAMPLE VOL 15P< 5/
,tt
1°
ft*
cpitot
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In. Hg-Gau
Percent Oj • |
Barometric
Pressure
'meter
'stack
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c
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Noz(Ideal)-
Noz(Actual)-
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/**
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'S
Total
9 (Start)
14 q(End)
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Total Vol. R2O
//^*U
-------
PARTICULATE
DATA
LeaX Check Bate
Vac
in. Hg ft3/«iin
ISOKINETICS -1
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
ample
Point
Time
METER CONDITIONS
AH
Meter Reading
2970.f1
TEMPERATURES, *F
Stick
Probe
Oven
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Out
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Pircent
Barometric
Pressure
Nomograph Setup
C
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12
t3
14 9(El>d)
Sil% /* I
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Total Vol. H20 / *" »]
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-------
PARTICULATE
DATA
Leak Check IUt«
V.c
in. Hg ft3>in
ISOKINETICS
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES, *F
ample
oint
Time
HETER CONDITIONS
A?JL
AH Meter Reading
Stuck
Probe
Oven
Impingers
In
Out
Meter
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-------
PARTICULATE
DATA
1EOKIHETICS -
TEST NUMBER_
vac
in. Hq
OPERATOR
FUEL
SITE d
PROBE LOCATION
ample
oint
Time
METER CONDITIONS
AH
Meter Reading
TEflPERAtUR£S, *F
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METER VOL
— / or/i
Vol.
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hq ft3/
1SOKINETICS
TEST NUMBER
OPERATOR J7*. aO.
FUEL ___^___
SITE C.
PROBE LOCATION
TEWERAtORES, CF
ample
oint
Time
METER CONDITIONS
A?,
AH
Heter Reading
Stack
Probe
Oven
Impinqers
In
Out
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-------
PARTICULATE
DATA
Lea* Check Ratt
Vac
in, Hq ft3/
1SOKINETICS
-/»«3 *
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
ample
oint
Time
hETER CONDITIONS
APS
Meter Reading
TEMPERATURES, §F
Stack
Probe
Oven
Impingers
In
Out
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STAR
SAMPLE VOL
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In. Hg-Cauge
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Pressure
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''meter "
AHg -
11
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169
13
1
1
14 qlEnd)
Silica
Gel
Total l^
g( Start) Aqr.
Total Vol. H2O
-------
PARTICIPATE
DATA
Leak Check Rat*
ISOKINTTICS -
TEST NUMBER
Vac
in. H
ft3/min
PROBE LOCATION
TEMPERATURES, *F
Sample
Point
Time
METER CONDITIONS
AP,
AH
Meter Reading
Stack
Probe
Oven
Impinqers
In
Out
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Vac.'
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. /3
14
^6
a(End) q(Start)
Total Vol. H-.O ' f • 7
-------
PARTICUUVTE
DATA
Leak Check Rate
Vac
in. Hg ffVnin
ISOKINETICS -
TEST NUMBER
J~ G
OPERATOR
FUEL
SITE C
PROBE LOCATIOM
METER VOL.
/,e£7*
£ gj pmet«r
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12
t3
Percent
14
Gel
(End) g(Start)
:s .
Aoraras
''ft
Total Vol. H2°
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hg ft3/min
ISOKIKETICS
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
^?z
TEr\PEKAtUR£S , *F
Sample
Point
Time
METER CONDITIONS
A Ps
AH
Meter Reading
Stack
Probe
Oven
Impingers
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Out
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7*
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99
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-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hg ftV
ISOKINETICS
. /*2. z
TEST NUMBER
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES, *F
Sample
Point
Time
METER CONDITIONS
AH
Meter Reading
Stack
Probe
Oven
Xmplnqers
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Out
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ff.33
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Barometric
Pressure
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Noi(Jdeal)-
Noz (Actual)-
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3(End)
Silica ff y
g(Start)
Total Vol. H20
-------
PARTICULATE
DATA
Leak Chpclt Rate
Vac
in. Hg ft3/
ISOKIHETICS -
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TEMPERATURES. *F
Sample
Point
Time
METER CONDITIONS
A
AH
Meter Reading
Stack
Probe
Oven
Implnqers
In
Out
Meter
o2,%
Vac.
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f*
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76
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21
32*
00
33°
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44
2J80
3/o
3
-------
PARTICULATE
DATA
Lea> Chech Rate
Vic
In. Kg ft3/
1SOKINETICS
TEST NUMBEK
DMT
OPERATOR
FUEL
SITE
PROBE LOCATIOM
TEWERAtURES. "F
ample
Point
Time
hETER CONDITIONS
AH
Meter Reading
Stack
Probe
Oven
Impinqers
In
Out
Meter
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Vac.
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270
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Average
.V7 .5*
METER VOL.
SAMPLE VOL
START Z2g2
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Percent O2 ™
Barometric
NoniogTaph Setup
C
Tst«ck "
AP
Noz(Ideal)-
Vol.(End) vol. (Start) &vol.l»J)
11
12
13
ft*
•4 qlEnd)
Silica
Gel
g (Start)
Total Vol. H20
-------
PARTICUIATE
DATA
Check Rite
ISOKIKETICS -
TEST NUMBER
Vac
in. Hg
Before
After
OPERATOR
FUEL
SITE
PROBE LOCATION
ample
Point
Time
METER CONDITIONS
A Ps
AH
Meter Readin
tURES , *F
Stack
Probe
Oven
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In
Out
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o
Total "^
X/2.
8 (End)
g (Start)
Ms. 7 - //*
Total Vol. B2o
-------
PARTICULATE
DATA
Leak Check Rate
Vac
tn. Hq ft3/min
ISOKINETICS
• TEST NUMBER 21
OPERATOR •J' O
FUEL
SITE C
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
A P5 AH Meter Reading
TEMPERATURES, *F
Stack
Probe
Oven
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put
Meter
oa,%
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31*
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.Si
23*1 1.
-------
PARTICULATE
DATA
Le«X Check R»t«
v.c
in. Hg ft3/mln
ISOKINETICS
TEST HUMBER_
OPERATOR
FUEL
SITE
PROBE LOCATIOH, SfJf M*~
TEMPERATURES, §F
ample
oint
Time
METER CONDITIONS
AN
AH
Meter Reading
Stack
Probe
Oven
Impingers
In
Out
Meter
o2,%
Vac.
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2.10
70
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70
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11
ti
13
14 q(End) 9(Start)
Silica
Gel .
Total Vol. H20
•^ **fCi
"I
-------
PARTICULATE
DATA
Leak Check Rate
ISOJCINETICS -
,.*.'.
V»c
in. Hg
ffVnin
TEST NUMBER
DATE
OPERATOR
FUEL
SITE C-
PROBE LOCATION
percent Oj •
Total Vol. H2o
-------
PARTICUIATE
DATA
Leak Check Rate
ft3/nin
Vac
in. Hq
ISOKINETICS -
12. \
TEST NUMBER
DATE tf -/- 79
OPERATOR J"t &.
FUEL
SITE C
PROBE LOCATION
TEMPERATURES, °F
Sample
Point
Time
METER CONDITIONS
A Ps
AH
Meter Reading
Stack
Probe
Oven
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In
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34"
2f. 1 3
3
-------
PARTICULATE
DATA
Leak Check Rate
Vac
1"- «9 *t3/
ISOKINETICS -
TEST miMBER_
DdTt
OPERATOR
FUEL
SITE
Sample
Point
Time
^ETER CONDITIONS
A P..
AH
Keter Reading
TEMPERAtORES , *f
Stack
Probe
Oven
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Total
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181
Total Vol. Hzo f'f "1
/^
-------
PARTICULATE
DATA
Lea* Check Rate
Vac
in. Hg ft•'/rnin
ISOKINETICS -
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
- 2 — 7
TEMPERATURES, *F
Ample
oint
Time
METER CONDITIONS
AP,
AH
Meter Reading
Stack
Probe
Oven
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»i /7/ - /*>*
& .
13
*4 g(End)
Silica
Gel
Total
q (Start) tgzi
Total Vol. H2O
-------
PARTICULATE
DATA
Leak Check Rate
ISOKINETICS -
TEST NUMBER
Vac
in. Ho
ftj/min
OPERATOR
FUEL
SITE
PROBE LOCATION
JO
ample
Point
Time
METER CONDITIONS
A H Meter Reading
TEMPERATURES , °F
Stack
Probe
Oven
Impingers
In
Out
Meter
Vac.
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.
-------
PARTICULATE
DATA
Leak Check Rate
-------
PARTICIPATE
DATA
Leak Check Rate^
3
Vac
in. Hg ftj/min
ISOKIHETICS
TEST NUMBER
OPERATOR
FUEL
SITE CL
PROBE LOCATION
Sample
Point
Time
METER CONDITIONS
./*
AH Meter Reading
TEtVERAtURES , *F
Stack
Probe
275"
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3/2.
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-------
PARTICUIATE
DATA
Leak Ch«ck. Rate
vac
in. Hg ffVmin
ISOKINETICS -
TEST NUMBER
DATE
OPERATOR
FUEL _
BITE 0_
PROBE UJCATICH fjjt fUT
TEMPERATURES, *F
Sample
Point
Time
METER CONDITIONS
AH Meter Reading
Stack
Probe
Oven
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Out
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Hoc(Actual)*
13
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M g(End) a(St«rtl
Silica /S4J
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-------
PARTICUIATE
DATA
Leak Check Rate
ISOKINETICS
-
72.
1.17
47
2.62.
72
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7
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Total vol.
H2O
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hg ft3/
ISOKINETICS -
TEST NUMBER
DATE
OPERATOR
FUEL
SITE
PROBE LOCATION
TERPERAtURES ,
Simple
Point
Time
hETER CONDITIONS
AH
Meter Readinc
Stack
Probe
Oven
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In
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11
12
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a (End) g (Start) nqram
X/.2.
total Vol. H20
-------
PARTICULATE
DATA
Leak Check Rate
Vac
in. Hq tt3/Bin
ISOKINETICS -
Before
After
TEST NUMBER_
DATE * *"/£:
OPERATOR J~*, t
FUEL
SITE C.
PROBE LOCATION
ample
oint
Time
METER CONDITIONS
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Keter Reading
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KETER VOL.
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14
Silica
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g(Start) Agrams
Total Vol. HjO
-------
PARTICULATE LAB WORKSHEET
TEST
Date
Test
Dry
I
NO ff (Hil«LT OuLllTLl LOCATION Sf+C
Final
nitial ranaj.
A DgV initial
A Vic
Irapinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H20 RINSE
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LOAD
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%
REMARKS:
8830-5
-------
PARTICUIATE LAB WORKSHEET
TEST NO. 7
Date f-J-7
Test Description
SLtfffHT
(Inlet-) Outlet)
I-7& Box No.
LOCATION^
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV_
Final
Initial
A Vic
1
2
3
Total
CONTENT
H20 RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
X
BEAKER NO.
V
\
DATE WT.
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REMARKS:
klb/hr
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
D»t* ^Z- /— 78 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
\ 1
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REMARKS:
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-------
PARTICIPATE LAB WORKSHEET
TEST NO
Date
Test Description^
, OllLim.)
Box N°-
LOCATION x5/«£ C
Eng.
Dry Gas Meter Voi (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
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1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
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\ /
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-------
PARTICIPATE LAB WORKSHEET
TEST NO. fSMRfW-l (Inlet', Outlet)
Date f- 3-78 Box No.
Test Description
Dry Gas Me
Final
Initial
A DgV
LOCATION ^;Jt
'. C.
Eng.
ter Vol (ft3)
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
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V
A
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REMARKS:
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TEST MO. /A our (Inlot-, Outlet)
Date 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
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REMARKS:
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9
8B30-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. //-
Date
(Inlet, OuLlut)
Box No.
LOCATION_
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final_
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
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POST TEST WTS.
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69. 473 1
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A Vic
A DgV
A Mn
ml
LOAD
REMARKS:
8830-5
r«v.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /2
Date _ &"
Test Description_
-, Outlet)
Box NO.
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fina1
Initial
Impinger Water Vol (ml)
A DgV_
Final
Initial
A Vic
1
2
3
Total
CONTENT
H20 RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
BEAKER NO.
s
23
\
DATE WT.
I
TARE WT.
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V
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\
POST TEST WTS.
\
X
AVG.
X
2//5T
A WT.
\
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A Vic »
A DgV -
A Hn
ml
LOAD
mgm
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
Date ^~— 4— 78 Box No .
Test Description
LOCATION ^~?Jc. C-
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DqV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/\
/ V
/ \
Impinge r Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
-&4
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6?.17
61. <& W
• :
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A Vic
3 Total
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POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
Y
A
/ \
/ \
61.2.6o<1
6 f . ^/^
6l.2(>ftJ
l<}. 2.6 f3
-------
PARTICIPATE LAB WORKSHEET
TEST NO.
Date
Test Description
Outlet)
No.
LOCATION_
Eng.
Dry Gas Meter Vol (ft^)
Final
Initial_
A DgV_
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
H20 RINSE
RINSE
FIASK
NO.
NO.
BOTTLE NO.
BEAKER NO.
\
DATE WT.
TARE WT.
V
\
:
AVG.
POST TEST WTS.
\
\/
A
"20.
-70.0487
•70.
NX
AVG.
63
A WT.
. o
A Vic
A DgV
A Mn
ml
LOAD
REMARKS:
8830-5 rev.
-------
PARTICIPATE LAB WORKSHEET
Date S^-tJ-78 Box No.
LOCATION S'+l C.
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H2O RINSE
V /
\ /
\ /
V
A
/\
/ V
/ \
1
2
3
4
AVG.
A WT.
A Vic «
\ /
\ /
V
A
/ \
/ \
-
Impinger Water Vol (ml)
1 2
Final
Initial
RINSE
Z7
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67. 31-42,
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9
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67. 0237
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67- 9734
67. 97 '7
W. 9734
£7. 1728
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NO.
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A Mn rf^^^T* 7 niQin REMAKKo *
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\
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/
/
/
\
\
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8830-5 rev.
-------
PARTICIPATE LAB WORKSHEET
MO. XV
Date
dniav, Outlet)
Box No.
Test Description
LOCATION^
Eng.
Dry Gas Meter Vol (ft3>
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Hater Vol
1
2
3
(ml)
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
5
DATE WT.
5- -^-
^
TARE WT.
Y.
A
63.SZT3/
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73.
\
X
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73.0/77
A WT.
\
22 . 5~7f 2
A Vic
A DgV
A Mn
ml
205". *? mgm
LOAD_
°2_
REMARKS:
klb/hr
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /4
Date
^- 1-7 8
(Inlet',
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final _
Initial
Iropinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/\
/ V
/ \
ACETONE
RINSE
31
3^-/2-*78
*4.S-*33
£4. s-032.
£4. 5*31
.
6*f
-------
PARTICULATE LAB WORKSHEET
TEST NO. /5"
Date ^V
(InliL, eulle-t.)
Box No.
Test Description
LOCATION
Eng.
,57.4 C
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.
*c^e
- —
3-z
- —
&>. 3*75-
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5T9-3073
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«ST>. 3073
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Initial
A Vic
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34
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NO.
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\
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POST TEST WTS.
73 .
AVG.
"75753^3
A WT.
0 .2.0-71
23.
\
A Vic =
h DgV =
A Mn
ml
LOAD
klb/hr
%
mgm
REMARKS :
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
/n&
TEST NO. /*T
-c#
Date f-/»~ 18 Box No.
LOCATION .5Vc/fc C.
Eng.
Test Description
Dry Gas Meter Vol (ft 3}
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)
1 2 3 Total
Final
Initial
ACETONE
RINSE
24
£--/£> -78
6J. &>s4
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64. &64£~
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64. &L43
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BLANK
NO.
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\
\
\
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/
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/
/
/
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-------
PARTICULATE LAB WORKSHEET
TEST NO. J*
Date
Test Description
(Inlitf, Outlet)
Box No.
LOCATION^
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial_
A DgV_
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
22.
DATE WT.
- 78
f-fl-78
TARE WT.
\/
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POST TEST WTS.
A
. 99/1
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-------
PARTICULATE LAB WORKSHEET
TEST NO. /b -
Date f-.//-'?*
i«t)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fina\
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FIASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
\
BEAKER NO.
_2Z
DATE WT.
I
TARE WT.
5
\£
67.
\
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POST TEST WTS.
\
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6*. o
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. 6773
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\
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\
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A Vic
A DgV
A Mn
ml
LOAD
02
kUb/hr
%
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /f
(Inlef, Outlet)
No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
H20 RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
2?
\
DATE WT.
.
TARE WT.
\
Y
63.35*7
\
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\
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\
63.
63.
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\
63.
2.6.
A Vic
A DgV
A Mi
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LOAD
2.6 . 83S-. "7
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. /f
Date
ftiet-, Outlet)
S~~-f2-~79 Box No. _
LOCATI ON
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
V
A
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/ v.
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64.
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-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
Test Description
gt
.44*2-
. L42.-L-
.tt/23
•
. 6422
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
AVG.
A WT.
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A DgV
A Mn
2
3
4
IS
SB
\ /
\ /
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07
REMARKS:
rt1 w
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. 9323
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8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
AlCC*
TEST NO._
Date
Ealefe-, Outlet)
Box No.
LOCATION_
Eng.
Test Description_
Dry Gas Meter Vol (ft3)
Final__
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
•
3-7
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A DoV
A Mn
1
2
3
4
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41. T7t>2-
0. /3S2.
LOAD
07
REMARKS:
x c3^
/
/
\
X
X,
210
8830-5 rev
-------
PARTI CULATE LAB WORKSHEET
TEST NO. 23
Date _
Unlat-, Outlet)
Box No.
LOCATION
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
Impinqer Water Vol (ml)
A DgV_
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\/
V
A
/ \
/ Y
/ \
ACETONE
RINSE
38
?7. 03/0
97. e>3c>l>
97. 030-2.
77. O3o£
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• •
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.^£•7
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-------
PARTICULATE LAB WORKSHEET
TEST NO. 23 (W Unlot'i Outlet)
Date Box No.
Test Descr
LOCATION -5/i^ (-
Eng.
iption
•
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
V
A
/ \
/ V
Final
Initial
A Vic
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.
31
£fr^~^ £. -^'"" r> £}
7. 43S7
S&.4387
3&. 439*7
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1
2
3
4
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A Vic
A DgV
A Mn
\ /
\ /
V
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£~7
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/
/
/
\
\
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\
\
X
X
/
/
/
/
/
/
\
X
\
LOAD klb/hr
C
>7
%
REMARKS:
8830-5
rev.
-------
PARTI CULATE IAB WORKSHEET
s*>
TEST NO. 2*4 -
?
Date Bo
Test Description
x No.
LOCATION ^,'•6. C
Eng.
'
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
-
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
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NO.
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/
/
/
/
/
/
/
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\
\
X
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1
2
3
4
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A WT.
\ /
\ /
V
A
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/ \
75: ff/fc'z
96~.ff£l&
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A DgV = ft3 Oj %
A Mn 31./33- 1 mgm REMARKS:
/
/
/
\
\
\
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO._
Date
*etr(Iiil«try
Box Mo.
Test Description
LOCATION
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
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47
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41
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61.
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NO.
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/
/
/
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/
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\
\
\
POST TEST WTS.
y
TV
SO 2.
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\
AVG.
\
A WT.
\
6.
X
A Vic -
A DgV -
A Mi
ml
LOAD_
°2_
REMARKS:
214
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
sur
Date Box No. E
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial Final
A DgV Initial
A Vic
ng.
Impinc
1
jer Watei
2
• Vol
3
(ml)
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ v.
/ N
ACETONE
RINSE
.
43
•
7 7 <*3*r>
17. 02.13
?7. *2.
-------
PARTICULATE LAB WORKSHEET
TEST NO. J?5"
Date
fy«r(Inlef, Outlet)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Impinger Water Vol (ml)
Initial_
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
W
<&-.?tf2g-
vs-.w/l
tt ?8/t>
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DRY
FLASK
43
.
64. 5~8
64-5-33-^
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64. S*3?
FILTER
NO.
.
27
.64//
. 64/Z
.64/4
—
• W2-
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
\
A
64. 6^3
AVG.
\
64.
A WT.
\
A Vic =
A DgV =
A Mn
ml
LOAD
02.
kLb/hr
%
mgm
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO 2& (Inlat't Out Iff.)
Date Box No-
Test Description
LOCATION ^57 *< C-
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
1
2
3
4
AVG.
A WT.
A Vic =
H2O RINSE
\ /
\ /
\ /
y
A
/ \
/ V
/ \
\ /
\ /
V
A
/ \
/ \
V
-
Impinge r Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
. .
3-y-
64 o(>37
64 o 6j6>
4^0646
•
64. &&
— •
, (,S"7^
BLANK
NO.
\
\
\
\
/
/
/
/
POST TEST WTS.
64 ?&7°
64. v-VffZ
b 4. 23 8*1
_
64. 2,99°
& • , z.2.3'7
J08. Wfl
/0$.<9frt>
/e$, 9/2'/
•
/08. 9/24
39 3S*S
&6LJ
* &&/^*
&/j -^ /
.em
0, 2,0
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet/, OuLlul)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
5-1
n.^tst
6f.$t3l
^f.ST^Zff
•
6
.649?-
.6413
• —
.Mri
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
k
X
*
94s*
\
AVG.
^
. \
A WT.
X
0. 2.S32.
N
A Vic
A DgV
A Mn
ml
LOAD
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 27 (I+tluL', OuLluL)
Date Box No.
LOCATION
£/& C.
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
v
A
/ \
/ \:
/ \
Impinger Water Vol
Final
Initial
A Vic
ACETONE
RINSE
-*~7
•
64.S^4°
64.SV3S-
64.&V33
.
64.$#3(r
1
DRY
FLASK
•
&
•
&». 3°-r?
5^.3*7^
&».3*8°
S&.3*7f
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
\/
A
/ \
64. e/3j
£4. 8/3^
^ 4.9l3£-
.
64. 8/33
<5>. 2,1-
#7.3°?°
87. 3o 1 8
36 W&J
(ml)
Total
BLANK
NO.
\
\
\
\
/
/
/
[/
. 07*2-
.&?//
• &7/Z
.
, &7/e>
0. 1-Z7,8
/
/
/
/
\
\
\
\
\
\
X
/
/
/
/
/
'/
\
\
\
LOAD fc lb/hr
07
%
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 27
Date
(Ifrlef, OuLlut)
Box No.
Test Description
LOG ATI ON
Eng.
.57^
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
v
A
/ \
/ v
/ \
ACETONE
RINSE
3-0
— .
^7. 8¥*t
6J. 8¥*<1
&7. &33
DRY
FLASK
s-/
—
41 . &z?
4
BLANK
NO.
\
\
\,
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS
\
X
AVG.
\
A WT.
\
0, 4/32,
0 .
A Vic
A DgV
A Mn
ml
LOAD
klb/hr
%
mgm
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 2.0
Date
(Inlet', OuLlut)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol vft3)
Fi na1
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO
BEAKER NO
DATE WT.
TARE WT.
AVG.
.
.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
Y
A
/ \
/ \'
/ \
ACETONE
RINSE
S-J
•
£3. sy&f
/3. ^^/f
63.S&3
63.5S42,
DRY
FLASK
.
5-2.
• •
&.431/
&V.43?/
£V. 4392-
.
S*. 437/
FILTER
NO.
32.
, 64/o
.64/3
, 64/2.
. 64/
-------
PARTICULATE LAB WORKSHEET
TEST NO._
Date
./£/V
s»./tr?
s~s>. fc/e
—
&*./(>/ 1>
FILTER
NO.
•
33
. 6313
. t3f£~
.f>3?sr
—
.4214
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
\
A
AVG.
\
A WT.
A Vic
A DgV
A Mh
X
ml
LOAD
REMARKS:
klb/hr
%
8830-5 rev
-------
PARTICULATE LAB WORKSHEET
TB/L^fUT'
TEST NO. 27 (Inlet", Outlet) LOCATION -SV«£ C.
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.
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ \:
/ \
-
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
. .
64
. .
17. & 322-
?7. £> 3/S
17. <£>5V3
7 7 02/7
A Vic
DRY
FLASK
— .
s~4
.
5V. 3 eve
^~Z>. 3&
£~& . 3*^3
^T5 . 3<*^'5~
FILTER
NO.
•
"^? •* *
^S* ^T
- —
, £5"37
, ^ S~4£~
£ tf^^J ~^}
— .
, 6£~4-2~
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
V
'A
/ \
/ \
17. 3&/3
97. "3$tl
17. -ze/°
^*^ ^3 & i i
7 / • <£> & / /
a . -zeW4
j4. "fo^e
^,, rt>-7 -~t(
ft ' / £• r*J
$4. ?D0Y
• *& »3 *^ ^f
^ff ^ ^TcJ
• 03S-7
- — -
. ^3c5^T
^? * / o / ^
\
\
\
/
/
/
A Vic = "ml LOAD klb/hr
A DgV = ft3 0? %
A Mn tf^/Sl- *? mgm REMARKS:
/
/
/
\
X
\
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
Test Description_
bef, OulleL)
Box No.
LOCATION^
Eng.
Dry Gas Meter Vol
Final
Impinger Water Vol (ml)
Initial
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ \:
/ \
ACETONE
RINSE
•
/£
/O? • /S~2^"
JO -2 . /S-/1
/02. JSY0
/02 , /^Zo
DRY
FLASK
^/
^. -2118
&>.3Z.3Z?S\
• •
S* . 321S
FILTER
NO.
.
3*-
, 6L-7-2.
.66^
, £673
.
.^73
BLANK
NO.
\
\
\
\
/
/
/
/
/-
/
/
/
\
\
\
\
POST TEST WTS.
\
X
102
. 70
\/
AVG.
\
A WT.
\
A Vic
A DgV
A Mn
ml
LOAD
klb/hr
%
mgm
REMARKS:
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inluf, OuLlCL)
Box No.
LOCATION^
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
k '
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
^2
^
9£~. 63-23
J5~. 6*33
7%~. &S33
?:T 65-3°
DRY
FLASK
•
to
•
67. <&?
, &7-2.1
. 6722.
. 6-7Z3
.$722.
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
l/
\
\
\
\
POST TEST WTS.
\
Y
5
•7$. 5V/°
AVG.
- \
A WT.
S
0 .
A Vic
A DgV
A Mn
ml
LOAD
7 mgm
REMARKS:
klb/hr
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Ii»l(-Lr, euliU
Box No.
LOCATION
Eng.
Test Description_
Dry Gas Meter Vol (ft*)
Final
Impinger Water Vol (ml)
Initial_
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/\
/ V
/ \
ACETONE
RINSE
•72
t*J.oll>2-
£4. otsv
6+ o t
ty. /&4Z
if./ 03 8
0. //83
ml
ft3
mgro
\ /
\ /
V
A
/ \
\
LOAD
Op
REMARKS:
, -77^-7
•
-Tx*/
o. e 1tf
\
\
\
/
/
Jclb/hr
%
'
/
\
N^
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST NO. 36
Date
(I-«letr-, Outlets)
Box No.
Test Description_
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKEH NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ \:
/ \
ACETONE
RINSE
•73
.
64. ST?^V
6>4.'S~z4S~
t>4. tret/
t>4.sv
DRY
FLASK
•
67
3~v./£oJ
$v./6°3
S&- /6°3
— •
3-0. Jbo?-
FILTER
NO.
3*
.t>-737
. ^737
,6738
.^>73-7
BLANK
NO.
\
\
\
\
A
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
_3_
4
A
7\
AVG.
\
A WT.
\
-2-1 t>O
b vie =
t^ DgV =
£^ Mn
ml
mgro
LOAD_
°2_
REMARKS:
klbAr
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Ii>let-f Outlet)
Box No.
LOCATION
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
H20 RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
BEAKER NO.
\
39
\
z
DATE WT.
I
TARE WT.
7
\SL
5
\
X
s
AVG.
69.
.67*8
POST TEST WTS.
\
¥
. -2-811
/i.
\
\
2
\
AVG.
\
. 74S-7
A WT.
\
0.
0.
A Vic
A DgV
A Mn
. 3
ml
mc[in
LOAD_
02
REMARKS:
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
(Inlaf, Outlet)
Box No.
Test Description
LOCATI ON
Eng.
Dry Gas Meter Vol (ft3)
Fi na1
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H20 RINSE
\ 1
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
-Tf
.
t?. 5*4(>
6. 43^
4». 4332-
61. 7^?
0. /4S&
ml
ft3
mgm
*-&> &£.
J9 • 3/&2»
S3. z
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Illlef, OuLlH.)
Box No.
LOG ATI ON
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Fi na1
Initial
Impinger Water Vol (ml)
A DgV_
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
X
BEAKER NO.
I
\
DATE WT.
i
TARE WT.
N»Z
5
X
\
£
. 3*77
\
S
AVG.
3° ~78
X
POST TEST WTS.
5
A
te.
AVG.
A WT.
A Vic
A DgV
A Mn
X
\
.***1
0. "2418
0.
X
ml
mgm
LOAD_
°2_
REMARKS:
klb/hr
230
8830-5
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Iftlef, Outlet)
Box No.
Test Description^
LOG ATI ON
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
Final
Initial
A Vic
Impinger Water Vol (ml)
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
v
A
/ \
/ V,
/ \
ACETONE
RINSE
.
77
•77.034°
17, 032.7
17 &3>?4
17> oZ2°
DRY
FLASK
-
•7*
— —
o j . *^«^5 C? *f
£*^7 tfP^?^?2?
^7. &3?3
67. ffSfZ.
FILTER
NO.
4?~
^7J5V
. 675-2.
.675-2.
— —
,*7S-2
BLANK
NO.
\
\
\
\
/
/
/
/
/
/
/
/
\
\
\
\
POST TEST WTS.
AVG.
A
f 7
3S~*/7
.0/33'
4/35-
A WT.
//,
A Vic
A DgV
A Mn
ml
LOAD
mgm
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO.
Date
(Inlet-', Outlet)
Box No.
Test Description
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Fi nal_
Initial
A DgV
Impinger Water Vol (ml)
Final
Initial
A Vic
1
2
3
Total
CONTENT
H2O RINSE
ACETONE
RINSE
DRY
FLASK
FILTER
NO.
BLANK
NO.
BOTTLE NO.
\
BEAKER NO.
s
Go
DATE WT.
\
TARE WT.
V
^z:
A
X
s
S
AVG.
/02 .
POST TEST WTS.
\
\
*
.3ffVS~5*
. -S3Z1
\
\
AVG.
\
\.
A WT.
\
0, 034?-
N
A Vic
A DgV
A Mn
ml
LOAD
°2_
REMARKS:
klb/hr
8830-5
rev.
-------
PARTICULATE LAB WORKSHEET
^/./Pw^r
TEST NO. 42, CbfrSLef, Outlet)
Date Box No.
Test Desert
LOCATION jSr'Je C
Eng.
iption ,_
Dry Gas Meter Vol ,ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
AVG.
AVG.
1
2
3
4
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ \i
/ \
1
2
3
4
A WT.
\ /
\ /
\/
A
/ \
/ \
-
Impinger Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
#/
<95~. yess
<^^^"~" ^&^2^^1D
^^?J ~/ v^*O
f55T W/7
fglfJSV
A Vic
3 Total
DRY
FLASK
. .
•77
•
f~) * &^) &*J
^^^~ /£^~^/
/^? » r^^--^
•
9S: L&.3
FILTER
NO.
•
44
•
, £?/£
, 67/7
* ^ f f f
w9 **7 f^J '
BLANK
NO.
\
\
\
\
/
/
/
|/
/
/
/
/
\
\
\
\
POST TEST WTS.
^» 2S7/
l6.-z&>1
jb. 24- 2,t£l
/2-1. 0333
/^?, ^^"55
/^^ 5iT^
—
/2f ^^SS"
^.2^/2-
s-Jptef-
- .
-------
PARTICUIATE LAB WORKSHEET
TEST NO. 4/2- (Inlefc-, Outlet)
Date Box No.
Test Descr
LOCATION ,5/^T C
Eng.
iption
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
Y
A
/ \
/ V
f \
1
2
3
4
AVG.
A WT.
A Vic
A DgV
A Mn
\ /
\ /
v
A
/ \
/ \
Impinoer Water Vol (ml)
1 2
Final
Initial
ACETONE
RINSE
k
g*J
. .
64, *W?
£*J* 0t4o
&*[• 06 fa
£<{. 064s
A Vic
3 Total
DRY
FLASK
-78
"
^>. 3Z.13
S9. 3294
^9.3ZfS
,5». 3213
POST TEST WTS.
//. 32/1
64. 3z/3
64. 3z&
64. 32/5
^. 25"7«>
SJ< 2£fJ
St. 2*S*
s/.tts*}
— -
sf.afst
*.f£~l3
FILTER
NO.
*J6*
•
,^7f^
./7^5*
, /7^T"
•
• 67?£~
-. fjff
< 9153
•
•
* U&&
&< 3/£°8
BLANK
NO.
\
\
\
\
/
/
/
/
\
\
\
/
/
/
- ml LOAD klVhr
^ ft Oo ^
* J^**m ^ i , „ DPMUPVC •
J4^ ^r ^Wm t InCJUi x\Etnn*\r^& •
/
/
/
/
\
\
\
\
s
/
/
\
X-
X,
8830-5
rev.
-------
PARTICULATE LAB WORKSHEET
TEST N0._
Date
(Inl-ef, Outlet)
Box No.
Test Description_
LOCATION_
Eng.
Dry Gas Meter Vol (ft3)
Final
Initial
Impinger Water Vol (ml)
A DgV
Final
Initial
A Vic
1
2
3
Total
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT.
1
2
3
4
AVG.
H2O RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
ACETONE
RINSE
85-
•
7 643^
—
41. 6433
FILTER
NO.
4*>
'
.U17
.Ul*
,&(>?€
- — '
,U
ml
mgm
LOAD
klb/hr
REMARKS:
8830-5 rev.
-------
PARTICULATE LAB WORKSHEET
TEST NO. 4*3 <
&.*
Date Box No.
LOCATION ^fsJt C
Eng.
Test Description
Dry Gas Meter Vol (ft3)
Final
Initial
A DgV
CONTENT
BOTTLE NO.
BEAKER NO.
DATE WT.
TARE WT. 1
2
3
4
AVG.
H20 RINSE
\ /
\ /
\ /
V
A
/ \
/ V
/ \
-
Impinger Water Vol (ml)
123 Total
Final
Initial
ACETONE
RINSE
$£>
.
£ /. && c/ 2-
6J.00&/
67. fft>7£~
6J. -77
A Vic
DRY
FLASK
03
&>.3o9l
S&. 3*05-
St>-3o?3
. —
sv. 3083
FILTER
NO.
^7
— -
, 6>&zg~
. 6Cz(>
. 6&-2J
f&t-zl?
BLANK
NO.
\
\
\
\
/
/
/
/
7
_^/_
—7—
\
\ _
X
POST TEST WTS.
1
2
3
4
AVG.
A WT.
\ /
\ /
Y
A
/ \
/ \
W.Z344
&1- 234 <
£*. 6/41
JV, 6/tfz
S#- &/.2^»*~
\
\
\
/
/
A Vic = " ml LOAD klb/hr
A DgV = ft3 O2 %
y
A Mn 7v2.& mgm REMARKS:
s
/
<
\
\
\
8830-5 rev
-------
SECTION 3,0
GASEOUS DATA
PAGE
3,1 GASEOUS EMISSION SUMMARY 238
3.2 GASEOUS EMISSIONS DATA 243
3,3 SOx DATA SUMMARY 288
3,4 SOx DATA SHEET 289
-------
Location:_
Fuel:
TEST
NO.
DATE
LOAD
GASEOUS EMISSION SUMMARY
CONDITIONS
02
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
ppm
Wet
HC
ppm
Wet
02
%
Dry
CO 2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
SO3
ppm
Dry
NOTES
4,0.
7-3
f-5
f-7
7-2.
//.*
337
//f
-20-7 a
/e.2,
303
8,2.
1.1
373
00
7"
7A
1.1
/*.!
5-7
3/6
32$
1.2,
X',2.
/0.1
322-
57
&9T
e
V-.2T-7I?
42.0
fe>.2.
$.8
253
10
/*.!
n
1.1
/0.0
NOTE: All parts per million (ppm) figures are corrected to a 3% 02 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
CO
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry
NOTES
2.73
9.1
/o. e
13
~- 4 -7*
91
231
/V
/a. o
3*3
~-/*- 79
S>'4£>
S3
6.7
337
is; as f=hm-f- e^A
37
3o
17 A
- 7*
37
ZffT,
ne
f.V
ow
I/.*
Z/
//-V
25"
32
233
2/Z
//f
£--12. -7$
*J?ea.*
/*.£
33.6
8.1
33/
9.L
333
-/b- 7*
44.7
1.*
26°
319
*$«.&«**£.
/lied. OT
p.o
/te
•2,1
47*
NOTE: All parts per million (ppm) figures are corrected to a 3% O2 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:_
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
Dry
co2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
C02
%
Dry
CO
ppm
Dry
NO
ppm
Dry
S02
ppm
Dry
S03
ppm
Dry
NOTES
$.9
ff.V
//.v
5"32^
72
12.
//v
•2ZC
361
377
23
/'.I
3/1
3*7
/A/
2&S 383
2V
S-7
43V
372.
2£T
- 7*
/73
/33
33
-------
Location:_
Fuel:
(.32.-
TEST
NO.
DATE
LOAD
GASEOUS EMISSION SUMMARY
CONDITIONS
02
%
Dry
co2
%
Dry
CO
ppm
Dry
NO
ppm
Dry
N02
ppm
Wet
HC
ppm
Wet
02
%
Dry
C02
%
Dry
CO
ppm
Dry
NO
ppm
Dry
so2
ppm
Dry
S03
ppm
Dry
NOTES
32,
7.2
3*1
7.
ff.3
241
341
//.*
02,
33
£--30-76
ff.l
/o.l,
322
v.v
3*7
1.*
/o.o
43.1
393
364
0a-
4-il
££
471
34
e.l,
32-7
357
/1. 2.
3&£ 3**
fl.o
all
ad.
25*
*.
(>-/- 78
3S-7
ff.*
//.£-
6-7-70
It. 3,
9*
/I. -3
6.3
£"7
.3*5-
1.4
z&l
Tfy-+B/r+DC.
L-/3-76
I*
374
40
NOTE: All parts per million (ppm) figxires are corrected to a 3% O2 constant dilution factor
#15900
-------
GASEOUS EMISSION SUMMARY
Location:
Fuel:
TEST
NO.
DATE
LOAD
CONDITIONS
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
NO2
ppm
Wet
HC
ppm
Wet
02
%
Dry
co
Dry
CO
ppm
Dry
NO
ppm
Dry
so2
ppm
Dry
so3
ppm
Dry
NOTES
-/5-- 78
243
4t
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
c.
1
4-/3-7*
FUEL £A£,r£f,c>.
f&S, 0-2.
DATA TAKEN BY "PLL
Probe
Posi tion
Time
\
(dry)
(dry)
CO •
ppm(dry)
NO
ppm ( dry )
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
fi.o
346
f.ZS
0.2.
31
/. 3
70
2JSI
1.1
/OS
7.3
281
e -7
Z&T 32.1
/e
23
235-30Z.
•7.3
25-
3.=?
275-
=?».<
AVERAGES
12
2*3
NOTE:
Parts per million (ppm) figures are corrected to 3%
•"> '•• • •?
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
0-2_
Probe
Position
/-£
7
/-£
7
l-L
•7
Time
*V2.<
/»;¥»
//:z°
#38
/z:z*
iz:.z
02
t
(dry)
?.3
*f
ff.l
e.f
7.Z-
L.1
C02
\
(dry)
y.7
/tf.2.
//.*
/•P.?
//»
//•f
CO •
ppm(dry)
unc
4o
3S-
35"
3o
3S~
4$-
cor
62.
5~2
v#
V2.
V5-
5-7
NO
ppjn ( drv )
unc
24^5"
z.*l
Ike
.ZSf
ZS-8
Z4°
cor
57»
431
3^o
36 2.
3J7
«Je6
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO -3
unc
cor
HC
unc
cor
REMARKS
r**Sf*
t>77. "
s&?» "
S-f?T "
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
4-20-78
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
/-*
7
/-£
7
;-£,
7
Time
/y;v*
/s:*t>
/5-/2/
/s-,y?
/l;a$
#>:&
02
%
(dry)^
8.8
9.2-
/o.l
1.J
//.$"
/^.«
C02
t
(dry)
/O.2.
/*.<}
1.1
?.*
7.*
1.0
CO •
ppm(dry)
unc
33
4*
go
4s-
f"
4*
cor
4s
*r&
/3-2.
-?*>
>-7i
7o
NO
ppm(dry)
unc
2*5-
24t>
Z^
23*
ZZe>
Z.Zt>
cor
3<>3
3
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
£ei*s
LOAD_
CONDITIONS_
DATA TAKEN BY
/fl>
Probe
Position
Time
02
t
(dry
C02
t
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO?
REMARKS
27.5
3-7
ofA
1.2-
32.
1-2-
Z/o
1.3-
/p. a
3-2.
23"
JSV
•or, i
53T
7 B4#
&fA
35-
2*7
of*
37.S
Zot*r
**?A
/-*
f.er
7"
Z&
AVERAGES
NOTE: Parts per million (ppm) f jures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C
TEST NO
DATE
&
FUEL eA*r*<* ±*~ M*»
LOAD /2 5" /(sn..
V~25"-7* CONDITIONS /V+tfMs&t 07
DATA TAKEN BY O~» 13
Probe
Position
/-£>
/— 5~
/ — 5"
/-3~
/H£c*l
/-5~
/— 5*"
Time
,*r>c
/5"/i.
/^;^
/*/^i
/7/^
/5T;?0
/7-'5S
02
(dry)
/*».3
/*-3
/».*>
/"-3
/0.3
/a-3
/*.c>
C02
t
(dry
e-7
ff.t>
f-l
8. 7
?.£>
9.5
f-»
CO •
ppm(dry)
33-
3«
55
5^"
35"
55"
3S~
^•7
^4^
7419
57
3*5
5~?
^7
NO
ppra ( drv )
/J'o
/?s-
2/o
2»S"
2/0
22$-
zy»
•
cor
:?z/
32^
3^5-
3^
3S2f
5^'
s^y
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
HC
REMARKS
•V&trf&UArG
•&L*,*>
f.e
tt.t>
^^
^%%
;^^
%M
fi>
£*?
%%%>.
v//y/s;
w/wfy
W/6
5S3
^SS
WM
'MM,
W///>
WM
v%%
WM
W%
'W//,.
Wflfr
WM.
m?/,
WM
Wffifr
w/%fr
V///S&
%//////
?»*?,>
NOTE: Parts per million (ppm) figures are corrected to 3%
02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
02
*
(dry)
C02
%
(dry)
CO •
ppra(dry)
NO
ppm ( dry )
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NOo
unc cor
unc cor
REMARKS
2-*
rs:/*
37
SB
37
2-
37
/
2e-&
AVERAGES
2#9
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
coNDiTior:s_
DATA TAKEN BY
Probe
Position
.2-^
2-£
2,-t
2--6
2.-1?
Time
?;
/»,~n
fc:3S
V',/2.
n.tB
°2
%
(dry)
*.9
1.*
4.1
i..
CO -
ppm(dry)
unc
*e>
sr
26
3f
44
cor
*r
s-3
31
^
*>i
NO
ppm(dry)
unc
2S»
?7°
ZS*
&>s-
2*T>
cor
37»
tfot*
372
«?/f
J/y
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
AVERAGES
T2^~ S/
NOTE: Parts per million (ppra) figures are corrected to 3% o?
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
2-6
2-k
z-£
2-6
2-4
Tine
A'.-A
#:s*
/z>
n:*s
/fizz
02
%
(dry
0.f
ff.fS
Vr
**
C02
1
(dry
/*.2.
/»,»
t.e
<*•*
/*,»
CO •
ppm(dry)
unc
3S~
37
3f
as
32-
cor
5~2.
S-S-
^S
^f
49
NO
ppm(dry)
unc
23f
238
27,«T
&n>
Z'J
cor
33*
^tr6
jar*
^/3
^62
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
.
AVERAGES
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
il'l
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
*
s-
4
3
2.
/
Time
13:39
t3:<&
'3'.41
wsj
tyff*
'4*7
02
\
(dry)
.6>
7,°*
S-SS
f.z
1*t
C02
\
(dry)
1.1
/Z.o
//Si
/*./
t.8
1.*
CO •
jgpin(cJry)
unc
32.
B2.
(1
32-
3?
W
cor
5-2.
^
2^~
^
5^
^f
NO
ppm(dry)
unc
/fV
264
25"
2Z&
225
2*>t>
cor
3/3
3S<=>
323
S*>
^V
S2S-
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO 7
unc
cor
HC
unc
cor
REMARKS
AVERAGES
/o.
3*
NOTE :
Parts per million (ppm) figures are corrected to 3% O2
15900
-------
TEST SITE £
TEST NO /2.
DATE S~-tJ-
.2-6 - ~BLf
Probe
Position
Time
02
*
C02
co -
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
unc cor
unc cor
REMARKS
32
'7?
37
/I'.&r
f-/*
%
27
272
7
8.36
33
/*•
274
7
12:4
35
,84
//* ~Ju£>t '-O
a;**
e.g
37
53-
2/V
$.1
35"
AVERAGES
ff'1
NOTE: Parts per million (ppm) figvires are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
OF*
Probe
Position
2-*
2-£
2-t>
z-(>
7 _
2-t>
7
Time
OJ'«>
/JT/r
/7/5S
^•27
«,y»
f*/53
/f»»
02
%
(dry)
^3
tf'.i'
tf./
^/^
^*
f.^.
7.7
C02
%
(dry)
f.ff
/*.*
//.«
/»./
//s
/p.»^
//v
CO •
ppmtdry)
unc
49
48
/z*
&0
isr
^r
^5"
cor
7V
£7
/*7
/^2
fff
*4
08
NO
ppm(dry)
unc
/52T
XT3
/^V
/5V
/:*•
/5»
/7<
'
cor
^?8
2Z«
229
23V
23f
22?
2.37
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO-j
unc
cor
HC
unc
cor
REMARKS
AVERAGES
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE_
TEST NO
DATE
£--
3
7
Z-t>
Z-6
•7
Time
H.'ev
'4/08
<4:'-2.
A/IZZ
^.'32
rt;4
—
&:*7
/£•:/»
/f.X.
#'./o
/t'.Zf
02
%
(dry
?.*
9-1
8.6
7.&
/*.
.
/o.2
/».y
//2
1.°
/e.i
/»,0
i.e
/o.e)
1-*
/O.2.
/o.
*
VV
NO
ppm(dry)
unc
/?*
Z3°
ZZf
22T
/ffo
2*Jo
S*r*
22°
22.0
2ft>
2Zo
Z3S
cor
Z9t>
3
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
%
(dry)
C02
\
(dry)
CO •
ppm(dry)
unc cor
NO
ppm(dry)
HOT LINE SAMPLES, PPM (WET)
unc cor
NO
unc cor
NO-)
unc cor
HC
unc cor
REMARKS
>,
3/y
4^/*.2
4*
3417
30
f.7
4°
•2/0
3"
44
3*
23*
332
V*
/f.o
•2f>
332
tf.o
22*
3*
2,-b
if.-}
40
322
2-
22f>
A/7
36 /
7.7 //-V 3o
AVERAGES
1.1
wm
63
328
w///,
NOTE: Parts per million (ppm) figures are corrected to 3% Oo
-
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C
TEST NO /£
DATE £~—
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
X=fctg ?crA/
Probe
Position
Tim
02
\
(dry
C0
(dry
CO •
ppm(dry)
unc cor
NO
pptn(drv)
unc cor
HOT LINE SAMPLES, PPM (WET)
NO
NO-j
HC
REMARKS
7.V
#5
/'.*
er/o
Zo
25
7.5
2LS
/o.
25
3°
+*
48
AVERAGES
'.7
NOTE: Parts per million (ppm) figures are^corrected to 3% 02
* . t'\
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
/7
LOAD
fur
CONDITIONS —_
DATA TAKEN BY
-7 —
Probe
Position
Time
02
(dry
C02
\
(dry
CO •
ppm(dry)
NO
ppm(dry)
HOT LINE SAMPLES. PPM (WET)
NOx
NO
NO?
REMARKS
2-
32.
2*2.
8.
35
/«.*>
ft*
3V
2/3
/&•!
?.*
/*
/-?*
-2*
•298
286
/t
ss-
2.S
2-1
22.7
7
2V/
AVERAGES
2*2,
w///,.
ma
W//6
w///,
W///,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
Position
2-t.
7
Z--£
7
2-£
r
Time
/2',n
fZ.I
tXZ
f2.'.£
'2.4
fZ.Sl
02
%
(dry
7.
ff.4
1.x>
?.s
C02
%
(dry
/?.<*
'(•1
//.*
///
/O.O
/e.a
CO •
ppm(dry)
unc
2o
B7
47
NO
ppm(dry)
unc
/**>
/7*
/t*
'7o
/t°
/•7S
cor
Z/2.
2/7
233
2*3
^*z>
275
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO 7
unc
cor
HC
unc
cor
-
REMARKS
^
AVERAGES
NOTE: Parts per million (ppm) figxires are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
— 7
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
firn.nO
Probe
Position
Time
°2
i
(dry
C02
t
_(dry)
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (MET)
unc cor
NO?
unc cor
HC
REMARKS
7
41
336
V/s
2*
A.
22°
V//
AVERAGES
VV
NOTE: Parts per million (ppm) figures are corrected to 3%
o,
2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
£.
2-0
<~-/3--?8
FUEL &*ton L*, ***><«
LOAD /*& ^^/JV).
" /
CONDITIONS //,&*?» ^2. — Aft>4Sls&£.
DATA TAKEN BY J~Q
Probe
Position
2-£
2
3
4
f
6
7
2-(e
2.
— »
3
Time
?;/2
r^
?/y*
7/35
'»;//
'»;ja
/*••<*•
///o*
//,/<•
///3«>
02
«
(dry
/*,7
//"
/*.'/
/».7
/».?
It-9
A*7
//.»
/?.•
//.7
C02
«
(dry
tf.S
y.y
*.z
«r.2
tf-2.
^'^
£>.<
8.4
7.y
7>
c
ppm
unc
^«
3S~
^>
Z<»
3*
4°
4*
3°
ts-
ST>
o •
(dry)
cor
5-3
63
SB
33
f3
72
70
JV
/3I
17
N
ppm
unc
/7T
/#5~
/y*
^"4T
2/tf
2n>
H»
{to
/&>
/7°
0
dry)
cor
3o7
334
333
31°
sts
&l
333
as
IO
cor
NC
unc
>•>
t
C
REMARKS
^V= vy«.
AVE RAGES
/f.ff
9.1
33L
NOTE
: Parts per million (ppm) figures are corrected to 3% 02
'
15900
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
•Bi.% OUT - 2-4 -Pt
/tfM./^ic/one-*•?- f^t>e£
LOAD /4°
CONDITIONS
DATA TAKElM BY
Probe
Position
;?-£
7
2-6
7
2-6
7
Time
/A32
//irz
/^.'J"
/2,'5l
/3:/V
^;./
02
%
(dry)
/*•?
f.^
f-2
?•*
9.1
*>./
C02
%
(dry)
7.2
y.*
/».»
/•/.«»
//.&
/0. 6
c
ppra_
une
1-75
S±°
//»
/^z
//«
?2
3 •
dry)
cor
2??*
ii*"
/^*
/*V
/3-V
#3
N
ppm
unc
2/o
245-
Z3°
Z6>o
2S*>
26?
D
dry)
cor
$?s
371
352
3T/
^Sz>
V^
•
HOT LINE SAMPLES, PPM (WET)
N
unc
3x
cor
^
O
NO
•)
h
C
REMARKS
AVERAGES
W///A
w////,
wm
w///,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
2-2-
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
Position
2-6
-
7
2-6
•7
2-6
7
Time
*;»
/5T*
/5-/5S
/£,*
fat
*;sr
02
«
(dry
r.e
*<1
7.1
f.4
/O.o
V*
CO?
«
(dry
//*
//v
/2.«
/AV
^
/p. i
-
CO •
ppm(dry)
unc
/^r
/5*
//*
/£*
ZZ*
rt°
cor
«7
^/i'
/W
2/5
S6/
2^«
NO
ppm(dry)
unc
2/o
2So
•Zle
ZZo
ZZ°
2^0
'
cor
3/1
3Z1
2&a
3/f
3tl
377
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO-)
unc
cor
HC
unc
-
cor
REMARKS
AVERAGES
NOTE- Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE C.
TEST NO
DATE
•BL*
/*)HI
Probe
Position
..
7
•z
3
4
5"
6
7
2.-t>
•&-tf*r
Time
~#3
f& ,2
XOV3*
fo.s*t
x/; /V
'2,'c6
/2-/6
—
23
V--/7--7S
rt
3«06&
\r£_ .
C02
%
(dry)
"^2
XX. 2
/*•. 2
y.v
/6».W
//'^
/ii.ti
/A*
//-£
••
/*-f
5 2-^
7
c
ppm
"XT?
/f<7
2tf*
35>
22tf>
/22.
/S*
2e^"
/6*>
^^
^^
2M2
o -
(dry)
25"?
^72
4^ZS
67*
3^5'
/^5
^•9
2-f*
2Xfe
JX/
FUEL (>ir£sr&{/v
LOAD /*t<4/(
CONDITIONS /^/4l4 <>xi'* — f.S~7»-O-2_
DATA TAKEN BY ^«
K
ppm
unc
^
^tfo
^Oo
^toe7
26*0
i»o
27"
25^
2//o
*
^^
mtm,
fff/f*/f
^^
o
(dry)
cor
£fOt
^Jy jg
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
(dry
C02
I
(dry
ppm(dry)
unc cor
NO
ppjn(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
/#:*»
330
-71
9-
//•*
433
1.*
22*
35*
23"
*•!>
31*
//,*
7.1
1.9
$3
23°
24°
377
AVERAGES
•Btftur
468
377-
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
1
Probe
Position
Z-£
6
f
4 \
3
2.
7
*-*
-
Time
/o;s*
ll'.fo
11'^
it:y£\
fZ,&
I2,&
1
•
ppm(dry)
unc
/2.Z-
n-
t$-
12.
/to
t?f
iv-
Ht>
cor
/ff
-------
KVB
GASEOUS EMISSIONS DATA
TEST SI'
TEST NO
DATE
TSJ-4 fM*
/Uu/t)clt
Probe
2-*
2-£
7
2.~t>
7
2
3
*f
5-
6
sofrttr
nu»ta*#6
tif'fft
/yv'
^vn*
*-.V»
>r«
/^y^
*.*»
^•v*
/P « 25
/4 *VC
_—
re C,
5--2S-7*
" ^/fotfes - 2-6
>*£ TK»&£. — 7
02
f. /
r<
f./'
f'f
*F £
*> f>
/fl-K
f.6
f' 1
1-1
+ 4
f f
C02
fo.*
/»•!
/e ,o
fO.o
/o.o
1'2-
4 ?
77
^.7
1.7
--
1 *
fr> o
CO -
ppm(dry)
2-fo
27°
/1o
2.7*
227
^S»
ggo
/TST
220
24$
W%%
^^
^y
Vz-T
ff2.tJ-
3»/
34&
3St
4^V
^V
2-T?
3t£
3K
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
NO
jppm(dry)
2J£~
27"
2-*»
2S*
zs»
25»
^SS"
•24°
7ZS
23°
•
5"2^
V^
W^
.?^2
J72
4/?V
/a^ff
^m&
373
^7V
•
^^r^f/u ^x«L
x^/ - 7* ^fCtfSSfi^
ff/^6 4/xv'ff^ <5^v4.
x*;j-
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
AVERAGES
5*^
3«t
Wtfr
w%%
wm
.^I'v
^/^
'4%%%
%jjjj%
Vssssss
*SS/Ssss
#?%;xx$
^^
gg^JS;
^J
cor
NO->
unc
plil
^^
^^^
^^^
cor
HC
unc
Wflk
Mtfjb
\&MA
cor
REMARKS
^Jftfar-estr
"^•^ = 7
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
-2V- 78
LOAD_
CONDITIONS_
DATA TAKEN BY
/?? J"
Probe
Position
Time
02
t
C02
%
(dry
co
ppm(dry)
unc cor
ppm(dry)
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO?
un c cor
HC
unc cor
REMARKS
» 57"
2.70
V/7
7-3
il.t,
/SO
•2.96
9.1
2^4
/O.I.
22T
1-
•27°
443
v//
'1$ /•>!
1,*
ff.e
2J6-)
25Z>
27"
ff.3
24°
fo.b
12.1.
f.2.
/o.e
11°
/SIS-
ZSS 3Sl
AVERAGES
e.es
38-?
NOTE: Parts per million (ppm) figures are corrected to 3%
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
f-2S~-
LOAD__ /a
CONDITIONS
DATA TAKEN BY
Probe
Time
02
%
(dry
C02
«
(dry
CO •
ppmtdry)
unc cor
NO
ppmtdry)
HOT LINE SAMPLES^ PPM (WET)
NOX
NO
NO?
HC
REMARXS
//a
= 93
* -71
6-
3/S
itrt- =
//•V
*f*t
3
/O.I
72?
II.2S
Vf*
27*
f.
AVERAGES
'tern
W///S.
W//4
NOTE
- Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
TEST SITE_
TEST NO
DATE
2,1
~-2(,- 7&
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
2-£
•7
6
5~
4
3
2.
4
7 _
S~
6
7
l-*>
Time
#*»
7/2$
##
1:$$
/•:K>
't>:z$
ft>;&
*:<&
tl.-*»
2,7*
i'.Zf
±
*•'!
14
4.}
7.3
^•7
7-7
$.6
&.7
ff.7
CO2
t
(dry
^*.y
ll.o
(6.k
/M
/o.$
/e.o
fO.O
(l.t>
/9.B
rl.*>
7/2,
/A*
II,"
CO •
ppm(dry)
unc
2/o
2Z»
2
/SS"
ff*
/s*
280
/»fo
•2S*>
/v*
38"
Z»o
24*
cor
3 06
2/3
42g
203
2.71
241
43-2.
;e4
3*7
25*
sis-s
/
V2S
5^2
V//
4&>
44*
4*1
437
393
4*7
4
-------
TEST SITE
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
3o
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Z-b
7
2-6
t~(f
~j
Time
///«
//:¥
f2.'
f2',3l
02
(dry
fl.5
//•7
f/,0
/e.»
/o.o
C02
(dry
9.7
7.9
e.t>
y,6
1.6
-
CO-
ppn(dry)
unc
m-
/<(»
fto
fZ
*?2
cor
^?z
272-
/•?«
/5~/
/5~/
NO
ppm(dry)
unc
2y»
2Je>
ZJ°
ZZ°
Z3*
cor
£f(Tt>
4/6^
37J
3LI
377
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
,
NO
unc
cor
NO->
unc
cor
HC
unc
cor
REMARKS
AVERAGES
NOTE
: Parts per million (PPm) figures are ^corrected to 3% O2
15' JO
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE LI-
TEST NO 3 /
DATE
FUEL /5V^5r^/f/l/
LOAD /
/Z2.
?2-
//°
f/°
/4°
0 •
(dry)
f7
/2/
/fz
/5V
/^y
/ff
253
N
ppm
/»^
//*>
/
K
REMARKS
AVERAGES
WM
Wtfc
'»
W/A
^^
^
«%%
g^^
«
^
^%%
W^
w%
m%
mzt
mz
%m.
mz
mat
sy/ss/Y
WM
W///,
ss/y///
'?/////'
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
TEST SITE
TEST NO
DATE
32-
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
%
(dry
C02
t
(dry)
CO
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOX
unc cor
NO
unc cor
NO?
unc cor
HC
unc cor
REMARKS
2-t
//.£.
/?*r
34
3S-/
/*.?
230
//. 6
1-1
/#. <•
2Z*
22*
MffP
22<=
AVERAGES
NOTE- Parts per million (ppm) figures are corrected to 3% 02
-
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
33
LOAD
-3°- 79
CONDITION5 /Hir>
DATA TAKEN BY
Probe
Position
"?
2--*
7
2. -6
7
Tine
//;/7
tr-&
H.S»
rz:/S
ft:&
02
%
(dry
it. A
9-1
7'5-
/*-?
1-s-
C02
\
(dry
/*-4
f*.t>
//y
e.t>
1.2.
-
CO-
ppn(dry)
unc
270
/?*
/*'
4rt>
3»S
cor
3V3
ZU
-2S*/
•7*1
V77
I
NO
ppn(dry)
unc
*£&B
22-
23"
24-
27'
• •
cor
36
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE t—
TEST NO -3-4
DATE $~-3*
FUEL
LOAD
CONDITIONS_
DATA TAKEN BY
Probe
(dry
C02
%
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPUX, PPM (WET)
NOX
unc cor
NO
unc cor
NO 9
unc cor
HC
unc cor
REMARKS
fl.*
32S
Stff
e.s
S7S
&:?.
an?
2-*
2*f
23S-337
9.*
f.f
Z.9I
f.8
//z
/if
2**
S64S
AVERAGES
WM
W#m
W%&
•'//////>
w%
mm
W%k
v/////,
WM
^P
Wfm
\mta
^^
Vwmi
vzzA
ma
W%
\z&A
NOTE- Parts per million (ppm) figures are corrected to 3% O2
274
159; >•
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
. -/£>.
_ 3 14
Probe
Position
Tim
02
(dry
C02
t
(dry
CO •
ppm(dry)
NO
ppm(dry)
unc cor
HOT LINE SAMPLES. PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
XT*
Z13
7
//;/.*
•2JTV
s/t
//*
/••
/t>0
iz-.sl
+
A 7
/to
/e.ti
ff.e
cl
0.
AVERAGES
1.*
vim
w%
tte.$2m,-22Z.s
m//,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
~ •
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
Position
Time
02
(dry
C02
\
(dry
CO •
ppm(dry)
unc cor
NO
ppm(dry)
unc cor
HOT LINE SAMPLES, PPM (WET)
NOx
unc cor
NO
unc cor
NO 7
unc cor
HC
unc cor
REMARKS
f.
32/7
61
7.3
255
- 43 V
/&>
.2*5
3
-52SS
38
•2-
e.i
Aisr
ZJS
-7
MS
7
ZSS-3&
AVERAGES
8.06
mat.
2V7
NOTE: Parts per million (ppm) figiores axe corrected to 3% 02
4 . VN
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE__ £•
TEST NO
DATE
FUEL_
LOAD
6-2-1*
CONDITIONS ۥ 3
DATA TAKEN BY
„-.. /^^g>f
fiiettjeeJf^
-------
KVB
GASEOUS EMISSIONS DATA
TEST SI1
TEST NO
DATE
Probe
2-&
2.
3
4
g-
6
7
2-6
•2.
3
4
/*•#
/0:4a
(9.S&
ff./3
M'.3o
//•5?
f2',3l
/2'.53
t3'*\
13'. 2'
DE C-
6-7-70
02
/y.z
//7
//^
/o.-?
/o.7S
//•V
/2.o
://,*
7/2<
// *
C02
1
(dry)
*-2
^^
^."
9.6
4-4
e.9
9.&
7.*
* & A
8.3
CO •
ppm(dry)
unc
3S"
t£
4*
3o
3>*
40
4*
3f
3£
3o
f7-4*"
cor
t*J
/33
78
5f
5T2
To.S
"75:4
7°
t(>
sit
4
2Z°
22.o
&SV
/IT
/jo
/?*
Jfs
2jo
cor
4/0*
4zl
s»*
4°$
39^
3fB
3f^
38 'z
3S*Z
3^1
36*
/44"9^ f-Us/tO)
/f& Jf jJoJ jts) •
Afyd 0&4. — ^SfccSS Oy //• 2,
C7-^>^
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO->
unc
cor
HC
unc
AVERAGES
1LKW
SfefrffM
—
— -
//3
^V
g.Zb
(f.<
w%%.
'///////,
'///////,
vvm
in
75
W%P>>383
wmn
w%?//
mm
£>$
yftvfc
'W%.
$Mt
'mA
%%%/.
HH
^^
\%&A
%%$%.
'jfttffr,
^HH
\&&A
mwfc
^^
W%k
\6ZOA
cor
REMARKS
NOTE
- Parts per million (ppm) figures are corrected to 3% 02
1590C
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
J~. 7~.
Probe
Position
2-1,
7
2.-6
7
•z--t>
7
Time
/
W,2£
M43
02
%
(dry
1,»
1-7
1-5
t.3
1*
T4
CO2
\
(dry
/". ^
1.*
/'•/
/0.3
/*.6
//.o
CO •
ppm(dry)
unc
*£
t/o
/f&
/fft>
/ft>
-/3
X57
/5V
*7
'4
NO
ppm(drv)
/v*
'16
/*»
/go
/*s~
/1*
cor
zs
3J2-
283
2.76
2?*
2?*>
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
NO-j
HC
REMARKS
AVERAGES
/Si
/*>.*.
/s-e
NOTE: Parts per million (ppm) figures are corrected to 3% 02
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SX1
TEST NO
DATE
Probe
•> — -^
•7
2-t>
2
3
4
g-
£
7
2—6
*>••*(•
fr-tt
if**
H'.l*
/f',
(t;
/e,1
CO •
ppm (dry)
^,<
^<
p-r
3f
3-
2°
^5 O
_^?^
^S"
25"
A//
ijp
41 1
£g~
•f*/
s$-
42-
4°
*{r>
38
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
NO
ppm ( dry )
unc
-?**>
225"
2.2$
22*>
2Z£
Z2S
26o
2&0
^^^O
^^JQ
•
cor
7-70
3!S*
«*?
4/09
4*7
3f7
.5^^
34/7
PI-7/
32/
•
£K*J.*.£.
sWJ
HOT LINE SAMPLES, PPM (WET)
NOX
unc
cor
NO
unc
cor
NO?
unc
AVERAGES
fi£/p$$>>$$
W/A
'5
NOTE:
Parts per million (ppm) figures are corrected to 1\ O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD
CONDITIONS
*,.— fr*?- ~
DATA TAKEN BY _ ^
Probe
Position
Time
02
I
(dry
COj
(dry
ppm(dry)
NO
ppm(dry)
NOx
HOT LINE SAMPLES,_ PPM (WET!
NO
NO?
HC
REMARKS
Z-3V
#,1
73
Z-K 3ti
//-Z
237
280
V/V
+5
/SS
242
22g 3S3T
AVERAGES
16.
w////,
W///,,
w///,
WM
m?/,
v/v
w////.
w///,
W////,
NOTE: Parts per million (ppm) figures are corrected to 3%
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SIT
TEST NO
DATE
Probe
2*J~b
-7
tj
z.
g-
£
2 *J-£>
7
2 V-4
/f/5j
•&>'&
Z».'3£
y)-,lo
z/:4c
22;*
ZZ'.(7
Z£:n
23'.9
CE ^
^ j^j •y ^y
C^ f f ^ g ^
02
^.2.
^0 <9^
?/*~
zt°
3*f,
N(
ppm(
^
Z65
273
23s'
^&£0
?SX
T^^^^
^7T
7>Mo
2Lo
FUEL
LOAD
CONDITIONS
DATA TAKEN BY
)
dry)
v-/
374
3Z*}
36 /
423
^43
*<&
37"
4/1
Tff
•
ȣ*&** &>+<-
/0o f^/M •
ff.S^o &K3SS&&
ij-Jl ~ *
2. K/XfA. Of,&*
^r»e>
HOT LINE SAMPliS. PPM (WET)
NC
2/0
)x.
223
N
2/7
AVERAGES
'BLKtw*
Mcc.4-
-,
f 3
if, 4
^./
// ^
vffifw
YS/fflSfr
-------
TEST SITE_
TEST NO
DATE
6-2.0-78
KVB
GASEOUS EMISSIONS DATA
FUEL_
LOAD_
CONDITIONS_
DATA TAKEN BY
£*<£&>
£>. ^
Probe
Position
Time
02
\
(dry
C02
\
(dry
CO •
ppm(dry)
NO
ppm ( dry )
NOx
HOT LINE SAMPLES, PPM (WET)
NO
REMARKS
1.2
3°
~7
1.1
/o.
277
f-/
70
Z8S-
A 2
42-
^-.-25
4*
&**>
-7
AVERAGES
/tf. 2
W///,
1-1
/e./
w///,
w////,
W////,
NOTE: Parts per million (ppm) figures are corrected to 3% O2
15900
-------
TEST SITE
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL f.
- 21 ~ -78
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
2.-t>
6
sr
4
3
2
a-4
#:&>
*&
02
%
(dry)
?.?
9.6
.•$
//.»
/*.$
1.&
C02
\
(dry)
1>L
/e.&>
/e.2.
3f
27
3"
cor
V?
3t>
33
3V
^
V^
V^
NO
ppw(dry)
unc
2.4°
*7sr
ztf
z*&-
23S
2S5
?41
cor
3^/
^<«>
3
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE 48 C
TEST NO
DATE
4*
FUEL £"&£•&')') £ot*s fltS'**!
LOAD f?0 tfft&/fr).
f-Z-J-je CONDITIONS t/*2y O.f? A
I/
DATA TAKEN BY SIT.
Probe
Position
2-^
2-6
2-t
2.-C,
2.-1*
•2.-L
2-£
z-t
z-f>
Time
/y;*»
/V/3C
#•4*
/y:*
/S'2*
&4S
• —
—
02
t
(dry
-
1.3
'/:3
1.3S
'*•
A3
#•3
f.s
fyts
C02
(dry
f.f
/tf.
/ff.f
/O.I
1.4
/*>.e
2&>
2&
•2tS~
cor
ijtfb
^Oi
3*/
3«a<-
^575
syi>
•
HOT LINE SAMPLES, PPM (WET)
NOx
unc
cor
NO
unc
cor
NO?
unc
cor
HC
unc
cor
REMARKS
Zf"e>fz#.
/£" &=&
^T** ^^C* >*-
«-* %9r^^^
/S"* «4
^^•"o^A-
f"o^A-
AVERAGES
^^
»
W/6
*w<
B79
317
39*
'wffm
'jtftffi
W///S.
W///,
I^P
^^
^^
#%^
x!v5>5^
YSSSsft
w//,.
w///,
^^
^^J
^^
^%^
s- " *&
XS-" o/tr^.
2^-/' o^^
NOTE: Parts per million (ppm) figures are corrected to 3%
-------
TEST SITE_
TEST NO
DATE
KVB
GASEOUS EMISSIONS DATA
FUEL
f^ttSfffT)
LOAD_
CONDITIONS_
DATA TAKEN BY
Probe
2-4
7
•Z-L
2-t>
7
Z-t>
•7
Time
//*>
//:*£
//:<&
//:*&
I-Z'.Z
as*.
te',s>
02
\
(dry)
fZ.f
t/.-»
'/).*
/o.<,
/o.6
-9-*
<*.*
CO2
\
(dry)
7*
7.3
7-V
s.t.
e.t>
1.*
1-9
CO •
ppm(dry)
unc
^5-
5&
S»
3*
2£~
•z*
/9
cor
/3«7
1*
74
S-2.
4Z
3^
27
NO
ppm(di-y)
unc
1-7*
/I*
/<*>
J<&
2*T
2?£
2/"
cor
373
372
3*2
33t>
3S3
3°8
3/6
•
HOT LINE SAMPIJES, PPM (WET)
NOX
unc
cor
NO
unc
cor
NOT
unc
cor
HC
unc
cor
REMARKS
AVERAGES
mm
vm.
NOTE
- Parts per million (ppm) figures are corrected to 3% O2
15900
-------
KVB
GASEOUS EMISSIONS DATA
TEST SITE_
TEST NO
DATE
FUEL
LOAD_
CONDITIONS
DATA TAKEN BY
Probe
•z-l>
-7
2-4
1
7,-L
7
Time
/V:i«
W3S
it:s&
/t:t°
><+:&
/y.'a
02
«
(dry)
•/».?
/f>.S
*A
*.»
1.2.
-7,1
C02
%
(dry)
ff.9
0.8
/*3
/».v
r/.6>
il,1
CO •
ppm(dry)
unc
4*
cor
72
4* 7/~\
4*
^t>
42
?2
4-7
74
tz*
111
NO
ppm ( dry )
unc
2^rr
•2/0
W
??£
/*>
-------
SOx DATA SUMMARY
Test
No.
Load
02
S02
(unc ppm)
SOl
(unc ppm)
SOx
(unc ppm)
S02
(corr ppm)
SO 3
(corr ppm)
SOx
(corr ppm)
Test Description
9.
6-73 .
674.S
. o
7,6
-7.3
USA
1.3
3.0
0f3
781
-712.°
V5-C
4-70
. -2.
/go. 7
ri
1.
• y
/e/z.
. f
/f/7.3
G.-2-
/•Z
/06Z.6
7.s
r
-------
Local
Date
Unit #
-S;Je C.
SOx DATA SHEET
Probe Location & Probe Length
Fuel
Load /*>
Test Description;
Test
No.
44*
44&
44 c-
Box
No.
/
3
Z
Sample
Time
23: lo
:z3 : 22.
- —
23 :s»
— '
Meter
Temp .(f)
//5~
//5-
/2-<>
/Z*
/£*-
/2-2-
Meter
^)press.
— ^> -^
{-
Meter
Reading
tf>. tfTrjp
/»^y?>
^» ^yp
/. <»?r2>
^#. tf>P
/,*&>
(p^'Baro.
Press.
^^3^
/
I
Port
|
'
Purge
Time
^*
«S»
&>
1
02
SI
x
CO
Q
U
Test #
Test # */*/&
Test #
Normality N
Dilution
Factor F
5pife
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
P + P
A - B
SO2
,/e>7
2
^•5?
^.7
SO 3
— '
/
2. 2.
^. /
2. •
?-/
3.2.
• —
__
3. 2-
/, / .
SOx
S02
2»
6.9
6.-?
&.
*r.<*
1T.1
^•l
£.°
£-«*-
6.°
SO3 ,
/
3.1
-
f.o
SOx
*7~
>!
SO2
SO2
(A-B)(N)(F)(460+T)(24)
V(P+p)
(/
SOS =
SO3 =
)24
SO2 @ 3% 02 =_
SO3 @ 3% 02 =
SOX @ 3% 02 =
>-7
)( )24
SO2
SO3 =
SO2 @ 3% 02 =
SO3 @ 3% 02 =
SOx @ 3% 02 =
/9IZ.O
t'1
,•'1
)24
SO2 =
SO3
803 =
SO2 @ 3% 02 =
S03 @ 3% 02 =
SOx @ 3% 02 =
-------
Local
SOx DATA SHEET
jf- '
Date 6- /7- "7& Probe Location & Probe Length "T2*-/- 2 • 2' •*"
unit f 6 -$;kc Fuel we&fan £*&J
Load /*° *lts*/hr.
Test Description:
Test
No.
?
*£
Box
No.
'
3
Z
Sample
Time
7.'2«r
714*
e:*g
ff'./f
013*
ff'.fS'
Meter
Temp.(T)
X2^
___
/2£
/^^
Meter
(f)press.
-0-
)
\
r
Meter
Reading
o.sr*
/.sr*
+.
/.**»
ff.*V»
7,evt>
Press.
C .
,1
1
Port
*
/
*^
Purge
Time •
e:e*
S!3o
ff f ,3^^
^y * £"£
£?* ' &fr
7:30
\
02
&.3
\
<
/
Test # Test # Test #
«
Q
W
Normality N
Dilution
Factor F
&i*C
Blank B
Averages
Ml. of
Titrant A
Averages
'SO + T
ample
Jol. V
+ P
A - B
SO2
,0/07
2"
2.2.
^-2-
•Z.2.
f.6
s:t
^' 7
f.t>3
S-7&
/.**»*
21.38
$*.(.3
SO3
• •
/
2.*
. —
—
2.*
.*
SOx
~
S02
—
2.e>
^7-T
f. f
S~.£~
Jif
S~?<>
£-.5-
SO3
/
2-f
z.f
.7
SOx
S02
•££>
&•?
-57^
^ 7
^^
jr.^
S03 ..
/
2.*
— ™'-
^. *
.^
SOx
^
»•
^
SO2 =
(A-B)(N)(F)(460+T)(24)
S02 =
S03 =
@ 3% 02
@ 3% 02
(3 3% 02
SO2 =
SO2 =
SO3 =-
SO3 =
S02 @ 3% 02 =
SO3 @ 3% 02 =
SOx @ 3% 02 =
•7^1
.o
(•fe)(" ) (' )(5)24
SO3 =
SO3
SO2 @ 3% 02 =
S03 @ 3% 02 =
SOx @ 3% 02 =
-------
Local
Date
Unit #
& - St
SOx DATA SHEET
Probe Location & Probe Length
Fuel <£0u>
Load
Test Description^
41*
Sample
Time
Meter
Meter
Meter
Reading
Press.
Port
Purge
Time
02
. /
V.1
Q
W
. a~pt>
4:2*5"
46 c
Test #
Test # "B
Test #
•
Normality N
Dilution
Factor F
Blank B
Averages
Ml. of
Titrant A
Averages
460 + T
Sample
Vol. V
+ P
A - B
S02
. ^>/0 7
2«
_ _
1
/
//. 3~
//. 7
//, 5T
//. ^
A /It*"
7- 7-v6
//.*
SO 3
/
/. *
—
—
/.*
/. «
SOx
S02
25-
f-7
/£>. *
f. f
f.jr<
^r^^
SO3
/
. *
—
. ^
. #
SOx
'
SO2
25-
?.*
4.6
4.L
f.6£
f.U
S03 .
/
/. /
• —
—
A/
„.- —
/. /
SOx
^
• ?"
^,
— "^
ffi
Q
E-
l-l
EH
SO2 =
S02 -
(A-B)(N)(F)(460+T)(24)
V(P+p)
•''
<**
5
503
)24
S02 @ 3% 02 =_
SO3 @ 3% 02 =
SOx @ 3% 02 =
7,
r
-------
BLANK PAGE
232
-------
SECTION 4,0
SPECIAL TEST DATA
PAGE
4,1 OVERFIRE AIR DUCT DIMENSIONS & SAMPLE
GEOMETRY 294
4,2 OVERFIRE AIR DUCT VELOCITY TRAVERSES 296
4,3 FLYASH RE INJECTION MASS FLOW RATES 333
4,4 MODIFIED SMOKE SPOT DATA SHEET 335
4,5 PARTICLE SIZE DISTRIBUTION - BRINK 337
- SASS 343
- BAHCO 344
-------
FRONT OVERFIRE AIR
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
FRONT OVERFIRE AIR
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
BACK OVERFIRE AIR -
% DIA
.021
.067
.118
.177
.250
.355
.645
.750
.823
.882
.933
.979
- MAIN PIPE
INCHES
.250
.795
1.40
2.10
2.96
4.21
7.65
8.90
9.77
10.47
11.07
11.62
- TOP - ID PORT
INCHES
.120
.380
.678
1.01
1.43
2.04
3.70
4.31
4.73
5.07
5.36
5.62
MAIN PIPE ID
INCHES
.200
.653
1.15
1.72
2.43
3.46
6.28
7.31
6.02
8.60
9.09
9.54
14 - 2.125 =
% DIA"
+ PORT
2.37
2.92
3.52
4.22
5.09
6.34
9.78
11.00
11.89
12.59
13.20
13.75
7.75 - 2.0
% DIA"
+ PORT
2.12
2.38
2.678
3.01
3.43
4.04
5.70
6.31
6.73
7.07
7.36
7.62
PORT 11.875
% DIA"
+ PORT
2.329
2.77
3.275
3.85
4.56
5.58
8.41
9.43
10.14
10.72
11.22
11.67
11.875 "DIA OF DUCT
5.75
- 2.125 = 9.75
-------
BACK OVERFIRE AIR - TOP DUCT ID PORT 9.75-2 = 7.75
SAME MEASUREMENTS AS REINJECTION
REINJECTION - ID PORT 10.0 - 2.125 = 7.875 ID
% DIA"
% DIA INCHES + PORT
.021 .165 2.29
.067 .527 2.65
.118 .929 3.05
.177 1.393 3.52
.250 1.968 4.09
.355 2.79 4.92
.645 5.07 7.20
.750 5.90 8.03
.823 6.48 8.60
.882 6.94 9.07
.933 7.34 9.47
.979 7.71 9.83
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
C.
SAMPLING LOCATION ;
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE '
NEAREST DOWNSTREAM DISTURBANCE
e>\i.
BARAMETRIC PRESS, in.Hg
_STACK PRESS., Ps , iwg
STK. GAS SP. GRAVITY,Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
1G.
17.
18.
Average
% OF STACK
DIAMETER
.
. d>"
. 2^S-o
,'77
, 11^
. eio'l
.oil
STACK GAS,VS = 174 Fg
SPEED
DISTANCE
FROM
INSIDE WALL
//.**
//• e 7
/o . 47
1.77
0. fo
^y, 6s
^. 2-1
2-. ?fr
2. 1
/ ^J
. Zi
VELOCITY
HEAD
( Aps) , in. HS0
—
•—
fi*4
i.?r
fi^
/. t>
1. f
2. 1
2 . 1
/. #
—
• —
—
/.
/. 7
/. «9
X •
/.
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO _
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE '_
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
STACK PRESS.
iwg_
JSTK. GAS SP. GRAVITY, Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
; 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
a,Yrr,-iOf>
% OF STACK
DIAMETER
.^7f
. 933
,002.
, $23
•7S*
. &4S'
• 3S£
. ZS-o
.f7-7
. u&
.Olel
, 02-1
DISTANCE
FROM
INSIDE WALL
//. ft?-
//. "-7
/0.141
f. 77
0. -
i£ - 76 • f ° &L/$e c .
OXYGEN
Si
STACK GAS
SPEED, Vs
ft/mi n
1
2l/° - / 2i~25~
7J- = S-=S-:T
7^ - 30. *
-------
Table C-ll-
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
BARAMETRIC PRESS, in.Hg_
J5TACK PRESS., Ps, iwg
STK. GAS SP. GRAVITY",GC
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Avcrnpe
% OF STACK
DIAMETER
, *J£~
. 355"
. 25"»
"77
. 067
,0-2-1
STACK GAS , Vs = 174 FS
SPEED
DISTANCE
FROM
INSIDE WALL
•
STACK •
TEMPERATURE
(Ts, °F
K
<**
*
I
(
}
i
I
&
/flu
OXYGEN
STACK GAS
SPEED, Vs
f t/min
x 3<>.ll
-------
Table C-ll. '
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)_
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS,in.Hg
_STACK PRESS., Ps, i wg
_STK. GAS SP. GRAVITY,Gg_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6-
7.
8.
9.
10.
11.
12.
13.
IS.
16.
17.
% OF STACK
DIAMETER
. m
, 1 33
, 882.
.82.3
. 7SV
. t>4£'
, 3S5~
. -Z.S~o
"77
. // &
. e-67
r O^l
- •-•
DISTANCE
FROM
INSIDE WALL
5", £2-
-S^.36
J"7 c?7
V- 7.3
-^/. 3/
-?. 70
21. ^V
/• V-3
/• e>/
< 67^
< 3 &
. /Z--,q «3 ^
1.00 ^
GS
STACK . •
TEI-1PERATURE
(Ts, °F
is-*
(
\
\
OXYGEN
STACK GAS
SPEED, Vs
ft/min
*.r C ^- /
f
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
, A c,
*/_/fc?_
SAMPLING LOCATION
INSIDE OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO "
OUTSIDE OF NIPPLE, (DISTANCE B)_
STACK I.D. (DISTANCE A - DISTANCE*
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
_STACK PRESS. , Ps , i wg
B)
_STK. GAS SP. GRAVITY, Gs_
-r*A
TRAVERSE
POINT
NUMBER
1.
2 .
3.
4.
5.
i 6.
7 .
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Average
1
STACK (
SPEED
f
% OF STACK
DIAMETER
.77?
,
, 6*/6
• 3S£~
• ~ZS*>
• IT?
. tie
•. 7
. P2.I
1AS,VS = 174 Fs
DISTANCE
FROM
INSIDE WALL
?.s*/
7/ ®9
€. t>
8>e>2.
-7.BI
b, 2.V
3> ¥&
2.^3
(• I'Z
1 1 /5~
. 6±3
. "ZJ>
Average
// A P(T + 46
V s
- 43. 77 &/£
VELOC:
HEAI
( APs)
. 3S~
' 3~7
• Z*?
. 36
, tJ'Z-
* 44
jj * 1
/I i
- —
0) 407
S
[TY
)
in. HS0
, •?.£"
- 42-
. *s4
* 44
i *{£~
f 4±T
' 4^
. 41
-——
—
1.00 '
5
STACK
TEMPERATURE
(T£, °F
*<* * *'
r*, — ~
OXYGEN
-5V
"*/
*1
STACK GAS
SPEED, Vs
ft/min
*
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
IXXTATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
BARAMETRIC PRESS, in.Hg_
_STACK PRESS.,Ps, iwg
_STK. GAS SP. GRAVITY ,GS
-rtft
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
IB.
i 6-
7.
8.
9.
icT.
11.
12.
13.
14.
15.
1 (,.
17.
1FT
hvfrrinP
% OF STACK
DIAMETER
.*7f
. ^ss
; ^6E-
. &7.Z
. 75P
,
.3SZT
>*zs*>
• /77
• /I8
i (^fa 7
« ^2- /
DISTANCE
FROM
INSIDE WALL
y.5^
"f, «>^
^. 6
8.02.
7,31
6. 2-V
3,46
2.43
/. 72-
/, /*"".
. 6&3
. 2-«>
VELOCITY
HEAD
( Ap_), in. HO
^> s
^c- ^
•
/. 2.
/ 2-
J.2-
/• /
/• /
/* /
/• /
•
IvBAr- &
/' •2-
/- 2-
/- 2-
/. 2.
/. /
/• /
/ /
/ 0
Average
STACK :•
TEr-lPERATURE
(Ts, °F
W/=
l
OXYGEN
STACK GAS
SPEED, Vs
f t/min
%> - /. /V-zf
STACK GAS,VS = 174 Fg A! A P (Tg* 460) 407 1.00 ' '» " ~' "^
SPEED " S Ps G^ - *P* = -5"'
?3 := 71. ** ""> ~ *-* °
-------
• Table C-ll. !
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
*/ -
SAMPLING LOCATION
INSIDE.OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE_
BARAMETRIC PRESS,in.Hg_
_STACK PRESS. ,Ps , iwg
_STK. GAS SP. GRAVITY,GC
NEAREST DOWNSTREAM DISTURBANCE_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
i 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
~ .
.
' .
eranp
% OF STACK
DIAMETER
.171
. 333
. B$2.
, 'S'iS
. 7SV
, 64£"
. 3S£~
. 2s&
•'77
.IIS
4 16&
I, 343
• ^2-1
. 5-2-7
VELOCITY
HEAD
( A p ) , in. HO
&(&r- A
—
— •
- —
. Z2.
i 2^>
* 24
.2.2.
.2-b
•
&fer-B
. 22
, 2^
. 2-3
.^5-
2_/cY
y//
•
Average
STACK GAS,VS = 174 F£ J A P (T + 460) 407 1.00 <
(/ S \n I lp / -
SPEED v *s ^s
STACK •
TEI4PERATURE
(Ts, °F
f'
/
_., . _ . ._
4-f*
*
OXYGEN
STACK GAS
SPEED, Vs
f t/min
/Mi*'., - 2,<7
3^x
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
c
£ -
SAMPLING LOCATION
INSIDE.OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO "
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE"
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE
7J.4C/T roP - of. 4.
BARAMETRIC PRESS, in.Hg_
STACK PRESS.,Ps , iwg_
B) STK. GAS SP. GRAVITY'Gc
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
1 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
(iyprnpe
% OF STACK
DIAMETER
, 77?
, 133
, eez
, &2-3
• 7S~D
. 64s
.355"
, 2s*>
• /77
./IS
.067
. C2-\
STACK GAS,V£ = 174 F£
SPEED
DISTANCE
FROM
INSIDE WALL
7-7/
*7 **? ^ /
h tf * I
£. *(•&
6~. 3°
-------
• Table C-ll-
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO _]
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO_
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
BARAMETRIC PRESS,in.Hg_
_STACK PRESS.,Ps , iwg
~STK. GAS SP. GRAVITY,Gc
NEAREST UPSTREAM DISTURBANCE
NEAREST DOWNSTREAM DISTURBANCE^
TRAVERSE
POINT
NUMBER
1.
2.
3.
4 .
c
i 6-
7
8.
9.
10.
11.
12.
13.
14.
15.
16
17
18
STACK
SPEED
% OF STACK
DIAMETER
171
. 133
g$2
923
7SV
645"
35-T
25TP
• /77
1 ,118
.obi
02-1
GAS,VS = 174 F,
•S :
DISTANCE
FROM
INSIDE WALL
7-7/
7. 3 4
6 14
6. tf-S
£~ 3°
S.°~l
z.7<7 I
/, 3^3
, £~
VELOCITY
HEAD
( A ps) , in. HS0
3 */
'3, 3
3. 2.
3 . 2-
3 1
"3. /
Average
- —
—
~
3. 1
3 . 3
3- 2-
3. 2-
3. 3
3, 3
!• • 1 1 IliMTM
- 1 2.1. 1 4 £^~/st<- .
STACK •
TEMPERATURE
(Ts, °F
^
t 1
\
1
A- ^
^ - 3
OXYGEN
STACK GAS
SPEED, Vs
f t/min
r. 22-43
0. if
-------
Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO._
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL TO
BARAMETRIC PRESS, in.Hq
OUTSIDE OF NIPPLE, (DISTANCE B)
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE _ ~
NEAREST DOWNSTREAM DISTURBANCE _
J5TACK PRESS. ,Ps , iwg
STK. GAS SP. GRAVITY^GC
— -T/TB
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
1 5.
; 6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
(^yprnpp
% OF STACK
DIAMETER
.1*1
. 433
. 6^2
. 'SIS
- 7$T>
. 64s-
. 3S£~
. 2S*>
• 111
. 118
. ok>1
>02-l
STACK GAS,VS = 174 F£
SPEED ^
DISTANCE
FROM
INSIDE WALL
7-7/
7,34
6. f*/
6. 48
6~. 3°
/. ^63
1, 343
, ^2-^.
. 5"z-7
« it>£~
VELOCITY
HEAD
( Aps), in. HgO
tfit-fl
,61
>tt
, (,£•
. -71
. 71
.
W&>r- (3
—
• 63
. ^5"
• t>7
• b11-]
• k^
, 63,
—
—
. —
Average
VA P(T * 460) 407 1.00 '
^ s l?T"^ •
STACK
TEMPERATURE
(Ts, °F
M
1
V
f
^
/
-7
/
/*
OXYGEN
I
STACK GAS
SPEED, Vs
f t/min
it &4*?3
tr-trd
'^ •• _ ij~j T
% -= 3e-<=l
7^ - ^ f , o
305
-------
•• Table C-ll.
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION NO.
DATE
SAMPLING LOCATION
INSIDE .OF FAR WALL TO
OUTSIDE OF NIPPLE, (DISTANCE A)
INSIDE OF NEAR WALL T0_
OUTSIDE OF NIPPLE,
STACK I.D. (DISTANCE A - DISTANCE B)
NEAREST UPSTREAM DISTURBANCE_
BARAMETRIC PRESS, in.Hg_
(DISTANCE B)
_STACK PRESS. ,Ps , iwg
~STK. GAS SP. GRAVITY, Gc
NEAREST DOWNSTREAM DISTURBANCE_
TRAVERSE
POINT
NUMBER
1.
2.
3.
4.
5.
• fc
7
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
Averape
% OF STACK
DIAMETER
. *7?
. 962-
. €2-9
. -73-0
. <**/3~
• 3SS~
Z&o
./-77
.//*
.02.)
DISTANCE
FROM
f3. 73T"
/3 2.
/2 . 3~1
it.gr
tl.c
1.76
.5-. «> ^4