oEFA
United States Industrial Environmental Research
Environmental Protection Laboratory
Agency Research Triangle Park NC 2771 1
Application of
Combustion Modifications
to Industrial Combustion
Equipment
(Data Supplement A)
Interagency
Energy/Environment
R&D Program Report
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
6. Scientific and Technical Assessment Reports (STAR)
7. Interagency Energy-Environment Research and Development
8. "Special" Reports
9. Miscellaneous Reports
This report has been assigned to the INTERAGENCY ENERGY-ENVIRONMENT
RESEARCH AND DEVELOPMENT series. Reports in this series result from the
effort funded under the 17-agency Federal Energy/Environment Research and
Development Program. These studies relate to EPA's mission to protect the public
health and welfare from adverse effects of pollutants associated with energy sys-
tems. The goal of the Program is to assure the rapid development of domestic
energy supplies in an environmentally-compatible manner by providing the nec-
essary environmental data and control technology. Investigations include analy-
ses of the transport of energy-related pollutants and their health and ecological
effects; assessments of, and development of, control technologies for energy
systems; and integrated assessments of a wide range of energy-related environ-
mental issues.
EPA REVIEW NOTICE
This report has been reviewed by the participating Federal Agencies, and approved
for publication. Approval does not signify that the contents necessarily reflect
the views and policies of the Government, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/7-79-015b
February 1979
Application of Combustion
Modifications to Industrial
Combustion Equipment
(Data Supplement A)
by
K.T. Fisher, H.J. Buening, W.A. Carter,
P.K. Engel, S.C. Hunter, and R.J. Tidona
KVB, Inc.
17332 Irvine Boulevard
Justin, California 92680
Contract No. 68-02-2144
Program Element No. EHE624A
EPA Project Officer: Robert E. Hall
Industrial Environmental Research Laboratory
Office of Energy, Minerals, and Industry
Research Triangle Park, NC 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, DC 20460
-------
Limitations On Application Of Data Reported
The data cited in this report are test results for measured pollutant
emissions from a wide variety of,industrial combustion equipment types. Only
a limited number of each equipment type could be tested. Therefore, these
emission levels are not suitable for use in estimating mean emissions from
industrial combustion equipment classes and should not be used alone in
compiling area-wide emission inventories. Also, they are not suitable for
predicting emissions from any one process or as regulatory limits or emission
standards. Use of these emissions as emission standards may place a large
proportion of the industrial combustion device population in noncompliance.
The data can however be of use in supplementing other data used for these
purposes. The purpose of this test program was to investigate the feasibility
of combustion modifications for emissions control, not to develop a compre-
hensive emissions data base.
Suppl. A
-------
CONTENTS
Page
FOREWORD iv
INSTRUMENTATION ' vii
GLOSSARY viii
CONVERSION FACTORS ix
SITE LOCATION NUMBER
Data Supplement A
1 Ceramic Tunnel Kiln 1
2 Internal Combustion Engine 10
3 Rotary Kiln 36
4 Petroleum Refinery Heater 58
5/1 Process Heater 136
5/2 Process Heater 178
6 Aluminum Melting Furnace 216
7/1 Petroleum Process Heater 225
7/2 Petroleum Process Heater , 275
7/3 Gas Turbine Combined Cycle 303
8 Gas Turbine Combined Cycle 338
9 Rotary Kiln 387
Data Supplement B contains the following location numbers:
10/1 Wood-Bark Boiler 491
10/2 Black Liquor Recovery Boiler 525
11 Carbon Monoxide Boiler 599
12/1 Petroleum Process Heater 624
12/2 Petroleum Process Heater 645
13 Wood-Bark Boiler 690
14 Open Hearth Furnace 763
15 Diesel Engine 820
16/1 Steel Billet Reheat Furnace 891
16/2 Steel Ingot Soaking Pit 914
Suppl. A
-------
FOREWORD
The purpose of this Data Supplement, which is presented in two volumes,
is to document data in greater detail than was practical in the final report
for this contract. It is intended to provide the necessary details to other
researchers who are interested in performing their own analysis..
Readers are referred to the contract final report for information
as to objectives, selection of units, measurement procedures, interpretations
and conclusions.1
All data presented for gaseous emission concentrations of NO, NO ,
X
CO, HC, S0_ and SO are expressed in parts per million by volume (ppm) on
a dry basis corrected to 3 percent O2 by volume (dry) in the flue gas.
The data are arranged in this volume by Location Number for Locations
1 through 16. A location is defined as one company or plant in which one or
more units were tested. Each unit tested at a location is identified by a
unit number. The contract final report refers to the test number when data
are discussed. The test number is of the form xx/yy-zz, where xx = location
number, yy = unit number, and zz = test number on that unit. For sites where
only one unit was tested the /yy unit number is deleted.
Hunter, S. C., et al., "Application of Combustion Modifications to Industrial
Combustion Equipment," EPA 600/7-79-105a, January 1979.
Suppl. A iv
-------
For each unit tested, the data supplement contains the following
information:
1. Equipment Design Data
Design data tabulations include: unit description, installation
date, process capacity, burner description, fuels burned, combus-
tion air temperature and other data pertinent to each unit.
2. Mobile Laboratory Data (Emission Measurements)
Emission measurements tabulated for each test include test number,
test load, combustion conditions (excess 02, CC>2), gaseous emis-
sions (NOX, NO, CO, HC, SOX and SO2 all at 3% O2, dry), total
particulates and solid (filterable) particulates, thermal
efficiency, Bacharach smoke spot number, and plume opacity.
3. Operating Data
Data pertinent to the process is tabulated for each test.
4. Fuel Analyses
Analyses of test fuels are included as reported for fuel samples
collected during tests.
5. Particulates Measurement Data
Particulates data includes measurements of total and solid
particulates by EPA Method 5.
6. Cascade Impactor Data
Impactor data include impactor flow conditions, stage collection
weights, and calculated aerodynamic particle size for each stage.
One impactor used was a Brink Model B (BMS-11) with the following
stage dimensions:
Spacing of
Jet No. Jet Dia., in. Jet Opening, in.
1 0.249 0.747
2 0.1775 0.533
3 0.1396 0.419
4 0.0946 0.282
5 0.0731 0.220
Suppl. A
-------
The second impactor used was an Ander.son 2000 Mark III with
the following stage dimensions:
Stage No. Jet Diameter, cm
1 0.1638
2 0.1253
3 0.0948
4 0.0759
5 0.0567
6 0.0359
7 0.0261
8 0.0251
7. Opacity Data
Plume opacity was observed by EPA Method 9.
8. Stack Traverse Data
Stack traverses are made with a pitot tube.
9. Trace Species and Organics Sample Data
Sample acquisition logs and results of sample analyses by
atomic absorption, spark source mass spectrometry, wet
chemistry, gas chromatography, and gas chromatography/mass
spectrometry are included.
Dash marks entered on the data forms indicate that data were not
available.
Suppl. A vi
-------
INSTRUMENTATION
The emission measurements were made with instrumentation contained in
a 2.5 by 9 meter (8 by 27 ft) laboratory trailer. The gaseous emission
measurements were made with analyzers located in the measurement console in
the trailer. The particulate concentration, particulate size, sulfur oxides,
and trace species concentration measurements were made with instrumentation
prepared in the wet chemistry area of the laboratory and taken to the sample
port. The weighing and titration were done in or near the laboratory.
The emission measurement instrumentation used for the program was
that shown in Table 1. The operation of the instrumentation is discussed
in detail in the contract final report.
TABLE 1. EMISSION MEASUREMENT INSTRUMENTATION
Emission
Symbol
Measurement Method
Equipment Mfgr s Model
Nitric oxide
Oxides of nitrogen
Carbon monoxide
Carbon dioxide
Oxygen
Hydrocarbons
Sulfur dioxide
Sulfur dioxide
and trioxide
Total particulate
matter
Particulate size
Smoke spot
Opacity
Trace Species
and Organics
NO
NO
y
CO
co2
°2
HC
S°2
so2
S°3
PM
. TSSO
Chemiluminescent*
Chemiluminescent*
Spectrometer*
Spectrometer*
Polarographic*
Flame ionization*
Photometric*
Absorption/
titration
EPA Std. Method 5
Cascade impactor
Reflection
EPA Std. Method 9
EPA SASS Train
Thermo Electron, 10A
Thermo Electron, 10A
Beckman, 864
Beckman, 865
Teledyne, 326A
Beckman, 402
Dupont 400
KVB Equipment Co.
Joy Mfg. Co.
Monsanto-Brink, B(BMS-11)
Anderson 2000, Mark III
Research Appliance Co.
Acurex/Aerotherm SASS
*Precision, + 1% of Full Scale
Suppl. A
vii
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GLOSSARY OF SYMBOLS USED ON DATA FORMS
Burner Type
Air
ChGrt
Pulv.
Ring
SpStk
Spud
Steam
Test Type
Air Reg
Atom Press
BOOS
Base
BrTune
CombCyc
Damper
HiAir
HiLoad
LowAir
LowLoad
LowNOx
NrmlAir
OFA
SCA
SnglCyc
Steamlnjec
VPH
Viscosity
Air Atomizer
Chain Grate
Pulverizer
Natural Gas Ring
Spreader Stoker
Natural Gas Gun
Steam Atomizer
Test Fuel
Coal
NG
Ref.Gas
NG/#6
#2
#5
#6
PS300
Air Register Adjustment
Burner Atomizing Pressure Adjustment
Burners Out Of Service
Baseline
Boiler Tuneup
Combined Cycle
Air Damper Adjustment
High Excess Air
High Load
Low Excess Air
Low Load
Low NOx Condition
Normal Excess Air
Overfire Air
Staged Combustion Air
Single Cycle
Steam Injection
Variable Combustion Air Temperature
Fuel Oil Viscosity
Coal
Natural Gas
Refinery Gas
Mixture, NG. and #6
No. 2 Grade Fuel Oil
No. 5 Grade Fuel Oil
No. 6 Grade Fuel Oil
Pacific Standard Fuel
Oil No. 300
Suppl. A
viii
-------
CQ
H-
X
CONVERSION FACTORS
SI Units to Metric or English Units
To Obtain
g/Mcal
106 Btu
Btu
lb/106 Btu
ft
in.
ft2
ft3
Ib
Fahrenheit
Fahrenheit
psig
psia
iwg (39.2 °F)
106 Btu/hr
GJ/hr ,
From
ng/J
GJ
gm cal
ng/J
m
cm
m
m
kg
Celsius
Kelvin
Pa
Pa
Pa
MW
MW
Multiply By
0.004186
0.948
3.-9685xlO~3
0.00233
3.281
0.3937
10.764
35.314
2.205
tF = 9/5 (tc) + 32
t = 1.8t - 460
•F K
P . = (P ) (1. 450x10 )-14. 7
psig pa
P . = (P ) (1.450x10 )
psia pa _3
iwg pa
3.413
3.60
To Obtain ppm
at 3% O_ of
Natural Gas Fuel
CO
HC
NO or NO
x
SO_ or SO
2 x
Oil Fuel
CO
HC
NO or NO
x
SO_ or SO
2 x
Coal Fuel
CO
HC
NO or NO
x
SO or SO
Multiply*
Concentration
in ng/J by
3.23
5.65
1.96
1.41
2.93
5.13
1.78
1.28
2.69
4.69
1.64
1.18
*These conversions depend on fuel composition.
The values given are for typical fuels.
-------
I .
> Vo Obtain
ng/J
ng/J
GJ
-
CB
•2
B3
kg
Celsius
x
Kelvin
Pa
Pa
Pa
MR
MR
English and Metric Units to SI Units
Fron
lb/106 Btu
- g/Mcal .
106 Btu
ft
in.
ft2
ft3
lb
Fahrenheit
Fahrenheit
psig
psia
iwg (39.2 °F)
106 Bto/hr
GJ/hr
Multiply By
430
239
1.055
0.3048
2.54
0.0929
0.02832
0.4536
t = 5/9 (1^. - 32)
C K
t = 5/9 (t - 32) + 273
P = (P . + 14.7)(6.895xl03)
pa psig
P = (P . ) (6.895x10 )
pa psia
P = (P. ) (249.1)
0.293
0.278
Multiply*
To Obtain Concentration
ng/J of in ppm @ 3% O0 by
Natural Gas Fuel
CO
HC
NO or NO (as NO )
S0_ or SO
2 x
Oil Fuel
CO
HC
NO or NO (as NO )
SO or SO
Coal Fuel
CO
HC
NO or NO (as NO )
SO_ or SO
0.310
0.177
0.510
0.709
0.341
0.195
0.561
0.780
0.372
0.213
0.611
0.850
•Ibese conversions depend on fuel composition.
Hie values given are for typical fuels.
-------
CERAMIC TUNNEL KILN DESIGN DATA
Location No. /
Unit No. /
Unit Description Ttt£
A
Sett,
fc># y 6 o?/e S
Installation Date
Process Capacity
Burner Description
Test Fuel
Fuel Temp, at Burner (°F)
Primary Air Temp. (°F)
/f,TV
600 TH£RMS/V££k.
tfofifH 4rf£K\CA» ZZI-I
NATURAL. 64$
AMtteti r
JM0t£fr
.
Comments:
-------
Test Number / - /
Onit Number TVMft ftltM
Fuel l-A. M4rt/#Al &A&
Capacity (kt/hr)
Furnace Type Tt/Af/^fft. KUAf
Test No. to
K V B, INC. „ . „ .....
Test Engr . W4 C
MOBILE LABORATORY DATA
Date AftlL f. 1176
MO, 2- Owner
Location
Identification
' Burner Type t/0. AH£t1C/(tf 223"
i
1. Test Number
2. Load (k#/hr) or Btu/hr
3. Flue Diameter (ft)
4. Probe Position
5. Process Rate
6.
7. Water Content (% vol.)
8. Oxygen (%)
9. NOxfhot line) readina/@3% O?(DDm)
10. NO (hot line) reading/33% 02
11. N02(hot line) reading/63% O2(ppm)
tn itnir ili-ir fl 3t O (hot line) mm
13. MO dry 0 3ft O2 (hot line) (ppni)
U. NOg dry 0 8% Oa (hot i,ino) (pp»>
15 . Carbon Dioxide (%)
16. Carbon Monoxide (ppm) uncor./cor.
17 • Hydrocarbon (ppm)
18 . Sulfur Trioxide (ppm)
19. Sulfur Dioxide (ppm)
!0. Total Particulate (g/Mcal)
!1. Total Particulate (Ib/Mbtu)
12. Smoke Number
3. NO (cold line) reading/dry 63% (ppm)
M.
S. Atmos. Temp. (FVC»)
£. Dew Point Temp. (F»/C*)
i7. Atmos. Pressure(in.Hg)
t'l
£'*('
c/*rr£*
if «-'*£-Y>t/.
177*
If
6
11
ft
2(
3.(
ff
21*
11
-
-
~
-
-
2.0
10
7o*r
60* f
21.10
S"f70
1-2
£'*('
eevTf*
" etty^
10: 00
If.
13
II
2.
77*
ff
tff
g
t.2
7f
?/y
If
-
-
—
-.
—
13.
f*
67
ri
3*. oo
(??•
1-2
f'xf'
cenTf*.
11:30
17.
20
11
1
0%
1*
16
i
3.
}o
H
i*f
19
—
—
—
—
-
17 \ 77
f2.f
ft
21.11
777.
/'i
('*<'
f* £ Ai^f 0
f * Cr K
1 «V 4^ 4^
17.^7.
ff
If
I
7Z
gg
if
s.i
{0
27f>
»7
It
73.
f6
fl
21.10
677.
60-3
-------
OPERATING DATA
Tunnel Kiln No. 2
Fuel L.A.
Page 1 of 2
Data taken
Test No.
Time
Date
Process rate
Test
Description
Pre Heater Temp.
T/C #3
#10
#14
#15
Main Furnace
Temperature
T/C #16
#19
#22
#25
#27
#29
Rapid Cooling
System
T/C #32
#34
#37
#39
Exit End Recirc.
System
T/C #43
/-/
/J57
y-/-?^
If C*tS.r
^krs.
tAWVZ
310
HHO
7tt
?7?
121
nsi
IHI2
1722
1110
2&) 0
121*
\22V
Hfl
1050
evr
I -2-
1-7-76
If f*#S/"
<%? hM.
r*#r.
ZV?
V7*
$0*
$30
i*
H-$-7(
If fAft&S
S$1 krs.
0#S£lffiJf
zrr
ytt
tit
103
1(1
1/12
IH60
mf
1101
2000
11 go
izif
1167
1*71
6$0
1-1
Ii't7
1-*-76
16 f*tSS
/2H hrt.
P4$/W£
ZfJ-
V 7*
fli
711
1ft
n?3-
Mft>
1720
1*11
111*
1 112.
121*
lie?
1071
€60
-------
OPERATING DATA
Page 2 of 2
Rapid Cooling
Fan Temp.
Final Cooling
Fan Temp.
Furnace Pressure,
in. W.C.
Fuel Flow
Start
Time
End
Time
South side
burners in
service
North side
burners in
service
H6*
V/
H''t7
2Z
*c
m
Hit
+ .07
x
mvpoo
in?
*$
2£
• .
•
-
-------
Location 1
Sampling and Gas Chromatographic Analysis
Non-Combustible Gases
Carbon Dioxide
Oxygen
Nitrogen
Water Vapor
Methane
Ethane
Propane
i-Butane
n-Butane
Pentanes
Hexanes
Heating Value
Gas Density (air-1.00)
0.35 (% by volume)
0.12
0.37
0.050
Combustible Gases
94.52
4.26
0.20
0.025
0.037
0.032
0.032
1042 BTU dry/SCF
0.575
-------
Test So. /- .2.
PARTICIPATE EMISSION CALCULATIONS
Date ^-7~7( Location /
H.
Engr.
Unit No. KttM
FuelX//*;:
Load JOY
** ff
Pi tot Factor, Fs
, f 3
Barometric Pressure, P 3O.OO in. Hg
Tot. Liquid Collected, V^ 81. 3 ml Total Particulate, M J/. f m gm
Velocity Head, AP , Ot iwg Stack Temp., Ts /"?/" "R Stack Area, As 5£ ft
Sample Volume, Vm /3f,VjFt3 stack Press., Psg -,75 iwg Excess O0, XO.» /^. 7
Orifice Press. Dif f., H /, /^ iwg Stack Gas Sp. Gravity, Gs
Sample Time, 6 tf2- min Nozzle Dia., Dn/i
2
n.d.
An. Meter Temp., T ^75 "R
•1. Sample Gas Volume Vm - 0.0334 Vm(P^ + H/13.6)
std i bar
2. Water Vapor ""•~vwstd = °-0474 vlc
3. Moisture Content Bwo = Eg. 2/(Eq. 1 4- Eq. 2)
4. Concentration a. C = 0.0154 Mn/Vm
std
b. C = 2.205 x 10~6 Mn/Vm
c. C «= Eq. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P,
std
3
-bar x 13'6 + PS9\
6. Stack Gas Speed Vs = 174 Fs /APIs
7. Stack Gas Flow a. Qsw = Eq. 6 x As x - x .,_
Rate @ 70CF Ts 40V
b. Qsd = Eq. 7a x (1. - Eq. 3)
8. Material Flow Ms = Eq. 7b x Eq. 4b x 60
9. XO factor
10. Emission
11. % Isokinetic
XO f - 2090/(20.9 - XO %)
a. E = Eq. 4b x Fe x Eq. 9
b. E = Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vm + Vw . .)
std std
I -
8 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0. 002636
SCF
SCF
.03.7 N.D.
grains/DSCF
I, Of 7 tie'* grams/DSCM
1*7,27 in. w abs.
. <* ft/min
WSCF/min
2*13? DSCF/min
l.07£ Ib/hr
Vf 7. / N.D.
, f X
j 2 .1 1 ng/ joule
•Multiply Vm . by 53Q/T (CF) if meter not temp, compensated.
Data Sheet 6002-4
-------
PARTICULATE CALCULATION SHEET
Test No. / -
Box No. /
Test Description:
(Inlet, Outlet)
Location
Test Date'
- 7-
Dry Gas Meter Vol (ft3)
Final
Initial"
Total/ *£,„ t/f
Final
Initial
Impinger Water Vol (ml)
•rot**-
«/.*
Total
£00
L lit
Beaker No.
£-_
Filter
No.
Blank
No.
Date
Weighed
.
*/- 7~7t>
V-7-76
,£3//
Tare
Wt.
/O //
/«/,
lit
4_
5_
£
Avg
9&.9178
Bottle No.
Content
Probe
(Acetone)
•Probe
(Water)
(Acetone)
Hinse (ml)
/eo
Date . 4-f-7k
Weighed or 250 Bake)
Final
Wt. 250
1/60.
ft>f.
itt,
Avg
/0/.6Z.7*
Residue Wt
Final 250 Tare)
Date
Weighed or 650 Bake)
Final 1^
Wt. 650 2
Avg
Residue Wt.
Final 650 Tare)
Comments:
A=
A f. octal1
toJP.H&J
-------
Date 1-7-7* Location
Load ic/m kH. Kl/hr or MBtu/hr
K V B. INC.
STACK DATA
/ Unit T
Test Ko. I'-Z
Kngr.
Fuel Mr.
Sample Box No.
Filter No. / &MK Z.
Meter Box No. f Probe Ko. / Probe Length j'
%
• °F
'/A in.
SO.OQ in.Hg
i
diam.
Filter Beater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather jtfNflY VAAM
Stack Gas Pressure, PS -.yjf iwg
Abs. Stack Press., AP-P +407- iwga
Stack Gas Sp. Gravity, Gs n.d.
Stack Area, As £t2
I
Remarks
Final Me ten
Initial Meten
1 1 <". ¥ /
Time
1031
1*00
ISIf
Hit
Total
Avg.
vm
Meter
Volume
Beading
(CF)
f^i.VI
701.9*
7(t.O«
7t0.fl
Vacuum.
Gage
Reading
(iwg) '
ir
t.f
7
ft*
Pitot
Tube
Pressur
(iwg)
.97
.0C
.Of
H
Orfice
Pressuri
Diff
(°F)
l.9f
1.11
1.00
•
Stack
Temp.
(°F)
If*
t*0
itr°*
°F
f 460
Xmpinger
Temperature
Out
(6P)
190
wo
If
'
•
In
(°F)
/f*
2fO
*?o
Filter
Box
Temp.
(°F)
9*0
*10
sto
Meter
Temp.
(°F)
110
110
IfO
8
-------
SMOKESTACK FLOW PROFILE
TEST NO.
LOCATION N0._
PATE A Ml I
SAMPLING LOCATION fl/AfiJ4Ce
INSIDE OP 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
BATSMETRTCpRSSS, in.Hc
_STACK PRESS.,Pfl, iwg -.73
B) STK. GAS SP. GRAVITY,Gfi
TRAVERSE
POINT
NUMBER
i. \.S mr
2. 1.5"
3. l.f
4. 3
5. 3
6. 3
7. <¥.*"
8. V.T
9. ¥.*"
10.
LI.
L2.
L3.
L4.
L5.
L6.
17.
L8.
kveraf*
•STACK
SPEED
% OF STACK
DIAMETER
GAS,VB • 174 F,
DISTANCE
FROM
INSIDE WALL
I.S"
3
*. '"
• t"
1
V.5"
.f
\
Htf
V f
Av«raq«
,y 4P(Ts*46
VELOCITY
READ
( Ap(), in. R_0
v —
*.tf 3 .173
*.I1 .1?*
.Of .»*V
.19 ,9/f
.01 .100
.01 ,*••
(-). a. o
.to .3i(
£ A.Ott
<*.*1
4M*
-------
INTERNAL COMBUSTION ENGINE DESIGN DATA
Location No.
Unit No.
Unit Description
r
Installation Date
Test Fuel
Fuel Temperature (°F)
r
Primary Air Temp. (°F)
Air Supply
Engine Speed (RPM)
3**
Comments:
1 0
-------
Tedt No
. 2- \
MOBILE LABORATORY DATA
Date y-2 &~76 Location .2-
Unit No.
: CAS Capacity ftO H1°
Unit Type\
Burner Type
Test No.
Engr. WA C-
1. Test No. v
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen . (%)
9. NOx (hot) read/3% QZ (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NOo (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (0F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
/
1200
It*
661
&'
130
#
\(7o
3
1075"
•jq
U
5*
/
2.
\3oo
12
9H5
710
ff
75~O
,7
1932
ni3
//?
1626
6.0
5?o
HH1
••
$
I33O
12
1?o
$00
$0
100
.5*
I7ff
UW
W
IW6
£.0
170
\
ftf
«-/
12
22$"
7*?
HO
l$o
f.
5*00
,?
1717
lf£2
*?
WOO
O
\o?\
£
IHHO
12.7
100 tf£2
130 woo
If2
tOf I7H6
5*. f
}JTO 7f1
*Correction to 3% 0, should not be performed if
the value is measured on a wet basis.
11
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date 1-20*76 Location
Test No.
Engr. KM C-
. £45 Capacity $10
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% Oa (ppm)*
11. NO? (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
£
I?0O
12.
1/0
&f
110
*?* (
3(0
1$
\^
iteo
./tr
I72i
?r
7??
-
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
1 2
Data Sheet 6002-2
-------
Test No..
Unit No.
MOBILE LABORATORY DATA
2-~2- Date 1-3-1-76 Location
Test No.
Engr.
Fuel/MiC GAS Capacity
Unit Type
Burner Type
Id Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/eor
IS. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A tiros. Temp. (*F/*C)
19. Dew Point Temp. (*F/*C)
20. Atmos. Pressure (in. Her)
21* Relative Humidity (%)
23.
24.
25.
26.
27.
28.
Sfl- — _
2-
I3t
I ^
110
t(0
s-o
1(2
r.
2?f
(990
7
6
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7
7
111
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a t ^*
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7$
9£0
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27$
tfOQ
10
2S~
2IW
/f7V
171
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7
f 9^9
1?
/*•
too
feO
10
120
f.
275
000
ro
i
im
1117
11?
WI7
6
w
11
IS.
$65"
100
6f
£
2W
iiW)
fO
25"
2001
Ifff
IS!
1100
\6
?12
•
IHHo
13.3
100 21*^
n$ tut
7? \76
100 \f?0
f.7
2(0 (02
tfQQ
„
•Correction to 3% 0, should not ba performed if
tho value is measured on a wet basis.
Data Sheet 6002-2
1 3
-------
Test No. 2 "" -?
Unit No.
Date
MOBILE LABORATORY DATA
Location -2-
Test No._
Engx.
Capacity__£££_J//f_
Unit Type_
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
-2-J/f
lt>IO
IMS'
7$e>
7/5-
65*
710
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71S
67?
70
670
€.
310
2700
tr
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£70
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210
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\77£
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7
976
2.-H A
lS0e
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67*
60
6?$"
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300
3000
0
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13.3.
7?5 \7i2
HO iff*?
75 173
65VIFOO
5~.f
160600
3801
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
\ 4
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No._a2~-£__ Date j'22~7» Location
Test No._
Engr.
Unit No.
Fuel MT. GAS Capacity
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atroos. Temp. (°F/CC)
19. Dew Point Temp. (°F/eC)
20. A twos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
2-S 'A
0*115
13.
620
500
\20
SoS
5".
310
5000
3
WW
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13.3
630
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560
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117
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MBIftiT
20.615
2.0
1.0
1.0
l.o
O.I
o
\25~
*
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
1 5
Data Sheet 6002-2
-------
OPERATING DATA
Location 2
Date:
Data Taken By; WA
Test No. ;
* /
Time
pMlHJA L
Engine Speed (RPM) flVCTVATtDtJS
Current Exhaust Temp. (°P)
No. 1
No. 2
No. 3
No. 4
No. 5
No. 6
No. 7
No. 8
First Stage Inlet Press, (psig)
First Stage Inlet Temp. (°F)
Second Stage Discharge
Press, (psig)
Ambient Air Temperature
Dry Bulb (°F)
Wet Bulb (°F)
Relative Humidity (%)
Manifold Vacuum (in. Hg)
Barometric Pressure (in. Hg)
)2o*
260
Zf/W
700
7?£>
610
610
*J/A
6$0
65-0
£0O '
\'3
fr
73-
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6$
~(
1305*
26*
260/21 a
720
7?o
700
£60
70O
6$G
&HO
S'SO
)}
f/
73-
#H
70
-/
IHOO
2 7*
260/300
7&6
7$0
700
tfo
630
t
-------
OPERATING DATA
Location 2
Date:
Data Taken By;
Test; i-
Test No.
Time
rf0rt(fi//U
Engine Speed (HPM) .FUKmritt)}
Current Exhaust Temp. (°F)
No. 1
No. 2
No. 3
No. 4
No. 5
No. 6
No. 7
No. 8
First Stage Inlet Press, (psig)
First Stage Inlet Temp. (°F)
Second Stage Discharge
Press, (psig)
Ambient Air Temperature
Dry Bulb (°F)
Wet Bulb (°F)
Relative Humidity (%)
Manifold Vacuum (in. Hg)
Barometric Pressure (in. Hg)
tf:35"
270
*6*/*tt>
660
72?
610
720
f{0
—
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7?e>
;?
11
73-
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67
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M.tf
tt'.ze
270
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630
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—
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12. 5~
6*
7$
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F7
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*6%i*
63$
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W
71?
6£0
—
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72?
II
ft.?
67
7$
6?
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- 6.$
21.W
W:/*
27f
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720
6*0
710
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67
71
6?
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62?
71?
6??
_
62?
730
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83-
67
7$
€1
V7
-^r
214*
1 7
-------
OPERATING DATA
Location 2
Date:
Data Taken By;
Test :
Test No
2 ~J
Time
VflVM//f£
Engine Speed (RPM) FLVcrvtTlffK
Current Exhaust Temp. (°F)
No. 1
No. 2
No. 3
No. 4
No. 5
No. 6
NO. 7
No. 8
First Stage Inlet Press, (psig)
First Stage inlet Temp. (°F)
Second Stage Discharge
Press, (psig)
Ambient Air Temperature
Dry Bulb (°F)
Wet Bulb (°F)
Relative Humidity (%)
Manifold Vacuum (in. Hg)
Barometric Pressure (in. Hg)
?:^
2. 70
*<*/it*
62?
62?
67?
71*
.-
675
t?f
700
/*r
?*
6-7
76
62
67
~6
21.15
to '.2?
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70?
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7fo
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WS*
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67
71
CB
ST
~7.f
21.1?
10'f?
2$~0
nr
6S0
rto
67?
*i
-------
OPERATING DATA
Location 2
Date:
Data Taken By;
Test;
Test No
Time
NOniV4L
Engine Speed (RPM) /* VefMTMS
Current Exhaust Temp. (°F)
No. 1
No. 2
No. 3
No. 4
No. 5
No. 6
No. 7
No. 8
First Stage Inlet Press, (psig)
First Stage Inlet Temp. (°F)
Second Stage Discharge
Press, (psig)
Ambient Air Temperature
Dry Bulb (°F)
Wet Bulb (°F)
Relative Humidity (%)
Manifold Vacuum (in. Hg)
Barometric Pressure (in. Hg)
M Iff
21?
6£5~
7/r
ft?
730
7*0
7/5~
^7r
^f^>
13.?
w
67
77
tr
?3
^6.£
J&.o
f3 :&
J7
*fr.
£
-------
OPERATING DATA
Location 2
Date:
Data Taken By;
Test No.:
Time
Engine Speed (RPM)
Current Exhaust Temp. (°F)
No. 1
No. 2
No. 3
No.' 4
No. 5
No. 6
No. 7
No. 8
First Stage Inlet Press, (psig)
First Stage Inlet Temp. (°F)
Second Stage Discharge
Press, (psig)
Ambient Air Temperature
Dry Bulb (°F)
Wet Bulb (°F)
Relative Humidity (%)
Manifold Vacuum (in. Hg)
Barometric Pressure (in. Hg)
?:'/r
J.S0
et?
700
67?
t?r
6(0
£3?
66*
f&0
I1~5~
Z?
££
72
6 3
€1
-v
et?
73 &
V'3
$$
£C
75~
^y
5"^
*>*.?
te.vg
20
-------
Gas Composition at Location 2
Methane 89.66 mol %
Ethane 3.30
Propane 3.05
. Iso-Butane 0.87
n-Butane 1.52
Pentane + 1.60
Heat Content 1225 Btu/ft
2 1
-------
Project«_
Date i
Locationt_
Itaiti
Ttsti
Puel«
VELOCITY TRAVERSE
*«st Descriptioat
Made Cross Section
- /
Personnel i
^9. 90
Baroaetric Press, (in. Bg)t
Absolute Static Press, in Stack (in. Bg)<.
Pitot Tuba Coefficianti J.Q
.*,»
TiM
Traverse Point
Port Depth
.5"
l.7f
}.r
t.f
te.tt
H. r
Velocity
Bead
(in. HjO)
AP
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5./
2.2
2.2
2.1
2.H
Gas Taap.
(T)
€40
Gas Teqp.
CW
*S
1120
-
Molecular
Nt.
««S
29.0
1
r
Velocity
(ft/sec)
vs
l?f>
HI
mi
jvv
ire
HI
.02
Cone.
(% Dry)
«ooa-i3
22
-------
FroJ«cti_
Oatei
lAcatiom_
Onitt
VELOCITY TRAVERSE
Test Inscription i__
Staci
Cross Section
Test«_
Fuelt
Personnel»
iSAS
Barometric Press, (in. Hg)i__
Absolute Static Press, in Stack (in. Halt 2-1,35" (P.)
Pitot Tubs Coefficient! /. O (c_>
85.48
11/2
Tiae
IZie>
Kaverse Point
Port Depth
./
/•f
l.f
?.3
//.^
/^.7
Velocity
Bead
(in. H,0)
&
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(*F)
62 f
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107*
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wt.
MS
2*1.0
\
*
Velocity
(ft/sec)
»S
IZf
IS?
112.
1*7
mi
1*0
02
Cone.
(» Dry)
6002-13
23
-------
Project!
VELOCITY TRAVERSE
Test Descriptiont
locationi_
Units
Stack Cross Section
Personnel i GR F
raei»
64 S
teroaatric Press, (in. Bg)»
Absolute Static Press, in Stack (in. Hg)i.
Pitot Tube Coefficient! I.O
(P,)
65.48
Vioe
/J/5
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
fiP
2..0
3.,^
3..1
3..1
Z.5
f.f
Gas Tecp.
CF)
(0O
ffO
Gas Te«p.
(*R)
TS
IO(O
ie>?a
\oio
1630
IW
1010
Molecular
wt.
MS
21.0
\|
*
1
Velocity
(ft/sec*
vs
I3t
HJ
us
IIS
iyo
I2H
02
Cone.
(% Dry)
' -
'
•
6002-13
24
-------
Projecti__
Patei
Location!,
Dniti
Hfoil-rt
VELOCITY TRAVERSE
*est Description!
•tact Cross Section
.2-.
Perconnelt
Fn.lt MAWKAL
21.
Barometric Press, (in. Bg)i_
Absolute Static Press, in Stack (in. Bg) i 2 f. f3 (P.)
Pitot Tube Coefficient! LO ft,)
85.48
.
1/2
TiM
/^?r
Traverse Point
Port Depth
Velocity
Bead
(in. H,0>
AP
2,0
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102*
1920
Molecular
Ht.
»s
w.o
\
f
Velocity
(ft/sec)
vs
>}*
l!f
13?
HI
1?g
117
.02
Cone.
(% Dry)
6002-13
25
-------
Projectt_
Date i
i tocationt_
. gniti.
'i-sti.
Fueli.
Barometric Press, (in. Bg)i__
Absolute Static Press, in Stack (in. Hg):_
Pitot lube Coeffieientt I.O
VELOCITY TRAVERSE
Teat Descriptiont
Stack Cross Section
Personnelt
&A S
.2 7.
Tine
Hoc
• .
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
AP
2.1
2*3
z.3
2.H
*.1
hg
Gas lop.
CP)
f7f
77?
Gas Tenp.
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120
\
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Kt.
MS
21.0
\
Velocity
(£t/BeO
vs
127
133
13$
I3f
I3£
lit
.Pa
Cone.
(% Dry)
6002-13
26
-------
Projecti_
.Date:
Location>_
Oniti
Testi
VELOCITY TRAVERSE
Test Description!
/ 21/76
Stack Cross Section
Personnelt
Barometric Press, (in. Bg)i
Absolute Static Press, in Stack (in. Bg)» 3-1.1H (P.)
Pitot Tube Coefficient! /> O
8S.4B
V.
Tine
IV2?
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
AP
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3. I
2. 1
a., 3.
3.. 3*
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5-73.
rtq
fff
5"*3
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loir
1033,
1031
10*6
103-$
10*0
Molecular
Nt.
MS
31.0
\
f
Velocity
(ft/seci
VS
12?
IS?
137
139
1*1
131
Cone.
(% Dry)
«002-13
27
-------
«rojecti_
tatai
Location i_
Onit»
*BStt
VELOCITY TRAVERSE
Vest Description!
Stack Cross Section
Personnel i 6R F
tric Press, (in. Bg)t
Absolute Static Press, lit Stack (in. Ha)i 3-f.f^. (P,)
Pitot Tube Coefficient! L0
1/2
TiM
oisr
t
t
Traversa Point
Port D*pth
Velocity
Bead
(in. H,0)
&P
1.7
2.2,
£.3
2.5
3.3
1.?
Gai Taop.
(•F)
610
\
//
f
r*
Gas Teap.
CR)
*s
1070
\
/
tore
Molecular
Nt.
NS
W.e
\
-'•
*
Velocity
(ft/see)
»S
121
HI
/VY
/•y/
/VV
12"?
02
Cone.
(t Dry)
>
6002-13
28
-------
Datai
VELOCITY TRAVERSE
*e*t Descriptions
location*
Stack Cross Section
Ohiti
fMtt
FB«I. NATURAL GAS
Saronetric Press, (in. Bg)s
Absolute Static Press, in Stack (in. Stall Af.
Pitot Tube Coefficient! /«^
Time
101 'f
Traverse Point
Port Depth
r
-
Velocity
Bead
(in. H,0)
tf
z.i
*.S
2.f
*.<
2.?
2-1
Gas Top.
CF>
/^
/fi
(21
€16
60%
fee
Gas Teap.
(•R)
*S
11*0
1012
low
107*
wet
10(0
•
Molecular
Wt.
MS
21.*
'
t
Velocity
(ft/see)
»s
IH1
tr\
151
/5*/
tye
l?7
<>2
Cone.
(% Dry)
6002-13
29
-------
Pro}
VELOCITY TRAVERSE
Test Description!
locntiont_
ttoiti _
Testi _
Stack OCOM Section
Personneli
Fuel. NArt/XAL 64 S
etric Press, (in. Hg)»_
Static Press, la Stick (in. Bg) i
Pitot Tube Coefficient* A ^
5-75-
Gas Tenp.
'CW
*S
\ff0
I*f7
t*1t
I»1I
loll
1*3 r
•
-
Molecular
Wt.
»«S
21. e
\
•*
Velocity
(ft/sec)
»S
\2f
lit
131
131
133-
nf
02
Cone.
(* Dry)
6002-13
«/!*
30
-------
froj ect s
Date. Ht22/7t
loeationt 3-
Onits
Vests 2- -*/
VELOCITY TRAVERSE
Test Descriptions
Stack Cross Section
Personneli
Barometric Press, (in. Hg)s
Absolute Static Press, in Stack (in. Bg)»
Pitot Tube Coefficients If 0
(P.)
(V
- 85.48
1/2
TIM
MI?
^
" *
t
Traverse Point
Port Depth
Velocity
Bead
(in. B,0)
AP
-2.V
*.6
2.£
2,1
*•£
2.2.
Gas tutf.
(*F)
rr*
fff>
Gas Teap.
<'R)
*S '
l»ie>
\
/
Molecular
Wt.
ns
21.0
\
r
velocity
(ft/seci
V8
112-*
iit.£
H1.<
151.2
/If-*
136.7
02
Cone.
(» Dry)
.1*
4002-13
31
-------
Prej*cti_
Datai
Locatiom_
Oniti
Iff
VELOCITY TRAVERSE
fast Descriptioni
Stack CTOM Section
Petaonnalt
malt
(ia. Bg)i
BaroiMtric
Absolut* Static Fran, in Stack (in. HB>I 3 3*
Pitot Tub* Co*f ficioatt _ f.0
(».)
ffi-}
85.48
*r FJC
TiM
//yf
Travarc* Point
Pert Depth
Velocity
Bead
(in. H,0)
tf
2.0
2.Z
2.3
2.3
$.1
ht
Cas Taap.
CFJ
f*.f
f*£*
Gat Temp.
C*R)
*s "
ffjr
11 f.
it?
Hf
Iff
frr
-
Molecular
Nt.
MS
^^, *
\
f
Velocity
(ft/*ae)
»S
we. ?
131.1
lit.*
191,0
111.1
122. 1
02
Cone.
(%»ry)
•002-11
32
-------
Prelect:
Date: 'V /2 3 /7f
VELOCITY TRAVERSE
Test Descriptions
Location: 2-
Dnit:
Stack Cross Section
*»st«
.2-5-
Personnelt GK F
Fuel. NATURAL. &AS
Baronetric Press, (in. Hg):
Absolute Static Press, in Stack (in. Hg);
Pitot Tube Coefficient: I.0
(P.)
- 85.48
1/2
Tine
01$0
t
.
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
to
/.*7
2.1
2.1
2.Z
9.0
1.1
Gas Tenp.
CF)
61*
fsa.
fit
eie
£0*
£00
,
Gas Tenp.
(*R)
Ts
11*0
1012.
l*W
I07f
I0(Z
1*60
Molecular
Kt.
«S
21.0
\
Velocity
(ft/seO
VS
133.
/5f
//^
/y/
//y
130
02
Cone.
(% Dry)
6002-13
33
-------
»*ojeets_
Dates
Locations_
Units
VELOCITY TRAVERSE
Test Descriptioni
Stack Cross Section
2. -
Personneli GR F
&AS
Test.
Fuels
Barometric Press, (in. Hg)i
Absolute Static Press, in Stack (in. Hg)s
Pitot Tube Coefficients /. O
(P.)
Vfi - 85.48
Tine
Ifff »
.
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
AP
l.f
2..0
2*1
*.t
2.1
l*f
Gas Te>9.
CF)
(ee>
(oS"
£(*
61*
6*0
flf
Gas Teiqp.
CR)
TS
I0£*
IMS'.
r*7*
107?
1010
Iffff
•
Molecular
Ht.
»S
M.o
\
/
Velocity
(ft/sec)
vs
1(1
ni
1)7
i?t
HZ
12*
°2
Cone.
(% Dry)
6002-13
34
-------
Data*
loeationi_
Otolti
VELOCITY TRAVERSE
Test Description!
Stack Cross Section
-5"
Personnel t
t*«tl__
Fuelt NATURAL £/f S
Barometric Press, (in. Bg)i
Absolute Static Press, in Stack (in. Eg): 2-1.12.
Pitot Tubs Coefficiect: /. O
V_ " 85.48
Tine
l»?o
Traverse Point
Port Depth
Velocity
Bead
(in. H,0)
AP
1.1
-2.5"
Z.7
z.f
z.(
2.3.
Gas Teqp.
(T)
6S-t>
£5-0
Gas Tenj>.
rw
Ts
III*
III 0
It/f
me
1110
1110
,
Molecular
Wt.
MS
21,0
\
*
Velocity
(ft/see)
VS
IS*
15 3
W
Itt
l?6
113
°2
Cone.
(% Dry)
6002-1S
35
-------
ROTARY KILN DESIGN DATA
Location No.
Unit No.
Unit Description
AT
Installation Date
Process Capacity
Burner Description
Test Fuel
£4$ /tf
Fuel Temp, at Burner
ISO "
Comments:
36
-------
•test Ho. 3" /
Unit No.
Date
MOBILE LABORATORY DATA
"f~ 76 Location _ 3_
Test No._
Engr.
Fuel tM£
Capacity
Onit Type
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/8C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
3-)
//^^
3. 1
—
—
—
1010
17
£0
U
II
Wit
£*
* *r
60
J-tJ
2.0
V?f
1f0
2?
I0?0
1?
ff
20
1
121
-------
Test No. P ""•2-
Unit No.
Unit Type R&TA
MOBILE LABORATORY DATA Test No. _
<~- £ — ~7£ %
Date y <> f " Location "> Engr.
Fuel £0K£f£A S Capacity
K Y K ' t' M Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/*C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
?-2- U
I3&O
\.35~
Z3£
no
15-
100
721
775
li
25*0
18,1
tj$~
-2J~
17
H3
£5"
5-7
*? & & £"*
««£ 0 t *7
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
Date $~ 7~ 'o Location
Test
Engr.
Fuel
Capacity
Unit Type ROT/MY
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO5 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide. (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
3-3 A -V
/we
l.5~
/f#
$60
20
*l}0
£22
711
2#
eft
I$,S
?0
2-?
If
2-tf
3~3$-V
12 /&
1.2.
17?
156
2f
\m
/%
Sf
//
22-
£7 ff f
Jy & £
Iff
22
1&1
.0
72-
• '
3-3C-U
ini?
I.6F
-------
Test No. 3~~?
Unit No.
Unit
Date
MOBILE LABORATORY DATA
Location 3
Test No._
Engr.
Capacity
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
1-3&-V
l£~$ 0
/ t
3$&
fy&
20
t£>f0
rjT
///
/y.z
/f
f/z
I7-*
ye
-------
KVB
LOCATION NO. 3
CONTROL BOOM DATA SHEET
DATE
jT-jT^r
TEST NO. 3 — / ; TIME / 7 ' /^
Meter
.Parameter Units Legend Meter No. Reading
1. Coke Rate tons/hr "Coal Mill H3-K2-BS1 5V ^
Feed Rate"
2. Cyclone Tempering
Air Temp. °F
3. Coal Mill Outlet
Temp.
4. Coal Mill Inlet
Temp.
5. Coal Mill Motor Amp
6. Coal Mill Inlet
Pressure
1. Coal Mill Outlet
Pressure
8. Coal Mill Fan «
Inlet Damper °
9. Fan Amps 15 &
10. Fan Damper Position H5-2-D01-POSR "33
11. Kiln Exit O % H3-2O R /• $~
£ £ _.-. i_
12. Klin Feeder Speed RPM 20
13. Kiln Speed RPH ? 3~
14. Max. Kiln Shell
Temp. "F
15. Cooler Undergrate
Air Temp
16. Cooler Undergrate ////.«
Air Pressure /^ & Jf %•
17. Material Temp H3-2-TSM 2-5"5 0
18. Gas Fuel Rate SCFH x 10.5 . . 70
(70°F)
t.
19. Clinker Rate tons/hr "Clinker H2-2-BSI-INT
Belt Scale
Int"
20. Feed Rate tons/hr (From Operator)
4 1
5/4/76 - 6002
-------
IVVD
DATE
TEST NO.
LOCATION NO. 3
CONTROL ROOM DATA SHEET
TIME
/f
. Parameter Units
1. Coke Rate
2. Cyclone Tempering
Air Temp.
3. Coal Mill Outlet
Temp.
4. Coal Mill Inlet
Temp.
5. Coal Mill Motor Amp
6. Coal Mill Inlet
Pressure
7. Coal Mill Outlet
Pressure
8. Coal Mill Fan
Inlet Damper
9. Fan Amps
10. Fan Damper Position
11. Kiln Exit O2
12. Klin Feeder Speed
13. Kiln Speed
14. Max. Kiln Shell
Temp.
15. Cooler Undergrate
Air Temp
16. Cooler Undergrate
Air Pressure
17. Material Temp
18. Gas Fuel Rate
Meter
Legend
Meter No.
Reading
tons/hr "Coal Mill H3-K2-BS1
Feed Rate"
32-*
H5-2-D01-POSR
33
RPM
RPH
°F
I. 7 +1.
It
H3-2-TSM
SCFH
<70°F)
19. Clinker Rate
20. Feed Rate
tons/hr "Clinker H2-2-BSI-INT
Belt Scale
Int"
tons/hr (From Operator)
4?
vy
5/4/76 - 6002
-------
KVB
LOCATION NO. 3
CONTROL ROOM DATA SHEET
DATE
TEST NO.
Parameter
1. Coke Rate
3 "~ 2- 5
Units
tons/hr
TIME
Meter
Legend
"Coal Mill
Feed Rate"
If '.If
Meter No.
H3-K2-BS1
Reading
2. Cyclone Tempering
Mr Temp. °F
3. Coal Mill Outlet
Temp.
4. Coal Mill Inlet
Temp.
5. Coal Mill Motor Amp
6. Coal Mill Inlet
Pressure
7. Coal Mill Outlet
Pressure
8. Coal Mill Fan
Inlet Damper
9. Fan Amps
10. Fan Damper Position
11. Kiln Exit ©2
12. Klin Feeder Speed
13. Kiln Speed
14. Max. Kiln Shell
Temp.
15. Cooler Undergrate
Air Temp
16. Cooler Undergrate
Mr Pressure
17. Material Temp
18. Gas Fuel Rate
19. Clinker Rate
20. Feed Rate
1.*)
%
RPM
RPH
°F
H5-2-D01-POSR
H3-202R
25
SCFH
(70°F)
tons/hr
"Clinker
Belt Scale
Int"
H3-2-TSM
H2-2-BSI-INT
7)
tons/hr .(From Operator)
5/4/76 - 6002
-------
LOCATION NO. 3
CONTROL BOON DATA SHEET
DATE 7 " /- '£>
TEST NO. ^-"3 TIME /2 5~5~
Meter
.Parameter Dnits Legend Meter No.
1. Cotfe Rate tons/hr "Coal Mill H3-K2-BS1
Reading
f.0
Feed Rate*
2. Cyclone Tempering
Air Temp. »F £2 &
3. Coal Mill Outlet fff
Temp.
4. Coal Mill Inlet »/C
Temp.
5. Coal Mill Motor Anp
6. Coal Mill Inlet
Pressure
7. Coal Mill Outlet
Pressure
8. Coal Mill Fan
Inlet Damper fitTfttl
/£c>
3CO
£.£
1.1
$.£
JT1
9. Fan Amps 1 3&
10. Fan Damper Position H5-2-D01-POSR
11. Kiln Exit O, % H3-2O.R
12. Klin Feeder Speed RPM
13. Kiln Speed RPH
14. Max. Kiln Shell
Temp. *F
15. Cooler Ohdergrate ^
Air Temp r
16. Cooler Dndergrate H u *»
Air Pressure H^ &
17. Material Temp H3-2-TSM
18. Oas Fuel Rate SCFH
fi
0,Z
Z° KfM
14
5TO
2- 00
7,2-
2 £90
70 xte>9 $*
(70°F)
19. Clinker Rate tons/hr "Clinker .. H2-2-BSI-IHT f2-
20. Feed Rate
* i .
Belt Scale
Int"
tons/far (From Operator)
rent. . *f
S/4/76 - 6002
44
-------
LOCATION NO. 3
CONTROL BOOH DATA SHEET
DATE
7
TEST NO.
TIME
/ *f 0 3
.Paramter
1. Co&e Bate
2.
3.
4.
Onits
tons/far
"Coal Mill
Feed Bate"
Meter Ho.
H3-K2-BS1
Cyclone Tempering
Air Temp.
Coal Mill Outlet
Temp.
Coal Mill Inlet
Temp.
5. Coal Mill Motor Amp
6. Coal Mill Inlet
Pressure
7. Coal Mill Outlet
Pressure
8. Coal Mill Fan
Inlet Damper
9. Fan Amps
10. Fan Damper Position
11. Kiln Exit O2
12. Klin Feeder Speed
13. Kiln Speed
14. Max. Kiln Shell
Temp.
15. Cooler Ondergrate
Air Temp
16. Cooler Ondergrate
Air Pressure
17. Material Temp
18. 6«a Fuel Bate
($0
%
BPM
BPB
H5-2-D01-POSR
H3-2O,,R
19. Clinker Bate
20. Feed Bat*
21. /4€ft0V*f Ifttfr
SCFB
(70«F)
tons/hr
"Clinker
Belt Scale
tot"
H3-2-TSM
H2-2-BSI-INT
tons/hr (Prom Operator)
rr* 'r
5/4/76 - 6002
-------
LOCATION 3
COKE SAMPLE
Ultimate Analysis:
Carbon, 7. 82.68
Hydrogen, % 3.67
Nitrogen, % 2.38
Sulfur, 7o 1.94
Ash, 7. 6.19
Moisture, % 2.01
Oxygen, 7o 1.13
(by difference)
Heat of Combustion:
Grass, BTU/lb 13,980
Net, BTU/lb 13,640
46
-------
GASEOUS FUEL ANALYSIS
Test No ?*>.. £
Unit No.
Date
Fuel i
Location Ticn-A.e^ GtMefrC
Test No
iL»l Engr
lo.fcg. iQls 2.03 H-2*
"V
CF fuel
SCF air/100 Btu 6 70eF,
29.92 in. Hg.
CF Prod _ 1()6 / Btu(HHV)
1.069*10*" Wet SCF Prod/106 Btu
Bt«
*100
331.5x10
(DSCF/106 Btu)
lb/10 Btu - (ppm
ag/J - (ppm e 3% 02>A'
3* 02)A
C«ta Sheet 6002-6 (Rev. 1)
47
-------
HP-67 KEYED CALCUIATION SHEET*
PARTICULATE EMISSION CALCULATIONS
Test No. 3-Z Date g-fe-"7fe Location "fin C^qg^rr J^itjd Ensr.
ttoit Mo. VJ \^-2. Fuel Co>gj&y4*£> Sampling Train and Method
Pitot Factor, Fs •83 Barometric Pressure, P' . 2A-9S in. Hg
b*! (STO Oj ^
Tot. Liquid Collected, V. Je>.S ml Total Particulate, M a4\7-6 » gm
*~ISTO 1) » (STO12)
Velocity Head, AP o-fe iva Stack Temp., »• VOOS •», stack foea, As &4 ft
15TU JJ • (STO 4) ISTO 51
Sample Volume, Vm 5.B& ft3 stack Press,, Psg - <=> iwg Excess O_, XO.% F&-fcS i
(STO 6) (STO 7) 2 2 (STO fl)
Orifice Press. Diff., H -feZ. iwa Bfceeli Pas Cp. Cja»i*yy Gs 1. 6 4- n.d.
Sample Time, 6 VO min Nozzle Dia., Dn YA in. Meter Temp., T
tsio BJ (STO C) m ISTO DJ
select Fe
SC Feet/104 Btu
Oil (A)
92.2
Gas (B)
87.4
Coal (c^
98.2
Other: €-«y^g 4S*>*
U4.X (D)
Press (E) if meter is not temperature compensated.
1. Sample Gas Volume Vm - 0.0334 Vm(P. + H/13.6) S-4-O SCF
8*0 oar .
2. Hater Vapor Vw . . - 0.0474 V, O • 5\
sta ic ———__
3. Moisture Content Bwo - Bq. i/(Eq. 1 + Eq. 2) *Q.S4-
4. Concentration a. C » 0.0154 Mn/Vm ^.
sta
b. C - 2.205 x 10~6 Mn/Vm . .
sta
c. C » Bq. 4b x 16.018 x 103
5. Abs. Stack Press. Ps - Pbar x 13.6 + Psg
~'~x
6. Stack Gas Speed Vs - 174 Fs /5pTs J,
7. Stack Gas Flow a. Qsw - Eq. 6 x As x ^ x f^_
Kate • 70°F w *07
b. Qsd • Bq. 7a x (1. - Bq. 3)
8. Material Flow Ms - Eq. 7b x Eq. 4b x 60
9. X>a factor XOjf * 2090/(20.9 - X>2%)
10. Emission a. E » Eq. 4b x Fe x Eq. 9
b. B - Bq. 4c x Fa x Bq. 9 x 1000
11. % Isokinetic x m i4077 *
6 x Vs * Ps x On2
•If calculating by handt
1) Convert T« and TB to *R
2) Multiply EQ 1 by 530/ta(*R) if meter not temperature compensated.
3> ». - 2.684 x ID'5 « F. O.t. g^tt 6002-4
Kevised 2/15/78
-------
PARTXCULATE CALCULATION SHEET
«••* *°
Box Mo.
lest Description
Pat* S- Ca-Tfe Location
Sample Probe Position,
Test Crew
Dry Gag Meter Vol. (
Fine* loSS-su-
Initial lOft.at
MC*1 >.fife
Beaker No. '
Bate
toished
Tare 1 lOo.cMd
Kt. 2 (00.0*4*,
3 jff> O%4 fi
4
5
6
,,, ...Aya JSfiifiSQ™
Bottle No. Z.
Xspinger
Content (Hater)
Rinse (ml) 49*2.
Date Neighed
or 250 Bake
Final 1 ltt>.cA*£
Wt. 250 2 (00.6^92.
3 )olp.*4A\
4
S
6
Avg \bb.O^&
Residue wt
Final 250-Tare '
Date Weighed
or 650 Bake
Final 1
Wt. £50 2
r*
4 -
'5
-6
Avq
Residue Wt O.OO^fc
Final 650-Tare
ft')
4
2.
let <»2.£tX
ib\ .Ca4-\
\Ol .b&!3
'OV. 624?.
5
Probe
(Acetone)
A«2.
toe. i\t*>
Irsj - *H,S
Irs9 . * It U
Io2..i\\l
0.^7!?
Final tc
Initial le
A Vol
3
lb( ^•lOl
M>1 XlOt
tt*t d IO4-
ltsl.4.(BK
4-
Probe
(Hater)
4-ST
tel.4S*"|
1C, I .4.64.7
tol . 4-S4S
»0\.4s4.-y
O«442>
Impinqer
1 2
1 4 lf>0
»Q 100
% b
4
^^•iS-O"?
«iO . 2565
%%'Z.Sfpl
y* . z.s»f
1
Cyclone
(Acetone)
"3JL2L
•t^.ZtL.9
tt^.'Z«S7
6,o> *e<^6i
%^.2«S^
0.03S4-
Hater Vc
3
o
—
o
5
SflSiSA-
%«.A?3%
4 2 SZiC"
M ^a^
Flask
(Dry)
5/7 /7b
loo.Tat?
too.jia,
too ~T&5^
io6-l3fo
l.e\Z4
>1 %44*
l.L«44A
total
• i&
Blank
No.
Z.
&.~IS£&
6.-7«^O
& -f^Oj |
O.TttdO-
O.T^f>&j
0.-?W
O.79&O
Ci."7fi»3O
Conanentst
Data Sheet 6002-3
49
-------
Test No.
CASCADE IMPACTOR DATA SHEET
TEST RUN NO. /""-?
IMPACTOR NO. /
SAMPLE POINT LOCATION
SUBSTRATE COATING
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
NOZZLE DIA. ^2.
"LOCATION 7 DATE f-/'/* ' rr7& <
CYCLONE NO. / OPERATOR
P0*>AJ£ r#£/(rt ffif tfvt, 77 &1 0/(ji
fiJ0AJ£- FUEL £#t(£. &d5 «»
H0RI&- • FLOW THRU IMPACTOR
~ & inH^O, VELOCITY /"^"" "^^/St,
mm IMPACTOR PRESSURE DROP /?* ...
3T IiOAP- £0 ykt* klb/hr
^^7 7 CFM
5*^^ *
ND TIME /3 ' y^
GAS METER END x7- ^ I CF
GAS METER START ^ CF
GAS VOLUME "?, 0 I CF
START TIME
DURATION
FLOW RATE
CFM
M//FT
AMBIENT TEMPERATURE
ei
77
PRESSURE
Hg. HUMIDITY
FLUE GAS MOLECULAR WT.
, TEMP.
*F, DENSITY
g/cc,VISCOSITY
POISE
Fetir-t- sample, g
Unused Foil, g
Sample, g
Correction
for Blank', g
Final Sample, g
/
Stage Number
1
Xxxp * r
?^V7/
0.1200
2
27:T
-------
TABLE 1.
Symbol
Value
Pressure drop across impactor
during test "Hg"
Static pressure at inlet to
impactor, atm.
Density of aerosol particle, grams/cc
Density of gas at inlet sampling
conditions, grams/cc
Molecular weight of sample gas
Molecular weight of calibration gas
Temperature of gas at sampling
conditions, °K
Temperature of gas at calibration
conditions, °K
Static pressure under calibration
conditions, atm.
Gas viscosity at sampling conditions,
poises
Stage jet diameter, cm
Sample quantity collected on each cup
Dimension conversion constant
MW
U
D
R3
R4
R5
R6
R7
f. 1
. /
1.0
.0751
,010*1
.0013
1
51
-------
TABLE 2.
Effective pressure drop, "Hg"
Inlet flow to impactor, cc/second
Pressure out of stages, atm.
Density of gas out of the various
stages, grams/cc
Characteristic diameter, microns
Criteria for validity of equation 18
Mean free path
Average molecular velocity
Symbol
Value
*°
""
PC6
Dpc6xl(f4
L
V
.000 ft
l.£71$f
-------
TABLE 2 (Continued)
Symbol Value
% on a cup of the total sample collected
Stage 2 Y
r3
'2
3 Y,
4
5 Yq 3. ? I 2,t>0
'5
r
Filter Y
e Y6 /•>*
7
Total 100.00*
*Any discrepancy due to rounding off should be buried
in the largest Y cumulative % smaller than D__
53
-------
K V B. INC.
STACK DATA
Test No._
Engr. "
Date
Load
Location
Unit No.
Fuel
Sample Box No.
Kf/hr or MBtu/hr
/ Meter Box No.
Filter No.
Probe No. 3 Probe Length
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather GL.OV0Y
Stack Gas Pressure> Ps - f iwg
Abs. Stack Press., AP=P +407= iwga
Stack Gas Sp. Gravity, 6s_ n.d.
Stack Area, As g*f ft2
Remarks
Final Meter;
Initial Meter; 101
.Time
WOO
1500
Ifef
\fio
Total
Avg.
Vm
Meter
Volume
Beading
(CF)
IW6M
\0\1.*6
103.}
iW.W
Vacuum.
Gage
Reading
(iwg)
3..O
H.5-
H.S~
H.f
ftp
Pitot
Tube
Pressuri
(iwg)
./
.f
.*
.*
0,8
H
Or f ice
Pressure
s Diff
<°F)
./z
.42
.fz
.(3-
'
Stack
Temp.
<°F)
fif
?if
flf
rvr
°F
^V^F
+ 460
Impinger
Temperature
Out
(dp)
130
7f
60
£$-
In
(°F)
/I?
If0
110
IfO
r
Filter
Box
Temp.
(°F)
^5"^
55-<5?
210
-2-25"
Meter
Temp.
(°P)
^-2
105"
I05~
i*r
"'
Ts- 100? °R
60-13
11/20/75
54
-------
»rojectt_
Datet
Ipcationt_
VELOCITY TRAVERSE
Test Description i
Stack Cross Section
f»«tt
Pltelt
Personnel «_
K It. A/ flSTlf T
Baronetric Press, (in. Bg)t
Absolute Static Press, in Stack (in. 1)9)1
Pitot Tubs Coefficienti 1.0
1/2
Tine
013*
Traverse Point
Port Depth
/
\
I
2.
\
t
/^'
10'
/V*
7'("
Ct"
r'Y*
>*'
iff1
f'i"
7'f"
f'v"
;'i"
Velocity
Head
(in. H,0)
AP
,3
. J-
./f
'If
.;-*
.07
.21
.3-
.It
.19
./*
.03
Gas Teaj>.
CD
llgt>
If/0
ll?t>
1*0
lit*
t/V*
nit
W
Gas Tenp.
CR)
»S
//^ *"
/^y^ r
/^y^
If00
irio
13 ft
we*
IffO*
161*
1600
we
ISge
Molecular
Wt.
MS
21.0
\
Velocity
(ft/sec^
vs
£1.3
rt.5-
JTI.3-
11.3-
•10.0
2f.T
65,2
&.*-
Vf.f
11,1
*{0,0
/f,6
02
Cone.
(% Dry)
At* mil l
.?;*/* F'l' f'ihts Tt.\
55
-------
f*ojeeti_
Datai
Loe*tiont_
flnlti
VELOCITY TRAVERSE
Test Description«__
Stack Cross Section
Personneli
ruelt __
Baronetric Press, (in. Hg)i
Absolute Static Press, in stack (in. 89) i.
Pltot Tube Coefficlenti /> 0
(P.)
(Cp)
4»» f£,0
\1* fH.3
Tine
Traverse Point
Port eeptir
3
>
f
«i
,
MNP
I
J
V
5"
4
7
1
\
2.
J
«f
s-
e
7
9
Velocity
Bead
(in. B20)
AP
'HI
./r
.1
,9?
.tf
.1
.1(
.27
.15
.$"
,tr
.17
.if
t.i
1.1
Gas Trap.
CP) ,
ri*
fH 0
S~5~0
5-5-5-
5- 60
f7*
$-75-
$*H0
5T0
rtt
ft?
^ £ 0
^>7 £P
' rif
f-ge
Gas Tenp.
TS
y 0 &&
/ &&&
1010
101?
I02O
1610
1*3?
1000
1010
1000
IPOS'
1020
t03t>
ItSf
I'Ho
Molecular
Wt.
»s
21.0
\
^
Velocity
(ft/sec^
vs
•41.7
61.1
61. 3-
7^ 7
7^9
?3-3
7f.1
31.(
£0.16
?3. *
tl.f
7/. 7
7^".?
f).2-
f)*i
02
Cone.
(% Dry)
6002-13
56
-------
f*oj«ctt__
*»*•'—
locations,
flnltt
VELOCITY TRAVERSE
Test Descriptions
Stack1 Cress Section
Personnel.,
Barometric Press, (in. Hg)i
Absolute Static Press, in Stack (in. Hg)i
Pitot Tube Coefficient. /. O
(P.)
Vg - 85.48 C,
An €7A
Ate (13
\
Tine
..'
••.
Traverse Point
Port Bepth-
2.
>
/
/
\
/
WW
3
fc/
>•
(
7
1
3
f
r
^
7
g
Velocity
bad
(in. B30)
AP
.6-r
,/7
.75"
.5
.3
I.I
.73
.1
.7*
.77
.13
,tf
Gas Venp.
(*P)
5"V^
/•v^
rvr
ff*
sr*
f70
ft*
FZ0
ns~
$-2$
?W
rye
Gas Tenp.
CR)
*S
)09*
\0»0
I$-
I0ft>
1010
JQ2.0
17*
1V0
1
(f.7
«.3
fl.O
70.3-
02
Cone.
(% Dry)
600J-13
57
-------
PETROLEUM REFINERY HEATER DESIGN DATA
Location No.
Unit No.
Unit Description
16 A \/£ trie ALLY
Installation Date
Heater Rating
ft.
Burner Description
/GAS
//./
Test Fuel Combinations
G/tS
Fuel Temp, at Burner (°F)
Primary Air Temp. (°F)
Comments:
58
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
7*f
7f
&
#7
'6
f
67
i-i
-r/^^-
r/$0
•
3-1
*1
61
(?
%2-
fr
12-
/
3^
?$-
72-
7*
&
ft
q
#
6 ~7
£ 1
-71
•
1-*
f-fetffo
120*
2*f
71 7f~
70 71
\ /
& &<1
/0,2-
13 X1/
/
3%
•
*Correction to 3% 02 should not be performed
the value is measured on a --*'*-'*—•
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date 5"X? y/7f Location ±__
Fuel &tf 5 Capacity
Test No..
Engr.
Typo
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
1-2-
5~/2
\
11
tf
Iff
H-
2-
r/j-il/s
/30
-------
MOBILE LABORATORY DATA
Test Ko. 7 ""
Unit Ko.
Location
Test No._
Engr.
Fuel
Capacity_
Unit Type flAf//M
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°P/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
f-3
rMfa
I&P0
?.
7*
*1
/
'//
2
?3
73-
1
t£
10.0
10
1
ft
/e>
»*' • '
,>
*Correction to 3% 02 should hot be performed if
the value is measured on a wet basis.
61
Data Sheet 6002-2
-------
Test No. y I
Unit No.
Unit Type
Date
MOBILE LABORATORY DATA
Capacity
Burner Type
Test No._
Engr.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO5 (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
it
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atitos. Temp. (°F/°C)
19. Dew Point Temp. (°P/°C)
20. Atroos. Pressure (in. Hg)
21. Relative Humidity (%)
22. '"
23.
24.
25.
26.
27.
28.
29.
30.
y-
y
rfer/K
0
///
!$£
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1*2-
/y/
/yy
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172-
l/,4
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2-
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//
y-
i
f/zf/r/
/03*
3- £
*??
l?7
I
163
12
/0
2-
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PM
/i?
/
I7/
,0
W
y-y
&/2f/K
/J00
,
/>7T
l?7
l?£
1
!7S
//-
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/
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H3
/iz
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7
/#
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•
y-f
£/?**/&
//20
3*3
J2* H3
jff ;^2
/ /
IT? IfS"
//,2_
'2- /3
/
fy
Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
62
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Location y
Test No._
Engr.
Fuel
Capacity_
Type
ft-jStf£A/ft£4T£A
Burner Type
//(/ '/£
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
y-y
f-2S-?t
/20e>
tf.
I3£
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I
U2
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0
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us
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1
177
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133 W
1 /
J53 /£2
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12- /?
0
13
*Correction to 3% O, should not be performed if
the value is measured on a wet basis.
63
Data Sheet 6002-2
-------
Test No. 7 •"-5"'
Unit No.
Date
Fuel
Onit Type fi-AStfft
MOBILE LABORATORY DATA
Location
Test No.,
Engr.
Capacity
Burner
MA/A?
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oz (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
#'
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) • uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
IB. Atmos. Temp. (*F/-C)
19. Dew Point Temp. (eF/*C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
'y-r
?-2f~7£
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/
1*1
.-2.
(2.
7£*F
*1V
21.11
rz%
•
•Correction to 3* 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No._
Unit No.
' 7
Date
MOBILE LABORATORY DATA
Location /
Test No.,
Engr.
Fuel
Capacity_
Unit Type
Burner Type ?6>///*J
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% ©2 (ppm)*
10. NO (hot) read/3% O2_(pj?m)*
11. NOj (hot) read/3% 65 (ppm)*
12. NO (cold) read/3% 03 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. ("F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
y-/
$-/*
S/K
/&£,£
e>AS.
g
,£>.$.
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1
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$~/J£/7f
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F,
ff
73
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17
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0.0.S.
f
17
1*
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1
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v *^. H
^ ^
» X
^ ^ w
•5 ^
va "*
v ^J "^
^
; £
*Correction to 3% 0- should not be performed
the value is measured on a wet basis.
65
if
Data Sheet 6002-2
-------
Test No._
Unit No.
Unit Type
Date
Fuel
MOBILE LABORATORY DATA
Location
Test No._
Engr.
Capacity_
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)* *fT
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 03 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%) •*« V
23. "^"V^
24. xs
25.
26.
27.
28.
29.
30.
*i-f
r/j. 7/ft
0 ^
Vj ^A
£ ^
^
.^ V
"s* ^
M\ ^
•x Hi
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^ «*
^ X
f-l
f/27/7S
/000
i
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63
I
f2-
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f'6
ft
ff
(
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1,
%
2.
/$
T
?3
72-
I
37
3*
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7j
70
I
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i'
^
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17
ff
7f
77
1
1 f
s
/
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No._
Engr.
Fuel Jiff. £* 5 Capacity
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Stroke Spot (Bacharach)
18. Atmos. Temp. (°F/"C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
y-
*#;
/*
>/ss
/300
7~
77
?f
1
1#
?<
16
2-
3-1
i
47
ft
/
/*£
^
'//
u
VI
^
IS.
Ml
X*
V xj"
rj ^
v^! W
^**'fc
**» s»
' i->i
r/2?/7t
1110
$-t
7f
7f
I
1$
W.
10
3-
23
, /
#1
ft
/
J05
2.
//
*¥
^
?
vrs
\
^ ^\
#0
0
J
^
V\
•
*Correction to 3% O- should not be performed if
the value is measured on a wet basis.
67
Data Sheet 6002-2
-------
Test No.
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No._
Engr.
Fuel
Capacity
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
4 . Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. .Oxygen (%)
9. NOx (hot) read/ 3"% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide ipptn) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atitos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
*/-/*
*~'2f'%
0*?0C>
5*-
1*3-
/'f
1
&0
f*.
to
0
11
3
1/7
II f
/
M
2
//
V*
j,
_.
--•
.
.
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
68
Data Sheet 6002-2
-------
KVB
Location 4
Control Room Data Sheet
Date
'**
Test No.
H" I
Parameter
Time
Fuel gas flow X , ?I(O 2
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34 X $(70
SR Residue
X Ifff 0
?
*
SR Residue to Htr. 33 - Pass A
»» - Pass B
X^l* - Pass C
ii - Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-Bast .
Hand indicating cdntroller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
II Q II
.« D ii
" A Out
" B "
,, c
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
A#*R-*82 IZf
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152.
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
—4
«»(%
-6
-7
-8
-9
-10
Units
HMSCFD
psig
%
*'/t
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
°F
" H2°
% Open
No Units
No Units
%
°F
•P
°F .
°F
8F
"F
«F
"F
«F
•F
«p
Read! no
/^ ; 00
6,3-^
5~ 1
£*-
r~3
. —
/^
7,4
7.3
7-1
7-1
75*
7^0
0,0 ff
*0
0*r
00JT
r,3
—
740
fit
*36
02*
V*f"
q*?0
—
10(0
-+*6&~ 11 5~
t*f~
6002 TP 5/20/76
69
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
ii B ii ii
II Q II II
II p II ..
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
" " " SW
Temp, of radiant section - NW
ii ll n n gw
Tempj pass C rad. sec. skin
II II n II II II
ii ii Q n n n
Temp. conv. - rad. crossover Pass A
II II II II II n
Temp, combined outlet A fi B
Temp. conv. - Rad. crossover Pass C
n n n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
Units
op
op
op
OF
•°F
OF
OF
oF
op
OF
OF
OF
op
OF
op
op
op
OF
OF
oF
op
OF
op
OF
OF
" H2°
»H20
" H2°
" H2°
" H2°
••H20
Readinq
— •
FV?
7
—
>2r
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
j~ I
Page 1
Parameter
Time
Fuel gas flow % , 3 / { C? 8
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 X $f?0
SR Residue X $~$00
KIF00
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
.. B
II r* II
" D "
" A Out
" B "
II f* II
» JJ II
" A Inner
Meter No.
FR 156
PI 191
LRC-103
ift-eesf^^
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
—.O
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
* */n
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
op
op
" H2°
% Open
No Units
No Units
%
OF
OF
oF
op
op
OF
oF
OF
OF
oF
°p
Reading
/^;j^
£?r
63
5,2 <-l^c>Scl
7-3 V2?*f0
2*1 ?if0
— iff*? 40
7-f$~
Z<7^
7, $5
7.1
-&&- 750
757
-.0)5 ~,#3
. 6t>
o& 5'
00$"
r.t
—
710
?1 0
*3
-------
Control Room Data Sheet
Test No.
H-l
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
n B M H
ii c n n
II n II II
Temperature indicating panel console
Temp, below conv. section - NE end
11 " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
SW
Temp, of radiant section - NW
II II » II CM
Temp* pass C rad. sec. skin
II II JJ II II II
II II Q II II II
Temp. conv. - rad. crossover Pass A
II II II O II B
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
II II II II II JJ
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (Bast cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
•F
°F
OF
°F
°F
•F
°F
op
OF
OF
op
OF
op
OF
op
op
op
op
op
°F
op
«p
op
«p
•F
" H2°
" H20
" H2°
" H2°
" H2°
"H2°
Readina
—
£~y o
?r
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 f£ 12$
SR Residue
SR Residue to Htr. 33 - Pass A
X %GO ~ Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller- West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
.11 Q II
" D "
" A Out
ii B
" C
n D .1
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR '382
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRO 132
TRO149
TRO150
PR-153
OPTR-152
HIO149
HIO150
AR-151
TR-231
-1
-2
' -3
-4
-5
"*D
-7 .
•tmQ
-9
-10
Units
MMSCFD
psig
%
S
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
.Bbl/day
»F
°F
" H2°
% Open
No Units
No Units
%
°F
°F
OF
op
op
op
OF
op
oF
op
op
Reading
l/-~o?
t.H
Vf
62-
S~,2
7-6
2.0
_
7,^5"
7.°t
' 7.
- ,
—
1100
160
$00
6002 TP 5/20/76
73
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
" c " "
II Q 11 II
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
it n H n gw
Tempj pass C rad. sec. skin
H II Q II II II
ii n Q n n n
Temp. conv. - rad. crossover Pass A
" " " " " B
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
ii n ii n n ft
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
Meter No.
TR-232
-1
"•2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
op
OF
op
oF
op
op
oF
op
op
op
op
op
OF
oF
OF
OF
op
op
oF
op
op
OF
op
op
oF
»H2o
" H2°
" H2°
" H2°
" H20
"H20
Readinq
720
7?t>
7?o
7?0
7^0
—
120?
12 Zl
ii fi
13*0
$-3-3
12 07
• 122)
1302-
)3^2
r^r
Hit
$27
F*l%
to?
75 7
605*
FW
7?)
12-1.0
-6,03
-1-0,02-
1-0,0?
-0,o5~
'0,#C
6002 TP 5/29/76
74
-------
KVB
Location 4
Control Room Data Sheet
Date
No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 — ^
SR Residue J
W
SR Residue to Htr. 33 - Pass A
X $00 - Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
n B it
H c H
.. D
" A Out
B
H c «
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
iB-68T— "
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-15i
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
8F
" H2°
% Open
No Units
No Units
%
op
°F
oF
op
op
op
op
op
op
op
°F
Reading
//'30
6,t
F0
*3
—
7.3
2.3-
5~,3-
7.*
7.*l
'7.1
7.1
75-0
7?%
,06
ft
&&<*)
603
?.f
_
7f£>
V2*
Z$~e>
#?o
ZFO
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
» B ii ii
II p W II
II D II II
Temperature indicating panel console
Temp, below conv. section - NE end
1 " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
n » ii n sw
Tempj pass C rad. sec. skin
It II n II tl II
II II rj II II II
Temp. conv. - rad. crossover Pass A
n ii n n n g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n n n n jj
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230. 2S
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
•
Units
°P
Op
•F
Op
op
OF
op
op
op
op
op
op
op
op
op
op
op
op.
op
op
op
op
op
op
op
11 H20
«H20
" H2°
" H2°
" H2°
"H20
Reading
7i0
7F0
7*0
7fO
7&0
—
1202-
12? 3
art
136 1
£27
12*3
' /2#3
12*? 7
1371
f31
HZ
12%
S~?7
£0?
7fl
£*$-
riz
75^1
«--/-!
- *02~
+ ~02-
+- ~ C>3~5~
-,o-?
-.OF
6002 TP 5/29/76
76
-------
KVB
Location 4
Control Room Data Sheet
Date
5.
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure HlS?#Pj££^
SR Resid. Surge Drum
Total. flow to #33, 34 — v
SR Residue )
(
W
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damps r position
Hand indicating controller-Bast
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B ii
» c "
H D ii
" A Out
II g II
" C "
II D II
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRO 132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149 i
HIC-150
AR-151
TR-231
-1
-2
-3
M
-5
-6
-7
-8
-9
-10
Units
- MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bbl/day
Bb I/day
Bbl/day '
Bbl/day
°F
OF
" H2°
% Open
No Units
No Units
%
°F
•F
°F
"F
«F
Of
•F
•F
°F
°F
•P
Reading
12' 00
/,y
r,*
.^ —
• 7.3
2.1
f.3L
?,
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
n B » H
ii p n n
n D » «
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
II II II H gW
Tempi pass C rad. sec. skin
II II 0 H 'I II
ii ii n H n n
Temp. conv. - rad. crossover Pass A
II M II II II n
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
II II II II II n
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
°F
°F
op
OF
OP
op
eF
op
Op
op
op
op
op
op
op
op
op
op
op
Op
op
Op
op
op
Op
" H2°
" H2o
" H2°
" H2°
•'H20
"H20
Reading
,T/^
-?
75-0
75~0
—
/-2*y
}2.- y
/.? -V^i
IZSf
$17
yy/
731
r
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flaw
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 -^
SR Residue /
(
^>
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
H B »
n c ii
" D "
" A Out
.. B ..
" C "
II Q II
" A Inner
Meter No.
FR 156
PI m//>/#
LRC-103
LR 382
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
' -3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
°F
. °F
" H20
% Open
No Units
No Units
%
°F
°F
°F
°F
OF
°F
°F
op
°F
op
«F
Reading
!2 - 3
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
« B ii ••
n c n u
n D n M
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE-
Temp, heater 33 stack
Temp, below conv. - NW
n n 11 sw
Temp, of radiant section - NW
i. n n H sw
Tempj pass C rad. sec. skin
II II n II II II
II II n II II It
Temp. conv. - rad. crossover Pass A
11 II II II II n
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
it ii n n ii Q
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Moter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
op
•F
OF
°F
°F
8F
°F
oP
op
op
op
°F
op
op
op
op
»p
op
op
op
°F
op
op
op
op
" HZO
" H2°
" H20
" H2°
" H2°
'• H20
Readinq
—
rzs
7
—
)/ -i.o
- .03
i~r03-
•hfo*~
-. *>£
-, 0f
6002 TP 5/29/76
80
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
1-2-
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34 -^
SR Residue /
/ .
^
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating co'ntroller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
» B "
" C "
" D "
" A Out
M B ti
" C "
" D "
" A Inner
Meter No.
FR 156
PI 191/f f
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
. -1
-2
<•. ^
-4
-5
-6
-7
-8 :
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bbl/day
Bb" I/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
op
11 H20
% Open
No Units
No Units
%
op
op
op
op
op
op
op
op
op
op
op
Reading
)3'0?
£«\
J7.5- /£&
—
17
7-1
L 2-2-
5~.3~
7, 1
7*1
'7,1
7.1
7iT/
7*7
-.02
ft
—
—
V. 7
—
7$0
tt*
t?0
t^P
25-Q
1$o
—
n*o
1000
#00
6002 TO 5/20/76
81
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
ii B ii »
" c " "
ii D ii ii
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
n H H ii sw
Tempj pass C rad. sec. skin
II II n II II II
II II Q II II H
Temp. conv. - rad. crossover Pass A
n n n n ii g
Temp, combined outlet A S B
Temp, conv- - Rad. crossover Pass C
it ig n n M n
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East) •
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
Units
Op
PF
OF
OF
PF
op
OF
op
op
OF
op
OF
°F
OF
op
OF
OF
OF
op
op
OF
op
«F
op
OF
" H2o
«H20
" H20
" H20
" H2°
"«2°
Readinq
5-30
7^0
7$~£>
76^0
7S~0
—
1200
}3-*) 1
)2^
1312.
4T-2J
1262
' 12? 3
12 f 7
13(7
23
-------
KVB
Location 4
Control Room Data Sheet
Date
5.6.
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Tota?. flow to #33, 34 — N
SR Residue x j
/
t—>
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
., B
» C "
" D "
" A Out
it g n
,. c
" D "
" A Inner
Meter No.
FR 156
PI 191/f /
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRO 132
TRO149
TRO150
PR-153
OPTR-152
HIO149
HIO150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
-*-
Bb I/day
Bb I/day
Bbl/day
Bb I/day
Bbl/day
Bbl/day '
Bbl/day
°F
op
" H20
% Open
No Units
No Units
%
op
OF
op
op
op
op
op
op
op
op
op
Reading
13' 3 f
6,0
31 / £-3-
£3
—
7.3
2,2-
?,2-
7-*!
7-1
7.$
7,1
753*
7J-8
-.*y
60
—
—
v.f
—
7$O
$10
*5~t>
$S~e>
?f*
1*0
—
1100
1000
310
6002 TP 5/20/76
83
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
» B M n
II £ II II
II D .1 II
Temperature indicating panel console
Temp, below conv. section - NE end
" " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
H ii « sw
Temp, of radiant section - NW
II II II II CM
Temp; pass C rad. sec. skin
II II Q II II II
n n Q » n n
Temp. conv. - rad. crossover Pass A
n N H n u g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
N H II II II JJ
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52 ,
.53 •
.54
' •
Units
op
°P
°P
°F
•F
OF
OF
op
°F
op .
OF
"F
op
op
op
op
op
op
op
op
op
op
op
op
op
" H2°
" H2°
" H2°
" «2°
" H2°
" H2°
Readinq
—
*-?&
7?tf
75~0
76~0
7S~O
—
111?
I2- t,0
- ,015
+• .02-
+• . O2-
-.05~
-.0C
6002 TP 5/29/76
84
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Y-J
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34 — ^
SR Residue )
/
^^
SR Residue to Htr. 33 - Pass A
- Pass B
t Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller- East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section '
Pass A - Mid
•;r;.;:,:»-.-, B- ,. « •
••,..; M c ••
« D n
A Out
« B
M c
" D "
" A Inner
Moter No.
FR 156
PI 191/^f
LRC-103
LR 382
FR-123
FR-102
FR-128
FRO- 129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
• TR-231
-1
-2
' -3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day '
Bbl/day
OF
OF
" H2°
% Open
No Units
No Units
%
op
oF
op
op
op
op
op
op
oF
op
°p
Reading
/i -0o
f.JL
"10 / S'S
^ 3
—
7,3*
2.2
sr.z
7. «?
7. 1
•7.f
7«?
-75"!
7??
-, 0f2-
Fi
—
—
v.r
—
7*0
ft*
$FO
e$~0
*?0
170
—
1/00
100 0
8/0
85
6002 TP 5/20/76
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
ii B ii »
II Q II It
n D « ii
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
" " SW
Tempj pass C rad. sec. skin
II II n tl II H
n it |j n » n
Temp. conv. - rad. crossover Pass A
ti n n ii n D
Temp, combined outlet A s B
Temp. conv. - Rad. crossover Pass C
N n M n H p
Temp, combined outlet C S D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
~.C
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
°F
°F
°F
°F
OF
°F
°F
OF
oF
OF
OF
OF
op
op
op
op
op
OF
oF
oF
OF
OF
OF
OF
oF
" H2°
" H2°
" H2°
" H2°
" H2°
"H20
Reading
T30
7
75*0
7F0
7?0
—
//??
1227
I3--77
1113
fil
13-3*0
• /2ZS
131 1
13 f£
*13
431
731
m
40%
7f*
Cog
602.
7Tt
•
-L0?
-c.iq
-C,0f
-o.ov
-0.) 3
•^,/z
6002 TP 5/29/76
86
-------
KVB
Location 4
Control Room Data Sheet
5
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 ~— ^
SR Residue /
I
~ ^
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating co'ntroller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
.. B
" C
• " D "
" A Out
B
,. c
" D "
" A Inner
Meter No.
FR 156
PI 191 /q$
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
—Q
-10
Units
MMSCFO
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bb I/day
°F
°F
"H2°
% Open
No Units
No Units
%
°F
op
°F
°F
OF
op
op
op
Op
op
op
Reading
^'38-
e.r
10 / $-2-
fl
— ^
7,3
2,2-
?'3-
7,3
7-1
•7,3
7.4
7*!
75T
-.022-
-------
Control Room Data Sheet
Test No.
Page 2
Ps IT a me t6 IT
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
M B n ii
M c n H
n £ M «
Temperature indicating panel console
Temp, below conv. section - NE end
" " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
H n n CM
Temp, of radiant section - NW
n n n n CM
Tempj pass C rad. sec. skin
ii n n n n n
II II Q II II H
Temp. conv. - rad. crossover Pass A
n n n n n g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n M n ii 0
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)!
Meter No
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
••
Units
op
op
op
Op
?F
«p
op
op
op
op
op
•p
op
op
op
op
op
op
op
op
op
op
op
op
op
" H2°
" H2°
" H2°
" H2°
" H2°
"H20
Readinq
—
*30
-?*$•
?5~0
7**
-?&*
—
HI?
)2*7
128V
ny*
?53-
I2t*
' 12 Z 3
/-2f y
1372
93V
13V
*le>
nz
eot
75~i
Se?
m
757
>-/,^
-.01
t ,02-
+• ,03F
- ,*&
-,0f
6002 TP 5/29/76
88
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34 ^
SR Residue /
(
^=>
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
n B it
" • C "
H D ii
" A Out
„ jj
II £ II
II Q H
" A Inner
Meter No.
FR 156
PI 191/
-------
Control Room Data Sheet
Test No.
Y-3
Page 2
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
ii B M n
H c n n
,n D n ••
Temperature indicating panel console
Temp, below conv. section - NE end
" " " " SB end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
n » ii sw
Temp, of radiant section - NW
n ti H n cw
Tempj pass C rad. sec. skin
II II n II II II
n n Q » n n
Temp. conv. - rad. crossover Pass A
II II H H II g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n » n n n jj
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
TR-232
-1
-2
» 1
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
op
°F
op
• op
op
Op
op
Op
°F
Op
op
op
op
op
op
op
op
Op
op
op
op
op
op
op
op
" H2°
»H20
" H2°
" H2°
" H2°
"H20
Readinq
-~
f3f
735-
71T0
7^0
7^0
—
t/17
12% 6
1273.
I3?V
*23
•'. ' •' 0
' ' 2.
/-,'-•• 3
' •• • ro
$11
W0
428
5~1t
toy
757
toy
Fit
7$-)
-l.oH
-0,62-
i-0,03-
f- fl f>2-
-•f.f r •
-f.C •-'
6002 TP 5/29/76
90
-------
KVB
Location 4
Control Room Data Sheet
Date
"test No. -
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34 — ^
SR Residue )
/
(-~&-
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
n B ii
" C "
" D "
11 A Out
ii B »
" C "
" D "
" A Inner
Meter No.
FR 156
PI 191/f g
LRC-103
LR 382
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HI C- 149
HIC- 150
AR-151
TR-231
-1
-2
' -3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
°F
" H20
% Open
No Units
No Units
%
op
°F
°F
°F
°F
op
°F
•F
°F
op
op
Reading
0H2 "7
1. $
33 /f3
62
—
ft
3.3
JT.J2.
7-1
7-1
'7r$
7-1
753
7F?
-.0/4
5~Z
II.*
II *£
1. 7
—
72*
$2-0
*5~0
$5~0
2S0
f&zo
—
It 20
120
210
ell- r*
ft -
9 1
6002 TP 5/20/76
-------
Control Room Data Sheet
Test No.
92
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
M n II II
11 £ It II
II j) II II
Temperature indicating panel console
Temp, below conv. section - NE end
' " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp,, below conv. - NW
sw
Temp, of radiant section - NW
ii » M n sw
Temp; pass C rad. sec. skin
II II D II II II
H II n II II II
Temp. conv. - rad. crossover Pass A
n H n n n p
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n II n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
,.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 -
.54
°F
°F
OF
op
°F
°F
°F
OF
oF
op
OF
°F
°F
oF
op
OF
oF
OF
OF
op
op
oF
op
op
op
" H2°
" »2°
"H2°
" H2°
" H2°
- H2°
Readinq
—
-?*/(?
7tf
-75-0
73?
—
12 5*3
1*273
lit?
13&S
?3I
1171
' /2-?3
/2
-------
KVB
Location 4
Control Boom Data Sheet
Date
5. G, -
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to. Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
H B n
" C "
N D n
" A Out
» a
" C "
" D "
" A Inner
Meter No.
FR 156
PI 191 /f g
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
. -1
-2
-3
^A
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
op
8F
«H20
% Open
No Units
No units
%
, °F
•p.
•F
°P
OF
•F
°F
•P
OF
°F
•F
Reading
*1 '-ft
1.1
?//***.
ei
if
6,1
3,1
sr,2
7-*
7.1
7.1S-
7*1
??3
If 7
- *,0J2.2
ft
l&. f
n.£
iftsrit. ttin6 — . , o
¥t9AK/0 0*1 5.] I
. • —
"7*0
*) *
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
II Q M II
II Q n n
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
SW
Temp, of radiant section - NW
» •• n n sw
Tempj pass C rad. sec. skin
ii n B ii ii n
n n rj n ti ll
Temp. conv. - rad. crossover Pass A
II II II II II n
Temp, combined outlet A S B
Temp. conv. - Rad. crossover Pass C
II II II II II r\
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26 '
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 -
.54
•
Units
op
OF
OF
op
PF
oF
oF
op
OF
op
op
»F
oF
op
op
op
oF
op
OF
op
• °F
op
op
OF
OF
" H2°
" H2°
" H2°
" H2°
" H2°
«H20
Reading
—
5-3.5-
7V0
7^0
7^0
7£/0
— -
/2.5V
1272-
1265-
1303
^31
1178
' )27S
I26
-0,0€
+ 0rO(
rc>,i
-0,07
-0,0-7
6002 TP 5/29/76
94
-------
KVB
Date
Location 4
Control Room Data Sheet
Test No.
5.6, = 0,07*
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
TotaS. flow to #33, 34
SR Residue
•
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
u B »
H p II
" D "
" A Out
B
II Q II
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bbl/day
OF
OF
»H2o
% Open
No Units
No Units
%
OF
OF
OF
op
. oF
°F
OF
oF
op'
op
°F
Reading
t£>'.31
?.*
W Sf2-
62-
if
7-#
I-?
.f-2-
?.&
7,1 X
7,*r
7,1
7?3
?r
-------
Control Boom Data Sheet
Test No.
Page 2
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
II Q II II
H c .1 ii
ii D H n
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - ME
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
II 11 II II CM
Temp i pass C rad. sec. skin
n II n H » H
II II n It el II
Temp. conv. - rad. crossover Pass A
n n n n n g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n n " n "0
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•F
°P
oP
op
op
°F
op
op
op
op
op
"F .
op
op
op
Op
«p
op
op
op
op
op -
op
«F .
Op
«H20
" H20
" H2°
" H2°
" H2°
"H20
Readino
—
rzr
?'/e
7F*
•?5~e>
?
$2-3
m
6& /
7f*
fei
mr
?tt
-l.O?
-,*5"
f~02-
+ -01
-~0-7
-.07
6002 TP 5/29/76
96
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
• Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue. to Htr. 33 - Pass A
- Pass B
. - Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating' controller-East
Hand indicating controller-West
• Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
ii B ii
H c ii
" D "
" A Out
" B "
" C "
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR U82
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
"-3
—4
-5 '
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day '
Bb I/day
°F
OF
" H2°
% Open
No Units
No Units
%
°F
OF
op
op
oF
op
op
op
op
op
op
Reading
fr-02-
1-1
?2/?3
62
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
M B ii .1
,, c „
ii D n n
Temperature indicating panel console
Temp, balow conv. section - HE end
II II II II C«T? n.«.3
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
n ii n n gw
Tempj pass C rad. sec. skin
n ll n ti « tl
n u rj n n n
Temp. conv. - rad. crossover Pass A
n li H n u 3
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n M n « " jj
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
°F
°F
oF
OF
OF
op
OF
OF
oF
OF
oF
Of
op
OF
op
oF
oF
oF
oF
OF
OF
oF
oF
OF
op
" H2°
»H30
" H2°
" H2°
" H2°
"H20
Reading
5-23~
7^0
75-0
77
-,e>7
6002 TP 5/29/76
-------
KVB
Location 4
Control Room Data Sheeb
Date
Test No. */--*/.
Page 1
Parameter
Time
Fuel gas flow (* ff.?!*??!*)
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube -wall temperature
Above convection section
Pass A - Mid
« B
ii c »
" D »
" A Out
H g
» c
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRO 132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
. -1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
RMSCFD
psig
%
%
Bb I/day
Bb I/day
Bbl/day
Bb I/day
Bbl/day
Bbl/day '
Bbl/day
°F
op
«H20
% Open
No Units
No Units
%
°F
°F
op
op
op
op
op
op
op .
Op
op
Reading
If: 3^
** f/.zs)
3? /jTJ
63
H2 •
7'0
1*0
?-?-
7,3
*-?
7~
$2-0
150
ts~*
*?0
/0W
//TO
1 000
tio
r*
6002 TP 5/20/7&
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B "
H p n H
ii p it n
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
H ii n sw
Temp, of radiant section - NW
n n ii n gw
Tempj pass C rad. sec. skin
n n n M n it
ii II n H II II
Temp. conv. - rad. crossover Pass A
n n n n " B
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
ii n n n n Q
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
mmj
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
Units
°F
°F
°F
op
pp
°F
°F
°F
op
OF
op
»F
OF
op
oF
OF
OF
OF
oF
oF
op
OF
OF
op
op
" H2°
" H2°
" H2°
" H2°
" H2°
" H2°
Readinq
6~3*
•?t/0
75~0
740
7*/0
—
)2~5~3-
12 73-
12-S~*I
150%
&26
t/£0
' 12? 3
12*2-
133?
rvv
W2.
*3~£
1
-0,0?
~oto?
6002 TP 5/29/76
too
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue,
SR Residue to Htr. 33 - Pass A
- Pass, B
- Pass C
- pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
•• B "
" C "
" D "
" A Out
ii B n
M ft n
» D it
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 382
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151 -
TR-231
-1
-2
-3
-4
-5
-6
-1
••8
-9
r-10
Units
MMSCFD
psig
%
%
Bb I/day
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
"F
op
" H2°
*{**«•££.
No Units
No Units
%
°F
°F
op
°F
op
op
°F
•F
op
op
«F
Reading
)2'2~?
1.2-
??/??
S3
ty
?.*>
2*3f
. ff %
&,7
IM
t'l X
.
7#0
if^*
#2-0
ZT0
t?0
/000
— -
//5> -
1*0
$3-0
6002 TP 5/20/76
1 0 1
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
n B M »
M p n M
n D n n
Temperature indicating panel console
Temp, below conv. section - NE end
" " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
n ii » n sw
Tempj pass C rad. sec, skin
II II |j II 'II II
II II p II II II
Temp. conv. - rad. crossover Pass A
n H n n » B
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n n n n n
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter Wo.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
op
°F
•F
Op
op
op
op
op
op
op
op
OF
op
op
op
op
op
op
op
op
op
op
op
op
op
" H2°
" H2°
" H2o
" H2°
" H2°
«H20
Reading
£?*
7?0
7f*
7?0
?55~
121*
H7J*
H43
15/0
f3f
I/?/
' &*/
/jf-y
/•**Y
iff
Wf-
f3-2-
5~
-------
KVB
Date
Location 4
Control Room Data Sheet
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Tota?. flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
" c "
•' D
" A Out
« B "
„ c
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRO- 131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bb I/day
op
«F
" H2°
% Open
No Units
No Units
%
Op
Op
op
op
op
op
op
op
op
op
op
Reading
A?:*/
1-t
3f/3"J
S^
cftf
f>1
f.0
^2-
7-1
?*3
'7,1
7*1
?,Z
l/,f
v.t
. —
•?
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
II o H II
II C II .1
II D « II
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
» „ n sw
Temp, of radiant section - NW
N N II II gJJ
Tempj pass C rad. sec. skin
n n D n ii n
n M jj n u n
Temp. conv. - rad. crossover Pass A
H n n n H D
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
"- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West) .
(East)
Meter No.
TR-232
-1
M *y
-3
-4
«. C
TI-230
230.25
.26
,27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
OF
°F
OF
°F
op
op
op
op
op
op
op
pp
op
«F
op
op
op
°F ,
op
op
op
op
op
op
op
11 H2o
" H2°
" H2°
" H2°
" H2°
" H2°
Reading
Z^S*
7V0
75&
74~0
7JT£-
,
/^r^
12-70
/^tt
15/3
fJ-7
//73~
' /Z72
IZ-fJ
13/3
#12-
tfljLS
#^2~
rlf
£03
7F3
£02.
Ft*
7f7
~ J.02 poMctfG
~0,C7
0,00
+ 0,01
-0,0?
-0,0$
6002 TP 5/29/76
1 04
-------
KVB
Date
Location 4
Control Room Data Sheet
•test No. l/-5~ fa I •" £
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
H c it H
» D H H
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
" n ii a sw
Tempj pass C rad. sec. skin
II II TJ II It II
II II r\ II II II
Temp. conv. - rad. crossover Pass A
n ii n ii H g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n il •• n Q
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
_c
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
^~~
Units
«F
°F
"F
op
"F
«P
op
op
op
op
op
op
Op
op
op
op
op
op
op
Op
op
op
op
op
op
»H20
" H2°
" H2°
" H20
" H2°
" H2°
Reading
.
6-2$-
7$Z
7^0
73?
?f0
/J2^/
I2tf~
12^3
)3/$~
F^
t/7f
• 13-7 *
12-03
l?03-
ztf
?f3
Z3-I
FVg-
£*>!
7^3-
£03-
r*£~
~?
6002 TP 5/29/76
1 06
-------
KVB
Date
Location 4
Control Room Data Sheet
Test Mo.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
n B n
" c "
.. D
" A Out
" B "
» C "
« D "
" A inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRO 132
TRC-149
TRO150
PR-153
OPTR-152
HIO149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
~fl
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bb I/day
°F ,
°F
" H2°
% Open
No .Units
No Units
%
OF
OF
°F
op
op
op
OF
OF
oF
op
op
Reading
/f.02-
Ctr3-
M/J-f
S2-
17
f.1
1.3
S-2-
7'f
?4
<7,3
7,1
7f*
7?r*
—0,60%
$-#
ft*,?
//-*
Lf-i.
—
#00
#3-0
#£0
#S0
£40
/&00
1/10
?$0
$)0
6002 TP 5/20/76
107
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
11 £ II »
II D II II
Temp, below conv. section - NE end
" " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
1 sw
Temp, of radiant section - NW
li ll ii n cw
Temp t pass C rad. sec. skin
II II g II II II
n n n n il li
Temp. conv. - rad. crossover Pass A
II II II II II g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n ii H " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
Meter No.
TR-232
-1
-2
-3
-4
-5
TT— 9^(1
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
°P
op
°F
op.
op
op
op
OF
op
op
op
op
op
op
op
op
op
op
°F
op
op
op
op
op
Op
" H2°
" H2°
" H,0
ft
" H2°
" H2°
»H20
Readinq
ir^5~
•75?
75-0
7?5~
7«0
I23Z
1 2-6-7
12-40
132-3
f^f
//?*/
' 12-tl
&g3
I?*'/
&S-2-
ff*
73-7
?7Y
S0f
7^3
£
-------
KVB
Date
location 4
Control Boom Data Sheet
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
8R Resid. Surge Drum
Tota? flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
» B
" c "
n D n
" A Out
II B II ,
" C
" D "
" A inner
Meter No.
PR 156
PI 191
LRCr-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRO 132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
. -1
-2
-3
-4
-5
-6
-7
Q
o
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
op
op
" H2°
% epeir£/
No Units
No Units
%
op
op
op
op
op
Op
op
op
op
op
op
Readina
11:33
?.&
39/4-1T
62-
Vf
?.l
1.2-
?*2.
&1
7,1
?.*$~
?.*!
?5*y
75-3-
~~<>f
3~g
{&,£
//~~7
V,g
- — •
$00
#30
#5*0
?$~0
#?#
/03~0
•
//3-0
ft*
13-0
1 09
71
6002 TP 5/20/76
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
M c it ii
ii D n M
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
n n » n gw
Tempj pass C rad. sec. skin
H II Q If II II
t* ii n n n n
Temp. conv. - rad. crossover Pass A
n H M n n »
Temp, combined outlet A S B
Temp. conv. - Rad. crossover Pass C
II II It II II r\
Temp, combined outlet C S D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31 T
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
°F
op
OF
°F
°F
°F
°F
OF
°F
OF
op
»F
°F
°F
°F
°F
op
OF
°F
°F
°F
°F
°F
°F
op
" H2°
" HO
" H2°
" H2°
" H2°
"H20
Readinq
^30
7ffO
750
~7?O
755~
tef 2-
)2-??-
12-72-
nc&[
-&.C-?
-0,07
6002 TP 5/29/76
1 1 0
-------
KVB
Location 4
Control Room Data Sheet:
Date
•test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SRPResid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand- indicating controller- West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
It Q It
" D "
" A Out
" B "
It £1 II
" D "
" A Inner
Meter No.
FR 156
PI 191/7 f
LRC-103
LR §82
FR-123
FR-102
FR-128
FRO 129
FRO 130
FRO131
FRO 132
TRO149
TRO150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
— 1
-2
" -3
-4
-5
-6
-1
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bbl/day
OF
op
" H20
% Open
No Units
No Units
%
°F
OF
OF
op
op
op
OF
oF
op
op
op
Reading
ie> :3- o
£. 2.
vo /
-------
Control Room Data S^eet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
II Q It II
II p II II
II p II II
Temperature indicating panel console
Temp, below conv. section - NE end
" SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
,< ii sw
Temp, of radiant section - NW
n n n n sw
Tampj pass C rad. sec. skin
n n D ii u n
II II Q II " II
Temp. conv. - rad. crossover Pass A
II II II II II 0
Temp, combined outlet A 6 B
Temp. conv. - Rad. crossover Pass C
n n n n n Q
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Met© r No
TR-232
-1
-2
-3
-4
-5
TI-230
230. ?5
.26
.27
.28
.29
.31
.32
' .33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
•
Units
•F
op
op
op
»P
Op
op
op
op
op
op
BP
op
op
op
op
Op
op
op
op
Op
op
°F
op
op
"'H2°
" H2°
" H2°
" H2°
" H2°
"H20
Readina
— —
4"Xf-
76/0
-?*/r
7*/5~
?*r
__
lit?
1202
tz&i
I2>*
^//
J200
' I3VH
>/ro
IWS
#1*
MV
*/l
FV?
£02-
7S~S-
£03
5" 3.
•h0,02-
+ 0,03
^0,0f
-0,07
6002 TP 5/29/76
1 1 2
-------
KVB
Location 4
Control Room Data Sheet
Date
NO.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
II g II
ii c »
11 D "
A Out
" B "
II p II
D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-13-1
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HI C- 149
HIC-150
AR-rlSl
TR-231
-1
-.O
-3
-4
-5
-6
-7
-8
— Q
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bbl/day '
Bb I/day
'F
op
" H2°
% Open
No Units
No Units
%
op
°F
oF
OP
op
OF
• op
op
op
op
op
Reading
W>5~0
6,3
3? /S0
£3
<*7
*.*f
?'1
jr,2-
?-£
3-5
$*2
*,-$
r*jr
— -
r^-^»
Z2-*
$5~e>
$3*
V3P
(62-0
,
//5~0
1000
$3-0
1 1 3
6002 TP 5/20/76
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
H B » M
H p n n
ii D H H
Temperature indicating panel console
Temp, below conv. section - ME end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
.. n » ii sw
Tempj pass C rad. sec. skin
II II n II II II
ii n Q ii n n
Temp. conv. - rad. crossover Pass A
II II II H II jj
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
ii n n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
Units
op
°p
OF
OF
oF
OF
oF
OF
oF
oF
OF
op
OF
op
OF
op
op
op
oF
op
op
op
op
OF
op
" H2°
"«2°
" H2°
" H2°
" H2°
"H20
Reading
.
r^tT
7V 3
75*0
7$~0
7£-0
. .
1272*
)30?
1211
)3^$~
rys
//
-------
KVB
location 4
Control Room Data Sheet
Date
test No.
Page 1
Parameter
Time
Fuel t>as flow
Fuel gas pressure
SR Resid. Surge Drum
Tota.«. flow to #33, 34
SR Residue
(1500*)
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 Bast
SR Resid out 33 West
Firebox pressure
.Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
II £ II
" D "
" A Out
i. B n
" C *
« D n
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153 '
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
. -1
-2
-3
-4
-5
-6
-1
-8
-9
-10
Units
• MMSCFD
psig
%
% '
Bb I/day
Bb I/day
Bb I/day
Bbl/day
Bb I/day
Bbl/day '
Bbl/day
8F-
°F
" H2°
% Open
No Units
No Units
%
OF
°F
OF
• op
op
OF
op
op
op
op
°p
Reading
/A'5V
t.3
3~3~
7,f5~
?'1
r.r
7,1
?sy
75^#
-.00?
?3
V'?.
V,3
£.7
— —
ffO-0
Z3#
*t0
$30
750
JG>i0
.
lit*
/0fi0
$30
6002 TP 5/20/76
1 1 5
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
» c n ••
" D " "
Temperature indicating panel console
Temp, below conv. section - NE end
" " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
n n n sw
Temp, of radiant section - NW
n n n n gw
Tempj pass C rad. sec. skin
n n n ii n n
II II r\ II II It
Temp. conv. - rad. crossover Pass A
II II II II 1* n
Temp, combined outlet A s B
Temp. conv. - Rad. crossover Pass C
n » n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
Units
op
op
op
op
op
op
op
op
oF
op
op
op
op
op
op
°F .
op
op
Op
op
op
op
OF
op
op
" «2°
" H2°
" H20
" H2°
"»2°
" H2°
Reading
f*20
75~&
7£~0
75~G
73^0
>
/JT^.^2.
1326
13 '/.Z
f j£~ %j /'
^ ^ &
/206
/3/~7
//tf^.
/?*//
Gr * f
£f 9 f^^
tf/3
z~i~?
£0g
7*3
fc?7
£00
• 75~0
—
~/,^y
— #, it
-0, O3-
•f- 0 f& l
- &,&#
— £? 0^
6002 TP 5/29/76
1 16
-------
KVB
Location 4
Control Room Data Sheet
Date
Test Mo.
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
" C " '
II Q II
A Out
" B "
" C "
» D "
" A . Inner
Meter No.
FR 156 '
PI 191
LRC-103
LR 382
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
H1C-150
AR-151
TR-231
. -1
-2
' -3
-4
-5
-»o
-7
-8
-9
-10
Units
' MlteCFD
psig
%
%
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
•F
• OF
" H2°
% epew-^T/
Mo Units
Mo Units
%
CF
«p
•F
•F
OB-
OP
°F
°F
•OF
•F
op
Reading
)2 s*fo
t.r.
$?/ff
63
2 7
£,<1
F'Z
IT-/
7..1.
7.1
7,1
7
-------
Control Room Data Sheet
Test No.
'f-7
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
» B ii ii
ii c » ..
ii p n ii
Temperature indicating panel console
Temp, below conv. section, - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
ii n n sw
Temp, of radiant section - NW
" " " " SW
Tempi, pass C rad. sec. skin
n II n ii tl II
II II r\ II II It
Temp. conv. - rad. crossover Pass A
n n ii n M jj
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
II II II II II T\
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
•47
.48
.49
.50
.51
.52
.53 -
.54
•
op
Op
op
Op
pp
°F
op
op
op
op
op
op
op
op
op
op
op
op
op
op
Op
op
op
op
oF •
" H20
" H20
" H2°
" H20
»H20
"H20
Reading
Tj-jr
75~#
7V0
7T0
7$~0
-
/277
1330
'201
I3-7Z~
5-?~£
J&07
' 1333
tz-ro
137*.
V2 2~
,#/
/- 0,03-
-f,?^
-0,0*}
6002 TP 5/29/76
1 1 8
-------
KVB
Date
No.
Location 4
Control Room Data Sheet
/C
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue X £~&&&
X I5~£?&
x $67^
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
" C "
'• D "
" A Out
it B ii
" C "
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day '
Bb I/day
op
op
»H20
% ep«*£7
No Units
No Units
%
op
OF
op
op
op
op
op
op
op
op
•p
Reading
01 '06
£' ~7
3$/f7
gf
V5~
7-*
3. 1
£~, 2-
frff
?, f
'7.^
-7.1
7 ftf
?fe
- 0>r0f2.
ft
%, (
#, 3
ttf+-*J^
?2-
-------
Test No.
Control Room Data Sheet
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
n c ii n
ii D H H
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
ii n ii sw
Temp, of radiant section - NW
« ii n n gj^
Temp; pass C rad. sec. skin
" " B '
II II JJ H II II
Temp. conv. - rad. crossover Pass A
II H ii ii ii n
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
n n n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East) •
««i
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.S3 •
.54
v»
0P
•p
«F
op
op
op
op
op
op
op
op
OF
op
op
op
op
op
op
op
op
op
°F
•p
°p
"F
" H2°
"«2°
" H2°
" H,0
ft,
" H2°
..„,„
Reading
-T3JT
7*/5~
73
-0,01
-0.02L
•&~
-#,(0
-6,)0
6002 TP 5/29/76
1 20
-------
KVB
Date
Location 4
Control Room Data Sheet
K&» f
Test Mo.
*-/~
*tl
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" a "
» c »
" D "
" A Out
.. B
" C "
" D "
" A inner
Moter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-1
-8
-9
-10
Units
M.MSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bbl/day
Bb I/day
Bbl/day '
Bbl/day
op
OF
" HO
% Q?**CI
No Units
No Units
%
°F
OF
op
op
op
op
op
op
op
op
op
Reading
1 fiies~
/,*?
3Z/r(
si
+• &3V
?3-0
Z3~0
*f£ 0
*t0
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
H B « »
II £ II II
II JJ II II
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
" n H sw
Temp, of radiant section - NW
it n n n sw
Tempj pass C rad. sec. skin
II II D I' " I'
II II T\ II II II
Temp. conv. - rad. crossover Pass A
II II II II H |V
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
" n n n n " p
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
°F
op
op
Op
op
op
op
op
op
op
op
OF
op
op
op
op
Op
op
op
op
op
Op
op
op
op
" H2°
" H2°
" H2°
" H2°
" H2°
"H20
Reading
£30
?*/
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
• Pass A - Mid
» B "
C "
" D "
" A Out
n B M
,. c
'• D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 382
FR-123
FR-102
FR-128
FRC-129
FRO 130
FRO 131
FRO 132
TRO149
TRO150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
"-3
-4
-5
-6
•»7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
°F
»H20
% Cpen^/
No Units
No Units
%
Op
»F
OF
op
op
op
op
°F
op
op
op
Reading
/&''?/
*,1
3? /^T
*r
tr
6-1
7.H .
S.3-
?-1
7, 1
7,3
7,7
7*3
7S0
-0,0/3
fir
t'2.
8.2-
<^T
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
1. g i. n
.. c „
II rj » tt
Temperature indicating panel console
Temp, below conv. section - NE end
SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
SW
Temp, of radiant section - NW
•• n n n sw
Tempj pass C rad. sec. skin
11 II J> 1* H 1*
II II r\ II II II
Temp. conv. - rad. crossover Pass A
II II II II M D
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
" D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 •
.54
•
oF
op
op
op
.OF
op
OF
op
op
op
op
OF
OF
OF
OF
op
op
OF
OF
OF
op
«F
OF
op
op
" H2°
" H2o
"H2°
"»2°
»H20
"H20
Reading
G~3C>
7V0
7cf£~
7*f$~
7f0
—
H tf 0
13-tf
y Y5".2-
M7*
5-^0
1213
!$/ 0
13
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR, Resid, Surge Drum
Total flow to %33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-Bast
Hand indicating controller- West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
,, B
M c n
H Q II ,
" A Out
i. a n
II q II
" D "
" A Inner
Meter No.
PR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-1S1
TR-231
. -1
-2
-3
-4
-3
-6
-7
-8
'-g
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
CF
°F
" H2°
% epe*
W
2¥*
6002 TP 5/20/76
125
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
II g II II
ii r* » n
II n n II
Temperature indicating panel console
Temp, below conv. section - NE end
" SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
SW
Temp, of radiant section - NW
" " " " SW
Tempj pass C rad. sec. skin
II II n II *l tl
ii ii n n ii n
Temp. conv. - rad. crossover Pass A
ll II II II ll »
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
ii n n n " D
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East) •
Motisir No
TR-232
-1
-2
-3
-4
-5
TT-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
Units
op
op
op
op
op
op
op
op
op
«P
op
»p
op
op
op
op
op
op
op
op
op
op
op
op
op
" H2°
" «2°
" H2°
-H20
"H2°
" H2°
Readinq
' '
$-30
7 ^S~
7 $ &
75" &
~75~&
// &8
12-0%
/t/fj-
/
-------
KVB
Location 4
Control Room Data Sheet
Date
Test No.
?''77
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass &
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
11 B "
» c „
» D "
11 A Out
'• B
" C "
" D ".
" A Inner
Meter No.
FR 156
PI 191/fjP
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231 .
-1
-2
-3
-4
-5
-6
-1
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
OF
" H2°
% Open
No Units
No Units
%
op
°F
8F
°F
°F
op
op
op
Op
op
op
Reading
//-•^(J7
*,?-
3^/5-7
*1
V?
6,3
?.
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
ii £ n H
n jj n n
Temperature indicating panel console
Temp, below conv. section - NE end
11 " " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
II II II II CM
Tempj pass C rad. sec. skin
" B " , "
ii n n n M ii
Temp. conv. - rad. crossover Pass A
II II II II II Jj
Temp, combined outlet A 5 B
Temp. conv. - Rad. crossover Pass C
n n n n H n
Temp, combined outlet C & 0
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)-
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
,27
.28
.29
.31
.32
.33
'.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
Units
•P
°F
oP
«F
•F
"F
°F
OF
°F
°F
op
op
°F
op
op
op
«F
°F
op
op
op
op
op
op
op
" H2°
" H20
" H2°
" H2°
" H2°
" H2°
Reading
—
fj$~
?5~0
75~#
7^0
7F0
,
12/2-
1 £.?-€>
11*7
/52-5~
m
(**-$
' l*7/
I*?*
13f*
f*/t
tf?2- ?
^7f
C*0
S0g
fry
£0 g
£#/
7f3
.
~/f*1
-6r 0$
~ffi,G>l
+-6.0\
-*,0g
-0,0*1
6002 TP 5/29/76
1 28
-------
KVB
Date
Location 4
Control Room Data Sheet
• f tt
19 0& **
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
n C "
n Q n
A Out
II B II
" . C "
" D "
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR '382
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRO- 132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MM'SCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day '
Bb I/day
°F
°F
" H2°
% Open
No Units
No Units
%
°F
°F
°F
op
°F
op
op
op
op
°F
op
Reading
13-33
4,3
W /
12-0
3/0
*r*
$5-0
— .
/^^^
?{
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
It £ II II
II D II II
Temperature indicating panel console
Temp, below conv. section - NE end
" " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
H n ii sw
Temp, of radiant section - NW '
» n n ii sw
Temp,* pass C rad. sec. skin
II * II D II II II
II II r\ II It It
Temp. conv. - rad. crossover Pass A
» n n n H Q
Temp, combined outlet A s B
Temp. conv. - Rad. crossover Pass C
II II II II II r\
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East)
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
•
Units
OF
«F
op
oF
.OF
OF
op
OF
op
OF
OF
OF
OF
oF
OF
oF
op
op
op
OF
oF
op
OF
OF
oF
" H2°
" H2°
" H2°
" H2°
" H2°
" H2°
Reading
T 35'
7T&
75-0
-75~0
-75-0
.
.// ^v'
/^//
/!>-£>&
15"?^
/T//y
13/3
' t33~5~'
,/'/<•/<-/
)V0/
#71
H77
%ef^
j" s*\ ,. ~t
6 <-• '^~
^:- '/ .
•?*i ,.-.-
ft
£e *
x>; y
^ —
-t,*3L
~ C, CJ2,
-f,C-3~
^~~
-
-------
KVB
Location 4
Control Room Data Sheet
Date
5 £ =
Test No.
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Res id. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
.. B
.. e
n D ii
" A Out
ii B »
" C
.. D »
" A Inner
Meter No.
FR 156
PI 191
LRC-103
LR 882
FR-123
FR-102
FR-128
FRC-129
FRC-130
FRC-131
FRC-132
TRC-149
TRC-150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
-8
-9
-10
Units
MMSCFD
psig
%
%
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day
Bb I/day '
Bb I/day
°F
°F
" H2°
% Open
No Units
No Units
%
op
OF
oF
op
op
op
oF
OF
oF
oF
op
Reading
/yr^.2.
^<£
^f/jf 7
*y-
16
•7r6
?'%
5-2-
7.1
7,4
zf
?^
7?y
7£0
— 0fe/£
5T
, — .
£.3
$20
Z 2.0
*t <&&
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
II g II II
II £ II II
" D "
Temperature indicating panel console
Temp, below conv. section - NE end
" " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv- - NW
" " " SW
Temp, of radiant section - NW
n ii H ii g^
Tempj pass C rad. sec. skin
II II n II II II
II II r-\ II II II
Temp. conv. - rad. crossover Pass A
n n n n " g
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
11 II II II II r\
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East coll)
(West cell)
Heater firebox (West)
(East)
Moter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
Units
OF
«F
op
op
op
OF
op
op
oF
OF
op
OF
OF
OF
OF
OF
OF
OF
op
OF
op
OF
oF
OF
OF
" H2°
" H2°
" H2°
" H20
" H2°
" H2°
Reading
^r?^r
? 3~0
75-0
75-0
-?$-&
its"?
13-1 f
I
-------
KVB
Location 4
Control Room Data Sheet:
Date
Test Mo.
!AJ
Page 1
Parameter
Time
Fuel gas flow
Fuel gas pressure
SR Resid. Surge Drum
Total flow to #33, 34
SR Residue
SR Residue to Htr. 33 - Pass A
- Pass B
- Pass C
- Pass D
SR Resid out 33 East
SR Resid out 33 West
Firebox pressure
Damper position
Hand indicating controller-East
Hand indicating controller-West
Oxygen in stack
Tube wall temperature
Above convection section
Pass A - Mid
" B "
H c it
n D M
" A Out
II B II
II £ II
» D .1
" A Inner
Meter No.
FR 156
PI 191 /f^
LRC-103
LR 882
FR-123
FR-102
FR-128
FRO 129
FRC-130
FRC-131
FRO 132
TR0149
TRO150
PR-153
OPTR-152
HIC-149
HIC-150
AR-151
TR-231
-1
-2
-3
-4
-5
-6
-7
"•fl
-9
-10
Units
MMSCFD
psig
%
%
Bbl/day
Bb I/day
Bbl/day
Bbl/day
Bbl/day
Bbl/day '
Bbl/day
°F
"F
«H20
% Open
No Units
No Units
%
°F
eF
"F
«F
°F
op
°F
"F
»F
op
op
Reading
&1&0
'[.5~
19/V7
t£
V(
7-0
*&-
K£
7-2-
*>",> 2~
7*2
^z.
7f~j-
7*0
.005-
£0
^
/^
r.f
— .
$00
32-e
s"f0
^0
ttf
/00£>
—
/^/^
J000
1W
6002 TP 5/20/76
-------
Control Room Data Sheet
Test No.
Page 2
Parameter
Oil Pass temperature
SR residue feed to 33 & 34
Pass A oil out
" B " "
M p ii n
II n II II
Temperature indicating panel console
Temp, below conv. section - NE end
" " " SE end
Temp, radiant section - NE
- SE
Temp, heater 33 stack
Temp, below conv. - NW
sw
Temp, of radiant section - NW
" » " " SW
Tempj pass C rad. sec. skin
If II n II " II
II II r\ II II II
Temp. conv. - rad. crossover Pass A
II II II II II n
Temp, combined outlet A & B
Temp. conv. - Rad. crossover Pass C
II It II II II r\
Temp, combined outlet C & D
Draft gages
Heater stack - above damper
- below damper
Heater roof tubes (East cell)
(West cell)
Heater firebox (West)
(East) •
Meter No.
TR-232
-1
-2
-3
-4
-5
TI-230
230.25
.26
.27
.28
.29
.31
.32
.33
.34
.42
.47
.48
.49
.50
.51
.52
.53 .
.54
Units
op
op
op
op
op
Op
op
op
«F
op
op
x>p
op
op
op
op
op
op
°F
op
°F
op
°F
op
°F
" H2o
»H2o
" H2°
" H2°
" H2°
" HO
Readinq
5-y5"
75-*
7^0
rcc>
-7V5"
—
13-2-2-
123 f
)3-£3
)2- 72.
jT/5-
H?3-
' !&*?*/
tZVtf
n&t
%2-tj
1(3$
$1 f
g o±]
£//
?sr
g/T
f*>1
~~,^ ?
-t.*
+• >$"?
4$"
+ r02-
+-,0 15~
* .ot IT
6002 TP 5/29/76
1 34
-------
Location 4
Fuel Oil Analysis
?est 4-4
Carbon, % 87.38
Hydrogen, % 11.87
Nitrogen, % 0.28
Sulfur, X 0.40
Ash, % Q.00
Oxygen (by difference), % 0.07
Gross Beat of Combustion, BTU/lb 19,070
Net Heat of Combustion, BTU/lb 17,980
Fuel Gas Analyses
Test 4-1 4-2 4r5 4-6 4-8
Oxygen , 4.23 < 0.01 0.13 0.21 0.10
Nitrogen 16.3 0.07 1.11 1.68 2.10
Carbon Dioxide 0.36 0.060 0.32 0.059 0.14
Carbon Monoxide 0.52 6.71 0.54 0.62 0.57
Hydrogen 9>2? 12.9 12.8 12.7 11.8
Methane 51.79 49.11 61.01 49.4 52.42
Ethane 9.63 17.2 12.8 16.2 14.3
Ethylene 1.07 0.96 1.41 1.71 1.62
Total C3 5,24 16.2 7.44 14.7 15.1
Total C4 1.02 1.72 1.55 1.92 0.91
Total C5 0.50 0/96. 0.79 0.73 0.86
Total C6 0.054 0.11 0.10 0.068 0.087
Heating Value 932.6 1372 1186 1325 1301
(BTU dry/SCF)
1 35
-------
PROCESS HEATER DESIGN DATA
Location No. 5 Unit No. /
Unit Description
»>rrti ig ft 002
Installation Date /"f 7
Burner Description // ^W/M/V*^ 0II/6AS & 'MM A S
Test Fuel
Fuel Temp, at Burner
Primary Air Temp. (*F)
Heater Rating
Comments:
1 36
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
~ 2 " So , Location -^
Test Nov
Engr.
Fuel
Capacity_
Onit Type_
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O;> (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. ("F/'C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
r-/
£'2-7f
0^00
H.
?<-/
71
3
$1
/*,
(0
$
f
6
*\
*7 &
f \r
J
12
D
u
3,3
P.?
ft
62
2
1
4
-------
Test No
Unit No.
. r//-.
MOBILE LABORATORY DATA
Date f~?~?£ Location JT~
Fuel £rf 5 Capacity
Test No._
Engr.
Onit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 03 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/eC)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity {%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
r-2-
6-2-#
12.00
5~.
7*
7*
2-
10
$-
27
ff
2.
10?
1.7
12
3
/
/V
3,5"
1-3
/7
( '2
21
f
12*
2.3-
£3~
f%
f 1
<21,1
21%
•
S~-2-
6-2-7S
/i#0
.
5~*3-
76 17
7? $&
\ /
f2. I&?
1.S
to II
2- 2<3
t 1.1
7^
6?
*H ^9 ^P^^
^£* ^f~+ mr t
73*7*
-
Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
138
Data Sheet 6002-2
-------
Test No/
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No._
Engr.
Fuel G>n
Capacity_
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
#
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (*F/°C)
19. Dew Point Terno. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
r-3
t~?-7£
0f/f~
3.i
£2
ft
1
71
/#.
(0
2.
r
t
*i
63
1
?2
>8
(0
($~
6i
3-
<^Q£
s».
?*£
^^^
S~~ ?
6~3~7f
/000
5.3
//
67
/
7
10
3-
7
*1
6*
I
#0
rff
jy
t0
ft
f£-
2
1
10
3
72
72
0
$3.
/.
10
ft
£3-
21,2$
73-
>
f-3
6-Z-7S
//00
,
H
70
ft
3-
$0
/#,
10
1
g
1?
72
70
3-
X3.
6
t0
Sf
£3-
27,3?
72-
r~3
t-?-7j
S/20
3'V
7& 72
70 72.
& 0
*l 9?
//*#
tO 10
1
1
£8
f2-
21'f
7S
*Correction to 3% 0- should not be performed if
the value is measured on a wet basis.
1 39
Data Sheet 6002-2
-------
Test No._
Unit No.
" 7
MOBILE LABORATORY DATA
Date 6 '3' 7 6 Location _ _
Test No._
Engr.
Fuel
Capacity
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke ' Spot (Bacharach)
18. Atitos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
r-i
£~3-7£
& 1'J~
£~,0
71
jf A
& r
2.
$3
/*>'
t
0
f~
#0
7#
2
13
0
1
5,£
£
/*,0
?7
33~
2-
it
& v
. 7
0
^
ft
£7
/
7f
6
11*
£.?
70
63
-2f.f
*3
•
5~-f
£-?-?(
I3f$~
tftf
I/
13
2
11
7,
7
\
6
*l
£l
2
73
r
I0.i
!•?
Z.I
70
£3
ll.fl
/f
r
'Y
(-3-7S
/5V5"
5~'5~
f/
ff
1
IJ*
/a
/£>
0
1
W
//^
/
)3-$
xy
"w
/3-
10
72.
£6
31.81
73
•
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
1 40
Data Sheet 6002-2
-------
Location 5
Control Room Data Sheet
Date
Vast No.
Unit Mo.
Parameter
Una
H-100 Temperature
Reformer Charge
H-100 Outlet Tang?
Stack 02
Reformer Charge
E-100B, E-100D
Firebox* west
Firebox, east
fWI Fit"* „
frftl rfff*S/>//f$
' Heaters outlet
tubeskin West
•
•
•
•
to
•
•
m
m
•
• «ast
Meter Mo.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
t
1000 BBLD
•F
•F
•%? */*'
•F
°F
•F
»F
•F
.•F
•F
•F
•F
•F
•F
•F
•F
Readings
f;
-------
Parameter
Tubeskin (test
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East^^j*
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
F1V201
—
—
__
_
—
—
—
Units
•F
•F
•F
•F
•F
°F
•F
PF
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
inches water
Readings
V002-
I0?0
005
f0f1
f*ir
/eye
yet
/200
Z.ffxZVfzlZZxio*
/0
—
-.ft j-.(f
-.13
-.ft
-. 2-
-,2
-.2-
142
-------
Location 5
Control Room Data Sheet
Heat Ho.
Onit Ho.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
?r£AM W/
1T£4f1 f>*ffS./r//1f.
Heaters outlet
tubeskin West
•
*
•
•
to
•
•
•
•
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
'-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
»F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
£>1
-------
Parameter
Tubeskih West
to
East
fop Convection
South end
Bottom Convection '
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East
Bef. Beaters
South stack
below Dangers
Kef. Heaters
South Stack
above Dangers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
—
—
_
—
~
—
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
inches water
inches water
inches water
laches water
inches water
inches water
Steadings
/^y/
/^^^-
/^^"/"
/
-------
Location 5
Control Room Data Sheet
Pate
*B8t HO. 4~-
Unit No.
Parameter
Time
B-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
srfAH fiew
fr£AM rt/ss./r/w
' Heaters outlet
tubeskin Nest
•
"
•
"
to
•
•
•
•
•
• Cast
Meter No.
TR-201-H100
FR-303
TIC-201
PIC- 301, 302
Tl-1-110
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
V.
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/0;J3~
U7
&-0
127
003
f,* /f, 0
J2*7
12* £
37 K
— /Wgf
127
117
1011
t*f£>
/c?S*3-
/0t0
It*
f^*
.f^^
31S
tet5
t02q
1 45
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East/^/sr
Kef. Heaters
South stack
below Oaapers
Ref. Beaters
South Stack
above Dangers
Oonv. sect, upper
between 100/101
Oonv. sect, center
between 100/101.
Oonv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FOS201
—
—
— •
__
—
—
—
Units
•F
•f
•F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Inches water
Headings
?7f
A?*//
/*5-y
/eyj~
102 7
f*l
ntt
^.^5-
/^
—
-^yx-.o'y
-.13
~'V*
—. 2-
-.2-
-.2-
1 46
-------
Location 5
Control Room Data Sheet.
Date 6-2-7*
test Ho. &~-/
Unit Mo.
Parameter
line
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
fTftn f£0"'
fre*n r*fsf/rfff/>
Heaters outlet
tubeskin West
•
•
•
M
to
•
•
•
•
•
• Bast
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
'-120
-121
-122
-123
•124
-125
•126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
*/t/x * /o*
•F
•F
•F
*F
•F
.'*
•F
•F
•F
•F
•F
•F
•F
Readings
/0J2-
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection '
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox Bastyj^/^
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FF-201
—
—
_
__
—
~
—
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD x 10
psig
.—
inches water
Inches water
inches water
inches water
inches water
inches water
Readings
te* 3
/ee 5-
— • —
/0ff
/0V/
/e>?5~
V#(
//ff
Zrff
S0
—
-. S2 /~.S2
~~ /2~
- .V7
--/'
— .2*
-J-?
148
-------
Location 5
Control Room Data Sheet
*est No. 5~—/
Unit Ho.
Parameter
Tine
H-100 Temperature
Reformer Charge
H-100 Outlet Tenp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox/ east
frfsrt ftt»
SrgAM 7£1t>
' Heaters outlet
tubeskin West
•
•
•
•
to
•
•
9
•
•
* But
Meter Mo.
TR-201-H100
FR-303
TZC-201
FIC-301,302
Tl-1-110
-111
•114
-115
-116
-117
-118
-119
'-120
-121
-122
-123
•124
•125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
#/M */0*
V
•F
•F
•F
•F
•F
. »F
•F
•F
•F
•F
•F
•F
•F
Readings
I1°3
127
12-
12-?
f,*
f/s
13-??
J2ZJ
?7
VS~/
-------
Parameter
Tubeskih West
to
East
Ttop Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East>j£«y.
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter Mo.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
^^
_
—
—
—
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Inches water
Readings
v^*
/'/y
. —
WJ
/e^e
/ffl
yoo
t/17
z,
-------
Location 5
Control Room Data Sheet
Pate
»BBt HO. f-^
Unit No.
10/10
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
B-100B, E-100D
Firebox, west
Firebox, east
*/"/>/-7 f{,t*>
srfArt rfrrfi
' Heaters outlet
tubeekin West
•
•
•
•
to
*
•
•
•
"
• East
Meter Mo.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
*$?
-114
-115
-116
-117
.-118
-119
'-120
-121
-122
-123
-124
-125
•126
Units
•F
1000 BBLO
•F
%
1000 BBLD
•F
•F
'V/p/e "-/^s
V
•F
•F
•F
»F
•F
• .F
•F
•F
•F
•F
•F
•F
•F
Readings
/206
12?
/0rO
3-
rfsr
1 5 1
-------
Parana tar
Tubaakin Heat
to
East
Top Convection
South and
Bottom Convection
Section
Gaa Flow to
Unit 100 x 348
Gaa Header Press.
Draft Gages
Firebox East^^f
Raf. Heater*
South stack
below Dampers
Raf. Heaters
South Stack
above Danpers
Oonv. sect, upper
between 100/101
Oonv. Met. center
batmen 100/101
Oonv. mot. lower
between 100/101
Meter No.
TI-l-138
139
140
141
142
143
244
248
FT-201
..
—
...
—
. _
—
-
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD X 103
P*i?
..
inches water"
inches water
inches water
inches water
inches water
inches water
Readings
' I0ff
tori
— •
/Ml
ff>*-3
/*//
«00
t/?*
--2-1
~~*0
1 52
-------
Location 5
Control Room Data Sheet
Data
Vest No.
Unit No.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-1000
Firebox, west
Firebox, east
frpsr? fif&
sreArt r£vr
' Heaters outlet
tubeskin Nest
•
•
•
•
to
•
•
•
•
•
• Bast
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
'-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
**
'F
•F
•F
•F
»F
•F
•F
•F
•F
•F
Readings
/3.?2
fef
/0, 4
-------
Parameter
Tubeukin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox Easty^jr
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv, sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
Tl-1-138
139
140
141
142
143
244
24S
FT-201
—
.
__
__
—
—
~
Units
•F
•F
«F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
inches water
inches water
, inches water
inches water
inches water
inches water
Headings
'/0*s
/0f3-
.
t0f7
f#Jl
I* /7
-------
location 5
Control Room Data Sheet
Date
*BBt NO. 5*~ 2-
Unit No.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
57>>**r TW
SrfAtf fH«J
1 Heaters outlet
tubesxin west
•
•
•
•
to
•
•
m
m
»
" Bast
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
*F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
IJ0-7
32$'
/0,e
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East/^,^^
Fef. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
__ ,
—
__
_
—
—
—
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD x 103
peig
—
inches water
inches water
inches water
inches water
inches water
inches water
Headings
1*11
/*?
-------
Location 5
Control Room Data Sheet
*Mt Me.
ttait No.
Parana tar
Una
H- 100 Temperature
Reformer Charge
H-100 Outlet Stop
Staok 02
Reformer Charge
S-100B, B-IOOD
Firebox, wast
Firebox, aast
tr/sn fiet*>
sr&* r/fiff
' M«at«n outlet
tube«Jein Neat
•
«
•
•
• to
•
•
•
•
•
• BMt
Hater No.
TR-201-H100
FIt-303
TZO-201
FIO-301,302
fX-1-110
-111
-114
-115
-116
-117
.-116
-lit
••120
-121
-122
-123
-124
-12S
-126
Units
•V
1000 BBLD
•*
%
1000 aau)
•F
•F
•F
•F
•F
»F
•F
. »F
«F
•F'
•F
fF
•F
•F
•F
Readings
/?30 \
12*11
I2*f
?e
*fff
1*7
?*Y
f*/*
f'ff
/en
/9*2-
Iff
*/s
-------
Parameter
Tubeskin West
to
East
Tap Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East/^^f
Ref. Heaters
South stack
below Danpers
Ref. Heaters
South Stack
above Dangers
Oonv. sect, upper
between 100/101
Oonv. sect, center
between 100/101
Oonv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
—
__
_
—
—
—
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFO x 103
psig
—
inches water
inches water
inches water
inches water
inches water
inches water
Headings
'/£>J7
/**¥
*/f
/off
/03f
/*2-V
-------
Location 5
Control Room Data Sheet
Pate f-2.-?S
lest No. 5~" "2-
Onit No.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-1000
Firebox, west
Firebox, east
}r£4ff ?t.f»J
trfAM res?/:
Heaters outlet
tubeskin West
•
•
•
•
to
•
•
•
•
•
• Bast
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
•-120 .
-121
-122
-123
-124
-125
-126
Units
•F
1000 HELD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
'F
•F
.**
•F
•F
•F
•F
•F
•F
•F
Readings
I ¥00
<7<2f-
/*,£>
2-0£
3f,2.
*S~t
IZf
V1V
W*
te$~0
/*f/
111
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection '
Section
Gas Flow to
Unit 100 x 348 '
Gas Header Press •
Draft Gages
Firebox Easty^^T
Raf. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Danpers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter Mo.
TX-1-138
139
140
141
142
143
244
248
FT-201
—
~
_
__
—
—
-.
units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD X 103
P»i«
—
inches water
inches water
inches water
inches water
inches water
inches water
Readings
y^$~
f0 32-
—
!05-$~
?*?
-------
location 5
Control Boom Data Sheet
test No.
Onit No.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
$T£AH ft**'
irfAf* rftff
' Heaters outlet
tubeskin West
•
•
M
H
to
m
m
.-
•
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-1-110
-111
*F3
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
>F
•F
•F
•p
•F
••F
•F
•F
•F
•F
Readings
W.00
121
<*/
121
f-3
?/7
tzfz-
l2'/f
21 K
frz-
1*1
/0/1
10 2-?
1072-
tef?
(etl
nr
— -
V*
IFf
/0fff
,?22-
I* 3?
1 6 1
-------
Parameter
Tubeskih West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox £ast/<£,£j^'
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
—
_
_
—
—
~
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
Inches water
inches water
inches water
inches water
inches water
inches water
Headings
>^-2 f
/0£V
.
/T3
/e>32-
/6*t
yet
.)*/1
2~*
ll.r
—
-.43/-.C3
-, S3
~,i7
<~-!7
~r?7
-~97
162
-------
. location 5
Control Room Data Sheet
Date
Test NO. 5" -3
Unit No.
Parameter
•Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-1000
Firebox, west
Firebox, east
SrttM Ft-**/
fr&rt TfrtP.
" Heaters outlet
.tubeskin West
*
•
•
•
to
•
•
•
•
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FlC-301,302
TI-1-110
-111
-**3
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•p
•F
•F
•F
»F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
to-. 30
121
ff
12
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox Easty^j,
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Danpers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
Ti-l-138
139
140
141
142
143
244
248
FT-201
—
.
__
_
—
~
—
Units
•F
•F
°F
•F
•F
•F
•F
PF
SCFD x 103
psig
—
Inches water
inches water
inches water
inches water
inches water
inches water
Readings
}<><**
fG7t
/0?2~
/
-------
Location 5
Control Room Data Sheet
Date
MO. 5^-
Unit Ho.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
B-100B, E-100D
Firebox, west
Firebox, east
ST//IM ftf*
*f/jn rfif
' Heaters outlet
tubeskin West
«
•
•
•
to
•
«
*
•
•
* Bast
Meter Ho.
TR-201-H100
FR-303
TIC-201
FIC-301,302
H-l-110
-111
•114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
. . • •p.--. -
•F
»F
•F
• .**
•F
•F
•F
•F
•F
•F
•F
Readina*:
/J''00
fte
w
730
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Reader Press.
Draft Gages
Firebox East/j^^^"
Ref. Heaters
South stack
below Dampers
Ref. Beaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
—
_
„
—
—
•—
Units
•F
•F
•F
•F
°F
•F
•f
PF
SCFD X 103
psig
—
inches water
inches water
inches water
inches water
inches water
inches water
Readings
/^/-2
/*ft
—
Mf
/**¥
/0?6
. yss
/23-/
2.?
//.7
—
-.S
-------
Location 5
Control Room Data Sheet
Date
Vest No.
Unit No.
Parameter
Time
H-100 Temperature
Jtef ormer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
*/2vf/7 fl0&
trfsff rfrtt
Heaters outlet
tubeskin West
•
•
•
•
to
•
•
.•
"
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
TI-'l-llO
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
•125
-126
Quits
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
*F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
//"^
12?
ff
;f*f
f.2*~
7/7
/2 ft
Ws
.31
.V*~i
<9*f
/S05'
/*??
/*>*£>
/e>?y
/**>£
ffe
—
f>^
fry
tff*£~
J0/*
1*37
1 67
-------
Parameter
Tubeskih Nest
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East/£,^y^-
Ref. Beaters
South stack
below Dampers
Ref. Beaters
South Stack
above Dangers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
F1V-201
~
—
...
_
—
—
—
units
•f
•F
•F
•F
•F
•F
•F
PF
SCFD X 103
psig
—
Inches water
inches water
inches water
inches water
inches water
inches water
Headings
W38
/0$~f
—
/^$"/
A?-2 "7
/**2y
i*r
:/z/t
3.,?
//.s-
—
-.(/-. S3
-.**
~.r
-.2.
~,5L
-,/f
168
-------
Date
Vest No.
Location 5
Control Room Data Sheet
Unit No.
Parameter
fine
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, £-1000
Firebox, west
Firebox, east
trSArt ft.""
sr/** Tfrtt
' Beaters outlet
tubeskin Nest
•
•
•
•
to
•
•
•
•
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
Ti-i-iio
-111
-114
-115
-116
-117
.-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
**
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
»F
•F
. «F
•F
•F
•F
•F
•F
•F
•F
Readings
a - if
12 7
/?-
-------
Parameter
Tubeskin West
to
East
lop Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gag Header Press.
Draft Gages
Firebox East •/£«* r
Kef. Heaters
South stack
below Danpers
Kef. Beaters
South Stack
above Daopers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Oonv. sect, lower
between 100/101
Meter Mo.
TI-1-138
139
140
141
142
143
244
248
F3V201
— •
~
„.
__
—
—
—
Units
•F
•F
•F
•F
•F
°F
•F
W
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
inches water
Readings
/*??
/tf?
/^5~/
/^i 7
/*/3
V0f~
/3-07
2- r
/*.r
~
-,< -/?
--?
-.2-
-. 2~
-,11
\ 70
-------
Location 5
Control Room Data Sheet
Date
«BBt HO.
Unit Ho.
Parameter
Tine
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
S7£*n W
frgttt rfrff
' Heaters outlet
tubeskin west
•
•
•
•
to
*
•
* -
•
•
• Cut
Meter No.
TR-201-H100
FR-303
TIC-201
FIC-301,302
Ti-i-iio
-111
2f3
-114
-115
-116
-117
-118
-119
'-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
*^/t */**
'/*
•F
•F
•F
*F
•F
.*'
•F
•F
•F
•F
•F
•F
•F
Readings
/3'-*-0
}»
te/f
/*£1
l*?3-
11 f
??z
—
1/3-
1S-I
{*/$
.111
1*/f
1 71
-------
Parameter
Tubeskin West
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox BMt/fc«r
Fef. Heaters
South stack
below Dampers
. Kef. Heaters
South Stack
above Dampers
Conv. sect, upper •
between 100/101
Conv. sect, center
between 100/101
Oonv. sect, lower
between 100/101
Meter No.
TI-1-138
139
140
141
142
143
244
248
FT-201
—
—
__
__
—
—
—
Units
•F
•F
•F
•F
°F
•F
•F
PF
SCFD x 103
psig
~
inches water
inches water
inches water
inches water
inches water
inches water
Readings
/*/?
/0fl
//?S
*.i
tf.S
—
-.W/-./S-
*-.*3
-- f
O
. 0
o
1 72
-------
Location 5
Control Room Data Sheet
Data
Vest Mo.
Unit No.
Parameter
tine
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack 02
Reformer Charge
E-100B, E-100D
Firebox r west
Firebox, east
SW1 ?(•*«/
srfAf* T£M?
' Heaters outlet
tubeskin West
• .
•
•
•
to
•
•
•
•
•
• Bast
Meter No.
TR-201-H100
FR-303
TOC-201
FIC-301,302
H-l-110
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
•123
-124
-125
-126
units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
*F
•F
»F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
!3 '-5~£>
yeff
/*f3L
/*?s
/*&#
11*
• —
f*0
Iff
. w
J0ffg
*f*51
1 73
-------
Parameter
Tubeskih Heat
to
East
Top Convection
South end
Bottom Convection
Section
Gas Flow to
Unit 100 x 348
Gas Header Press.
Draft Gages
Firebox East/£,^f
Kef. Heaters
South stack
below Dampers
Ref. Heaters
South Stack
above Dampers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. sect, lower
between 100/101
Meter Mo.
TI-1-138
139
140
141
142
143
244
248
F1V201
—
—
__
__
—
—
—
Units
•F
•F
•F
•F
•F
•F
•F
SF
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
inches water
Headings
\/e*'i
/T3
/
-------
Location 5
Control Room Data Sheet
HO.
Unit Ho.
Parameter
Time
H-100 Temperature
Reformer Charge
H-100 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
trfAM ft.**/
srfjfi r£l?.
Heaters outlet
tubeskin West
M
•
•
•
to
•
II
•
II
•
• East
Meter No.
TR-201-H100
FR-303
TIC-201
FIG- 301, 302
TI-1-110
-111
-114
-115
-116
-117
-118
-119
•-120
-121
-122
-123
-124
-125
-126
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
•F
•F
•F
**
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/f-/0
?*/
S3-
32?
S,94~
f/r
/3^i
/&#g
tw
y$~/
7*7
-------
Parameter
Vubeskin West
to
East
Top Convection
South end
Bottom Convection '
Section
Gas Flow too
Unit 100 x 348
Gat Header Press.
Draft Gages
Firebox Sast/£^y/
Ref. Heaters
South stack
below Dangers
Kef. Beaters
South Stack
above Daapers
Conv. sect, upper
between 100/101
Conv. sect, center
between 100/101
Conv. seet. lower
between 100/101
Mater Mo.
TI-1-138
139
140
141
142
143
244
24S
FT-201
—
—
•mm
~.
—
—
-
Units
•F
•F
•F
•F
•F
•F
•F
PF
SCFO x 103
p»ig
._
inches water
inches water
inches water
inches water
inches water
inches water
Headings
103- 2-
/03~*-
/^/^
A?.*/
/&/3
*iSl
/03Z
2-
-------
LOCATION 5
GAS CHROMATOGRAPHIC ANALYSIS
_d=?
5/t~£,
Oxygen 0.03 0.02 0.06
Nitrogen 2.07 1.11 1.40
(by difference)
Carbon Dioxide 0.31 1.02 0.67
Carbon Monoxide 0.11 0.071 0.10
Hydrogen 8.70 7.62 10.03
Methane 47.18 56.76 46.78
(by difference)
Ethane 7.2 8 6.63 8.12
Ethylene 0.06 0.05 0.06
Total C3 17.6 14.9 18.0
Total C4 ^14.5 10.3 12.9
Total C5 1.93 1.34 1.53
Total C6 0.23 0.18 0.35
1645 1495 1606
Heating Value
(BTU dry/SCF)
1 77
-------
PROCESS HEATER DESIGN DATA
Location No. 5
Unit No,
Unit Description
>f £.
A
Installation Date
Burner Description
Test Fuel
64?
Fuel Temp, at Burner (dF)
Primary Air Temp. (°F)
Heater Rating
Comments:
1 78
-------
Test No..
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No..
Engr.
Fuel
Capacity
Unit Type
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 03 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%) ••• "
22.
23.
24.
25.
26.
27.
28.
29.
30.
5X2 -/
f- y-T*
lt>30
7.1
£S
^t
6*1
0
71
/#
#
/
^
f?
£7
0
7
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date /"" y~?f Location
Test No.,
Engr.
Fuel £4$ Capacity
Unit Type
Burner Type
1. Test No.
2. Date
3. Time , .
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% Oa (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
j-^2.
6~f~7£
1300
2.-
vi
i2
2.
?*
//-
f
1
2
€7
i2
iff
2
f£°
7
e
\
2~
•76
?i
21'1#
5~2-
5~/3-2
6'f-7e
/330
<2*
re
if
2
(2.
/2
*
I
2.
f
ii
i7
2.
£1
,0
#
\
2.
7£
**f
21.1*
5*2.
f/2'2
£~t-7£
W00
2.
Y/
ti
2
£2
'2
g
\
?„
1
y$~
13
2-
£0
.0
2
\
3*
7*f
£5~
21-f?
£3
f/2-3
£~'/'7£
/1 50
.
1.
r*t
ft
(
7/
/#.
10
(
^
1
£J
£2
/
7£
g
II
/
^L
7f
£?
21,17
&£
••'
-
''•
Correction to 3% 02 should not be performed if
the value is measured on a wet
Data Sheet 6002-2
-------
Test Mo..
Unit Mo.
I
Date
Fuel
MOBILE LABORATORY DATA
£/7/7£ Location
Test No..
Engr.
Capacity
Unit Type MQC/Sf #£472A. Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. N09 (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (eF/°C)
19. Dew Point Temp.
/{
e>
f~
5-
1*
gy
I
J0f
*?
//
e>
f
7V
62
21.11
ff
f/2-f
C-7-7*
1200
10W
f
77
77
O
tf
/*
t*
2-
r
7
;/
f7
37
^
17
,0
//
SL
s
1
£i
2-1*15'
5~3
•
fte-r
f- 7-7 f
1230
L0US
4T,0
71 W
7t *Z
/ ;
*7 1$
-------
Test No.,
Unit No.
Date
Fuel
MOBILE LABORATORY DATA
6/7/76 Location
5"
Test No.
Engr.
Capacity
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atroos. Temp. (°F/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
-T/2-/
6-7-7S
'f
W ' k*%
),
Ft
ff
5
62
12
IS
1
-------
Location 5
Control Room Data Sheet
Date
Test Mo.
Unit Mo.
.Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
. -
to
"
* east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter Ho.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units •
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f /hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/****
32-Z
/2^0
32-?
t-iref
S/t
/y*j
/?y.2.
10.2-
y*~l
-------
Parameter
Gas Flow to
..Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Beaters
South stack
below Dampers
Kef. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower.
between 101/102
Mater No.
F1V201
„-
—
»
_
—
Units
SCFD x 103
P«i9
—
inches water
inches water
inches water
inches water
inches water
Readings
W
-------
Location 5
Control Boom Data Sheet
Date
Test No.
Unit No.
&
Parameter
Tine
B-102 Temperature
Reformer Charge
B-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
•
" to
•
* east '
Reformer Beaters
north/south stack
*
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
PR-303
TIC-203
FIC-301,302
TI-1-144
-145
PR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Unite .
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
i/hr x 103
•F
•F
- «F
•F
•F •
•F
•F
•F
•F
•F
Readings
//;**
-------
Parameter
Gas Flow to
"•Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Beaters
South stack
below Dampers
Ref. Beaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FT-201
—
—
_
_
_
—
Units
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2-S
1..r
—
~.Sf /-.Sf
-.Sf
~.n
-,*ir
~.*s~
1 86
-------
Date
Test Mo.
Location 5
Control Room Data Sheet
Unit No.
.parameter
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack 0
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
•
* east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter Mo.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units •
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
i/hr x 103
•F
•F
•F
•F
•F •
•F
*F
•F
•F
•F
Headings
//-' J *'
72-Z
12-
?2f
F-0
4/t
/'/*2-
/?*&
?5~
W?/ f^Z.
V>0s
f/77
1 87
-------
Parameter
JZas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Kef. Beaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FT-201
—
—
— ^
_ i
—
~
Units
SCFD-x 103
psig
~
inches water
inches water
inches water
inches water
inches water '
Readings
2'* .
i .
—
,s-> /-.r?
•^-,/r
~-*~ .
-^2-3
--3-i
1 88
-------
Location 5
Control Room Data Sheet
Test Ho.
Unit No.
.Parameter
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack 02
Reformer Charge
E-100B, Z-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
TUbeskin west
•
" to
- •
* east '
Reformer Beaters
north/south stack
x Top Convection
north center
Bottom convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
7-149
-150
-151
-152
-153
243/242
245
250
Units •
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F .
•F
•F . '
•F
•F
•F
•F
•F
Readings
/3Z00
73-f
'-2-
-------
Parameter
Gas Flow to
"unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Kef. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No. .
FT-201
—
—
WMm
— —
—
—
units
SCFD'X 10
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2r
-------
Location 5
Control Room Data Sheet
Date
Test No.
Unit No.
parameter
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
TubesJcin west
•
" to
•
• east
Reformer Heaters
north/south stack
Wop Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units .
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
i/hr x 103
•F
•F
•F
•F
•F •
•F
•F
•F
•F
«F
Readings
/-2'3jT
^^
/y
7S
-------
Parana tar
Gas Flow to
* Unit 100 x 197
Gas Header Praia.
Draft Gagas
Firebox aaat/west
Kef. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Mater No.
FT-201
—
—
— —
MB[
~
~
Unit*
SCPD-x 103
psig
—
inches water
inches water
$
inches water
inches water
inches water
Readings
z.rf*
//,0
—
~.*r /-.
-------
Location 5
Control Room Data Sheet
Test Mo.
-.2.
Unit No.
' Parameter
Time
B-102 Temperature
Reformer Charge
B-102 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
•
• to
•
* east
Rflfonnsr Heaters
north/south stack
•
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-i-144
-145
FR-505
-253
-148
• -149
-150
-151
-152
-153
243/242
• 245
250
units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
"F
•F
•F
•F
•F
•F
Readings
/Ji 00
<73'S?
/I
-------
Parameter
Gaa Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Kef. Beaters
South stack
below Dampers
Ref. Beaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter Mo.
FT-201
—
' —
•**»
^^
__
~
Units
SCF0-X 103
psig
'
inches water
inches water
inches water
inches water
inches water
Readings
2~?5~
//
~
-, /5- /-.S5~
--//
~-.f~
-~,2-/
~-*l
194
-------
Locution 5
Control Room Data Sheet
Date
Test No.
Unit No.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
• Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
•
" to
' m
" east
Reformer Heaters
north/south stack
Top Convection.
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
PIC-301,302
Tl-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
i/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
13-30
1*1
/y
1*1.
1-2L
7/7
ivy*
tjrs
«#'?
VFf
V*1
f0£0
/o?-?
?rt
1*1
/tot
w/ *>j-
fo?
/irr
195
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Kef. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FT-201
—
—
— —
^IL-
—
—
Units
SCFD x 103
psig
~
tnches water
inches water
inches water
inches water
inches water
Readings
^/•-T
//
—
-~Sf / '-.*?
~- //
-r$~
-- 2- /
--2I
1 96
-------
Location 5
Control Room Data Sheet
No.
Unit No.
Parana tar
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet leap
Stack 02
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
•
" to
•
• ;;,*.«asV
Reformer Beaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter Mo.
TR-203-H102
FR-303
TIC-203
PIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/24?
245
250
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
I Ar x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/*}**
124
/y
f-2?
1. 0
f/<
tViZL
/*f?~
•il.f
V5"/
f^f
/^y
/^^ ^
f ?*/
^fi
/*/2-
*(ojl/
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Hef . Heaters
South stack
below Dampers
Hef. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter Ho.
FT-201
~
—
•*
— ^
__
—
Units
SCFD X 103
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2^ Z5~
//
—
--SS- / ~.S5~
— ^X-2- .
' 5~
-.^^ ^
--^/
1 98
-------
location 5
Control Room Data Sheet
Date
Test No.
Unit No.
Parameter
Tine
B-102 Temperature
Reformer Charge
B-102 Outlet Temp
Stack 0
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
•
• east
Reformer Beaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TXC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
//-'.?*
f-2f
. 12-
1*4
f-f
s/s
/5?f-
/$I1
*f£>,2
•fr*
4*1
/'fr
/etl
1t*
ft*
*
fat
fir?
199
-------
Parana ter
Gas flow to
Unit 100 x 197
GUI Header Press,
Draft Gages
Firebox east/west
Raf. Heatera
South atack
balow Danpera
Raf. Heatera
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Hater No.
FT-201
—
—
^^
^^
—
~
Units
SCFD-x 103
psig
',-.
inches water
inches water
inches water
inches water
inches water
Headings
2,7
1-*
—
-.<1 /-.*r
-,/r
-.**
~.&3-
-.23
200
-------
Location 5
Control Room Data Sheet
Date
Test No.
Unit No.
-2-
-Parameter
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
«
" to
•
* east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
Tl-1-144
-145
PR-505
-253
-148
-149
-150
-151
-152
-153
243/24?
245
250
units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/0f00
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Conv. sect, upper
between 101/102
Conv. sect, lower
between 101/102
Meter No.
FT-201
—
—
H
^^
—
—
Units
SCFD x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2-£
*' 7
—
-- 11
— ^ /
-'*!
202
-------
Location 5
Control Room Data Sheet
Date
Test NO.
Unit No.
Parameter
Tine
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack 0
Beformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
•
• east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units
•F
1000 BBLD
•F
%
1000 BBLD
. »F •
•F
fAr x 103
•F
•F
•F
**
•F
•F
•F
•F
•F
•F
Readings
/f'~00
12- -7
/0
327
7,0
r/r
/3f
-------
. Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FT-201
—
—
..
_
—
—
units
SCFD-x 103
psig
—
inches water
' inches water
inches water '
inches water
inches water
Headings
-z-y
6,6
. —
-£? /-.*!
r> /-2L
-% -^/
-.-2.2.-
~, 2~(
204
-------
Location 5
Control Doom Data Sheet
Date
Test No.
Unit Mo.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O2
Hie former Charge
E-100B, E-100D
Firebox, west
. Firebox, . east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
M
" east
Rafortoer Beaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter Ho.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
//:?*
1/
/^/^
1tt
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Conv. sect, lower
between 101/102
Meter No.
FT-201
__
—
— —
j_m.
—
—
Units
SCFD x 103
psig
--
inches water
inches water
inches water
inches water
inches water
Readings
-j^rj.-i
f,*f
—
->*"? /-,«r5~
-,//
-.*-
-,15-'
~-t -7
206
-------
Location 5
Control Room Data Sheet
Date
Test No.
Unit No.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack 0
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
•
* east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units
•F
1000 BBLD
•F
t
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
J2~ee>
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FP-201
—
—
^mm
— —
•• — •
__
Onits
SCFD x 103
psig
.—
inches water
inches water
inches water
inches water
inches water
Headings
-2.V
7-0
—
-,^'/-v*2-
^•/^
-^
' —~&l
~r3-')
208
-------
Location 5
Control Room Data Sheet
Date
£-7-7*
Test No.
Unit No.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam .Flow
Steam Temp.
Heater outlet
Tubeskin west
•
" to
•
• east
Reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TR-203-H102
FK-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153.
243/242
245
250
Units .
' ' »F
1000 BBID
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
^F
•F
•F
•F
•F
Readings •
./2:30 "
*J 7
S0
7J27 ' •
•7-*1
*r/r
wri •
/&?0
j^y
^^?
^^••7
/*35~
/0o3 .
fst
1S* •
?**".:
?'*/?/*
3^f .
/If*
2-09
-------
Parameter
Gas Flow to
* Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Beaters
South stack
•above Dampers
Conv. sect, upper
between 101/102
Conv. sect, lower
between 101/102
Meter No.
FT-201
—
—
^ ^
Lr
—
—
Units
SCFD-x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2-1
7^0
—
--iff /-~*l
•-> //
~,5~
-.^ /
-, 3-1
2 1 0
-------
Location 5
Control Room Data Sheet
Date
£-7-7*
Test No.
Unit No.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Beater outlet
Tubeskin west
•
" to
•
* east
reformer Heaters
north/south stack
Top Convection
north center
Bottom Convection
Section
Meter No.
TO-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units .
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
i/hr x 103
•F
•P.
•F
•F
•F
•F
•F
•F
•F
•F
Readings
Af'tfT
*?3#
n
-------
Parameter
Gas Flow to
Unit 100 x 197
Meter No.
FT-201
Units
SCPD X 10
Headings
Gas Header Press.
psig
Draft Gages
Firebox east/west
inches water
/ -.
Jtef. Beaters
South stack
below Dampers
inches water
Ref. Beaters
South stack
above Dampers
inches water
Conv. sect, upper
between 101/102
inches water
Conv. sect, lower
between 101/102
inches water
2 1 2
-------
Location 5
Control Room Data Sheet
Date
Test NO. ?/2 ~ 7
Unit No.
Parameter
Time
H-102 Temperature
Reformer Charge
H-102 Outlet Temp
Stack O2
Reformer Charge
E-100B, E-100D
Firebox, west
Firebox, east
Steam Flow
Steam Temp.
Heater outlet
Tubeskin west
"
• to
"
• east
Reformer Beaters
north/south stack
Top Convection
north center'
Bottom Convection
Section
Meter No.
TR-203-H102
FR-303
TIC-203
FIC-301,302
TI-1-144
-145
FR-505
-253
-148
-149
-150
-151
-152
-153
243/242
245
250
Units
•F
1000 BBLD
•F
%
1000 BBLD
•F
•F
f/hr x 103
•F
•F
•F
•F
•F
•F
•F
•F
•F
•F
Readings
/ */ Z^t?
rf f~ 3 0
/y
*??0
?'5~
7/7
tFi
/030
370
^
f*7
/ f ^r £ *
/ 1 & &
21 3
-------
Parameter
Gas Flow to
Unit 100 x 197
Gas Header Press.
Draft Gages
Firebox east/west
Ref. Heaters
South stack
below Dampers
Ref. Heaters
South stack
above Dampers
Oonv. sect, upper
between 101/102
Oonv. sect, lower
between 101/102
Meter No.
FT-201
•
—
—
»
^a|
—
—
units
SCFD-x 103
psig
—
inches water
inches water
inches water
inches water
inches water
Readings
2*15-
//.*
—
-,f? /-,fz
-.1
-. n
^,2-
-, 2-
2 14
-------
LOCATION 5
GAS CHROMATOGRAPHIC ANALYSIS
Oxygen
Nitrogen
(by difference)
. Carbon Dioxide 1.23
Carbon Monoxide 0.092
Hydrogen 7.40
Methane 53.46
(by difference)
Ethane 7.07
Ethylene 0.05
Total C3 16.2
Total C4 11.6
Total C5 1.42
Total C6 0.28
1552
Heating Value
(BTU dry/SCF)
2 1 5
-------
ALUMINUM MELTING FURNACE
Location No.
-------
Test No.
Unit No.
Unit Type /
£
1
1
*f$
1 $
2-
/£>4
J/
r*f
6-1
IV tf
//'0
_«
—
—
ft>
7,
f
&
0
—
—
—
(t/tf
%
f
o
&
^3"
73
3
-------
Test No._
Unit No.
Unit Type
MOBILE LABORATORY DATA
Date
* ~-
Fuel
Mr
Location
Test No._
Engr.
Capacity tf-J
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (pom) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
6-2
/01/0
7^ /<
5-.
75~
72
2-
$7
/#.
7
£>
I
f
$7
??
2-
I0/
$%?
g
0
1
&5~
7*
it
-
£-3-
///#
3'-
##
#7
I
/oi
//'
1
/
2-
r?
f/
-------
MOBILE LABORATORY DATA Test No.
Test No. «
Unit No.
Unit Type /7/V
Date 0~20~7{ Location
Fuel &2- 011- Capacity
& Engr.
*f3 T&M 5
- 7~/fiJ& f&/?/dfr££ Burner Type flJ0fl Ttf tfff^fi t C d tf
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
/'/
/f?+
/f
^^*
*-~
—"•••
65
6,
£
^^••^
«*••»
v/
••*
•• i"*
142.
if
/t
H^B»
m^tm,
f-2
}3/5~
7-<
126
trff £T^
t
/ % ^F
* *r fy
//>*
Q
0
13-0
35-
///
Iff
1
/$2-
r
#
^^
t jf*&
t *? V
#3
7f
yq
6-7
12* S
^
Ml
12*
I.
W3
//'
f
0
)}2-
1
170
te#
/
it?
7
%
G>
If*
$1
7?
17
£-3
/?r 172
fe1! /?£
/ 1
/75 W5
/2*?
$ *?
0 0
HI )57
$3
73-
f*i
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis, 219
Data Sheet 6002-2
-------
Date:
Date Taken By:
OPERATING DATA
Location 6
Test:
Test 80.:
Time
Gas Flow Rate x 4000
(SCFH)
Integrated Gas Flow
100 (SCH)
South Side Gas Pressure
(in. H20)
Oil Flow Rate (GPM)
Integrated Oil Flow
(gallons)
Oil Pressure at Burner
(PSIG)
Furnace Temperature (°F)
Flue Gas Temperature
CP)
Load (Ibs)
n vr
T
M A,
two
i2-'WT
1.7
fJ.J-
-------
Datet
Date Taken Byi
OPERATING DATA
location 6
Tests
Test Mo.»
Tine
Gas Flow Rate x 4000
(SCFH)
Integrated Gas Flow
100 (SCH)
South Side Gas Pressure
(in. H2o;
Oil Flow Rate (GPM)
Integrated Oil Flow
(gallons)
Oil Pressure at Burner
(PSX6)
Furnace Temperature (°F)
Flue Gas Temperature
(•F)
toad (Urn)
10'-*?
1,2
672?'*
1*1
0.4-
„
vrs*7
ir-'i
tri
€ 72&»
I-*
*,4,
•fff*?
II--30
t,/r
67zetl
1'!
. t$f*
7
12*3**
7'*
j7*ftZ
f. *
W*0
••^
irfr?
-
^
22 1
-------
OPERATING DATA
Location 6
Date: £~ ?0 ~ ?£ fleBtj 0
Date Taken By:
Tine
Gas Flow Rate x 4000
(SCFH)
Integrated Gas Flow
100 (SCH)
South Side Gas Pressure
(in. H20)
Oil Flow Rate (GPM)
Integrated Oil Flow
(gallons)
Oil Pressure at Burner
(PSIG)
Furnace Temperature (*F)
Fte$e tlti" '*> Fto* 64$
Flue Gas Temperature
(*F)
Load (Ibs)
tl'^f
"-. 7
l*tft>
»,A.
Test
//.V5-
"if
A/o
H-.2V
»«;
a*r
I7f5
?7W
222
-------
GASEOUS FUEL ANALYSIS
Test No
Test No
Date
Location
Engr
Unit No.
Fuel
Fuel Sample No
Fuel Sample Point
Fuel Analysis by
Gas
CH4
"
Methane
Ethane
Propane
Butane
Pentane
Ethylene
Propylene
Butylene
Pentylene
Acetylene
Benzene
Oxygen
Nitrogen
Garb. Diox
Carb. Monox
Hydrogen
% CF air Btu(HHV)
Volume CF fuel
54.52 x 0.0955
4.2k x 0.1671
x 0.2387
CF CO2
CF H20 CF_Prod Ib Prod
fe.Q2Sx 0.3103
0.3819
x 0.1432
x 0.2148
Oxfe*? x 0.2869
x 0.3580
x 0.1193
.x 0.3580
"x -0.0477
O.VJ
_x 0.0239
~x 0.0239
CF fuel
9.94
17.51
25.19
33.21
41.11
15.80
23.33
31.23
39.16
14.57
38.48
3.15
3.18
CF fuel
0.01
0.02
0.03
0.04
0.05
0.02
0.03
0.04
0.05
0.02
0.06
I
0.01
0.01
CF fuel
0.02
0.03
0.04
0.05
0.06
0.02 :
0.03
0.04 \
0.05
0.01
0.03
0.01
CF fuel
0.1055
0.1821
0.2587
0.3353
0.4119
0.1532
0.2298
0.3068
0.3830
0.1343
0.3730
-0.0377
0.01
0.01
0.0289
0.0289
CF fuel
0.000416
0.000786
0.001171
0.001548
0.001864
0.000726
0.001087
0.001449
0.001813
0.000682
0.002017
0.000828
0.000728
0.001145
0.000724
0.0000522
Total
Theoretical Air:
SCF air _ CF air
/bQ.
,6 / Btu(HHV)
^02.4
1.044. 2.037-
10& Btu CF fuel
WSCF Prod CF Prod
u / CF fuel " —-^
6 /Btu (HHV) f.0^tw|l
10& Btu CF fuel / CF fuel
CF HoO _„ / CF Prod \a& ""7**
* '^•i-fai.uiu £3, fuel A xww^r cp fuel _--: _
DSCF Prod WSCF prod _, (100 - % Moisture) r ^
106 Btu ~" 10b Btu
% C02, tky - ^ fuel x
331.5xl06
" ~MW X (DSCF/106 Btu)
K' -K/430
lb/106 Btu - (ppm @ 3* 0
ng/J » (ppm @ 3% 02)/K'
100 -**=
100 /F* Pr°d ^ -H2° V
100 / VCF fuel CF fuel>T -
MW
NOx 46
CO 28
>9)A
* HC 16
SOx 64
223
— 29.92 in. Hg.
r\.4^ ft
D Wet SCF Prod/10 Btu
,\l\4 Dry SCF/106 Btu
U'S>"7 % CO,., dry
K for K1 for
lb/106 Btu ng/J
\. i^Sx.io"2' .ste»&
Data Sheet 6002-6 (Rev. 1)
-------
LOCATION 6
FUEL OIL ANALYSIS
Carbon, % 86.40
Hydrogen, % 13.12
Nitrogen, % 0.040
Sulfur, * 0.25
Ash, * 0.062
Oxygen (by difference), % 0.13
API Gravity at 60*F 34.5
Gross Heat of Combustion, BTU/lb 19,490
Net Heat of Combustion, BTU/lb 18,290
224
-------
PETROLEUM PROCESS HEATER
Location No. ( Unit No.
Unit Description
Installation Date
Heater Rating _ \&S Wl\0 ( 52 .&> ^ lQb
Burner Description _ OoU>4 ZlQkC
Test Fuel Combinations
KEF I
Fuel Temp, at Burner (°F) Amth*
-------
Test No.
Unit No.
Unit
Date
MOBILE LABORATORY DATA
Location _
Test No.
Engr. tf.
Capacity
Burner Type 70^
/*//.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate C^-'Ct, P/tf
6. Flue Diam. or Size, ft
7. Probe Position '
8. Oxygen (%)
9. NOx (hot) read/3% ©2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (eF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/t-f
7'tf '-76
013e
/(/A
f,25-x/0s
f'f
"CD
/f&£A
7.V
67
{7>
•&-
7?
/0.
?
25**
&-
tit>r .
$~
&&
&&
&~
f& t
2*
n
*$f
<&-
r/ftftJ
MS-
7$.0
3*,0g$~
76.0
7//-I
7-!3~?(
/G>y$-
/.32
7,1*
/£
££
•&-
71
7,
f
* /0
•&-
q I
a 1
t^1
/^f
7
tl
/t-l
0
#<,0
7g,0
?),0&0
?(,f>
7//-f
7~/j~7£
/1 30
#.20
/£
71
72
2-
U
f.
/
#
yd*
7
/^
17
3
//6
0
?
/I
5"1
fS'#
77,0
30,01
68,0
7/t-/
7-tZ'76
}?? o
r,0t
7,
£&
^ 0
-e-
72
7.
£
7
-&-
7
ft
fl
•&-
17
1
g
/2~
&
f£,0
7f,0
20.0$
6%,O
7//-1
7-tf'7t
/FG5~
«»^
•^^
f.0
*"^> *
-_
*J^
"7 & ^t
f£> £2
S
-------
Test No.yV/"/
Unit No. I
MOBILE LABORATORY DATA
Date 7-/3~7£ Location
7
Test No.
Engr.^
Fuel g/
S*
7
F
•&
7^f
7?
/ '
1*
•
^^~
*^
"
*Correction to 3% O_ should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date 7-/ef-7f Location 7_
Test No.
Engr
Capacity £2. X
Onit Type
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% QI (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/1-1
7-/i
0335-
f,3f
5~-6"0P
££Vf£#
7,
(US
to
\ 25
72.5
?,
u
1^
&
• -
j
10.5
71,$
in
1ST
&
$-
13
&
#?
75~
30
-------
Test No
Unit No.
. 7f f~
Obit Type
MOBILE LABORATORY DATA
Date 7~lf-7( Location _ 7
Capacity
Burner Type
Test No.
Engr
//W -
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate — I* ' f"f 3/h r ~"~
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O5 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. N09 (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. AtlWS. Temp. CF/'C)
19. Dew Point Temp. (eF/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/1-3
7*}?
0*100
- f,,22
f'f'0,0.
e&r§*
(,
£*
fi
/
7?
f.
5"
f
^
^**»
1
77
7£
1
It
ffi
g
/i
$
MMBM
f$"
77
30.3-1
7f
7-t?
0130
_
#,20
f'("0,P.
cfvrf/z
W f
tt
43
\
7f
r.
£
-------
Test No._
Unit No.
Unit Type
MOBILE LABORATORY DATA
Date 7-/?-7f Location 7
tf£*T£ A
Capacity -
Burner Type
Test No.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate /# f"ff/hf
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO5 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Xtiros. Temp. (°F/°C)
19. Dew Point Temp. (?F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7//-1
?'/$'
Jt?f
(,63
$'(**.!>.
££*>r£fi
7-
fj.
Si
/
7?
f.
6
f
2.
0
$0
7*
/
1*
2-
z
6
J
#7
73
30.21
7*
7//-J
7-/5~~
Jf3P
—
g,0f
f't*'*
cg^rfz
7-
6**
62
J
$0
Q *•
3
3
/
2-
?sr
&l
i
)0f
2
f
i
/
ft
fff
30.2-3.
72.
-
-
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis. u,
230 I
^ ^
v^ ^ ^t
\c\ ^ ^
Data Sheet 6002-2
-------
Test No
Unit No.
MOBILE LABORATORY DATA
. X/ /~3 Date 7-/j~7f Location
Onit Type
Kff.
Test No.
Engr
Fuel /f//f £/iS Capacity
2 * 1 1>
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5; Process Rate fi^-rrr
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% Q2_(ppm)*
11. NO? (hot) read/3% 02- (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atncs. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/f~3
7-/1-76
IFZe
f.20
?'£"*,£
ffWf£
-?r
62.
6]
1
7f
2.
91
f0
1
3$
#,0
i
4
Ft
j$~
#
70*
—
ft
7%
J0-/3
7o
7/S-3
7-ff" 7f
(£00
•
#,20
^*w ff£
$$ iff.
7-t
/-2-
62-
•&-
77
&,
f
1
2,^
f
&t
*)
&-
/00
y .
f
•f
32-
r?
r*
30, (j
71
*
•
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
23 1
I
-------
EXPLANATION OP COMPUTER PRINTOUT OP OPERATING DATA
Location 7'
Unit 1
TO13 Product Temperature in S.H. Section, °P
T014 Product Temperature in S.H. Section, °F
TO15 Product Temperature in S.H. Section, °P
T016 Product Temperature in S.H. Section, °F
T017 Product Temperature in S.H. Section, °F
T018 Product Temperature in S.H. Section, °F
T019 Product Temperature in S.H. Section, °F
T020 Product Temperature in S.H. Section, °P
T021 Stack Gas Temperature, °F
T022 Convection Section Temperature, °F
T023 Convection Section Temperature, °F
TO24 Product Temperature to Generator Section, °F
T026 Product Temperature After Superheater, °F
T246 Superheater Inlet, °F
T250 Generator Outlet, °P
T251 Drum Outlet, °P
T252 Economizer Outlet, °F
A009 % 0. (Control Room Monitor)
F022 Fuel Gas Flow, MCFH
F029 PRODUCT Feed, MCFH
F104 Feedwater Flow, GPM
232
-------
HLT
199 0
TEST DATA
THE DATE IS 7-13-1
TIME 9:29
CURRENT
LOOP READING
T013 .0000
T01 4 802 .0000
T01 5 790 .0000
T01 6 798.0000
T017 783.0000
T018 780.0000
T019 771 .0000
T020 782.0000
>T021> 608.5000
T022 ' 1239.0000
T023> 1256.0000
T024- 641 .5000
T026 790.0999
T246^ 7 68 Si 000
T250 447.5000
T251 446.0000
12 52 450.0000
A009 13.2000
h022' C"5& «1 ^ifl0^J>
F029' 8.25130
F104 108.5000
6552 STOP
1
. ! MONITOR ffr
NEXT?
976
SINCE
4 Ah
.0000
798.9986
789.2254
796.0893
782 .9984
780.1348
769 .9981
781 .31 65
607.6120
1241 .4973
1250.6330
641 .22 60
789 .3166
768.0439
447.2263
446.271 7
449.9992
12 .9549
55.8953
8.2904
108.9406
/ xn>* set
/
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig ^V/v- •• /,- ;
x7//-/
7- /2 - ?,J/4/-,
-.2-f
-~w
-,23-
S0.0
234
-------
HLT
199 0
TEST DATA
THE DATE IS 7-13-1
976
TIME ^10! 4 4 . T- / ~7 /J /
CURRENT
LOOP R EA DI NG
T013 .0000
T014 795.0000
T01 5 785.0000
T01 6 792.0000
T017 778.0000
T018 776.0000
1019 765.0000
1020 777.0000
1021 605.5000 •
1022 1223.0000
T023 1231 .0000
>,T024 642.5000
T026 784.5000
T246 764.5000
T250 447.5000
1251 446.0000
T252 450.0000
A 009 13.4000
F022 53.7000
F029 8.2199
F104 109.2000
6552 STOP
SINCE
4 AM
.0000
799 .0720
789.1459
796.0721
782 .99 80
780.1462
769.9605
781 .2570
607.4794
1240.2558
1249.6625
641 .4244
789.2130
767.7388
447.2395
44'6.2952
449.9990
13.0233
55.5294
8.2729
109.0478
YESTERDAYS
AVERAGE
.0000
797.5961
788.5128
795.2425
782 .72 1 k»
779 £635
769 .3881
780 .4604
605.961 7
1233.6420
1251 .0693
642 .8465
788.5340
764 .3461
447.5637
446.2353
449.8917
12 .9825
5 5 .2 3 69
8.1861 -
109 ,tf7tfb
MONITOR
NEXT?
HLT
235
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-I
7 - / 3 - 7S
/*'f5-
#,22- * W3 -fr-Vtr
-.3
-,2s
-.2-
/f-4
236
-------
HLT
HIT
199 0
TEST WTA
THE LATE IS 7-13
TINE 11:28
CURRENT
LOOP R EA DI NG
T013 .0000
T01 4 796.0000
T01 5 786.0000
\ T01 6 793.0000
T017 780.0000
T018 777.0000
1019 765.0000
102w 777.0000
1021 607.5000
1022 1233.0000
T023 1245.0000
1*24 637.5000
T026 786.0000
1246 764.0000
T250 447.5000
T251 446.0000
T252 450.0000
A009 13.0600
F022 54.4000
F029 8.2000
F104 108.6000
-1976
SINCE
4 AN
.0000
798.4975
788.5308
795 ,431 11
782.3977
779.5643
769 .4305
780.7641
607.3311
1238.1 625
1247.5290
641 .3148
788.5878
767.2811
447,1986
446.2988
449.9655
13.0576
55.2331
8 .2 666
109.0196
/e-st ?//-/
f
YESTERDAYS
AVERAGE
.0000
797.5961
788.5128
795.2425
782 .72 1 0
779.2635
7 69 .3 881
780.4604
605.961 7
1233.6420
1251 .0693
642 .8465
788.5340
764.3461
447.5637
446.2353
449.8917
12.9825
55.2369
8.1861
109 .0708
6552 STOP
MONITOR
NEXT?
HLT
237
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
•7/t-l
?-/J- 7S
tl~?o
f,2 */J3 ff*/Ar
-.jo
-.-ar
~rl7
/*•¥
238
-------
HLT
HLT
199 0
TEST DATA
THE DUE IS 7-13-1
976
T*st ?//_/
TIME 13t29
CURRENT
LOOP R EA DI NG
1013 .0000
T01 4 792 .0000
T015 782.0000
T01 6 789 .0000
T017 776.0000
1018 774.0000
T019 762.0000
T020 774.0000
T021 604.5000
T022 1215.0000
T023 1227.0000
T024 637.0000
T026 781.8000
T246 758.5000
T250 447.5000
T251 446.0000
T252 450.0000
A009 12.9200
F022 56.4000
F029 8.0100
F104 109.3000
SINCE
4 AM
.0000
797.2601
787.3652
794.1286
781 .1286
778.3391
7 68 .1 54 6
779.6020
606.8393
1235.4948
1244 .4680
640.5369
787.3181
766.0891
447.1036
446.2354
449 .8932
13.0586
55.2445
8.2331
109.1153
YESTERDAYS
AVERAGE
.0000
797.5961
788.5128
795.2425
782 .7210
779.2 635
769 .3881
780.4604
605.9617
1233 .6420
1251 .0693
642 .8465
788.5340
764.3461
447.5637
446.2353
449.8917
' 12.9825
5 5 £ 3 69
8.1861
109 .0708
6552 STOP
MO NI TOR
EXT?
KLT
239
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7/1-1
7.//S / 7f
/r-2-1
f.ot x 10* ff*/6r
-- Jo
-r2J
-,?3
Hi
240
-------
HLT
199 0
TEST DATA
THE IATE IS 7-13-1
HOE 15: 4
CURRENT
LJ30P READING
T013 .0000
T01 4 789 .0000
T01 5 781 .0000
T01 6 787.0000
T017 774.0000
T018 771 .0000
T019 762.0000
T020 772.0000
T021 602.0000
T022 1215.0000
-T023 1238.0000
_-T024 636.0000
T026 779.4000
1246 753.5000
T250 448.5000
1251 446.0000
T252 450.5000
A009 12.4800
F022 57 .2000
F029 8 .0000
F104 110.0000
6552 STOP
976
SINCE
4 AM
.0000
796.4509
786.6099
793.2465
780.2918
777.4738
767.1779
778.7465
606.3831
1233.3347
1243.6298
639.7698
786.3966
764.8144
447.1345
446.2254
449.9300
13.0074
55.4474
8.2067
109.1268
list 7//- /
/'
YESTERDAYS
AVERAGE
.0000
797.5961
788.5128
795.2425
782.7210
779.2635
769.3881
780 .4 604
605.9617
1233.6420
1251 .0693
642 .8465
788.5340
764.3461
447.5637
446.2353
449.8917
12 .9825
55.2369
8.1861
109 .0708
MONITOR
NEXT? .
24 1
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7/t-l
7/13 /7g
fool
f.o x ft* ^^/hr
->- 3 o
-^2- J
-./y
ii-i
242
-------
HLT
~HLT
199 0
TEST DATA
THE EATE IS 7-1-3-1976
7/7^7
n«E ij&
LOOP
T013
T01 4
T01 5
TCI 6
T017
. T019
T020
T021
T022 -
T023
T024
T02 6
1246
1250
T252
A 009
F022
F029
F104
6552 S
CURRENT
READING
.0000
789 .0000
781 .0000
787 .0000
775.0000
771 .0000
764 J0000
772 .0000
600*5000
1213 .0000
1240.0000
.635.0000
780.3000
753.5000
447.5000
446.0000
450.0000
12 .4800
55.8000
8 .0000
109 .2000
TOP
SINCE
4 AM
.0000
796.2137
786.3875
• 792 .9748
780.0397
777.2138
7 66 .9 52 6
778.5180
60 6 .1 92 5
1232.6240
1243.1455
639 .5622
786.122 6
764.4091
447.1 720
446.2263
449 .9 439
12 .9 792
55.4714
8.1979
109.1212
YESTERDAYS
AVERAGE
.0000
79 7 .59 61
788.5128
795.2425
782 .72 1 0
779 2635
769.3881
780.4604
605.9617
1233.6420
1251 .0693
642 .8465
788.5340
764 .3461
447.5637
4462353
449 .891 7
12 .9825
552369
8.1861
109 .0708
MONITOR
NEXT?
243
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-/
•7//7//V
t$*;3r hrj
fc0O x /^J ff7/jr
-.2*
-v/f
-v-2-/
/f. y
244
-------
HLT
199 9
TEST DATA
ILLEGAL MODE
HLT
199 0
TEST D&TA-
THE DATE IS 7-13-1
976
•r^s6 -ili~ i
TIME 16s0
CURRENT
LOOP READING
T013 .0000
•p~ T01 4 789.0000
L>T01 5 781 .0000
T01 6 786.0000
T017 774.0000
T018 771 .0000
1019 763.0000
T020 771 .0000
T021 620.5000
T022 1211 .0000
T023 1239 .0000
1024 637.0000
T026 779.6000
1246 751 .0000
T250 447.5000
T251 446.0000
T252 450.0000
A 029 12.3200
F022 55.7000
F829 8.0100
F104 110.1000
6552 STOP
MONI TOR
NEXT?
SINCE
4 AM
.0000
795.8710
786.1 419
792 .6629
779.7878
7~76.93~3~7
766.7458
778.2253
605.9342
1231 .7849
1242.9096
639.4553
785.8380
763.8814
447 .1855
446.2271
449 .9460
12 .9538
55.4476
8.1901
109.1057
A'. MX U1*
YESTERDAYS
AVERAGE
.0000
79 7 .59 61
788.5128
795.2425
782 .7210
7 79 £65 5
769.3881
780.4604
605.9617
12 33.. 6420
1251 .0693
642.8465
788.5340
764.3461
447 .5637
446.2353
449.8917
12 .9825
55.2369
8.1861
109.0708
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-/
7//J?/V
If06> hrjr
frOf * /fi? -f+*Ar
-,2 f
-^^ 0
- ,2 £>
/1, i
246
-------
HLT
7?
HLT
199 0
TEST DATA
THE DATE IS 7-14-1
TIME 9! 34
CIBRENT
LOOP READING
T013 .0000
T01 4 789 .0000
^T015 780.0000
T016 788.0000
T017 774.0000
101 8 771 .0000
T019 761 .0000
T020 771 .0000
B21 605.5000 '
.1422 1243.0000
T023 1249.0000
T024 630.5000
T026 779.6000
T246 7©. 5000
T250 446.5000
T251 446.0000
T252 449.0000
A009 14.3500
F022 58 .5000
F029 8.3600
F104 108.7000
976
SI NCE
4 AM
.0000
788.2711
778.61 65
785.7713
772 .7713
769 .81 65
760.1 800
770.31 64
602 .7030
1233.6794
1247.9514
632.2031
778.0667
762 .7938
447 .7491
446.4763
450.1 582
13.4417
56.5817
8 .3 62 7
108.9043
7//-c*(l*\ 0* **/•*<»
YESTERDAYS
AVERAGE
.0000
791 .8353
782 .3256
788.7628
776.1278
773 .1491
763.3778
774.2950
6042685
1226.6743
1240.5473
636.9620
781 .6318
760.4505
447.6210
446.4124
450.0845
12 .5851
54.6901
82103
1 09 .02 81
6552 STOP
MO NI TOR
NEXT?
247
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-2
7-/^-7/
1:3$~
Z.3C
-^ 3 3
--2 5~
-v /5~
^2-/
248
-------
HLT ^\
199 0
TEST EATA
'THE Q&TE IS 7-14-1
TIME 10:21
CURRENT
LOOP R EA DI NG
T013 .0000
^01 4 789 .0000
T01 5 780 .0000
_ T01 6 787 .0000
T017 774 .0000
^ T018 771 .0000
T019 760.0000
T020 771 .0000
T021 605.5000'
T022 1239.0000
T023 1257.0000
T024 630.5000
T026 779.6000
T246 769 .0000
T250 446.5000
T251 445.0000
12 52 449.0000
A009 15.0400
F022 57.0000
F029 8.2900
F104 108.4000
976
SINCE
4 AN
.0000
788.31 81
778.7580
785.8784
772 .7983
769 .8780
760.1 578
770.3579
602 .99 81
1234.2770
1248.1 562
631 .9584
778.3022
763 .4581
447.5589
446.3389
449.9790
13.5871
56.7878
8.3575
108.9917
-7//-Z^ ] #**/.'»<.
'
YESTERDAYS
AVERAGE
.0000
791 .8353
782.3256
788.7S28
776.1278
773.1491
763.3778
774.2950
604.2685
122 6.6743
1240.5473
636.9620
781 .6318
760.4505
447 .6210
446.4124
450.0845
12 .5851
54.6901
8.2103
109.0281
6552 STOP
MONITOR
NEXT?
249
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
-7//-2-
?- /y-/v
/0'2-O
f,2-f
~~3Z
~~2F
~^!t
H't
250
-------
HLT
199 0
TEST EATA
THE DATE IS 74 44
TIME .12; 0
CIRRENT
LOOP R EA DI NG
T013 .0000
T014 795.0000
Ik)l 5 774.0000
T01 6 786.0000
T017 771.0000
1318 7®. 0000
T019 757.0000
T020 768.0030
^ T021 596.5000*
T022 1252.0000
'~ T023 1277.0000
. T024 631 .0000
1 T026 778.0999
T246 753.5000
1250 446.5000
T251 446.0000
1252 450.0000
A009 1 1 .1 700-A
F022 56.100^-7*
F029 8.3299-7^
F104 .108.6000
976
SINCE
4 AN
.0000
789.21 66
778.5913
786.1 538
772.9038
769.9974
760.0283
770.4346
603.1383
1236.6833
1250.6203
631 .7320
778.5664
763.4349
447.4205
446.2018
449 .8424
13.3187
56.6686
8.3471
108.9965
/^/ ;
*
cT
YESTERDAYS
AVERAGE
.0000
791 .8353
782 .3256
788.7628
776.1278
773.1491
763.3778
774 2950
604 £ 685
1226.6743
1240.5473
636.9620
781 .6318
760.4505
447.6210
446.4124
450.0845
12 .5851
54 .6901
8 2 1 03
109 .0281
^ ««^ /
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
/W2
7~/
#,j 3
-~7*
~ 3
~.2f
2*< t
252
-------
HLT - - -
199 0
TEST EATA
THE DATE JS 7-1 4-1
TIME 13:54
CURRENT
LOOP R EA DI NG
T013 .0000
T01 4 797.0000
Ttfl 5 777.0000
T01 6 787.0000.
T01 7 . 774.0000
1018 771 .0000
T019 761 .0000
T020 770 .0000
^ T021 590 .0000*
. T022 1253,0060
T023 1270.0000
T024 635.0000
T026 779 .4000
1246 736.000k)
1250 448.5000
1251 446.5000
1252 450.0000
A009 11 .92001
F022 52 .7000*
F029 8 .0900 *
F104 109 .2000 I
976
SINCE
4 AN
.0000
790.7222
778.1219
786.2467
772 .8468
770.0717
760.1463
770.3215
601 .0467
1237.3942
1254.7692
631 .8846
778.7744
759 .4093
447.4358
446.1232
449.8109 <
12 .9971
56.2048
8.3157
109.0795
, (*>\
let / 7// - s
J?e*t'ffet
YtSlERDAYS
AVERAGE
.0000
791 .8353
782 .3256
788.7628
776.1278
773.1491
763.3778
7742950
604 £ 685
1226.6743
1240.5473
636.9320
781 .6318
760.4505
447.6210
446.4124
450.0845
12 .5851
54 .6901
82103
109.0281
6552 STOP
MO NI TOR
NEXT?
253
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-*-
?/H/7£
/Lf'.OO
f,01
~-*t
~~3-r
-^3. Z
tf-s~
254
-------
199 0
TtbT CATA
THE DftTE IS 7-1 5-1
TIME _93 1
CURRENT
LOOP R £A DI NG
TiC 13 .0000
T014 798.0000
Ttfl 5 780 .0000
T01 6 788.0000
T017 776.0000
T01B 771 .0000
T019 765.0000
Ttf£tf 773.0000
(^T&Zj) 594.5000
^-T£22 12 62 .0000
T023 12 75.0000
T024 636.0000
T026 781 .3000
T246 748.5200
T250 448.5000
T251 446.5000
T252 450.5000
A009 11 ,5300
CjH^ 56.8000
F029 8.2199
F104 108.6000
6552 STOP
MONITOR
976
SINCE
4 AM
.0000
799.3485
780.9486
790.0981
776.7984
772.3983
7 65 .09 8 6
773.6987
595.1 734
1273.0971
1281 .4472
633.7985
782.4736
749.4986
448.5991
447.5991
450.8742
11 .3864
56.5949
8.2719
109.0548
J-
K
/
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressuref psig
7/1-3 $Jffi/^£
-?- / jr - ?f
4'*l
#,*2-
-.3*
- , 2-f
-, 2 i
3
-------
HLT
HLT
199 0
TEST DATA
THE DATE IS 7-1 5-1
976
1
/<»*•/ ?Ss -/?)
r ( f
f£<& t& // *t» ^
TIME 9:3i).
CURRENT
LOOP R EA DI NG
T013 .0000
Bl 4 799 .0000
T01 5 782 .0000
T01 6 789 .0000
T01 7 777.0000
T018 773.0000
T019 765.0000
% T020 774 .0000
- T021 594.0000
T022 1262.0000
T023 1277.0000
T024 636.0000
T026 782.6000
T246 745.5000
1250 449.0000
T251 447.5000
T252 450.5000
A009 10.9200
F022 55.1000
F029 8 .2000
F104 108.7000
6552 STOP
MONITOR
NEXT?
SINCE
4 AM
.0000
799.3619
780.9984
790.0435
776.8619
772 .4526
7 65 .1 802
773.7258
59 5 .0 89 1
1272 .3603
12 81 .1 789
633.9530
782.51 66
749 .1120
448.5898
447.5899
450.8173
11 .3599
56.381 7
8 .2 654
1 09 .0 679
YESTERDAYS
AVERAGE
.0000
793.5651
779 .6697
786.3564
774 .7321
768.8153
762 .6271
769 .1378
594 .5551
1245.8188
1276.6730
632 .9985
779 .5517
749 .1 748
448.0274
446.3710
450 .0843
12 .1866
55.3869
8.2570
109.1427
i • "" "
257
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7?//-jr
7 //jT/^
4'"3*
f'2-
~_/32-
*~~ -^-/"
--2- 2
2-& rl
258
-------
HLT
199 0
TEST DATA ,( &
THE DATE IS 7-15-1
HME 10:14
CURRENT
LOOP R EA DI NG
T013 .0000
T01 4 804.0000
Tdl 5 785.0000
Bl 6 790.0000
1017 778.0000
T01 8 767.0000
"T019 768.0000
-'T020 765.0000
T021 593.0000
T022 1241 .0000
T023 1207 .0000
T024 635.0000
T026 783.3000
1246 743.0000
1250 448.5000
1251 446.5000
1252 450.5000
A009 10.8100
F022 55.5000
F029 8 J 400
F104 109.0000
976
SINCE
4 AM
.0000
799 .51 80
781 .2380
789 .9578
776.8780
772 .1177
765.3181
7732382
594.8581
12 69 .2363
1276.0766
634 .1 580
782 .5062
748.4581
448.6188
447.4989
450.7789
11 .3207
56.3358
82503
109.0997
7
.g' /?£?€?£
YESTERDAYS
AVERAGE
.0000
793.5651
779 .6697
786.3564
774.7321
768.8153
762.6271
769 .1378
594.5551
1245.8188
1276.6730
632 .9985
779 .5517
749 .1 748
448.0274
446.3710
450.0843
12 .1 866
55.3869
82570
109 .1427
6552 STOP
MONITOR
KEXT? ,
259
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit J.-
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
/>// - 3 000S
7//1T/7*
/#- /S~
fr/i
~r 32- .
~r 3~$~
~r2-
2 F- /
260
-------
I?
HLT
199 0
TEST DATA
THE DATE IS 7-15-1
976
«f ^
3-&00S
TIME 11:35
CURRENT
LOOP R EA DI NG
T013 .0000
1014 795.0000
^ 101 5 784 .0000
T01 6 794 .0000
" 1017 775.0000
T018 772.0000
T019 759.0000
102 0 773.0000
—"1021 592.5000
T022 1277.0000
1023 1219.0000
T024 635.0000
1026 782.4000
1246 744.5000
£50 448.5000
£51 446.5000
1252 451 .5000
A009 11 .0600
F02~2 55.1000
F029 8.0600
F104 109.5000
6552 STOP
MO NI TOR
NEXT? ,
SINCE
4 AM
.0000
800.1311
781 .7976
790.3640
776.8977
771 .6641
76T2642
772 .3311
594.4975
12 67 .22 82
12 65.2958
634.3643
782 .651 1
747.6976
448.6152
447.3486
450.7486
11 .2519
56.0631
8.2283
1 09 .0 © 7
^
YESTERDAYS
AVERAGE
.0006
793 .5651
779.669?
786.3564
774.7321
768.8153
769 !l378
594.5551
1245.8188
1276.6730
632 .9985
779 .5517
749 .1 748
44 8 .02 74
446.3710
450.0843
12.1866
55.3869
8,2570
109 .1427
26 1
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//-J
7//r/rf
/?''7T
&,0c
-^32..
--y-?
- -16
2-7,1
262
-------
HLT
199 0
TEST EATA
THE DftTE IS 7-15-1
TIME 13:23
CURRENT
LOOP READING
T01 4 801 .0000
>T015 787.0000
( T01 6 795.0000
T017 777.0000
T01 8 774.0000
T019 761 .0000
T020 774.0000
tfdZT 588.0000
"T022 1281 ,0000
T023 121 6.0000
T024 637.0000
T026 785.0000
T246 736.5000
T250 448.5000
T251 447.5000
T252 450.5000
A 009 10.6400
F022 52.0000
F029 7.9700X
F104 109.5000
976
r
SI NCE
4 AM
.0000
800.2076
782.6547
79 1 .2 59 7
776.8127
772.0494
764.2076
772.5760
59 3 . 62 85
1269.8098
1254.7839
634 .8 654
782 .91 30
746.5101
448.6299
447 .2484
450.6564
11 .1373
55.5550
8.1876
109.1022
7^/y
3 ,
YESTERDAYS
AVERAGE
\
.0000
793.5651
779 .6697
786.3564
774.7321
768.81 53
762 .6271
769 .1378
594 .5551
1245.8188
1276.6730
632 .9985
779.5517
749.1748
448.0274
446.3710 .
450.0843
12 .1866
55.3869
82570
109 .1427
<-{$
?//•&)
f Vx^
&*0 S
{
6552 STOP
MO NI TOR
NEXT?
263
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7/f-J
? //f/rs
//'zr
?rf?
-,-?}
-^J? f
~./l'
2-7^6
264
-------
HLT
199 0
TEST DATA
THE DATE IS 7-1 5-1
TIME 14:32
CURRENT
LOOP R £A DI NG
TtflS .0000
T01 4 802.0000
T015 777.0000
T01 6 797.0000
T017 769.0000
T01 8 778.0000
T019 754.0000
T020 783.0000
1021 588.0000
B22 1327.0000
T023 1232.0000
-, T024 638.5000
T026 782.6000
T246 7-47.0000
1250 448.5000
T251 446.5000
12 52 4 50 .00i00
A009 10.9799
F022 52.7000
F029 8 .0300
F104 • 108.4000
976
SI MCE
4 Art
.0000
800.3300
782 .5440
791 .7104
776.3775
772 .4249
763.4967
773.1 633
593.1035
1273.1 838
1251 .8986
635.0799
782 .9 51 5
746.2227
448.6292
447.1887
450.61 73
1 1 .12 61
55.41 16
8.1694
10.9.0876
YESTERDAYS
AVERAGE
.0000
793.5651
779.6697
786.3564
774 .7321
768.8153
762 .62 71
769 .1378
594 .5551
1245.8188
1276.67316
632 .9985
779.5517
749 .1748
448.0274 x
446.3710
450.0843
12 .1866
55.3869
8 £570
109.1427
7//- 5
' '/
?> $00$
f1 ct I *X
(^ 1 *~~ * -s
6552 STOP
MONITOR
NEXT? . . ,
??P.* »
265
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7/1-3 Pt">s 6-1-1?
?i/S/7£
>1'3?~
$,#3
-' ? $~~
-,2.e
— /1 •
y-6,3 •
266
-------
HLT
199 0
TEST DATA .
THE DATE IS 7-1 5-1
976
fetf 1\ -3
/
n ME 1 5: 31
CURRENT
LOOP READING
T013 .0000
T01 4 798.0000
T01 5 785.0000
T01 6 790.0000
T017 782 .0000
, 1018 774.00013
' T019 768 .0000
1020 774.0000
C T021 588.0000
T022 1254.0000
T023 1268.0000
1024 636.0000
T026 784.8000
T246 736.0000
1250 448.5000
T251 447.5000
1252 450.5000
A009 10.6800
F022 51 .9000
F029 8.0500^
F104 108.7000
6552 STOP
SINCE
4 AM
.0000
800.3878
782.343?
791 .8870
776.2572
772.7352
763.2790
773.6051
592.6700
1274 .3840
1252.0585
635.2027
783.0421
745.6809
448.5959
447.1176
450.5960
11 .1053
55.1975
8.1564
109.0691
YESTERDAYS
AVERAGE
.0000
793.5651
779 .6697
786.3564
774.7321
768.8153
762 .6271
769.1378
594.5551
1245.8188
1276.6730
632 .9985
779.5517
749 .1748
448.0274
446.3710
450.0843
12 .1866
55.3869
8 2 5 70
109.1427
1*30 NI TOR
NEXT?
267
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7//' 3 ^/j^/*/^
7//*/7
-------
HLT
199 Id
TEST Dft
TA
THE DftTE IS 7-14
TIME 15s 58
LOOP
T013
Tt214
T015
T01 6
T017
•T018
T019
T020
1021
^T022
- B23
T024
T026
T246
T250
T251
T252
A 009
F022
F029
F104
CURRENT
R EA DI NG
.0000
792 .0000
782 .0000,
783.0000
777.0000
761 .0000
763.0000
761 .0000
589 .0000
1230 .0000
1312 .0000
634.5000
777.3000
740.5000
44S .0000
447.5000
450.5000
11 .8900
52.2000
8.2000
1 09 .7000
•
-1976
SINCE
4 AM
.0000
791 .3924
778.4548
786.1 624
773.3503
769.3503
760.6414
769.4959
. 599.1104
1236.3471
1261 .8056
632 £ 674
778.7817
756.2877
447.6126
446.1856
449.9043
12 .81 68
55.5914
8.2874
109.0536
/erf ~?//-3
f
tfo&S
YESTERDAYS
AVERAGE
.0000
791 .8353
782.3256
788.7628
776.1278
773.1491
763.3778
774.2950
604 2 685
1226.6743
1240.5473
636.9620
781 .6318
760.4505
447.6210
446.4124
450.0845
12 .5851
54 .6901
82103
109.0281
6558 STOP
MO W TOR
NEXT?
Lfrtt-J :
Z1,A * (OH /ft/l.'f > Wtllt?
269
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7 ft- 3
7//f/7f
/£:0o
f'2-
-v 32.
~. 3
~^jT
?-7,r
270
-------
HLT
199 &
TEST DATA
THE DATE IS 7-14-1
TIME 15; 31
CURRENT
LOOP R £A DI NG
T013 .0000
T01 4 795.0000
T015 782.0000
101 6 785.0000
T017 777.0000
T018 762.0000
T019 764.0000
T020 762.0000
-T021 589 .0000
. T022 1224.0000
T023 1317.0000
T024 633.5000
T026 778.3000
1246 743.0000
12 50 448.5000
T251 446.500G
T2 52 4 50 . 50 00
A009 11 .9500
F022 53.8000
F029 8.2000
F104 109.1000
6552 STOP
MO NI TOR
NEXT?
976
SINCE
4 AM
.0000
791 .2576
778.2575
786.1917
773.1701
769 .6484
760.4741
769 .7786
599.4962
1236.5585
1259 .2980
632.2142
778.7878
756.8332
447.5742
446.1 503
449.8786
12 .871 6
55.7649
8.2905
109.0647
/'f/ ?//-.f
V '
So&s
YESTERDAYS" " """ ""
AVERAGE
.0000
791 .8353
782 .3256
788.7628
776.1278
773.1491
763.3778
774.2950
604 £ 685
1226.6743
1240.5473
636.9620
761 .6318
760.4505
447.6210
446.4124
450.0845
12 .5851
54 .6901
8.2103
109.0281
2 7 1
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 1
Test
Date
Time
Load
Stack Draft
Convection Section Draft
Furnace Draft
Fuel Gas Supply
Pressure, psig
7/1 -3
9+tf-rs .,
}&3f
r**
--3
- ,2-S
-,*1
2 1*1
272
-------
LOCATION 7
Fuel Gas Analysis
Unit 1
METHOD:
Mass Spectrometry
Component
Refinery Gas
Test 7/1-3
methane
ethane
propane
i-hutane
n-butane
pentane
hexane
C +
60.95 mole %
3.94
4.90
,63
1.01
.51
.34
.07
ethene
propene
butene
.89
1.14
.67
cyclohexane
benzene
.02
.01
nitrogen
oxygen
carbon dioxide
water
hydrogen
2.34
.63
.06
.08
21.81
273
-------
LOCATION 7
Date / ' 2- 76 unit
Probe Position
(inches from back wall) Ptfrtl
f-'-f"
I'-//"
V '- r"
-$'-//"
3'-r"
2'-//"
z'-s-"
)'-'/"
}>-$•»
H"
?"
Average
O Traverse
/ Sample Point
0.
(%T &&£
#,3? t?,7
#,23*
#.2?
V'l
t.l
€,0
#')
f,0
3,0
7,1
7,1 80.5
CO
(ppm)
274
-------
PETROLEUM PROCESS HEATER
Location No. / Unit No.
Unit Description
Installation Date
Heater Rating
UM
Burner Description
OoMkl
Test Fuel Combinations
Fuel Temp, .at Burner (°F) ^rr?£)/&}^ /
Primary Air Temp. (°F)
Comments:
275
-------
Test No..
Unit No.
~ I
Date
MOBILE LABORATORY DATA
Location /
Test No.
Engr
Fuel///; CAS. Capacity 3 ?' f * /*'
Unit Type ft £ F,
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate 10* /BO '
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A twos. Temp. (eF/°C>
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28. '
29.
30.
7/2.- 1
7- ft- 76
/f 00
•
tf/f J /
37" tv
f't.
£e
£?
f
(7
O'~
/o
I
3
•PI i—
f
f?
$0
7
17
r
/f
1
y
• "^
. n
7£
3* }0
f 1
7~M-7t
/tjfF
" •
w,r?
37" '/fit
Q f
.rr
£T~bt
1
£1
i
71
77
I
f/
7-0
g
0
H
//
0
6
q if
(3
3027
^i
7-H-7C
/5~20
—
it. 17
3?" /A/
&,
5-3
f2
1
(2~
*,
g
2-
i
«^™"
{
77
75~
/
10
f
12
3
£
^mm*^
f/
rl
20,27
£/
?-/f~7f
/{00
—
*•/}. F6
37"
f'
5T
f~/
1
ei
JAJ .
f/V -
7
#6
75~
(p
fS £f
7.2
f
/•j
f
.MM
f
f
7
U
77
J0,2f
it
•^~
7-Jf'7S
/Off
—
<-//,00
^
—
&y
rr- 7^
F2 71
3 y
^/ f/
7*i
1 fl
£ f
3- 3
.
If
7?
90.30
9~&
-
*Correction to 3% 0, should not be performed if
the value is measured on a wet
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
Unit Type
MOBILE LABORATORY DATA
Location _ ?
*, GAS capacity
Burner Type
Test No.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atttss. Temp. (°P/eC)
19. Dew Point Temp. (eP/°C)
20. Atxnos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/2-2-
7~2- &
0^00
— _
y/^?
*-3?"^
f-
/y
*e
i
£0
7-
i
/_3 ~ jd*-' ^^
— -
W-t£
•^
r,7
i/ £0
it 60
o o
i7 £1
7r?
& ?f
i £
I /
. —
17
ft
y#,33
2*0
*Correction to 3% 0. should not be performed if
the value is measured on a wet basis. . _
Ki U4 7
5 ^
Data shMt 6002.2
Si
v
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
- 7£ Location _ 7
; 6*S Capacity ? ?-
Unit Type
Burner Type
Test No.
Engr.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atros. Temp. (°F/eC)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/2-2-
7-20
>3?4~
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2.
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3
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0
-------
Test No..
Unit No.
MOBILE LABORATORY DATA
Date /~2(~7f Location 7
Test No.
Engr.
Capacity 3?-
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A tiros. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24;
25.
26.
27.
28.
29.
30.
7/2'3
7-2/-7f
01/4~
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3
62
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71
70
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7-
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5~0 72.
7.<(
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3 1
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1S
7t
30,21
£~2-
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis. 'fo 7 Q
t K ' a
1
Data Sheet 6002-2
t t
N tS
\rt nL jv ^*
-------
MOBILE LABORATORY DATA
Test No. 7/2- ~3 Date 7'2I~7£ Location
.2-
Test No.
Engr
No.
Unit Type
Fuel /^ g/f ^ Capacity -?7-
Burner Tvr>e
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oz (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 i3£>
—
1?'0f
^37"^,
f'
y*
y&
2~
fi
f,
£
0
0
f
£0
rf
?
7?
0
t
^
0
ft
77
?0,^g
£2-
7/2-3
7-2/--?(
}f-&0
—
?J
•P*"
4& 49
tf f
-77
Ja^f
j~f
7/2-3
7-2-t-7f
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—
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^37'"^
f.
tf?
V4
/
FT
7,
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/-
&
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6?
£/
/
7*
0
//
^?
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MBM.
1 '/
7?
?0~2S-
3~£
>'
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis. ^ 2
80
Data Sheet 6002-2
k
-------
EXPLANATION OF COMPUTER PRINTOUT OF OPERATING DATA
Location 7
Unit 2
T401 Product Outlet Temperature
T423 Product Inlet Temperature, left side
T424 Product Inlet Temperature, right side
F403 Product Feed (Naphta)
F441 Recy. Gas Flow
Total Product Feed
F442 Recy. Gas Flow
T601 Temperature in Convec.,Section
T603 Stack Temperature
F440 Fuel Gas Flow
28 1
-------
HALT!
243 «T
L00p DISPLAY
ENTER LOOP TJO.
TYPE A
TYPE A-
TYPE A
TYPE A
YPE "A
TYPE A
TYPE A
-TYPE A
TYPE A
TYPE A
"COD IT ' '
cnn c.
T401
T423
T424
F403
T44T
F442
T601
T602
T603
T507
T7~~l
580.625 DEGF
4B0T0-0t3-DEGF~
469.503 DEGF
41.375 M3PD
364T!
364.875 MCFH
1084.000 DEGF
945.000 DEGF
-6272-S7J3P
MONITOR
UEXT7™"
T510??
NEXT?
HALT!
24ZI 0
"LOOP DISPLAY"
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE A T511
ERR E 77 240 6272 STOP
MONI TOR
NEXT?
282
-------
F
2-
7 - /
-------
SUPERVISOR INITIALIZATION
ERR R 306 148 228
HALT!
"24? $
LOOP DISPLAY
ETTER LOOP MO. (LETTER t 3 DIGITS)
TYPE A
TYPE TV
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPZ-TT
TYPE A
HALT!
T42J1 = 580.000 DEGF
T4?3 =" 479.25irt>EGF--
T424 = 469.500 DEGF
F403 = 41 .968 MBPD
F441 = 3647500-MCFFT
F442 = 364.125 MCFH
T601^= 1076.000 DEGF
T 633~= 9 47.1300 DEGF "
--/
HALT!
240 0
"LOOP DISPLAY-
7-
ENTER LOOP NO. (LETTER & 3 DIGITS)
T401 =
T423 =
T603 =
580.000 DEGF
479.250 DEGF
-470V250-DEGF
41 .562 MBPD
365.625 MCFH
-3S1T5130- flCFH"
1069.000 DEGF
946.000 DEGF
284
-------
HALT!
240 0
LOOP DISPLAY
7-
INTER 100P NOT-aETTER-&-3"DI-GITSr
TYPE A T401 = 578.750 DEGF
TYPE "A' T423 ~—479T250 -DEGF--
TYPE A T424 = 468.750 DEGF
363.750'MCFH
362.250 MCFH
1066.000 DEGF
;000"DEGF—
TYPE A
TYPE A
TYPE A
TYPE' "A
TYPE A
HALT!
F441
F442
T601
T603
285
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 2
Test No.
Date
Time
Load frfJ
Firebox east
Firebox west
Stack Pressure
Plenum PT. 1
Plenum PT. 2
Plenum FT. 3
C.R. Stack (X, (%)
Pressure in Gas
Manifold
7/2-1
7^1
IW
ti. n
«"l,0
«"•/. 1.0
>/*0
-73
-^1
-.5-J
~.*2
13,0
M
7/2-1
7-11
l'f:5P
W, ?f
-.15
-, 1*
-.73
-'fl
-.r3
-**•
/}.?
/w
7/2-1
7- If
V'-?*
W.1?
>/.0
-.ft
-.75"
-,rj
-,?3
-.?
—
/t.1
7fr-l
7-n
t£e>o
W.f
-.10
-.ft
-**
-.&
~-.rf
-.f*-
}2.f
J1.fi
7/^-1
7-11
K:3*
~.tr
~.tr
~.7l
-.?!
~?2.
'ft
tf,0
/f.7
9
283
-------
LOOP DISPLAY
ENTER 1.00P "NOT tLETTER "& 3 DT GI TS)~
TYPE A T401_=_580.625 DEGF __
TYPE A T424 = 469^500 DEGF
TYPE A F403 = 41 .093 MBPD
TYPt-A- F 441"-s—3 607750 TICFH
TYP.E A F442 = 357.000 MCFH
3YPE A T601 = 1080.000 DEGF
fP"E~A —
TYPE A
HALT!
287
-------
HALT!
~240"~0'
LOOP DISPLAY
ENTER LOOP NO. "(LETTER ~& 3 DIGITS)
TYPE A T401 = 581.250 DEGF
TfPE A " T423~s—-481V500-DEGF-
TYPE A T424 = 470.250 DEGF
TYPE A F403 = 41.406 MBPD
TYPE"A—F~441 - 3S0.000~MCFH
TYPE A F442 = 361 .500 MCFH
TYPE A T601 = 1114.000 DEGF
'TYPE"A -T603"=-
TYPE A
288
-------
HALT!
240 0
LOOP DISPLAY
2 0 1978
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPEHA
HALT!
F440
T401
T423
T4?4
F403
F441
F44J*
T601
T603
52.01*
580.625 DEGF
480.000 DEGF
468.000 DEGF
41.718 MBPD
363.000 MCFH
7-
1065.000 DEGF
917.030 DEGF
289
-------
HALT1
240 0
LOOP DISPLAY
JUL 2 0 1976
7/
fr^s
2 -
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE
TYPE
TYPE
-TYPE
TYPE
TYPE
TYPE "A
TYPE A
TYPE A
TYPE-A
HALT!
F440
T401
T423
T 42*
F403
F441
T601
T603
579.375 DEGF
480.000 DEGF
41 .875 MBPD
360.000 MCFH
1036.000 DEGF
917.000 DEGF
290
-------
JUL 201976
240 0
LOOP DISPLAY
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE
TYPE
TYPE
TYPE
TYPE
TYPE
A
A
A
A
A
A
F440
T401
T423
T424
F403
F441
— -
;
-
-
—
—
— 51
579
480
468
41
364
•
*
•
•
*
•
449-
375
750
750
156
875
MCFH"
DEGF
DEGF
DEGF
MBPD
MCFH
~TYPE~A~ T442~= — 3 64 ;~8 75~P1C FH ~
TYPE
TYPE
A
A
T601
T603
;
~
1041
913
*
•
000
000
DEGF
DEGF
TYPE'*
HALT!
29 1
-------
JUL 2 0 1976
HAITI
240 0
LOOP DISPLAY
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE
TYPE
TYPE
TYPE
TYPE
TYPE
TYPE
TYPE
TYPE
A
A
A
A
A
A
A
A
A
F440
T401
T423
T424
F403
F441
- F442-
T601
T603
^
—
—
r
—
—
~
~
-
" "513
5S0
481
^468
41
363
—365
1042
913
•
*
*
*
•
•
•~
•
*
531-
000
500
750
281
000
000
000
tlCFH
DEGF
DEGF
DEGF—
MBPD
MCFH
ticm —
DEGF
DEGF
292
-------
JUL 201976
240 0 -
LOOP DISPLAY
'ENTER LOOP "HI
1YPE A
-TfPE "A
TVP.E A
TYPE A
fPE IT-
JfPE A
WPE A
TYPE A
TYPE A
TYPE A
HAITI -
F440 =
T423
T424
F403
F441
F442
T 601
T603
53.024 MCFH
- -57B 7750-1) E6F"
479.250 DESF
468.000 DE3F
^4r.-S75-WBPD
364.500 MCFH
361 .875 MCFH
1046.000 DEGF"
935.000 DEGF
4*
293
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 2
Test No.
7/2-2
Date
7-20
7-2*
7-20
Time
Load
V/,72
Firebox east
~ f
Firebox west
-13
Stack Pressure
-.7%
-. 73
Plenum PT. 1
-ft
- 7J?
-.7?
-.73
Plenum PT. 2
-,77
Plenum PT. 3
'.72
C.R. Stack O2 (%)
Pressure in Gas
Manifold
20-5*
2! -2
X
K
^
X
K
294
-------
HALT!
-240-0
LOOP DISPLAY
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
TYPE A
T401 = 578.750 DEGF
T423 = 4777T50~DEGF
T424 = 466.500 DEGF
F403 = 42.750 MBPD
F440 = 53. 593 TIC FH
F441 = 363.750 MCFH
F442 = 361 .125 MCFH
T603 = 9501000 DEGF
HALT!
295
-------
"HAITI —
240 0
LOOP DISPLAY
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE A T401 = 579.375 DEGF .
TYPE A T423 = 478.500 DEGF
TYPE A T424 = 467.250 DEGF
42;G2"5 WBPD --
TYPE A F440 = 53.243 MCFH
TYPE A F441 = 363.750 MCFH
TYPE A T60I = 1127.000 DEGF
TYPE A T603 = 946.000 DEGF
TYPE A "
HALT!
296
-------
HALT!
240 0
LOOP DISPLAY—
ENTER LOOP NO. (LETTER & 3 DIGITS)
TYPE
TYPE
-TYPE
TYPE
TYPE
"TYP1T"
TYPE
TYPE
A
A
A-
A
A
ir
A
A
TYPE~A
TYPE
A
T401
T423
-
-
581
479
*
•
250
250
DEGF
DEGF
~T 42^4-= — 46772 52TD EGF '
F403
F440
TW
F442
T601
'7603
i.
-
— fc— •
-
-
"i '
42
52
—359-
358
1110
"937
•
*
•
*
•
•
968
850
250
875
000
000
MBPD
MCFH
-flCFir
MCFH
DEGF
"DEGF
HALT!
297
-------
7-
T
F
/=
r
r
36
-------
tsT 7/a-3
T Mo i 5-79 V
r
T
F /S'o^ ^a 3^ fl
r «/*/ sr^o */"
r
T
T to/
r
-------
SUPPLEMENTAL OPERATING DATA
Location 7
Unit 2
Test No.
7/2--J
7/2-3
Date
7-2^
7-2!
Time
01 /r
Load
Firebox east
-lo
-.ft
Firebox west
-.ft
Stack Pressure
- 77
-to
-.7*
Plenum PT. 1
-.67
Plenum PT. 2
- 70
Plenum PT. 3
C.R. Stack 02 (%)
2*2
3.7
Pressure in Gas
Manifold
300
-------
LOCATION 7
Fuel Gas Analysis
Unit'2
METHOD:
Mass Spectrometry
Component
Fuel Gas
Test 7/2-2
methane
ethane
propane
i-butane
n-butane
pentane
hexane
C +
6
ethene
propene
butene
58.08 mole %
6.75
5.91
.46
1.02
.29
.30
.07
.67
.58
.69
cyclohexane
benzene
.03
.01
nitrogen
oxygen
carbon dioxide
water
hydrogen
1.11
.30
.06
<.01
23.67
30 1
-------
LOCATION 7
O_ Traverse
Date
Unit -2-
Sample Point
Probe Position
(inches from back wall)
*
/2-
//
*y
?
-------
GAS TURBINE COMBINED CYCLE
Location No. i Unit No.
unit Description GAS.
150. MvO (515,000
Installation Date
Heater Rating \ SO
Burner Description
8
Test Fuel Combinations
Fuel Temp, at Burner (°F)
Primary Air Temp. (°F)
Comments:
303
-------
Test No._
Unit No.
'I
Date
MOBILE LABORATORY DATA
Location
Test No.
Capacity
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
r
6. Flue Diam. or Size, #£ A**"
7. Probe Position
8. Oxyqen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 0? (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (8F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7#~l
7~2£
tft/f
tf£8 '/£
— _
/#>'V/7y"
gie.£x#.
2 0
77
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100
&
2f*
#
0-
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^2*
13
1
//?
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to
••I i •*.
ft
7f
29,4*
//
///-/
7-2S
2000
Iff tfU/
• —
. —
6.r, £*#.
J7.
^MMH
•a^
•M •
37
/
//
VMM!
-*—1"
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5"
•••••
•*••**
IMBHh
110
1
#2-
MBWBMW
••••••i
•••^Hk
f?
7f
1
-------
MOBILE LABORATORY DATA
Test No.,
Unit No.
Unit Tvoe
Date
Fuel
Test No.
Engr.
Capacity
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. N05 (hot) read/3% 03 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (BF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23. /
24. ,/^J
25.
26.
27.
28.
29.
30.
7/?-f
7-2 '?' ft
//:*5~
17.
<~ _
? •—
0
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11
2.
11
11
16
2
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3*0
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2.
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2.
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f?
7$
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£S"7o
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Si
N
1
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i?f
f
c? ^?
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—
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7/7 -f
7-27-7S
J/r/f
(x)
%
—
_
--
107
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13-0
f
#^"f
—
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7/3-1
7-2 7 -?f
/??20
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S,
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^-
f/:/
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6
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2.<7
—
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—
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/#.£
&00 IWl
— —
— —
— _
•Correction to 3% 02 should not be performed if
the value is measured on a wet basis%
" ' '-—• : 3 D o
. Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date 7~2 7-7f Location
Fuel
Unit Type C0f?g, C
Test No.
Engr
K
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/ 3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
if
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7ft 't
7-27-7S
//: 2£
17
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Data Sheet 6002-2
-------
Test No. 7f
Unit No.
Onit Type ^
MOBILE LABORATORY DATA Test No.
x'"~-^ Date /~^7~S* Location / Engr. tf^A/5
-** Fuel ££ £ &$£ Capacity ^/$~ K (S>5 fftf.
"&/"?/. <£" ¥£(-£ Burner Type fftSfifC//?^^
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NOo (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (CF/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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tho value is measured on a wet basis.
307
Data Sheet 6002-2
-------
Test No._
Unit No.
Onit Type
MOBILE LABORATORY DATA
Test No.
Fuel///:
Location
Capacity
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (0F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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308
Data Sheet 6002-2
-------
Test No..
Unit No.
7/3
MOBILE LABORATORY DATA
Date 7-2 7~76 Location 7
Capacity f}$~ /K fh//ir
Test No.
Engr.
Unit Type_
Burner Type
1. Test No.
2. Date
3. Time
.4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7, Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% Oz (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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the value is measured on a wet basis.
309
Data Sheet 6002-2
-------
Test No
Unit No.
. 7/3~2-
Date
MOBILE LABORATORY DATA
Location 7
Test No.
Engr
Capacity
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 03 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (eF/°C)
19. Dew Point Temp. (°F/"C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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3 1 0
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No..
Unit No.
Date
Unit Type
7
Capacity
Burner Type
Test No.
Engr
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% O2 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
#
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°P/eC)
19. Dew Point Temp. (°P/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30,
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Data Sheet 6002-2
-------
Test No._
Unit No.
Type
pate
MOBILE LABORATORY DATA
Location f_
Test Mo.
Fuel///-:
Capacity
Burner Type
Engr.
/h/4+
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 0? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. ("F/'C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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the value is measured on a wet basis.
312
Data Sheet 6002-2
-------
Test No. 7(
Unit No.
Unit Type «
'J'-Z- Date/7'
3 Fuel fo
Wt/, £fCL
MOBILE LABORATORY DATA Test No.
3y~7& Location "7 Engr. //4/^S
rf, £j£ Capacity f~/5~ S£ /#$ //£/-
£~ Burner Type yfVfl p(J/£/(/^/^
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO9 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°P/eC)
19. Dew Point Temp. (eP/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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the value is measured on a wet basis.
313
Data Sheet 6002-2
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date 7'21~76 Location "f_
Fue 1 fi£ft (?A $ Capacity
Test No.
Engr.
Unit Type
f C t £
Burner Type
1. Test No,
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
T. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°P/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/5-3
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the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No._
Unit No.
Type
MOBILE LABORATORY DATA
pate 7-2l~7f Location 7
Fuel /M 6Af Capacity
Burner Type
Test No.
Engr.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/3-3
7-2JWO>JMC
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Test NO._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No.
7
Fuel///;
Capacity
OnitType
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% O2 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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3 1 6
Data Sheet 6002-2
-------
Test No..
Unit No.
Unit Type_
MOBILE LABORATORY DATA
pate 7-21-7f. Location 7
Capacity
Burner Type
Test No.
Engr.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% Oa (ppm)*
11. N09 (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Baeharach)
18. Atnos. Temp. (*F/'C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity («)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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>!**/
t// f
(D
5~~
73
7?
^
fff
4T*
n.
$,
&•
.>
•Correction to 3% O2 should not be performed if /
the value is measured on a wet b
'
Data Sheet 6002-2
-------
Test No
Unit No.
. 7/7-.
J
Unit Type
MOBILE LABORATORY DATA
Date
Fuel///^
Location
/
Test No.
Engr
Capacity
Burner Type SfC/0
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
1. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (eF/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/J'J
?-J?-?f
1203
1*8
^Z>
>i.
— •
.-—
fO
&
0s
2000
r—
» in —
•^•••^
*?5~
—-^
?0
q
1000
f V
&2-
3
f0
\
?/fr?
7-2$'7t
teflf
L&
3.
•>. •*
^i-
?0
*?>•
2000
*—«•*•
— • -^
• l-
f
•*v
• ^,
&Y
2
">
**-*.
m i -
- '
7/3-?
7-31-76
/20f
(l)
£,
••••
•"•"•"
#7
^F
v^
I7W
*»M.
•^ -•
t^«^
i
«— *
•• iliii^,
J02.
z
%>3y
-*fc-*^
•***.
^M.i
•M«WMMM
7/?-3
7-29-/S
12- //
(/e>J
3i
**~
••*
&>r
t*
2000
,"""
* '
3
— **.
I—I ..»
,»."••
c5 v
r
jtetto
— ^
• in-^
• 1
«
•
7/3-3
'7-24 -7S
}2/y
C'iJ
£",
•Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
3 1 8
Data Sheet 6002-2
-------
Date
Test No. 7/3" 3
Unit No. 3 Fuel///f ^
MOBILE LABORATORY DATA
~7£ Location /
Test No.
Engr
Capacity
Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO5 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uneor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/3-3
7-2J-76
!2/7
ys#
ce>w*s/r£
f.
•i nan
*~ '
».ni»"
10
$'
7000
«M
•*"••
•^B—
f
...
•—-v
too
6
>
— MS
M
^f &i
#2
30,00
6 &
7/1-3
?~24 -y
0
Y?
•***-.
7/3-3
7-2?-7S
/e/23
*^t«
+**^
&
f-3
..
, — .
/t>2 1(0
/0,2-
i?0 Ws
«_ —
^
-^
-------
HO. 7/3".
Unit No. "3
Date
MOBILE LABORATORY DATA
Location
Test No.
Engr.
capacity
Onit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NOa (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uneor/cor
15. Hydrocarbon (ppm) uneor/cor
16. Sulfur Dioxide (ppm) uneor/eSr
17. Smoke Spot (Baeharach)
18. Atinos. Temp. (*F/*C)
19. Dew Point Temp. f*F/*C)
20. Atinos. Pressure (in. Ha)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7/3-3
7-2f'?(
/f 3?
y^z
(D
5.
gOMM
„..
•M*
#$"
M
frifff
mm
ma
•-»•
2
•***.•
W
,£
Iffl
mttm^..,
•*«»»:
•WO,
f/
f3-
JjzJLJL^L.
£"T
7/3-3
?~2
-------
fott-ZZ.
OPERATING DATA
Unit 3
Test: Time: /f!f0 Date: JUtf 23,W
Load - Steam Flow (Red Pin) *-*/!)&.
Air Flow x £0,00* ^/ftf **/t/A
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES *** rW£ W£*
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H0O)
Gas Turbine Exhaust Pressure (in. H0O)
Windbox Pressure (in. H^O)
Furnace Pressure (in. HnO)
Economizer Inlet Pressure (in. H_O)
Economizer Outlet Pressure (in. HnO)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine. Exhaust
vysr.eoo
j/ 6^000
*T0f ' #0 0
^^0 00 O
tf ^
f,jT
f*f0 000
ft 2-
t ^gr ^^^ ^^ ^^ .•lain *"^ j^fc
&/ & ' ^ *^P J? /^J^t
^
/ f
Jf
12. 5~
1- 2-
1.0
0.
-------
OPERATING DATA
Location 7 //7A " '
Unit 3
Test: 7/2.-\ Time: /$'fl'/5~ Date: <7"^ ^ -^ V /??f
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/(5+6)J - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES <*r *'**'
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H^O)
Gas Turbine Exhaust Pressure (in. H0O)
Windbox Pressure (in. H.,0)
Furnace Pressure (in. H.,0)
Economizer Inlet Pressure (in. H.,0)
Economizer Outlet Pressure (in. H«0)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas-Turbine Exhaust
iff * /* )6s/j,r
l.f
Mf* Am
2?
/#, F
ft-*
/2,£~
1,0
V'0
+ .i
7*r
2?S~
210
?t*
7S*
7/iT
3f7
7F
-------
OPERATING DATA
Location 7
Unit 3
Test: ~7./3~\ Time: //-'2 5~ Date. J£fc ^ ^ ?J
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x t5/(5+6)] - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H..O)
Gas Turbine Exhaust Pressure (in. H0O)
Windbox Pressure (in. H^O)
Furnace Pressure (in. H.,0)
Economizer Inlet Pressure (in. H_O)
Economizer Outlet Pressure (in. HnO)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas_ Turbine- Exhaust
*7S
60g$~00
270000
/0.0
7,0
f '60000
l.f -r 2.f
t**
27,5-
/1.0
!<+.£>
/2-$"
1.0
?
2*0
Jgf
7/5"
72*
7F5-
Comments:
-------
OPERATING DATA
Location 7
Unit 3 f&6. Jff*rrf'
Test: 7/7-2 Time: 13-10 Date: 7^ Y 2-7.W76
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/ (5+6)1 - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H^O)
Gas Turbine Exhaust Pressure (in. H0O)
Windbox Pressure (in. H0O)
Furnace Pressure (in. H00)
Economizer Inlet Pressure (in. H_O)
Economizer Outlet Pressure (in. H_O)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
yY^ K !h /Mr (***? MM
f2-3^
<£/f5~5~0
2 70 £>(?O
7- &
10. o
FJ-o £ )+s/ffr
.1 * I-/
*?*
2f.#
11.0
t
-------
OPERATING DATA
Location 7
Unit 3
Tests 7/7 --2- Time. } £ :00 Date. JUt? £7 /f
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated - 4 x [57(5+6)1 - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H0Q)
Gas Turbine Exhaust Pressure (in. H«0)
Windbox Pressure (in. H-0)
Furnace Pressure (in. HQ0)
Economizer Inlet Pressure (in. H«0)
Economizer Outlet Pressure (in. H.QJ
TEMPERATURES (°Fj_
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
^eyppo C Let/Iff tSsJfTJ#£-£)
£2 ##&&
£3 fffQ 0
2 7r**e>
/t,0
?, 0
rt00&o
, 7
*?•
-27.*
H.0
N /^
[2.
1*3
i<0
f**i
7f*
*,
-------
OPERATING DATA
Location 7
Unit 3
Test: 7(2 *~^ Time: *^'/5^ Date: J"^i-f 2#j/$
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen.
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H^O)
Gas Turbine Exhaust Pressure (in. H0O)
Windbox Pressure (in. HnO)
Furnace Pressure (in. H0O)
Economizer Inlet Pressure (in. H_O)
Economizer Outlet Pressure (in. H.O)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
ffV + VfY t-w MWfct
5~/6
ffo 000
2f00£>*
IZr*
^2-
4~/2
2*3
r**
2^f
j £& SJ
/ 1*/ A
/2~0
<7~0
?~7
•s-y
??r
2-S0
J
-------
OPERATING DATA
Location 7
Unit 3
Test: ~?/3~2 Time: l# ' V * Date :
-------
OPERATING DATA
Location 7
Unit 3
Tests 7/7^3 Time: f'V* Dates 7^ f Htf
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MH)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated - 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H*0)
Gas Turbine Exhaust Pressure (in. H«0)
Windbox Pressure (in. H«0)
Furnace Pressure (in. H.O)
Economizer Inlet Pressure (in. H.O)
Economizer Outlet Pressure (in. H.O)
TEMPERATURES (°F)
Superheated Steam
Hater Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
t/- «Mk
4*** ff • JJF~
M.0
w.r
t£'1
?•$"
4* ^
1+ ff
r, i
?*r
2S0
3#*
?£'£'
7S0
7/7
?rr
7?7
Comments
328
-------
OPERATING DATA
Location 7
Unit 3
Test: 7/J>"3 Time: /^??,/f
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. HnO)
Gas Turbine Exhaust Pressure (in. H.,0)
Windbox Pressure (in. H.,0)
Furnace Pressure (in. H0O)
Economizer Inlet Pressure (in. H«O)
Economizer Outlet Pressure (in. H.O)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
/"
r/s
60$r#0
^? ^^>9 -X^^^!^?
jfC- *y p £r&f^S
I2<2~
7'S~
f-/1^
,2
#2*
t^"^ $ * 2
/ & ^^
f^o
I2'5~
f,v
2r9
S-rV
7ff
2f~f
?f*
75~2-
7f0
7ff~
Jff
732
Comments*
-------
OPERATING DATA
Location 7
Unit 3
~~7 / "? "^ 1 *1 m- ** ^ "*f/if *3 J& /4Sf*?S
Test: /rj-^ Time: /X-^? Date: «/**- >^7. /7/»
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load MW)
Gas Turbine B (Load MW)
Fuel Flow to Gas Turbine A
Calculated = 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H.,0)
Gas Turbine Exhaust Pressure (in. H.O)
Windbox Pressure (in. H.,0)
Furnace Pressure (in. H.,0)
Economizer Inlet Pressure (in. H^O)
Economizer Outlet Pressure (in. HnO)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine- Exhaust
&/ f £t
^y^/ 9
rs&7/
/ ^J 4^^
f ^f* ^ ^f "
1, 2-
?. 7
"t-'V
7?S
2~$~7
12-
Comments^
330
-------
OPERATING DATA
Location 7
Unit 3
Test: 7/J-3 Times W'30 Date: MY -2? /?/
Load - Steam Flow (Red Pin)
Air Flow
Fuel Flow to Boiler (SCFH)
Fuel Flow Both Turbines (SCFH)
Gas Turbine A to Boiler (Load Mff)
Gas Turbine B . (Load MW)
Fuel Flow to Gas Turbine A
Calculated » 4 x [5/(5+6)l - (SCFH)
Feedwater Flow
Percent Oxygen
PRESSURES
Superheater Outlet (psig)
Refinery Gas Burner Heater
Pressure (psig)
FD Fan Discharge Pressure (in. H0O)
Gas Turbine Exhaust Pressure (in. H^O)
Windbox Pressure (in. H0O)
Furnace Pressure (in. H00)
Economizer Inlet Pressure (in. H^O)
Economizer Outlet Pressure (in. H_0)
TEMPERATURES (°F)
Superheated Steam
Water Economizer Inlet
Water Economizer Outlet
Combustion Air
Furnace Exit
Gas Economizer Inlet
Gas Economizer Outlet
Gas Turbine Exhaust
V72-
r/*
5~ty&00&
J2- &5~00&
/2r2-
~?rJ~
Ft '
/f,$~
;1, 0
I2'2.
f'2.
3'^
i-^i
7?r
2$~f
?f5~
?r$~
7f1
7^&
Jfy
f/2-
Comments i /(/•£ / 2. T/~ $~ £ £ £ /S 7~£ & &&%> 0/&/AJ / ^Frffff &
s /
-------
LOCATION 7
Fuel Gas Analysis
Unit 3
METHOD; Mass Spectrometry
RESULTS;
Component Concentration
methane 91.67 mole %
ethane 2.81
propane .46
butanes .05
nitrogen 2.71
oxygen .57
carbon dioxide 1.60
argon .03
water .03
hydrogen <.01
332
-------
Date
Load
Location
K V B. INC.
STACK DATA
Unit No.
Test No. 7/3
Engr
K. MM K#/hr or MBtu/hr
Sample Box No. / Meter Box No.
Fuel
Filter No. .
[ Probe No.
Filter Heater Setting */
Probe Heater Setting 2.
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather
I
diam.
Stack Gas Pressure, PS ,/ iwg
Abe. Stack Press., AP-P +407- iwga
Stack Gas Sp. Gravity, Gs n.d.
Stack Area, As ft2
I Probe
•MwMMie
Remarks
Final Meter:
Initial Meter: 1 03-7.
Time
HOWS
1700
tfO
).e
Stack
Temp.
(°F)
%0
3ff0
3£0
760
/&®*
6F
4- 460
Impinger
Temperature
Out
(6>F)
f*
go
tr
!00
In
(°F)
230
2>7Q
27$
3.70
Filter
BOX
Temp.
(°F)
Me
IVff
JC/0
$io
Meter
Temp.
(°F)
106
)2f>
l*£
;^r
• - • -- ,
Ts-
60-13
11/20/75
333
-------
LOCATION NO.
OWNER
DATE
POINT OF EMISSION
PLUME OPACITY OBSERVATION RECORD
POINT OF OBSERVATION
Test Run Mo
. 7/3-
7
OBSERVER
BOILER HO.
CAPACITY
Jclb/hr
: FUEL TYPE #£f. £<*S BURNER TYPE # M G
Yd K PS
TEST
NO.
Y
Tine
an/pm
Type
Test
Load
k#/hr
Opacity
-
WIND
Speed
mph
Direct
Sky
Cond,
•
•
Sun
Posi-
tion
Comments
.-
DO A11>6 Sttnc.
60-25
334
-------
VELOCITY TRAVERSE
Projects
bates
locations
Units
Tests
?~2<-7f
7
3
7/3-1
, _ Test Descriptions
Personnel:
Stack Cross Section
FWBlt
Barometric Press, (in. Hg)s
Absolute Static Press, in Stack (in. Hg) i_
Pitot Tuba Coefficients
(P.)
1/2
Time
Traverse Point
Port Depth
33"
&*
?!"»,•
^"
M"
Velocity
Head
(in. H,0)
ts
0,(* *
«*« *"
^,t>5~ X
^.t?7 *-
tf-^y ^
Gas Teatp.
CD
3(?
a
?ff
u
^
Gas Temp.
CR)
TS
t*s
1 1
ir
n
>i
Molecular
Wt.
»S
Velocity
(ft/sec^
vs
67.}f
2t,1
19.62-
22*1
tt.(2-
W.-?I,C>7
02
Cone.
{% Dry)
6002-13
335
-------
LOCATION 7
O Traverse
Date
23/17* Unit 3 Sample Point 6«*
*
Probe Position
(inches from back wall)
/
10
20
?(?
HO
5~o
£0
70
#0
1*
100
If*
120
Average
S3
j?,f
-------
LOCATION 7
O- Traverse
Date
2?J17( Unit 7 Sample Point .81*.
Probe Position
(inches from back wall)
S3
CO
(ppm)
20
a
Ho
6,2
50
(0
70
10
- 7
too
#0-12.0
Average
337
-------
GAS TURBINE COMBINED CYCLE
Location No. Q Unit No. &_
Unit Description
200
Installation Date
Heater Rating
Burner Description
-«Jip>4t^
Test Fuel Combinations
Fuel Temp, at Burner (°F)
Primary Air Temp. (°F) A-^l. °C-
Comments:
338
-------
Test No
Unit No.
. %// ~ /
Unit Type
Date ~
MOBILE LABORATORY DATA
Location.
Fuel/f/f/f
Test No.
Engr.
Capacity
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/ 3% O2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
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*
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18. Atnos. Temp. (°F/°C)
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12. NO (cold) read/3% O2 (ppm)*
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14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
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18. Atmos. Temp. (°F/°C)
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23.
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Location t
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1. Test No.
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17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
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346
Data Sheet 6002-2
-------
Test No
Unit No.
.///-
Date
MOBILE LABORATORY DATA
Location _
Test No.
Capacity
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18. Atnos. Temp. (°F/°C)
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347
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
~J ~r* Location o
Test No.
Engr.
Fuel >fig/- g/ff capacity
Unit Type £ Of? 0/^/0 CfCt-£ BUI
1. Test No.
2. Date
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5. Process Rate
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12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide {%)
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*
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16. Sulfur Dioxide (ppm) uncor/cor
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18. Atiros. Temp. (°F/°C)
19. Dew Point Temp. (0F/"C)
20. Atmos. Pressure (in. Hg)
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23.
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Data Sheet 6002-2
348
-------
Test No
Unit No.
MOBILE LABORATORY DATA
..0ff~<2- Date f~/~7& Location O
Test No.
Fuel/f/Vf
Capacity /,jT X
Unit Type &&r7#fiVf-ff C r£(.fr
1. Test No.
2. Date
3. Time
4. Load
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6. Flue Diam. or Size, ft
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9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 02 (ppm>*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°P/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
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28.
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349
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA
Test No.
Test No._
Unit No.
Date JT- /~
Location
f
Capacity
Unit Type £-P/'?*//V£P (2 T&££
1. Test No.
2. Date
3. Time
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10. NO (hot) read/3% O2 (ppm)*
11. NOj (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbqn Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
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350
Data Sheet 6002-2
-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
" f"_7£ Location
Test No.
Engr. /•/•$/* 5
Fuel //"/f £A$ Capacity /'$~ ><
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3?= 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
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35 1
Data Sheet 6002-2
-------
MOBILE LABORATORY DATA Test No.
Test No. Of 1 ~ 2-
Unit No.
Date o~ I'rv Location
Fuel/f^^ Grf£ Capacity /, 5
O Enar. ffn"^
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Burner Type
1. Test No.
2. Date
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6. Flue Diam. or Size, ft
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8. Oxygen (%)
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10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 03 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
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14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (eF/eC)
19. Dew Point Temp. (°F/*C)
20. Atmos. Pressure (in. He?)
21. Relative Humidity (%)
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Data Sheet 6002-2
-------
Test No
. ///-
Date
MOBILE LABORATORY DATA
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Location
Test No.
Engr.
Unit No.
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10. NO (hot) read/3% 02 (ppm)*
11. NOs (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
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14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
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353
Data Sheet 6002-2
-------
Test No
Unit No.
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MOBILE LABORATORY DATA
Date *""» "X* Location 0
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12. NO (cold) read/3% 02 (ppm)*
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14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
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18. Atmos. Temp. (°F/°C)
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Data Sheet 6002-2
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-------
Test No._
Unit No.
Date
MOBILE LABORATORY DATA
Location
Test No.
Engr.
Capacity /;
Unit Type ^frf f//V£ff C-T^f-^-
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1. Test No.
2. Date
3. Time
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9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO2 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atraos. Temp. (°F/°C)
19. Dew Point Temp. (°F/eC)
20. Atxnos. Pressure (in. Hg)
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Location
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capacity
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Burner Type
1. Test No.
2. Date
3. Time
4. Load X ft
5. Process Rate
6. Flue Diam. or Size, ft
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10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atitos. Temp. («F/°C)
19. Dew Point Temp. ("F/'c)
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1. Test No.
2. Date
3. Time
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6. Flue Diam. or Size, ft
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9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% O? (ppm)*
11. NO? (hot) read/3% Oa (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (•F/eC)
19. Dew Point Temp. (°F/dC)
20. Atnos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
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Data Sheet 6002-2
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-------
Test No..
Unit No.
Date
MOBILE LABORATORY DATA
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2. Date
3. Time
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6. Flue Diam. or Size, ft
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8. Oxygen (%)
9. NOx (hot) read/3% Q2 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
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-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HnO)
GT Inlet Pressure (" H_0)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" H»0)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
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-------
OPERATING DATA
LOCATION 8
8-7.
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" H^O)
- — 2 -- -"
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HJD)
** 2 f ' •
GT Inlet Pressure (" HJ3)
GT Inlet Temperature (°F)
GT Exhaust. Pressure (" H«O)
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36 1
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" H^O)
2 —
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" H?O)
GT Inlet Pressure (" H^O)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" HnO)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
O//-2-b e>-s
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/,*1 * /0*
f?60
/000
*i 7
5-5-,$-
J.-f
7^0
J2,#
fife
Y/
V^
c$ ^
tf'2-
2 & ^ f
3~%5~
7&0
-
27. f
V26
362
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HO)
GT Inlet Pressure (" H.,0)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" H_O)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
&//-Z-) ©-4-
#*- 7-7s~
/y; 00
/, 0% * W f
/?60
/t>1/0
Vf
VI
#5~
f
^75"
f1l
71*
3-7* )
t2 -7
/io\ fii\ Sirh foS £//?£ PJ5£l-/fiJ£
U2) QJJ LLQ) 19J
363
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HO)
GT Inlet Pressure (" HnO)
GT Inlet Temperature (°F)
GT Exhaust. Pressure (" H»0)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
OW- 2-) &-S
/- 7^ 7f
/^; ?- x /& ^
) 36"&
ffS
32r5~
61
i.t
//-Z-
M-0
?6 &?eg
2-S'*t
^£2-
®tjf\ MTl l£\ """"
y& \f3^. v2/
<2) (S) © (a)
364
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" H^O)
GT Inlet Pressure (" HnO)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" HjOJL
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (*F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
(#//--2r) B-£>
&- 3 ~ 7f
l£'/5~
/, *
f£~
yt>
#i
t.r
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" H^O)
GT Inlet Pressure (" H^O)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" H^O)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
G^/A-20 8-7
f-i^ •?*-
/0'?5~
/,/ x /#<"
*?
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
t*
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HO)
GT Inlet Pressure (" H^O)
m*
GT Inlet Temperature (°F)
GT Exhaust. Pressure (" HJD)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
(V//-^-) e-6
r- /- 7s
/ ^
}?
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr) j
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" H?0)
GT Inlet Pressure (" H^O)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" H_O)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
Gvv--2-) 8-/o
f--S- 7f
q:0#
/,#$ X f0 *
/7/V
/^^^
/f /
6-y.j-
/./ +1.3
6,3
tl
MS&
-1 7
11
#5^
1
272.
5~7
-------
OPERATING DATA
LOCATION 8
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" HO)
4*
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" H_O)
GT Inlet Pressure (" H_0)
GT Inlet Temperature (°F)
GT Exhaust. Pressure (" HnO)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
f^//-2-) e-/(
f-s-rr
/?'/f~
/,*? */fif
/y/*
/*&#
VI
Sf
i.r
t
/*
J700
<•/*
•fl
$1
1
2? y
rtt
?1*~
4il
27,*)
H2 f
369
-------
OPERATING DATA
LOCATION 8
)T.'V,.V"J.?
Test No.
Date
Time
Main Steam Flow (Ibs/hr)
Main Steam Pressure (psig)
Main Steam Temperature (°F)
Fuel Gas Flow (0-100%)
Air Flow (0-100%)
Oxygen (%)
Windbox Pressure (" H_O)
Burner Fuel Pressure (psig) for Gas
Feedwater Pressure (psig)
FD Fan Discharge Pressure (" HO)
GT Inlet Pressure (" HJ3)
GT Inlet Temperature (°F)
GT Exhaust Pressure (" H2O)
Windbox Temperature (°F)
Econ. Inlet Temperature (°F)
Econ. Outlet Temperature (°F)
GT Exhaust Temperature (°F)
Fuel Gas (Btu)
GT Load (MW)
Oil Flow (GPM)
Stack Temperature -48- (°F)
& / J "- 1
O / ^~ '
f^$-r -7^
/2-0C?
/. 0 3 »' /2-
£0
2.£~ -r 3. tf
e&
t.f
/
-------
LOCATION 8
FUEL GAS ANALYSES
Component Concentration
methane
ethane
propane
iso butane
n-butane
pentanes
C6+
ethene
propene
nitrogen
carbon dioxide
hydrogen
FUEL OIL ANALYSES
SPECIFIC GRAVITY, 60/60 F.
CARBON
HYDROGEN
OXYGEN
SULFUR
NITROGEN, PPM
VISCOSITY, SAY. UNIV. © 60°F.
HEAT OF COMBUSTION, BTU/LB (GROSS)
M « BTU/LB (NET)
77.65 mole*
1.89
.76
.16
.24
.03
.09
.67
.11
.28
.81
17.31
0.8756
80,14%
11.80%
7.93%
0.109%
171
43.2 sec.
19,697
18,482
37 1
-------
Test No.
Unit No. . 6,
PARTICULATEIBMISSJpN CALCULATIONS
- /-/ Oat«_£o.-T4_ Location
Test No. )?- /
Enar.ftt.lgAJ/AJg
Fuelfcgp.
Load
Pitot Factor, Fs
Barometric Pressure,
- 9
/
in. Hg
Tot. Liquid Collected, V
Velocity Head, AP
ml Total Particulate, M ft.? « gm
_iwg Stack Temp., Ts g iwg stack Gas Sp. Gravity, Cs / n.d.
Sample Time, 6 /ffO min Nozzle Diameter, Dn Ijtf in.
1. Sample Gas Volume Vm . . - 0.0334 Vm(P. + B/13.6)
sea oar
2. Water Vapor . V*tt& - 0.0474 V
3. Moisture Content Bwo - Eq. 2/(Bq. 1 + Eq. 2)
4. qoncentration a. C - 0.0154 Mn/Vm
std
b. C - 2.205 x 10"6 Mn/Vm
c. C - Eq. 4b x 16.018 x 10
*
5. Abs. Stack Press. Ps - P^._ x 13.6 + Psg
'std
3
6. Stack Gas Speed Vs - 174 Fs iTs x
7. Stack Gas Flow a. Qsw - Bq. 6 x As x x
Rate 6 70"F
22_
407
b. Qsd - Eq. 7a x (1. - Eq. 3)
ft. Material Flow Ms • Eq. 7b x Eq. 4b x 60
XO2f - 2090/(20.9 - XO.,%)
10. Emission a. E «• Eq. 4b x Fe x Eq. 9
9. XO_ factor
11. % Isokinetic
b. E - Eq. .4c x Fin x Eq. 9 x 1000
14077 x
J -
Vwgtfl)
0 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fa SC Meters/104 joules
Oil
92.2
0.002475
Gas
1>««W»
0.002346
Coal
98.2
0.002636
72. f£ SCF
_ SCF
N.D.
, ffO/98 grains/DSCF
///.
X/?
jf grams/DSCM
in. w abs.
ft/min
WSCF/min
DSCF/min
Ib/hr S
N.D.
lb/MMBtu^
ng/joule S
Data Sheet 6002-4
372
-------
Test No. &//-/
Unit No. £
PARTICULATE EMISSION CALCULATIONS
i**s,yt-eer rre/£
Date £?•?* ?£ Location,
Fuel
Test No.
, Engr
Load
/** X
Pitot Factor, Fs
Barometric Pressure, P.
in. Hg
Tot. Liquid Collected, V,
Velocity Head, AP »
bar-
jul Total Particulate, M .36.$ m
_iwg stack Temp., Ts &?£ °R Stack Area, As X£2' ft2
Sample Volume, Vm
ft
stack Press., Psg -'/j"iwg Excess Oj, XO.%
Orifice Press. Diff., H_
Sample Tine, 6
min
JLwg stack Gas Sp. Gravity, Gs /
Nozzle Diameter, Dn sfr in.
n.d.
1. Sample Gas Volume V»fitd - 0.0334 Vm(Pbftr + H/13.6)
2. Water Vapor
* °-0474 v
lc
3. Moisture Content Bwo - Eq. 2/(Eq. 1 + Eg. 2)
4. Concentration a. C - 0.0154 Mn/Vm
'std
3
std
b. C - 2.205 x 10"6 Mn/Vn
c. C - Eg. 4b x 16.018 x 10
5. Abs. Stack Press. Ps ~ Pbar x 13.6 -f Psg
6. Stack Gas Speed Vs • 774 Fs
l.OQ
Gs
7. Stack Gas Flow a. Qsw « Eg. 6 x As x |-^ x ^Ir
. Rate i 70«F Ts 407
b. Qsd « Eg. 7a x (1. - Eg. 3)
ft. Material Flow Ms - Eg. 7b x Eg. 4b x 60
9. K>2 factor »>2f - 2090/(20.9 - XD2%)
10. Emission a. E - Eg. 4b x Fe x Eg. 9
11. % Isokinetic
b. E - Eg. 4c x Fm x Eg. 9 x 1000
14077.3
I —
6 x Vs x Ps x Dn'
Fe SC Feet/104 Btu
Fm SC Meters/104 joules
Oil
92.2
0.002475
Gas
87.4
0.002346
Coal
98.2
0.002636
SCF
SCF
N.D.
grains/DSCF
'z grams/DSCM
in. w abs.
. / ft/min
WSCF/min
7 DSCF/min
10.8 / Ib/hr
///, 76 N.D.
'* Ib/MMBtu
ng/joule
Data Sheet 6002-4
373
-------
PARTICULATE EMISSION CALCULATIONS
Test Mo. W3- / Date $knL At) Location
*• I ' "*""
Unit No. fc» FuelQ/C £&.G • Load /.04~*/0*
Test No.Jjl/2- /
Eorix.f/d/VS %
Pitot Factor, Fs
Tot. Liquid Collected,
Barometric Pressure, P.
oar
^ ml Total Particulate,
Velocity Head, AP__/£___iwg Stack Temp., Ts
. ? 3- in. Hg
/// m gm
*R Stack Area, As
n.d.
Sample Volume, Vm %?.9frt3 Stack Press., Psg ".27 iwg Excess O2, X>2%_
Orifice Press. Diff., H I .35" iwg Stack Gas Sp. Gravity, Gs /.
Sample Time, 6 /SLp min Nozzle Diameter, Pn
+ H/13.6)
1. Sample Gas Volume Vmgta - 0.0334
2. Water Vapor Vw .. - 0.0474 V,
sta ic
3. Moisture Content Bwo = Eg. 2/(Eg. 1 + Eg. 2)
4. Concentration a. C «= 0.0154 Mn/Vm . .
8ta
b. C - 2.205 X 10~6 MnAm
c. C - Eg. 4b x 16.018 x 10
5. Abs. Stack Press. Ps = P._ x 13.6 4- Psg
6. Stack Gas Speed Vs * 174 Fs
std
3
7. Stack Gas Flow a. Qsw - Eg. 6 x As x •
Rate e 70°F
b. Qsd « Eg. 7a x (1. - Eg. 3)
&. Material Flow
10. Emission
11. \ Isokinctic
Ms - Eg. 7b x Eg. 4b x 60
a. E • Eg. 4b x Fe x Eg. 9
b. E » Eg. 4c x Fo x Eg. 9 x 1000
14077 x
6 x Vs x Ps x Dn
FeOsC Feet/104 Btu
Fm\)sC Meters/104 joules
Oil
92.2
0.002475
Gas
67.4
0.002346
Coal
98.2
0.002636
in.
90.
SCF
•00!
-------
Test No.
No.
Date
PARTICULATE EMISSION CALCULATIONS
/fcff/SfeS STie /*,.*'"
-f- 7£
Location_
^5. Load .
Test
Engr.
Pitot Factor, Fa
Barometric Pressure, P
bar-
_in. Hg
Tot. Liquid Collected, V^ 33<&>i>~ ml Total Particulate, M 7&~9S~ m ga
Velocity Head, AP /.0 iwg Stack Temp., Ts ?&£ *R Stack Area, As_,
Sample Volume, V
ft
Stack Press., Psg -»
Excess 0 , XO t
& .2
Orifice Press. Diff.,
Sample Time, 6
jlwg Stack Gas Sp. Gravity, Gs_
Bin Nozzle Diameter, Dn • ^g"
+ H/13.6)
n.d.
1. Sample Gas Volume Vn> td * 0.0334
2. Water Vapor Vt» . . - 0.0474 V,
std lc
3. Moisture Content Bwo - Eg. 2/(Eq. 1 + Eg. 2)
4. Concentration a. C « 0.0154 Mn/Vm
std
b. C - 2.205 x 10~6 Mn/Vm
c. C - Eg. 4b x 16.018 x 10
SCF
7 SCF
N.D.
grains/DSCF
std
3
S. Abs. Stack Press. Ps - P. x 13.6 + Psg
6. Stack Gas Speed Vs - 3 74 Fs /APTs 1^- x ^
7. Stack Gas Flow a. Qsw » Eg. 6 x As
Rate e 70°F
b. Qsd - Eg. 7a x (1. - Eg. 3}
&. Material Flow Ms - Eg. 7b x Eg. 4b x 60
9. X02 factor X>2f - 2090/(20.9 - X02%)
10. Emission a. E » Eg. 4b x Fe x Eg. 9
b. E - Eg. 4c x Fffl x Eg. 9 x 1000
11. % Zsokinetic
"Jr& ~* grams/DSCM
in. w abs.
ft/min
IffiCF/min
DSCF/min
•37.003 Ib/hr
I -
14077 x Ts(Vmgtd +
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fa SC Meters/104 joules
Oil
92.2
0.002475
Gas
67.4
0.002346
Coal
98.2
O.D02636
Data Sheet 6002-4
375
-------
Test Ho. —.-
Box No. /
PARTICULATE CALCULATION SHEET
location
Test Date
Test Description!
Dry Gas Meter Vol (ft3)
Impinqer Water Vol (ml)
378
-------
PARTICUIATE CALCULATION SHEET
Test No.
Box No. "
Test Descriptions & /
L-Jjtfl
Avg Qf
ot>.
Bottle No.
Cr
9
Probe
(Acetone)
Probe
(Water)
Flask
(Dry)
Jate
Weighed or
Final
Wt. 250
ZZ&
Zzz
fot.0
Avg_
Residue Wt .
Final 250 Tare)/
f*7
Date
Weighed or 650 Bake)
44^.
Final
Wt. 650
2*9**f
Aeff»isf
'/****
Residue Wt.
Final 650 Tare)
Comments:
.Off? If
.0033
.0016
.Oil 1
.fill
.b
-------
Date
Sample Box No.
Location %
K#/hr or MBtu/hr
/ Meter Box No.
K V B. INC.
STACK DATA
Unit NO.
Test No.
Engr
Fuel
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather CLoVfi Y - f/>*/
Stack
Abs.
Filter No.
j_ Probe No.
74*
Gas Pressure, Ps ~*/5" iwg
Stack Press., AP=P +407=
Stack Gas Sp. Gravity, 6s
Stack Area, As 7*23'
iwga
_Probe Length
Remarks
Final Meter;
Initial iMeter; ////.3f
_ 72.2-1
Time
1720
I7?0
l€20
ig?0
nzo
^--— '
'2*0H,
Total
Avg.
Vm
Meter
Volume
Reading
(CF)
////35~
1130*0
))W.tO
DM. 00
tltltf
'$
73-21
Vacuum.
Gage
Reading
(iwg)
5:3-
5:^
5;^
r.r
f.75"
35-0
3/0
3?*
3i*
310
&P
Pitot
Tube
Pressun
-------
Date
Location
K V B. INC.
STACK DATA
% Unit No.
Test No.
Engr. tf.
Fuel
GAS
Load/. 4?:? X lt>
Sample Box No.
Kf/hr or MBtu/hr
/ Meter Box No.
Filter No.
/ Probe No.
3_ Probe Length & */
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather £L0C>0
-------
Date
Location
K V B. INC.
STACK DATA
Unit NO.
Test No.
Enqr
Fuel
Load/. Kf/hr or MBtu/hr
Sample Box No. ^ Meter Box No.
Filter No.
J2. Probe No.
Probe Length
I
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter
Atmospheric Pressure
Weather tfer. HV/1/D i-irf .
Stack Gas Pressure, Ps -.27 iwg
Abs. Stack Press., AP=P +407= iwga
Stack Gas Sp. Gravity, 6s n.d.
Stack Area, As ifl ft2
12.
-*&- «~« diam-
>^ m.
,12- in.Hg
I
Remarks
Final Meter: 5TJ7, f/
Initial Meter: f 4*2-3. 7- 7
Time
.1117
113-0
1131
1/12.
//«
US'?
Total
Avg.
Vm
Meter
Volume
Beading
(CF)
r^j.0
100
)0Q
Ts«
60-13
11/20/75
380
-------
ANDERSEN CASCADE IMPACTOR DATA
Test No.
Location
Owner
Impactor No.
Stack Temperature f 7" 5"
Nozzle Size >y
_°F Impactor Flow Rate_
Filter No.
V -
CFM
.
Plate
Tare (q)
Final (g)
Net (g)
Cum. %
ECD (M)
tut
CO
00
, /f //
.mi
Back Oj?
Filter /
Data Sheet 6002-5
-------
LOCATION NO.
OWNER
DATE
PLUME OPACITY OBSERVATION RECORD
OBSERVER
Test Run No.
~~ '
CAPACITY
_ BOILER NO.
fSttr _
'-FUEL TYPE ff £ BURNER TYPE <7~
I,?*/* f klb/hr
POINT OF EMISSION
POINT OF OBSERVATION
TO
0f
TEST f/3.—)
No.
Tine
aa/pm
l/:0o
I}'**
I/-!'
H-'f
//:2t>
/I'-ir
l/'fr
tl*9f
//-vr
//'•?*
Type
V4 ^
^ ^
^ vi
- c
fc ^
^ 5$
Jp ^
^ s
«\
§ ^
^ $
W V.
^
^i
Test
Load
k#/hr
•
.
Opacity
%
•
WIND
Speed
nph
Direct
•
Sky
Cond
'
Sun
Posi-
tion
Comments
•
382
-------
Project:.
Datet
tocationt_
Onitt
Testt
Fu«l«
VELOCITY TRAVERSE
Test Description i__
. 2.. 1174
Stack Cross Section
Personnel:
Barometric Press, (in. Bg)s
Absolute Static Press, in Stack (in. Hg):_
Pitot Tuba Coefficient:
(P.)
(Cp)
- 8S.4B
1/2
Tine
Traverse Point
Port Depth
a"
*i
3£
If
£0
72.
#1
16
Velocity
Bead
(in. B20)
AP
.
-------
Projecti
Data. /a
Cone.
(% Dry)
6002-13
jff.
384
-------
Projects
Dates
Location:_
Bnlts
VELOCITY TRAVERSE
Te»t Descriptions
Stack Cross Section
Personnels
Test«_
Fnels_
Barometric Press, (in. Hg):_
Absolute Static Press, in Stack (in. Hg) s -21?.
Pitot Tube Coefficients
(P.)
1/2
Time
Traverse Point
Port Depth
12"
Zt"
?s"
it-
s'"
71''
ti"
K"
ft*
Velocity
Bead
(in. H20)
AP
//
i.*r
i.r
t.i
/,/
.t(
l.2f
}./
/.?
Gas Temp.
CF)
VjT?
Gas Tenp.
CR)
Ts
Molecular
Wt.
MS
Velocity
(ft/sec}
VS
°2
Cone.
(» Dry)
I.f7
6002-13
385
-------
Project i _
Patet
Locationi_
Pniti
Testi. _
Fuel i
VELOCITY TRAVERSE
Tert Descriptiont
Stack Cross Section
Personnel:
Barometric Press. (In. Hg)« _
Absolute Static Press, in Stack (in. Rg)s_
Pitot Tube Coef ficienti _ _
CP.)
vs - es.48
1/2
Tine
Traverse Point
Port Depth
12"
2V"
K"
i*"
f*"
71*
*Y'
V"
10!"
Velocity
Head
(in. H,0)
AP
/.$-
),7
l<3~
,ff
,£f
.i
,tt
.
-------
ROTARY KILN DESIGN DATA
Location Ho.
Unit No. /
Unit Description
Installation Date
Process Capacity
Burner Description
Test Fuel
Combustion Air
Temperature at Burner
Length of Kiln
Diameter of Kiln
If S3- :
$,f £ * /O > *?/V*y (jOO +o*-S/dJ
//^^ #t/tffl£'£
A/, G,
W-1S* ?
*1f~0 ft
12 ft
Comments:
387
-------
Test No._
Unit No.
MOBILE LABORATORY DATA
Date &'//" 7£ Location _ Y_
5" Capacity _
Test No
Engr.
Fuel
Onit Type K/l
Burner Type
1. Test No.
2. Date
3 . Time
4. Load To
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) un cor /cor
*
15. Hydrocarbon (ppm) unoor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (0F/°C)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
^/
$~//~7t
5
£.
I?o0
1725
ft
5
o.et.o.
-•— -
!7f2-
////
3 (
2
/e
&
*-
>1/
//
0
75"
75~~
^<7r & e
*/&
72-0
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
1
Data Sheet 6002-2
"^
§ V
V
5
-------
Test No. 7 ' 3~
Unit No.
Unit Type K J L ^
MOBILE LABORATORY DATA
Date ?J/2 "?£ Location 1
Fuel £<1~5 Caoacity
Burner Type S/ft (y£~£ £,
fs & r&
Test No.
Engr. //^ *
+ $
tf) (T>
1. Test No.
2. Date
3. Time
4. Load 9e>
S. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oz (ppm)*
10. NO (hot) read/3% 02 (ppm)*
LI. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29. CCflg. j/Jt T£rtP
30.
f'Z
f'&~7f
0i/r
?3
s.
7f&
£37
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1*7$
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2-0
0,0,0
0
100
$21
7.5~
WO
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77
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100
127
0
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7$
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23
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73
30,00
£2.
100
f-j?
t- M-7S
"fr-0
%3
f,
>&•*
(475
/ "/"
*Correction to 3% 02 should not be performed if
the value is measured on a wet basj-
Data Sheet 6002-2
Sf 3
vo
5"
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
2- Date $'t3'7£ Location
£
Fuel
Capacity
Unit Type
Burner Type
Test No.
Engr.
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
f-2-
$'/?-%
!03
-------
Test No
Unit No.
MOBILE LABORATORY DATA Test No.
1-3 Date 1-2?-7i
Fuel GA ^
KH*>
' ^!
Location 7 Engr. ti/^f/y
Capacity
Burner Type Z/M&t't
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% O? (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3?» 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atiros. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
7-
?
?v7
/
5~e
IC75~
/7.
2$
V-/T
$~
/
—
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2*?.$^
7-
t **-
3
4 - ;;'/
f:v o^r
/.
770
15
2-*!
*r
,3-
•
*Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
-------
Test No.
Unit No.
"
MOBILE LABORATORY DATA
Date*?' 4<'' '•>•' Location £_
Fuel 6.'-7 ..•>' Capacity
Test No.
Unit Type Ax Y -V
Burner Type
1. Test No.
2. Date
3 . Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
f~
- P
/ ,/'
'#&
/.
IS?
20
7f>0
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6
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5
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V7
fct
i.
r*"
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ye/
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6
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5
'/
V 7S
' ,' 9
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f
•*"i m,
_.
ft?
2-
yf
...
+Mt*^
&
~/
.?.$
/
•
^Correction to 3% 02 should not be performed if
the value is measured on a wet basis.
Data Sheet 6002-2
392
-------
MOBILE LABORATORY DATA Test No.
f- <"
-^
Unit No.
Unit Type XV 7-*
If or uttf >* *
Date /0fV(7£
Fuel M, £.
If > .*'// AJ
aNV.ec-t i re ktt-fi
Location ( Engr. ^C/ CrfXTf •
Capacity
Burner Type
f)~ fC/P //H-'/1 7? StS 0tyf>j/~ X
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 03 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atnos. Temp. (°F/eC)
19. Dew Point Temp. (°F/eC)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
f-jT/f
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7
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f
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o
q-fc
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(0751331
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3 3
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-
*Correction to 3% O2 should not be performed if
the value is measured on a wet basis.
3 9 o ^ ii- M\
Data Sheet 6002-2
-------
Test No. 7 " ?
Unit No.
MOBILE LABORATORY DATA
Date IP--1'7f Location f_
Fuel M v> Capacity
Test
Engr.
Unit Type
Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 63 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
#
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (eF/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
1'fff
#-¥'?{
HYf
71"* ft"
fsr /#
4C
fo$P
fo2£
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7
1171
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I7tf
f
i^
?t
22
7f
£3
21.70
6f%>
V-* P
/0-f-7{
tjf-f
fsr 0t<)
Data Sheet 6002-2
-------
Test No.
Unit No.
MOBILE LABORATORY DATA
Date l0~5~-7f Location
Test No.^
Engr. **j
Fuel
// (£„
Capacity_
Unit Type
Burner Type_
1. Test No.
2. Date
3. Time
'4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
f'^
!£>'$"- ft
lief
/*"/*/
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si
66
J-1,78
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1-{ A
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£$? /y
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ecs
0
77
& T'
*3 £ & yj?
£
-------
Test No._
Unit No.
Dnit Type
Date
MOBILE LABORATORY DATA
Location
Fuel AJ,
Y
Test No..
Engr. M
Capacity
Burner Type_
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% Oj (ppm)*
10. NO (hot) read/3% 03 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atmos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
1-e c.
/6-r-7f
te/tr
f$r /t*
1' ?
lew
1*r
WO
17-
36
#*
£>
H71
/031
167?
3.
ft
$1
£>
f -<<• c
/0'S~'76
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ftr t>»r
7.
— -
—
lot?
/<•
22
/5~
#
f
Iff?
0
12-
2*
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/°/f/7S
/720
fsr /*>
f~,0
g?r
%&>
1200
'$
ie
i*
3*1
1&
I3?0
*f
ft
f - #sr
£.S
—
— -
$?o
//
1*
If
e
fe>£2
• Z
f~0
yy
£>
76
£7
Z-^Z?
63%
*Correction to 3% O2 should not be performed if
the value is measured on a wetJjasis.
Data Sheet 6002-2
-------
Test No. I °
Unit No.
•
Unit Type fifftf.C
MOBILE LABORATORY DATA Test No.
Date fffr5/7£ Location ^ Engr. W. £*/?/>•'.';>
Fuel /^v v, Capacity
Y /f///v Burner Type
1. Test No.
2. Date
3. Time
4. Load
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
8. Oxygen (%)
9. NOx (hot) read/3% 02 (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO5 (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% 02 (ppm)*
13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
*
15. Hydrocarbon (ppm) uncor/cor
16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. A twos. Temp. (°F/°C)
19. Dew Point Temp. (°F/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
1-( £.
fe/f/K
fsf /fl>
V'*
7f'0
#v-
tot?
/?.
if
"}0
2-0
?
*?1
7ft
fetf
£
ft
32-
3-1
3-6 £
fe/f?rs
&f w
£,
.....
_
fte
//.
ft
—
. —
0
tew
f
US'
—
.--
74
f
-------
OPERATING DATA
LOCATION 9
Test No. II (fj/ Time: f£/• v
-------
OPERATING DATA
LOCATION 9
Test No.
?'/
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
'Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID pamper position % open
Pressures
ID Draft "H20
Grate Press. "I^O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O
Time:
//
J
DATE:
75"
, 5"
399
-------
OPERATING DATA
LOCATION 9
. f' / (?) Time, 3.--10 ft* n^. /W. //
Pressures
Test No
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH &3' >/ J 5~ /
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F _ / 2^2 &
Kiln Gas Temp. , Chains °F _ X Y 7 ^
Comb. Air Temp. °F _ / 3 &
Kiln ID intake temp. °F _
Gas Flow % _ _
Cooler Speed %/RPM _ ^ '/ / / % *•>
ID Damper position % open _
ID Draft "H20
Grate Press. "H2O &• I
Hood Press. "H20 ~
Fuel Gas Supply Press,PSIG Q 7>
1 &
Burner Gas Press, PSIG .X o
Vent. Damper pos. % open
Control Room 02 rr 0
400
-------
OPERATING DATA
LOCATION 9
Test NO.
Kiln Speed, %/KPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Time:
DATE
4 0 1
-------
OPERATING DATA
LOCATION 9
Test No. ("2 l«V Time: 7'^cx DATE
Pressures
ID Draft "H2O
Grate Press. "I
Hood Press. "H20
Fuel Gas Supply Press,PSIG
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH &3
Temperatures
Kiln Temp. °F 2-
Kiln Feed end Temp. °F 3 2~
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM ?# /13' ~?
ID Damper position % open
Burner Gas Press, PSIG ^ 7* &
Vent. Damper pos. % open
Control Room Oo
Z)
402
-------
OPERATING DATA
LOCATION 9
Time: // : /5~~
Test No. / •*- 'Ox Time: // - / > DATE:
Knn Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O &r f
Hood Press. "H20
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG 2- /*
Vent. Damper pos. % open •**•"
Control Room 02 * f ~^
///e
403
-------
OPERATING DATA
LOCATION 9
Test »o
.
-------
OPERATING DATA
LOCATION 9
Test NO.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H20
Grate Press. "HgO
Hood Press. "H20
Fuel Gas Supply Press,PSIG
Burner Gas Press/ PSIG
Vent. Damper pos. % open
Control Room Oj
Time:
DATE.
405
-------
OPERATING DATA
LOCATION 9
Test NO.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Time:
DATE:
7/0
X /
406
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H26
Grate Press. "I^O
Hood Press. "^O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room 03
Time:
DATE:
407
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperature s
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2b
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room 02
££-.
Time:
£/*ck
I
DATE:
(OZO
37
bo
S.O
yr
408
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/BPH
Kiln Feeder Speed, %/BPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "^O
Hood Press. "H2O
Fuel Gas Supply Press, PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Boom
6-4$
Time:
t
-------
OPERATING DATA
LOCATION 9
7~V
Test No. V" Time:
7 %
3 ^;^K
Kiln Speed, %/RPH 97/ // V
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow % ~^TJ
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O £>
Grate Press. "H2O 7_
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
4 1 0
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Time: AS"3 7
DATE:
3/0
n
1-0
4 1 1
-------
OPERATING DATA
LOCATION 9
Test No.
1-
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Time:
I LOO
HATE
- /^>3
4 1 2
-------
OPERATING DATA
LOCATION 9
Test No.
(£
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H20
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room 02
Time:
?/
1320
33
3?
•V.3
A/'
DATE:
4 1 3
-------
OPERATING DATA
LOCATION 9
Test No
. 1 "
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
r
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Time:
DATE:
^270
Id It
4 1 4
-------
OPERATING DATA
LOCATION 9
Grate Press. "^O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room O2
Test NO. f~S> Time: ^^6/7 DATE
/
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O V"S>
4 1 5
-------
OPERATING DATA
LOCATION 9
Test NO.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. PP
Kiln. Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H20
Grate Press. "H2O
Hood Press. "H2b
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room 02
Time:
(010
To,
-o*» y
Al
DATE:
4 1 6
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "^O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room 02
- 79
a
Time: -1*111*
#$"00
to
6*0
o.oy
DATE:
-------
OPERATING DATA
LOCATION 9
Test No.
Kiln Speed, %/RPH
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °P
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Ccanb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/RPM
ID Damper position % open
Pressures
ID Draft "H20
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room Oo
Time:
78
DATE:
X/3
4 18
-------
OPERATING DATA
LOCATION 9
Test NO. 4-L Time: I 7/0 DATE: /d - F~ 7L
Kiln Speed, %/KPH ^^ ///JI
Kiln Feeder Speed, %/RPH
Temperatures
Kiln Temp. °F
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F
Kiln ID intake temp. °F
Gas Flow %
Cooler Speed %/KPM / ^Y
ID Damper position % open YO
Pressures
ID Draft "H2O
Grate Press. "H2O
Hood Press. "H2O
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open J
Control Room O2 O* /
TTf
-------
OPERATING DATA
LOCATION 9
*2l
Grate Press.
Hood Press. "H2b
Fuel Gas Supply Press,PSIG
Burner Gas Press, PSIG
Vent. Damper pos. % open
Control Room Oo
Test No. / Vg Time: _ I '1™ DATE:
Kiln Speed, %/RPH _
Kiln Feeder Speed, %/HPH _
Temperatures
Kiln Temp. °F _
Kiln Feed end Temp. °F
Kiln Gas Temp., Chains °F
Comb. Air Temp. °F _
Kiln ID intake temp. °F _
Gas Flow %
Cooler Speed %/RPM _
ID Damper position % open
Pressures
420
-------
LOCATION 9
FUEL GAS CHROMATOGRAPHIC ANALYSIS
V»VJIX^ 1 I 1 VC.I* 1
HELIUM
CARBON DIOXIDE
OXYGEN
NITROGEN
.METHANE
ETHANE
PROPANE
ISOBUTANE
N- BUTANE
ISOPENTANE
. N-PENTANE
I HEXANES+
*
TOTALS
1 IUL. A
0.01
1.00
0.0
0.78
96.44
1.32
0.27
0.03
0.04
- 0.01
0.01
0.09
1 00. 00
i- - - !
uHU/riur
*****
*****
*****
*****
*****
0.35
0.07
0.01
0.01
0.0
0.0
0.04
-
0.48
,1
TOTAL GAL/MCF, W/0 ETHANE = 0.13
CALCULATED SPECIFIC GRAVITY = 0.580
CALCULATED INTERCHANGE FAC. = 1312.
HYDROGEN SULFIOE = NO
CALORIMETER BTU = 999 ,
CALCULATED BTU = 999,
42 1
-------
LOCATION 9
FUEL GAS CHROMATOGRAPHIC ANALYSIS
CHROMATOGRAPH
ANALYSIS! MOL # GPM @ \lj .fa ps |A
CARBON DIOXIDE 0.10
NITROGEN 0^88
METHANE 95.64
ETHANE 2.0V
PROPANE o!?0 0.192
ISO-BUTANE 0.15 0.0%
N-BUTANE 0.21 0.066
ISO-PENTANE Q.06 0.022
N-PENTANE O.06 0.022
HEXANES PLUS p. 16 . 0.0.68
100.00 0.419
SPECIFIC GRAVITY @ 60° F. (AIR = 0 0.5891
B.T.U./cu. FT. @ 1^.696 PSIA AND 60°F.:
DRY BASIS IOHH
WET BASIS 1026
422
-------
Test Mo. */ £&•»*
/
Fuel 4/. & . Load 0 & ^£>
• g& Barometric Pressure, P. *"^f*
• - - - JLNU.
Tot. Liquid Collected, V. /30 ml Total Particulate, M ^.
Test No.
e*>? Engr. /&.
7 in. Hg
&#. if m gm
f-/
*•
Velocity Head, AP .02f - 2090/(20.9 - »D,%)
a. E - Eq. 4b x/fe*>c Eq. 9
b. E - Eq. 4c x Fm x Eq. 9 x 1000
14077 x Ts(Vm
std
6 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/10 joules
Oil
92.2
0. 002475
Gas
87.4
0.002346
Coal
98.2
0.002636
; S/*r *•»*>
/<»' f-S *
c r
Excess 0 , XO %
Gs /*?.? n.a.
." in.-
_ SCF
SCF
grains/DSCP
Ib/DSCF
grams/DSCM
in. w abs.
ft/min
3~Tt2Z. WSCF/min
DSCF/min
i?.386*K>3 Ib/hr
M.D.
Ib/MMBtu
'ng/joule
Data Sheet 6002-4
423
-------
Test No..
Unit No.
Date_
Fuel
PARTI
rt
-/s
R EMISSION CALCULATIONS
tV*f*. f .
Location
load
Pi tot Factor, Fs
Tot. Liquid Collected,
._
1C
Barometric Pressure, P. ?£ && in. Bg
bai ' .' '
ml Total Particulate, M_ t$7/<0. 3 n gm
Velocity Head, flP -09 iwa Stack Temp. » T«
*» Stack Area, As ftf"" ft2
Sample Volume, Vm 7.f3 ft3 Stack Press., Psg "^ f! Li*9 Excess Oj, «>2%
Orifice Press. Diff., H_
Sample Tine, 6 /A"
£2 iwg Stack Gas Sp. Gravity, Gs_
min Nozzle Diameter, Dn
+ H/13.6)
1. Sample Gas Volume Vm>td - 0.0334 Vm(P
2. Water Vapor ^td ™ °'0474 vi
3. Moisture Content Bwo • Eq. 2/(Eq. 1 + Eq. 2)
4. concentration a. C • 0.0154 Mn/Vm
std
b. C - 2.205 x 10"6 Mn/Vm
c. C - Eq. 4b x 16.018 x 10
'std
3
5. Abs. Stack Press. Ps - Pfaar x 13.6 + Psg
6. Stack Gas Speed Vs - 174 Fs
' Bq. 6 x As x
7. Stack Gas Flow a.
Rate • 70*F
b. Qsd • Eq. 7a x (1. - Eq. 3)
e. Material Flow
Ms - Bq. 7b x Eq. 4b x 60
9. XO, factor XO.f - 2090/(20.9 - XO.%)
10. Emission
11. % Isokinetic
"H* — s»^r7%r/ ^*w* 9 «•»*—^
a. B - Eq. 4b x Fe x Bq. 9
b. E • Eq. 4e x Fn x Bq. 9 x 1000 ' )(0
I "°77 * *<*»td * W.td>
6 x Vs x Ps x On2
Fe 6C Feet/104 Btu
Fn SC MeUrs/104 joules
Oil
92.2
0.002475
Gas
J^T
f
0.002346
Coal
98.2
0.002636
( iM*G VrUtV-
n.d.
SCF
SCF
N.D.
grains/DSCF
grams/DSCM
in. w abs.
f t/min
KSCF/min
DSCF/min
N.D.
ng/joule
Sheet 6002-4
424
-------
Test MO.
PARTICUIATE EMISSION
. Date IT/It/It* location
Vest Mo
,Engr
Onlt Mo. /
Pitot P»ctor. Fs_
Barometric Pressure, P
. f fr in.
lot. Liquid Collected,
<
Velocity Bead, If £
Sasple Voluee, Vm_
• ** *»tal Particolate,- M^ff75.7 m gm
JLwg Stack Hasp., Ts "770 *R Stack Area, As 4$
,.3
Stack Press.. Psq ^
Excess O , ao % »
2
%
Orifice Press. Diff., H_
Sasple
•in
_iwg Stack Gas Sp. Gravity, Gs
Norzle Diameter, Dn 4 *IM g4».
n.d.
1. Sasple Gas Vbluse ^"^ - 0.0334 '•'ff^
^ q/13.6)
2. Mater 'Vapor Wstd " °-°*7* vic
3. Moisture Content Bwo - Bq. 2/(Bq. 1 «*• Bq. 2)
4. Concentration a. C - 0.0154
std
b. C - 2.205 x 10~6 Mn/Vsj^^
sta
C. C - Bq. 4b x 16.018 x 103
SCP
SCF
grains/DSCP
Ib/DSCP
2V.
5. JUbs. Stack Press. Ps - PJ)&r x 13.6+Psg
6. Stack Gas Speed Vs « 174 Ps /Sis"/~
v vs
7. Stack Gas Plow a. Osw - Bq. 6 x As x
Bate t 70*P
b. Q»d » Bq. 7a x (1. - Bq. 3)
8. Material Plow Ms « Bq. 7b x Bq. 4b x 60
Gs
530 Ps
fc 407
9.
10.
factor
2090/C20.9 -
ion a. B « Bq. 4b x Pe x Bq. 9
11. % Isokinetic
b. B - Bq. 4c x Psi x Bq. 9 x 1000
14O77 x IfcOffc-ta + *W
I- .
6 x Vs x Ps x Dn
WSCP/ndn
£06 40- PSCFAdn
ib/hr
M.D.
Ib/MMBtu
ng/joule
Pe 6C Peet/104 Btn
Pa SC Jteters/10 joules
Oil
92.2
O. 002475
Gas
87.4
0.002346
Coal
98.2
0.002636
60%
Data Sheet 6002-4
425
-------
Test HO. f -
Unit No.
/
PARTICULATE EMISSION CALCULATIONS
/**•/*. rf~
Date #-/?-?£ Location ^<<
• ~
fuel J/, &.
Pitot Factor, Fs
Barometric Pressure, P
Tot. Liquid Collected, V.
nl Total Particulate, M_
JLn. Hg
'n gm
Velocity Head, AP . /t? iwg Stack Temp., Ts 73~o *R Stack Area, As.
Sample Volume, Vat 7. 9£ ft3 Stack Press., Psg - £, 9 iwg Excess O,, X0,%
2 2
Orifice Press. Diff., H »ff iwg Stack Gas Sp. Gravity, Gs /,&J n.d.
Sample Time, 6 /^~ nin Nozzle Diameter, Dn ,S7S~ in.
H/13.6)
ft
1. Sanple Gas Volume Vmgta - 0.0334 Vm(P
2. Hater Vapor
Vw
std
0.0474 V.
3. Moisture Content Bwo - Eq. 2/(Eq. 1 4- Eq. 2)
4. Concentration a. C - 0.0154 Mn/VD ^.
std
b. C - 2.205 x 10~6 Mn/V» ^M
sta
c. C - Eq. 4b x 16.016 X 103
5. Abs. Stack Press. Ps • P x 13.6 + Psg
6. Stack Gas Speed Vs - 174 Ps /Spis" /~ x ^29.
7. Stack Gas Flow a. Qsw • Eq. 6 x As x
Rate i 70»F
b. Qsd - Eq. 7a x (1. - Bq. 3)
6. Material Flow
9. X0_ factor
10. Emission
11. % Isokinetic
Ms - Eq. 7b x Bq. 4b x 60
»2* - 2090/(20.9 - *>2%)
a. E - Eq. 4b x Fe x Eq. 9
b. E - Eq. 4c x Fa.x Bq. 9 x 1000
14077 :
I
6 x Vs x Ps x Dn"
Fe SC Feet/104 Btu
Fn SC Meters/104 joules
Oil
92.2
0.002475
Gas
^««t"~\
0.002346
Coal
98.2
O. 002636
~3
SCF
SCF
N.D.
grains/DSCF
Ib/DSCF
grams/DSCM
in. w abs.
ft/min
HSCF/min
DSCF/min
. K.D.
Ib/MMBtu
ng/joule
Data Sheet 6002-4
426
-------
Test No.
PARTICULATE EMISSION CALCULATIONS
f7*cS,f. /71s/U . A'
Date g-/?-7£ Location ^,/ y Sra*t
ttait Mo.
Fuel
Load
Pi tot Factor, Fs
Barometric Pressure, P
bar-
mi Total Particulate,
in. Hg
m gm
Tot. Liquid Collected, V.
Velocity Head, AP . /Z iwg Stack Temp., Ts /V~0 "R Stack Area, As
Sample Volume, Vm 7.J2 ft3 Stack Press., Peg -g. ? iwg
Orifice Press. Diff., H ,£~9 iwg Stack Gas Sp. Gravity,
Sample Time, 6 /A" ain Nozzle Diameter, Dn
~ ft2
Excess O_, XO,%
2 2
1. Sample Gas Volume Vmgtd - 0.0334 Vm(P + H/13.6)
2. Water Vapor ^td " °'0474 vic
3. Moisture Content Bwo - Eq. 2/(Eq. 1 + Eq. 2)
4. Concentration a. C » 0.0154 Mn/Vm
std
b. C - 2.205 x 10~6 MnA»
C. C - Eq. 4b x 16.018 X 10
5. Abs. Stack Press. Ps - Pbar x 13.6 + Psg
std
3
6. Stack Gas Speed Vs - 174 Fs
7. Stack Gas Flow a. Qsw - Eq. 6 x As x x r-
Rate t 70»F M 407
b. Qsd - Eq. 7a x (1. - Eq. 3)
a. Material Flow
9. XO factor
10. Emission
11. t Isokinetic
Ms " Eq. 7b x Eq. 4b X 60
XO2* - 2090/(20.9 - X02%)
a. B - Eq. 4b x Fe x Eq. 9
b. E - Eq. 4c x Fm x Eq. 9 X 1000
X -
8 x Vs x Ps x Dn
Fe SC Feet/104 Btu
Fm SC Meters/10 joules
Oil
92.2
0.002475
Gas 1
Coal
_*»*<~>J 98.2
0.002346 j
0.002636
Gs /&3 n. d.
in.
. SCF
SCF
grains/OSCF
grams/DSCM
in. w abs.
/377, 98 ft/min
WSCF/min
{366?. 6 DSCF/min
Ib/hr
M.D.
lb/MMBtu
. 70 ng/joule
Data Sheet 6002-4
427
-------
PARTICUIATE CMjCUIATION SHEET
Test Mo. Q-f
Box Mo.
(Inlet, Outlet)
location
Test Date
Test Description:
.r C?g«
g///7£
g«* g
-------
PARTICU1ATE CALCUIAT1ON SHEET
Test No. T-ot
Box No.
Test Description^
(Inlet, Outlet)
Dry Gas Meter Vol (ftS)
initial
Total
. a.
/ A6.JT
Final
Jtaitial
A Vol
Impinger Water Vol (ml)
joe
-4?
Total
3 22
A.OO
V » i
Beaker Ho.
9
Filter
HO.
Blank
No.
Tar7
Wt.
...1W
9S.9srt
tf, *fgff
Vf,*?V7
SSL
rr.
100 . 4S/X
Bottle Ho.
^
Content
Final 1_
Wt. 250 2
.9373
l&l,
.t,b
-------
Date
Load
Location
KVB. INC.
STACK DATA
Unit No.
Test
Fuel
__JLLZ£__**/hr or MBtu/hr Filter No. J
Sample Box No. / Meter Box No. / Probe No. / Probe Length
y
Filter Heater Setting
Probe Heater Setting
Stack Moisture eft.
Ambient Temperature gy_ °F
Nozzle Diameter 3/g in.
Atmospheric Pressure—-jZf.yf in.Hg
Weather //7£" M*
PW,M>
1137.00
W1. &
Vacuum
Gage
Reading
(iwg)
/
f,7f
7.0*
7.0
ft?
Pitot
Tube
Pressuri
(iwg)
.01
, °F
°F
+ 460
Impinger
Temperature
Out
(°F)
7T
7f
75~
72-
In
(°F)
200
22-6
2^0
2£0
Filter
Box
Temp.
(°F)
?0#
2$C
3/0
?2&
Meter
Temp.
(°P)
*75
-------
Date pfll/rf Location
Load Kf/hr or MBt
Sample Box No. ( Meter B
Filter Heater Setting 7
Probe Heater Setting J
Stack Moisture *~ /5~_
Ambient Temperature
Nozzle Diameter ^fr
Atmospheric Pressure .2f,/f
Weather CL eWS Her fJU/ilO
Stack Gas Pressure, Ps -£.*/
Abs. Stack Press., AP=P +40*3
Stack Gas Sp. Gravity, Ss //^
Stack Area, As t/J^
KVB. INC. Test No. 1-2-
STACK HATA En^r • M- BVfMiriG
Y Unit No. Fuel /^' ($,
u/hr Fi
ox No. [
. I
Op
. diam.
in.
in.Hg ,
= iwga
/_n.d.
Iter No. 1 ///fX/K 5"
Probe No. / Probe Length H
r^\
v^_j^4
Remarks
Final Meter: lliy.ff
Initial Meter: 13^3- '2*i
7. YZ
^ A^/i^ s^
wJ*
Time
1031
\oHH
wit
ufi-
/r
Total
Avg.
/fc*A
Vm
Meter
Volume
Beading
(CF)
IM2.2i
IWS.06
IW1.00
/5Y?,//
? /^
Vacuum.
Gage
Reading
(iwg)
f.5~
5"x5"
r,r
*rtP. '
&p
Pi tot
Tube
Pressuri
(iwg)
.12-
,12
J2-
C
H
Orfice
Pressure
s Diff
/£"?
-------
Date
Load
Sample Box No.
Location /
K#/hr or MBtu/hr
/ Meter Box No.
KVB, INC.
STACK DATA
Unit No.
Test No.
Engr .
Fuel
Filter No.
/ _ Probe No.
/
Filter Heater Setting
Probe Heater Setting
Stack Moisture ^35* %
Ambient Temperature J?JT °F
Nozzle Diameter */W^ &«-.
Atmospheric Pressure 2-ff0 ^
>. •?
ftp
Pitot
Tube
Pressun
(iwg)
,0^
^ PLUG>
H
Orf ice
Pressure
s Diff
,0f
6&P
Stack
Temp.
310
3to°?
°F
+ 460
770
Impinger
Temperature
Out
100
°R
In
I2&"
Filter
Box
Temp.
/20
Meter
Temp.
l/g~
60-13
11/20/75
432
-------
Test No.
CASCADE IMPACTOR DATA SHEET
TEST RUN HO.
IMPACTOR MO.
f " f
TOCATION
DATE
CYCLONE NO.
OPERATOR
SAMPLE POINT LOCATION
SUBSTRATE COATING
AV^- ' ' •" > T. *
IMPACTOR ORIENTATION
FLOE STATIC PRESSORE
NOZZLE D1A.
FUEL /(/ r 6> , TEST LOAD o 7 f
FLOW RATE
/ /
CFM
AMBIENT TEMPERATURE
tf 2
PRESSORE
Pi Bg. HUMIDITY
FLUE GAS MOLECULAR WT.
, TEMP.
*F, DENSITY
g/cc,VISCOSITY
POISE
Foil + Sample, g
Unused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
•
Stage number
1
*JtW
1,0 U1
,2035
,lot$
2
Wit
?.fV*
.0171
SW
3
1,1*1
1,075%
.wtl
SHI
4
?ff7*f
?.**'?'
.*&?
,O}&3
5
W12
H,I7£5
,0V £7
,0&$ 7
Stage
Blank
FILTER NO.
Sample Blank
FULL CONTAINER, g
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
BLANK, g
FINAL SAMPLE, g
.U/ff
1.22*0
EMPTY CONTAINER, g
CYCLONE CATCH, g
7
60-20
-------
TABLE 1.
Static pressure at inlet to
impactor, atm.
Density of aerosol particle, grams/cc
Density of gas at inlet sampling
conditions, grams/cc
Molecular weight of sample gas
Molecular weight of calibration gas
Temperature of gas at sampling
conditions, °K
Temperature of gas at calibration
conditions, °K
Static pressure under calibration
conditions, atm.
Gas viscosity at sampling conditions,
poises
Stage jet diameter, cm
V
Sample quantity collected on each cup
v
"4
R5
Dimension conversion constant
*'4 f' /
\K\PAvCTo
Pressure drop across impactor
during test "Hg"
Symbol
AP0
Value
I.S3
2- /
127
I,*
203.?
f.
434
-------
TABLE 2.
Effective pressure drop, "Kg"
Inlet flow to impactor, cc/second
Pressure out of stages, atm.
Density of gas out of the various
stages , grams/cc
Characteristic diameter, microns
Symbol Value
APE A'/f
*»„ #, 33
j; . ,. ., . .1. .1 —
P 0 *? ' f
s, •" L -
P fit tf ^
SA '
?„
*• ** f ^ f ^^
P? /,72 ^/^"J
D"6 ;> , /; .
D / ^ & ^
D*"4 ^. S~f
. **??
Criteria for validity of equation 18
Mean free path
Average molecular velocity
PC. x
o
L
V
7,17
435
Continued
-------
TABLE 2 (Continued)
Symbol Value
% on a cup of the total sample collected
Stage 2 Y, 70'
3 Y. 16'?
4
_J^
6 Y^ 3~ 0
Filter Y7
n.
3.0
436
Total 100.00*
*Any discrepancy due to rounding off should be buried 10 O
in the largest Y cumulative % smaller than D
-------
Date
Load
Location f
K V B. INC.
STACK DATA
Unit No.
Test No. "
Engr.//..
Fuel
£ V&ftte or MBtu/hr Filter No. ,
Sample Box No. ( Meter Box No. { Probe No.
Probe Length ( ^C ' f
I
diam.
Filter Heater Setting
Probe Heater Setting
Stack Moisture
Ambient Temperature
Nozzle Diameter *
Atmospheric Pressure 3.1.g7 in.Hg .
Weather eioiSDi' Her T
Stack Gas Pressure, Ps -£. 3 iwg |
Abs. Stack Press., AP=P +407=Y^,7iwga
Stack Gas Sp. Gravity, 6s 1.03 n.d.
Stack Area, As V3" ft2
Remarks
Final Meter;
Initial Meter: / 3 V f .
Time
H^o
j/fi
i
i
Total
Avg.
f££
Vm
Meter
Volume
Beading
(CF)
//yf,/f
lisv. li
?ff£
Vacuum.
Gage
Reading
(iwg)
-7/
2-1
^S
ftp
Pitot
Tube
Pressun
(iwg)
,13-
^ Pl>V(>
•
H
Orfice
Pressure
s Diff
x^^"
&gp
Stack
Temp.
300
°F
°F
+ 460
Impinger
Temperature
Out
1&
In
- —
^
Filter
Box
Temp.
Meter
Temp.
1/0
60-13
11/20/75
437
-------
Test No.
CASCADE IMPACTOR DATA SHEET
TEST RUN NO. V ' ' ^~
IMPACTOR NO. 1
"LOCATION 7
CYCLONE NO. /
DATE ^ ' -S ' *
OPERATOR A- ' r/fiAJeJStf
SAMPLE POINT LOCATION VP57/?£14,*1 £> 'F ?£/'• C 1 P 1 T/}7~ #&•
SUBSTRATE COATING
IMPACTOR ORIENTATION
FLUE STATIC PRESSURE
NOZZLE DIA. V
fa/0/ti £ FUEL / inH2O, VELOCITY >*
ran IMPACTOR PRESSURE DROP
£d£ TEST LOAD &~2 ft? 'telb/hg-
IMPACTOR ,/f2-5~ JCFM
^/^^ ^C/^^
y
H "H±0 END TIME f/5~f
GAS METER END
CF
GAS METER START
GAS VOLUME
CF
START TIME
DURATION
f Jt g / IN Hg. HUMIDITY_
, TEMP. ^<^^ *F, DENSITY g/cc,VISCOSITY POISE
Foil + Sample, g
Unused Foil, g
Sample, g
Correction
for Blank, g
Final Sample, g
Stage Number
1
Wtf
1,0/71
MM
/^iU
2
?Ml
U&$
Sltl
,oUl
3
i.0&7
f f(S r(fj
,M#3-
flfl^p "J
fJUQ j^_
4
Wtt
Apof^
•00H5
,0*13
5
1./1&
YJ/0
t<%>2£-
,002?
Stage
Blank
.0727 .
FILTER NO.
Sample
Blank
FILTER + SAMPLE, g
FILTER TARE, g
SAMPLE, g
CORRECTION FOR
BLANK, g
_ FINAL SAMPLE, g
.0^1
.0137
,0*07
0
,00° 7
FULL CONTAINER, g
EMPTY CONTAINER, g
CYCLONE CATCH, g /^fe 5 0
4 38
60-20
-------
TABLE 1.
Molecular weight of sample gas MW
Molecular weight of calibration gas MW
Temperature of gas at sampling
conditions, °K T
Temperature of gas at calibration
conditions, °K T.
Static pressure under calibration
conditions, atm. P
Gas viscosity at sampling conditions,
poises y
Stage jet diameter, cm D
Sample quantity collected on each cup
Dimension conversion constant
Symbol Value
Pressure drop across impactor
during test "Hg" AP, ^^
Static pressure at inlet to
impactor, atm. P? £>'.
Density of aerosol particle, grams/cc P 2
Density of gas at inlet sampling
conditions, grams/cc P I•
R3 /£- I
R\f */
* o <^~
4 *•
R5 IZJ-
-^
R7 0* t
' ' 1312-
439
-------
TABLE 2.
Effective pressure drop, "Hg"
Inlet flow to impactor, cc/second
Pressure out of stages, atm.
Density of gas out of the various
stages, grams/cc
Characteristic diameter, microns
Criteria for validity of equation 18
Mean free path
Average molecular velocity
Symbol
F
Dpcfi x l
-------
TABLE 2 (Continued)
Symbol Value
% on a cup of the total sample collected £1.1 •*&»*•*• *i 7 •
Stage 2 Y
*Any discrepancy due to rounding off should be buried
in the largest Y cumulative % smaller than D
pc
44 1
3 Y3 21-1 It- *
4 Y4 //•> r, f
5 YS jCf J?'/
6 Yc 3-J I' $
D ^ ^^^~"~
Filter !•?
Total 100.00*
it..3 ?.y
^Y 2,3
-------
PLUME OPACITY OBSERVATION RECORD
LOCATION HO.
OWNER
DATE
OBSERVER
BOILER NO.
. If. /17*
1FUEL TYPE
POINT OF EMISSION
Test Run Ho.
H,
CAPACITY
klb/hr
BURNER TYPE
POINT OP OBSERVATION ^ 2-00 Y/IRP$
0?
TEST
No.
/
Time
ara/pm
&'- 30
It'iZ
K> :?<1
19 '-X
10:5 f
tO-,10
10: fr
/•'W
It'-i*
/titfg
It : ffi
Type
rwtc.
!•
i>
it
H
it
/»
it
H
>i
H
Test
Load
k#/hr
Opacity
%
2^
f
f
2-0
5*
5"
2$-
20
f
r
f
HIND
Speed
nph
V0
",
}
/
Direct
'/(JO
Sky
Cond
Mtrt f
CWW
\
/
Sun
Posi-
tion
?e T
*f.
Comments
»/? tffT 6f
£XV££.
442
-------
LOCATION NO.
OWNER
DATE
PLUME OPACITY OBSERVATION RECORD
f
POINT OF EMISSION
POINT OP OBSERVATION
OBSERVER
BOILER NO.
VFUEL TYPE
Test Run No.
CAPACITY
BURNER TYPE
YAK. PS A/0#T#
4 C. £
klb/hr
TEST
No.
•
Tine
am/pm
/t'~2$~
to' $7
f0-31
ID -HI
10'- V3
/o- If
/*:*/•)
10 -^
If'fl
Type
pMric.
t
Test
Load
ki/hr
^7^
» j 7e
\
f
Opacity
%
^ f
^^
^5"
<*-S~
Sky
Cond
ett
V
»PY
/
~
Sun
Posi-
tion
To rn
*&
Comments
f IffT Of
SfXVEK.
443
-------
ProJecti
Date. AM. II, ! "
1 "
? "
Velocity
Read
(in. B20)
AP
,$T
,/?
.1
,05-
Gas leap.
C*F>
Gas Tenji.
CR)
Ts
Molecular
Ht.
MS
Velocity
(ft/sec^
vs
02
Cone.
(% Dry)
6002-13
444
-------
fccoj eett
Data.
loeatiom
Pniti
t»»tl
VELOCITY TRAVERSE
Pg»egiptioni
Stack Cross Section
Personnel!
Ba)»
Barenetrie Pr*n.
Absolute Static Press, in Stack (in. Hg)i_
Pitot »ib« Ceefficianti _____
Tim
q;&
Traverse Point
Port Depth
/ f*>»
2 "
3 "
W
Velocity
Head
(in. H20)
iP
.2*
,T
-------
VELOCITY TRAVERSE
Test Description!
Date:
location!
Cniti_
Testt_
rual:
Stack Cross Section
Personnels
Barometric Press, (in. Hg)t_
Absolute Static Press, in Stack (in. Bg)t_
Pitot Tube Coefficient:
-------
Project:.
Data: OCT.
location:,
Onitt
VELOCITY TRAVERSE
Test Description:
-IT
Personnel i
Test:
Fueli
Barometric Press, (in. 119):
Absolute Static Press, in Stack (in. Hg)i_
Pitot Tube Coefficient:
-t
Vs - 85.48 Cf
i/a
Stack Cross Section
I
2
3
1
£
7
f
Iff
$
i
Time
OiffO
Traverse Point
Port Depth
("
I'ff"
)' f"
*'*"
3't"
3 "ft"
3f(*
y'0"
v'/"
f'#"
v't>"
2'0"
/'„"
0'<"
Velocity
Bead
(in. H,0)
US
,12
,r?
l.f
).3
1.1
1.3
1,3-
.11
I,M
(•*
112
^2
,f7
tf£?
Jit
.7ff
l,tt
uw
I.W
i./yp
Left
.Iff
t.*0
i.tit
tftf
I.M
,10
Jff
Gas Temp.
CF)
zeo w
Gas Temp.
CR)
Ts
•
Molecular
Ht.
»S
Velocity
(ft/sert
vs
m
5"£'f
77, f
g*'?
107^3
gf. 7
ff,2
7t.£
77.1
tt.7
7V.£
1r,1
7f.t
#6Stt.1
Cone.
(% Dry)
s*»ftf/>ic
is in pvcr fern/fed
four fe/t sAMritfii6.
sr*ci<
fo#r a «»*-**
rute >s A
ft
447
-------
TABLE TRACE SPECIES AND OR6ANICS SAMPLING CONDITIONS
LOCATION 9 - ROTARY CEMENT KILN
TS « 0 Run Ho.
Teat Number
Date (1976)
Port location
Velocity, m/atr/a)
Staek Tenp. X (•!*)
Oxygen content, * dry
Nolature *
Sample Tine* Bin,
Cyelone' f low, awemm (awo&O
Xaokinetlo Rate,
OvenTertp., X (*r)
XKD2Temp., X (*r)
Meter Tenp., X (»F)
Roiiledie, mi (in.)
No. ot Hltera Oeed
•ample now, dry, aem (aefm)
Volume Collected, dry, BOM dot)
Total Particulatea, ng/J(ib/KMB)
Slnlt Conditional
Teat Time t win. . ,
Nat. cai Burned, 10, aendo'aof)
Dry reed, 10* g. (10s Ib)
•lurry reed, 10" g (103 Ib)
•lurry Moiature, t.weight
Clinker, 10« g (103 Ib)
Precipitator Catch 10'g (10'lb)
8
9-3
9/29
BSP inlet
8.17 (16.98)
418 (287)
4.8
34.31
78
0.102 (3.891)
96.8
478 .(400)
303 (88)
.311 (00)
19.08 (.78)
1
.0343 (1.382)i
2.937 (103.64)
7307 (17.0) .
^,
7.241 (288. 8)
76.64 (168.6)
119.0 (261.8)
38.6
48.75 (100.7)
3.131 (4.688)
*
6
9-4
9/30 1 .f-
BBP eurteft .
1
9*8
10/4
BSP outlet
8.06 (16.60) 17.48 (87.381
428 (308)
2.3
411 (280)
6.8
44.74 37.88
78
300
•0.097 (3.438) 0.087 (3.067)
118.3
478 (400)
297 (78)
319 (118)
19.08 (.78)
1
0.0386 (1.3631)
2.897 (102.23)
8848 (13.9)
75
7.754 (273,6)
70.61 (185.4)
108.6 (239.0).
35,0
42.18 (92.69)
2.131 (4.688)
108.8
478 (400)
299 (77)
309 (97)
9,53 (.378)
1
0.0381 (l;3384)
10.829 (371.83)
22.7 (.083)
-
316.8 ^
27.60 (973.. 7)
293.7 (646.0)
462.8 (1017.4)
36.8
178.0 (388,1)
1.378 (20.61)
8
9-6
io/s
ESP outlet
17.41 (57.10)
408 (274*
6.6
38.31
300
0.087 (3.078)
104.8
478 (400)
294 (69)
410 (99)
9.83 (.338)
1
0.348 '(1*2188)
10.389 (368.88)
39.47 (.069)
313.2
(28.46 J1004, 1)
334.2 (738.3)
517.3 (1138.0)
38.4
199.4 (438.6)
1.378 (20.63)
1
448
-------
Project:
Date:
Location:
Unit:
Test:
KVB, INC. TRACE SPECIES AND ORGANICS SAMPLING DATA
WASC -Qt. MSS Personnel: f/fifi. ivtte Barometric Press: -2-?-&"5"
Probe Noccle Diameter (inches):
(On)
GAS
Absolute Static Press. In Stack (in. Hg) : 2-f-it (Ps)
Pitot Tube Coefficient: ' (Cp)
TIME
Real
Kfo
I6f5~
1 7(t>
I '72$-
I7f0
i?rf-
F/
Elapsed
4-
15-
10
fs-
60
7*~
ctiAnee
7f
i.0
t-t,£P,
Traverse
Point
Depth
VT
ft
II
II
•1
II
' fl
•>K£f>
£t
Pitot
fiP
(in H20)
.06
.06
,0(
,0e
."7
.10
crfe.
AT
Me Li,
Orifice
AP
(in H2o)
1.2-
1.2-
1.2-
1.2-
1,2-
1-3-
* D
I rt
f>££>
CUB.
Meter
Volume
(ft3)
Wife?
(20.100
etz.iw
gtl.eoo
7*t.3n
ffSte*
7*t. US
ICKOfiJ
rzsr
Punfp
Suction
(in.Hg)
6-0
7,r
11
13.0
17.2
22,$-
vr
cYi
A-7
TEMPERATURE ( ' P )
Stack
2?t
2-T2-
2-13
2-tf
y-g-f
**i
-^i.e>^£
* - rtf
Probe
yf<
•rreerg
Meter
In/Out
too
l'f
H>1
let
14
1*
Y
too
101
1Z
17
1C
if
°2
Cone.
% dry
CD
KVB 6002-12
-------
KVB, INC. TRACE SPECIES AND ORGANics SAMPLING DATA
Project: /
Date:
Location:
Unit: Cff
Test>
Fuel: U#T
M fMff 3T f.
1/1e/7f
1
wr Kit-fl
ge>0 Barometric Press: -^
Probe Nozzle Diameter (inches):
Absolute Static Press, in Stack (in. Hg) :
Pitot Tube Coefficient:
v.. 7 ?
ton)
(Ps)
(Cp)
cn
o
T I
Deal
132
II
Pitot
AP
(in H20)
,*6
,e>£
j?6
.07
jXr
,e>7£>
Orifice
AP
(in H20>
1,2.
1-2-
1.2.
1,2-
I-Z.
1-2-
Cum.
Meter
Volume
(ft3)
712.126
7ff,1l>0
7*7.700
7?i.7ffo
foW
tx.rrt
PUBP
Suction
(in. Hg)
^-2
7-e>
i,r
11,0
H,0
22,5~
TEMPERATURE
Stack
20 X
MS"
211
7*y
?ti
?£>X
Probe
i&e
-------
Project:
Date:
Location:
Unit: C^
/>*G£ T. KVB, INC.
f4 wse _-? WSS Personnel:
/* ' /*f / 7*
TRACE SPECIES AND ORGAN ics SAMPLING DATA
/f
(On)
test: 1~f Absolute Static Press, in Stack (in. Ha): (Ps)
Fuel: M7~, GAS PJ
TIME
Real
1717
If33-
irf7
1(02.
>ei7
It2.»
/fir
itro
1765-
I72e>
I73S-
I73Z
I7f3
ISOZ
Elapsed
•0-
/$-
30
fs*
€0
£0
7?
10
/ro
'fr
Traverse
Point
Depth
/f^.
//
n
',
n
CM/U6i
,,
I,
II
II
II
II
C»j})6
"
i'
it
Pitot
AP
(in H20)
.75-
,f
.f
,f
,f
cp ft
,f
,f
,f
,f
.f
,?
£P J.
,g
,tf
,f
tot Tube Coefficii
Orifice
AP
(in H2O)
1.2-
,
111.700
!/7~
111,700
1tl.*>°
HI. too
ffol. loo
63-1. IffO
010.3*0
tti-r
61f,*.«>
0(2.20*
e>*1.7fff
uit:
Pump
Suction
(in. Hg)
f,r
y.r
H,2.
f,i
H,l
3,6
3-t
y,o
f,l
H-2-
1.1
f,e
?,}
I,?
ICp)
Stack
277
3-7g
2*7
2-12.
213
2-12-
y-?*}
2*5-
^fZ
271
2-77
2?g
272
? "'>"
Probe
US'
31 1
?1<
t{ff>G>
ft>3-
fffl
i°3
foi
fe>3
^(02-
its-
toe
yc '3
•(**
XAD-2
7£
f/
^f
7S
7V
71
71
7f
72-
#1 •
7f
77
7£
7f
Impinger
Out
ft
to
77
71
go
«?/
tl
Z2-
tt
$i
Zf
12-
f5"
f2
Oven
371
3*1
3tt
ye/
1&I
f02-
y02-
100
i?t
ypj
tf0/
'/CZ
'/C2-
>/r"l
101
11
IPO
>CI
12
11
ft
11
It
IPS
/t>(
pi
102-
lol
im
ISO
11
!0t>
1*
ft
It
-------
Projecti fffl PHAlf JIT
B, INC. TRACE SPECIES AND ORGANics SAMPLING DATA
Personnel: cjtTfz, c#fwy Barometric Press: 2-1. 7
Date:
10/ti/ff
Location: ?
Dnit:
Test:
Fuel:
£ffl£fi>r KIL/O
1-6-
tf*r, GAS
Probe Nozzle Diameter (inches): %/f
Absolute Static Press, in Stack (in. Hg) :
Pitot Tube Coefficient: '$i
(Dn)
(PS)
(Cp)
TIME
Real
lfZ3
ItJS
Itlf
1103
111*
1133
Hi*
2e>t>3
2e>l f
**3?
Elapsed
>ee
Hr
/fr
21"
?.2S-
2-10
3-S-f
270
zsr
?00
Traverse
Point
Depth
t«"^~
tg"^~
}TOf •>
l\
h
ft
n
"
n
!•
II
Pitot
AP
(in H20)
.f
,t
Ffr-,
.*
*t
.1
.r
,t
,/
,/
./
Orifice
AP
(in H20)
.^
.f
•ff/TY
,1
•f
,f
.f
.f
ff
.f
,f
Cum.
Meter
Volume
(ft3)
tfg,l
H7,lfX
(**„
117.15-g
13 f. If a
If (,7t>o
I7f,l(t>
Ht.1/t
Zil.W
23?.t
ZSJ.I«»
Pump
Suction
(in. Hg)
f,t
5~<
'W6£K-
?*0
r,'
?,£>
?,0
5-0
*,£
f,i.
$-,?
Stack
27 (
^75-
AflS *.
3-71
273
1.7?
272-
7.73
27-1
?71
276
Probe
foi
W1
ef/tl k.
fos
Hoi
i*l
iff
ioo
W
fO]
te>i
XAD-2
f2
go
tr» ff
^
t3
73
71
77
77
#2.
fo
Irapinger
Out
fj
?S~
t/T/eAS
1"
7f
76
7g
7?
7f
?2-
tt
Oven
tto
iw
e#/M
yoi
tee
We
/ff
too
fee
too
•3ft
Meter
In/Out
?7
fr
Sft>
11
V)
11
15
ts
11
fJ
f/
1(
ff
l>f:
fi
fj
12-
11
1)
1*
10
10
°2
Cone.
% dry
S/ejtiT
en
KVB 6002-12
-------
KVB, INC. TRACE SPECIES AND ORGANics SAMPLING DATA
Personnel! ctfffKY. CMTft Baroaetric Pressi 21. 7?
„,,
"
27t
locations
Unit:
Probe Hozzle Dimeter (Inches) i
Absolute Static Press. In Stack (la. Hg) t
Pitot Tube Coefficient.
V?
_(Dn)
_(Ps)
cn
co
If*
15 If
1333
131*
1103
11*3
If/f
Elapsed
3*
6*
1*
Iff
If 7
Traverse
Point
Depth
Pitot
AP
(in H20)
.f
.f
,1
,g
Orifice
AP
(In H20)
.1
.1
.f
.f
.1
.1
.f
Meter
Voluae
27f,200
311.100
V/p.700
Vff.XV
Hit. see
Pu>p
Suction
(in.Hg)
f.f
r.7
(.£>
£.1
£.1
£.3.
(.3
f.f
Stack
270
2-71
2-73.
271
271
27 f
3-7*
277 Iff?
Probe
102-
31 1
•{Of
103
103-
Z»D-2
{£
€(
£1
71
7.2-
7*
71
71
73
fff.
re
Ispinser
Out
77
92-
76
go
7f
77
/t£F/llt f
ctf
IffO
vet
Vfl
Ifff
quo
•/£>{
31?
31?
317
7_r 397__1< 17
Meter
In/Out
1!
11
IT
11
If
17
11
/of
103.
we
11
Cone.
% dry
KVB 60O2-12
-------
JT
Project, ft Witt
KVB, INC. TRACE SPECIES AND ORGANics SAMPLING DATA
^f55" Personnel t Cffft/tY. Cfl^rfft Barometric Press i
Date:
location:
Unit; Cf
Test:
Fuel: ^7
!<>/$ /7f
4
KMT 1'it.v
f-<
-V/t#l, fiAt
Probe Nozzle Diameter (Inches):
Absolut* Static Press, in Stack (in. Hq) i
Pitot Tube Coefficient:
(On)
(PS)
5~
2-2-0
S-3S-
25*
3~fS-
2 1'
300
Traverse
Point
Depth
ft
tr
H
II
II
/t
ft
II
Pitot
AP
(In H2O)
T7
.f
,f
,/
-/
,/
,/
>?
'/
Orifice
AP
(in H20)
,f
.f
,f
ff
.f
.f
,f
,?
Cum.
Meter
Volume
t£t3)
?V.1»f
fM.teo
fW.0*>
f(*.0f*
f?S,to*
f?f,1t<>
(f7.(00
ffZWO
Puqp
Suction
(in. Hg)
f.f
(,*
£,0
f.'
(,0
e,o
f,i
6,1
TEMPERATURE
Stack
27*
275
2-70
2?Z.
270
2<7
2S1
271
Probe
fee
f03
fe>2-
Yet
f02
fez
f02
¥02.
XAD-2
^5~
£7
47
Sf
ff
7/
ft
?0
Impinger
Out
7?
77
7?
7?
7?
7£
71
7?
• F >
Oven
*?/
?f/
??g
Wl
??g
311
125
271
Meter
In/Out
1f
17
17
f/
f/
17
If
1C
17
17
ff
1(
1$~
f?
11
11
°2
Cone.
% dry
KVB 6002-12
-------
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Test So. -
Date
Sanple Port Position
location
\o
CeMej4T
ibc.
455
-------
KVB
Test Mo.
Date
Sanple Port Position
TRACE SPECIES AND ORGANXCS TEST
SAMPLE RECOVERY LOG
location
"To
CvU
Container
Number
Sample Description
Container
gyp*
Net
vt/vol.
Comment
•ass 4
(50^
22.2.
1.5
7.0.0
UP\IJ&C£
P.
IQQfr
E.S.P
L- m. \
Oat* iheet KVB 6002-15
456
-------
Test 9-3
TABLE
Inlet to ESP
OLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
iarium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
4
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
384
O. S
3/0000
3'
•2.0
12.000
***
/foo
V*
70?
/So
386
-------
Test 9-3
TABLE
Inlet to ESP
POLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
437
04
0.07.
a/fa
O.DZ.
0.02.1
-------
Mr. S. C. Hunter _2_
KVB ANALYSIS DATA
Test 9-3 Sample Number
263
273
296
384
386
393
437
837
1016
1017
G
H
* I
J
POM's
< 10 ug/1
< 1 ug/g
* 1 ug/g
0.1 ug/g
0.1 ug/g
<0.1 ug/g
< 10 ug/1
< 10 ug/1
0.5 ug/g.
*0.1 ug/g.
10 ug/1
256 ug/1
17 ug/1
64 ug/1-
PCB's
' 1 ug/1
'1 ug/g
'1 ug/g
*1 ug/g
"1 ug/g
"1 ug/g
<1 ug/1
< 1 ug/1
*1 ug/g
'1 ug/g
*1 ug/1
< 1 ug/1
< 1 ug/1
< 1 ug/1
G 253, 254, 256, 257, 255, 258, 259, 261
H 213, 222
I 441, 442
J 330, 438
459
-------
COMMERCIAL TESTING & ENGINEERING CO.
•CNCRAI OrriCMi tit NOITH LA (ALLC iT»MT, CHICAGO. IUINOII MIOI • A»EA CODE il» Tf t-§4i«
Reply tO IHS1IUMMTA1 ANAlTtlt DIVISION. t«J5 WKI 44tH AVENUE, GOLDEN, COIOSADO KMOI, MONE. »OM7Mgl
To: Mr. John G. M1cha1ov1c
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P. O. No.: 27810
Sample No.: 9.3* f334, 386, 393, 273
CONCENTRATION IN PPM WEIGHT
Date: March 11, 1977
Analyst: S. Sweeney
IAD No.: 97-A101-134-21
ELEMENT
Uranium
Thorium
Bismuth
Lead
Thallium
Mercury
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Hoi ml urn
Dysprosium
CONC
4
4
0.5
30
3
NR
<1
1
0.2
1
0.2
0.5
0.7
1
ELEMENT
Terbium
Gadolinium .
Europium
Samarium
Neodynrfum
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.2
0.9
0.5
2
3
1
28
25
200
35
22
<0.8
0.7
STD
<0.4
0.4
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
1
8
34
8
100
140
20
1
22
0.5
8
30
10
10
6
MC
40
36
ELEMENT
Vanadium
Titanium
Scandium
CaVtium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
40
930
5
MC
MC
900
MC
820
MC
MC
MC
MC
.560
NR
NR
NR
6
0.3
13
NR
NR - Not Reported
All elements not reported <0.2ppm weight
460
-------
COMMERCIAL TESTING & ENGINEERING CO.
Reply to
orrioiti tit NORTH LA »*u.t •TUCCT, CHICAGO, IUINOI* •ocei • ARIA CODE »>» »*-Mi4
INSftUMINTAl ANAlVSIt DIVISION, I4MJ WEST *»TH AVINUI, GOIDIN. COUMAOO IMOI. PHONCi X0-37t4»l
To: Mr. John G. M1chalov1c
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P.O.No., 27810
Sampl* No.: 9.3 B 1296
Date: March 11, 1977
Analyst: S. Sweeney
IAD No.: 97-A101-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead <2
Thallium
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Hoi ml urn
Dysprosium
heterogeneous
NR • Not Reported
All •WYWttl not f*pQrt$C
Sample was thermal 1)
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium
Lanthanum
Barium 4
Cesium 1
Iodine <4
Tellurium
Antimony
Tin
Indium STD
Cadmium <0.9
Silver i.0.5
Palladium
Rhodium
1 <0.5 ppm weight
t ashed 9 350° C for one
ELEMENT
Ruthenium
Molybdenum'
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Z1ne
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
Approvedt
hour 1n a ISM
CONC.
<1
0.7
0.7
<7
<2
<0.3
<0.4
6
3
2
an»1v«1«
46 1
-------
COMMERCIAL TESTING & ENGINEERING CO.
•ENERAL OFFICE*: 111 NORTH LA IA LIE ITHEET, CHICAGO, ILLINOII IOIOI • A»E» CODE III »ll-«4»4
Reply tO INStlUMINTAL ANA1VUS DIVISION. 14335 WEST 44TH AVENUE, CCHDtN. COIOIADO MMOI. FMONE: JOWTMSJI
Te: Mr. John G. Michalovic XlJK
Calspan Corporation ^^5?!!^^
Post Office Box 325
Buffalo, NY 14221
P.O. No.: 27810
Sample No.: 9.3 C 1213, £22, 441, 442, 437, 330, 438,
CONCENTRATION IN M9/ml
ELEMENT
Uranium
Thorium
Bismuth
Lead
Thallium
Mercury
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Hoi mi urn
Dysprosium
CONC. ELEMENT CONC.
Terbium
Gadolinium
4). 008 Europium
0.04 Samarium
Neodymium 0.02
NR Praseodymium <0.02
Cerium 0.02
Lanthanum <0.03
Barium 0.02
Cesium 0.01
Iodine 0.2
Tellurium
<0.2 Antimony 0.08
Tin 0.02
Indium STD
Cadmium
Silver MC
Palladium
Rhodium
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
Date: March 11, 1977
Analyst: S. Sweeney
IAD No.: .
CONC.
0.02
0.01
<0.003
0.009
0.1
0.04
<0.1
0.004
<0.002
0.006
0.4
0.05
0.08
0.004
0.9
0.05
0.1
97-A101- 134-21
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC
0.009
<0.1
<0.005
MC
MC
3
MC
0.8
1
0.5
0.9
MC
MC
NR
NR
NR
0.01
0.004
NR
NR - Not Reported
All elements not reported <0.004
Approved:
462
-------
Reply to
COMMERCIAL TESTING &*ENGINEERING CO.
•ENERAL OFFICES: *t* NORTH LA SAU.E STREET, CHICAGO, ILLINOI* 60601 • AREA CODE 112 716-6414
INSmiMENTAl ANALYSIS DIVISION. 14115 WEST 44TH AVENUE. COIDEN, COLORADO 60491. PHONfe JOMTMttt
To: Mr. John G. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo. NY 14221
D»t«= March 9, 1977
Analyst: s. Sweeney
P.O. NO.: 27810
Sample No.: 9-3 D 11016 1/27/77 IAD No.: 97-A101-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium 3
Thorium *
Bismuth 0.4
Lead 5
Thallium
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmlum 0.5
Dysprosium 1
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodyml urn
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.2
1
0.4
2
6
2
17
22
150
1
3
0.9
STD
0.4
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
1
5
35
5
140
8
0.6
<0.7
9
<0.2
6
28
23
9
4
MC
240
24
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
32
MC
2
MC
MC
24
22
820
MC
MC
MC
MC
=300
NR
NR
NR
7
0.7
12
NR
NR •— Not Reported
All elements not reported <0.2 ppm weight
Approved:
463
-------
COMMERCIAL TESTING & ENGINEERING CO.
Reply to
OFFICE*: 111 MOUTH LA IAUE (TKCT, CHIOAQO, ILLINOIS COIOI • A»EA CODE tit f*l-*4«4
INS1IUMENTAI ANALTtll OIVIIION, I4MS WIST "TH AViNUE, COLDIN, COlOtADO «MOI, MONti JOW7WSJI
To: Mr. John 6. Michalovic
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P.O.NO.: 27810
Sample No.: 9.3 £ 11017
March 11, 1977
Analyst: s. Sweeney
IAD No, 97-A101-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium 2
Thorium 4
Bismuth
Lead 3
Thallium
Mercury NR
Gold
Platinum ^
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium 0.1
Erbium 0.4
Holmium 0.6
Dysprosium 0.9
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.3
0.9
0.4
3
5
2
9
16
80
<0.1
0.3
<0.3
0.4
STD
ELEMENT
Ruthenium .
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
1
4
50
5
75
3
0.5
£0.6
5
£0.2
4
28
6
5
3
MC
64
20
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
•Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
30
500
2
MC
MC
47
40
810
MC
MC
MC
MC
"440
NR
NR
NR
1
<0.1
3
NR
NR - Not Reported
All element* not reported <0.2 ppm weight
Approvedi
464
-------
*»«t *>• 9-4
Sample Port Position
TRACE SPECIES AND ORGANICS TEST
SAMPLE RECOVERY LOG
Location
I/.. .1
fcJUS.T o
Ij
Container
Number
.4-10
£74.
2.70
aas
Sainple Description
P4.
357
447
fi
L KfcD- 2
Container
Type
li
Net
vt/vol.
\TbMl
Iffcldl
18,4
ZCOit
Comment
-SL1
}
tza-iesr- 4*2
ce
444
u
A
VlesNlC
3
tots
762
102.0
l^-S Te.k.tl Lioo.be
Data Sheet KVB 6002-15
465
-------
Test 9-4
TABLE
inlet to ESP
POLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
594
VSODOO
"2,1
H
«TSO
fioo
Vo
/3
410
-------
Test 9-4 TABLE Inlet to ESP
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
iarium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
C
A2,
*0.02_
^O* •
» o • oos
O.OZ.S
o.si
0.O2-
0.0*
0.02-
o.r»
0.08
0.0/0
•T0.0DS
0.0?-
^}
<*y
-------
COMMERCIAL TESTING & ENGINEERING CO.
eENERAl OFFICES: lit NORTH LA lAUt STREET, CMIOAOO, ILLINOIS SBS01 • AREA CODE »II »t»-R4S4
Reply tO INSIIUMINTAl ANAIVM DIVISION, WJM WEST 4JTH AVINUE, GOIMN, COIMAOO KMOI. PHONEi
TO. Mr. John G. Nlchalovlc
Calspan Corporation
Post Office Box 235
Buffalo, NY 14221
P.O. No.: 27810
Sample No.: 9.4 p f 1Q20
Date: March 11, 1977
Analyst: S. Sweeney
IAD No.: 97-A101-134-21
CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium <4
Thorium <4
Bismuth <0.4
Lead 18
Thallium 2
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Hoi ml urn
Dysprosium
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium
CONC.
0.2
0.5
0.3
2
6
3
13
10
100
20
9
<0.5
STD
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium
CONC.
1
5
33
6
160
200
13
<1
5
0.2
8
33
8
9
1
MC
290
25
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
38
MC
3
MC
MC
850
MC
390
MC
MC
MC
MC
*200
NR
NR
NR
5
0.3
11
NR
NR - Not Reported
All elements not reported <0.2 ppm weight
Approved:
468
-------
TRACE SPECIES AND ORGANXCS TEST
SAMPLE RECOVERY
Test *>. &~S Date >O/4/T4* Location _
Sample Port Position OUTLET Qg 1ZSP
OaTnefcs SM«*S»
•
{
Container
Number
4oo
fc.Z.3,
445
102,4
440
3
464-
J2£c3L
4
Sample Description
L
4, \>»Pi»iSce.«t I
4- \
"8 (2."N
t-,O
• \ » "n~ re
itf Ci_i
L^gpy
i/eP
S~2
L - lo
Container
gyp*.
HT
ila
ll.
S:
Z k
Net
wt/vol.
Q-^g.t4ft
I74.J
Comment
5
298
I
Data Sheet KVB 6002-15
.A
489
-------
Test 9.5
TABLE
Outlet of ESP
POLLUTANT
SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
275
XS
fc
ZJD
Woooo
ZSO
So
^£OOD
3So
2.7.0
110
223
0-02-
£0.01
l.i
O.OB
o.oz.
t.i
o.zz.
f
/.o
0.0-2.
0.0(0
o.o/
o.os
0.0 Vfc,
-------
Test 9-5 TABLE Outlet of ESP
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Jhromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin ^
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
364
&
1.1*
ss
2/^0
/£>3
7.22.
-------
Test 9-5 TABLE Outlet of ESP
POLLUTANT SAMPLE NUMBER
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Chromium
Cobalt
Copper
Iron
Lead
Manganese
Mercury
Nickel
Selenium
Tellurium
Tin
Titanium
Vanadium
Zinc
Chloride
Fluoride
Nitrates
Sulfates
E*
<0. /
fO.oo3
S
|