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

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                  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.

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                             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

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                 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

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                           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

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                                  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

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        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

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            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

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                               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

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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.

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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.

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                       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/.


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60-3

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        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









































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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£









• .








•
-

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                    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

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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

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                           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









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Gage
Reading
(iwg) '
ir
t.f
7










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Pitot
Tube
Pressur
(iwg)
.97
.0C
.Of










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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


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•

In
(°F)
/f*
2fO
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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



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3
1075"



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U

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100
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W
IW6
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5*00



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1717
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O
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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



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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
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6











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7













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10




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7
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too
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10
120
f.
275
000

















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im
1117
11?
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100
6f

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25"
2001
Ifff
IS!
1100
\6
?12














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13.3
100 21*^
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7? \76
100 \f?0
f.7
2(0 (02
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 •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.
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70
670
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310
2700


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7
976
















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60
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3000


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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

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620
500
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20.615
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*

 *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-

$2
6$

~(

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
—
/J*
7?e>
;?
11
73-

7$
67
?7
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M.tf
tt'.ze
270
*<%**

61?
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630
7/5
€6&
—
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71?
12-
12. 5~
6*

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67
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W
71?
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—
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72?
II
ft.?
67

7$
6?
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- 6.$
21.W
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720
6*0
710
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72$
10
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67

71
6?
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62?
71?
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_
62?
730
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83-
67

7$
€1
V7
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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?
7*£>
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£?f
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~
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13.?
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67

77
tr
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^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?
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6(0
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66*
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6 3
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et?
73 &
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                                     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


















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l.7f
}.r
t.f
te.tt
H. r










Velocity
Bead
(in. HjO)
AP
/./
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)
&
l.f
2.0
Z.3-
*.1
2.2
1.6










Gas Tenp.
(*F)

62 f




€10










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CR)
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lets'
to f 2.
1071
l» 7 f
I&73
107*










Molecular
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




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Gas Te«p.
(*R)
TS
IO(O
ie>?a
\oio
1630
IW
1010










Molecular
wt.
MS
21.0




\|














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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
3.1
2.1
2.S
2.3-
1.6










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W

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r?z
fd
f<£
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ft*










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<*R)
»s
i*?r
IOJ3,
\03-el
102 C
102*
1920










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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.
CR)
*S
120




\















Molecular
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
\.t
3. I
2. 1
a., 3.
3.. 3*
/. 7










Gas Tenp.
CF)

$-75-
5-73.
rtq
fff
5"*3
$-f0










Gas Tenp.
CR)
*s
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




\















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(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









•
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Ht.
»S
M.o




\




/










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(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



,






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Wt.
MS
21,0




\




*










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(ft/see)
VS
IS*
15 3
W
Itt
l?6
113










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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
///
!$£
-2
1*2-
/y/
/yy
^
172-
l/,4
/e
2-
/0f

//
















y-
i
f/zf/r/
/03*




3- £
*??
l?7
I
163
12
/0
2-
Ilt
PM
/i?
/
I7/
,0
W
















y-y
&/2f/K
/J00


,

/>7T
l?7
l?£
1
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//-
/*
/
/0JL

H3
/iz
I
tff
7
/#





'








•

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£
)3?
I
U2
//.
12.
2,
1*3

0
wy
us
1
t?2
5-
15











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?-2f~7£
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ui
13^
I
if?
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&
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fi
W
15*
1
177
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C






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/300




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13 £
13*
1
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tw
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f-2£-7t
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tfi f/J-
133 W
1 /
J53 /£2
/2<0
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£
HZ*




j.
IK
i?i
I
IS*
a
12
1
/'*

7
Me
#1
/
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
,£>.$.

*3~
ft
W0
1
//7

/i
















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$~/J£/7f
/2&0




F,
ff
73
/
17

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0,0.5,
0.0.S.

f
17
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f





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u ^ '
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1



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^ ^
» 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
-4 V
^ «*
^ X

f-l
f/27/7S
/000




i
ftt
63
I
f2-

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^* ^ ^
^


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^ >^^

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ff
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2.
/$

T
?3
72-
I
37
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1








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7j
70
I
*3
i'
^
/
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
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1
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16
2-
3-1

i
47
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u
VI
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23

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^
?
vrs
\
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^
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•































 *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'%
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2
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.

























 *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
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* *r fy
//>*
Q
0
13-0

35-
///
Iff
1
/$2-
r
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^^
t jf*&
t *? V

#3
7f

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6-7

12* S




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Ml
12*
I.
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//'
f
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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
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Ft

j$~
#
70*
—
ft
7%
J0-/3
7o









7/S-3
7-ff" 7f
(£00
• 	
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^*w ff£
$$ iff.
7-t
/-2-
62-
•&-
77
&,
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2,^

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&-
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f
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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
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f
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71
77
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(3
3027
^i











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77
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20,27
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£ 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-
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i
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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
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£,
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2.
2.
«•• 	 ••
3
?#
?#
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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71
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*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'
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f,
£
0
0

f
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rf
?
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0
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77
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7?
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>'


















 *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.
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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.
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-------
                            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
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8. Oxygen (%)
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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
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26.
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28.
29.
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      "  '       '-—•	:	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
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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)*
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14. Carbon Monoxide (ppm) uncor/cor
if
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16. Sulfur Dioxide (ppm) uncor/cor
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18. Atnos. Temp. (°F/°C)
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23.
24.
25.
26.
27.
28.
29.
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                                             Data Sheet 6002-2


-------
Test No. 7f
Unit No.
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MOBILE LABORATORY DATA Test No.
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                                  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)*
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12. NO (cold) read/3% 02 (ppm)*
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15. Hydrocarbon (ppm) uncor/cor
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17. Smoke Spot (Bacharach)
18. Atmos. Temp. (0F/°C)
19. Dew Point Temp. (eF/°C)
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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
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12. NO (cold) read/3% 02 (ppm)*
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*
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18. Atmos. Temp. (°F/°C)
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20. Atmos. Pressure (in. Hg)
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22.
23.
24.
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26.
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28.
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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 (%)
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11. NO? (hot) read/3% 03 (ppm)*
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. Atmos. Temp. (eF/°C)
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23.
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25.
26.
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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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*Correction to  3% O2 should not be performed if
 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
7-21-7*
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 *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.
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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71
21,3?
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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.
7/3-3
7-21-7C
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  the  value is measured on  a wet basis.
                                     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.
7/3-7
7-21-7*
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                               '
                                                                 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
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 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
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-------
    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
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7/3-3
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-------
   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
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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
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1,0
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+ .i
7*r
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210
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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
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<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^
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t^"^ $ * 2
/ & ^^
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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,$~
;1, 0
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f'2.
3'^
i-^i
7?r
2$~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 (%)
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. Atroos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
#//-l
7-2-7f
lift



0)
1.
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i? J J /
0 f / f
f-2 ~7
-------
Test No._

Unit No._

Unit
                   Date
MOBILE LABORATORY DATA


      Location     	
Test No.

Engr.
                   Fuel /f^X^ G>^5 Capacity  /x 5~~

                   £ f££ £      Burner Type_
1. Test No.
2. Date
3. Time
4. Load
^>, 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% O2 (ppm)*
12. NO (cold) read/3% 03 (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. Atmos. Temp. (°P/eC)
19. Dew Point Temp. (8P/°C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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*Correction to  3%  02 should  not be performed if
 the value is measured on a  wet basis.
                                    340
                                                                  Data Sheet 6002-2

-------
Test No

Unit No.
i. %ff~2-
                    Date
                            MOBILE LABORATORY DATA

                                  Location _ i
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% Oa (ppm)*
10. NO (hot) read/3% 02 (ppm)*
11. NO9 (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. (eF/«C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
22.
23.
24.
25.
26.
27.
28.
29.
30.
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-------
                              MOBILE LABORATORY DATA
Test No

Unit No.
... %f I" 2-  Date if " S  /O  Location
                                                                 Test No.

                                                                 Engr
                                                                             5
                             Capacity  /, \
Unit Type
             C
                                    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. Atinos. Temp. (0F/°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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-------
Test No

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MOBILE LABORATORY DATA

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Engr
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Onit Type
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1. Test No.
2. Date
3. Time
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13. Carbon Dioxide (%)
14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
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18. Atnos. Temp. (°F/°C)
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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% O2 (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. Atmos. Temp. (°F/°C)

19. Dew Point Temp. (°F/°C)

20. Atmos. Pressure (in. Hg)

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23.
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27.
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-------
Test No._

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g / Y
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*
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18. Atnos. Temp. (°F/°C)
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                                    346
                                             Data Sheet 6002-2

-------
Test No

Unit No.
.///-
Date
                            MOBILE LABORATORY DATA


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                                                              Test No.
                                 Capacity
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10. NO (hot) read/3% 02 (ppm)*
11. NO? (hot) read/3% 02 (ppm)*
12. NO (cold) read/3% O2 (ppm)*
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14. Carbon Monoxide (ppm) uncor/cor
15. Hydrocarbon (ppm) uncor/cor
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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.
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Unit Type £ Of? 0/^/0 CfCt-£ BUI

1. Test No.
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12. NO (cold) read/3% 02 (ppm)*
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*
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16. Sulfur Dioxide (ppm) uncor/cor
17. Smoke Spot (Bacharach)
18. Atiros. Temp. (°F/°C)
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22.
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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
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Unit Type &&r7#fiVf-ff C r£(.fr


1. Test No.
2. Date
3. Time

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6. Flue Diam. or Size, ft
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10. NO (hot) read/3% 02 (ppm>*
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12. NO (cold) read/3% O2 (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. Atmos. Temp. (°F/°C)

19. Dew Point Temp. (°P/°C)

20. Atmos. Pressure (in. Hg)

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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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12. NO (cold) read/3% 02 (ppm)*
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*
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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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22.
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                                  A       00
                         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
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2. Date
3. Time
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7. Probe Position
8. Oxygen (%)
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12. NO (cold) read/3% O2 (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. Atnos. Temp. (°F/°C)
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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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Unit Type_
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2. Date
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12. NO (cold) read/3% 02 (ppm)*
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*
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17. Smoke Spot (Bacharach)

18. Atnos. Temp. (eF/eC)

19. Dew Point Temp. (°F/*C)

20. Atmos. Pressure (in. He?)

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22.
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                                                               Data Sheet 6002-2

-------
Test No
. ///-
Date
                             MOBILE LABORATORY DATA


                         ~  ~~
Location
Test No.


Engr.
Unit No.
             Fuel/f//*  £4$  Capacity
                                                *
Unit Type C0tffff/J£P C fCt.£


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2. Date
3. Time
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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. NOs (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)

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                                  353
                                                        Data Sheet 6002-2

-------
Test No

Unit No.
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                            MOBILE LABORATORY DATA

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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
*
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/0C)
20. Atmos. Pressure (in. Hg)
21. Relative Humidity (%)
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-------
Test No._

Unit No.
Date
                            MOBILE LABORATORY DATA


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Engr.
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2. Date
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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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1. Test No.
2. Date
3. Time
4. Load X ft
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. 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.
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-------
Test No.,

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                            MOBILE LABORATORY DATA


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                                   Capacity
                                                * / 0*
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% 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.
24.
25.
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-------
                           MOBILE LABORATORY DATA
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-------
Test No..



Unit No.
                  Date
          MOBILE LABORATORY DATA


      r- £~l~ 7S
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                                                              Test No.
FuelW_t£*f Capacity /, $~ * 10
                                                              Engr.




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                                          */*!
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2. Date
3. Time
4. Load X /^ *
5. Process Rate
6. Flue Diam. or Size, ft
7. Probe Position
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)
Stack Temperature -48- (°F)
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£
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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)
Win_a
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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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      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)
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     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
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         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-£>
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f£~
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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 (" 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
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6-y.j-
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6,3
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11
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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
/'?
1*7$
/jf
2i
2-0
0,0,0

0
100
$21
7.5~
WO
2-
2-1
3-1
—

#?•
77
?a u iff
#5



f,
100
127
0
&?$•
/*•
2S
J-0
—

/
/W1
let/
o*
iyi?
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 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-
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!03
-------
Test No

Unit No.
MOBILE LABORATORY DATA Test No.
1-3 Date 1-2?-7i
Fuel GA ^
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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.
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25.
26.
27.
28.
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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
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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
*
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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)
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                                              Data Sheet 6002-2
                                     392

-------
MOBILE LABORATORY DATA Test No.
f- <"
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Unit No.
Unit Type XV 7-*
If or uttf >* *
Date /0fV(7£
Fuel M, £.
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1. Test No.
2. Date
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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.
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                         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.
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-------
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.
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-------
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.
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*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.
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-------
                              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

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£t






Pitot
fiP
(in H20)
.06
.06
,0(
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."7
.10
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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
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Punfp
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(in.Hg)
6-0
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11
13.0
17.2
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TEMPERATURE ( ' P )
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2?t
2-T2-
2-13
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too
l'f
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let
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101
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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,*.«>
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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
?,}
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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-

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yc '3
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7£
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^f
7S
7V

71
71
7f
72-
#1 •
7f

77
7£
7f
Impinger
Out
ft
to
77
71
go

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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
.7-S
o.oy
o.o'Z.
/3
3

-------
                                  KVB
^4
^
     Test No.  9-4»   Date

     Sample Port Position _

             - Si. & PR Us.
                       TRACE SPECIES AND ORGANICS TEST
                            SAMPLE RECOVERY IOG
                             fc  Location
Container
 Number
  VUtle.
  40ft
  44-7
  4TO
   4ns
   44.cs
   4S2.
  454
  457
  102,7
                        AJJ Sug^-T
                    Sample Description
            S
                        1 ,J
            &
                        1 u   Vlk^U
                       UftOS- V
                                    *6M
Container
   TV**
                                           AL
                                      Jfa.
                                                K
                                                          Net
                                                        wt/vol.
                                                       O.S-7TS>
                                                         417.
                                                   IM
                                                         4-Ot
                                                         44^
                                                           Comment
                                                                     TEST
                                                            £866 JlM-.
                                             Data Sheet KVB 6002-15
                                  473

-------
                                   KVB
                        TRACE SPECIES AND ORGANICS TEST
                             SAMPLE RECOVERY LOG
Test No.
                 Date
         \Ws /To
                                 Location
Sample Port Position     Op-rlgy OF ESfi
 Container
  Number
 Sample Description
                                        Container
                                           Type
  Net
wt/vol.
                                              Comment
             L1S    \nvt> 2.3'B
                                  .OR
   loao
P   ESPCATCU
                                              Data Sheet KVB 6002-15
                                     474

-------
   Test 9-6
                                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
           276
.O2_

-------
Test 9-6 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
361
0.1-
o.o«/
O.tS
Co.oor
D.OI
1*0
o.ro
y
<:•*_
• 0
/Vo
<0.2-
2.Z_
<:4
<5o
<:So
2.^00
40
*/z-
fS.*
-iv.s

-------
Test 9-6 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
1 Sulf ates
409+










i
g
o
S-
p-4
*H
O •
.t-l
i-l
1
1




408+
«z.u
o.feS
«»&
<0.1

-------
            COMMERCIAL TESTING &  ENGINEERING CO.
            BENEtAL OFFICE!: tit NO«TH LA tALLE STREET, CMICAOO, ILLINOII tOtOI  • AREA CODE tl» Tlt-t4t4
 Reply IO     IHSttUMtMTAl ANALYSIS DIVISION,  »4MS WES1 4OH AVENUE. COlDEN, COIMADO KMOt. PHONii MMTMSII
 To:  Mr.-John G. Michalovic
     Calspan Corporation
     Post Office Box 235
     Buffalo, NY 14221
 P. O. No.:   27810
 Sample No.:   276 Test 9-6
              Date,  April 12.  1977


              Analyst:  S. Sweeney


              IAD No.:   97-A165-134-03
                                 CONCENTRATION IN PPM WEIGHT
ELEMENT CONG
Uranium 2
Thorium 4
Bismuth
Lead 7
Thallium <1
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium

CONC.
0.2
0.7
0.4
2
3
3
16
13
130
100
13

±0.5
<).6
STD
<0.5
0.5



ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

14
6
36
4
90
MC
54
3
47
6
7
37
8
12
5
MC
32
210

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen^
CONC.
28
730
2
MC
MC
MC
MC
970
MC
MC
MC
240
=400
NR
NR
NR
59
0.2
26
NR
NR - Not Reported
All elements not reported <
-------
Reply to
COMMERCIAL TESTING & ENGINEERING  CO.
•ENCIAL OFFICE!: at* MOtTM LA »ALLC STREET, CHICAGO. ILLINOII *0«OI • AtEA CODE in TJ»-»4»4
  1NSTUMMN1AI AHAirSK DIVISION.  IO3S Wt$l 44TH AVENUE, GOIOEN. COUMAOO «MOI. FMONE: KM7§-W31
To:  Mr.  John G. Hichalovlc
    Calspan Corporation
    Post Office Box 235
    Buffalo. NY 14221
p. o. NOJ   27810
Sample No.: 408 Test 9-6
                                                   Date:  April  12, 1977
                                                              Analyst: S.  Sweeney
                                                   IAD No.: 97-A165-134-03
                                 CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium 5
Thorium 9
Bismuth
Lead 8
Thallium
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetiunr
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymi ui
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium

CONC.
0.5
2
0.8
4
8
i. 6
21
22
110
16
25

<0.9
2
STD
<0.9
1



ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

6
7
69
8
170
310
100
3
28
1
14
35
14
88
13
MC
230
130

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
160
MC
8
MC
MC
MC
MC
MC
MC
MC
MC
MC
MC
NR
NR
NR
20
0.9
17
NR
 Nit - Not Reported
 All element* not reported <0.5 ppm weight
                                       Approved:
                                             479

-------
 Reply to
           COMMERCIAL TESTING  & ENGINEERING CO.
           •ENIRAI OFFICE!! Ml MOtTH IASAIXE STREET, CMIOA*O, ILLINOI* «0«OI • AREA CODE »ll Tt*-»4»4
            INiTIUMfNTAl ANMYM DIVISION.  MSW WIST 44TM AVfNUt COUXN. CCHOtAOO (MOI, PHONii MMTMfil
 To:  Mr. John  6.  Mlchalovlc
     Calspan Corporation
     Post Office Box 235
     Buffalo,  NY 14221
P.O. No.:  27810
Stmple No.t 409 Test
                     9-6
O.te: April  12. 1977


Analyst!  S.  Sweeney


IAD No., 97-A165-134-03
                                CONCENTRATION IN PPM WEIGHT
ELEMENT CONC
Uranium <4
Thorium <5
Bismuth
Lead 26
Thallium 2
Mercury NR
Gold
Platinum
Iridium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium

CONC.
0.4
1
0.6
2
5
5
20
18
120
26
9

10.8
10.9
STO
10.7
10.5



ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese •
Chromium

CONC.

4
4
37
6
150
830
83
2
20
2
6
63
15
M
3
MC
490
66

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine'
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
44
MC
5
MC
MC
MC
MC
MC
MC
MC
MC
MC
MC
NR
NR
NR
8
0.5.
41
NR
NR - Not Reported
All •(•nwntt not reported <0.4 ppm weight
                                              Approved:
                                            480

-------
Reply to
          COMMERCIAL TESTING  & ENGINEERING CO.
          eiNSRAl OWICUl lit NOKTH U tALLC »TMCT, CNIOA*0, IlltNOIt •0*01 • AH* OODC MS Tlt-8414
            INMIUMfNTAl ANMVIU DIVISION. I4JM WtSt MM AVINUS, OOIMN, COIOIAOO W40I, MONfi MM7MB1
To:  Mr. John G. M1cha1ov1c
    Calspan Corporation
    Post Office Box  235
    Buffalo. NY 14221
P.O. No.:  27810

Sample No.<  9-6 A #471, 467.  466,  470, 465

                              CONCENTRATION
                                                          Date: March 11, 1977
                                                          Analyst.  S.  Sweeney
                                                          IAD No.:   97-A101-134-21
                                             IN
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead £0.06
Thallium
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten 
-------
Reply fo
           COMMERCIAL TESTING  &  ENGINEERING CO.
           GENERAL OFFICE*: It* NOVTH LA tALLE STIECT, CHIOA80, ILLINOIS *0«0> • AREA CODE t» 7II-I4M
            INSTIUMCNIAI ANAIYSIS DIVISION,  Mas wist am AVIMUJ, coiofN. CCHOMOO KMOI. mom-.
 To: Mr. John 6.  Michalovic
    Calspan Corporation
    Post Office  Box 235
    Buffalo, NY  14221
 P.O. NO.I  27810
 Sample No.: g.g B 1295
                                      /tfc.
                                                         Date:  March 11. 1977


                                                         Analyst:  S. Sweeney


                                                         IAD No.:  97-A101-134-21
                               CONCENTRATION IN PPM WEIGHT
• ELEMENT . CONC.
Uranium <4
Thorium <4
Bismuth
Lead <2
Thallium
Mercury NR
Gold
Platinum
IHdlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
NR - Not Reported
All elements not reported
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium
Lanthanum
Barium 2
Cesium <0.2
Iodine <0.7
Tellurium
Antimony <1
Tin 1
Indium STD
Cadmium
Silver
Palladium
Rhodium

<0. Sppm weight
ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

Approved: '
CONC.

3

£0.8

0.5
0.2
2
<1
<0.4

<0.4
2
2
0.4
<>.!
14
0.1
6

^
ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
jfi
JuL^*&~&
CONC.
0.4
113
<0.3
260
80
14
7
64
MC
110
*110
140
«9
NR
NR
NR
1

0.2
9
6
'Heterogeneous    Sample w.as  thermally ashed 9 350° C for
                  n * ouartz .crucible  orJor to inaly$1$,
                                                                    In a laboratory furnace
                                          482

-------
Reply to
          COMMERCIAL TESTING  & ENGINEERING  CO.
          eCNEKAL OFFICE*: »• MONTH U* »AUE •T*EET. CMICAOO, IL'.INOI* »0»01 • AHEA CODE »1t T»»-M»4
            INSnUMfNTAl ANAIYSIS DIVISION. USM WEST 44TM AVENUE. OOICXN, COlOtADO **», PHONE. KO-J7WSSI
TO!  Mr. John 6. Michalovlc
    Calspan Corporation
    Post Office Box 235
    Buffalo, NY 14221
                                       21k
P.O. No.:  27810

Sample No.:  9.6 C *449,  460, 451, 452, 453, 456,  457,
                                                          Date:  March 11. 1977
                                                           Analyst:  S. Sweeney
                                                           IAD No.: 97-A101-134-21
1027, 500, 525, 362
368, 370
ELEMENT CONC.
Uranium <0.04
Thorium <0.04
Bismuth
Lead 0.02
Thallium
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmlum
Dysprosium
* 529' ' CONCENTRATION IN yg/ml
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium 5.0.02
Cerium 0.009
Lanthanum 4). 03
Barium 0.1
Cesium 0.002
Iodine 0.4
Tellurium
Antimony 0.1
Tin 
-------
          COMMERCIAL TESTING  & ENGINEERING CO.
Rtply to
          MNllAk OFPIOMl III NOITM U «AUt WHIT, OMIOAeQ, IIUNOII
           INMIUMINTAl ANMTUI MVWON,  UJM Will MM AVINUt OOUXN. '
                                                           AM* 0001 Ml TM-MI4
                                                          n«i. momi j
Te>   Hr.  John  G. M1chalov1c
     Calspan Corporation
     Post Office Box 235
     Buffalo.  NY 14221
P. O. No..   27810
Simple Me..  9.6 D  1360
                                                           ;  March 11, 1977
                                                       AM)/**  S. Sweeney
                                                       IAD No.:  97-A101-134-21
                             CONCENTRATION IN
ELEMENT CONC.
Uranium <0.07
Thorium <0.08
Bismuth
Lead 0.06
Thallium
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten £0.05
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmlum
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium 0.02
Lanthanum 0.02
Barium 0.2
Cesium
Iodine 0.01
Tellurium
Antimony 10.02
Tin
Indium STD
Cadmium «0.02
Silver 0.04
Palladium
Rhodium

ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Z1nc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

*0.05

0.02

0.02
<0.002
0.03
10.03
10.005

£0.00?
0.07
0.03
0.01
10.003
0.2
0.005
0.02

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
.Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
0.003
10.2
£0.001
8
1
0.6
0.6
4
3
0.3
2
MC
-7
NR
NR
NR
0.02

0.006
NR
NR - Not Rtportod
Alt elements not reported <
   ^Heterogeneous
                      0.01
ApprovMt
                                       484

-------
••ply to
COMMERCIAL TESTING  & ENGINEERING  CO.
•INtMl OPFIOO. ttl NORTH LA tALLt STRUT, CHICAGO, ILLINOIS (0*01 • ARIA COOt Ml ftl-14M
  INSTIUMINTM ANAIMII OIVItlON.  14M5 W«T 44TH AVINUI, OOlOtN. COIORADO MMOI. PHONI. JOWTWUI
TO.   Mr. John 6. Mlchalovlc
     Calspan Corporation
     Post Office Box 235
     Buffalo. NY 14221
P. O. No.:   27810

Sample No.,  9-6 E 1367
                                                 Date: March 9, 1977


                                                 Analyst!  S.  Sweeney


                                                 IAD NO.: 97-A101-134-21
                                CONCENTRATION IN
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead <>.07
Thallium
Mercury NR
Gold
Platinum
IHdlum
Osmium
Rhenium
Tungsten <0.06
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmlum
Dysprosium
ELEMENT CONC
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium 0.02
Lanthanum 0.03
Barium 0.1
Cesium 0.004
iodine 0.02
Tellurium
Antimony
Tin 10.02
Indium STD
Cadmium
Silver 3>-01
Palladium
Rhodium

ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

0.06

0.02

0.02
0.003
0.02
<0.02
0.01

<0.009
0.03
0.03
*0.08
0.002
0.5
0.01
*0.06

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
,. *
CONC.
0.002
0.06
£0.002
MC
0.7
0.3
0.4
0.5
1
0.1
0.5
MC
•0.4
NR
NR
NR
0.01
<0.001
0.01
NR
 NR - Not R*port*d
 All •Imwnls not reported < 0.01

 heterogeneous
                                     Approved:
                                           485

-------
            COMMERCIAL TESTING  &  ENGINEERING CO.
            •ENERAL OrriCCt: tt« NORTH LA (ALLE STREET, CHICAOO, ILLINOIS IOM1 • AREA CODE 111 T*»-«414
 Reply to      iNsiniMtNTAi ANMYSIS OIVUION,  UMS WEST tm» AVENUE, GOLDCN, COLORADO KMOI, rttom-. 30-27*401
TO! Mr. John 6. Michalovic ^••iJBiv
Calspan Corporation •—•«>•
Post Office Box 235
Buffalo. NY 14221
P.O. No.: .27810
Sample No.: 9-6 F 1361
Date: March 11, 1977
Analyst: S. Sweeney
IAD No.: 97-A101- 134-21
CONCENTRATION IN PS/ml
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead ^3.07
Thallium
Mercury NR
Gold
Platinum
Iridlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium £0.04
Cesium
Iodine 
-------
Reply to
COMMERCIAL TESTING  & ENGINEERING  CO.
BINE*Al OFFICE*: tit NORTH LA tAUE tTtECf, CHICAOO, ILLINOIt tOttl • AREA CODE tU »»«-M14
  INSTHIMiNIAl ANALYSIS DIVISION.  U*M WIST MTM AVENUE. 6OUXN. COlOtADO KMOI, MONEi 1O-27MSI
To:  Mr.  John G. M1cha1ov1c
    Calspan Corporation
    Post Office Box 235
    Buffalo. NY 14221
P.O.No.:  27810

Sample No.: g.g Q 1355
                                                  Date:  March 11. 1977
                                                             Analyst:  s. Sweeney
                                                  IAD No.:  97-A101-134-21
                                CONCENTRATION IN
ELEMENT CONC.
Uranium
Thorium
Bismuth
Lead £0.2
Thallium
Mercury NR
Gold
Platinum
IHdium
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetium
Ytterbium
Thulium
Erbium
Holmium
Dysprosium
ELEMENT CONC.
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium 0.2
Cesium
Iodine £0.5
Tellurium
Antimony 0.2
Tin 0.1
Indium STD
Cadmium «>-07
Silver HC
Palladium
Rhodium

ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

<0.1

0.08
0.03
0.06
0.02
<0.8
<0.3
0.1
0.07
0.2
<0.06
0.07
0.05
<0.007
0.7
0.05
0.1

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
s
CONC.
0.008
<0.1
<0.006
7
MC
0.3
MC
0.2
MC
0.02
2
MC
MC
NR
NR
NR
0.09
0.002
0.005
NR
 NR - Not Reported
 All elements not reported < 0.04 |ig/ml
                                      Approved:
                                                         f
                                             487

-------
 Reply to
COMMERCIAL TESTING &  ENGINEERING CO.
•INMAI OPFIOUl lit MORTN LA IAUI CTMtT, OMIOASO, IUINOII «0«01 • AM* CODE It* TK-I4I4
  INITIUMINTM ANAITMI PIVItlON.  M3M VMS? 44TN AVINUI, OOIMN, OHOtAOO IMOI. WONIi MMWMI
To:  Mr.  John 6. Mlchalovlc
     Calspan Corporation
     Post Office Box 235
     Buffalo, NY 14221
 P.O. No.:  27810

 Sample No.,  g_6 H KVB 11028
                                                 D.to:  March 9, 1977


                                                 Analyst!   S.  Sweeney


                                                 IAD No.,  97-A101-134-21
                               CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium 6
Thorium 3
Bismuth <0.4
Lead 8
Thallium
Mercury NR
Gold
Platinum
IHdlum
Osmium
Rhenium
Tungsten <1
Tantalum
Hafnium
Lutetian
Ytterbium
Thulium
Erbium 0.5
Holmlum 0.5
Dysprosium 1
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymlum
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium'
Silver
Palladium
Rhodium

CONC.
0.2
1
0.5
4
5
3
26
21
86
3
4

<0.4
0.5
STD





ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Z1nc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

2
5
32
7
140
14
1
0.8
10
0.5
5
13
5
7
3
MC
68
18

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
CONC.
20
590
0.9
MC
MC
45
14
340
MC
MC
MC
MC
•280
NR.
NR
NR
5
0.1
6
NR
NR - Not Reported
All •(•nwnti not reported <0.2 pom weight
                                   Approved:
                                        4 88

-------
          COMMERCIAL TESTING &  ENGINEERING  CO.
          MNIMl OrCIOMl til MOUTH LA »AUI «T*IIT, OHIOAeO, ILIINOI* «OI01 • ARIA COB* 31* tII-I4I4
Reply 10      INITMMMNtM ANAlYtll MVWON, MIU WIST 44TN AVINUI, COIMN, COIOIAM MM), MONt. MMTMitl
To>  Mr. John 6. M1chalov1c
    Calspan Corporation
    Post Office Box 235
    Buffalo, NY 14221
P.O. Me..  27810

Semple No..g_6 I f 1029
                                    Due: March 11.  1977


                                    Analyst! s.  Sweeney


                                    IAD No..  97-A101-134-21
                              CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium <4
Thorium <5
Bismuth <0.9
Lead 4
Thallium <1
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
Lutetlum
Ytterbium
Thulium
Erbium 0.9
Holmlum 2
Dysprosium 2\
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodynrium
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium

CONC.
0.7
2
1
7
6
3
20
23
220
<0.3
0.6

<0.9
<1
STD
0.8




ELEMENT
Ruthenium
- Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

<3
3
73
7
180
9
<2
2
8

6
27
5
14
9
MC
100
45

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron
Beryllium
Lithium
Hydrogen
jt
CONC.
30
MC
6
MC
MC
60
35
MC
MC
MC
MC
MC
MC
NR
NR .
NR
16
0.6
50
NR
 NR - Not Reported
 All «lem«nti not reported
<0.2ppm weight          Approved,   ^jjrj
                                         489

-------
          COMMERCIAL TESTING & ENGINEERING CO.
          •CNEtAi orricet: »»§ »O»TM LA *AUC »T*»T, CMICABO, IUINOI* ioioi • A»E* cooe »« »»»-»«»4
Reply to      uanuMfMiAt ANAITM DIVISION.  UMS WIST 4«H AVSMUI, GOIWN. CQUKAOO Knot, mom,
To:   Nr. John 6. Michalovlc
     Calspan Corporation
     Post Office Box 235
     Buffalo. NY 14221
P.O. No.: 27810

Sample No.: 9-6 J 11030
             Date:  March 9,  1977
                                                           Analyst:  S.  Sweeney
             IAD No.: 97-A101-134-21
                               CONCENTRATION IN PPM WEIGHT
ELEMENT CONC.
Uranium 3
Thorium 5
Bismuth <0.3
Lead 64
Thallium 5
Mercury NR
Gold
Platinum
Irldlum
Osmium
Rhenium
Tungsten
Tantalum
Hafnium
lute t.1 urn
Ytterbium
Thulium
Erbium
Hoi ml urn
Dysprosium
ELEMENT
Terbium
Gadolinium
Europium
Samarium
Neodymium
Praseodymium
Cerium
Lanthanum
Barium
Cesium
Iodine
Tellurium
Antimony
Tin
Indium
Cadmium
Silver
Palladium
Rhodium

CONC.
0.2
0.7
0.3
2
5
4
26
48
190
26
21

0.6
0.7
STD
0.3
0.3



ELEMENT
Ruthenium
Molybdenum
Niobium
Zirconium
Yttrium
Strontium
Rubidium
Bromine
Selenium
Arsenic
Germanium
Gallium
Zinc
Copper
Nickel
Cobalt
Iron
Manganese
Chromium

CONC.

5
6
46
6
230
300
34
2
25
0.4
6
39
6
7
3
MC
180
27

ELEMENT
Vanadium
Titanium
Scandium
Calcium
Potassium
Chlorine
Sulfur
Phosphorus
Silicon
Aluminum
Magnesium
Sodium
Fluorine
Oxygen
Nitrogen
Carbon
Boron.
Beryllium
Lithium
Hydrogen
CONC.
33
MC
3
MC
MC
MC
MC
760
MC
MC
MC
-*IC
^-620
NR
NR
NR
7
0.2
55
NR
NR -~ Not Rtportta
All element* not reported <0.2ppm weight
Approved:
                                         490

-------
                          m.m ™,^ECHISICAL REPORT DATA
                          (neate read Inaructiom on the reverse before c
         fore completing)
 EPA-600/7-79-015b
                           2.
                                                      3. RECIPIENT'S ACCESSION NO.
         SUBTITLE
Application of Combustion Modifications to Industrial
Combustion Equipment (Data Supplement A)
               6. REPORT DATE
               February 1979
               6. PERFORMING ORGANIZATION CODE
                      > H.J.Buening, W.A.Carter,
P.K. Engel, S. C. Hunter, and R. J. Tidona
               8. PERFORMING ORGANIZATION REPORT NO.

               KVB 6002-734a
  •ERFORMING ORGANIZATION NAME AND ADDRESS'
KVB, Inc.
17332 Irvine Boulevard
Tustin,  California  92680
               10. PROGRAM ELEMENT NO.
               EHE624A
               11. CONTRACT/GRANT NO.
               68-02-2144
 12. SPONSORING AGENCY NAME AND ADDRESS
 EPA, Office of Research and Development
 Industrial Environmental Research Laboratory
 Research Triangle Park, NC 27711
               13. TYPE OF REPORT AND PERIOD COVERED
               Supplement; 1/76 - 1/78
               14. SPONSORING AGENCY CODE
                EPA/600/13
 is:SUPPLEMENTARY NOTES ffiRL-RTP project officer is Robert E. Hall, MD-65, 919/541-
 16. ABSTRACT
          The supplement provides raw data from a study of the effects of combustion
 modifications on air pollutant emissions from a variety of industrial combustion
 equipment. Tested were 22 units, including refinery process heaters; clay and
 cement kilns; steel and aluminum furnaces; boilers burning black liquor, woodbark,
 and CO gas; internal combustion engines; and gas turbine combined cycles.  Process
 variables, fuel types,  excess air reduction, burner adjustments, and staged combus-
 tion were evaluated primarily for their effect on NOx emissions. Emissions of NOx,
 SOx, CO, and HC were measured on all units. Emissions of particulate mass and
 size, trace species, and organics were measured on selected units. This data
 supplement is intended for researchers who wish to perform their own detailed
 calculations.
 17.
                              KEY WORDS AND DOCUMENT ANALYSIS
                 DESCRIPTORS
   b.lDENTIHERS/OPEN ENDED TERMS

   Air Pollution Control
c. COSATI Field/Group

13B
 Air Pollution
 Combustion
 Boilers
 Furnaces
 Nitrogen Oxides
 Dust
 Fossil Fuels
Chemical Analysis
Industrial Processes Statio
Gas Turbine EnginesjCombus
Reciprocating En-
  gines
Organic Compounds
Inorganic Com-
  oounds	
         mary Sources
         iustion Modification
    Particulate
    Excess Air
    Staged Combustion
21B
13A

07B
11G
21D
07D
13H
2 IE

21G
07C
 lit DISTRIBUTION STATEMENT
 Unlimited
    19. SECURITY CLASS (TltOKepor
    Unclassified	
    20. SECURITY CLASS (Thitpagel
                                                                       501

                                                                  22. PRICE
   Form aaao-i CM*   ^SUppl. A)   ~~

^U.S.GOVERNMENTPRINTINGOFnCE: 1979-640-
    Unclassified

 1§T

itl90REGIONNO.4

-------