v>EPA
United States      Industrial Environmental Research EPA-600/7-80-075b
Environmental Protection  Laboratory         April 1980
Agency        Research Triangle Park NC 27711
Environmental
Assessment of Utility
Boiler Combustion
Modification  NOX
Controls: Volume 2.
Appendices

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-600/7-80-075b

                                              April 1980
Environmental Assessment of Utility
Boiler Combustion Modification  NOX
    Controls:  Volume 2. Appendices
                          by
                K.J. Lim, LR. Waterland, C. Castaldini,
                  Z. Chiba, and E.B. Higginbotham

               Acurex/Energy and Environmental Division
                      485 Clyde Avenue
                  Mountain View, California 94042
                    Contract No. 68-02-2160
                  Program Element No. EHE624A
                EPA Project Officer: Joshua S. Bowen

              Industrial Environmental Research Laboratory
            Office of Environmental Engineering and Technology
                 Research Triangle Park, NC 27711
                        Prepared for

              U.S. ENVIRONMENTAL PROTECTION AGENCY
                 Office of Research and Development
                     Washington, DC 20460

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                              ACKNOWLEDGEMENT

       The work presented in this final report was performed as part of
the NO  Control Technology Environmental Assessment program under
      J\
Contract 68-02-2160 to the U.S. Environmental Protection Agency,
Industrial Environmental Research Laboratory, Combustion Research Branch.
The support and assistance of Dr. J. S. Bowen and Messrs. R. E. Hall,
D. G. Lachapelle, W. S. Lanier, and G. B. Martin of the Combustion
Research Branch are most gratefully acknowledged.
       The authors would also like to thank the following individuals for
graciously supplying background and support information:  J. Barsin and
E. Campobenedetto of the Babcock and Wilcox Company; J. Vatsky of the
Foster Wheeler Energy Corporation; W. Barr, F. Strehlitz, and E. Marble of
the Pacific Gas and Electric Company; R. Meinzer of the San Diego Gas and
Electric Company; G. A. Hollinden of the Tennessee Valley Authority; and
W. Pepper of the Los Angeles Department of Water and Power.
                                     iii

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                                  PREFACE

       This is the first in a series of five process engineering reports
documented in the "Environmental Assessment of Stationary Source NO
                                                                   A
Combustion Modification Technologies"  (NO  EA).  Specifically, this
                                         A
report documents the environmental assessment of NO  combustion controls
                                                   A
applied to utility boilers.  The NO  EA, a 36-month program which began
                                   A
in July 1976, is sponsored by the Combustion Research Branch of the
Industrial and Environmental Research Laboratory of EPA  (IERL-RTP).  The
program has two main objectives:  (1) to identify the multimedia
environmental impact of stationary combustion sources and NO  combustion
                                                            A
modification controls applied to these sources, and (2)  to identify the
most cost-effective, environmentally sound NO  combustion modification
controls for attaining and maintaining current and projected NOp air
quality standards to the year 2000.
       The NO  EA is assessing the following combination of process
             A
parameters and environmental impacts:
       •   Major fuel combustion stationary NO  sources:  utility
                                              A
           boilers, industrial boilers, gas turbines, internal combustion
           (1C) engines, and commmercial and residential warm air
           furnaces.  Other sources (including mobile and noncombustion)
           will  be considered only to the extent that they are needed to
           determine the NO  contribution from stationary combustion
           sources.
       •   Conventional and alternate gaseous, liquid and solid fuels
       t   Combustion modification NO  controls with potential for
                                     /\
           implementation to the year 2000; other controls (flue gas
           cleaning, mobile controls) will  be considered only to estimate
           the future need for combustion modifications
                                     iv

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       •   Source effluent streams potentially affected by NO  controls
                                                             J\
       t   Primary and secondary gaseous, liquid and solid pollutants
           potentially affected by NO  controls
                                     /\
       •   Pollutant impacts on human health and terrestrial or aquatic
           ecology
       To achieve the objectives discussed above, the NO  EA program
approach is structured as shown schematically in Figure P-l.  The two
major tasks are:  Environmental Assessment and Process Engineering
(Task B5), and Systems Analysis (Task C).  Each of these tasks is designed
to achieve one of the overall objectives of the NO  EA program cited
                                                  A
earlier.  In Task B5, of which this report is a part, the environmental,
economic, and operational impacts of specific source/control combinations
are evaluated.  On the basis of this assessment, the incremental
multimedia impacts from the use of combustion modification  NO  controls
                                                             A
will be identified and ranked.  Systems  analysis in turn uses the results
of Task B5 to identify and rank the most effective source/control
combinations to comply, on a local basis, with the current  N02 air
quality standards and projected NO,, related standards.
       As shown  in Figure P-l, the key tasks  supporting Tasks B5  and  C are
Baseline Emissions Characterization  (Task Bl), Evaluation of Emission
Impacts and Standards  (Task B2),  Experimental Testing  (Task B3),  and
Source Analysis Modeling  (Task D).  The  arrows  in  Figure  P-l show the
sequence of subtasks  and  the major interactions  among  the tasks.  The oval
symbols identify  the  major outputs of each  task.   The  subtasks  under  each
main task  are shown on the  figure from the  top  to  the  bottom of  the page
in  roughly the  same order  in which they  will  be  carried  out.
       As  indicated above,  this  report  is  a part of  the  Process
Engineering and  Environmental  Assessment Task.   The  goal  of this  task is
to  generate process evaluations  and  environmental  assessments  for specific
source/control  combinations.   These  studies will  be  done in order of
descending priority.   In  the  first year  of  the NO   EA, all  the sources
                                                  A
and controls  involved in  current and  planned  NO  control  implementation
                                                A
programs  were  investigated.   The "Preliminary Environmental Assessment of
Combustion Modification  Techniques"  (Reference P-l)  documented this effort
and established a priority ranking  based on source emission impact and

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potential for effective NOX control, to be used in the current ongoing
detailed evaluation.
       This report presents the assessment of combustion modification
NO  controls for the first source category to be treated, utility
  A
boilers.  Other environmental assessment reports documented are:
       •   Environmental Assessment of Industrial Boiler Combustion
           Modification NO  Controls (Reference P-2)
                          ^
       •   Environmental Assessment of Combustion Modification Controls
           for Stationary Gas Turbines (Reference P-3)
       •   Environmental Assessment of Combustion Modification Controls
           for Stationary Internal Combustion Engines  (Reference P-4)
       •   Environmental Assessment of Combustion Modification Controls
           for Residential and Commercial Heating Systems  (Reference  P-5)
                                     vn

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                           REFERENCES FOR PREFACE
P-l.   Mason, H. B., et al., "Preliminary Environmental Assessment of
       Combustion ModTFication Techniques.  Volume II:  Technical
       Results," EPA-600/7-77-119b, OTIS-PB 276 681/AS, October 1977.

P-2.   Lim, K. J., et a!., "Environmental Assessment of Industrial Boiler
       Combustion Modification NOX Controls," Acurex Draft Report
       TR-79-10/EE, EPA Contract 68-02-2160, Acurex Corp., Mountain View,
       CA, June 1979.

P-3.   Larkin, R., et al., "Environmental Assessment of Combustion
       ModificationToTilrols for Stationary Gas Turbines," Acurex Draft
       Report TR-79-18/EE, EPA Contract 68-02-2160, Acurex Corp.,
       Mountain View, CA, June 1980.

P-4.   Lips, H. I., et al., "Environmental Assessment of Combustion
       Modification Controls for Stationary Reciprocating Internal
       Combustion Engines," Acurex Draft Report TR-79-14/EE,  EPA Contract
       68-02-2160, Acurex Corp., Mountain View, CA, July 1979.

P-5    Castaldini, et al., "Environmental Assessment of Combustion
       ModificationTontro 1 s for Residential and Commercial Heating
       Systems," Acurex Draft Report TR-79-17/EE, EPA Contract  68-02-2160,
       Acurex Corp., Mountain View, CA, September 1979.
                                    viii

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                             TABLE OF CONTENTS


Section                                                                Page

            PREFACE	     iv

APPENDIX A  NOX CONTROL DATA FROM BABCOCK & WILCOX COMPANY ....     A-l

APPENDIX B  NOX CONTROL DATA FROM FOSTER WHEELER
            ENERGY CORPORATION 	     B-l

APPENDIX C  SUMMARY OF NOX CORRELATION TEST DATA	     C-l

APPENDIX D  NOX EMISSIONS CORRELATION:  ANALYSIS OF VARIANCE ...     D-l

APPENDIX E  INPUTS TO COST ANALYSIS CALCULATION ALGORITHM  ....     E-l

APPENDIX F  CONVERSION FACTORS .....  	     F-l

APPENDIX 6  LIST OF ABBREVIATIONS	     6-1
                                      IX

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                                 APPENDIX A
              N0¥ CONTROL DATA FROM BABCOCK & WILCOX COMPANY
                A

       All four major boiler manufacturers were invited to submit process
data to aid in the assessment of NO  control technology.  For those who
                                   /\
did respond, their replies are provided here in Appendix A and in
Appendix B.
       The information presented in this appendix was graciously supplied
by the Babcock & Wilcox Company of Barberton, Ohio to aid in the NOX
control assessment.  It is reproduced here in its entirety.
                                     A-l

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Babcock&Wilcox
                                  Power Generation Group

                                  Barberton. Ohio 44?03

                                  Telephone: (216) 753-1511
                                     November 15,  1977
  Mr. Ken Lim
  Acurex/Aerotherm
  485 Clyde Avenue
  Mountain View,  CA

  Dear Ken:
94042
  In response  to your  request  for  information to complete your
  environmental assessment  contract with the EPA,  the following
  information  is provided as a review of the Babcock And Wilcox
  Company achievements in NOX  control.

  A.   TECHNICAL PAPERS

       "The Dual Register Pulverized Coal Burner - Field Test
       Results", E. J.  Campobenedetto

       "The Dual Register Pulverized Coal Burner",  J. A. Barsin

       "NOX Formation  In Premixed  Combustion:  A Kinetic Model
       And Experimental Data",  H.  B.  Lange,  Jr.

       "Nitric Oxide Control For Oil And Gas Fired Utility Boilers",
       D. E. James

       "Effect Of Coal And  Multi-Fuel Firing On Industrial Boiler
       Design", J. D.  Blue

       "Nitric Oxide Control - A Program Of  Significant Accomplish-
       ments", W. H. Barr and  D. E.  James

       "Nitric Oxide Reduction Through Controlled  Combustion - A
       Challenge To The Boiler Designer",  B.  C.  Krippene

       "Burner And Boiler Alterations For NOX Control",  B. C.
       Krippene

       "The Effect Of  Design And Operation Variables On NOX
       Formation In Coal Fired Furnaces:  Status Report", W.  J.
       Armento and W.  L. Sage

                                  A-2
                      The Babcock&Wilcox Company / Established 1867

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BabCOCk&WilCOX                      -2-                 November 15, 1977
         "Control Of NOX In Power Plant Operations", W. H. Barr

         "Liquid Fuel Analysis  - Their Effect On Combustion And
         Emissions", G. H. Weidman  and P. M. Utterback

         "Pulverized Coal  - New Requirements And Challenges", 0.
         W.  Durrant

         "Design Of Large  Coal  Fired  Steam  Generators", K. H. Haller

         "A  Boiler Manufacturer's View On Nitric Oxide Formation",
         D.  E.  James

         "Design Considerations For NOX Control Of  Natural Gas -
         Fired  Power Boilers",  B. C.  Krippene


    B.    DESIGN COMPARISON

         Prior  to  enactment  of  the  New Source Performance Standards,
         modifications  were  made  to units  to decrease  the slagging
         potential in  the  furnace.  The major design change  was  a
         reduction in  heat input  to furnace plan  area  from an average
         of  2.1 x  106  BTU/sq.  ft. hr. to  about  1.8  x 106  BTU/sq.  ft.
         hr. This change, which  took place in  1970, also helped to
         reduce NOX emissions.

         A comparison  of  a unit designed  with  the above  liberal  heat
         release per plan, but prior  to  the NSPS  with  a  unit designed
         to  control NOX emissions to  meet the  current NSPS levels in-
         dicate very little  change  outside of  the burner zone.   Attached
         are copies of Performance  Summary Sheets and Sectional  Side
         Views  for two typical eastern  fuel-fired units.   Unit No.  1
         was sold  prior to the NSPS  (no  NOX guarantee)  and Unit  No. 2
         was sold  to meet the NSPS  NOX  limit  of 0.7 lbs/106BTU.

         Both units are identical in  physical  size and steam generating
         capacity.  The design differences were included in  Unit No. 2
         for NOX control.  The differences include:

         1.   Replacing the high turbulence, rapid mixing cell burner
             with the  limited turbulence dual register burner,

         2.   Increasing the  burner zone by spreading the burners
             vertically to include 22%  more furnace surface, and

         3.   Metering and controlling the air flow to each row of
             burners with a compartmented windbox.


                                    A-3

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Babcock&Wilcox                      -3-                November 15, 1977
        To provide these changes for NOX control, the price increase
        was about $1.75 - $2.50/KW.

        Overfire air ports were also included on Unit No. 2 since
        NOX data for the dual register burner was not available at
        the time the unit was designed.  To account for the five  (5)
        percent excess air required to cool the ports, the total
        excess air at full load was increased from 20% to 22%.
   C.   NOy REDUCTION TECHNIQUES - OIL FIRING

        Over the past years, B&W has been involved in a wide variety
        of NOX reduction programs on oil-fired units.  The majority
        of these programs have included utilizing one or more NOX
        control techniques.  The methods used are dependent on the
        size, and age of the unit as well as the final level of NOX
        to be achieved.  The following is a list of NOX control
        methods applicable to new units or as retrofit solutions
        to meet increasingly lower NOX levels.

        1.  Burner Zone Sizing

            This is applicable to new units only.  NOX emissions
            can be decreased by reducing the quantity of heat
            released per square foot of cooling surface in the
            burner zone.  For a decrease of 40% in heat release
            rate, NOX can be reduced by up to lOOppm.  This
            decrease in heat release rate is achieved by spreading
            the burners through larger vertical spacings.

        2.  Burner Design

            This NOX control technique can be applied to both new
            and existing units.  Based on NOx reductions of up to
            50% on P.C. firing with the dual register burner, a
            similiar concept has been applied to oil fired units.
            Data from an oil-fired unit retrofitted with this
            burner has shown a 20-30% reduction in NOX formation
            through controlled air and fuelmixing at each burner.
            However, this method is costly and may not be applicable
            on small units.  Also,  depending on the remaining life
            of the unit and the number of burners to be retrofitted,
            this method may not be cost effective.
                                   A-4

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Babcock&Wilcox                       -4-                November  15, 1977
              Gas  Recirculation

              The  gas  recirculation is  effective  on new units  designed
              to handle the  additional  mass  flow  of the recirculated
              flue gas.   On  units  recently tested,  a 25-30%  reduction
              in NOX was achieved  utilizing  gas recirculation  through
              the  windbox or furnace hopper.   The above reduction is
              based on a base line condition with the gas recirculation
              fans out of service.

              Gas  recirculation can also be  used  as a retrofit for NOX
              reductions.  However, based on test results, NOX reductions
              are  not  as pronounced as  for new units.  NOX reductions
              of up to 20% have been obtained depending on the base
              line NOX emissions and the size of  the furnace.   It
              appears  that the increased mixing and turbulence caused
              by the additional mass flow limits  the NOX reductions.
              Again, the cost effectiveness of this technique  should
              be compared to other methods of NOX control for  each
              specific application.

              Two-Stage Combustion

              Two stage combustion using NOX ports is an effective
              method of NOX reduction.   NOX reductions of up to 50%
              have been achieved by using NOX ports.  However, this
              type of firing requires special attention for several
              reasons:

              1.  The mixing of fuel and air must be maximized to
                  prevent both smoking and excessive CO emissions,

              2.  To maintain adequate mixing normally requires
                  additional quantities of excess air to prevent
                  smoking, and

              3.  There  is an increased potential for lower furnace
                  tube wastage when burning high sulfur oil under
                  sub-stoichiometric conditions.  -The above will add
                  additional operating and maintenance costs  to a
                  unit  designed with ports.

              The above  problems  also  exist when a  unit  is  retrofitted
              for two  staging.  Mixing becomes a problem  due  to  the
              reduced burner pressure  drop with  the  15-25%  reduction
              in  air  flow to the  burners.  In  addition,  some  units
              may not  have  the  required  furnace height  to add ports
              eight (8)  feet above the top row of  burners.  The  cost
              of  this  retrofit  includes  not only  the NOX  ports,  but
              also  the  additional windbox and  flues  required  to  get
              air flow  to this  elevation of  the  furnace.

                                     A-5

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Babcock&Wilcox                      -5-                November 15,  1977
        5.    Burners Out Of Service (BOOS)
             This method of off-stoichiometric firing requires little,
             if any,  boiler modification.   BOOS can be applied to both
             new and  existing units as an  effective NOX control tech-
             nique.   BOOS consists of removing one or more selected
             burners  from oil service and  admitting air through the
             idle burner(s).  NOx reduction of up to 35% can be achieved
             while manitaining acceptable  levels of CO (less than
             lOOppm).

             This method of NOX reduction  would require testing the
             unit in  question to establish the BOOS pattern that most
             effectively reduces NOX while maintaining acceptable
             operating conditions.  Depending on the capacity of
             the existing burners, the only modification necessary
             would be a change of sprayer  plate size to permit full
             load operation with one or more burners out of service.
             This method of off-stoichiometric firing keeps the
             combustion air in the burner  zone where it is most
             effective for combustion.

        6.    Low Excess Air Operation

             This method is very cost effective as well as an effective
             NOX control device.   For each five (5)  percent reduction
             in excess air to the burners  a 25-35ppm reduction in NOX
             is obtained.   Depending on the burner used,  it is possible
             to reduce the excess air to the burner to %5 with acceptable
             CO emissions.  Excess air levels as low as 3% to the burners
             have been achieved during recent testing.

        7.    Change Of Oil Supply

             The amount of nitrogen in the fuel oil directly affects
             the NOX  emissions.   Laboratory tests indicate that about
             50% of the total NOX is attributable to fuel bound nit-
             rogen.   The nitrogen in oil can vary from 0.1%N   to
             1.0% N    by weight and above.   On a given unit,  NOX can
             be decreased by 15-25ppm per  0.1% decrease in fuel nit-
             rogen content.

        The  above control techniques are not additive.   However,  it is
        normally possible to apply a combination of the above methods
        to optimize NOX reductions.   Before a decision can be made as
        to the  optimum combination for lowest NOX,  each specific unit
        must be reviewed regarding age,  size,  base line NOX emissions,
        and  the final  NOX emission level required.
                                   A-6

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Babcock &WHCOX                       -6-                 November  15,  1977
    D.    PACIFIC  GAS AND  ELECTRIC  DATA

         The data you  requested regarding the Pacific  Gas  And Electric
         Company's boilers  retrofitted  for NOx control will  be forwarded
         to you through Mr.  W.  H.  Barr  of Pacific Gas  And  Electric  as
         requested in  his letter of October 20,  1977.

    After you review the  above  information, please call me if you have
    any other questions concerning Babcock & Wilcox's  experience in
    NOX control.

    The above has been submitted to Acurex/Aerotherm with  the under-
    standing that Babcock & Wilcox will reserve the right  to review
    and approve or edit the final  report with regard to any information
    submitted by Babcock  &  Wilcox  under this project.

                                     Very Sincerely yours,
                                                  LV
                                      E. J. Campobenedetto,
                                      Combustion Systems
    EJC:er

    CC: G.W. Bouton
        A.M. Frendberg
        L.W. Yoder
                                    A-7

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A-8
Babcock&Wilcox

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A-9
                     Babcock&Wilcox

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ENTERINC RtrtEAlER 2
LEAVING ECOMMIZEI
LEAVIHC AN fEia.LIG)
UAVIK AN (IKL. (.U.}
ENTERING WIT
FuMACE t COIVECT10I >A«C
FLUtS TO AH OUTLET
AID NEATER
TOTAL - FURNACE TO
^PH c/irrLfiT
FUEL BURIED* A 11110(01
DUCTS 1 FLO* NETE.lt
All HEATH

APH INLET
tot. FRON TO FURNACE
Mr CAS
Hj « «?0 |, fotl
NOISTURE II All
MIUDKO COMWSTIIU
•lOMTIO*
UUCC. F0« t NIR5. HARCII

TOTAL HEAT LOSS
rnciEnci OF mil, i



•0. IN USE KB BOILER
TOTAL "Jut », Or hi/Ton NOTOR OUTtU
1 TNRtl 200 U.5.S. SIEVE









Z.-850
2525
3doo '
^66 )
i *
^LV. COAL] PULV. COAL »
NORMAL NORMAL •
41
20
^Q^Q
20 7
20 «
502': 1
1
^bl 457 i
4604 5005 i!
1 i<136 ^v? '




i 1
2550 2620 i
WO 5H?' i
i
21 aa K









2
It 25 2
85 j 150 i
10O5 1005 2
1005 1005 2
59^ 640 >
i

670
\ 206




— m—
100
jH
'
698 ?
^Op ?
i~"4ii '
100 3
S"ij — '
4.9 j
5.9 1.5 3
	 4.1 6.0 3

j 8.1 . 12.4 i
1.9 3.0 .


1.7 2.6 i
2.9 1.4 <
i I '
• i

6.5 10.0
1, B5 i 1.51 i
5.01
0.12
0.^0
0.22
1.50

; liJ.oo
w.oo


•3
13.7

ftCOICTEO KfffORMktCE IS BASED Ol COKftJSTtO* AIR EiTEftlli'
76
5.06 .
0.11 •
0.30 <
0.17 !
1.50

1 1 Jb5 i
B8.35 ,
5
4 5 5
11.0 11.5 s
71 . 74 s

r,l
ux

tfciiHOT r« HUT

RAl
s|![ RBC - p^.
DESIGN PRESSimE 2925/725









j
"


•«TE« ;001.EC SCREfl (CI»CU«IE»E«I IAL)
BATIK iXi.l: InnjEcTiD) 36^190
sunmiEATER IGIKLMFER.EITIAL)



D3
TOTAL FUftNACt NEATIIt SLIHTA^ 70 ^Q ^
SATMATED (CIRCUMFERENTIAL) 7 110
SUPERHEAT R [CIRCUNFEREKT UL) \52.2
•EHCATER (CIKUNFERINTIAL)
51
:o>oNi2E 83.1

70

37
43 '
- TOTAL Fun. i con. rtcssuiE FAIT. HTC. su*F. 3yti.b3b
S FLAT
TOJECTED rUMACE HEAIIK SURFACE
" TO f»Ct Of fWTCRS ^ti,9
TO FACE OF COMECTIO* WtFACE 71 , O
FURIACE


oo
90
VOLUME. CUFT 425.000

TOTAL NEAT IK SlXfACE, S? FT 424.600
Tim: TUBUUVH IPKI. AIR) NO: 1
TOTAL HEATING SURFACE. SO. P^1: 1^9 395

fulL
t«M«
S
3
Tt« CELL BURNER
««. 20
tin MPS HIE ?Q B. 5
10.8OO w« coil AI 71 f r«u nt u.s.s. SIEVE
IS 59. NAIIMM SURFACE MISTUtt 11 10 f REOUUIK 5^0
f All





j
3 «•
til
**•
- « i
MAJ.N STKAM - SPHAV ATOEMrfclKATION
REHEAT STEAM - SPRAY ATTEMPERATION -
EXCESS AIH

BALANCE DRAFT
MEMBRANE WALL
CASING TYPE ROOF SEALS
INDOOR










TTfo-
~f
;J
•I

OESCRIfTIM 1 IV
**1 \
UNIT +±
I


QA.TE





-------
?*






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ANALYSES


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MIlE
SEAM
DISTRICT


£ i;i\:A&1LlTT
s>--:t K:ISTURE. i




*
s
i
',* SOrT.TEMP..F (DEDUCINS)
MvlMoBC, TOTAL
 INLET
STEAM AT SH* INICT
*
.
a
?!


«
*

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-


REHEATED 1
REHEATED 2
EiropioiizfRTo Dhuh e
DHUM TO SH OUTLET
if ». mi. suprtnEAiER
LEAVINC REnEAIER 1
ENTERING REHEATED i
LEAVING REHEATED !
ENTERING VtHtATfR ?
LEAVIku ECQNPMI-'tli
LEAiiwi AH (EICL.LKG)
LEAVING Ah fluri. LKG)
KAIfD EliTEIiUu FC31.0MIZER
ENTEKING UNIT
Lf»JIW. >l« «[»IIB
FLUES TO AH OUTLET
AIR HEATER

TOT: FURN. TO AHH OUT
H.EL tuRNER'J 4 •IdC'iJOl'
purrs t FLO* METER
AIR HEATED


o FROMAPH IN. TO FURN
•i &»i
"> « "?0 IN full

UNluRNED CONBuSTIBlE
RADIATION
UNACC. FOR t MFKS. MARGIN

TOTAL HEAT 1 U. S.i. M»l
1 L'S^O I ^800
' 2f>2fj • TT66

' PULVKRI2ED COAL
NORMAL MAX.
i D1 P:2
'10 -'I >
T->7^ (502ti
'42% 5^00


.'I'.'hO 1)67^
2'*'.1 2AC

2'.';0 2620
'l-'lO l"-H7

22 TO

1 •'!
K(' l£)r;
i'M)5 ion'}
i oo'j loo1;




670 P-)8
286 TOO
270 200
'lr;i? IMfj
100 100
••' 	 ?T5 	 r"5 	
1.2 1 . 4
5.1 fc.3

!''.'• 12 rl
1.0 2.0
c?.» T. 14
T.3 . Ii.6


7.7 10.0
• i.Ko i.^
S.OJ S.02
0. 12 O. 12
O . TO 0 TO
O.ilc! O.17
1.50 l.'O

12.00 VI.7C
8H.OO 38. 2H

	 , rj.Y . ils
"" 7& 7<4
Cl . tOUIPd-NT »{» -»IT
r TIPE RADIANT BOILER
RflC 6^4/PC
DESIGN PRESSURE 2925/725




•
.
,
i
J
:
WATER COOLED VCPCEN (CIRCUMFERENTIAL)
«AT[B COOLED (PROjtCUOl 5
; SUPERHEATED (CIKCUMFEDEKTIAL)
• SUPERHCATCR (PROJECTED) "•

fa. 19o

4 Bo^

SATURATE:. (CI«CU«TE»E'.TI»L) 7 ^10
iuPE»«£ATE» (CIBCu-FERENTIAL) 1521270
• RfHEATER t (CIRCUMFERENTIAL f
4 QS6
• REHEATER J (CIRCUMFERENTIAL)
ECONOMIZER £
T.107
TOTAL CONVECTION HEATING SURFACE 327.6'lT
TOTAL Fu«N. i COM. PMSSuRE PART. HIG. SURF. 39b.bT6

FLAT PROJECTED FURNACE HEATING SuDFACE

; TO FACE of ri»TE»S ^8.900
TO FACE OF CONVICTION SURFACE 71.&90
FURNACE VOLUME. CU FT A 2
• IN
HiATIH
S.OOO
TifPE SEC. AIR REGENERATIVE N0.2 SIZE 29-VI-S9
TOTAL HEATING SURFACE. SO FT 424. 600


PRI. AH: TUBULAR NO. 1
TO
FUEL


TAL HEATING SURFACE. SO. FT. 149. *9<;
TYPE mqFqfSf~pT£p^ Jt£&A4r*-Ji



NO. 40
TTPE MPS SIZE 89 NO. 5
CAPACITr OF PULV. ISTUOO M LB STEAM/HR BASED ON

59 GRIND
10 BOO BTI COAL AT 71 » THDU »o u.s.s. SIEVE
F0«12bx LS COAL/PULV.-HR AT 7Ql THOU 200 U.S.S. SIEVE WN. GRIND




\\\
**
i o S
" m

3m"
WfllN S'J'ISflM: SPKAI /crrJiMfKHATDK
REHEAT STEAM: SPRAY ATTEMPERATOR Ic
EXCESS
AIR

BALANCED DRAFT
MEMBRANE WALL


CASING TYPE ROOP SEALS
INDOOR






• 0


DESCRIPTION 1

4//V/7~ «*-2.


U_ SHI



                                                                      ON 297
                                                                                    nu. B**"-MI ft/IC
                                                                                                              On CONDITIONS t

-------
                                 APPENDIX B
         N0¥ CONTROL DATA FROM FOSTER WHEELER ENERGY CORPORATION
           A

       All four major boiler manufacturers were invited to submit process
data to aid in the assessment of NO  control technology.  For those who
                                   A
did respond, their replies are provided here and in Appendix A.
       The information presented in this appendix was graciously supplied
by the Foster Wheeler Energy Corporation of Livingston, New Jersey to aid
in the NO  control assessment.  It is reproduced here in its entirety.
         A
                                     B-l

-------
      FOSTER WHEELER  ENERGY  CORPORATION

        11O SOUTH ORANGE AVENUE • LIVINGSTON, NEW JERSEY O7O39 • PHONE 201-533-1100

                                 ADDRESS REPLY TO:
                       100 Pino Slrool, Sultn 1795, Snn Francisco, California fM 111
                          Telephone 4)6 • 4?I-R042  TWX: 910-37P-730B


                                                            November 6, 1978
 Acurex Corporation
 U8£ Clyde Avenue
 Mountain View,  California  ?I|OU2

 Attention Dr. K. Lim
                                     Subject:  Final Report for NO,,. Environmental
                                               Assessment Program
                                               F.W.E.C. Contract #2-U3-32U£
                                               Aourex Reference JC68383A
Gentlemen:
Attached please  find three (3)  copies of the subject report entitled,
"Effectiveness of  NOx Emission  Controls on Utility Steam Generators."  This
report may be provided to EPA,  by Acurex, for publishing; any comments made
by Acurex  along  with Foster Wheeler's replies, if any,  are to be appended to
the report.

Also attached are  one set of drawings and data for each of four steam generators
discussed  in the report (labeled Units A, 8, C and E).   The drawings and data
are to be  considered confidential information and are being provided for
Acurex's internal  use only in performing analyses of the steam generators.

We trust this information is in compliance with your requests.  Please advise
us if any  clarification is required.

                                         Very truly yours,

                                         FOSTER WHEELER  ENERGY CORPORATION
                                         J. W.  Keelty?
                                         District Manager
                                         Equipment/Fired Heater Sales
                                         San  Francisco Office
JV:JWK:vo
Eno.
oo Mr. J. Vatsky, FWTO New Jersey
                                         B-2
                        CABLE ADDRESS: REWOP LIVIN03TONNEWJEB8EY

-------
FOSTER WHEELER ENERGY CORPORATION
  11O SOUTH ORANGE AVENUE • LIVINGSTON NEW JERSEY 07O39 • PHONE 2O'-533-HOO
             EFFECTIVENESS OF NOX EMISSION CONTROLS

                             ON

                   UTILITY STEAM GENERATORS
                         Prepared for

                      Acurex Corporation
                   Mountain Tiew, California
                 Acurex Contract No. JC68383A
                  FWEC Contract No. 2-1^3-32^5
                FWEC Project Manager:  J. Yatsky
                   CABLE ADDRESS: REWCP LIVINQSTONNEWJERSEY

-------
                               TABLE OP CONTENTS






SECTION                                                                  PAGE NO.






  1.0         INTRODUCTION                                                 1-1






  2.0         NOX EMISSIONS:  POHMATION AND CONTROL                        2-!




              2.1  NOX Formation                                           ?-1




              2.2  Methods of Control                                      2-5






  3.0         PRACTICAL LIMITATIONS ON LOW BOX Firing    -                  3-'






  U.O         STEAM GENERATOR TEST DATA                                    U-1




              U.1  Pre-NSPS Coal-Fired Units                               k~3




                   U.1.1  Opposed-Fired Steam Generator:   Unit  A          1^-3




                   U.1.2  Front-Wall Fired Stean Generator:   Unit B       i+-*$




                   U.1.3  Sxunmary of Pre-NSPS Unit Data                   U-21;




              U.2  NSPS Coal-Fired Unit                                    U-29



              U-3  Low NOX  Burner Data                                     U-i;1






    5.0        COST DIFFERENTIAL FOR EMISSION CONTROLS                      5-1






    6.0         OIL FIRED UNIT Rffim-FIT F7A 1IOX CONTROL                     6-1




               6.1   Chronology of Unit Performance Modification             6-1



               6.2  Effectiveness of Controls                               6-10




               6.3  Operational Difficulties                                6-15




               6.U  Cost of Modifications                                   6-1?

-------
                                LIST OF FIGURES


FIGURE .NO.                            TITLE                              PAGE .NO.

    2.1          Furnace Flame Basket                                      2-2

    2.2          NOX vs. Q/S                                               2-k

    2.3          Ash Softening Temperature                                 2-7

    2.k          Boundary Air                                              2-9

    2.5          Intervane Burner                                          2-12

    2.6          Low-N0x Coal Burner                                       2-11+


    3.1          Example of Fireside Tube Wastage                          3-2


    U.1          Pre-NSPS Unit A:   Opposed-Fired                           k-k

    U.2          NOX Data Composite:  Unit A                               U-7

    U.3          CO .Data Composite:  Unit A                                U-8

    k.k          Pre-NSPS Unit B:   Front-Wall Fired                        IH7

    U.5          NOX Data Composite:  Unit B                               U-19

    U.6          Pre-NSPS Units:   NOX Reduction Summary                    1^-25

    U.7          NSPS Unit C:  Front-Wall Fired                            U-30

    U-8          NOX Data Compcsite:  Unit C                               U-33

    U.9          CO Data Composite:  Unit C                                h-3k

    U.10         NSPS Units:   NOX  Reduction Summary                        U-UO


    5.1          Unit D:   NSPS Unit (Recently Sold)                         5.6

    5.2          Unit D as Modified to Pre-NSPS Design                     5-7


    6.1          Unit B Pr-s-NSPS Oil-Fired (Retrofit NOX Controls)          6-2

    6.2          Initial Test Results                                      6-5

    6.3          Effect of Gas Recirculation                               6-13

    6.1*          Effect of Load on NOX                                     6-1 k
                                       ii

-------
                                LIST 0? TABLES








TABLE NO.                            TITLE                               PAGE NO.



   U-1              Opposed-Fired Unit Design Parameter                    U-5



   U-2              Measured Test Data:  Unit A                            U-3



   l±-3              Front-Wall Fired Unit Design Parameters                U-18



   ii-U              Measured Test Data:  Unit B                            U-20



   k-5              Typical Ash Constituents:  Units A and B               U-26



   \4-6              NSPS Unit Design Parameters                            U-31



   i;-7              Measured Test Data:  Unit C                            U-35



   U-8              Typical Ash Constituents:  Unit C                      U-33






   5-1              Unit D Design Parameters                               5-8






   6-1              Unit E Design Data and Performance Fuels               6-3



   6-2              Burner Out  of Service  Test Patterns                    6-6



   6-3              Unit E Modification Costs                              6-19
                                       iii

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1.0  INTRODUCTION



     This report is presented by Poster V/heeler Energy Corporation in cooperation



     with the NOX Environmental Assessment Program of the U.S.  Environmental  Pro-



     tection Agency.  Data contained herein were provided from Foster V/heeler's




     test data inventory and are representative of steam generators designed




     prior to and after the advent of the New Source Performance Standard.






     The following information is provided:






     (1)  Emissions and operating data for two pre-NSPS coal-fired steam generators.






     (2)  Emissions and operating data for a coal-fired unit designed to meet



          the NSPS.






     (3)  Incremental costs for NOX controls on a typical 500 MW steam generator;



          as compared to the cost of that unit without NOX controls.






          Emissions and operating data for a pre-NSPS oil-fired steam generator



          that was  subsequently retrofitted with NOX emission  controls after it  was



          sold.   Also, some of the costs associated with the retrofit are supplied.
                                       1-1

-------
2.0  NOv MISSIONS;   FORMATION AMI METHODS OF CONTROL



     A short review of the current view of NOX emissions is presented in order



     that a better understanding of Poster Wheeler's control philosophy will



     be obtained.





     2.1  HO.;;. Formation



          It is generally agreed that the total NOX emission from a coal-fired



          boiler has three components:





          A.  Thermal NQy



              This component is formed from the high temperature fixation of



              atmospheric nitrogen.  Thermal NOX varies exponentially  with



              flame  temperature and is thus dependent on available cooling



              surface.  However,  since it  generally accounts for the smallest



              of the NOX  components, measures  to reduce flame  temperature have



              only a moderate  effect  on  total  NOX  emission.





              Boiler design affects  the  NOX emission in that burner  zone cooling



               surface  influences  the  amount of thermal  NOX formed.   Thus,  for a



               given firing system and fuel,  as unit size  decreases NOx emissions



               increase.   The criterion used to quantify this effect  is the



               Burner Zone Liberation Rate, which is defined as:






               The net sensible heat input to the burner flame basket divided by



               the effective projected surface.  The burner flame basket is the



               six-sided box started at the hopper knuckle and extending ten feet



               above the top row of burners, including all cooling surfaces in



               that  volume.  Figure 2.1 illustrates the flame basket region for a
                                        2-1

-------
OVER FIRE
AIR PORTS
   FLAME BASKET OF TYPICAL  LARGE
    BOILER  BURNER  ZONE SURFACE
     DEFINED BY  H, D AND W.
                  2-2
                                  FIGURE 2-1

-------
    typical  "boiler.  Figure  2.2  demonstrates  the variation of total NOx




    with Burner Zone Liberation  Rate.   It  is  a  composite  of  full load




    test data from front-wall  fired units  all utilizing similar high




    turbulence burners.   The NOX emission  obtained from the  curve




    represents that which would  be  generated  in a  unit, at full load,




    having the specified Q/BZS.   There are a  set of curves which are




    parametric in fuel nitrogen  content per million Btu.






B.  Volatile-Fraction Fuel NQy



    This component of the total  emission is formed from that portion




    of the fuel-bound nitrogen which is contained in the  volatile




    fraction of the fuel.  It is generated in the near-throat region




    of the flame (approximately one to two throat diameters into the




    furnace).  Figure 2.2 also shows the estimated fraction which is




    volatile  fuel NOx; generally at least $0%.






C.  Char-Fraction Fuel NOY



    This component of the total NOx emission is formed from the fuel




    nitrogen contained in the char and is  generated  in the  later




    portion of the flame as the  char  is consumed.  As much  as 2?%




    of  the  total  emission may originate in the char.






A variable  which has  a  major  impact on NOX emissions is  fuel composition




 quality. The specific  parameters  of  interest  are percent fuel nitrogen




 content (% ^2) and. higher heating  value (HSV,  Btu/lb)  on an as-received




 basis.   These parameters determine the total quantity of fuel-bound




 nitrogen being supplied to the  burners.  It  can be expressed as  Ib




 NO 2/106 Btu of heat input (N02/Q).
                              2-3

-------
           UNCONTROLLED  NOX  EMISSIONS

            SINGLEWALL - FIRED  UNITS
  NO.
LB/I06BTU
                                         THERMAL-NO
                                              CHAR FRACTION
                                              FUEL-NOX

                                             VOLATILE
                                             FRACTION
                                             FUEL NOX
        50  100  150  200  250  300  350  400  450
       BURNER ZONE LIBERATION RATE, 1000 BTU/HR-FT2
                         2-1*
                                            FIGURE 2-2

-------
    A coal with high nitrogen content and low heating value will have a




    high NOX emission, most of which will be from  fuel-bound nitrogen.




    Thus measures which affect thermal NOX only  (such as  flue gas recir-




    culation and additional cooling surface) will  have  a  correspondingly




    smaller influence  on  total NOX emission.






    Since  the  total NOX emission contains three  components, each of which




    has a  separate origin,  different NOX control techniques will affect




    each component differently.   Some control methods will reduce all




     three  components  while  others may reduce  only one.






2.2 Methods  of Control




     The New  Source Performance  Standards have had a major impact on the  design




     of steam generating equipment. Many units  sold between  1971 and 1978  were



     designed to burn low sulfur coal  as a means of meeting the  sulfur emission




     regulation of the NSPS.  Generally, the physical size of these units was




     increased to accommodate a wider range  of slagging and fouling character-




     istics of these  coals.   The primary means of NOX reduction has been com-




     bustion modification, but size increase is also necessary to provide the




     additional cooling surface required to accommodate low NOx combustion.






     A.  Reduced Burner Zone Liberation Bate




         The increase  in unit size  caused in part by the NSPS SC>2 and NOX re-




         gulations provides a lowering of the Burner Zone Liberation Rate




         thereby decreasing the  thermal NOX component of  the total NOX emission.




         Thus, the uncontrolled  NOX emission (that  is with no combustion modi-




         fications) is reduced.






         Increased furnace  size,  providing greater burner basket cooling sur-




         face, is advantageous when using low emission  burners  or substoichiometric





                                    2-5

-------
    levels of staged combustion.  When the lower furnace becomes re-




    ducing the ash softening temperatures decrease thereby promoting




    the formation of slag.  The effect of atmosphere condition on ash




    characteristics is illustrated in Figure 2.3-  In general, the lower



    flame temperatures provided by low Burner Zone Liberation Rates



    will decrease ash temperature thereby reducing the potential for




    slag formation.  Also, the abundant cooling surface increases total




    absorption which results in lowar gas temperatures throughout the



    furnace,  thus further reducing slag potential.






    Poster Wheeler uses a combination of techniques which minimize the




    need for larger furnaces, beyond that required by coal quality and




    low KOX combustion.  These are discussed in detail in the following



    section.






B.  Effect of Staged Combustion on NOY




    In general,  the most effective means of reducing all three NO




    components,  simultaneously, is staged combustion.  Reducing air to




    the burners  will decrease thermal and volatile-fraction fuel NOX




    by creating a local reducing atmosphere in the near-throat burner




    region.  Thus the two NOX components, which together account for




    approximately 75% sf the emission,  are affected immediately.






    Char-fraction fuel NOX will also be decreased since most of the




    char will burn out in an oxygen deficient region; oxygen combines




    preferentially with carbon in a reducing atmosphere.  In order to




    maintain low values of carbon monoxide and unburned carbon in the




    flue gas  it  is imperative that proper mixing between the lower
                              2-6

-------
                 I  : I
           I   I
---
—
\£
•r

 :
                 ASH  SOFTENING TEMPERATURE

                                               OXIDIZING BASIS
                                              1  ..:) '  .
                                                 REDUCING
                          TOTAL IRON
COOL ASH (As Fe),
                                               FIGURE 2-3

-------
furnace gases aad the overfire airport air flow be maintained; also,




sufficient residence time below the convection pass is required.






Although staged combustion is a highly effective means of NOx




control it also has the potential for causing severe problems.




With many coals, particularly those with high sulfur, iron and




alkali contents, slagging and waterwall tube wastage can be major




problems.  These are most likely to occur when hot ash particles




approach the furnace walls in a reducing atmosphere.






Poster Wheeler utilizes staged combustion for NOx control but




with two considerations for minimizing the slagging and waafcage




potential:






(1)  The minimum burner stoichiometry recommended for continuous




     operation is $6% of theoretical air.






(2)  Boundary Air is used to provide an oxidizing atmosphere along




     the waterwalls in the hopper and burner zone.  This technique,




     which is illustrated in Figure 2.1;,  consists of air entry




     slots located in the hopper throat and along the hopper slopes




     and ports located on the burner walls.   It has been shown to




     be an effective means of controlling slag in numerous cases.






Staged combustion of coal, at burner stoichiometric levels below




the minimum suggested above,  is possible  from a combustion stability




viewpoint.  Indeed,  there are some low sulfur coals with good




slagging characteristics which would not  be  expected to cause
                         2-8

-------
OVERFIRE
AIR PORTS
BOUNDARY
AIR PORTS
     HOPPER
     SLOPE AIR
                       UNDER HOPPER AIR
         BOUNDARY AIR  CONCEPT
                                    FIGURE 2-4
                     2-9

-------
    wastage problems; although this possibility lias yet to be demon-



    strated in the field.  However, Poster Wheeler would not recommend



    suoh low levels of sub-stoichiometric firing with most coals.



    Boundary Air, which works well when the burner zone is operated



    approximately at or above the stoichiometrio level, would be in-



    effective at low atoichiometric levels with high slagging-potential



    coals.





    Staged firing is thus limited in its practical applicability due to



    the effect on unit availability (slagging) and reliability (tu'oe



    wastage).  Certainly this technique would not be recommended for



    most older, pre-NSPS, coal ficsd units where the Buner Zone



    Liberation Bate would be too high to accommodate staged combustion



    for Continuous operation.  However, this technique may be considered



    on some older units where furnace sizing and coal characteristics



    are acceptable.





C.  Effect of Burner Design



    The actual fraction of each NOx component, formed in a given unit,



    depends primarily on unit design, burner design and coal charac-



    teristics; the relative emissions can thus vary from unit to unit.



    However, since volatile-fraction fuel NOX is formed in the early



    part of the flame and comprises the major part of the emission,



    burner design will have a drastic effect on NOX emissions.  Burner



    Zone Liberation Rate will "lave aa important but secondary influence



    on the NO-^ ^ulssion for ooal or high nitrogea-content oil.
                             2-10

-------
The Foster Wheeler Intervane Burner, shown in Figure 2.5»  was used



"or many years prior to the advent of the NSPS.  Tftis burner was



design-id for high combustion efficiency in the physically small



(high Burner Zone Liberation Rate) pre-NS?3 boilers.  As guuh i L.



is a high intensity, high turbulence device which vas very success-



ful in achieving the purpose for whi^h it was designed.  However,



its highly turbulent nature results in relatively high N0-.t -Missions.



In order to permit staged combustion to be used with a wide range



of coals, as the primary means of NOX control on earlier HSP3



boilers (those  soli between 1971 and 197$), without resorting to



burner shoiihiometries below 9^6 it was necessary to modify the



Intervaa? Burner.  Initial modifications permit bed  the  single



register design to be  retained while geometrical relationships



were changed to provide reduced turbulent  mixing in the early



part of the flame.  This Reduced Turbulence Burner,  which is



similar to that shown  in Figure 2.5, provides NOX levels  1£-20$



below historical levels for Foster Wheeler Intervane Burners.





In order  to provide greater flexibility of operation,  and further



assurance  that the NOX emission regulation of 0.7 It) N02/10° Btu



can be  achieved with a minimum of overfire air, Foster Wheeler



has developed a dual register low NOX coal burner.   This design



 is shown in Figure 2.6.   NOX reductions of UO-50S4 ^-~r^ 'oeon ob-



 tained with this burner when retrofitted to older steam generators.



 Functionally, the low NOx burner consists of the following components:
                           2-11

-------
                                             INTERVANE   BURNER

                                              (PRE-NSPS  DESIGN)
ro
                         OIL GUN
                           OR
                         IGNITOR
                                                                        C.LCUHDAK\ AIR
                                       ASPIRATOR RING
PULVERIZED RJFL AND
 PRIMARY AIR INI LT


       PULVLRI/EO Ultl BODY  /  ADJUSTABl I  VAfJfS
                                   GAS RING
                           GAS CANCS
                                         VANF OPERA
                                           MLCHANISM
ING
                 SICONI.V-.iv'Y AIR
                                                                                      STUDiHT.
                                                                                       i: cnru f
                                                                                      IHROA1
                                                                           FIGURE 2-5

-------
Two registers;  to provide independent control of the




secondary air swirl in each of the two secondary air



annulii.  The rate of mixing between secondary air and the




primary air/coal stream can therefore, be controlled.







Annular coal noazle;  with an axially movable inner sleeve




to provide a method of optimizing the velocity of the



primary air/coal stream, at constant air flow.






Perforated plate air hood, and movable sleeve.?  Pressure drop




across the perforated plate is measured to provide an




index of relative air flow to the burners; the movable




sleeve permits balancing of the  secondary air between the




burners.  Thus, burner  atoichionetry  can be nore closely




controlled  than has boon historically possible.
                       2-13

-------
         LOW  NOX  DUAL REGISTER  COAL BURNER
         0-,
plate
fc O O OC
 O OO 
3 © © ©€
movable
air hood
                                       —4
   outer coal nozzle
                               movabl
                               •i»
                               tip
          _air
          vane
                       air divider
          air register
                                   iiirnace
                                   side
                              LOW NOx  BURNER
                                (coal fired)
                            2-1
                                              FIGURE 2-6

-------
3.0  PRACTICAL LIMITATIONS ON LOW NO  FIRING
                                    JL
     It has been demonstrated that large reductions in NO  emissions can be
                                                         jC
     attained by various types of combustion modifications; including staged
     combustion and burner redesign.  The existing NSPS has been attained on new

     units using overfire airports only and, under specific conditions which are
     not commercially acceptable, on older unmodified units.  Also, the limit has
     been attained on older units retrofitted with a low NOX burner.

     Although very low levels of NOX have not yet been demonstrated on operating
     steam generators, more radical combustion modifications than those already
     demonstrated do appear to have the potential to provide additional reductions.
     Certainly,  staged combustion, at burner stoichiometries well below 100%
     theoretical air, has that capability.  Second and third generation low NOX
     burners may also demonstrate such ability.

     However,  there are  other factors of major importance,  which strongly  affect
     boiler performance,  that can limit the applicability  of these  techniques.
     The  foremost among these are:

           -   tube wastage which  can affect unit  life and reliability
           -   increased  slagging  which can affect unit  availability
           -   burner stability can affect unit integrity

     Tube wastage and slagging have been two of  Poster V/heeler's greatest  concerns
     in designing steam generators  to meet  the NSPS.   When a boiler is operated in
     a manner which produces a reducing (oxygen  deficient) atmosphere along a water-
     wall,  and the  fuel and ash  properties  are  such as to  promote  slag formation,
      severe tube wastage can result.  An example of this is shown  in Figure 3.1.
     This is a cross-section of  a sidewall  tube  that had been subjected to a reducing
                                        3-1

-------
EXAMPLE OF FIRESIDE TUBE  WASTAGE
                                FIGURE 3-- 1
                  3-2

-------
atmosphere for approximately 30 months.   A high-sulfur (^3-0 percent),  high




iron (Fe203^20 percent) bituminous coal with a low reducing ash fluid tempera-




ture was used.





The unit involved was designed prior to the advent of the NSPS and had been




operating with 20-25 percent excess air at the burners.  Poor air distribution





on this unit result in side wall reducing atmosphere that is essentially




the same as that which occurs with substoichioiaetric burner operation, as with




overfire air ports.  Other pre-NSPS units firing similar coal do not have a




tube wastage problem; this was an isolated case.
The  sidewall reducing atmosphere has since been eliminated by redistributing




the  windbox air  flow and adding sidewall  slots to permit air entry  to the



furnace.  This has  significantly alleviated  the tube wastage problem thereby




confirming that  there is a  strong  link between this condition and oxygen




level  along the  wall.   It must also be noted that, although the  wastage



problem on this  unit has been solved,  this particular  fuel, which is a




troublesome one, has not yet been  used in an NSPS  steam generator with  over-



fire air ports.






The  reason for noting this  particular example is  to graphically  demonstrate




the  rapidity  with which tube wastage  can occur, when  the necessary  conditions




exist along  the  wall.   Foster Wheeler believes that this problem could  become




endemic if the NSPS NOX limit was  lowered sufficiently to require staged




 firing at burner stoichiometric levels below those now deemed acceptable.



 It must also  be  noted that it has  not yet been demonstrated that there  are



 no adverse  long-term effects with the methods used to attain the current






                                   3-3

-------
NSPo; either low-NOx burners  or  werfire airports.  The Environmental Protec-



tion  Agency also recognizes  this problem and is  sponsoring a  long-torm program



fco quiafcify the ef-fects of low NOX combustion techniques  on tube wastage anl



unit  operaMlity.  Poster ¥neeler, as  the first  boiler manufacturer to support



this  prograa, has been cooperating with EPA  for  over two  years in an active




wastage teat program.






Historically coal burners have beoa designed -;o  provide high-iitensity,



stable flames with turn down  ratios t; at least  ^0% •-•? rated  capacity.  Low



1OX burners, in contrast, utilize aerodynamics to control rnLxing rates



?>••»•!; laan fuel and combustion air.  Aa acceptable  low NO-^ burner must permit



the steam generator to be opera0^1 o/sr the  sante range of conditions as bhe



historical Mgh turbiilflace burners.  Flame stability and combustion efficiency



must be maintained over the same historical  turndown ratio.   Those low NOx




ooal burners which have been  successfully demonstrated on utility steam



generators have maintained these criteria while  producing N9X emissions 5^



below historical levels.






More advanced low NOX burners, which may yisld NOX emi.g«lo:is  significantly



lower than those already attained, have not  yet  been demonstrated on



utility staam generators.  The ability of more advanced low NOX designs



to maintain their low emission character with stable flaaes will have to



be shown over wide ranges of  throat velocity and fuel inputs.






Flame stability is critical to safe operation of the boiler.  There ie no



cost-benefit tradeoff which will permit degradation of this operating



parameter.
                                  3-U

-------
STEAM GENERATOR TEST DATA
Poster Wheeler has tested numerous pre-NSPS coal-fired steam generators  in
order to characterize the parameters which control the formation of NOx?
the effect of various combustion modifications has also been determined.
The primary parameters of interest are the following:

     1.  Unit Design
         (a)  Opposed-fired vs. single-wall fired
         (b)  Available cooling surface compared to heat input
              (Burner Zone Liberation Rate)

     2.  Fuel Qualities
         (a)  Heating value
         (b)  Nitrogen content
         (c)  Slagging properties
         (d)  Sulfur content

     3.  Operational Parameters
         (a)  Load
         (b)  Excess air
         (c)  Burner out  of service  operation (staged combustion)

In addition to  the  field  test  program Poster  V/heeler also began a  program to
develop a new coal  burner which would be  inherently  low in  NOX  production.
The resultant burner was  successfully demonstrated in Japan by  Poster Wheeler's
licensee, Ishikawajima-Harima  Heavy Industries Ltd.  (IKE),  on three older
utility boilers.  This  Dual Hegister Burner,  described earlier, has been
offered commercially since late  1976.  However, to date there are  no NSPS
units in operation  using this  burner although new units have been  sold  with
 this design.

-------
Consequently the data for the NSPS units presented here were obtained with



the  Intervene Burner and overfire air ports.  This combination has been



successful in permitting the current emission regulation of 0.7 lb N02/10^



Btu to be achieved with no apparent detrimental impacts to boiler ingetrity



or operation.
                                 k-2

-------
PBE-NSPS COAL-FIHED UNITS



Data from two pre-NSPS steam generators are presented, they are representa-



tive of the two utility boiler types designed "by Poster Wheeler:  single-



wall fired and opposed-fired.  The units chosen from the test data inventory



are typical of those sold just prior to the advent of the NSPS regulations.



As such they were designed with the high turbulence Intervane Burner and



have relatively high Burner Zone Liberation Rates to maximize efficiency.



NOX emissions are, therefore, high.






1+.1.1  Opposed-Fired Steam Generator;  Unit A




       Figure 1+.1 shows a side elevation view of the opposed-fired unit




       which was  tested for NOX emissions.  The unit utilizes  21+  Intervane



       Burners, 12 per firing wall in a 1+ wide x 3 high  arrangement,




       supplied by six Foster wheeler medium speed MB-22 pulverizers.  It




       is a natural circulation reheat type steam generator with  a capacity




       of 3,620,000 Ib. per hour  superheated steam at  21+85 psig and  1000F



       at the  outlet  and  3,206,500 Ib/hr reheated steam  at 570 psig  and



        1000F at  the outlet.






       Table I+-1  lists  the unit  design parameters and performance fuel.






       Emissions  tests  were  performed to characterize the  effect  on NOX



        production of:






               -  Unit  load



               -  Excess  air



               -  Staged combustion
                                   U-3

-------
          UNIT  A
FOSTER  W WHEELER
                                          EL. 222'.0"
         J_   SPRAr CONTROL JlfAOERS
                            FIGURE 4 - 1

-------
              TABLE U-1 .   UNIT A DESIGN DATA AND PERFORMANCE FUEL
Convection surface boiler
Walls in furnace
Radiant superheater
Convection superheater incl. ERA walls
Reheater
Economizer
Air heater primary
Air heater secondary
Total furnace volume
Total furnace surface
Firing equipment
Superheat control by
Performance based on fuel  specified below:
  Kind
  Grindability
  Size
  Max. moisture
Prox. Analysis Percent
  Moisture
  Volatile matter
  Fixed  carbon
  Ash
  Softg. temp,  of  ash
Ultimate Analysis
  Fuel
  Percent by
  Ash
  S
  H2
  C
  H20
  N2
   02
  Btu-lb as fired
  3,800 sq. ft.
 26,014* sq. ft.
 35,223 sq. ft.
 3U,1£5 sq. ft.
 98,135 sq. ft.
153,600 sq. ft.
 14l,200 sq. ft.
U85,800 sq. ft.
291,100 cu. ft.
 62,763 sq. ft.
Six MB 22 Pulverizers
Spray

Bituminous Coal
55
1-1/2"
8.5
38.0
U5.o
8.5
2000F

Bituminous Coal
Weight
8.5
3-7
U.7
66.6
8.5
 1.2
 6.8
 12,000
 *Surface moisture 5%

-------
Overfire air port operation (staged combustion) was simulated by




removing the top opposed burner rows from service.  Since it was




necessary to remove one-third of the mill capacity from operation




during the staged combustion tests all of these tests were per-




formed at 70% of Maximum Continuous Rating (NCR); other, higher




load normal firing, tests were performed with all burners in




service.






Figure U«2 is a composite plot of the measured data using a mapping




procedure which permits the parametric relationships between IvOx,




load, excess air and degree of staging to be immediately apparent.




Figure U-3 is a composite mapped plot of the measured carbon




monoxide (GO)  data.






Table 1+-2 is a listing of all relevant measured parameters, including




fuel ultimate analysis for each test.







Evaluation of the test data indicates that NOX emissions are sensi-




tive to the operating parameters being tested.  In order of importance:






(a)  Burner Excess Air (Degree of Staging);




     Utilizing overfire air ports, in this case by simulation, to




     reduce the burner air while maintaining unit excess air constant




     provides a significant reduction in NOX emissions.  At 75% MCR




     a NOX reduction of I|.0?6 was obtained by removing the top eight




     burners from service and opening the registers to the 37-5%




     position,  at 2C% excess air.   Burner stoichiometry was lowered
                           U-6

-------
_— C
                         TO   H




                       «EUFFEL a essen co
                                  20
                               NOX  COMPOSITE'- UNIT A



." '.

i- - '.'
i
;:


: ' - .

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r~ 	
•
.


: - .
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— 	 	
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: : • .; : - ' - .
: ::;- :. :: : : . ~ r
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	 , _. ._ — * -
8GL

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6 Q^
. X^ . - . - . .

, \*J O
1

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\

\
-
^p
-

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%PYr*PQQ AID
. I .
: "
/ MMBTU LB NO2 /
: ;_^v -. . ;-:' : : -! -•
— , — . - - - - ..._. i_ ._..., j .
:;.__.r;--, .: .-_:»:_ : 	 . :..;:.:.. j
. • -r 	 ! - - • ' '
t il~^-: :--; -' - . . _:.: i -r::L:p
.^-:^r, /.:u;-:_ :;;- . fj. \ ^
• - - -t -- • - ' : : • -; ~ ; 	 f
•- — f • - -- -• •- • - - 0 g - - •
_zr^:.i-^ : -.: f _ ^ :.r
— I 	 1.. .._. 	 L. . 	 _. . 	 l 	
- t - - •- --. { --- -. • - -- / / 	 ; •
/ /
M.O / / 10-^

:i'---f ": p^2 ' ": ^4
t • - ...


b (*)

r- • - 4 Vi/
: . : . • • I • :
• ' 	 i — .,__,.... : . . . . . ;
3O
0.5- —0.5-
*
• ^r
: ; : ; \ l \
	
• ----- ----- -- l-
0 50 75 100


; . --.
i . ...
MMBTU
- 1 • ... .


... _. .. .;. .
: . : :- -

:: ' -;': ' :
(7\ o

—01
^-~- r . .: ..^_v.
j 70 --H
^
•e<^ : :-:- 	 	 	
. 	 > v ._._... . . . — -_-


V. . ^^v -
U0!4
: ..:.;:. \ _ ;.
\
\
;N03
— : 	 : 	 : 	 : 	 . 	 . 	 :
>


0 50


FIGURE 4-2
IT -		i_

-------
    -
CO  COMPOSITE: UNITA
_.::.": ; :": . . :~: ; :
CO,
!:':":•"..: : '. '.

;.:...: . :
i : ;..' :... ; . .;..;. ; : .:-.:..": ;
:•::._• : :.
- .:.-.-• . . . . - _:: ir
— 	 - - - -___ --
.
.
— ..... ... — ...
-
. . ...... 	
4 (•}..
(. .. ; ~. .;; :-:- ; "© 3 - ..... ,_
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^ "^
[___ 	 	 g QT 	 	 	 	 	 — 	 : 	 •

....
...'.-....
- . - -
•. - . ........
i
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6
: ®_^-© 2 :
7 vi/ ft)


.-. -;-•.--:.:-.- : :: •- : ::~-; -
\ 	 . .... , . ,
:': -. :

40 30 20 10 0

% EXCESS AIR

; .
..
PPM


_ : : .

.:-; r:: -.

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1*>0
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-


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-100


:




en
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i n
- IU
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-: :-_..:-.-- L - ; --.L -' .: :-
: r ~ --- - " r;_.--rr:_- . : .— ^:. : .; -- :
	 • 	 — 	 -._- -.- 	 	
_-_____-_.:_ i .:: — ^'^LI,
"1*iO
	 • «**

4©

®3 ;
1©

..... . .
8© 100 -]

	 	 	 	 	 i ......

.;• • .: ..:_;.
— • 	 	 . 	 ....

:
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.:.-.:. :....:_•-:-;:..•. : .


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50 75 100

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L_ r . ; :: - - .
	 . .....
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<^»4
v: -_•:::- ©
: r r 3 


-------
                         TABLE U-2.   UNIT A TEST DATA
TEST NO.

Steam .  .  M Ib/hr
Pressure superheater outlet .  .  psi
Temperature steam superheater outlet
Pressure Boiler Drum .  .  psi
Reheat steam .  . M Ib/hr
Temperature steam entering reheater
Temperature steam leaving reheater .
Pressure steam entering reheater . .
Pressure steam leaving reheater . .
                               II
                         III
                 IV
             . F
             psi
           psi
Temp. feed, entering unit . . F
Temp, feed leaving econ. . . F
Temp, air entering unit avg. pri & sec . F
Temp, air leaving air heater avg. pri & sec I
Temp, gas leaving furnace (HVT)  . . F
Temp, gas leaving boiler . . F
Temp, gas leaving economizer . . F
Temp, gas leaving air heater . . F
Ditto corrected for leakage avg. pri & sec F
Excess air leaving  .  . %
Wet gas entering air  heater  .  . M Ib/hr
Wet gas leaving air heater .  . M Ib/hr
Air entering air heater . . M  Ib/hr
Air leaving air heater .  . M Ib/hr
        3333
        2380
         992
        2500
        3010
         637
         973
         555
         52U
                        U76
                        636
                        151+
                        1+75
                       1960
                       N.A.
                        738
                       N.A,
                        292
                         20
                       1*231*
                       N.A.
                       N.A.
                       3905
2550
2397
1001
251+7
2300
619
990
l+l+o
MO
1+57
607
166
1+92
1860
N.A.
695
N.A.
236
19-5
3291+
N.A.
N.A.
3031+
2600
2275
980
21+88
2350
603
955
l+l+o
Uio
U61
6117
167
US 8
1860
N.A.
698
N.A.
286
20.5
31+51
N.A.
N.A.
3175
2550
2300
985
2U50
2300
550
980
i+l+o
U1C
U63
629
166
U92
1825
N.A.
717
N.A.
291
32.0
3652
N.A.
N.A.
3377
 Pressure  in  furnace
in. H20
         N.A.
13.5
12.0
11+.1+
Air &  gas  loss  total  .  .  in.
Pressure loss Drum  to Sho Hdr .  .
Fuel burned  .  . M Ib/hr
Liberation,  total vol Etu/hr  x cu
Furn.  cooling  factor  net  Btu/hr  x
Heat Losses
   Dry gas .  .  %
   Hydrogen  and moisture  in fuel ,
   Moisture  in  air  .  .  %
   Unburned  combustible . . %
   Radiation .  .  %
   Unaccounted for  .  .  %
Total  losses .  .  %
Efficiency .  .  %
          psi

          ft.
          sq.
ft.
N.A.
120
365
11+, 915
69,155
3.921
1+.398
.091+
.221
.190
.50
9-321+
90.676
N.A.
150
287
11J3U
51+, 1+02
3.1+03
U.20U
.083
.155
.250
.50
8.595
9LU05
N.A.
213
303
11 ,803
51+, 726
3.539
1+.301+
.086
.um
.25
.50
9.093
90.907
N.A.
150
299
11,71+i
51+, 1+36
3.959
1+.502
.097
.1+03
.25
.50
9.711
90.289
                                        U-9

-------
                          TABLE  U-2.  UNIT A TEST DATA
TEST NO.

Steam . .  M Ib/hr
Pressure superheater outlet .  .  psi
Temperature steam superheater outlet
Pressure Boiler Drum .  .  psi
Reheat steam .  . M Ib/hr
Temperature steam entering reheater
Temperature steam leaving reheater .
Pressure steam entering reheater . .
Pressure steam leaving reheater
                                       F
                                    . psi
                                    psi
                                               2500
                                               2370
                                                995
                                               2522
N.A.
 979
         VI

         2600
         2406
          990
2350
N.A.
 965
VII

 2543
 2370
  998
 2522
 2290
 N.A.
 1000
 UOO
 MO
VIII

 3327
 2398
  993
 2507
 2940
 N.A.
  991
  549
  517
Temp,  feed entering unit  .  . F
Temp,  feed leaving econ.  .  . F
Temp,  air entering unit ave. pri. & sec. F
Temp,  air leaving air heater ave. pri. & sec.F
Temp,  gas leaving furnace . . F
Temp,  gas leaving boiler  .  . F
Temp,  gas leaving economizer
Temp,  gas leaving air heater
Ditto  corrected for leakave ave. pri. & sec.F
U55
615
166
U78
N.A.
N.A.
692
N.A.
277
U59
622
157
U59
N.A.
N.A.
698
N.A.
270
157
622
160
US6
N.A.
N.A.
713
N.A.
287
klS
650
1 1*7
U96
N.A.
N.A.
7U5
N.A.
292
Excess air leaving . . %
Vet gas entering air heater . . M Ib/hr
Wet gas leaving air heater . . M Ib/hr
Air entering air heater . . M Ib/hr
Air leaving air heater . . M Ib/hr
20.5
3383
N.A.
N.A.
3115
30.0
3U76
N.A.
N.A.
3210
31.
3618
N.A.
N.A.
3356
35.
U8U3
N.A.
N.A.
U505
 Pressure  in  furnace
                        in.  H20
12.2
         15.3
          N.A.
Air & gas loss total . . in. H20
Pressure loss Drum to Sho Hdr . . psi
Fuel burned . . M Ib/hr
Liberation total vol. Btu/hr x cu ft.
Furn. cooling factor net Btu/hr x sq. ft.
Heat Losses
   Dry gas . .  %
   Hydrogen and moisture in fuel . . %
   Moisture in . . %
   Unburned combustible .  .  %
   Radiation .  . %
   Unaccounted for . . %
Total losses .  . %
Efficiency . .  %
N.A.
152
30U
11,529
53,U70
3.531
U.520
.086
.258
.260
.500
9.155
N.A.
104
300
11,880
55,102
3.958
U.313
.095
.258
.25
.500
9. 374
N.A.
152
290
11,816
54,805
3.861+
4.223
.09k
.155
.250
.500
9.086
N.A.
109
379
14,865
68,997
4.644
4.623
. .112
.230
.190
.500
10.299
                                             90.81*5   90.626   90.91U   89.701

-------
                                         TABLE l*-2.  UNIT A TEST DATA
 TEST NO.

 Prox. Analysis (%)

    Moisture
    Volatile Matter
    Fixed Carbon
    Ash

 Ult.  Analysis  (%} By Weight

    Ash
    S
    H2
    C
    H20
    N2
    02
    Btu/lb (as fired)

Wet Flue Gas Analysis By Volume

   % C02
   % H20
   % S02

Gas Emission Data
   NOX fppm)
   N02 (lb/10b
   S02 (ppm)
   CO (ppm)
Btu)
 Aah Fusion Temp.°F (Red./Oxid.)

   Initial Deform.
   Soft.  Temp.  Sph.
   Soft.  Temp.  Hem.
   Fluid  Temp.
7.10
36.56
1*6.66
9.68
9.68
2.59
1*.52
65.56
7.10
1.1*2
9-13
11,879
13.91*2
8.701
.207
797
1.096
2209
115
7.88
35.99
1*6.80
9.33
9.33
2.86
U.28
65.1*2
7.88
1.26
8.97
11,878
11*. 101
8.591
.231
668
0.912
2503
14*
N.A. 1900/2310
N.A. 1930/2380
N.A. 1960/21*20
N.A. 2000/2500
9.37
36.11
1*5.70
8.82
8.82
2.75
3.99
65.27
9.37
1.35
8.1*5
11,31*7
11*. 103
8.1*69
.221*
390
0.550
255U
128
N.A.
N.A.
N.A.
N.A.
10.1*0
35.19
1*6.68
7.73
7.73
2.31*
1*.12
61*. 20
10.1*0
1.30
9.91
11,1*11*
12.903
8.308
.177
1*65
0.705
2360
133
1 920/2360
1 960/21*60
2000/2500
2250/2530
9.61
31*. 62
14*. 13
11.61*
11.61*
3.06
1*.07
62.70
9.61
1.22
7.70
11,030
13.891
8.760
.255
5U5
0.771*
2505
38
N.A,
N.A.
N.A.
N.A.
7.38
31*. 79
1*6.57
11.29
11.29
2.96
i*.26
65.21
7.38
1.30
7.60
n,5l*o
13.927
8.1*26
.237
559
0.851*
2338
1>8
N.A.
N.A.
N.A.
N.A.
7.88
35.99
1*6.80
9.33
9.33
2.86
i*.28
65.1*2
7.88
1.26
8.97
11,878
12.921
8.032
.212
632
0.91*1*
221*2
UO
1900/2310
1 930/2380
1960/21*20
2000/2500
6.90
36.95
1*5.14*
10.72
10.72
3.18
1*.58
61*. 09
6.90
1.31
9.22
11,1*18
12.355
8.105
.230
728
1.153
1908
100
N,A.
N.A.
N.A.
N.A.

-------
                 from 120%  bo approximately 9$%.  The reduction rate varies




                 from unit to unit depending on unit and burner design as




                 well as coal characteristics.






            (b)  Unit Excess Air;




                 Total excess air has a moderate affect on NOX emissions under




                 normal firing, all burners in service, operation.  However, with




                 staged firing the sensitivity of NOX emissions to excess air is




                 increased significantly.  This sensitivity is not due entirely




                 to excess air.  Under the conditions of these tests the burners




                 were operating at maximum design heat liberation only during the




                 staging tests; during all other tests they were well below




                 maximum.  This is demonstrated by the following tables
   Load



3333 KLb/hr



2550 Mlb/hr



2550 Mlb/hr
Burners in Service




        2k




        2k



        16
NOY Change with Xs Air



   ~3      6
                                 Burner Liberation



                                          6
 3«33 x 10~  lb/10  Btu/%Xg Air   181  x 10  Btu/hr



 ii.167x10~3 lb/106 Btu/%Xs Air   11+2  x 106 Btu/hr



13.33 x 10~3 lb/106 Btu/%Xs Air   213  x 106 Btu/hr
Maximum Design Burner Liberation:  22^ x 10^ Btu/hr






                 The maximum sensitivity of NOx emissions to excess air,  on this




                 unit, occurs at maximum burner liberation.  Since the unit is




                 designed for operation at 18% excess air, and the burner is




                 optimized for that level, increases in excess air at maximum




                 liberation will cause a. significant increase in turbulence.




                 This is due mainly to the burner throat velocity increasing




                 beyond its optimum design value.
                                       U-12

-------
(c)   Unit Load;



     NOX is generally expected to decrease with unit load,  as is  the



     case here.   The reduction is due to decreasing the Burner Zone



     Liberation Bate as well as to reduced burner turbulence.  The



     reduced turbulence decreases the formation rate of fuel NOX



     while decreasing the lower furnace heat input reduces the




     formation of thermal NOX.






(d)  Unit Operability;



     As  shown in Table U-2 there is no detrimental effect on combus'iim




     efficiency due to staging.  At 759^ load there is an increase



     in  CO as idle registers are opened.  The full load CO level



     of  about 100 ppm is high  for a unit  of this type which  should




     emit  levels well below 50 ppm; the reduction in CO as the top




     burners are idled may indicate that  one or more of those



     registers  was maladjusted.






 (e)  Furnace Conditions;



     When utilizing staged  combustion a primary consideration is,



      as discussed  earlier,  the effect on  slag formation of reducing



      atmospheres in the  lower furnace. Consequently,  during all



      tests furnace and flame  conditions were  closely observed.   The



      following observations were made during the test  sequence:






      (l)  Full Load Tests (all burners in service):  Furnace condi-



           tions very good;  bright and clear.   Superheater clean with



           a slight accumulation of dry ash on the leading edge.




           Furnace walls good with dry ash on front wall and light




           sponge ash on middle section of rear wall.




                           U-13

-------
(2)  75% NCR (all burners in service, 20% Xs Air):   Spongy




     ash on front leading edges of finishing superheater;  dry




     ash on walls. Fires bright and stable;  eyebrows on some




     burners .
(3)  75% MCR (all burners in service; 32# Xs Air):   All upper




     furnace walls clean; 2" ash on leading edges of pendant




     superheater.  Burner basket rear wall is clean; ^" wet




     sponge ash on front wall;  sidewalls £" c*ry ^°  ve^ sponge.
(k)  75% MCR (top burners out of service and registers closed;



     20% Xg Air):  (Burner Stoichiometrff approximately 110%)




     Upper furnace walls clean;  2" ash on finishing superheater.




     Burner basket front wall clean, £" wet sponge ash on side




     and rear walls.   Hopper clean.






(5)  75% MCR (top burners out of service and registers 2596 open;




     20% Xg Air):  (Burner stoichiometry approximately 100%)




     Slag conditions  are the same as previous test but eyebrows




     on top row of burners are running.






(6)  73% MCR (top burners out and registers 37.5% open; 20%




     Xg Air):  (Burner stoichioaetry approximately 90-95%)




     Furnace walls have accumulation of dry ash;  2"-3" of




     sponge ash on leading edges of superheater tubes.  Heavy




     eyebrows on many active burners; rear burners eyebrows




     more plastic than front but not running.  Flames carrying




     high into furnace and superheater.

-------
(?)  75% MCR (top burners out and registers 00% open;  20%




     Xg Air):   (Burner stoichiometry approximately 80-8E9o)




     Loss of flame definition, fires filling flame basket and




     carrying very high into pendant section.  Upper furnace and




     pendant conditions the same as previous test.  Plastic slag




     in mid-furnace, 1-^" on burner walls and 1" on side walls.




     Burner zone front and side wall 1" wet sponge ash; rear




     wall 1^" plastic slag.  Eyebrows on top burner row running




     excessively.  Large slag logs on both right sidewall hopper




     slopes.






All of these tests were of short duration, yet it is clear  that




furnace  and flame conditions would prohibit  substoichiometric




burner operation of this unit, with  this fuel.  Similar




results  have been obtained on other  tests performed by Foster




Wheeler  on  other pre-NSPS steam generators.






It should be noted  that  these  staged combustion tests  were  all




performed at 75$ of unit maximum continuous  rated load.  Although




those  short tests with non-substoichiometric staged combustion




(that  is with  burner  stoichiometry greater than 100%  but less




than total  unit air)   were acceptable,  it  is unclear  whether




these  conditions could be  maintained continuously.  Certainly a




unit of this design and Burner Zone Liberation Rate would be




unable to operate at  full load under staged combustion conditions.
                      U-15

-------
U.1.2  Front-Vail Fired Steam Generator;   Unit B




       Figure l±'k shows the side elevation view of the single-wall fired




       unit.  It contains 16 Intervene Burners, in a k x U matrix, on the




       front wall supplied by four Poster Wheeler MB-22 pulverizers.   It




       is a natural circulation reheat type steam generator with a capacity




       of 2,320,000 Ib. per hour superheated steam at 262$ psig and 1005°F




       at the outlet and 2,030,000 Ib. per hour reheated steam at 560 psig and




       1005°F at the outlet.






       Table U-3 lists the unit design parameters and performance fuel.






       This unit was tested in the same manner as Unit A:   overfire air was




       simulated by removing the top row  of burners from service and opening




       their registers.  NOX emissions as functions of load and excess air




       were also investigated.






       Figure U.5 is the composite, mapped data showing the parametric re-




       lationships between NOX, load, excess air and degree of staging.




       Table k-k is a listing of all relevant measured parameters.






       Evaluation of the test data for this front-wall fired unit indicates




       that NOX emissions are sensitive to the same operating parameters




       as the opposed-fired unit discussed previously.  All trends are




       similar, although levels and rates of change are different.  The




       following is a discussion of the individual parameter effects in the




       same order as previously:

-------
                     UNIT  B
              FOSTER  W WHEELER
F

              1"   '
 I 	  	
                         U-17
FIGURE 4-4

-------
                TABLE U-3.  UNIT B DESIGN .DATA AMD PERFORMANCE DATA
Walls in furnace
Radiant superheater
Convection superheater (A)
Convection enclosure
Reheater
Economizer
Air heater
Total furnace volume
Firing equipment
                               17,982  sq.  ft.
                               25,380  sq.  ft.
                               34,610  sq.  ft.
                               2,8U3  sq.  ft.
                               73,961  sq.  ft.
                               99,000  sq.  ft.
                             kShikQO  sq.  ft.
                             160,000  cu.  ft.
                              Pour MB22 Mills
Performance based on fuel specified "below:
   Kind
   Grindability
   Size
   Max. moisture
Prox. analysis percent
   Moisture
   Volatile matter
   Fixed carbon
   Ash
   Soft temp, of ash
Ultimate Analysis
   Fuel
   Percent by
   Asli
   S
   H2
   C
 Bituminus Coal
 Weight
 7.7
 1.2
 k.l
59.6
                              Bituminum Coal
                              50* Hardgrove
                              1-1 A»
                              13.1
                              13.1
                              35.6
                              U3.6
                               7.7
                              2100 min.
H20       13.1
R2         1 .2
02        12.5
Btu/lb
as fired  10.662

-------
 'IO-   NCH
X IO INCHES

 KEUFFEL « EJSCR CO.
   - I32_
   • ADI IN U t.A.
NOV  COMPOSITE: UNIT B
  ^Ar

-------
                                              TAPLE k-k*  UNIT E TEST DATA
IV)
o
TEST NO.

% MCR

% Excess Air

Steam (MLB/HR)

Fuel Burned (MLB/HR)

Air Leaving AH (MLB/HR)

Wet Gas Entering AH (MLB/HR)

Ultimate Analysis (96) By Weight

   Ash
   S
   H2
   C
   H20
   N2
   02
   Btu/Lb (as received)

Wet Flue Gas Analysis (%) By Volume

   C02
   HpO
   S02

Gas Emission Data

   NOX (ppm)
   N02 (lb/MM Btu)
   S02 (ppm)
   S02 (lb/MM Btu)
   CO (ppm;
1
75
24.5
1800
234
2412
2620
2
75
28.2
1800
238
2526
2737
3
75
56.7
1800
240
3046
3259
4-
75
53-3
1800
251
3186
3408
5
75
26.8
1800
256
2585
2816
6.
93
26.8
2150
299
3020
3289
7
75
53.7
1745
274
3047
3282
8
75
27.5
1800
236
2491
2700
11.38
0.66
5.17
59.90
9.60
1.22
12.07
10169
11.38
0.66
5.17
59.90
9.60
1.22
12.07
10169
11.38
0.66
5.17
59.90
9.60
1.22
12.07
10169
11.38
0.66
5.17
59.90
9.60
1.22
12.07
10169
10.06
0.66
4.29
60.54
9.25
1.20
14.00
10377
10.06
0.66
U.29
60.514
9.25
1.20
1U.OO
10377
13.86
0.55
3-77
56.60
8.18
1.09
15.95
9534
11.38
0.66
5.'7
59.90
9.60
1.22
12.07
10169
13.086
10.053
.054
12.730
9.836
.053
10.524
8.486
.043
10.746
8.622
.044
13.549
9.033
.055
13.549
9.033
.055
11.601
7.670
.042
12.796
9.876
.053
346
0.53
529
1.10
N.A.
563
0.90
511
1.09
N.A.
543
1.06
439
1.15
N.A.
651
1.24
458
1.17
N.A.
863
1.29
510
1.06
N.A.
960
1.44
567
1.18
N.A.
815
1.47
475
1.19
N.A.
634
1.00
541
1.15
N.A.

-------
(a)  Burner Excess Air (degree of staging)

     Removing the top row of burners from service and using them as

     overfire air ports permits very significant NO  reductions  to be obtained

     on this unit.  At 75$ MCR NOX was reduced 5996 (from the all

     burners in service case) by opening the idle burner registers

     50?6; a reduction of U7% was obtained from the case with the

     top burners out of service and registers closed.  However,  there

     was running slag formation during the performance of the lowest

     NOX test (No. 1).  These tests were performed with unit excess

     air held approximately constant at 25%.  Burner stoichiometry

     was about 90% for the minimum NOX test condition.


(b)  Unit Excess Air

     The effect of unit total excess air shows  the same trends as

     before:  a moderate increase of NOx with excess air during

     normal  firing with all burners in service;  a much greater

     sensitivity is exhibited during staged firing.  As with the

     tests performed  on the opposed-fired unit  the burners were

     operating near their maximum design liberation  in the region

     of maximum NOX sensitivity  to  excess air.   This is demonstrated

     by  the  following table:
Burners in
  Service
 Load     	

79% MCR       16

    MCR       12

1% MCR       12
NOY Change with Xg Air
Idle Reg.
 % Open
              6.67 x 10 3 lb/106 Btu/tf Xs Air      —

             13.6  x 10~3 lb/106 Btu/ft XS Air

             1U.3  x 10~3 lb/106 Btu/% Xs Air      50%
                                                                Burner
                                                              Liberation

                                                           166 x 106 Btu/lb

                                                           200 x 106 Btu/lb

                                                           200 x 106 Btu/lb
                           U-21

-------
     Thus, the sensitivity of NOX emission to the combined effects




     of burner turbulence and increased oxygen availability is again




     demonstrated for the high turbulence Intervane Burner used on




     this unit.






(c)  Unit Load




     The variation of KOX with load is similar to that of the opposed




     fired unit in that the emission decreases as load is reduced.




     Unit B demonstrates a slightly greater slope (change in NOx/




     change in load) than does Unit A which may be due to the higher




     full load NOX level of single-wall fired units.






(d)  Unit Operability




     There were no apparent detrimental effects,  apart from slagging,




     to unit performance during the staged firing tests,  as indicated




     by a comparison of unit input  to output during normal  and staged




     combustion.   CO was monitored  during the tests as were combus-




     tibles,  which were checked on  the station combustibles meter.




     There was no significant increase in CO or combustibles during




     any of the low NOX tests.






(e)  Furnace Conditions




     Furnace conditions were observed, during the testing of this




     unit, in the same manner as during the test of Unit A.  It was




     found that "there were conditions of excess air and staging




     which would promote the formation of running slag.  The following




     observations were made:
                          U-22

-------
(1)  All Burners in Service,  Normal Firing Tests;   Daring all




     of these tests, at 75% MCR or greater, furnace conditions




     were generally good with bright stable flames.  Furnace




     side and rear walls had a covering dry ash which is con-




     sidered normal for this unit.






(2)  75% MCR, Top Burners Out of Service;  During these staged




     firing tests excess air was varied from 60% to 25% and




     idle burner registers were opened from 0% to 50%.  When




     the idle registers were set at 50% open and the unit excess




     air was about 60% (test 3» Figure U.5) furnace conditions




     were about the same as during normal  firing; however, active




     burner stoichiometry was approximately 120%.  As excess air




     was gradually lowered, increased slag formation in  the lower




     furnace was noticed.  At 25% excess air (test  1, Figure U.6)




     slag was running rapidly on the rear  wall.  Although data




     was recorded and showed a NOX emission of only 0.53 lb/10




     BtU| furnace conditions were totally unacceptable  for continuous




     operation.  Burner  stoichiometry was  approximately  90-95%«






     A similar  test sequence was performed with excess air




     constant at about  27%.  With  idle registers closed  furnace




     conditions were  similar to those during normal firing.   As




     idle registers were open toward 50% slag began to run  on




     the rear wall;  again when burner stoichiometry was  reduced




     below  95%. The  fires were stable but the  furnace was  very




     hazy.
                      U-23

-------
1.3  Summary of Pre-NSPS Unit Data




     The two pre-NSPS steam generators reported here are typical of the




     designs used "by Foster Wheeler just prior to the advent of emission




     regulations.  They therefore have high turbulence burners  and high




     burner zone heat release rates.   Figure l±.6 shows some of  the normal




     firing and staged firing data for each unit as NOX vs. Burner Zone




     Liberation Rate.  Table k-B contains a listing of the coal  ash




     characteristics.






     Unit B, which is front-wall fired, has a clearly higher NOX emission




     than does Unit A, which is opposed-fired.   This is a typical result:




     opposed-firing generates less NOX than single wall firing,  all other




     factors being the same.  Since the burners are basically the same  and




     the fuels are similar it would seem unlikely that the difference in




     emissions is due to a higher rate of NOX formation at the  burners




     of the single-wall fired unit.  Rather, the major differences in




     boiler-geometry, bulk gas mixing, combustion gas stratification and




     cooling rates more likely affect the reverse reaction  (NO reducing




     to N2 in the burner zone)   ani char burnout rates.






     Significant NOX reductions were  obtained under reduced load conditions,




     but in both cases a slag threshold was reached, below 95>%  burner




     stoichiometry, which would have  prevented continuous operation.




     Although the flame and slag conditions were different in each unit




     the result was the same:  unit availability would have been seriously




     affected if long term operation had been attempted.

-------
„.....„! .._U__.___'PRE_
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H '/I ' WALL BOILERS; MIGHT"
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REGISTERS % OPEN

HE TOP BURNER
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| i FIGURE 4-6
' .: T ; ' i ' : •• • • ; i ; ! ' !
U-25

-------
                          TABLE U-5.  ASH CONSTITUENTS
303




MgO



Na20




Si02



A1703
CaO



K20



Ti02



P2o5
Cr203
NiO




01
Initial Deform.




Soft. Sph.




Soft. Hem.




Fluid
Unit A
6.6
1.1
O.U
18.0
18. U
5.6
2.1
0.8
nil
-
-
-
-
-
-
98.6
Red Oxid
2000 2220
2070 2300
21 30 2350
2180 21410
Unit B
11.0
2.5
0.1
1U.7
8.2
18.6
1.7
O.U
2.1
0.1
0.1
0.1
0.1
0.1
0.1
103.7
Red Oxid
2100 2200
21 80 22UO
221 0 2300
22^0 2550
                                       k-26

-------
However, it must be noted that these tests were performed with the



intent of obtaining information which would be applicable t~> new



units designed to meet the NSPS; not as a means of developing NOX



controls for these pre-NSPS units.  Foster Wheeler does not consider



reduced load operation (derating) to be a viable means of controlling



HQ,r emissions.
  Jt




The results of these tests, and of similar tests performed on other



units, have been Foster Wheeler's recognition that, in general, there



is a limit to the  degree of staged combustion which is practically



achievable on   utility steam generators.  There can, however, be



some specific exceptions where a low sulfur, low slagging potential



coal is available.





NOX emissions are  sensitive to load,  total excess  air and  degree  of



staging (burner  excess air).  The effect  of excess air  seems  to vary



with relative burner loading; that  is,  whether or  not -the  burner  is



operating at maximum design liberation during staged  combustion.



Note that the maximum design  liberation itself (burner  size)  does



not  affect the  NOX emission:  a 100 MM Btu/hr burner  can have the



 same NOX  emission as a  200 MM Btu/hr  burner if they are of the same



 design, firing the same  fuel, within  furnaces of the same Burner Zone



Liberation Rate.  Burner  design,  not  liberation, controls  NO   formation.
                                                            X




 The  results of  Foster Wheeler's extensive field test  program on



 pre-NSPS  steam  generators, of which the information  provided here



 is only a part, have confirmed that staged combustion is a viable



 means of reducing NOX emissions.  However, in order for this




                            U-27

-------
technique to be acceptable certain precautions must be taken to




prevent slag formation or tube wastage.  Foster Wheeler uses the




following design and operating criteria to control these potential




problems:






(1)  Larger more conservative furnace designs to provide lower




     Burner Zone Liberation Rates (cooler furnace), which usually




     results from a wide variation in performance coal quality.






(2)  The staged firing system is generally limited to burner




     stoichiometries greater than 36% of the theoretical air




     requirement.






(3)  Boundary Air is provided to insure that an oxidizing atmosphere




     will be maintained along the walls of the burner basket.






(U)  A reduced turbulence Intervane Burner permits NOX levels,




     with unit design excess air at the burners, to be sufficiently




     low as to allow the NSPS limit to be attained with burner




     stoichiometries no less than 96%.






The validity of this design approach has been demonstrated on NSPS




units which are currently in operation.  A dual register low NOX




burner has also been developed to provide greater flexibility of




both design and operation.  In most cases with the use of the dual




register low NOX burner the NSPS NOX regulation should be attainable




without also using staged combustion.
                            U-28

-------
U-2  NSP3 COAL-FIRSD UNITS



     The coal-fired steam generators which Foster Wheeler has recently started-




     up utilize overfire air ports (staged combustion) as the primary means of




     N0;c reduction:  lower Burner Zone Liberation Rates are inherent in the




     designs.  Data are presented from one unit designed to meet the NSPS with




     the Intervane Burner.






     it.2.1  TJnit _C;  Front-Wai 1 Fire d




            This is a natural circulation reheat type steam generator with a




            capacity of 929,1;00 Ib. per hour superheated steam at 1975 psig and




            100$F  at the outlet and 7^0,200 Ib. per hour reheated steam at




            1+69 psig and 1005F at the outlet.  It utilizes eight Foster Wheeler




            Intervane Burners, in a two (wide) by four  (high) matrix, supplied




            by two Foster Wheeler Ball Mill Pulverizers.






            The unit has a low Burner Zone Liberation Rate (215,000 Btu/hr/ft2)




            and  a  good  quality coal with  a relatively low  fuel  nitrogen  content




             (<  2.8 Ib  N02/10° Btu).  A standard  Intervane Burner is  used since




             this unit  is  similar  to other Foster  Wheeler units  on  this  station;




            use  of the  same  burner  significantly  simplifies  the maintenance




             requirements  of  the station.  The  boiler design,  fuel quality and




             use  of overfire  airports  permit  the NSPS to be attained without




             modifying the burner.






             Figure U.7 is a  side  elevation view of the unit;  Table  U-6 contains



             unit design and  performance  fuel information.
                                       U-29

-------
          UNIT   C.
FOSTER  ©WHEELER
             :±==3K5SSs£±i J SUPt'iHEATER OUTLET
               DIVISION WALL
               SUPERHEATER 11-
                                           FIGURE 4-7
                          U-30

-------
               TABLE U-6.  UNIT C DESIGN DATA AND PERFORMANCE FUEL
Each Unit Will Include the Following:
Convection surface toiler
Walls in furnace
Radiant superheater
Convection superheater
Reheater I
Reheater II
Economizer (Bars Tube)
Air heater
Total furnace volume
Total furnace surface
Firing equipment
       3,1+92  Sq.  ft.
      11,070  sq.  ft.
       8,525  sq.  ft.
      19,738  sq.  ft.
      21,626  sq.  ft.

      22,U20  sq.  ft.
      97,600  sq.  ft.
      69,U95  cu.  ft.
      20,295  sq.  ft.
      Two FW  D-8-C Pulverizers
Performance based on fuel specified below:

   G-rindability
   Size
   Max. moisture

Prox. Analysis Percent
   Moisture
   Volatile matter
   Fixed  carbon
   Ash
   Softg.  temp, of  ash

Ultimate  Analysis

   Percent by                Weight
   Ash                        7.20
   S                         0.52
   H2                        5.08
   c                        67.50

   * Surface  Moisture % J+.2
       U8 (Hardgrove)
       1-1A
       7.2*
       R/0 2280/2390
H20
N2
02
Btu/lb
  as fired
 7.20
 1.10
11.UO

12.UOO
                                        U-31

-------
This iroit was characterized with respect to overfire airport operation,




excess air and load.  Since the unit contains overfire air ports,




staged combustion can be attained at full load with all burners in




service at maximum design liberation rate.






Figures U.8 and k-3  are the composite NOX and GO plots, respectively,




showing the parametric relationships between load, excess air and




staging.  The relationships are quite similar to those obtained on




the pre-NSPS units.  The sensitivity to excess air at maximum burner




liberation rate is about 1U.6 x 10~3 lb/10^ Btu/% Xg Air which is




comparable to that of the older units.






Table U-7 is a listing of measured test data and applicable fuel




analyses.






Furnace conditions vera observed during all tests to determine if




staged combustion caused any adverse effects on the unit.  During




all operating conditions flames were stable and there was no change




in furnace cleanliness with overfire air ports open or closed.




Slag was minimal and considered normal for a boiler of this Burner




Zone Liberation Rate firing this particular fuel.






Tube wastage is not considered to be a potential problem.  The low




sulfur content of the coal and the ash properties provide added




confidence for this expectation.  However,  even if a high sulfur




slagging coal had been used,  good furnace sidewall conditions would




be maintained by proper adjustments to unit and Boundary Air design.
                           U-32

-------
               > x id   , INC   9 13_.
              7 X IO INCHtS    nut I* u. >. >.
                KEUFFEL ft rasCR CO.
                        NOX COMPOSITE'- UNIT C
                                                      l :
                                             LB NO2 / MMBTU r
11 1 :..-Lll J i il 1.1
% EXCESS AIR

-------
Hi X 10 TO '.• INCH
KtiJl-TEL a tSSIR CO
46 1320
       CO  COMPOSITE: UNIT C
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-------
                         TABLB U-7.   UNIT  C  TEST DATA
TEST NO.

Steam .  .  .  M Ib hr
Pressure superheater outlet .  .  psi
Temperature steam superheater outlet
Pressure Boiler Drum .  .  psi
Reheat steam . . .  M Ib/hr
Temperature steam entering reheater
Temperature steam leaving reheater
Pressure steam entering reheater .
Pressure steam leaving reheater .  .
                                                        II
                 III
IV


F


. F
. F
psi
psi
935
1890
993
21 OU
7U6
675
995
518
500
930
1890
1000
2102
7U2
677
1000
510
U95
637
1880
980
2003
N.A.
N.A.
980
N.A.
363
855
1890
1003
21 U2
N.A.
N.A.
990
N.A.
500
Temp, feed entering unit .  .
Temp, feed leaving econ. .  .
Temp, air entering unit . . .
Temp, air leaving air heater
Temp, gas leaving furnace . ,
Temp, gas leaving boiler .  .
Temp, gas leaving economizer
Temp, gas leaving air heater
Ditto corrected for leakage
U65
$ko
140
5U7
N,A.
N.A.

697
298
i|63
5^7
51
565
N.A.
N.A.

706
311
N.A.
523
119
566
N.A.
N.A.
673
N.A.
338
N.A.
569
100
582
N.A.
N.A.
713
N.A.
351
Excess air leaving  .  . %
Wet  gas entering air  heater  .  . M Ib/hr
Wet  gas leaving air heater .  . M Ib/hr
Air  entering air heater . . M  Ib/hr
Air  leaving air heater  .  . M Ib/hr
25.1
1276
N.A.
N.A.
1183
21.6
1236
N.A.
N.A.
11U3
20
81U
N.A.
N.A.
751
32.3
1231
N.A.
N.A.
1114^
 Draft  in  furnace
                     in.  H20
-0.75    -0.60    -0.70
 -1.0
Air & gas loss total .  .  in.  H20
Pressure loss Drum to Sho Hdr .
Fuel burned . .  M Ib/hr
Liberation, total val.  .
Furn. cooling factor net
Heat Losses
   Dry gas . . %
   Hydrogen and moisture in fuel
   Moisture in air . .  %
   Unbumed combustible . . %
   Radiation . . %
   Unaccounted for . .  %
Total losses . . %
Efficiency  . . %

Overfire Airport (% open)
                                   psi
                            Btu/hr  x cu  ft.
                            Btu/hr  x sq.  ft,
N.A.
21 U
102
17,930
61,395
6.03
5.25
«ili5
.35
.25
.50
12.51
87. U9
N.A.
212
101.9
17,920
61 ,361
5.896
5.23
.1)42
.35
.25
.50
12.368
87.63
N.A.
123
68
11,922
U0,827
U.86U
5.06
.117
.35
.25
.50
1* -4 1
i . 1 [\
88.86
N.A,
252
°u
16,I|S2
56.U37
6.12
5.176
.1U8
.35
.25
.50
12. 5U
87. U6
                                               100
                                        U-35

-------
                                TABLE k-7
TEST DATA
Prc-csaro superheater  outlet
Te:np.-'ratii.re steam  superheater outlet
Pressure  Boiler  .
Reheat s team
Temperature steam  entering reheater
Temperature steam  leaving reheater
Pressure steam entering reheate
Pressure steam leaving reheater
Temp feed entering  uvut
T~ap Toed, leaving econ
Te'iip ?ir entering uait
Temp alv leuving air  heater
Ter.p gas leaving rurnu-Te
T'.?:r.p .-ri3 leaving boiler
Temp gas leaving economizer
Tc~p .-j'i.3 leaving air  heater
Litto corrected for leakage
hj'ioes.? air leaving
Wet g-xs entering air heater
V/et gas leaving air heater
air entering air heater
Air leaving air heater
Draft in furnace
Air &  gas less total
Precsuro  loss Drum t> SHO KDR
Fuel burned
Liberation, total vol
?.ir:i.  i^o?.ing Factor -net
Heat Losses:
     Dry  Gas
     Hydrogen & moi3t:i;?e in  fuel
     Moisture in air
     Unoomed combustible
     Radiation
     U.i-'V.coun '• ^d for
'Tota.L  Bosses
Efficien.jy


Overfire Airport  (% open)

M Ib. hr.
psi
outlet F


=ater F
ater F
?r psi
r psi
F
F
F
F
F
F
F
F
F
%
M Ib/hr
M Ib/hr
M Ib/hr
M Ib/hr
in. H20
in. H00
2
psi
M' Ib/hr
Btu/hr x cu ft
Btu/hr x sq. ft
%
-.1 %

%
%
t%
%
%
V
865
1893
980
21kk
N.A.
N.A.
977
N.A.
502
N.A.
552
116
532
N.A.
N.A.
70k
N.A.
353
19.9
1088
N.A.
N.A.
100k
-0.90
N.A.
251
91
15956
>;|63'>
5.26
5.11
.13
.35
.25
•5^
11.60
88. kO
VI
861
1835
965
21k5
N.A.
N.A.
960
N.A.
502
N.A.
5k9
107
566
N.A.
N.A.
696
N.A.
3k6
33.3
122k
N.A.
N.A,
1139
-0.80
N.A..
260
92
L&.51)
y.> *•••• '
5.922
5.09k
.11*3
.35
.25
• 5o
12.26
87.7k
VII
860
1832
938
2102
N.A.
N.A.
985
N.A.
502
N.A,
559
110
576
N.A.
N.A.
705
N.A,
350
20.1
1119
N.A.
N.A.
1033
-0.75
N.A.
220
93
in '3 )0
55919
5.356
5.088
.129
.35
•25
.50
11.67
__88^3J
                                                                       100
                               100
                                         k-36

-------
                           TABLE  ij-7.  UNIT C TEST DATA
TEST NO.
Prox. Analysis (%)
I & II
                                              III &  IV
          VI
VII
Moisture
Volatile Matter
Fixed Carbon
Ash
Hit. Analysis (%) By Weight
Ash
S
H2
C
H20
N2
02
Btu/lb (as fired)
Wet Flue Gas Analysis by Volume
5.86
U3.61
U2.U3
8.10

8.10
0.50
5-UO
67.78
5.86
1.0U
11.32
12,221

6.92
U0.81
hk.&9
7.38

7.38
Q.2U
5.36
67. 3k
6.92
0.82
11. 3k
12,185

6.92
U0.81
1*U.89
7.38

7.38
0.2U
5.36
67. 3k
6.92
0.82
11.91*
12,185

6.39
U2.21
U3-66
7-7U

7.7U
0.37
5.38
67.56
6.39
0.93
11.63
12,203

6.39
U2.21
U3.66
7-7U

7.7U
0.37
5-38
67-56
6.39
0.93
11.63
12,203

     C02


     H20


     S0
 Gas Emission Data


   NOX (ppa)


   N02 (Lb/106 Btu)


   S02 (ppm)


   CO  (ppm)
 13.259/    13.830/
 13.621     12.606
  9.0057     9.UU57
13.8U1    12.U53    13.801
 9.U51     8.6U5
9-360
9.195
.0377
.037
390/630
0.5757
0.901
N.A./N.A.
N.A./N.A.
8.790
.018/
.017
U50/660
0.623/
1.011
N.A./N.A.
26/35
.018
601
0.832
N.A.
39
.026
398
0.619
N.A.
35
.028
307
O.U28
N.A.
kk
                                         k-31

-------
                     TABLE ii-8.  UNIT C TYPICAL ASH CONSTITUENTS
MgO
Si02
A1203
CaO
K20
Ti0
Air Fusion Temp.
Initial Deform.
Soft. Sph.
Soft. Hem.
Fluid
6.1+
2.1
1.8
56.8
17.0
5.1
8.1
2.1
0.9
0.2
Red/Oxid
201+0/211+0
21 20/2200
2160/221*0
21+20/2500
9.1*
1.6
1.9
1*3.1
11*.8
7.0
17.9
0.1+
0.8
0.2
Eed/Qxid
2000/2060
2020/2080
2060/2110
2200/231+0
Note:  These samples were taken prior to the test series reported here.  Ash
       analyses were not performed during the NOX tests.

-------
Figure U-10 shows the NOX emission, at full load, as a function of




Burner Zone Liberation Rate compared to a typical full-load curve




(the development of this curve is as explained for Figure 2.2).




This figure also contains two measured data points from another




single wall fired NSPS unit.  The second unit uses a coal with a




higher nitrogen content, approximately 3«6 Ib N02/106 Btu, and was




equipped with a reduced turbulence Intervene Burner.  The predicted




emission point represents that NOX level which would be expected if




the high turbulent Intervane Burner had been used.  The measured




data point  is about  17% lower and confirms the effectiveness of the




reduced turbulence design.  It is, therefore, possible to fit  the




burner and furnace designs  to the  coal  so  as  to  prevent violating




our 96% minimum  stoichiometry limitation.
                             U-39

-------
.
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$$ UNIT C':
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SINGLE WALL-FIRED WITH REDUCED TURBULENCE
__4_.
it
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INTERVANE BURNER. N02/Q=3.58

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	 • i :
FIGURE 4 -10
i
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i


-------
U«3  LOW MQy BURNER TEST DATA




     Foster Wheeler has developed a dual register,  dual throat,  coal burner which




     is inherently low in NOX emissions.  The burner, which has  been functionally




     discussed in Section 2.2C and shown in Figure  2.6, was developed on a four




     burner industrial-sized steam generator test facility.






     Although the NSPS of 0.7 Ib N02/106 Btu has been attained,  using the pre-




     viously-explained design philosophy, the need for a niore advanced burner




     design was also recognized.  This would permit greater design and operational




     flexibility.  In particular, the possible need for substoichiometric firing




     with some high nitrogen low heating value coals could be eliminated.  This




     goal has been achieved by the successful operation of the low NOX dual throat




     coal burner.






     Utility experience with this burner has been obtained on three  older,




     operational steam generators in Japan.  These  units,  two 265 MWe opposed-




     fired and one 75 MWe front-wall fired, were retrofitted with dual register




     burner designs functionally identical to that of Figure 2.6.  When designed




     in the early 1960's these units had no NOX controls.   They were designed




     for 20 percent excess air operation, with all air through the burners.




     All units were equipped with Foster Wheeler Ball Mills.  These three units




     are all  located  in Japan and were  designed and fabricated by Foster




     Wheeler's licensee Ishikawajima-Harima Heavy Industries, Ltd. (IKE), in




     cooperation with Foster Wheeler.






     The  opposed-fired units  were  later equipped with  overfire air  ports for  NOX




     control, with the original  Intervane  Burner.  However,  the  boilers  could not

-------
be operated with overfire air ports 100% open for more than 8-12 hours due




to increased slag buildup in the lower furnace, along the sidewalls and




around the burner throats.  This situation was caused by the lower furnace




reducing atmosphere which results when the overfire airports on these units




are 100% open and precluded long term continuous minimum NOX operation.  How-



ever, with overfire air ports 100% open NOX reductions of 30% were obtained.






Since 1976 all three units have been retrofitted with a dual throat low




NOX burner,  Figure U-11 shows results typical of one of the 265 MVfe steam




generators.






The unit design is similar to that of Unit A in Figure 1+.1.   Twenty-four




burners are utilized, 12 per firing wall in a lj wide x 3 high arrangement.




It is a natural circulation reheat type steam generator with a capacity of



1,8ij.8,000 Ib per hour superheated steam at 2500 psig and 1050F at the



outlet.






NOX emissions have been reduced approximately U8% by the low NOX burner




only (overfire airports closed) as compared to the high turbulent Inter-




vane Burner.  When overfire airports are 100% open the total NOX reduction




is about 67%.  Boundary air was also retrofitted to these units at the




same time as the low NOX burners.  The slagging situation has been sub-




stantially alleviated, though not eliminated when overfire air ports are




100% open,  by the combined effect of the low NOX burners' cooler, less




turbulent flame and the lower furnace oxidizing atmosphere provided by



Boundary Air.
                                 k-k*

-------
              N0y   EMISSIONS
                A
          265 MWe UTILITY BOILER
        700-
        600-!
   HIGH TURBULENT BURNER
            J
NOX,PPM 50°
(5) 3% 02
        400
        300-i
        200 -;
         100-
TYPICAL
OPERATING
REGION
           LOW NOX BURNER
                   OPTIMUM OPERATING REGION
            0    20  40    60   80   100
            OVERFIRE AIR PORT DAMPER OPENING(%)
                      U-U3
                                         FIGURE 4-11

-------
     After installation of the dual register burner, unit performance is vir-

     tually the same as with the initial design.  There were no detrimental

     effects to any aspects of steam generator operability.  However, with

     overfire airports there is an increase in unburned carbon in the ash;

     this increase is still well within acceptable limits.  The following

     table compares emissions performance under various operating conditions:


                                                                Unburned Carbon
Burner Type     OFAP (% Open)    NOx (ppa @ 3% 02)    02 (%)    (% in Flvash)
Intervane       min. (cooling          600             3-^          1.J>0
                      air)
Intervane            100               i±25             3.U          2.5
Low NOX         min. (cooling          310             3.5          1.5>0
                      air)
Low NOX              100               200             3.6          2.5


     Tests were performed with coal having the following typical properties:


                        Volatile Matter       1*1 ,8#
                        Fixed Carbon          30.1

                        Sulfur                 O.U5
                        Nitrogen               1.1 8

                        Moisture              12.1

                        Ash                   15.2

                        HHV                   11,500 Btu/lb


     Note  that,  for this coal,  an additional  1% unburned carbon  represents an

     efficiency loss of 0.19% and that  the unburned carbon  levels for the

     Intervane  and low NOX burners are  the same.  The combined use of overfire

     airports and low NOX burner has only a marginal effect on unit efficiency.
                                      u-w*

-------
Foster Wheeler's experience with low NOX coal burners has been obtained on




four older steam generators which had been initially equipped with the




Intervane Burner and later retrofitted with dual register burners.  The




steam generators capacities range from 125»000 Ib/hr steam flow (four




burners) to 1,850,000 Ib/hr (2k burners).  It is clear from these experiences




that combustion efficiency is the same with the low NOX burner as with the




Intervane Burner.






Although there is an increase in unburned carbon when overfire air ports are




100% open, with both types of burners, unit efficiency remains within guaran-




tee limits.  However, the long term effect on unit performance, of combining




low NOX burners with overfire air ports, is not yet fully quantified.
                                  k-kS

-------
5.0  COST SIFgEtttSraiAL FOR EMISSION CONTROLS




     The low-NO  system utilized "by Poster Wheeler consists of a low-NOx dual




     register burner,  overfire air ports and Boundary Air.   Although these




     components have all teen proven on operating utility steam generators




     (cverfire airports and Boundary Air on NSPS units and the complete systen




     on retrofitted pre-NSPS units) and this system has been sold on a number



     of new units, it is not yet in operation on a new NSPS steam generator.




     Consequently, a direct cost comparison bet-ween two units, an NSPS unit




     equipped with the complete NOX control system and a similar pre-NSPS unit.




     is not possible.






     In order to develop a meaningful cost differential imposed by the addition




     of NOX controls the following procedure has been used:






     A recently sold NSPS steam generator, Unit D, containing the complete HOX




     control  system has been used as a baseline.  The cost  increase  imposed by




     the  NSPS has been evaluated in two ways:






     (1)  The  cost increment imposed by  the use  of active NOX control measures




          (i.e., low emission burners, overfire  air ports)  was estimated by




          comparing  the cost of unit D as  sold with the  cost of that  unit if  it




          were redesigned without  any NCX controls.   When redesigning the unit,




          the  following constraints were applied:






          (a)   The lower furnace  was sized according  to  the burner spacings and




               Burner Zone Liberation Bate used  in pre-NSPS units of this type.






          (b)   Exit  gas temperature,and therefore total furnace surface, was



               maintained the same as the NSPS unit.
                                         5-1

-------
     (c)  Partial division wall (radiant superheater) surface was main-




         tained the same as the NSPS unit.






     (d)  The Heat Recovery Area was not changed; since the inlet and outlet




         gas temperatures were held constant it was assumed that the cost




         of this portion of the unit would not change, even if there were



         some minor dimensional changes.






(2)  The cost increment imposed by increasing boiler size (increasing




     cooling surface area can be considered to a passive NOX and slag




     control measure) has been estimated by comparing the cost of Unit D,



     as reconfigured to the pre-NSPS design, with that of Unit A.  It will




     be recalled that Unit A is a pre-NSPS unit firing high sulfur bituminous




     coal and represents the latest pre-NSPS boiler design.  As such it




     can be used to provide a baseline against which the larger pre-NSPS




    Unit D design can be compared.  The result of such a comparison would



    be the cost increase due to changes in furnace structure and associated




    equipment related to differences in fuel quality.






Figure 5-1  shows an outline drawing of NSPS unit as sold in 1977-  The




unit utilizes 2i| dual register low-NOx burners, 12 per firing wall in a



U wide x 3 high arrangement, supplied by six Poster Wheeler medium speed




MB-23 pulverizers.  It is a natural circulation reheat type steam generator




with a capacity of 3»800,000 Ib. per hour superheated steam at 2630 psig




and  1005? at the outlet and 3,300,000 Ib. per hour reheated steam at 580




psig and 1005F at the outlet.  Table 5-1 contains the unit design and fuel



parameters.
                                   5-2

-------
Figure 5«2 shows an outline drawing of this unit reconfigured as a pre-NSPS



design.  The following is a tabulation of the changes considered as the



boiler is reconfigured from the NSPS design to the pre-NSPS design.






(1)  'Pim is si on Control Equipment



     (a)  Low NOX burners (replaced by Intervane burner)



     (b)  Overfire air ports (eliminate)



     (c)  Boundary air system (elimimate)





(2)  Boiler Structure (reduced plan area; increased height)



     (a)  Structural steel (reduced)



     (b)  Windbox size (reduced by eliminating OFA port supply)



     (c)  Erosion baffles  (reduced)



     (d)  Furnace seals  (reduced)






(3)  Circulation System



      (a)  Waterwall  panels (decreased number)



      (b)  Downcomers (increased length)






 (U)   Field  Erection



      The effect of all modifications on the number of field labor man-



      hours  has been estimated.





 When all of the above are considered, the cost differential due to the  active



 NOx controls is obtained.  If this differential only is considered a biased



 viewpoint regarding the impact of the NSPS on boiler design will be obtained.



 This is due to the requirement that sufficient cooling surface be available



 when overfire airports are used with most coals, particularly those with



 high sulfur and iron contents.  Data has been presented earlier, in Section






                                    5-3

-------
U.O, which demonstrates that off-stoichiometric combustion is unacceptable

with pre-NSPS units which have high Burner Zone Liberation Rates, such as

units A and B.


Also, no such pre-NSPS units have been retrofitted with low emission burners

(those that were have cooler furnaces usually with at least one full division

wall).  It has, therefore, not yet been demonstrated that the pre-NSPS high

Burner Zone Liberation Rate design can accommodate a low emission burner.


In order to obtain a realistic indication of the cost of a new NSPS unit,

with respect to the more typical high Burner Zone Liberation Rate units,

the increase in furnace size (to provide lower Burner Zone Liberation Rates)

must be taken into account.  We must also note that unit D was designed to

use a low-sulfur sub-bituminous coal which also requires a larger furnace.

If there were no NSPS sulfur regulations it is possible that this unit could

have used a bituminous coal similar to that used by Unit A.


Thus, when all factors are considered the following relative costs are in-

curred due to the NSPS regulations:


               Boiler Design                              Relative Cost

1.  Unit A (pre-NSPS base design)                             100%

2.  Unit D (large furnace; no active NOX controls)            111;%

3.  Unit D (NSPS design; large furnace, low NOX               115.5$
            burner, overfire airports)


It is apparent that the cost of combustion modifications is significantly

lower than the cost of increasing furnace size to accommodate those modifica-

tions.  However, it must also be recognized that low emission burners pre-

sently being sold commercially are first generation equipment.  As more


                                   5-U

-------
knowledge is gained in the area of reducing NOX via combustion controls




burner complexity will undoubtedly increase.  It is difficult to predict



the costs of second and third generation low emission burners and their




ancillary control systems, but we can be safe in assuming they will




represent greater increases than those estimates presented above.




Although each increment in complexity will increase costs accordingly,




combustion controls will still be significantly less costly, in both



capital and operating expenses, than the use of any foreseeable post-




combustion cleanup technique.
                                    5-5

-------
                       UNIT  D:  NSPS  CONFIGURATION
 170' 3"
 106' 3"
 52' 3" —
           t-
           Z
           o
           cc
           LL
10'

Ma«


10'
 29' 3".
                                    37°)
                             •5 PART.


                           DIV. WALLS
                   DEPTH  5V 6%
ELEVATION  0' 0'
                                        —131' 6'
                              Ul
                              oc
                                               WIDTH  59' 7%"
                                          15' 7"
  9' 6"
O O  O  O

o o  o  o

o o  o  o
                                       5-6
                                                        FIGURE 5-1

-------
                      UNIT  D:  PRE  - NSPS  CONFIGURATION
   181' 6"-
   94' 6'
             O
             
-------
               TABLE 5-1.  UNIT D DESIGN DATA AND PERFORMANCE FUEL
Convection surface boiler
Water walls in furnace
Radiant Superheater
Convection Superheater
Reheater
Economizer
Air heater, Trisector
Total furnace volume
Total furnace sxvrface
Firing Equipment
     U.900 sq, ft.
    36,0^3 sq. ft.
    37,275 sq. ft.
    60,925 sq. ft.
   106,OUO sq. ft.
  131,307 sq. ft.
1,036,000 sq. ft.
  U72,260 cu. ft.
   7U,988 sq. ft.
Six FW MB Pulverizers
Performance based on fuel specified below:
  Grindability
  Size
  Max. moisture (%)
  Surface moisture (5)
52 (Hardgrove)
1-1A x 0
29.0
17.U
Ultimate Analysis
  C (% by weight)
  H2
  S
  N2
  02
  Ash
  H20
  HHV (as fired)
 3.50
 0.50
 0.70
12.00
 5.78
29.00
8520 Btu/lb as rec'd.
                                      5-8

-------
6.0  OIL FIRED UNIT RETRO-FIT FOR NOX CONTROL





6.1  CHRONOLOGY OF UNIT PERFORMANCE MODIFICATION



     Unit B is a natural gas and oil fired, supercritical once-through,  reheat



     steam generator.  It is rated at 5»600,000 Ib/hr main steam now at 100$F



     and 1;,700,000 Ib/hr of reheat steam at 1005*1.  Firing equipment consists of



     32 Foster Wheeler intervane burners arranged in four rows, four columns wide



     on both the front and rear furnace walls.





     This unit was designed just prior to the implementation of emission regula-



     tions for NOX emissions.  It was designed primarily for natural gas firing



     and has a burner zone liberation rate of 725,000 Btu/hr-ft2.  Because of



     limited gas supplies the unit has operated almost exclusively with oil fuel.



     Figure 6.1 shows the arrangement of the steam generator and Table 6-1 lists



     the design performance parameters.





     In anticipation of forthcoming emissions regulations the unit was designed



     with  overfire air ports  and  a  guarantee limit  of 500 ppm of NOX at  Jfa 0%



     was set.  During construction  it became apparent that the local authority



     would set the NOX limitation at 250 ppm for  both oil and  gas fuels.   In



     order to meet this regulation,  a flue gas recirculation system was added.



     The addition  of the flue gas recirculation system increased velocities



      through the burners  in excess  of optimum values.










     A test  program  was initiated after  the  start-up of  the unit (December 1971)



      to determine  NOX  emission compliance  status.  During this program the NO^



      control capabilities  of overfire air  ports,  off-stoichiometric firing and



      flue  gas recirculation were determined.  These techniques  were evaluated



      individually and  in combination to  obtain maximum NQx reduction capability.





                                        6-1

-------
                      FIGURE  6.1


            UNIT E   PRE  NSPS  OIL 8  GAS  FIRED



                (RETROFITTED  FOR  NOX CONTROLS)
               FOSTER  W  WHEELER
       i' I I     I   'I  • <->>

       .d.^lLI. il fl 0!.,,) iU (I'lCT,.::;
       Itf.'     . ,   '  11  i
      J-
  "'!pr

  • -:-!-l-.
       I'l.






        PMTE
           N SUPEPHra7£H
     i;
       ' FINISHING SUflEpHEATE
flEPHE
     a
            REME^ER OUTLETS'
V^-KQ^tf^^'ti
          «i
R
                   i
                       liftjrlM
                        '—^ -^.'
       J^T—
                                    T\
                                      1
                                     i i;
                             •r

                         !     'h
             tl;.
             ^IJI.TJ.
           •HIT
              —•* ^

           iSr^
           ^
            VI
                            l.Jr
h
                           6- 2

-------
 TABLE 6-1.  TRirr d DB3IGN DATA AND EERPOHM4.1B1!
Walls in Furnace
Radiant Superheater
Convection Superheater
Reheater I
Economizer ext. sur.
Air Heater (2)
Total Furnace Volume
Total Furnace Surface
 22,165 sq. ft.
 1^,276 sq. ft.
110,14*5 sq. ft.
 82,880 sq. ft.
172,600 sq. ft.
9U3.800 sq. ft.
208,U50 cu. ft.
        sq. ft.
TJltimate  Analysis
Fuel
Per cent  by
 C2H1+
 C2H6
 C02
 C3H8
 N2
 Btu/lb as fired
 Btu/cu ft @ F-30 in. Hg.

 Fuel
 Per cent by
 Ash
 S
 H2
 C
 H20
 N2
 02
 Btu/lb  as  fired
 Natural Gas
 Volume
 O.U
 86.5

 8.2
 0.1+
 1.9
 2.6
  22.U29
  1085

  No. 6 Oil
  Weight
  0.06
  1.70
  9-90
  86.29
  1.00
  1.00
  0.05
  18,000
                            6-3

-------
The emission obtained for these firing modes during oil fired operation




are shown in Figure 6-2, Curves A through D.






The combined effect of these NOX reduction techniques permitted oil fuel




operation, in compliance, at loads up to 630 MW.  Operational problems




resulted from the application of the NOX control techniques, however,




and load capability, due to boiler vibration, was limited to 600 MW.  At




loads above 600 MW, burner flame instability induced a condition of boiler




vibration that was unacceptable for continuous operation.






In order to improve the   unit   load capability, modifications were made




to the steam generator and a test program was initiated in March 1973.






The purpose of this program was to evaluate the following items with respect




to NOX emissions and boiler vibration:






1.  Optimization of burner pattern and increased number of burners




    out of service.






2.  Experimental burner modifications.






3.  Enlargement of the overfire air ports.






6.1.1   Optimization of Burners Out-of-Service Pattern




       In March 1973>  a program was initiated to optimize  the off-stoichio-




       metric combustion operating procedures for oil fuel at Unit E.  This




       program involved selectively removing up to 25 percent of the burners




       (8 of 32) from service in such a manner as to minimize NOX formation.




       The result of this phase of testing was to increase NOx compliance
                                  6-k

-------
  FIGURE  6-2    INITIAL TEST  RESULTS


               AS DESIGNED WITHOUT
              nNOx CONTROLS
                                         ;;OVERFIRE AIR (OFA)
O/S (4 BURNERS )a=
  PLUS OFA
                                             i-t—'-nt"' TT~~r '' :","'\
                                   . 0/S (8 BURNERS) OFA
                                       15% GAS  RECIRCULATION
            O/S (4 BURNERS)
            OFA PLUS 15%
            GAS RECIRCULATION
                   !-_•• .;i-r:Ttrrr-r
                  3LOAD ( MW

-------
    TABLE  6-2
BURNER  OUT OF SERVICE
   TEST  PATTERNS
TEST
1
2
3
4
5
PATTERN
OOOOJOOOO
oooqoooo
oooqoooo
OOOQOOOO
••••oooo
oooqoooo
••••
oooo
oooo
oooo
oooo
oooo
oooo
••••
oooo
oooo
oooo
oooo
••••
oooo
oooo
0*0*b«0«
oooopooo
oooopooo
NO, PPM
(DRY AT
3% 02)
195-225
200-245
205-275
220-265
230-265
MIN 02
%(N/S
AVE.)
3.1
3.5
4.6
4.0
4.1
TEST
6
7
8
9
PATTERN
•0*0
oooo
oooo
oooo
oooo
•0*0
oooo
oooo
oooo
oooo
••••booo
oooopooo
OOOOJOOOO
oooopooo
oooqoooo
NO, PPM
(DRY AT
3% 02)
235-275
240-325
245-300
255-300
MIN. 02
%(N/S
AVE.)
4.2
4.8
4.5
4.7
• BURNER OUT-OF-SERVICE, AIR
REGISTER OPEN
            6-6

-------
      load capability to 680 MW, with the third row of burners out of



      service.  For continuous operation, however, the actual load



      limit was set at 630 MW to avoid damage due to boiler vibration,



      see Figure 6-2, Curve E.  As shown by the summary in Table 6-2,



      this pattern had the lowest emissions of those tested.  The



      range of NO  emissions shown in the Table are given for  1  percent



      excess  oxygen over the minimum value which  is the smoke threshold.



      Boiler  vibration was not  significantly  affected by the various



      patterns tested.






6.1.2 Experimental Burner Modifications



      Efforts to  increase oil  fuel  load  capability and reduce boiler



      vibration,  continued in the  form of an experimental  burner program.



      This program involved the modification of four burners in the unit,



       and filming at high speed and the  effect on flame characteristics.



       Each of the following modifications were made to a different



       burner:  (a)  increased burner throat diameter,  (b)  addition of



       an oil gun diffuser plate, (c) extended oil gun, and (d)  10 percent



       burner tertiary air nozzle and sleeve.
                                   6-7

-------
The increased burner throat diameter and diffuser plate modifications did
not produce stable flame characteristics, and they were, consequently,
rejected.  High speed films taken during operation showed the extended oil
gun did seem to produce the desired flame characteristics and, subsequently,
32 extended oil guns (10 in.) were obtained for testing.  This test could
not be completed, however, due to extremely high boiler vibration which
resulted before all the extended oil guns could be installed.

The burners were also modified to provide a 10 percent teriary air flow
around the oil gun.  High speed films indicated that this modification would
produce stable flame characteristics, and preparations were made to
modify all 32 burners.

The burner tertiary air nozzle and sleeve modification involved manufacture
of equipment and taking the unit out-of-service for two months.  As a
result, this modification was not completed until November 1973-  In con-
junction with the burner modification, the overfire air ports were increased
in size by a factor of two.
Between November 1973 and January 197U? the boiler modifications were
thoroughly tested.  These tests showed that the 10 percent tertiary
air nozzle and sleeve burner modification increased the maximum NOx
compliance load to 710 MW (test condition-not acceptable for continuous
operation) with boiler vibration at an acceptable level.

The load limiting factor of the 10 percent tertiary air system (710MW)
was FD fan capability, due to a high minimum excess oxygen level (5>.5>
percent) which was required to stay above the smoke threshold, or to maintain
a clear stack condition.

In an effort to increase load capability, the amount of tertiary air was
decreased to 5 percent.  During the next series of tests, which were
conducted from February to- April 197k» it was found that  boiler vibration
was still within acceptable limits, the minimum excess oxygen requirement
decreased to k*5 percent and NOx compliance was achieved at a maximum load
730 MW under test conditions,
                                 6-8

-------
Although the tertiary air was decreased to 5 percent,  the load limiting
factor was still a high excess oxygen requirement, and further modification
would be required to achieve full load.  In June 197U» the unit was again
taken out-of-service and, at that time, three 1+5 deg swirl vanes were
installed in the tertiary air nozzle.  Testing of this burner configuration
showed that the excess oxygen requirement was reduced to 3 percent and NOx
complaince was achieved at a maximun load of 750 KW under test conditions.
This configuration also precipitated a condition of continuous boiler
vibration at load above UOO MW.

The next phase of testing involved a study of the boiler vibration charac-
teristics in an attempt to improve this condition by adjusting existing
operating parameters.  This was not successful, but the study did suggest
a  further modification which involved  removing the swirl vanes from all but
the top row of burners.  This was accomplished in October 197U. and testing
showed that boiler vibration was reduced  to  an acceptable level.

The maximum load capability of the unit was  significantly limited at  that
time  due  to two factors.  The first being an increase  in the  excess  oxygen
requirment  to U percent  due to removing 75 percent of the  tertiary air
 swirl vanes; and  the second was  the  revised oil  fuel  NOx emission limit
 of 225  ppm effective January  1,  1975«  Operating within the constraints
 of acceptable   boiler vibration   and NOx compliance,  the unit is now capable
 of loads up to  680 MW.
                                   6-9

-------
6.2  EFFECTIVENESS 0? CONTROLS



     As noted in the preceding section there were basically three  periods  of




     data taking on unit E.   The first was immediately after initial  startup.




     The findings of this period are discussed in the  preceding section and




     are shown in Figure 6-2.  To summarize "briefly the following  conclusions




     could be drawn:






     1.  The most effective  means of NOX control  was a combination of gas




         recirculation and staged firing which allowed the  unit to operate




         at a maximum of 799^ of its rated capacity without  exceeding  250 ppn




         of NOX.






     2.  The use of these controls resulted in excessive boiler vibration  and




         flame instability due to very high burner velocities.   This  is because




         the unit, especially the burners,  was not designed for either of




         these control techniques.






     3.  High levels of excess air were required  to avoid smoking  when using




         staged combustion.






     Following this initial  period the unit was modified in the following  way:






         a.  overfire air ports were enlarged




         b.  10% tertiary air nozzles were added




         c.  igniters and flame scanners were extended






     Another period of data  taking following during which the burner  pattern




     for staged combustion was optimized.   Maximum NOX compliance  load was




     increased however, the high excess air levels and  boiler vibrations con-




     tinued to be a problem.   Consequently,  the unit was modified  again.   This





                                      6-10

-------
time swirl vanes were added,  and adjustable tertiary air nozzles were



installed.  This was the last group of modifications made to the unit to



date.  The current oil fuel NOX compliance capability of the unit is 680MW



or 8^)d of its original rated capacity.
The results of the testing and modifications were summarized in figures




6-3 and 6-U.  The control techniques which have been effective in reducing




NOX are gas recirculation, staged combustion (interstage air) and load




reduction.  Overfire air has not been particularly effective in reducing




NOX.  This is because excess air had to be increased whenever the overfire




air ports were opened in order to maintain a clear stack.  It appears that




the air entering  the furnace was unable to mix properly with the combustion




gases.
 Figure  6-3 shows  the  effect  of gas  recirculation and interstage  air with



 unit load as a parameter.  It  can be  seen that gas recirculation produces



 a very  steep drop in  emission, for  example the difference in emission from



 point a to point  b represents  a decrease of almost
 The quantity of gas recirculation which can be used is limited by the



 capacity of both the gas recirculation and forced draft fans.  In particular,



 because of the high excess air levels which must be maintained when using




 staged combustion, as well as the increased draft losses resulting from gas




 recirculation the forced draft fan capacity becomes a limiting factor.






 Figure 6-3 shows a steeper slope for line a-b than for line c-d.  This is



 to be expected since for line c-d the interstage firing has already reduced
                                   6-11

-------
the thermal NOX somewhat and consequently, gas recirculation will have a




lesser comparative effect.






Figure 6-1; shows the effect of reduced load on NO  emission for the uncon-




trolled condition as well as for interstage firing.  One data point with




flue gas recirculation is included.  Load reduction is not an acceptable




emission control technique however, for this unit there has been no modifi-




cation which would allow compliance and so the unit has been derated.




Line a-e indicates a reduction in emission of 3^% for a load reduction




of 18% for the unit with no controls.  If interstage firing and flue gee




recirculation are added however, the effect of load reduction is reduced




to 32% reduction in NOX emission for a load reduction of 22%.
                                 6-12

-------
8:
(0 =
o =
o--
- « «
                FIGURE 6 - 3     EFFECT  OF  GAS  RECIRCULATION
NOy ,PPM
          500
    j_l.i 4

         — 300
          •:':
         F-250
         -frrrr-
           200
          — 180
            •

               s^
                ::: •;:

                  TT-

                U4-
                 ..:

              X
                        —
            tJC(
                              .
                           •:;

                            •
                           S3

                           rr-
                   tit

                   X

                    • ::•

                EEIE^^r|~-
                                  FfV
                                    N
                                                t—
                                            ,-r.;-u


                        X
                             £$
                                         :XI

                                                    !
                                                   =e


                                                  - --
                                         -*-t

                                         -.--
                                       it^^rtr


  S
                                                        X

                                        S^
                                S5
                                       rrr:
!"_'.«V
                                                 Js-rrrr

                                                                           ALL  BURNERS

                                                              ~
                                                                      ^4--^ INTERSTAGE
                                                                                        '
                                                                        (%) -  % XS AIR

                                                                                    1 .  :   j

                                                                                       '
                                                                         _,'4._
                                                                   i


                                                                 : '  .uhri:
                                                            '-f-

                                                                                    :T-'~ '

                                                                               _i^4
                                                                         .      ,   :•
                                                                      ^ife




                                                                18%
                                                g
                                                          h.t

                                                15
                                                               —(—— —
                                                               --~r= - :--4^.
                                                                             	^j...

                                                                       -i	r

                                                                                ! ____ i _ ...



                                                                                    ~ ^
                                                                 ::lr


                                                                *	rr.t- !
                                                            ==ra=%M..R.=
                                                6-13

-------
0
 i
n



-------
6.3  OPERATIONAL DIFFICULTIES




     Modification of Unit E to comply with air quality regulations has introduced




     severe operational problems.   These problems have occurred in two areas:






                            1.  boiler vibrations




                            2.  high excess air requirements






     The boiler vibrations have occurred as a result of flame instabilities at




     the burners.  These instabilities are caused by extremely high secondary




     air and gas flows through the burners which are a result of  the addition




     of gas recirculation.  These instabilities are exacerbated by the use of




     interstage  firing which  raises  the heat  output per burner.   A whole series




     of burner modifications  have been attempted  to alleviate  the boiler vibra-




     tions however,  these have met with limited  success.  Development work is




     still continuing in this area.






     Tne  other  major operating problem  at Unit E has  been an unusually high




     excess  air requirement whenever off-stoichiometric  firing is used.  This




     is  especially debilitating because the  increased excess air has  the effect




      of  increasing UOX emissions  and reducing the effectiveness cf the  enis.sier.




      controls.   In addition, high excess air levels reduce  boiler efficiency and




      increase the unit's fuel usage.






      The requirement for very high excess air is especially severe when the




      overfire air ports are in use but, even with staged combustion excess air




      must be kept unusually high to avoid a  smoky stack.  The high excess air




      requirement also increases velocity through the burners adding to flame
                                       6-15

-------
instability and boiler vibration problems.  A secondary effect of the




high excess air requirement is increased fan power consumption and an




attending limitation on unit capability with emission controls in opera-




tion due to the capabilities of the fan and its drive.






These operational difficulties have under certain circumstances,  caused




a greater derating of Unit E than is required to meet NOX emissions




alone.  However, none of these problems occur when the unit is operated




without emission controls, up to its design rating.
                                 6-16

-------
6.U  COST OF MODIFICATIONS




     The attached Table 6-3 indicates the cost of the  modifications which were



     made to Unit E.   In examining this table it is necessary to  keep  several




     points in mind:






     1.   Costs shown are only for those modifications  which were  carried out




         through Foster Wheeler.  There may have been  modifications performed




         by others, either in engineering, fabrication or erection, the cost



         of which is unavailable to Foster Wheeler.  For example, the  last




         group of modifications were not installed by Foster Wheeler  and




         consequently, the cost of that installation cannot be included in




         the table.  We do believe however, that the most important modifica-




         tions were carried out through Foster Wheeler and are included in




         Table 6-2.






     2.  The table includes only summary costs for all of the work accomplished




         under a particular contract between Foster Wheeler and the owner.




         These totals may include work which was not  aimed at NOx control.



         However,  the  scope of work listed in our records includes only the




         modifications for NOX  control.  Furthermore, if other work was included




         it would  have been a very small portion of the total, since the major




         items in  the  scope of  each group of modifications are easily identified.




         In any case the  amount of effort required to break down these totals




         on an item by item basis is well beyond what is reasonable for a study




         effort of this type.






      3.  The  dates listed for each group of modifications  are average  dates.




         The  actual work  was performed over  periods of  several months.
                                       6-1?

-------
U.  The second group of modifications shows the cost for enlarging the




    overfire air ports.  This cost should be comparable to the cost of



    adding overfire air ports to a unit which had none.  In order to




    enlarge the ports the waterwall tube sections containing the smaller




    ports had to be removed which is just what would have to be done if




    there were no ports to begin with.






5.  On Unit E the flue gas recirculation system was added while the unit




    was in construction.  The cost of adding this system is therefore




    somewhat lower than it would have been if construction were complete.




    However, the difference in this instance is small because the flue



    and duct erection work had already been completed by the time the



    flue gas recirculation system was added.  The only savings was in that




    the contractor's personnel and their equipment were already on the




    jobsite and able to start work.  Therefore, the cost of adding flue




    gas recirculation to Unit E is basically the same as it would have



    been if the addition were made after the unit was in operation.
                                6-18

-------
                                   TABLE 6-3

                            UNIT E MODIFICATION COSTS
APPROXIMATE
   DATE
   5/71
   7/73
   7/74
                 SCOPE
Add Gas Recirculation fan, ductwork,
mixing device, motor dampers and con-
trols.  Includes erection.
Enlarge overfire airports, add tertiary air
ports extend igniters and scanners.  In-
cludes erection.
Add Burner Swirlers. Add adjustable
tertiary air ports.  Further modifica-
tion of scanners and ignitors.  Does
not include erection.
  COST   I   COST
(Actual)  (1978 Dol.)
                                                                   $751,575.00
          $1,7U6,000
                                                                    707,670.00'  1,319,000
                                                                              I

                                                                              i
                                                                    11^,000.00
             166,800
                                       6-19

-------
                                 APPENDIX C
                   SUMMARY OF NOY CORRELATION TEST DATA
                                /N

       A listing of the data used in the regression analysis of Section 4
correlating NO  emissions to degree of control, boiler design and
              ^
operating variables, and fuel properties is given in Tables C-l through
C-7.  Data sources have been referenced in Section 4.2.2.  (Detailed
process engineering data have been summarized in Section 5, and will not
be reproduced here.)
       For the NO  correlation test data, Tables C-l through C-7, a
                 /\
different table itemizes input data for each specific equipment/fuel
classification according to the following scheme:

                       Table         Equipment/Fuel
                        C-l          Tangential/Coal
                        C-2          Opposed Wall/Coal
                        C-3          Single Wall/Coal
                        C-4          Opposed Wall/Oil
                        C-5          Single Wall/Oil
                        C-6          Opposed Wall/Gas
                        C-7          Single Wall/Gas

Within each  table,  the  data  are  divided  into  sets,  with  each set
representing a  single test run.   Each  set  contains  four  rows of  numbers.
The  first  three rows of the  data contain  information  on  fuel and  boiler
variables  while the fourth row gives emission  levels.  Data  from the  first
test on  tangential  coal-fired boilers  have been  repeated below.   The
meaning  of each entry  is  described  by  its  assigned  footnote.
                                     C-l

-------
                                                                        DATA KEY

                           la     lb      1C     3d     le       1.42f    113.859     173.1h    805.71    64.0*         2k     O.O1
113.859
0.0n
0.0*
n rf1
173.1h
100.0°
°-S
0.
-------
                       v -- Burner  tilt  (degrees  above or  below  horizontal  position);  when zero,  information  was  not  available

                       w — Overfire  air  tilt  (degrees above  or  below horizontal  position);  when  zero,  Information  was  not

                            available
                       x -- Heating value of the  fuel (kj/kg) on a dry basis  for  coal  and  oil,  MJ/m  for  natural  gas

                       y -- Code number indirecting the type of test and type of  NOX controls applied

                            1.0 — Baseline and low excess air tests
                            2.0 — Off stolcMometrlc combustion test with  burners out of  service
                            2.1 -- Off stolchiometric combustion test with  biased burner firing
                            3.0 — Off stolchiometric combustion test with  overfire air
                            4.0 ~ Burners out of service and overfire air
                            5.0 -- Flue gas recirculation
                            6.0 — Burners out of service and flue gas recirculation
                            7.0 — Overfire air and flue gas recirculation
                            8.0 -- Burners out of service, overfire air, and  flue gas  recirculation

                       z — NOX emissions (ppm dry 9 3X 02)

                            S02 emissions (ppm dry 9 3t 02); If zero, data  not available
                            SO. emissions (ppm dry 9 3% 02); 1f zero, data  not available

o                    Y  — CO emissions (ppm dry 9 3X 0,,); If zero, data not available

co                    A  — Particulate emissions (ng/J); if zero,  data not available

-------
TABLE C-l.  NO  CONTROL TEST DATA FROM TANGENTIAL COAL-FIRED BOILERS
1
2
2
4
1
2
3
4
1
2
1
2
3
4
1
2
0 ^
1
2
3
1
2
3
4
1
2
3
4
1
2
3
1
3
4
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
1
1
1
1
1
1
1
1

1
1
1
1
1
1
1
1
1
1
1
1
1
t
1
1
1
1

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
1
1
1
1
2
2
2
2
3
3
3
3
4
4
4
4
5
5
5
5
6
6
6
6
7
7
7
7
8
8
8
a
9
9
9
9
10
10
10
10
1.42000+00
0.00000
1.34700+02
5.68000+02
1.42000+00
0.00000
1.15POO+02
4.14000+02
1.42000+00
0.00000
1.22000+02
4.18000+02
1.42000+00
0.00000
1.11000+02
3.01000+02
1.30000+00
0.00000
1.17300+02
4.05000+02
1.30000+00
0.00000
1.09700+02
3.64000+02
1.30000+00
0.00000
9.40000+01
2.55000+02
1.30000+00
0.00000
8.90000+01
1.95000+02
1.30000+00
0.00000
1.07000+02
2.74000+02
1.30000+00
0.00000
A.4AOOO+01
1.52000+02
1.17990+02
O.OOOOP
0.00000
0.00000
1.17990+0?
0.00000
0.00000
0.00000
9.43920+01
0.00000
0.00000
o.oocoo
9.43920+01
0.00000
0.00000
0.00000
1.29996+02
0.00000
0.00000
0.00000
1.29996+02
0.00000
0.00000
0.00000
1.27616+02
0.00000
0.00000
0.00000
1.29271+02
0.00000
o.oooon
0.00000
1.07640+02
O.POOOO
0.00000
0.00000
1 .06916+02
0.00000
0.00000
o.noooo
1.79465+02
1.00000+02
0.00000
0.00000
1.79465+02
1.00000+02
0.00000
0.00000
1.43565+02
8.00000+01
0.00000
0.00000
1.43565+02
8.00000+01
0.00000
0.00000
2.37761+02
8.78000+01
0.00000
0.00000
2.37761+02
8.78000+01
0.00000
0.00000
2.33440+02
8.62000+01
8.00000+00
0.00000
2.36405+02
8.73000+01
8.00000+00
0.00000
1.96878+02
7.27000+01
0.00000
0.00000
1.95522+02
7.22000+01
8.00000+00
0.00000
8.35050+05
1.34700+02
0.00000
0.00000
8.35050+05
1.15800+02
0.00000
0.00000
8.35050+05
1.22000+02
0.00000
1.20000+01
8.35050+05
1.11000+02
0.00000
6.70000+01
1.38589+06
1.17300+02
-3.00000+01
2.60000+01
1.38589+06
1.09700+02
-3.00000+01
1.50000+01
1.38589+06
1.18100+02
-3.00000+01
4.20000+01
1.38589+06
1.10800+02
-3.00000+01
5.30000+01
1.38589+Q6
1.07000+02
l.OOOOO+Ol
0.00000
1.38589+06
1.13100+02
1.00000+01
0.00000
6.40000+01
5.60000+00
0.00000
0.00000
6.40000+01
3.00000+00
0.00000
0.00000
6.40000+01
3.90000+00
0.00000
0.00000
6.40000+01
2.20000+00
0.00000
0.00000
4.00000+01
3.20000+00
0.00000
0.00000
4.00000+01
1.90000+00
0.00000
0.00000
3.20000+01
3.30000+00
0.00000
0.00000
3.20000+01
2.10000+00
0.00000
0.00000
2.40000+01
1.50000+00
0.00000
0.00000
3.20000+01
2.50000+00
0.00000
0.00000
2.00000+00
0.00000
2.97238+0*
0.00000
2.00000+00
0.00000
2.97238+04
0.00000
2.00000+00
0.00000
2.97238+04
0.00000
2.00000+00
0.00000
2.97238+04
0.00000
2.00000+00
0.00000
2.84656+04
0.00000
2.00000+00
0.00000
.2.56230+04
0.00000
2.00000+00
0.00000
2.75709+04
0.00000
2.00000+00
0.00000
2.8*190+04
0.00000
2.00000+00
0.00000
2.52805+04
0.00000
2.00000+00
0.00000
2.54762+0*
0.00000
0.00000
*. 97000+00
1.00000+00
o.ooooo
0.00000
5.97000+00
1.00000+00
0.00000
0.00000
5,97000+00
1.00000+00
0.00000
o.ooooo
5.97000+00
1.00000+00
0.00000
0.00000
8.50000+00
1.00000+00
0.00000
o.ooooo
9.1*000+00
1.00000+00
0.00000
o.ooooo
8.29000+00
2.00000+00
o.ooooo
o.ooooo
6.88000+00
2.00000+00
0.00000
o.oooon
7.48000+00
1.00000+00
o.ooooo
o.ooooo
6.26000+00
2.00000+00
0.00000

-------
                                                      TABLE C-l.  (Continued)
                               TANGENTIAL COAL FIRED  BOILERS
o
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
'i
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
1
1
J
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
t
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
11
11
11
11
12
12
12
12
13
13
13
13
14
15
15
15
15
16
16
16
16
17
17
17
17
Ifl
Ifl
18
18
19
19
19
19
20
?0
1.20000+00
1.31978+00
1.25000+02
5.69100+02
1.30000+00
1.31978+00
1.17900+02
4.23400+02
1.20000+00
1.31976+00
1.07200+02
3.06000+02
1.20000+00
1.31978+00
1.09200+02
3.67700+02
1.20000+00
1.31978+00
9.73000+01
2.83700+02
1.20000+00
1.31978+00
1.51300+02
6.15400+02
1.20000+00
1.3197P+00
1.30600+02
5.40900+02
1.10000+00
1.31978+00
1.28000+02
4.59400+02
1.10000+00
1.31978+00
9.47000+01
2.44300+02
1.10000+00
1.3197P+00
1.1PSOO+02
1.37655+02
2.36220+00
0.00000
1.24700+03
1.37655+02
2.36220+00
0.00000
1.40700+03
1.37655+02
2.36220+00
0.00000
1.22900+03
1.06087+02
2.36220+00
0.00000
1.40100+03
1.03396+02
2. 36220+00
0.00000
1.34?00+03
7.18290+01
2.36220+00
0.00000
1.40900+03
7.34850+01
2.36220+00
0.00000
1.97000+03
7.08975+01
2.36220+00
0.00000
2.01300+03
1.05467+02
2.36220+00
o.onooo
1.95200+03
7,o"975+01
2.36220+00
o.onono
1.59500+03
7.791e4+01
1.00000+02
0.00000
0.00000
7.7918*+01
1.00000+02
0.00000
0.00000
7.79184+01
1.00000+02
0.00000
0.00000
6.00634+01
7.71000+01
0.00000
0.00000
5.65177+01
7.51000+01
4.00000+00
0.00000
4.06627+01
5.22000+01
0.00000
0.00000
4.16091+01
5.34000+01
0.00000
0.00000
4.01264+01
5.15000+01
0.00000
0.00000
5.96849+01
7.66000+01
4.00000+00
0.00000
4.01264+01
5.15000+01
4.00000+00
o.oooon
3.23472+05
1.25000+02
0.00000
2.83000+01
3.23472+05
1.17900+02
3.00000+00
2.66000+01
3.23472+05
1.07200+02
0.00000
1.31100+02
3.23472+05
1.09200+02
8.00000+00
3.34000+01
3.23472+05
1.29300+02
1.00000+01
2.66000+01
3.23472+05
1.51300+02
7.00000+00
6.86000+00
3.23472+05
1.306QO+02
3.00000+00
2.06000+01
3.23472+05
1.28000+02
0.00000
2.554QO+02
3.23472+05
1.26300+02
-5.00000+00
2.31000+01
3.23472+05
1.49300+0?
0.00000
2.49000+01
1.60000+01
5.02000+00
0.00000
0.00000
1.60000+01
3.90000+00
0.00000
1.84900+02
1.60000+01
2.26000+00
0.00000
0.00000
1.20000+01
2.40000+00
0.00000
0.00000
1.20000+01
4.76000+00
0.00000
0.00000
1.20000+01
7.90000+00
0.00000
0.00000
1.20000+01
5.59000+00
0.00000
0.00000
1.20000+01
5.30000+00
0.00000
0.00000
1.20000+01
4.20000+00
0.00000
0.00000
1.20000+01
6.90000+00
0.00000
0.00000
1.00000+00
0.00000
2.75126+04
0.00000
1.00000+00
0.00000
2.70932+04
4.54400+00
1.00000+00
0.00000
2.71165+04
0.00000
1.00000+00
0.00000
2.70466+04
0.00000
1.00000+00
0.00000
2.70723+OH
0.00000
1.00000+00
0.00000
2.72563+04
0.00000
1.00000+00
0.00000
2.70723+04
0.00000
1.00000+00
0.00000
2.67647+04
0.00000
1.00000+00
0.00000
2.70000+04
0.00000
1.00000+00
0.00000
2.55321+04
o.ooono
0.00000
7.40000+00
1.00000+00
0.00000
0.00000
6.60000+00
1.00000+00
0.00000
0.00000
7.00000+00
1.00000+00
0.00000
0.00000
9.80000+00
1.00000+00
0.00000
0.00000
9.00000+00
2.00000+00
0.00000
0.00000
7.60000+00
1.00000+00
0.00000
0.00000
6.80000+00
1.00000+00
0.00000
0.00000
9.50000+00
1.00000+00
0.00000
0.00000
9.4QOOO+00
2.00000+00
0.00000
0.00000
1.19000+01
2. 00000 + 00
0.00000

-------
                     TABLE C-l.   (Continued)
TANGCNTIAL COAL FIRCD BOILERS
1
2
3
«
1
2
3
1
1
2
3
>»
1
2
3
i
1
2
3
o ,
o»
1
2
3

-------
                     TABLE  C-l.   (Continued)
TflMGErv.TTAL  COAL  FIREO  BOILEKS
1
2
3
4
1
2
3
4
1
2
3
4
1
?
3
4
1
2
0 3
-I* "
1
2
3
14
1
2
3
4
1
2.
3
4
1
2
3
4
1
2
3
4
3
3
3
3
i*
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
1
1
\
1
1
1
1
\
1
1
\
\
\
1
1
]
1
1
1
1
1
1






1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
,3
3
31
31
31
31
32
32
32
32
33
33
33
33
34
34
34
34
35
35
35
35
36
36
36
36
37
37
37
37
36
?a
3fl
34
39
3-9
39
39
40
40
40
40
I. 00000+00
1.11978400
rt.flOOOO+01
2.6S300+02
1.39000+00
0.00000
1.34000+02
4.16000+02
1.40000+00
0.00000
1.29000+02
3.66000+02
1.40000+00
O.OQOOO
1.23000+02
3.35000+02
1.40000+00
a. ooooo
l.lflPOO+02
3. 32000+02
i.4nooo+oo
0.00000
1.05500+02
2.93000+02
1.40000+00
0.00000
1.10300+02
3.46000+02
1.39000+00
0 . 0 0 0 0 (1
1.09400+02
-5.49000 + 02
1.36000+00
n.noooo
1.0411)0 + 02
^.floono+02
l.4fioon + ou
o . o n o o 0
i.^2fjon + 02
^.7*000+02
6.92415+01
?. 36220+00
0.00000
2.07400+03
1.34550+02
0.00000
O.OUOOO
0.00000
1.34550+02
0.00000
0.00000
0.00000
1.34550+02
0.00000
0.00000
0.00000
1.34550+02
0.00000
0.00000
0.00000
1.34550+Q2
0.00000
0.00000
0.00000
1.3455P+02
o.oooon
o.oooon
o.onooo
J.34«S50 + 0?
0.00000
o.noooo
0.00000
1.34550+02
n. noono
0.00000
(i . o u o n o
1.34*i50 + n2
0 . 0 1) 0 0 0
o.nuonn
0 . 0 0 0 0 (1
3.91800+01
5.03000+01
0.00000
0.00000
0.00000
1.00000+02
0.00000
0.00000
0.00000
1.00000+02
0.00000
0.00000
0.00000
1.00000+0?
0.00000
0.00000
0.00000
1.00000+02
0.00000
0.00000
0.00000
1.00000+02
0. 000(10
o.ooonn
0.00000
1.00000+02
0.00000
o.oooon
0.00000
i.ooono+02
0.00000
o.ooono
0.00000
1. 00000+02
0.00000
0.00000
0.00000
i.ooono+02
0.00000
o.ooonr
3.23472+05
1.54000+02
-1.50000+01
2.11000+01
1.77324+06
1.34000+02
1.00000+01
0.00000
1.77324+06
1.29000+02
l.OOUOO+01
0.00000
1.77324+06
1.23000+02
1.00000+01
0.00000
1.77324+06
1.23000+02
1.00000+01
0.00000
1.77324+Q6
1.17000+02
1.00000+01
0.00000
1 .77324+06
1.26000+02
1 .10000+01
0.00000
1.77324+06
1.25000+02
1.20000+01
0.00000
1.77324+06
1 .19000+02
1 .00000+01
O.OUOOO
1.77324+06
1.32000+0?
l.OOOOO+Ol
0.00000
A. 00000+00
6.70000+00
-1.00000+01
0.00000
5.60000+01
5.40000+00
1.00000+01
0.00000
5.60000+01
4.90000+00
0.00000
0.00000
5.60000+01
4.00000+00
0.00000
0.00000
5.60000+01
4.00000+00
1.00000+01
0.00000
5.60000+01
3.80000+00
1.00000+01
0.00000
5.60000+01
4.60000+00
l.OOOOO+Ol
0.00000
5.60000+01
4.40000+00
1.00000+01
0.00000
5.60000+01
3.70000+00
1.00000+01
0.00000
5. 60000+01
5.20000+00
1 .00000 + 01
0.00000
1.00000+00
0.00000
2.86567+04
0.00000
2.00000+00
0.00000
2.74288+04
4.27000+00
2.00000+00
0.00000
2.85891+04
0.00000
2.00000+00
0.00000
2.85891+04
0.00000
2.00000+00
0.00000
2.85891+04
0.00000
2.00000+00
0.00000
2.85891+04
0.00000
2.00000+00
0.00000
2.90528+04
6.85000+00
2.00000+00
0.00000
2.74288+04
6.26000+00
2.00000+00
0.00000
2.92718+04
2.R7000+00
2.00000+00
0.00000
2.85891+04
0.00000
0.00000
9. 6QOOO + 00
4.00000+00
0.00000
0.00000
1.32700+01
1.00000+00
o.uoooo
o.ooouo
1.28600+01
1.00000+00
0.00000
0.00000
1.28600+01
1.00000+00
0.00000
0.00000
1.28600+01
3.00000+00
0.00000
0.00000
1.28600+01
3.00000+00
0.00000
0.00000
1.35400+01
3.00000+00
O.UOOOO
0.00000
1.32700+01
3.00000+00
0.00000
o.uoooo
1.28100+01
3.00000+00
0.00000
o.uooon
1.28600+01
l.UOOOO+00
o.oooon

-------
                    TABLE  C-l.  (Continued)
TftNGtNTlAL COAL FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
*
1
2
0 3
1 4
09
1
2
3
•»
1
2
3
*
1
2
3
4
1
2
3
4
1
2
3
4
4
4
4
**
4
4
4
*»
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
1
1
1
t
1
1
1
1
1
1
t
1
1
t
1
1
1
1
1
1
1
1
1
t
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
41
41
41
41
42
42
42
42
43
43
43
43
44
44
44
44
45
45
45
45
46
46
46
46
47
47
47
47
48
48
48
48
49
49
49
49
50
50
50
50
1.40000+00
0.00000
1.11400402
3.18000402
1.40000400
0.00000
1.02900402
2.59000402
1.00000400
0.00000
1.22000402
3.89000402
1.00000400
0.00000
1.18600402
3.73000402
1.00000400
0.00000
1.19000402
3.55000402
1.00000400
0.00000
1.13600402
3.06000+02
1.00000400
0.00000
1.02600402
2.61000402
1.00000400
0.00000
9.75000401
2.66000402
1.00000400
0.00000
1.21000402
4.28000402
1. 00000400
0.00000
1.16200402
3.6POOO+02
1.34550+02
0.00000
0.00000
0.00000
1.34550+02
0.00000
0.00000
0.00000
1.40656402
0.00000
0.00000
0.00000
1.40656402
0.00000
0.00000
0.00000
1.38690402
0.00000
0.00000
0.00000
1.38690402
0.00000
0.00000
0.00000
1. 37758+02
0.00000
0.00000
0.00000
1.37344402
0.00000
0.00000
0.00000
1.33722+02
0.00000
0.00000
0.00000
1.33722+0?
0.00000
0.00000
0.00000
0.00000
1.00000+02
8. 00000 + 00
0.00000
0.00000
1.00000+02
8.00000+00
0.00000
1.41767+02
9.71000+01
0.00000
0.00000
1.41767+02
9.71000+01
0.00000
0.00000
1.39717+02
9.57000+01
0.00000
0.00000
1.39717402
9.57000401
0.00000
0.00000
1.38834402
9.51000401
0.00000
0.00000
1.38392+02
9.48000+01
0.00000
0.00000
1.34733+02
9.23000+01
0.00000
0.00000
1.34733+02
9.23000+01
0.00000
0.00000
1.77324+06
1.30000+02
1.00000+01
0.00000
1.77324+06
1.20000+02
1.00000401
0.00000
9.76276405
1.22000402
-1.50000401
0.00000
9.76276405
1.21000+02
-1.60000401
0.00000
9.76276405
1.25000402
.1.70000401
0.00000
9.76276405
1.25500402
-1.70000401
0.00000
9.76276405
1.18000402
-1.70000401
0.00000
9.76276405
1.17000402
-1.80000401
0.00000
9.76276405
1.21000402
-2.00000401
0.00000
9.76276405
1.22000402
-2.00000401
0.00000
4.80000401
5.00000400
1.00000401
0.00000
4.80000401
3.60000400
1.00000+01
0.00000
2.00000401
3.90000+00
0.00000
0.00000
2.00000401
3.60000400
0.00000
0.00000
2.00000401
4.10000400
>1.50000401
0.00000
2.000004Q1
4.20000400
-1.50000401
0.00000
2.00000+01
3.70000400
-1.50000401
0.00000
2.00000401
3.50000400
-1.50000401
0.00000
2.00000401
3.80000400
0.00000
0.00000
2.00000+01
3.90000+00
0.00000
0.00000
2.00000+00
0.00000
2.85891+04
0.00000
2.00000+00
0.00000
2.85891+04
0.00000
1.00000400
0.00000
2.76781404
3.11000400
1.00000400
0.00000
2.76548+04
0.00000
1.00000+00
0.00000
2.76548+04
0.00000
1.00000400
0.00000
2.76548+04
0.00000
1.00000+00
0.00000
2.76548+04
0.00000
1.00000+00
0.00000
2.76548+04
0.00000
1.00000+00
0.00000
2.76548+04
0.00000
1.00000400
0.00000
2.76548+04
0.00000
0.00000
1.28600+01
2.00000+00
0.00000
0.00000
1.28600+01
2.00000+00
0.00000
0.00000
3.18600+01
1.00000+00
0.00000
0.00000
3.15500401
3.00000400
0.00000
0.00000
3.15500401
3.00000400
0.00000
0.00000
3.15500401
3.00000400
0.00000
0.00000
3.15500401
3.00000400
0.00000
0.00000
3.15500401
3.00000400
0.00000
0.00000
3.15500401
1.00000400
0.00000
0.00000
3.15500401
3.00000400
0.00000

-------
                     TABLE C-l.   (Continued)
TANGENTIAL COAL FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
2
3
£ *
i
2
3
it
1
2
3
4
1
2
3
u
1
2
3
4
1
2
3
5
5
5
5
6
6
6
6
6
6
6
6
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
1
1
1
1
1
1
1
1
1
1
1
1
1
I
t
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
51
51
51
51
52
52
52
52
53
53
53
53
54
54
54
54
55
55
55
55
56
56
56
56
57
57
57
57
58
58
58
58
59
59
59
59
60
60
60
1.00000+00
0.00000
1.10000+02
2.45000+02
1.33000+00
0.00000
1.44000+02
5.44000+02
1.33000+00
0.00000
1.42000+02
5.15000+02
8.00000-01
1.88062+00
1.37800+02
6.15400+02
8.00000-01
1.88062+00
1.30100+02
5.74300+02
1.20000+00
1.88062+00
1.24800+02
4.56900+02
9.00000-01
1.88062+00
1.16400+02
4.08000+02
1.00000+00
1.88062+00
1.50000+02
6.29100+02
1.30000+00
1.88062+00
1.26400+02
4.06*00+02
1.20000+00
1.PK062+00
5.7340(1 + 0?
1.32894+02
0.00000
0.00000
0.00000
9.81180+01
0.00000
0.00000
0.00000
1.02258+0?
0.00000
0.00000
0.00000
1.39311+02
1.44780+00
0.00000
3.20600+02
1.38172+02
1.44780+00
0.00000
3.39400+02
1.39311+02
1.44780+00
0.00000
3.32600+02
1.37758+02
1.44780+00
0.00000
0.00000
9.45266+01
1.1*4780 + 00
0.00000
2.79400+02
9.38020+01
1.44780+00
0.00000
2.02300+n?
7.51203+P1
1.44780+00
0.00000
4.06300+02
1.33881+02
9.17000+01
0.00000
0.00000
1.55111+02
5.24000+01
0.00000
0.00000
1.61641+02
5.46000+01
0.00000
0.00000
2.37509+02
1.11200+02
0.00000
0.00000
2.35585+02
1.10300+02
0.00000
0.00000
2.37509+02
1.11200+02
0.00000
0.00000
2.34954+0?
1.10000+02
0.00000
0.00000
1.61231+02
7.54800+01
0.00000
0.00000
1.59969+02
7.49000+01
0.00000
0.00000
1.28108+0?
5.99800+01
o.ooono
0.00000
9.76276+05
1.21000+02
-2.00000+01
0.00000
1.53151+06
1.44000+02
0.00000
0.00000
1.53151+06
1.42000+02
0.00000
0.00000
1.13098+06
1.37800+02
1.50000+01
2.31000+01
1.13098+06
1.30100+02
1.30000+01
2.14000+01
1.13098+06
1.24800+02
1.10000+01
0.00000
1.13098+06
1 .16400+02
1 .40000+01
0.00000
1.13098+06
1.50000+02
6.00000+00
1.46000+01
1.13098+06
1.26400+02
6.00000+00
1.29000+01
1.13098+06
1.46600+02
1 .30000+01
1.37000+01
2.00000+01
3.80000+00
0.00000
0.00000
3.20000+01
6.50000+00
0.00000
0.00000
3.20000+01
6.3QOOO+00
0.00000
0.00000
2.00000+01
6.20000+00
0.00000
0.00000
2.00000+01
5.30000+00
0.00000
0.00000
2.00000+01
4.60000+00
0.00000
0.00000
2.00000+01
3.40000+00
0.00000
0.00000
1.60000+01
7.10000+00
0.00000
0.00000
1.6QOOO+01
4.60000+00
0.00000
0.00000
1.60000+01
6.90000+00
0.00000
0.00000
1.00000+00
0.00000
2.76594+04
0.00000
2.00000+00
0.00000
2.98240+04
0.00000
2.00000+00
0.00000
2.98240+04
0.00000
1.00000+00
0.00000
2.57745+01*
0.00000
1.00000+00
0.00000
2.85705+04
0.00000
1.00000+00
0.00000
2.79414*04
0.00000
1.00000+00
0.00000
2.51920+04
0.00000
1.00000+00
0.00000
2.82233+04
0.00000
1.00000+00
0.00000
2.82909+04
0.00000
1.00000+00
0.00000
2.88687+04
0.00000
0.00000
3.15700+01
3.00000+00
0.00000
0.00000
9.14000+00
1.00000+00
0.00000
0.00000
9.14000+00
1.00000+00
o.ooouo
0.00000
8.10000+00
1.00000+00
0.00000
0.00000
7.70000+00
1.00000+00
0.00000
0.00000
7.30000+00
1.00000+00
0.00000
0.00000
8.40000+00
1.00000+00
0.00000
0.00000
8.80000+00
1.00000+00
0.00000
0.00000
9.00000+00
1.00000+00
0.00000
0.00000
7.00000+00
1.00000+00
0.00000

-------
       TABLE C-l.   (Continued)
COAL FIRED BOILEHS
1
2
3
i*
1
2
3
4
1
2
3
i»
1
2
3
if
1
0 2
1, 3
0 «•
1
?
3
<4
1
2
3
4
1
2
3
4
1
2
3
1
1
2
3
4
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
1
1
1
1
1
1
1
1
1
1
1
1
1
t
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
i
i
3
3
3
3
6
3
3
3
3
3
6
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
6
3
3
3
3
3
61
tl
fal
61
62
62
62
62
63
63
63
63
64
64
64
64
65
65
65
65
66
66
66
66
67
67
67
67
66
06
68
68
69
69
69
69
70
70
70
70
1 .30000+00
I.«fl06i> + 00
I .31100 + 02
4.91100+02
1.30000+00
l.flP062+00
1.27900+02
4.02900+02
1.^0000+00
1.HP062+00
1.24300+02
3.75400+02
1.30000+00
i.8tfo62+oo
9.97000+01
2.65700+02
1.30000+00
1.S8062+00
9.73000+01
2.28000+02
1.30000+00
1.6*062+00
1.20200+02
4.39700+02
1.20000+00
1.R6062+00
i.ii£.on+n2
3. 96000+02
l.?0000+00
1.H6062+00
1.07100+02
3.68600+02
1.30000+00
1.8*062+00
1.05400+02
3.57400+02
1. 50000+00
1.4*062+00
9.92000+01
3. 13700+02
7.43751+01
1 .44760 + 00
0.00000
3.11100+02
7.54P25+01
1.44780+00
0.00000
3.84000+02
7.47«»77+01
1.44780+00
O.OUOOO
3.82300+02
7.95067+01
1.44780+00
0.00000
3.80600+02
7.98709+01
1.44780+00
0.00000
3.45400+02
1.36?06+02
1. 44780+00
0.00000
3.87400+02
1.36?06+02
1.447BO+00
0.00000
3.17100+02
1.35585+02
1.4476(1 + 00
0.00000
3.44600+02
1.3s5b5+02
1.447PO+00
O.OOPOO
3.56600+02
1.35585+02
1.1*4780 + 0(1
o.oonoo
3.40300+02
1.26846+02
5.93900+01
0.00000
0.00000
1.28739+02
6.02700+01
0.00000
O.OOOnt)
1.27477+0?
5.96900+01
0.00000
0.00000
1.35616+02
6.34900+01
0.00000
0.00000
1.36215+0?
6. 37800+01
0.00000
0.00000
2.32399+02
1.08800+02
0.00000
O.OOUOO
2.32399+02
1.08800+02
0.00000
0.00000
2.31326+02
1.08300+02
0.00000
0.00000
2.3132fe+02
1.08300+02
o.ooonn
0.00000
2.31326+02
1.08300+02
o.ooonn
0.00000
1. 13098+06
1.31100+02
1 .10000+01
1.37000+01
1.13098+06
1.27900+02
1.30000+01
0.00000
1.13096+06
1.24300+02
1.20000+01
1.28000+0i
1.13098+06
1.23900+02
0.00000
1.28000+01
1.13098+06
1.22800+02
0.00000
5.40000+01
1.13098+06
1.28200+02
-1.00000+01
1.26000+01
1.13098+06
1.26200+02
-1. 00000+01
1.28000+01
1.13096+06
1.25500+02
-1.40000+01
1.28000+01
1.13098+06
1.25500+02
•1 .20000+01
1.28000+01
1. 13098+06
1.22000+02
-2.00000+01
1.30000+01
1.60000+01
5.20000+00
0.00000
0.00000
1.60000+01
4.80000+00
0.00000
0.00000
1.60000+01
4.30000+00
0.00000
0.00000
1.60000+01
4.10000+00
3.00000+01
0.00000
1.60000+01
4.00000+00
3.00000+01
0.00000
2.00000+01
4.70000+00
0.00000
0.00000
2.00000+01
4.50000+00
0.00000
0.00000
2.00000+01
4.40000+00
0.00000
0.00000
2.00000+01
4.30000+00
0.00000
0.00000
2.00000+01
3.90000+00
0.00000
0.00000
1.00000+00
0.00000
2.89200+04
0.00000
1.00000+00
0.00000
2.86870+04
0.00000
1.00000+00
0.00000
2.62676+04
0.00000
1.00000+00
0.00000
2. 83188+04
0.00000
1.00000+00
0.00000
2.84773+04
0.00000
1.00000+00
0.00000
2.71725+04
0.00000
1.00000+00
0.00000
2.79414+Q4
0.00000
1.00000+00
0.00000
2.68929+04
0.00000
1.00000+00
0.00000
2.76385+04
0.00000
1.00000+00
0.00000
2.76152+04
0.00000
O.UOOOO
6.70000+00
1.00000+00
O.UOOOO
O.UOOOO
6.00000+00
1.00000+00
O.UOOOO
O.UOOOO
9.00000+00
1.00000+00
0.00000
0.00000
7.6QOOO+00
3.00000+00
o.ooouo
0.00000
6.5QOOO+00
3.00000+00
0.00000
0.00000
9.40000+00
3.00000+00
0.00000
0.00000
6.30000+00
3.00000+00
0.00000
0.00000
6.30000+00
3.00000+00
0.00000
0.00000
6.70000+00
3.00000+00
o.ooouo
0.00000
8.10000+00
3.00000+00
0.00000

-------
         TABLE C-l.   (Continued)
COAL FIKEU BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
•*
1
e
3
4
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
8
8
6
8
8
8
8
8
8
8
8
e
8
a
8
8
{,
^
8
e
i
i
i
i
i
j
i
1
1
i
i
i
1
i
i
i
i
i
i
1
i
i
i
i
1
i
1
i
i
i
1
i
,
i
i
i
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
7,
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
71
71
71
71
72
72
72
72
73
73
73
73
74
74
74
74
75
75
75
75
76
76
76
76
77
77
77
77
76
7ft
78
78
79
79
79
79
flu
10
MO
00
l.?0000400
I .88062400
1.07100402
2.91400402
1.30000400
1.88062400
1.06500402
3.11100402
1.30000400
1.8B062400
1.26900402
5.67400402
1.30000400
1.86062400
1.21300402
5.07400402
1.300U0400
1.8P062+00
1.09100402
3.60900402
6.00000-01
1.67640400
1.37800402
5.57100402
7.00000-01
1.67640400
1.14300402
5.36600+02
7.00000-Ql
1 .67^40+00
1.20SOO+02
ta.l 5400+02
7.00000-01
1 ,h7640+GO
1 .31400402
1.13400402
7.00000-01
1.67640+00
1.27f>00 + 02
b.1 9400+02
1.37344+0?
1.44780400
0.00000
3.58300402
7.98709401
1.44780400
0.00000
3.07700402
1.09192402
1.44780400
0.00000
3.73700402
1.09192402
1 .44760400
0.00000
3.47100402
1 .OB054+02
1.44780400
0.00000
3.48000402
1.16024402
1 .44780400
0.00000
9.90900402
I.l3f,43 + 02
1 .44780400
0.00000
1 .02600403
1 .11883402
] .44780400
O.OUOOO
1 .02000403
1.05?59+0?
1. 44700400
0.00000
8.59700402
1.03707402
1 .44780400
0.00000
1 .00370403
2.34323402
1.09700402
4.00000400
0.00000
1.3fe2l540?
6.37800401
4.00000400
0.00000
1.86215+02
8.71900+01
0.00000
0.00000
1.86?15402
8.71900401
0.00000
0.00000
1.84354402
8.63100401
4.00000400
0.00000
2.0971740?
9.19000401
0.00000
0.00000
2.0539540?
9.00000401
0.00000
0.00000
2.Q2178+0?
6.86000+01
0.00000
0.00000
1.90316+0?
8.34000+01
0.00000
o.ooooo
1.87351+02
8.21000+01
0.00000
0.00000
1.13098406
1 .19800402
6.00000400
4.80000401
1.13098406
1.22600402
6.00000400
1.37000401
1.13098406
1.26900402
0.00000
0.00000
1.13098406
1.21300402
0.00000
1.20000401
1 .13098406
1.29300402
7.00000400
1.46000+01
1.50485406
1.17800402
-4.00000+00
1.37000401
1.50485406
1.14300402
-4.00000400
0.00000
1 .50485406
1.20900402
-4.00000400
1.37000401
1.5o485+06
1.31400402
-2.00000400
1.54300401
1.5Q485406
1.2750040?
-4.00000400
1 .45700401
1.60000401
3.60000400
0.00000
0.00000
1.60000401
4.00000400
0.00000
0.00000
2.00000401
4.80000+00
0.00000
0.00000
2.00000401
4.00000400
0.00000
0.00000
1.60000+01
4.90000400
0.00000
0.00000
2.00000401
4.30000400
0.00000
0.00000
2.00000401
3.50000400
0.00000
0.00000
2.00000401
4.30000400
0.00000
0.00000
2.00000401
5.70000400
0.00000
0.00000
2.00000401
5.20000+00
0.00000
0.00000
1.00000+00
0.00000
2.83608+04
0.00000
1.00000+00
0.00000
2.8267&404
0.00000
1.00000400
0.00000
2.77317404
0.00000
1.00000400
0.00000
2.85006404
0.00000
1.00000400
0.00000
2.77084404
0.00000
1.00000400
0.00000
1,97607404
0.00000
1.00000+00
0.00000
1.96000404
0.00000
1.00000400
0.00000
1.90850404
0.00000
1.00000400
0.00000
1.96862404
0.00000
1.00000400
0.00000
1.97724+04
0.00000
0.00000
8. 00000 + 00
2.00000400
0.00000
0.00000
6.30000400
2.00000400
0.00000
0.00000
8.10000+00
1.00000+00
0.00000
0.00000
6.40000400
1.00000400
0.00000
0.00000
6.10000400
2.00000400
0.00000
0.00000
2.5iOOO+Oi
1.00000400
0.00000
0.00000
2.46000+01
1.00000+00
0.00000
0.00000
2.79000+01
1.00000400
0.00000
0.00000
2.44000+01
1.00000400
0.00000
0.00000
2.49000+01
1.00000+00
0.00000

-------
                     TABLE C-l.   (Continued)
TflMGENTIAL COAL FIRCD HOILPRS
1
2
3
4
1
2
3
4
1
2
3
u
1
2
3
4
1
2
0 3
1* "
ro
1
2
3
11
1
2
3
U
1
2
3
U
1
2
?
(4
1
2
j
i*
A
P
6
8
8
A
8
A
A
8
8
A
8
A
e
A
8
8
6
A

8
A
8
8
8
A
A
A
8
A
8
8
A
8
8
8
A
8
8
rt
1
1
1
1
1
1
1
1
1






1
I
1
1
1

1
1
1
1
1
1
1
1
1
1
1
1
1
1






3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
6
3
3
3
3
5
81
81
8i
81
82
82
P2
82
83
83
83
83
Al*
84
84
84
85
85
85
85

86
86
86
86
87
87
87
87
88
88
86
88
89
89
«9
89
90
90
90
90
7.00000-01
1. 67640 + 00
l.?9000+02
5.77700+02
a. 00000-01
1.67640+00
1.41400+02
5. 67400+02
7.00000-01
1.67640+00
1.36200+02
5.59700+02
7.00000-01
1.67640+00
1.26700+02
5.08300+02
9.00000-01
1.67640+00
1.17200+02
«». 59400 + 02

7.00000-01
1.67640+00
9.47000+01
2.79400+02
7.00000-01
1.67640+00
1.15800+02
4.76600+02
7.00000-01
1.67640+00
1.04700+02
3.94300+02
7.00000-01
1.67640+00
9.97000+01
3.30000+02
6.00000-01
1.67<,40 + 00
'i. 900110 + 01
2. 94400+02
1.04432+0?
1 .44780 + 00
0.00000
1.10P30+03
7.05870+01
1.44780+00
0.00000
1.05430+03
7.07940+01
1.44780+00
O.OOOOP
1.18200+03
7.01730+01
1.44780+00
0.00000
1.16740+03
6.92415+01
1.44780+00
0.00000
1.12970+03

6.92415+01
1.44780+00
0.00000
1.07310+03
1.15P99+02
1.44780+00
0.00000
8.82000+02
1.15817+02
1.44780+00
o.noooo
8.26300+0?
1.16024+02
1.44780+00
o.noooo
8.06*00+02
1.15S06+02
1.447PO+00
o.onooo
I .l)6?yO + 03
1.86739+02
8.27000+01
0.00000
0.00000
1.27572+02
5.59000+01
0.00000
o.ooono
1.28013+02
5.61000+01
0.00000
o.ooono
1.26878+02
5.56000+01
0.00000
0.00000
1.25048+02
5.48000+01
0.00000
0.00000

1.25048+0?
5.48000+01
4.00000+00
0.00000
2.06361+02
9.13000+01
4.00000+00
0.00000
2.09276+0?
9.17000+01
0.00000
0.00000
2.09717+02
9.19000+01
0.00000
0.00000
2.0880?+0?
9.15000+01
0.00000
0.00000
1.50485+06
1.29000+02
-4.00000+00
1.62900+01
1.50485+06
1.41400+02
9.00000+00
6.00000+00
1.50485+06
1.36200+02
l.OOOOO+Ol
5.10000+00
1.50485+06
1.26700+02
1.00000+01
4.30000+00
1.5Q485+06
1.17200+02
1.00000+01
4.30000+00

1.50485+06
1.19700+02
1.00000+01
4.30000+00
1.50465+06
1.18400+02
-4.00000+00
0.00000
1.50485+06
1.26200+02
2.00000+00
1.29000+01
1.50485+06
1.19100+02
1.00000+00
6.51000+01
1.50485+06
1.15100+02
1 .00000+00
O.OOOOU
2.00000+01
5.50000+00
0.00000
0.00000
1.60000+01
6.50000+00
0.00000
0.00000
1.60000+01
6.00000+00
0.00000
0.00000
1.60000+01
4.90000+00
0.00000
0.00000
1.60000+01
3.70000+00
0.00000
0.00000

1.60000+01
3.70000+00
0.00000
0.00000
2.00000+01
4.30000+00
0.00000
0.00000
2.00000+01
4.70000+00
3.00000+01
0.00000
2.00000+01
3. 50000 + 00
1.00000+01
0.00000
2.00000+01
3.50000+00
0.00000
0.00000
1.00000+00
0.00000
1.97724+04
0.00000
1.00000+00
0.00000
2.05320+04
0.00000
1.00000+00
0.00000
1.97607+04
0.00000
1.00000+00
0.00000
1.98796+04
0.00000
1.00000+00
0.00000
2.0t597+0«>
0.00000

1.00000+00
0.00000
2.02733+0*
0.00000
1.00000+00
0.00000
1.93646+04
0.00000
1.00000+00
0.00000
1.94369+04
0.00000
1.00000+00
0.00000
2.01592+04
0.00000
1.00000+00
0.00000
2.00427+0*
0.00000
0.00000
2.49000+01
1.00000+00
O.OQOOO
0.00000
2."»7000 + 01
1.00000+00
o.oooon
0.00000
2.51000+01
1.00000+00
o.ooooo
0.00000
2.55000+01
1.00000+00
0.00000
0.00000
2.45000+01
1.00000+00
0.00000

0.00000
2.54000+01
2.00000+00
o.ooooo
0.00000
2.56000+01
2.00000+00
0.00000
0.00000
2.57000+01
3.00000+00
0.00000
0.00000
2.51000+01
3.00000+00
o.ooooo
0.00000
2.49000+01
3.00000+00
o.ooono

-------
                     TABLE C-l.   (Continued)
TftNGEMTjftL COflL FIRED BOILERS
1 8
2 8
3 8
4 ft
1 8
2 8
3 8
4 8
1 A
2 8
3 8
4 8
1 8
2 8
3 8
4 A
1 8
2 8
3 A
4 8
1 8
2 8
3 8
4 8
1 13
2 13
3 13
4 13
1 13
2 13
3 13
4 13
1 13
2 13
3 13
4 13
1 13
? 13
3 1}
1
1
t
1
1
1
1
1
1
1
1
1
1
t
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
91
91
91
91
92
92
92
92
93
93
93
93
94
94
94
94
95
95
95
95
96
96
96
96
97
97
97
97
98
98
9fl
96
99
99
99
99
100
100
100
100
6.00000-01
1.67640+00
1.06000+02
3.33400+02
a. 00000-01
1.67640+00
1.28200+02
5.09100+02
8.00000-01
1.67640+00
1.18800+02
"». 72300 + 02
a. 00000-01
1.67640+00
1.11500+02
4.15700+02
6.00000-01
1.67640+00
1.06100+02
2.92300+02
7.00000-01
1.67640+00
1.07000+02
1.59000+00
1.49870+00
1.30000+02
3.65000+02
1.59000+00
1.49870+00
1.17000+02
1.96000+02
1.59000+00
1.49870+00
1.16?00+02
2.94000+02
1.59000+00
1.49P70+00
1 ,0?000+02
2. 65^00+02
1.16«S41 + 02
1.44780+00
0.00000
fl. 03100 + 02
1.04P45+0?
1.44780+00
o.ooooo
1.08600+03
1.02^72+02
1.44780+00
0.00000
1 .15030+03
1.
1.
0.
1.
6.
1.
0.
8.
o!
8.
1.
2.
0.
0.
1.
2.
0.
0.
1.
0.
0.
I .
?.
0.
0.
02361+02
44780+00
00000
13910+03
92415+01
44780+00
00000
22000+02
00000
86300+02
37655+02
43«40+00
00000
00000
33411+0?
43840+00
00000
ooono
37655+02
00000
ooooo
43*40+00
(10001
OOOOO
2.10632+02
9.23000+01
0.00000
0.00000
1.89402+02
8.30000+01
0.00000
0.00000
1.85521+02
8.13000+01
0.00000
0.00000
1.85080+02
8.11000+01
0.00000
0.00000
1.25048+0?
5.48000+01
0.00000
0.00000
1.23216+0?
5.40000+01
0.00000
0.00000
7.79184+01
1.00000+02
0.00000
0.00000
7.54894+01
9.69000+01
0.00000
o.ooono
7.79184+ot
1.00000+02
0.00000
0.00000
7.67512+01
9.85000+01
O.OOOPO
o.ooonn
1.50485+06
1.26900+02
-5.00000+00
1.37000+01
1.50485+06
1.36800+02
2.00000+00
0.00000
1.50485+06
1.35800+02
1.00000+00
0.00000
1.50485+06
1.30000+02
3.00000+00
0.00000
1.50485+06
1.32500+02
7.00000+00
3.40000+00
1.50485+06
1.34200+02
1.20000+01
4.30000+00
3.23472+05
1.30000+02
-1.70000+01
0.00000
3.23472+05
1.17000+02
-1.70000+01
O.OPOOO
3.23472+05
1.29400+02
-1.70000+01
0.00000
3.23472+05
1.27500+02
-1 .70000+01
0.00000
2.00000+01
4.60000+00
0.00000
0.00000
2.00000+01
5.80000+00
0.00000
0.00000
2.00000+01
5.80000+00
0.00000
0.00000
2.00000+01
5.00000+00
0.00000
0.00000
1.60000+01
5.50000+00
1. 00000 + 01
0.00000
1.60000+01
5.40000+00
1.00000+01
0.00000
1.60000+01
4.92000+00
0.00000
0.00000
1.60000+01
3.14000+00
0.00000
0.00000
1.60000+01
4.78000+00
0.00000
0.00000
1.60000+01
4.69000+00
0.00000
0.00000
1.00000+00
0.00000
2.05320+04
0.00000
1.00000+00
0.00000
2.00427+0*
0.00000
1.00000+00
0.00000
2.03223+04
0.00000
1.00000+00
0.00000
2.05529+04
0.00000
1.00000+00
0.00000
2.05529+04
0.00000
1.00000+00
0.00000
2.03223+04
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
0.00000
2.42000+01
3.00000+00
0.00000
0.00000
2.40000+01
3.0QOOO+00
0.00000
0.00000
2.39000+01
3.00000+00
0.00000
0.00000
2.40000+01
3.00000+00
0.00000
0.00000
2.3lOOO+Oi
3.00000+00
0.00000
0.00000
2.41000+01
3.00000+00
o.ooooo
0.00000
5.51000+00
1.00000+00
0.00000
0.00000
5.51000+00
1.00000+00
0.00000
0.00000
5.51000+00
3.00000+00
0.00000
o.ooooo
5.51000+00
3.00000+00
o.ooooo

-------
         TABLE C-l.   (Continued)
COftL FIRED BOILERS
1
3
4
1
2
3
1
2
3
1
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
3
1
1
2
3
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
13
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
I
1
1
1
1
1
t
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
S
3
3
3
3
3
3
101
101
101
101
102
102
102
102
103
103
103
103
104
104
104
105
105
105
105
106
106
106
106
107
107
107
107
108
108
108
108
109
109
109
109
110
110
no
11"
1.59000+00
1.49870+00
1.06?00+02
1.82000+02
1.59000+00
1.49fl70+00
9.60000+01
1.69000+02
1.56000+00
1.49870+00
1.51000+02
4.52000+02
1.56000+00
1.49870+00
1.35700+02
4.11000+02
1.56000+00
1.49670+00
1.16500+02
2.53000+02
1.56000+00
1.49670+00
1.12000+02
3.30000+02
1.56000+00
1.49670+00
9.60000+01
2.12000+02
1.56000+00
1.49P70+00
1. 90000+01
2.72nOO+02
1.56000+00
1.49*70+00
8.41000+01
1.9POOO+02
1.5*000+00
1.49*70+00
1.70000+02
2.84000+02
1. 36*17 + 02
0.00000
O.OOOPO
1.36517+0?
2.43pi»o + 00
0.00000
0.00000
1.00602+02
2.43P40+00
0.00000
0.00000
9.84285+01
2.43fl1o+00
0.00000
0.00000
9.84285+01
2.43640+00
0.00000
0.00000
9.95670+01
2.43P40+00
0.00000
0.00000
1.00602+02
2.43P10+00
0.00000
0.00000
2.43BUO+00
0.00000
o.oonoo
1.00602+0?
o.ooooo
o.nonoo
5.71320+01
2.43P40+00
0.00000
o.noono
7.72875+01
9.92000+01
0.00000
0.00000
7.72875+01
9.92000+01
0.00000
0.00000
5.69719+01
7.31000+01
0.00000
0.00000
5.57101+01
7.15000+01
0.00000
0.00000
5.57101+01
7.15000+Ql
0.00000
0.00000
5.63410+01
7.23000+01
4.00000+00
0.00000
5.69719+01
7.31000+01
4.00000+00
0.00000
5.57101+01
7.15000+01
4.0000H+00
0.00000
5.69719+01
7.31000+01
4.00000+00
0.00000
3.23346+01
4.15000+01
0.00000
0.00000
3.23472+05
1.16100+02
-1.70000+01
0.00000
3.23472+05
1.20000+02
-1.70000+01
0.00000
3.23472+05
1.51000+02
-2.00000+00
0.00000
3.23472+05
1.50800+02
-2.00000+00
0.00000
3.23472+05
1.29400+02
-2.00000+00
0.00000
3.23472+05
1.49300+02
-2.00000+00
0.00000
3.23472+05
1.26000+02
-2.00000+00
0.00000
3.23472+05
1.47000+02
-2.00000+00
0.00000
3.23472+05
1.24500+02
-2.00000+00
0.00000
3.23472+05
1.70000+02
9.00000+00
0.00000
1.60000+01
3.54000+00
0.00000
0.00000
1.60000+01
3.62000+00
0.00000
0.00000
1.60000+01
7.29000+00
0.00000
0.00000
1.60000+01
7.12000+00
0.00000
0.00000
1.60000+01
4.82000+00
0.00000
0.00000
1.20000+01
7.11000+00
0.00000
0.00000
1.20000+01
4.59000+00
0.00000
0.00000
1.20000+01
6.81000+00
0.00000
0.00000
1.20000+01
4.31000+00
0.00000
0.00000
8.00000+00
8.77000+00
0.00000
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
1.00000+00
0.00000
3.01735+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.95561+04
0.00000
1.00000+00
0.00000
2.87242+04
0.00000
0.00000
5.51000+00
3.00000+00
0.00000
0.00000
5.51000+00
3.00000+00
0.00000
0.00000
6.96000+00
l.OOOUQ+00
0.00000
0.00000
6.96000+00
3.00000+00
0.00000
0.00000
6.96000+00
3.00000+00
0.00000
0.00000
6.96000+00
2.00000+00
0.00000
0.00000
6.96000+00
2.00000+00
0.00000
0.00000
6.96000+00
4.00000+00
0.00000
0.00000
6.96000+00
4.00000+00
0.00000
0.00000
1.23000+01
1.00000+00
0.00000

-------
                 TABLE C-l.  (Continued)
TANGENTIAL COAL FIRED BOILERS
1 13
2 13
3 13
« 13
1 13
2 13
3 13
1 13
1 13
2 13
3 13
1 13
1 10
2 10
3 10
4 10
1 10
2 10
3 10
o ii m
*" 1 10
2 10
3 10
1 10
l in
2 10
3 10
1 10
1 10
2 10
3 in
i in
1 10
2 10
3 lo
«4 10
i in
? in
3 lo
110
1
1
1
1
1
1
1
1
1
1
1
I
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
}
1
1
1
1
1
1
]
1
1
1
3 111
3 111
3 111
3 111
3 112
3 112
3 112
3 112
3 113
3 113
3 113
3 113
3 111
3 111
3 11"*
3 111
3 115
3 115
3 115
3 115
3 116
3 116
3 116
3 116
3 117
3 117
3 117
3 117
3 118
3 118
3 118
3 llfl
3 119
3 119
3 119
3 119
3 1?0
3 120
3 1?0
3 120
1. 55000 + 00
1.19A70+OC
1.18000+02
2.51000+02
1.15000+00
1.19fl7o+00
1.27000+02
3. 11000+02
1.15000+00
1.19870+00
1.15200+02
2.13000+02
1.36000+00
1.52100+00
1.17000+02
3.96000+02
1.32000+00
1.52100+00
1.13000+02
3.70000+02
1.52000+00
1.52100+00
1. 00000+02
3.31000+02
1.12000+00
1.52100+00
1. 10000+01
2.88000+02
1.39000+00
1.52100+00
9.20000+01
?el7noo+o2
1.11000+00
1.52100+00
8.70000+01
2.58000+02
1.51000+00
i ."iPion + oo
1.15000+02
i ,?nnnn+o2
5.71320+01
2.13^10+00
o.oonoo
o.ooooo
1 .10663+02
2.13P10+00
0.00000
0.00000
1.33111+02
2,15*10+00
0.00000
0.00000
1.29061+02
0.00000
0.00000
0.00000
1 .21717+02
0.00000
0.00000
0.00000
1.29996+02
0.00000
0.00000
0.00000
1.26f5n+02
0.00000
0.00000
0.00000
1.21717+0?
0.00000
0.00000
o.noono
1.23372+02
o.oonoo
o.oooon
O.OQOOO
1.13?11+02
0.00000
0.00000
0. 00000
3.23316+01
1.15000+01
0.00000
0.00000
7.97165*01
1.02300+02
0.00000
0.00000
7.51891+01
9.69000+01
0.00000
0.00000
3.89971+02
8.37000+01
0.00000
0.00000
3.76910+02
8.09000+01
0.00000
0.00000
3.92717+02
8.13000+01
1.00000+00
0.00000
3.86551+02
8.31000+01
1.00000+00
0.00000
3.76910+02
8.09000+01
1.00000+00
0.00000
3.72715+02
fl.OOOOO+Ol
1.00000+00
0.00000
1.32810+0?
9.29000+01
O.OOOOO
0.00000
3.23172+05
1.18000+02
9.00000+00
0.00000
3.23172+05
1.27000+02
1.00000+00
0.00000
3.23172+05
1.28000+02
0.00000
0.00000
9.73639+05
1.17000+02
-8.00000+00
3.60000+01
9.73&39+05
1.15000+02
-A. 00000+00
1.70000+01
9.73639+05
1.11500+02
0.00000
3.30000+01
9.73639+05
1.30100+02
0.00000
5.00000+01
9.73639+05
1.28100+02
-8.00000+00
1.80000+01
9.73639+05
1.17700+02
-8.00000+00
1.77000+02
9.73639+05
1.15000+02
0.00000
2.00000+01
8.00000+00
6.93000+00
0.00000
0.00000
1.60000+01
1.26000+00
0.00000
0.00000
1.60000+01
1.68000+00
0.00000
0.00000
1.60000+01
5.00000+00
0.00000
0.00000
1.60000+01
1.50000+00
0.00000
0.00000
1.60000+01
6.30000+00
0.00000
0.00000
1.60000+01
1.90000+00
0.00000
0.00000
1.60000+01
1.60000+00
0.00000
0.00000
1.60000+01
3.30000+00
0.00000
0.00000
2.00000+01
1.70000+00
0.00000
0.00000
1.00000+00
0.00000
2.87212+01
0.00000
1.00000+00
0.00000
2. 95327+01
0.00000
1.00000+00
0.00000
2.95327+0*
0.00000
1.00000+00
0.00000
3. 21336+01
0.00000
1.00000+00
0.00000
3.21219+01
0.00000
1.00000+00
0.00000
3.13611+01
0.00000
1.00000+00
0.00000
3.18558+01
0.00000
1.00000+00
0.00000
3.03319+01
0.00000
1.00000+00
0.00000
3.17206+01
0.00000
1.00000+00
0.00000
2.96959+01
0.00000
0.00000
1.23000+01
i.ooouo+oo
0.00000
0.00000
1.01500+01
1.00000+00
0.00000
0.00000
1.01500+01
3.00000+00
0.00000
0.00000
9.31000+00
1. 00000+00
o.ooooo
0.00000
a. 62000+00
i.ooouo+oo
0.00000
0.00000
1.05800+01
2.00000+00
o.ooooo
0.00000
7.95000+00
2.00000+00
0.00000
0.00000
8.16000+00
2.00000+00
0.00000
0.00000
9.15000+00
2.00000+00
0.00000
0.00000
8.15000+00
l.ooooo+oo
o.ooono

-------
                  TABLE C-l.   (Continued)
TANGTNTIAL COAL FiRto BOILERS
1
2
3
4
1
2
u
1
2
3
4
1
2
3
4
1
2
3
2 *
2
3
4
1
2
3
1
2
3
U
1
2
3
u
1
2
3
4
10
10
10
10
10
lo
10
10
10
10
10
10
in
10
in
10
10
10
10
10
10
10
10
10
in
10
in
lo
ll
ll
ll
11
11
11
11
11
11
ll
ll
11
i
1
l
l
1
l
t

1
1
l
1
I
1
l
l
l
l
1
l
l
l
i
l
l
l
l
l
l
i
t
l
l
l
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
121
121
121
121
122
122
122
122
123
123
123
123
124
124
124
125
125
125
125
126
126
126
126
127
127
127
127
128
128
128
128
129
129
129
130
130
130
130
1. 50000 + 00
1.52400+00
1.07000+02
3.36000+02
1.46000+00
1.52400+00
1.15000+02
4.15000+02
1.46000+00
1.52400+00
1.12000+02
3.98000+02
1.42000+00
1.52400+00
1.00000+02
3.38000+02
1.42000+00
1.52400+00
9.70000+01
2.61000+02
1.42000+00
1.52400+00
8.30000+01
1.89000+02
1.42000+00
1.52400+00
8.40000+01
2.00000+02
1.57000+00
0.00000
1.25000+02
5.68000+02
1.47000+00
0.00000
l.2lonn+o2
4.S4QOO+02
1.57000+00
n.ooono
1.09000+02
5.79000+02
1.44486+02
0.00000
0.00000
0.00000
1 ,53?83+02
0.00000
0.00000
0.00000
1.53283+02
0.00000
0.00000
0.00000
8.18685+01
0.00000
0.00000
0.00000
8.11440+01
0.00000
0.00000
0.00000
8.18685+01
0.00000
0.00000
0.00000
7.92810+01
0.00000
O.OOPOO
0.00000
1.385B7+0?
o.oooon
0.00000
0.00000
1.33722+02
0.00000
0.00000
0.00000
1.33722+02
o.ononn
o.onroo
o.ooroo
4.36532+02
9.37000+01
0.00000
0.00000
4.63094+02
9.94000+01
0.00000
0.00000
H. 63094+02
9.94000+01
O.OOOPO
o.oooon
2.47383+02
5.31000+01
4.00000+00
0.00000
2.45049+02
5.26000+01
4.00000+00
0.00000
2.47383+02
5.31000+01
4.00000+00
0.00000
2.39465+02
5.14000+01
4.00000+00
0.00000
4.52242+02
1.03000+02
0.00000
0.00000
4.36406+02
9.94000+01
0.00000
0.00000
4.36406+02
9.94000+01
o.ooono
O.OOOPO
9.73639+05
1.07000+02
0.00000
2.27000+02
9.73639+05
1.15000+02
0.00000
2.40000+01
9.73639+05
1.12000+02
0.00000
1.15000+02
9.73639+05
1.55400+02
0.00000
2.20000+01
9.73639+05
1.48500+02
0.00000
3.00000+01
9.73639+05
1.20400+02
0.00000
2.81000+02
9.73639+05
1.22000+02
0.00000
2.11000+02
8.95115+05
1.25000+02
0.00000
2.40000+01
6.95115+05
1.21000+02
0.00000
3.00000+01
8.95115+05
1.09000+02
0.00000
2.25000+02
2.00000+01
2.40000+00
0.00000
0.00000
2.00000+01
4.40000+00
0.00000
0.00000
2.00000+01
3.90000+00
0.00000
0.00000
1.20000+01
7.70000+00
0.00000
0.00000
1.20000+01
7.10000+00
0.00000
0.00000
1.20000+01
3.70000+00
0.00000
0.00000
1.20000+01
3.90000+00
0.00000
0.00000
2.00000+01
4.40000+00
0.00000
0.00000
2.00000+01
3.90000+00
0.00000
0.00000
2.00000+01
2.10000+00
0.00000
0.00000
1.00000+00
0.00000
2.96050+04
0.00000
1.00000+00
0.00000
3.09610+04
0.00000
1.00000+00
0.00000
3.10496+04
0.00000
1.00000+00
0.00000
3.09541+04
0.00000
1.00000+00
0.00000
3.09541+04
0.00000
1.00000+00
0.00000
3.09541+04
0.00000
1.00000+00
0.00000
3.09541+04
0.00000
1.00000+00
0.00000
2.70676+04
1.48000+00
1.00000+00
0.00000
2.60485+04
0.00000
1.00000+00
0.00000
2.79717+04
0.00000
0.00000
9.03000+00
1.00000+00
0.00000
0.00000
6.32000+00
1.00000+00
o.ooooo
o.ooooo
6.73000+00
1.00000+00
0.00000
o.ooooo
3.44000+00
2.00000+00
0.00000
o.ooooo
3.44000+00
2.00000+00
0.00000
0.00000
3.44000+00
2.00000+00
0.00000
0.00000
3.44000+00
2.00000+00
0.00000
0.00000
1.39900+01
1.00000+00
0.00000
0.00000
1.22300+01
1.00000+00
0.00000
o.ooooo
1.09700+01
1.00000+00
0.00000

-------
                     TABLE C-l.  (Continued)
TaMGENTlAL COAL FIRED BOILERS
1 11
2 11
3 11
1 11
1 11
2 11
3 11
1 11
1 11
2 11
3 11
1 11
1 11
2 11
3 11
1 11
1 11
2 11
3 11
<« 11
1 11
2 11
3 11
1 11
1 11
2 11
3 11
1 11
I 12
2 12
3 12
1 12
1 12
2 12
2 12
1 12
1 11
2 1<«
3 11
i* la
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
I
1
1
1
1
1
1
1
1
1
1
1
1

1
1
1
1
1
3 131
3 131
3 131
3 131
3 132
3 132
3 132
3 132
3 133
3 133
3 133
3 133
3 131
3 131
3 131
3 131
3 135
3 ]35
3 135
3 135
3 136
3 136
3 136
3 136
3 137
3 137
3 137
3 137
3 138
3 138
3 138
3 138
3 139
3 139
3 1?9
3 139
3 i"*0
3 110
3 1 tQ
1.58000+00
o.oooon
8.80000+01
2.36000+02
1.58000+00
0.00000
1.27000+02
5.37000+02
1.58000+00
n.ooooo
9.90000+01
3.01000+02
1.58000+00
0.00000
9.10000+01
2.65000+02
1.58000+00
0.00000
l.lftOOO+02
1.58000+02
1.58000+00
0.00000
7.80000+01
1.69000+02
1.58000+00
0.00000
7.10000+01
1.82000+02
7.50000-01
0.00000
1.21000+02
1.31000+02
7.50000-01
O.OOOOO
1.17000+02
3.86000+02
1.13000+00
o.ooono
1.17100+02
'4. innnn + n2
1.25515+02
0.00000
0.00000
o.ooono
1.01132+02
0.00000
0.00000
0,00000
1 .05981+0?
0.00000
0.00000
0.00000
1.08051+02
0.00000
0.00000
0.00000
8.11110+01
0.00000
0.00000
o.oonoo
8.07300+01
o.ooono
0.00000
0.00000
8. 15580+01
0.00000
0.00000
0.00000
1.15092+02
n.nonno
0.00000
0.00000
1.13A50+02
0.00000
0.00000
O.OOOnn
1. 59390+02
o.oooon
0.00001
o.onnno
1.09621+02
9.33000+01
1.00000+00
0.00000
3.10696+02
7.76000+01
0.00000
0.00000
3.15961+02
7.88000+01
1.00000+00
0.00000
3.52557+02
8.03000+01
1.00000+00
0.00000
2.61765+02
6.03000+01
0.00000
0.00000
6.00000+01
1.00000+00
n.ooooo
?. 66058+02
6.06000+01
1.00000+00
0.00000
2.69718+0?
9.00000+01
0.00000
0.00000
2.67036+0?
0. 91000+01
0.00000
0.00000
2.096->"* + 02
1 . 00000+02
O.ooono
o.noono
8.95115+05
1.11100+02
0.00000
1.10000+01
8.95115+05
1.27000+02
0.00000
3.00000+01
8.95115+05
1.29100+02
0.00000
1.10000+01
8.95115+05
1.19900+02
0.00000
6.20000+01
8.95115+05
1.18000+02
0.00000
2.00000+01
8.95115+05
1.26200+02
0.00000
2.70000+01
8.95115+05
1.17100+02
0.00000
5.60000+Qi
1.01319+06
1.21000+02
0.00000
1.90000+01
1.01319+06
1.17000+02
0.00000
5.60000+01
6.51269+05
1.17000+02
0.00000
6.10000+01
1.60000+01
2.70000+00
0.00000
0.00000
2.00000+01
1.90000+00
0.00000
0.00000
1.60000+01
1.90000+00
0.00000
0.00000
1.60000+01
3.60000+00
0.00000
0.00000
1.60000+01
1.20000+00
0.00000
0.00000
1.20000+01
1.50000+00
0.00000
0.00000
1.20000+01
3.20000+00
0.00000
0.00000
2.00000+01
1.20000+00
0.00000
0.00000
2.00000+01
3.20000+00
0.00000
0.00000
1.80000+01
3.10000+00
0.00000
n.ooooo
1.00000+00
0.00000
2.77759+01
0.00000
1.00000+00
0.00000
2.75220+01
0.00000
1.00000+00
0.00000
2.75220+01
0.00000
1.00000+00
0.00000
2.75220+01
0.00000
1,00000+00
0.00000
2.75220+01
0.00000
1.00000+00
0.00000
2.75220+01
0.00000
1.00000+00
0.00000
2.75220+01
0.00000
1.00000+00
0.00000
2.32161+01
0.00000
1.00000+00
0.00000
2.36215+01
0.00000
2.00000+00
0.00000
3.08818+01
0.00000
0.00000
1.33600+01
2.00000+00
0.00000
0.00000
1.29300+01
1,00000+00
0.00000
0,00000
1.29300+01
2.0QOOO+00
o.ooooo
o.ooooo
1.29300+01
2.0QOOO+00
0.00000
o.ooooo
1.29300+01
2.00000+00
0.00000
0.00000
1.29300+01
2.00000+00
0.00000
0.00000
1.29300+01
2.0QOOO+00
o.ooooo
0.00000
1.59200+01
1.00000+00
0.00000
0.00000
1.65100+01
1.00000+00
0.00000
0.00000
1 .00500 + 01
1.00000+00
0.00000

-------
            TABLE C-l.   (Concluded)
COAL FIPtD BOILERS
1 1*
2 1*
3 1*
U 1*
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1 15
2 15
3 15
* 15
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3.
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
1*1
1*1
1*1
1*1
1*2
1*2
1*2
1*2
1*3
1*3
1*3
1*3
1**
1**
1**
1**
1*5
1*5
1*5
1*5
1*6
1*6
1*6
1*6
1*7
1*7
1*7
1*7
1*8
1*8
1*8
1*8
1*9
1*9
1*9
1*9
i.*3oon+oo
o.ooooo
1.06000+02
3.10000+02
l.*0000+00
0.00000
1.17000+02
3.87000+02
l.*0000+00
0.00000
1.11000402
3.85000+02
l.*0000+00
0.00000
8.90000+01
2.5*000+02
l.*0000+00
0.00000
1.09000+02
3.*5000+02
1.1*0000+00
0.00000
«. 90000+01
1.77000+02
l.*0000+00
o.oonoo
1.07000+02
2.7*000+02
l.*0000+00
0.00000
8,soonn+oi
l.5Pnon+o2
i.*ooon+oo
o.onooo
a. 10000+01
1.95000+02
1
0
0
0
1
0
0
0
1
0
0
0
9
0
0
0
9
0
0
0
9
0
0
0
6
0
0
0
6
0
0
0
6
0
0
0
.59390+02
.ooono
.00000
.00000
.01223+02
.00000
.00000
.oonoo
.01223+02
.00000
.00000
.00000
.73935+01
.00000
.00000
.00000
.27360+01
.00000
.00000
.00000
.27360+01
.00000
.ooono
.00000
.7*820+01
.00000
.00000
.00000
.7*P2n+01
.00000
.00000
.00000
,3176*+01
.00000
.ooono
.oooon
2.0965*+0?
1.00000+02
0.00000
o.ooono
2.**260+0?
6.73000+01
0.00000
0.00000
2.**260+02
8.73000+01
0.00000
0.00000
2.35017+02
8.*0000+01
8.00000+00
0.00000
2.23816+02
8.00000+01
0.00000
0.00000
2.23618+02
8.00000+01
8.00000+00
0.00000
1.628*0+0?
5.82000+01
0.00000
0.00000
1.628*0+0?
5.62000+01
A. 00000+00
0.00000
1.52*93+02
5.*5000+01
e.ooonn+oo
o.ooono
6.5*269+05
1.06000+02
0.00000
1.00000+02
l.*06*5*06
1.17000+02
0.00000
0.00000
l.*08*5+06
1.11000+02
0.00000
0.00000
l.*08*5+06
1.11300+02
0.00000
0.00000
l.*08*5+06
1.09000+02
0.00000
0.00000
l.*08*5+06
1.12000+02
0.00000
0.00000
l.*08*5+06
1.07000+02
1.00000+01
0.00000
1.*08*5+06
1.13000+02
I.OOOOQ+OI
o.ooooo
l.*08*5+06
1.08000+02
0.00000
0.00000
*. 80000 + 01
1.30000*00
0.00000
0.00000
*. 00000+01
3.10000+00
0.00000
0.00000
*. 00000+01
2.20000+00
0.00000
0.00000
*. 00000+01
2.30000+00
0.00000
0.00000
*. 00000+01
1.90000+00
0.00000
0.00000
*. 80000+01
2.*0000+00
0.00000
0.00000
2.*0000+01
1.50000+00
0.00000
0.00000
2.*0000+01
2.50000+00
0.00000
0.00000
2.*0000+01
1.70000+00
0.00000
0.00000
2.00000+00
0.00000
3.08818+0*
0.00000
2.00000+00
0.00000
3.06725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
2.00000+00
0.00000
3.06725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
2.00000+00
0.00000
3.08725+0*
0.00000
0.00000
1.00500+01
1.00000+00
0.00000
0.00000
8.09000+00
1.00000+00
o.ooooo
0.00000
8.09000+00
1.00000+00
0.00000
0.00000
8.09000+00
2.00000+00
0.00000
0.00000
8.09000+00
1.00000+00
0.00000
0.00000
8.09000+00
2.00000+00
0.00000
0.00000
0.09000+00
1.00000+00
0.00000
0.00000
8.09000+00
2.00000+00
0.00000
o.ooooo
8.09000+00
2.00000+00
0.00000

-------
TABLE C-2.  NO  CONTROL TEST DATA OPPOSED WALL COAL-FIRED BOILERS
              A
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
£ *
£ !
2
3
<«
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
i*
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
3
3
3
3
?
2
2
2
2
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
?
3
?
2
?
2
?
?
?
?
2
?
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
1
1
1
1
2
2
2
2
3
3
3
3
K
4
i»
H
5
5
5
5
6
6
6
6
7
7
7
7
e
a
e
a
9
9
9
9
10
10
10
10
1.17000+00
0.00000
1.49000+02
7.67000+02
1.17000+00
0.00000
1.18000+02
7.33000+02
1.17000+00
0.00000
8.62000+01
7.23000+02
1.17000+00
0.00000
1.39000+02
9.08000+02
1.17000+00
0.00000
1.38000+02
9.02000+02
1.38000+00
0.00000
1.40000+02
6. 36000+02
1.36000+00
0.00000
1.29000+02
7.81000+02
1.38000+00
0.00000
1.35000+02
6.65000+02
1.36000+00
0.00000
1.27000+02
6.21000+02
1.19000+00
1.44780+00
1.29000+02
7. 64000+0?
1.08054+0?
o.oonoo
0.00000
0.00000
1.06571+02
0.00000
0.00000
0.00000
1.08571+02
0.00000
o.oonoo
0.00000
1.46667*02
0.00000
0.00000
0.00000
1.44279+02
0.00000
0.00000
0.00000
1.42726+02
0.00000
0.00000
0.00000
1.17162+02
0.00000
o.ooonn
0.00000
9.09765+01
0.00000
0.00000
o.oooon
9. 28395+01
0.00000
0.00000
0.00000
1 .30306+02
0.00000
0.00000
o.ooonn
1.87730+02
7.04000+01
0.00000
0.00000
1.88518+02
7.07000+01
6.00000+00
0.00000
1.88518+02
7.07000+01
1.20000+01
0.00000
2.55175+02
9.57000+01
0.00000
0.00000
2.50664+02
9.40000+01
0.00000
0.00000
2.13976+0?
9.38000+01
0.00000
0.00000
1.75646+02
7.70000+01
0.00000
0.00000
1.36436+02
5.96000+01
0.00000
o.oooon
1.39149+02
6.10000+01
0.00000
0.00000
2.35396+02
8.39000+01
o.ooonn
O.ooono
2.07297+06
1.490nn+02
0.00000
1.12000+01
2.07297+06
1.47800+02
0.00000
1.10000+01
2.07297+06
1.46500+02
0.00000
1.08000+01
2.07297+Ofe
1.39000+02
0.00000
1.22000+01
2.07297+06
1.36000+02
0.00000
1.25000+01
1.52770+06
1.40000+02
0.00000
3.00000+00
1.52770+06
1.29000+02
0.00000
1.60000+01
1.52770+06
1.35000+02
0.00000
2.30000+01
1.52770+06
1.27000+02
0.00000
2.10000+01
1.47232+06
1.29000+0?
0.00000
0.00000
2.40000+01
7.10000+00
0.00000
0.00000
2.40000+01
7.00000+00
0.00000
0.00000
1.60000+01
6.90000+00
0.00000
n. ooooo
3.00000+01
6.10000+00
o.ooono
0.00000
3.00000+01
5.90000+00
0.00000
0.00000
2.40000+01
6.20000+00
0.00000
0.00000
2.00000+01
4.90000+00
0.00000
0.00000
2.00000+01
5.60000+00
0.00000
0.00000
2.00000+01
4.70000+00
0.00000
0.00000
4.00000+01
4,fl5non+no
o.oonoo
o.onooo
2.00000+00
o.nonoo
3.00407+04
0.00000
2.00000+00
0.00000
3.00407+04
o.ooono
2.00000+00
0.00000
3.00407+0*
0.00000
2.00000+00
0.00000
3.00407+04
0.00000
2.00000+00
0.00000
3.00407+04
0.00000
1.00000+00
0.00000
2.99778+04
0.00000
1.00000+00
o.oonoo
2.99778+04
0.00000
1.00000+00
0.00000
3.04275+04
o.onooo
1.00000+00
0.00000
3.04275+04
o.onooo
1.00000+00
0.00000
2.91716+04
o.onono
0.00000
5.45000+00
1.00000+00
0.00000
o.ooooo
5.45000+00
2.00000+00
0.00000
0.00000
5.t5000+00
2.00000+00
o.uoonn
o.ooooo
5.**5000 + 00
1.00000+00
o.oooon
o.uoooo
5.45000+00
1.00000+00
o.ooono
1.00000+00
1.14000+00
1.00000+00
0.00000
1.00000+00
1.14000+00
1. 00000+00
o.ooouo
1.00000+00
i.4ioon+oo
1. 00000+00
o.ooooo
1.00000+00
i.4ioon+oo
1.00000+00
o.oooon
o.ononn
i. 61000+00
i .uoonn+oo
o.uoonn

-------
                  TABLE C-2.   (Continued)
HORIZONTALLY OPPOSED COAL FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
«l
1
2
3
o ,
8 i
2
3
4
1
2
3
«»
1
2
3
it
1
2
3
M
1
2
3
<4
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
?
2
?
2
2
2
2
2
2
2
2
2
2
?
?
2
2
2
2
?
?
?
?
?
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
11
11
11
11
12
12
12
12
13
13
13
13
1*
14
14
14
15
15
15
15
16
16
16
16
17
17
17
17
18
Ifl
18
18
19
19
19
19
20
20
20
20
1.19000400
1.44760+00
1.24000+02
7.35000+02
1.19000+00
1.44780+00
1.26000+02
7.30000+02
1. 19000*00
1.44780+00
1.28000+02
7.85000+02
1.19000+00
1.44780+00
1.28000+02
6.66000+02
1.19000+00
1.44780+00
1.29000+02
6.78000+02
1.19000+00
1.44780+00
1.30000+02
6.56000+02
1.19000+00
1. 44780+00
1.28000+02
7.23000+02
1.19000+00
1.44780+00
1.29000+02
5.94000+02
1.19000+00
1.44780+00
1.28000+02
7.81000+02
1.19000+00
1.44780+00
1.22000+02
7.77000+02
1.30306+02
0.00000
0.00000
0.00000
1.31238+02
0.00000
0.00000
0.00000
1.27512+02
0.00000
0.00000
0.00000
1.26684+02
0.00000
9.70000+00
0.00000
1.27201+02
0.00000
1.17000+01
0.00000
1.26684+02
0.00000
1.50000+01
0.00000
9.84285+01
0.00000
0.00000
0.00000
9.70830+01
0.00000
1.57000+01
0.00000
1.38690+02
0.00000
0.00000
0.00000
1.37*51+02
O.OOOPO
o.oooon
0.00000
2.35396+0?
8. 39000+01
0.00000
o.ooono
2.37067+09
8.45000+01
0.00000
0.00000
2.30348+0?
8.21000+01
0.00000
0.00000
2.28929+02
8.16000+01
0.00000
0.00000
2.29760+02
8.19000+01
0.00000
0.00000
2.28929+02
8.16000+01
0.00000
o.oooon
1.77887+02
6.34000+01
o.ooono
0.00000
1.75364+02
6.25000+01
0.00000
0.00000
2.50538+02
8.93000+01
0.00000
0.00000
2.48582+0?
8.86000+01
0.00000
o.ooono
1.47232+06
1.24000+02
0.00000
0.00000
1.47232+06
1.26000+02
0.00000
0.00000
1.47232+06
1.28000+02
0.00000
0.00000
1.47232+06
1.28000+02
0.00000
0.00000
1.47232+06
1.29000+02
0.00000
0.00000
1.47232+06
1.30000+02
0.00000
0.00000
1.47232+06
1.20000+02
0.00000
0.00000
1.47232+06
1.29000+02
0.00000
0.00000
1.47232+06
1.28000+02
0.00000
0.00000
1.47232+06
1.22000+02
o.ooono
o.ooono
4.00000+01
4.16000+00
n.oonoo
0.00000
4.00000+01
4.39000+00
o.ooono
n.oonoo
4.00000+01
4.73000+00
0.00000
0.00000
4.00000+01
4.70000+00
0.00000
0.00000
4.00000+01
4.9onon+nn
0.00000
0.00000
4.00000+01
5.00000+00
0.00000
0.00000
4.00000+01
4.70000+00
0.00000
0.00000
4.00000+01
4.65000+00
0.00000
0.00000
4.00000+01
4.68000+00
0.00000
0.00000
4.00000+ni
3.90000+00
0.00000
o.oonoo
i.onooo+oo
0.00000
2.91716+04
o.onooo
1.00000+00
0.00000
2.91716+04
o.onooo
1.00000+00
0.00000
2.91716+04
o.oooon
1.00000+00
0.00000
2.91716+04
o.noooo
1.00000+00
o.noooo
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
i.ooooo+no
0.00000
2.91716+04
o.onooo
1.00000+00
o.onooo
2.91716+04
o.onooo
1.00000+00
o.ooono
2.91716+04
0.00000
o.ooooo
1.61000+00
i.uoooo+oo
o.ooono
o.oooon
1.61000+00
1.00000+00
n.nooon
o.ooooo
1.61000+00
l.UOOOO+00
O.OPOOO
0.00000
1.61000+00
5.00000+00
0.00000
o.ooono
1.61000+00
5.00000+00
o.ooono
o.ooouo
1.61000+00
5.00000+00
0.00000
0.00000
1.61000+00
1.00000+00
o.uoooo
o.ooooo
1.61000+00
5.00000+00
0.00000
0.00000
1.6ioon+oo
1.00000+00
o.ooonn
O.OOOOP
1. 61000+00
i.onooo+oo
o.oooon

-------
                   TABLE C-2.   (Continued)
HORIZONTALLY OPPOSED coat FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
0 *
HO .
>-• 1
2
3
4
1
2
3
4
1
2
3
1
2
3
1
2
3
14
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
P
2
2
J
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
21
21
21
21
22
22
22
22
23
23
23
23
24
24
24
25
25
25
25
26
26
26
26
27
27
27
27
28
28
28
28
29
29
29
29
30
30
30
30
1.19000+00
1.44760+00
1.20700+02
7.17000+02
1.19000+00
1.44760+00
1.26000+02
7.11000+02
1.19000+00
1.44780+00
1.26000+02
6.93000+02
1.19000+00
1.44780+00
1.25000+02
8.27000+02
1.19000+00
1.44760+00
1.25000+02
7.80000+02
1.19000+00
1.44780+00
1.24500+02
7.27000+02
1.19000+00
1.44780+00
1.27000+02
6.06000+02
1.19000+00
1.44780+00
1.03000+02
5.49000+02
1.19000+00
1.44780+00
1.27000+02
6.27000+02
1.19000+00
1.44780+00
9.aenoo+oi
4.56000+02
1.39414+02
0.00000
0.00000
0.00000
1.38690+02
0.00000
1.61000+01
0.00000
1.45631+02
0.00000
0.00000
0.00000
1.45521+02
0.00000
0.00000
0.00000
1.46452+02
0.00000
6.90000+00
0.00000
1.44693+02
o.onooo
1.50000+01
0.00000
1.17058+02
0.00000
0.00000
0.00000
1.17886+02
0.00000
0.00000
0.00000
1.306 17+02
0.00000
1.70000+01
o.oooon
1.30306+02
0.00000
l.AOOOO+01
n.oonno
2.51957+0?
8.96000+01
2.00000+00
O.OOOPO
2.50538+02
8.93000+01
0.00000
0.00000
2.63440+0?
9.39000+01
0.00000
0.00000
2.62872+02
9.37000+01
0.00000
0.00000
2.64576+02
9.43000+01
0.00000
0.00000
2.61484+0?
9.32000+01
0.00000
0.00000
2.11547+02
7.54000+01
0.00000
0.00000
2.12935+0?
7.59000+01
8.00000+00
0.00000
2.35963+0?
8.41000+01
0.00000
0.00000
2.35396+02
8.39000+01
fl. 00000+00
o.noono
) .47232+06
1.27000+02
0.00000
0.00000
1.47232+06
1.26000+0?
0.00000
0.00000
1.47232+06
1.26000+02
0.00000
0.00000
1.47232+06
1.25000+02
0.00000
0.00000
1.47232+06
1.25000+02
0.00000
0.00000
1.47232+06
1.24500+02
0.00000
0.00000
1.47232+06
1.27000+02
0.00000
0.00000
1.47232+06
1.28800+02
0.00000
0.00000
1.47232+06
1.27000+0?
0.00000
0.00000
1.47232+06
1.23500+02
0 .00000
0.00000
3.60000+01
4.55000+00
0.00000
0.00000
4.00000+01
4.43000+00
0.00000
4.60100+03
4.00000+01
4.69000+QO
0.00000
0.00000
4.00000+01
4.31000+00
0.00000
0.00000
4.00000+01
4.31000+00
0.00000
0.00000
4.00000+01
4.23000+00
0.00000
0.00000
4.00000+01
4.50000+00
0.00000
0.00000
3.20000+01
4.79000+00
o.ooono
0.00000
4.00000+01
4.51000+00
0.00000
n. ooooo
3.20000+01
4.13000+00
o.oonoo
n.onnoo
1.00000+00
0.00000
2. 91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.91716+04
0.00000
1.00000+00
0.00000
2.^1716+04
0.00000
l.onooo+00
0.00000
2.91716+04
o.onooo
l.cnooo+oo
o.nnnno
o.ononu
o.ooooo
1.61000+00
2.00000+00
o.ooooo
o.ooooo
l.flOOO+00
5.000UO+00
o.ooooo
o.ooono
1.61000+00
1.00000+00
0.00000
0.00000
l.6ioon+oo
1.00000+00
0.00000
o.ooooo
1.61000+00
5.00000+00
o.ooooo
0.00000
1.61000+00
5.00000+00
0.00000
o.uoooo
1.61000+00
1.00000+00
0.00000
o.oooon
1.61000+00
2.00000+00
O.uooon
o.ooono
l.tioon+oo
5.00000+00
0.00000
0 . u o o n o
l .Monn+on
n. i1 oooo

-------
                      TABLE C-2.   (Continued)
HORIZONTALLY OPPOSED COAL FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3

-------
                   TABLE C-2.   (Continued)
HORIZONTALLY  OPPOSED COAL PIRED BOILERS
1
2
3
4
1
2
3
4
I
2
3
U
I
2
3
4
1
2
3
0 4
PO
<*» 1
2
3
4
1
2
3
4
1
2
3
14
1
2
3
4
1
2
3
4
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
6
6
6
6

6
6
6
6
6
6
f>
6
6
6
6
6
6
6
6
6
6
6
6
6
2
2
2
?
?
?
2
2
2
2
2
?
2
2
2
2
2
2
2
2

?
2
2
2
2
?
?
2
2
2
2
2
2
2
2
2
?
?
2
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
5
3
3
3
3
3
3
3
3
3
3
3
3
3
42
42
42
«»2
43
43
<*3
43
44
44
44
44
45
45
45
45
46
46
46
46

47
47
47
47
48
48
48
48
49
49
49
49
50
50
50
50
51
51
51
51
1.04000400
0.00000
1.22000+02
5.69000+02
1.04000+00
0.00000
1.10000+02
4.47000+02
1.03000+00
0.00000
1.12000+02
5.60000+02
1.03000+00
0.00000
1.04000+02
3.75000+02
1.26000+00
0.00000
1.19000+02
7.41000+02

1.29000+00
0.00000
1.10000+02
6.30000+02
1.24000+00
0.00000
1.12000+02
6.41000+02
1.23000+00
0.00000
1.00000+02
5.60000+02
1.31000+00
0.00000
9. jOOOO+Oj
4.88000+02
1.26000+00
0.00000
1.42500+02
fl. 16000+02
1.34550+02
o.oooon
0.00000
0.00000
1.34550+02
0.00000
0.00000
o.ooono
1.34550+02
0.00000
0.00000
0.00000
1.34550+02
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000

0.00000
0.00000
0.00000
o.ooono
0.00000
o.ooono
o.oooon
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
o.ooono
0.00000
0.00000
0.00000
o.nooco
0.00000
o. nopnn
2.08550+02
1.00000+02
0.00000
0.00000
2.08550+02
1.00000+02
0.00000
0.00000
2. 08550+02
1.00000+02
2.00000+00
0.00000
2.08550+02
1.00000+02
2.00000+00
0.00000
1.67666+02
9.44000+01
0.00000
0.00000

1. 67666+02
9.44000+01
o.ooono
0.00000
1.67666+02
9.44000+01
0.00000
0.00000
1.61010+02
9.06000+01
1.20000+01
0.00000
1.76310+02
9.92000+01
1.20000+01
0.00000
1.33250+02
7.50000+01
0.00000
o.ooonn
6.78002+05
1.22000+02
0.00000
2.40000+01
6.78002+05
1.10000+02
0.00000
2.83000+02
6.78002+05
1.24500+02
0.00000
2,30000+01
6.78002+05
1.15100+02
0.00000
2.31000+02
2.15003+06
1.19000+02
0,00000
2.10000+01

2.15003*06
1.10000+02
0.00000
4.23000+02
2.15003+06
1.12000+02
0.00000
1.56000+02
2.15003+06
1.24900+02
0.00000
4.00000+01
2.15003+06
1.17300+02
o.nnoon
1.72000+0?
2.15003+06
1.42500+0?
0.00000
i.70ono+oi
2.00000+01
3.90000+00
0.00000
0.00000
2.00000+01
2.10000+00
0.00000
0.00000
1.80000+01
4.20000+00
0.00000
0.00000
1.80000+01
2.80000+00
0.00000
0.00000
5.40000+01
3.40000+00
0.00000
3.28950+03

5.40000+01
2.00000+00
0.00000
0.00000
5.40000+01
2.30000+00
0.00000
0.00000
4.20000+01
4.30000+00
0.00000
3.60340+03
4.20000+01
3.20000+00
0.00000
n. ooooo
4.2oooo+ni
6.50000+00
o.ooono
o.noono
1.00000+00
0.00000
2.45768+04
0.00000
1.00000+00
0.00000
2.45768+04
o.onooo
1.00000+00
0.00000
2.52991+04
0.00000
1.00000+00
0.00000
2.52991+04
0.00000
1.00000+00
0.00000
2.36006+04
0.00000

1.00000+00
0.00000
2.35377+04
0.00000
1.00000+00
0.00000
2.37334+04
0.00000
1.00000+00
0.00000
2.35214+04
0.00000
1.00000+00
0.00000
2.36006+04
0.00000
l.onooo+oo
0.00000
2.?H196+04
o . o o n n o
0.00000
3.64400+01
1.00000+00
o.oonoo
0.00000
3.64400+01
1.00000+00
o.ooono
0.00000
3.44200+01
2.00000+00
0.00000
o.oooon
3.44200+01
2.00000+00
0.00000
1.00000+00
1.29100+01
1.00000+00
0.00000

1.00000+00
1.28800+01
1.00000+00
0.00000
i.oooon+oo
l.39?no+oi
l.QOOOO+OQ
o.ooooo
1.00000+00
1.17100+01
2.00000+00
0.00000
1.00000+00
1.29100+01
2.00000+00
o.ooooo
1.00000+00
1. "0500 + 01
1.00000+00
o . u n o n n

-------
                                                    TABLE C-2.  (Concluded)
                               HORIZONTALLY OPPOSED  COAL FIRFD BOILERS
1
2
3
4
1
2
3
4
6
6
6
6
6
6
6
6
?
2
2
2
2
2
2
2
3
3
3
3
3
3
3
3
52
52
52
52
53
53
53
53
1.26000+00
o.onooo
1.10000+02
8.01000+02
1.26000+00
0.00000
9.00000+01
4.52000+02
0.00000
0.00000
0.00000
o.noooo
0.00000
0.00000
0.00000
0.00000
1.33250+02
7.50000+01
1.20000+01
0.00000
1.30916+02
7.37000+01
1.20000+01
0.00000
2.15003+06
1.42500+02
0.00000
0.00000
2.15003+06
1.15900+02
0.00000
3.30000+01
4.20000+01
6.40000+00
0.00000
o.ooooo
4.20000+01
3.00000+00
0.00000
0.00000
1.00000+00
0.00000
2.38196*04
0.00000
1.00000+00
0.00000
2.3S429+04
0.00000
i.oooon+oo
1.40500+01
2. 00000+00
0.00000
l.COOOO+00
1.40500+01
2.00000+00
0.00000
o

-------
TABLE C-3.
NOX CONTROL TEST DATA FROM SINGLE WALL COAL-FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
0 4
ro
01 1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
1
2
3
14
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1

1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
1
1
1
1
2
2
2
2
3
3
3
3
4
4
4
4
5
5
5
5

6
6
6
6
7
7
7
7
a
8
8
8
9
9
9
9
10
10
10
10
1.30000400
0.00000
1.20000+02
6.56000+02
1.40000+00
0.00000
1.18000+02
6.69000402
1.29000>00
0.00000
1.17000+02
5.77000402
1.29000400
0.00000
1.10000402
4.91000402
1.40000400
0.00000
1.07000+02
5.18000+02

1.35000400
0.00000
1.00000+02
3.68000+02
1.37000+00
0.00000
1.03000+02
3.97000+02
1.43000+00
0.00000
1.02000+02
3.43000+02
1.31000+00
0.00000
1.29000+02
6.29000+02
1.31000+00
0.00000
1.14000+02
4.50000+02
2.26769+02
0.00000
0.00000
0.00000
2.21490402
o.ooono
0.00000
0.00000
2.21490402
0.00000
o.ooono
0.00000
2.21490402
0.00000
0.00000
0.00000
2.21490402
0.00000
0.00000
0.00000

2.12589402
0.00000
0.00000
0.00000
2.21490402
0.00000
0.00000
o.noooo
?. 12589+02
0.00000
0.00000
0.00000
1.94fl9ru02
O.oooon
o.noooo
0.00000
1 .87653+0?
0.00000
0.00000
o.ooonn
2.1804540?
1.02400402
0.00000
o.ooooo
2.12935402
1.00000+02
0.00000
0.00000
2.12935+02
1.00000+02
0.00000
0.00000
2.12935402
1.00000+02
0.00000
o.onooo
2.12935402
1.00000402
2.00000+00
0.00000

2.0«»'»l7402
9. 60000401
2.00000+00
o.ooono
2.12935+0?
1.00000+02
2.00000+00
O.OOOPO
2.0441740?
9.60000+01
2.00000400
0.00000
1.87383+02
A. 80000401
o.ooono
0.00000
1.80569+0?
fl. 48000+01
o.oonon
0.0000"
3.32262+05
1.20000+0?
0.00000
5.20000+01
3.32262+05
1.18000+02
0.00000
3.94000+0?
3.32262+05
1.17000+02
0.00000
3.29000402
3.32262405
1.10000402
0.00000
8.14000402
3.32262405
1.23600+02
0.00000
3.83000+02

3.32262+05
1.14200402
0.00000
8.33000402
3.32262405
1.16000402
0.00000
4.1400040?
3.32262405
1.20000402
0.00000
8.67000402
3.32262405
1.2900040?
0.00000
5.20000401
3.322*2405
1.1400040?
o.onooo
^.soono+o?
1. 60000 + 01
3.60000+00
o.ooooo
0.00000
1 .60000+01
3.30000+00
0.00000
8.60000+02
1.60000+01
3.20000+00
0.00000
0.00000
1.60000+01
2.00000+00
0.00000
0.00000
1.40000401
4.10000400
0.00000
1.72000+03

1.40000+01
2.70000+00
0.00000
0.00000
1.40000+01
3.30000+00
0.00000
0.00000
1.40000+01
3.00000+00
0.00000
0.00000
1.60000+01
4.80000+00
0.00000
o.ooono
1.6000P+01
2.7onon+no
n. oiooo
n.noono
1.00000+07
0.00000
2.81790+04
7.89000+00
1.00000+00
0.00000
2.82070+04
4.65000+00
1.00000+00
0.00000
2.73519404
0.00000
1.00000+00
0.00000
2.73519+04
0.00000
1.00000400
0.00000
2.82070404
0.00000

i.onooo+oo
0.00000
2.77783+04
0.00000
1.00000+00
0.00000
2.83514+04
5.62000+00
1 .00000+00
0.00000
2.94652+04
3.84000+00
1.00000+00
0.00000
2.811*4+04
0.00000
1.00000+00
0.00000
?.flllfl'* + 04
o . o n o n o
1.00000+00
5.10000+00
l.onoOO+00
o.ooouo
1.00000+00
5.*»0000 + 00
1.00000+00
0.00000
1.00000+00
6.30000+00
i.nnooo+oo
O.UOOOO
1.00000+00
6.30000+00
l.UOOOO+00
o.ooouo
1.00000+00
5.4QOOO+00
2.00000+00
0.00000

1.00000+00
5.85000+00
2.00000+00
o.ooono
1.00000400
7.70000400
2.00000400
o.oooon
1. 00000+00
7.20000+00
2. 00000 + 00
o.oooon
i.oooon+oo
8.70000+00
i.onoon+oo
o.oooon
1 .00000 + 00
8.7ooon+on
i .unoon+uo
n."noon

-------
                    TABLE C-3.   (Continued)
FRONT WALL  COAL FIRED OOII.FRS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
o 4
ro
<* j
2
3
4
1
2
3
4
1
2
3
4
1
2
3
it
1
2
3
it
1
1
1
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2

2
2
2
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
5
3
3
3
3
3
3
3
3
j
3
3
3
3
5
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
11
11
11
11
12
12
12
12
13
13
13
13
14
1«»
11
1»
15
15
15
15

16
16
16
16
17
17
17
17
18
18
18
18
19
19
19
19
20
20
20
20
1. 1*0000 + 00
o.ooono
9.40000+01
4.60000+02
1.35000+00
0.00000
8.70000+01
3.45000+02
7.70000-01
0.00000
1.30000+02
4.54000+02
7.90000-01
0.00000
1.25000+02
4.09000+02
8.10000-01
0.00000
1.02000+02
3.47000+02

8. 40000-01
0.00000
8.80000+01
2.14000+02
1.25000+00
0.00000
1.17000+02
6.70000+02
1.27QOO+00
0.00000
1.07000+02
5.56000+02
1.20000+00
0.00000
1.06000+02
6.44000+02
1.26000+00
0.00000
9.60000+01
4.74000+02
1.9UP90+0?
0.00000
0.00000
0.00000
1.91371+02
0.00000
0.00000
0.00000
1.32376+0?
0.00000
0.00000
0.00000
1.32376+02
0.00000
0.00000
0.00000
1.35Q67+02
0.00000
0.00000
0.00000

1.29789+02
0.00000
0.00000
0.00000
1.67566+02
0.00000
0.00000
0.00000
1.64358+02
0.00000
0.00000
0.00000
1.66946+02
0.00000
o.oonno
o.ooooo
1.59080+02
0.00000
O.POOOO
0.00000
1.80569+02
6.80000+01
4.00000+00
0.00000
1.83976+0?
8.64000+01
4.00000+00
0.00000
1.06657+02
9.61900+01
o.ooonn
0.00000
1.06657+02
9.61900+01
0.00000
0.00000
1.08770+02
9.81000+01
3.00000+00
0.00000

1.04543+02
9.429QO+01
6.00000+00
0.00000
2.10790+0?
1.00000+02
0.00000
0.00000
2.06657+0?
9.80500+01
0.00000
0.00000
2.09970+02
9.96100+01
2.00000+00
o.oonoo
2.0006*» + 0?
9. 49200 + 01
2.00000+00
0.00000
3.32262+05
1.26600+02
0.00000
7.73000+0?
3.32262+05
1.16100+02
0.00000
1.92000+03
3.14096+05
1.30000+02
0.00000
1.12000+02
3.14096+05
1.2500Q+02
0.00000
7.31000+02
3.14096+05
1.27400+02
0.00000
3.70000+02

3.14096+05
1.31900+02
0.00000
9.62000+02
6.32587+05
1 .17000 + 02
0.00000
6.90000+01
6.32587+Q5
1.07000+02
0.00000
9.30000+01
6.32587+05
1.21400+0?
0.00000
l.POOOO+01
6.3?587 + 0«>
1.10300+0?
0.00000
2.00000+0?
1 .20000 + 01
4.50000+00
0.00000
n. ooooo
1.20000+01
3.00000+00
0.00000
0.00000
1.50000+01
5.00000+00
0.00000
0.00000
1.50000+01
"». 30000 + 00
O.OOPOO
0.00000
1.20000+01
4.60000+00
0.00000
0.00000

1.20000+01
5.20000+00
0.00000
0.00000
1.60000+01
3.20000+00
0.00000
0.00000
1.6QOOO+01
1.50000+00
0.00000
0.00000
1.40000+01
3.BOOOO+00
0.00000
0.00000
1.40000+01
2.00000+00
0.00000
0.00000
1.00000+00
o.onooo
2.B2070+04
o.ooooo
1.00000+00
0.00000
2.K1790+04
0.00000
1.00000+00
0.00000
2.31089+04
0.00000
1.00000+00
0.00000
2.39943+0*
0.00000
1.00000+00
0.00000
2.54925+04
0.00000

1.00000+00
0.00000
2.54389+04
0.00000
1.00000+00
0.00000
2.89293 + 01*
0.00000
1.00000+00
o.ooono
2.91623+04
0.00000
1.00000+00
0.00000
2.B6101+04
0.00000
l.noooo+no
O.OUOOO
2.918^2+04
0.00000
i.ooooo+no
5,"»0000 + 00
2.110000 + 00
o.ooono
1 .UOOOO + 00
5.10000+00
?.onooo+oo
o . i' n o o o
0.00000
2.60500+01
1.00000+00
0.00000
o.ooooo
2.72500+01
1 .00000 + 00
o.oooon
o.ooooo
2.SP500+01
2.00000+00
o.ooooo

0.00000
2,75400+01
2.00000+00
0.00000
o.opooo
J .59700+01
1. UOOOO+00
o.ooono
o.ooooo
1. 56000+01
i.couon+oo
o.ooooo
0.00000
1.70700+01
2.00000+00
o.oooon
o.ooono
l.(>5!>00 + 01
?. 1)000(1 + 00
o.onooo

-------
                   TABLE  C-3.   (Continued)
FRONT WALL  COAL FIRED BOILERS
1
2
3
4
1
2
3
4
I
2
3
4
1
2
3
4
1
2
3
o „
ro
^ 1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
U
1
2
3
4
3
3
3
3
3
3
3
3
4
4
4
4
4
4
4
4
4
4
4
4

4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
U
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
3
3
3

3
3
3
3
3
j
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
21
21
21
21
22
22
22
22
23
23
23
23
24
24
24
24
25
25
25
25

26
26
26
26
27
27
27
27
28
26
28
28
29
29
29
29
30
30
30
30
1.23600400
0.00000
1.240004-02
6.66000+02
1.25000-fOO
0.00000
1.06000402
5.16000402
1.33000400
0.00000
1.20000402
fl. 50500402
1.33000400
0.00000
1.12000402
7.17000402
1.33000400
0.00000
1.04000402
6.46500402

1.43000400
0.00000
1.01000402
5.31000402
1.37000400
0.00000
1.21000402
7.94000402
1.37000400
0.00000
1.05000402
6.97000402
1.37000400
0.00000
9.05000401
5.36000402
1.37000400
o.ooono
6.60000401
5.16000402
1.38690402
o.oooon
0.00000
O.OOOOP
1.3361640?
0.00000
0.00000
0.00000
1.97665402
0.00000
0.00000
0.00000
1.97685402
0.00000
0.00000
o.oooon
1.976B540?
0.00000
0.00000
0.00000

1.96443402
0.00000
0.00000
0.00000
1.68084402
0.00000
o.ooonn
0.00000
1.66064+0?
0.00000
o.nooon
o.noooo
1.5442240?
0.00000
O.OOOPO
o.noooo
1.600«<» + 02
o.noono
O.OOPOO
o.oooon
1.74575402
P. 26100401
0.00000
0.00000
1.67982402
7.96900401
0.00000
0.00000
4.55523402
1.00000402
o.ooono
0.00000
4.55523402
1.00000402
o.ooono
0.00000
4.55523402
1.00000402
2.00000400
o.ooonn

4.369U + 02
9.93600401
2.00000400
o.ooono
3.6719440?
8.50000+01
0.00000
0.00000
3.67194+0?
6.500004Q1
o.ooono
o.ooono
3.55901+02
7.81300401
4.00000+00
o.oooon
3.67194+02
e.5nnnn+oi
4.ooooo+nu
o. ooono
7.38067+05
1.2400040?
0.00000
0.00000
7.38067405
1.080004Q2
0.00000
0.00000
8.84274405
1.20000402
0.00000
2.25000401
8.64274405
1.12000402
0.00000
1.10000402
8.84274405
1.18300402
0.00000
3.30000401

6.84274405
1.14100402
0.00000
4.00000401
8.64274405
1.21000402
0.00000
0.00000
8.84274+05
1.05000+02
0.00000
0.00000
6.64274+05
1.20900402
0. 00000
o.onono
fl. 84274+05
1 .1690040?
0.00000
n. ooooo
1. 60000401
4.20000+00
0.00000
0.00000
1.60000401
1.60000400
0.00000
0.00000
1.60000401
3.60000400
0.00000
0.00000
1.60000401
2.40000400
0.00000
0.00000
1.40000401
3.40000400
0.00000
0.00000

1.40000401
2.70000400
0.00000
0.00000
1.60000401
3.80000400
0.00000
0.00000
1.60000401
2.10000+00
n. ooooo
n.oonno
1.20000401
3.75000400
0.00000
0.00000
1 .20000+01
3.15000400
o.ooono
o.oonnn
1. 00000400
0.00000
2.93161+04
o.onooo
1.00000400
o.onono
2.93370+04
0.00000
1.00000400
0.00000
2.88314+04
0.00000
1.00000+00
0.00000
2.86314+04
o.onooo
1.00000400
0.00000
2.88314404
0.00000

1.00000400
0.00000
3.02294+04
0.00000
1.00000*00
o.noooo
2.97122+04
0.00000
1.00000+00
0.00000
2.97122+04
0.00000
1.00000+00
0.00000
2.97122+04
0.00000
1.00000+00
o.ooooo
?. 07122 + 04
0 . U 0 0 0 0
0.00000
1.59400+01
1.U0000400
o.ooooo
o.ooono
1.60400401
1.00000+00
o.ooono
0.00000
9.60000+00
1. 00000 + 00
O.OPOOO
o.ooono
9.60000+00
1.00000400
0.00000
0.00000
9.^0000400
2.00000400
o.uoooo

o.ooono
8.13000400
2.00000400
o.ooonn
0.00000
9.3F-000 + 00
1.00000400
o.ooooo
o.onooo
9.36000+00
i.onooo+oo
o.uoooo
o.ooooo
9.36000+00
2.00000+00
o.ooonn
0.00000
9.36onn+oo
?. 00000+00
o . o n o n n

-------
                     TABLE C-3.   (Continued)
PROMT WALL  cnai. FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3

6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
8
e
e
8
6
e
e
f
a
«
8
a
*
3
3
3
3
3
3
3
3
3
3
3
3
3
5
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
it
3
.1
1
3
3
»
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
31
31
31
31
37
37
37
37
38
38
38
38
39
39
39
39
40
40
40
40
4l
41
41
41
42
42
42
42
46
46
46
46
47
47
47
47
U8
48
«S
48
1.37000*00
o.oonoo
8. 75000+01
5.29000*02
1.40000*00
0.00000
1.22000*02
5.94000*02
1.40000*00
0.00000
1.15000*02
5.06000*02
1.40000*00
0.00000
1.10000*02
5.23000*02
1.40000*00
0.00000
1.02000*02
3.38000*02
l.HOOOO+00
0.00000
1.15000*02
4.62000*02
1.40000*00
0.00000
8.60000*01
2.98000*02
1.36000*00
0.00000
1.23800*02
6.01000*02
1.36000*00
0.00000
1.16400*02
5.27000*02
1.36000*00
0.00000
9.70000*01
1.50000*02
1. £6842*02
o.oooon
0.00000
o.ocoon
2.21490+02
0.00000
o.oooon
0.00000
2.2H«90*02
0.00000
0.00000
0.00000
2.21U90+02
0.00000
0.00000
o.oooon
2.21490*02
0.00000
0.00000
0.00000
1.94690*0?
0.00000
0.00000
O.OOOOP
1.94890*0?
0.00000
0.00000
0.00000
J. 95201+02
o.noooo
0.00000
o.nonno
1. 93855+02
0.00000
0.00000
o.nonoo
1.93pf>5 + n?
o.onooo
o.nooon
o.nonoo
3.8U355+02
fl.43ftnu+oi
4.nnono+no
o.oooon
2.12935+02
1.00000+0?
o.ooonn
o.onooo
2.12935+02
1.00000+02
0.00000
0.00000
2.12955+02
1.00000+0?
2.00000+00
o.ooono
2.12935+02
1.00000+02
2.00000+00
0.00000
1.87383+02
8.80000+01
0.00000
o.ooonn
1.87383+02
8. 80000+01
4.00000+00
0.00000
2.89371+02
8.05700*01
0.00000
o.oooon
2.87320*n2
a.ooono+oi
o.oooon
o.ooonn
2.87320+02
«.nnoon+oi
4.00000*00
n.ooono
n.a^TH+o*
i .if.ooo+0?
o.ooono
n. ooooo
3.32262+05
1 .22000 + 0?
n. ooooo
0.00000
3.32262+05
1.15000+02
0.00000
0.00000
3.32262+05
1.26000+02
0.00000
0.00000
3.32262+05
1 .17000+02
0.00000
0.00000
3.32262+05
1.15000+02
0.00000
0.00000
3.32262+05
1.15000+02
0.00000
0.00000

-------
                   TABLE C-3.   (Continued)
FRONT WALL  COAL FIHEP ROILERS
1
2
5
4
1
2
3
<4
1
2
3
4
1
2
3
4
1
2
3
o 4
ro
UJ 1
2
3
i»
1
2
3
4
1
2
3
4
1
2
3
14
1
2
3
i*
6
a
8
e
a
a
a
a
9
9
9
9
9
9
9
9
9
9
9
9

9
9
9
9
9
9
9
9
9
9
9
9
10
10
10
10
10
10
10
10
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
.1
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
49
49
49
49
50
50
50
50
51
51
51
51
52
52
52
52
53
53
53
53

5«»
5*
5«»
5«»
55
55
55
55
56
56
56
56
57
57
57
57
53
53
53
53
1.36000+00
0.00000
8. 90000-t-Ol
3.00000402
1.36000+00
0.00000
S. 60000+01
2.25000+02
1.29000+00
0.00000
1.33700+02
1. 48000+03
1.29000+00
0.00000
1.19500+02
1.49000+03
1.29000+00
0.00000
1.53000+02
1.20000+03

1.29000+00
0.00000
1.36000+02
1.16000+03
1.29000+00
0.00000
9.54000+01
1.28000+03
1.29000+00
0.00000
8.47000+01
1.19000+03
1.50000+00
0.00000
1.17000+02
5.82500+02
1.30000+00
0.00000
1.10000+02
4.60000+02
I .91061+02
o.oooon
0.00000
0.00000
1.99341+02
0.00000
o.oooon
0.00000
1.51007+02
0.00000
0.00000
0.00000
1. 5794J+02
0.00000
0.00000
0.00000
9.19080+01
0.00000
0.00000
0.00000

9.19080+01
0.00000
0.00000
0.00000
1.06812+0?
0.00000
o.ooooc
0.00000
1.10P49+0?
0.00000
0.00000
0.00000
2.13624+02
0.00000
o.ooono
0.00000
2.23974+02
o.oooon
0.00000
O.OOOPO
2.83219+0?
7.88600+01
4.00000+00
0.00000
2.955-54 + 02
8.22900+01
4.00000+00
0.00000
2.10695+02
8.34900+01
o.noooo
0.00000
2.20317+02
8.73000+01
0.00000
o.ooono
1.28171+0?
5.07900+01
0.00000
o.oooon

1.28171+02
5.07900+01
o.ooono
o.ooono
1.49023+02
5.90500+01
a. ooooo+oo
0.00000
1.54638+0?
6.12700+01
e.oooon+oo
o.noonn
1.94323+0?
9.60000+01
o.ooono
o.oooon
2.04039+02
l.ooano+n?
0.00000
o.ooono
4.03705+05
1.18100+02
0.00000
?. 58000+0?
4.93705+05
1.15100+0?
0.00000
5.58000+02
8.86032+05
1.33700+02
0.00000
0.00000
8.86032+05
1.19500+02
0.00000
0.00000
8.86032+05
1.53000+02
0.00000
0.00000

8.86032+05
1.36000+02
0.00000
0.00000
8.86032+05
1.43100+0?
0.00000
0.00000
8.86032+05
1.27100+0?
0.00000
o.onouo
3.47791+05
1.17000+0?
0.00000
2.00000+01
3.47791+05
i.iooon+o?
o.ooono
f.flOOOO+02
1.20000+01
3.30000+00
0.00000
0.00000
1.20000+01
2.80000+00
0.00000
0.00000
2.40000+01
5.40000+00
0.00000
0.00000
2.40000+01
3.50000+00
0.00000
0.00000
1.60000+01
7.50000+00
0.00000
0.00000

1.60000+01
5.70000+00
0.00000
0.00000
1.60000+01
6.50POO+00
0.00000
0.00000
l.6ooon+oi
4.60000+00
0.00000
n. ooooo
1.6QOOO+01
3.20000+00
0.00000
o.oonoo
i.6oooo+ni
?.oonno+oo
0.00000
0. OOOOO
1.00000+00
o.oooon
2.79833+04
o.noooo
1.00000+00
0.00000
2.80532+04
0.00000
2.00000+00
0.00000
3.23404+04
0.00000
2.00000+00
0.00000
3.23404+04
0.00000
2.00000+00
0.00000
3.23404+04
0.00000

2.00000+00
0.00000
3.23404+04
o.onooo
2.00000+00
0.00000
3.21540+04
0.00000
2.00000+00
0.00000
3.23404+04
O.OUOOO
1.00000+00
o.ooono
2.44067+04
o.onooo
1.00000+00
o.onooo
2.65853+04
o.onooo
i.onooo+oo
9.90000+00
2.00000+00
o.onono
1.00000+00
9.40000+00
2.000UQ+00
o.uoooo
0.00000
7.21000+00
1. 00000+00
0.00000
o.uoooo
7.21000+00
1.00000+00
o.ooooo
O.OQOOO
7.21000+00
1.00000+00
0.00000

0.00000
7.21000+00
1.00000+00
0.00000
0.00000
7.21000+00
2.10000+00
0.00000
0.00000
7.21000+00
2.10000+00
o.oooi n
1.00000+00
8.90000+00
l.oooon+oo
o.ooooo
1.00000+00
6.10000+00
i.cinooo+oo
o . u o u o n

-------
                  TABLE  C-3.   (Continued)
FRONT WALL COSL FIRED BOILERS
1
2
3
*»
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
!
2
3
4
1
2
3
*
1
2
3
4
1
2
3
4
1
2
3
4
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
5
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
59
59
59
59
60
60
60
60
61
61
61
61
62
62
62
62
63
63
63
63
64
64
64
64
69
65
65
65
66
66
66
66
67
67
67
67
68
68
68
68
1.30000+00
0.00000
1.03000+02
5.01500+02
1.30000*00
0.00000
1.13000*02
5.02000*02
1.30000*00
0.00000
1.02000*02
4.40500*02
1.30000*00
0.00000
1.16000*02
5.26000*02
1.30000*00
0.00000
1.14000*02
4.46500*02
1.30000*00
0.00000
1.17000*02
4.70500+02
1.20000+00
0.00000
1.13000*02
3.68000*02
1.30000*00
0.00000
1.73000*02
6.04000+02
1.40000+00
0.00000
1.63000*02
5.69000*02
1.20000*00
0.00000
1.85000+02
5.59500+02
?. 20765+02
0.00000
0.00000
O.OOPOO
2.22525+02
0.00000
o.onnoo
0.00000
2.19006+02
0.00000
0.00000
0.00000
1.76260+02
0.00000
0.00000
0.00000
1.76260+02
0.00000
0.00000
0.00000
1.81539+02
0.00000
0.00000
0.00000
1.78020+02
0.00000
0.00000
0.00000
8.54910+01
0.00000
0.00000
0.00000
8.54910+01
0.00000
0.00000
o.oooon
8.90100+01
0.00000
0.00000
0.00000
2.00790+02
9.92000+01
2.00000+00
0.00000
2.02399+02
1. 00000+02
0.00000
o.ooono
1.99181+02
9.84000+01
2.00000+00
0.00000
1.60316+02
7.92000+01
0.00000
0.00000
1.60316+02
7.92000+01
0.00000
0.00000
1.65174+02
8.16000+01
4.00000+00
0.00000
1.61610+02
8.00000+01
4.00000+00
0.00000
7.77291+01
3.84000+01
0.00000
0.00000
7.77291+01
3.84000+01
o.ooono
0.00000
8.n94f,fl + 01
4.00000+01
0.00000
O.OOOno
3.47791+05
1.18500+02
0.00000
1.53000+02
3.47791+05
1 .13000+02
0.00000
0.00000
3.47791+05
1. 15100+02
0.00000
H. 24000+02
3.47791+05
1.16000+02
0.00000
3.90000+01
3.47791+05
1.14000+02
0.00000
6.80000+01
3.47791+05
1.23200+02
0.00000
4.00000+01
3.47791+05
1.14600+02
0.00000
5.84000+02
3.47791+05
1.73000+02
0.00000
1.50000+01
3.47791+05
1.63000*02
0.00000
1 .40000+01
3.47791+05
1.85000+02
0.00000
?. 10000+01
1.4(1000 + 01
3.30000+00
n. ooooo
0.00000
1.60000+01
2.50000+00
0.00000
0.00000
1.40000+01
2.80000+00
0.00000
0.00000
1.60000+01
3.00000+00
0.00000
0.00000
1.60000+01
2.65000+00
0.00000
0.00000
1.20000+01
4.00000+00
0.00000
0.00000
1.20000+01
2.80000+00
0.00000
0.00000
8.00000+00
9.00000+00
0.00000
0.00000
8.00000+00
8.20000+00
n. ooooo
0.00000
A. 00000+00
9.60000+00
0.00000
n. ooooo
i.onooo+oo
o.onooo
2.7^385+04
o.onoon
1.00000+00
0.00000
2.63523+04
0.00000
1.00000+00
0.00000
2.78132+04
0.00000
1.00000+00
0.00000
2.74031+04
0.00000
i.onooo+oo
0.00000
2.67927+04
0.00000
1.00000+00
0.00000
2.72284+04
0.00000
1.00000+00
0.00000
2.70140+04
0.00000
1.00000+00
0.00000
2.59888+04
o.onooo
1.00000+00
0.00000
3.28530+04
0.00000
l.nnooo+oo
o.onono
2.57651+04
o.onooo
1.00000+00
7.400UO+00
2.00000+00
0.00000
l.UOOOO+00
6.70000+00
1 .00000 + 00
o.ononn
1.00000+00
7.10000+00
2.00000+00
o.ooooo
1.00000+00
7.50000+00
1.00000+00
o.ooono
l.UOOOO+00
7.70000+00
1.00000+00
0.00000
1.00000*00
6.60000+00
2.00000+00
0.00000
1.00000+00
5.10000+00
2.UOOOO+00
0.00000
1.00000+00
i.ieooo+oi
1.00000+00
o.uoooo
1.00000+00
1.10000+01
1.00000+00
o.ooouo
1.00000+00
9.BOOOO+00
1.00000+00
o.nnono

-------
                  TABLE C-3.   (Continued)
FPOMT WftL COAL FIHEl) K
1
2
3
4
1
2
3
<4
1
2
3
it
1
2
3
4
1
2
3
O l»
£ 1
2
3
"
1
2
3
u
1
2
3
it
1
2
3
U
1
?
3
(4
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
in
in
10
10
3
*
3
3
*
3
3
T
3
3
3
1
3
3
3
3
j
3
3
3
3
3
?
3
3
3
3
3
* •
3
3
3
,
TI
*
*
»
*
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
.*,
69
69
69
69
70
70
70
70
71
71
71
71
72
72
72
72
73
73
73
73
74
74
74
74
75
75
75
75
76
76
76
76
77
77
77
77
78
7H
7H
78
1.10000+00
p.opnno
1.57000+02
4.5750P + 0.2
1.30000+00
0.00000
1.61000+02
3.79500+02
1.30000+00
0.00000
1.40000+02
3.25500+02
1.20000+00
0.00000
1.51000+02
5.05000+02
1.30000+00
0.00000
1.28000+02
3.91000+02
1.30000+00
0.00000
1.29000+02
4.93500+02
1.30000+00
'J . 0 0 0 0 0
1.17000+02
3.33500+02
1.4POOO+OU
O.OOOOP
1 .28000+02
6. ?3 000+02
1.40000+00
0.00000
1.22000+02
5.72000+02
1.30000+00
0.00000
1 .07000+02
5 .91 onn+02
f .90100+01
o.onopp
0 . 0 0 P P n
O.OCOOO
S.362rn + m
o.noono
o.onono
O.OOOPO
8.3628P+01
0.00000
o.ooono
o.oonoo
1.33515+0?
o.oooon
O.OOPOO
0.00000
1.31755+02
0.00000
0.00000
o.oonoo
l.SSM'r + O?
o.onooo
O.OOOPO
O.POOPP
1 .29996+09
o.oooon
O.onnpn
0.00000
?.??*?5+U2
o.onoon
0.00000
o.noono
?. 3401.5 + 0?
o.noopo
n . n o n o n
0. (1(1000
?.?p76"- + o?
n . n o n n o
o . n n n p i '
o.ooono
ft ,u9«»6n + ni
4.0 POP') + 01
O.noonn
o.ooono
7.6nflP7+ni
3.760nn+01
2.nnonn+oo
o.noono
7.608«7+01
3.76000+01
2.0PPOO+OU
O.OOOPO
1.21452+02
6.00000+01
O.OOOPO
0.00000
1.19811+0?
5.92000+0*
o.noonn
o.noooo
1.21452+02
6.ooono+oi
2.00000+00
n.ooono
1.18203+02
5.84000+01
2.ooonn+oo
O.OOOOP
2. 023^ + 02
1.00000+02
0.00000
n . u P c n p
?. 137*5 + 02
1 .05600 + 02
n . o o o P o
n . onopo
2 .(I079P + 0?
9.920PP+01
?.ooooo+nn
(i . nncnn
3. 47791+0^
1.57000+0?
o . o P n f j (j
1.40000+01
3.47791+05
1.90900+0?
o.onono
7.8000U+01
3. 47791 + 05
1.60400+02
0.00000
6.10000+01
?. 47791 + 05
1.51000+0?
o.onooo
4.20000+01
3.47791+0^
1.28000+0?
0.00000
o.ooono
?.47791+n5
1.52000+0?
o.ooooo
0.00000
3.47791+05
1.25100+0?
0.00000
0.00000
3.47791+05
1 .28000+0?
0.00000
o.onooo
3.47791+05
i .22onn+o?
0 . 0 0 0 0 U
n.onono
3.477«jl+n5
1 . ? ? 0 0 P + 0 •>
o.ooono
r. . nnonn
P. 00000+00
7.flooon+oo
n.ooono
n.oonoo
4
1 .1 of-nn + nl
l."noon+oo
7,^i>nnn + on
i.i'ponn + oo
o.i.ponn
1. '10000 + 00
H.dOOOn+00
?.OOI1PO + 00
O.noono
1.00000+00
7.nnooo+oo
2.UOOUO+OP
o.c^oono
i.oooon+oo
6.!->POOn + 00
l.ooooo+oo
o.uooon
i.onooo+oo
6.^0000+00
1.00000+00
o.unono
l.UOOOO+OO
6.eoooo+oo
?. jnunp+oo
o.nnnoo
1.1:0000+00
6.?nunn+oo
2.:iP(jOO + 00
o.noonn
1 . CPOOO+OO
6.?nooo4.oo
i .uooon+oo
o."ouno
l.opoon+oo
fl.7ooon+on
i .(in (inn + nn
o.unono
i .( ooon + no
" . r- r o n o + o 0
? . 1 1 n P o n + n P
0 . , POLIO

-------
                  TABLE C-3.   (Continued)
FRONT WALL COAL FIRED BOILTKS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
0 4
1
co
N> 1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
n
1
2
3
4
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10

10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
3
3
3
3
3
3
3
3
3
3
5
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
79
79
79
79
80
80
80
80
81
81
81
81
82
82
82
82
83 .
83
83
63

84
84
64
84
85
85
65
85
86
86
86
86
87
87
87
87
68
68
68
86
1.40000+00
0.00000
1.01000+02
3.76000+02
1.20000+00
0.00000
1.47000+02
6.95000+02
1.20000+00
0.00000
1.38000+02
6.01000+02
1.30000+00
0.00000
1.04000+02
3.98000+02
1.30000+00
0.00000
1.01000+02
3.91000+02

1.30000+00
0.00000
1.66000+02
5.64000+02
1.30000+00
0.00000
1.56000+02
4.27000+02
1.30000+00
0.00000
1.26000+02
3.62000+02
1.30000+00
0.00000
1.22000+02
3.62000+02
1.30000+00
0.00000
1 .65000+02
3.69000+02
?. 20765+02
0.00000
0.00000
0.00000
1.81539+02
0.00000
0.00000
0.00000
1.8b««72+0?
o.onooo
0.00000
0.00000
1.74501+02
0.00000
0.00000
o.oonno
1.76?60+02
0.00000
0.00000
0.00000

1.33515+0?
0.00000
0.00000
0.00000
1.35?74+0?
o.onooo
0.00000
0.00000
1.29996+02
0.00000
o.oooon
O.OOOPO
1.29996+0?
o.noono
o.oonoo
0.00000
8. 36280+01
O.OOOPO
O.OOOPO
O.OOOPO
2.00790+0?
9.92onn+oi
2.00000+00
0.00000
1.65174+02
8.16000+01
n.ooono
0.00000
1.70032+02
8.40000+01
0.00000
0.00000
1.58676+0?
7.84000+01
4.00000+00
0.00000
1.60316+02
7.92000+01
4.00000+00
o.ooonn

1.21452+02
6.00000+01
0.00000
0.00000
6.72243+01
6.naono+oi
0.00000
0.00000
1.18203+02
5.64000+01
2.00000+00
0.00000
1.16203+02
5.84000+01
2.00000+00
o.ooonn
7.60867+01
3.76000+01
0.00000
o.noono
3.47791+05
1.15000+02
u. ooooo
o.onooo
3.47791+05
1.47000+0?
0.00000
0.00000
3.if7791 + 05
1.38000+02
o.onono
o.onooo
3.47791+05
1.39000+02
0.00000
0.00000
3.47791+05
1.35000+02
0.00000
0.00000

3.47791+05
1.68000+02
0.00000
0.00000
3.47791+05
1.560no+0?
0.00000
0.00000
3.47791+05
1.51000+02
o.ooono
0.00000
3.47791+05
1.46000+0?
o.onono
o.ooono
3.47791+05
1.85000+02
n.ooono
n.ooono
1 .40000 + 01
2.90000+00
0.00000
o.ooono
i.6ooon+ni
6.70000+00
n.onooo
0.00000
1.60000+01
5.70000+00
0.00000
0.00000
1.20000+01
5.70000+00
0.00000
0.00000
1.20000+01
5.30000+00
0.00000
0.00000

1.20000+ni
8.50000+00
0.00000
0.00000
1.20000+01
7.50000+00
0.00000
0.00000
1 .00000+01
7.00000+00
o.oonoo
n.ooono
1.00000+01
6.60000+00
o.ooono
n.oonno
8.00000+00
9.6000P+00
n.ooono
0.00000
1.00000+00
o.onooo
2.66999+04
6.76000+00
1.00000+00
0.00000
?.84423+04
1.02100+01
1.00000+00
0.00000
2.76967+04
1.01800+01
1.00000+00
0.00000
2.78482+04
1.03100+01
1.00000+00
0.00000
2.84377+04
1.03800+01

1.00000+00
0.00000
2.84120+04
7.27000+00
1.00000+00
0.00000
2.82792+04
4.67000+00
1.00000+00
0.00000
2.62769+04
6.71000+00
i.noooo+oo
o.noooo
2.7*764+04
9.260PO+00
i.oonon+no
o.onnon
?.e>67?6 + 04
4.86000+00
l .onoon+oo
5.70000+00
2.00000+00
o.uooon
i. onoon+oo
5.7POOO+00
i.unooo+oo
o.uoooo
1 .00000 + 00
6.50000+00
1.00000+00
o.ooooo
1.00000+00
7.10000+00
2.00000+00
o.ooono
I.OOOUQ+OO
7.90000+00
2.00000+00
o.oooon

1.00000+00
7.10000+00
i.onooo+no
o.oonoo
i.oooon+oo
e.2nooo+oo
l.UOOOO+00
0.00000
1.00000+00
1.06000+01
2.00000+00
o.onono
1 .00000+00
9.90000+00
2.00000+00
o.coono
1 .00000+00
4.t>ooon+on
i.t'nono + oo
u.'iooon

-------
          TABLE  C-3.   (Continued)
WALL COflL  FIRED  BOII.FPS
1
2
3
4
1
2
3
4
1
2
3
4
I
2
3
i*
1
2
3
0 *
1
00 1
oo *
2
3
4
1
2
3
4
1
2
3
H
1
2
3
U
1
2
3
>*
10
10
10
10
10
10
10
10
10
10
10
10
11
11
11
11
11
11
11
11

11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
3
3
3
3
3
y
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
jl
3
3
3
3
»
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
89
09
69
89
90
90
90
90
91
91
91
91
92
92
92
92
93
93
93
93

9«»
94
94
9«*
95
95
95
95
96
96
96
96
97
97
97
97
9ft
9fl
98
98
1.30000+00
0.00000
1.74000+02
3.11000+02
1.30000+00
0.00000
1.16000+02
2.67000+02
1.30000+00
0.00000
1.090004-02
2.75000+02
1.21000+00
0.00000
1.23000+02
5.97000+02
1.21000+00
0.00000
1.17000+02
5.02000+02

1.21000+00
0.00000
1.13000+02
4.41000+02
1.21000+00
o.noooo
1.12000+02
4.09000+02
1.21000+00
0.00000
1.01000+02
4.66000+02
1.21000+00
0.00000
1.35000+02
6.60000+02
1.21000+00
o.onono
1.16000+02
4.62000+02
fl. 36280+01
0.00000
o.nnopo
o.oooon
9. 25290+01
0.00000
0.00000
O.OOOPO
9.4^920+01
0.00000
0.00000
0.00000
?. 15383+0?
o.oonoo
0.00000
0.00000
2,10105+02
0.00000
0.00000
0.00000

2.22525+02
0.00000
0.00000
0.00000
2.22525+02
o.ooono
0.00000
0.00000
2.15383+0?
0.00000
0.00000
0.00000
l.ftl«539 + 0?
o.oooon
o.nonoo
0.00000
1.74501+02
0.00000
1) . 0 0 0 0 0
o . o r P n n
7.6o*fl7+ol
3.76000+01
0.00000
0.00000
8.41960+01
4. 16000+01
2.00000+00
0.00000
8.580i*9+01
4.24000+01
2.00000+00
0.00000
1.95932+02
9.66000+01
o.ooono
o.noooo
1.91074+02
9.44000+01
0.00000
o.ooooo

2.023el9+02
1.00000+02
0.00000
0.00000
2.02399+0?
j.00000+02
0.00000
0.00000
1.95932+0?
9.66onn+oi
2.00000+00
0.00000
1.65143+0?
a.lf.000 + 01
o.ooono
o.oooon
1.58f.76 + nP
7.f"4onn + oi
o. ononn
o.nouno
3.47791+05
1.7*000+02
0.00000
0.00000
3.47791+05
1.55000+0?.
0.00000
0.00000
3.47791+05
1.H5000+02
0.00000
0.00000
3.'»7791 + 0'5
1.23000+02
0.00000
0.00000
3.47791+05
1.17000+02
0.00000
0.00000

3. 47791+05
1.13000+02
0.00000
0.00000
3.47791+05
1 .12000+0?
P. 00000
0.00000
3.47791+05
1.15000+02
0.00000
0.00000
3.47791+05
1.35000+0?
0.00000
n. ooooo
5.47791+0^
1.16000+0?
n. onooo
0. 001)00
P. 00000+00
9.10000+00
0.00000
n.ooooo
6.00000+00
9.10000+00
0.00000
0.00000
6.00000+PO
a. 30000+00
o.oonoo
o.ooooo
1.60000+01
4.00000+00
0.00000
0.00000
1.60000+ni
3.20000+00
0.00000
n.ooooo

1.6(1000 + 01
2.50000+00
0,00000
0.00000
1,60000+01
2.40000+00
0.00000
0.00000
i.4oooo+nl
3.00000+00
0.00000
0.00000
1 .60000+01
5.5000P+00
0.00000
o.ooooc
i .feonon+nl
3.00POO+00
o.connn
o.ooonr
l.onooo+oo
o.oooon
2.98496+04
4.52000+00
1.00000+00
0.00000
2.«4819+04
5.71000+00
1.00000+00
0.00000
2.91110+04
5.11000+00
1.00000+00
0.00000
2.79903+04
0.00000
1.00000+00
0.00000
2.79903+04
0.00000

1.00000+00
0.00000
2.66272+04
7.48000+00
1.00000+00
0.00000
2.86963+04
7.46000+00
1.00000+00
o. onooo
2.79903+04
0.00000
l.onooo+oo
o. onooo
2.7
-------
                    TABLE C-3.   (Continued)
FRONT  MLL COftL FIRED  ROILCHS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
o *
i
£ i
2
3
*
1
2
3
4
1
2
3
*
1
2
3
4
1
2
3
4
11
11
11
11
11
11
11
11
12
12
12
12
12
12
12
12
12
12
12
12

12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
12
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
J
?
3
3
3
3
3
3
3
3
i
3
S
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
99
99
99
99
100
100
100
100
101
101
101
101
102
102
102
102
103
103
103
103

104
104
10H
104
105
105
105
105
106
106
106
106
107
107
107
107
108
108
108
108
1.21000+00
0.00000
9.40000+01
3.29000+02
1.21000+00
0.00000
6.60000+01
3.02000+02
1.53000+00
0.00000
1.22000+02
1.38300+03
1.53000+00
0.00000
1.09400+02
1.14700+03
1.52000+00
0.00000
1.23500+02
1. 31900+03

1.52000+00
0.00000
1.29500+02
1.25600+03
1.52000+00
0.00000
1.44200+02
9.06000+02
1.52000+00
0.00000
1.30000+02
7.78000+02
1.52000+00
0.00000
1.08000+02
7.71000+02
1.52000+00
o.onooo
6. 30000+01
3.4100n+02
1.76?60+02
0.00000
0.00000
0.00000
1.79779+0?
o.oooon
0.00000
o.onooo
1.56492+0?
0.00000
0.00000
0.00000
1.53387+0?
o.ooono
0.00000
o.ooono
1.53387+02
0.00000
0.00000
o.oooon

1.48108+02
0.00000
0.00000
o.oooon
7.99020+01
0.00000
0.00000
0.00000
7.99020+01
o.ooono
0.00000
o.oooon
6.01090+01
0.00000
0.00000
o.oooon
S.01090+01
o.oonoo
o.nooon
o.noorn
1 .60265+02
7.92000+01
4.00000+00
o.oooon
1.63534+0?
e. oeono+oi
4.00000+00
0.00000
1.59023+02
1.09600+02
0.00000
0.00000
1.55837+0?
1.07400+02
o.ooono
0.00000
1.55837+0?
1.07400+02
0.00000
o.oooon

1.50442+0?
1.03700+n2
0.00000
o.ooono
8.11361+01
5.593nn+01
0.00000
o.oooon
8.11361+01
5.593no+0l
o.onono
0.00000
e.i42nn+ni
5.61?no+0l
8.00000+OU
o.ooonn
8.i4?nn+ni
5.M?nn+nl
w.noono+oo
o.oonon
3. 47791+05
1.250nO+02
o.onooo
o.ooonn
3.47791+05
1.17000+0?
0.00000
o.onooo
7.80259+05
1.22000+02
0.00000
0.00000
7.80259+05
1.09400+02
0.00000
0.00000
7.80259+05
1.23500+0?
0.00000
0.00000

7.80259+05
1.29500+0?
0.00000
o.onooo
7.80259+05
1.14200+0?
o.ooono
o.onono
7.80259+05
i.3oono+o?
0.00000
o.onono
7.80259+05
1.62900+0?
0.00000
n. ooooo
7.60259+oR
l.?5000+0?
o.onnoo
n.onono
1 ,20000 + nl
4.50000+00
0.00000
o.oooon
1.20000+01
3.30000+00
n. ooooo
0.00000
2.40000+01
3.90000+00
n. ooooo
1.12660+03
2.40000+01
1.86000+00
0.00000
0.00000
2.400on+ni
4.10000+00
0.00000
0.00000

2. 40000+01
4.90000+00
0.00000
n. ooooo
1.60000+01
6.60000+00
0.00000
0.00000
1.80000+01
4.98000+00
0.00000
o.ooono
1.60000+01
6.21000+00
0.00000
o.oonoo
1.60000+01
4.29oon+no
n.ooono
n.nnono
l.onooo+00
o.ooono
2.79903+n4
0.00000
l.onooo+oo
o.onooo
2.79903+04
0.00000
2.00000+00
0.00000
3.21983+04
0.00000
2.00000+00
o.onooo
3.21983+04
o.onooo
2.onnoo+no
o.onooo
3.19117+04
0.00000

2.00000+00
0.00000
3.19117+04
0.00000
2.00000+00
0.00000
3.19117+04
0.00000
2.onooo+oo
0.00000
3.19117+04
0.00000
?.onopo+oo
o.onono
3.19117+04
o.onono
2.nnooo+on
o.ouono
3.19117+04
o . o n o (MI
1 .UOOOO+00
1.07500+01
?. UOOOO+00
o . (/ o o n o
1.00000+00
1.07500+01
2.00000+00
o.unooo
o.ooono
6.o?oon+on
1.00000+00
n.oooon
o.uoono
6.U2000+00
i.oooon+oo
o.unooo
0.00000
6.32000+00
1.00000+00
o.onooo

o.ooooo
6.32000+00
1.00000+00
o.ooono
o.noono
6.3?000+00
1. UOOOO+00
o.uoono
o.ooooo
6.32000+00
1.00000+00
o.onoon
o.ooooo
6.3?000+00
2.00000+00
o.ononn
0 . i) 0 0 0 0
f>.-5?000 + 00
2.i'oonn+on
0 . P (1 0 0 0

-------
                    TABLE  C-3.   (Concluded)
FdONT WflLL  COAL FIRE.D BOILFRS
1 12
2 12
3 12
«» 12
1 12
2 12
3 12
<< 12
1 12
2 12
3 12
4 12
1 12
2 12
3 12
* 12
1 12
2 12
0 3 12
' 4 12
CO
Ol
1 12
2 12
3 12
4 12
1 12
2 12
3 12
4 12
1 12
2 12
3 12
4 12
3
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3


3
V
3
3
3
3
3
3
3
3
3
3
3 109
3 109
3 109
3 109
3 110
3 110
3 110
3 110
3 111
3 111
3 111
3 ]11
3 112
3 112
3 112
3 112
3 113
3 113
3 J13
3 113


3 114
3 114
3 im
3 114
3 115
3 115
3 115
3 115
3 116
3 116
3 116
3 116
1.52000*00
0.00000
9.73000*01
7.6900P+02
1.52000400
0.00000
8.00000*01
3.86000*02
1.52000*00
0.00000
1.36000*02
1.13600*03
1.52000*00
0.00000
1.17000*02
1.01900*03
1.52000*00
0.00000
1.17500*02
9.36000*02


1.52000*00
0.00000
1.23000*02
7.14000+02
1.52000*00
0.00000
9.93000*01
6.89000+02
1.52000*00
0.00000
1.20000+01
3.62000+02
1.15?99+02
o.ooono
0.00000
0.00000
1.15299*02
0.00000
o.ooono
O.OOPOO
1.25*56+02
0.00000
o.noooo
0.00000
1.22751+02
0.00000
0.00000
0.00000
1.19542+0?
0.00000
0.00000
o.ooono


8.72505*01
0.00000
0.00000
0.00000
fl.56P8p+ni
o.noooo
0.00000
o.ooono
8.569BO+01
o.ooonn
o.nonno
o.onono
1 .17130+0?
s. 07400+ni
8.00000+00
0.00000
1.17130+02
8. 07100 + 01
8.00000+00
0.00000
1.278ft7+02
8.81500+01
0.00000
0.00000
1.24669+0?
8.59300+01
0.00000
0.00000
1. 21452+02
P.370no+01
0.00000
o.ooono


8. 86755+01
6.11100+01
0.00000
0.00000
fl. 70667+01
6.00000+01
8.00000+00
o.ooono
8.70667+01
6. OOOPn.,.01
fi.ooonn+oo
o.ooono
7.80259 + 01?
1.46000+0?
0.00000
o.ooono
7.80259+05
1.20000+0?
O.OOOOU
0.00000
7.80259+05
1.38000*02
0.00000
0.00000
7.80259+05
1.17000*02
n. ooooo
0.00000
7.80259*05
1.17500+02
0.00000
0.00000


7.80259*05
1.23000+02
0.00000
o.onono
7.80259+05
1.49000+02
0.00000
o.noono
7.80259+05
1.23000+02
0.00000
0.00000
l.6onoo+ni
6.78000+nO
0.00000
o.ooono
1.60000+01
3.60000+00
0.00000
n. ooooo
2. 40000+01
5.86000+00
0.00000
0.00000
?. 40000 + 01
3.15000+00
n. ooooo
0.00000
1.80000+01
3.22000*00
0.00000
0.00000


1.80000*01
4.00000+00
0.00000
0.00000
1.60000+01
7.02000+00
n. ooooo
0.00000
1.60000+01
4.16000+00
0.00000
o.ooono
2.00000+00
o.nnono
3.1e»117 + 04
o.ooono
2.00000+00
O.OOOPO
3.19117+04
0.00000
2.00000+00
0. (10000
3.19117+04
o.noooo
2.00000+00
o.onooo
3.19117+04
0.00000
2.00000+00
0.00000
3.19117+04
0.00000


2.00000+00
0.00000
3.19117+04
o.noooo
2.00000+00
0.00000
3.19117+04
o.onooo
2.00000+00
o.onooo
3.19117+04
o.onooo
o.onooo
6.32onn+oo
2.unoop+oo
o.onoon
0.00000
6.??oon+oo
2.00000+00
o.cnonn
0.00000
6.32000+00
1.00000+00
o.uoono
o.ooono
6.32000+00
1.00000+00
o.onooo
0.00000
6.32000+00
1.00000+00
o.ooooo


o.ooono
6.32000+00
1.00000+00
0.00000
0.00000
6.32000+00
2.ooooo+on
o.noooo
o.oooon
6.32000+00
2.00000+00
o.ooono

-------
TABLE C-4.  N0  CONTROL TEST DATA FROM OPPOSED WALL OIL-FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
i«
1
2
0 3
1 4
CO
CT>
1
2
3
it
1
2
3
4
1
2
3
U
1
2
3
it
1
2
3
4












1
1
1
1
1
1
1
1

1
1
1
1
1
1
I
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
?
2
?
2
2
2
2
2
2
2
2

2
2
2
2
2
?
2
2
?
2
2
?
?
2
2
2
2
2
2
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2

2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
1
1
1
1
2
2
2
2
3
3
3
3
4
«»
4
4
5
5
5
5

6
6
6
6
7
7
7
7
8
e
6
a
9
9
9
9
10
10
10
10
4.60000-01
0.00000
1.06700+02
"4.1*2000 + 02
4.60000-01
0.00000
8.20000+01
3.08000+02
4.60000-01
0.00000
7.30000+01
2.92000402
4.60000-01
0.00000
5.50000+01
2.84000+02
4.60000-01
0.00000
1.06000+02
2.20000+02

4.60000-01
0.00000
A. 30000+01
1.73000+02
4.60000-01
0.00000
7.40000+01
1.52POO+02
4.60000-01
0.00000
5.67000+01
1.18000+02
2.50000-01
0.00000
1.27600+02
2.46000+02
2.50000-01
o.oonoo
1.19800+02
2.23000+02
?. 9*871+0?
0.00000
0.00000
0.00000
2.95803+0?
0.00000
0.00000
0.00000
2.96631+02
0.00000
o.oooon
0.00000
2.97562+02
0.00000
0.00000
0.00000
1.30514+02
0.00000
0.00000
0.00000

1.27823+02
0.00000
0.00000
0.00000
1.30514+02
0.00000
O.OOOOP
0.00000
1.31445+02
0.00000
0.00000
0.00000
2.68065+0?
0.00000
0.00000
o.oooon
2.68065+0?
O.OOOPO
0.00000
0.00000
6.21202+02
9.94000+01
0.00000
0.00000
6.23095+0?
9.97000+01
0.00000
0.00000
6.24956+02
1.00000+02
8.00000+00
0.00000
6.26849+02
1.00300+02
8.00000+OU
0.00000
2.74986+02
4.40000+01
0.00000
0.00000

2.69370+0?
4.31000+01
0.00000
0.00000
2.74986+02
4.40000+01
8.00000+00
o.ooono
2.76847+02
4.43000+01
8.00000+00
0.00000
5.35H92+0?
9.45800+01
0.00000
0.00000
5.35492*0?
9.45800+01
0.00000
0.00000
9.22950+05
1.06700+02
0.00000
5.30000+01
9.22950+05
1.09000+02
0.00000
6.60000+01
9.22950+05
1.08800 + 0?.
0.00000
9.20000+01
9.22950+05
1.10900+02
0.00000
6.10000+01
9.22950 + 0*>
1.08000+02
0.00000
6.00000+01

9.22950+05
1.10600+02
0.00000
5.90000+01
9.22950+05
1.11100+02
0.00000
5.20000+01
9.22950+05
1.13400+02
0.00000
5.90000+01
1 .29887+06
1.27600+0?
0.00000
1.50000+01
1.29887+06
1.19600+0?
0.00000
2.00000+01
?. 40000+01
1.40000+00
O.OOOPO
0.00000
2.40000+01
1.80000+00
0.00000
0.00000
1.60000+01
1. 80000+00
O.OOOPO
0.00000
1.60000+01
2.20000+00
0.00000
0.00000
2.40000+01
1.70000+00
0.00000
0.00000

2.40000+01
2.10000+00
0.00000
0.00000
1.60000+01
?. 20000+00
0.00000
0.00000
1.60000+01
2.60000+00
0.00000
0.00000
1.60000+01
4.70000+00
0.00000
0.00000
1.60000+01
3.60000+00
0.00000
0.00000
i.onooo+oo
o.onooo
4.37411+04
0.00000
1.00000+00
0.00000
4.37411+04
0.00000
1.00000+00
0.00000
4.37411+04
0.00000
1.00000+00
0.00000
4.37411+04
0.00000
1.00000+00
0.00000
4.37411+04
0.00000

1.00000+00
0.00000
4.37411+04
0.00000
1.00000+00
0.00000
4.37411+04
0.00000
1.00000+00
0.00000
«». 37411 + 04
0.00000
1.00000+00
0.00000
4.50040 + 1)4
0.00000
1.00000+00
0.00000
4.50040+04
0.00000
o.ooooo
o.uouun
1. "0000+00
o.noooo
o.uoooo
0. (10000
3.110000 + 00
0.00000
0.00000
0.00000
2. 00000+00
0.00000
0.00000
0.00000
4.00000+00
o.ooooo
o.uoooo
0.00000
1.00000+00
o.ooooo

o.ooooo
O.UOOOO
3.00000+00
o.ooooo
0.00000
0.00000
2.00000+00
0.00000
o.ooooo
0.00000
4.00000+00
o.nnooo
l.onooo+oo
o.ooooo
1 .00000+00
0.00000
l.unooo+oo
n.oooon
l .unooo + oo
o.unoon

-------
                     TABLE C-4.  (Continued)
HOPIZONTALLY  OPPOSED  OIL  FIRfO EiOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
3
0 4
CO
-J 1
2
3
4
1
2
3
1
2
3
4
1
2
3
1
3
4
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
11
11
11
11
12
12
12
12
13
13
13
13
1*
14
It
15
15
15
15
16
16
16
16
17
17
17
17
18
18
18
18
19
19
19
19
20
20
20
20
2.50000-01
0.00000
9.50000+01
2.00000+02
2.50000-01
O.OPOOO
1.32000+02
2.19000+02
2.50000-01
0.00000
1.20000+02
1.83000+02
2.50000-01
0.00000
9.50000+01
1.64000+02
2.50000-01
o.onooo
9.20000401
1.63000+02
t. 20000-01
o.oonoo
1.21300+02
2.91000+02
«. 20000-01
0.00000
1.13300+02
2.35000+02
<*. 20000-01
0.00000
1.43000+02
3.19000+02
4.20000-01
0.00000
1.32000+02
2.93000+02
4.20000-01
0.00000
1.3500n+02
3.06000+02
2.70963+0?
o.onooo
o.oonno
o.ooooo
0.00000
0.00000
o.ooono
2.17246+02
0.00000
0.00000
0.00000
2.11347+02
0.00000
0.00000
0.00000
2.17246+02
0.00000
0.00000
0.00000
2.6144J+02
0.00000
0.00000
0.00000
2.60199+02
0.00000
0.00000
0.00000
1.46142+02
0.00000
o.ooonn
0.00000
1.4490n+02
o.oonno
O.OOOPO
o.oooon
1.829fl«+02
o.onooo
o.oooon
o.nncno
5. 4J422+02
9.56300+01
O.OOOOP
O.ooono
4.29308+02
7.58300+01
o.ooono
0.00000
4.34072+02
7.66700+01
0.00000
0.00000
4.22242+02
7.45800+01
0.00000
0.00000
4.34072+02
7. 66700+01
0.00000
0.00000
5.21632+02
1. 00000+0*
0.00000
0.00000
5.19498+02
9.95500+01
0.00000
0.00000
2.91768+02
5.59100+01
n.ooono
0.00000
2.89371+02
5.54500+01
o.nooon
o.ooono
3.65270+0?
7.nooon+ol
o.ooonn
o.ooono
1.29887+06
1.26900+02
0.00000
2.10000+01
1.29887+06
1.32000+02
0.00000
1.90000+01
1.29887+06
1.20000+02
0.00000
1.90000+01
1.29887+06
1.26900+02
0.00000
2.10000+01
1.29887+06
1.22500+02
0.00000
2.10000+01
6.34931+05
1.21300+02
0.00000
1 .90000+01
6.34931+05
1.13300+03
0.00000
1 .90000+01
6.34931+05
1.43000+02
0.00000
2.20000+01
6.34931+05
1.32000+02
0.00000
2.00000+01
6.34931+05
1.35000+0?
0.00000
1 .20000 + 01
1.60000+01
4.60000+00
0.00000
0.00000
1.60000+01
5.30000+00
o.oonoo
n.ooono
1.60000+01
3.60000+00
0.00000
0.00000
1.60000+01
4.60000+00
0.00000
0.00000
1.60000+01
4.00000+00
0.00000
0.00000
2.40000+01
3.90000+00
0.00000
0.00000
2.40000+01
2.60000+00
0.00000
1.29000+03
2.40000+01
6.60000+00
0.00000
0.00000
2.40000+01
5.30000+00
0.00000
n. ooooo
2.40000+01
5.70000+00
0.00000
n. ooooo
l .onooo+oo
o.onoon
4.50040+04
o.onooo
1. onooo+oo
o.onooo
4.5nn4o+n4
o.onooo
1.00000+00
o.ooooo
4.500*0+04
0.00000
1.00000+00
o.onooo
4.500*0+04
0.00000
l. onooo+oo
0.00000
4.50040+04
0.00000
1.00000+00
0.00000
4.42467+04
0.00000
1.00000+00
0.00000
4.42467+04
0.00000
1. 00000 + 00
o.onooo
4.41906+04
o.onooo
l.noooo+oo
o.onooo
4.41906+04
o.ooono
1. 00000 + 00
o.ooono
4 . '« 1 9 n o + n '*
o . o n (i n o
i.onoon+oo
o.unono
3.UOOOO+00
o.ooooo
1.00000*00
o.uoooo
i.onono+oo
o.onono
i.oooon+on
o.ooono
1.00000+00
o.ononn
1.00000+00
o.ooooo
3.00000+00
o.oooon
1.00000+00
o.uoono
3.00000+00
0.00000
1.00000+00
o.uoooo
1.00000+00
0.00000
1.00000+00
o.ooooo
l.UOOOO+00
o.onooo
1.00000+00
o.uoooo
1.00000+00
o.ooooo
1.00000+00
o.oroon
i. onooo+oo
o.onono
T .nnonn + oo
o.iio on n
l .ippoon+on
(i.nnunn

-------
                   TABLE  C-4.   (Continued)
HORIZONTALLY OPPOSED OIL  FIRED BOILERS
1
2
3
•4
1
2
3
14
1
2
3
4
1
2
3
<4
1
2
3
0 4
to
CO 1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
14
3
3
3
3
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
5
5
5
5
5
5
5
5
5
5
5
5
?
2
2
2
2
2
?
2
9
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
?
2
?
2
2
?
2
2
2
2
?
?
2
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
21
21
21
21
22
22
22
22
23
23
23
23
24
24
24
2t
25
25
25
25
26
26
26
26
27
27
?7
27
28
28
28
28
29
29
29
29
30
30
30
30
4.20000-01
0.00000
1.01000402
1.72000+02
2.60000-01
2.43840400
1.21000402
2.97400402
2.60000-01
2.43840400
9.10000401
2.55800402
2.60000-01
2.43840400
1.23000402
2.49200402
2.60000-01
2.43840400
8.70000401
2.17500402
2.60000-01
2.43840400
1.29000402
2.62400402
2.60000-01
2.43840400
8.60000401
2.22100402
2.60000-01
2.43840400
1.22000402
3.04000402
2.60000-01
2.43840400
9.45000401
2.49100402
2.60000-01
2.43840400
1.26000402
2.63200402
1.9012940?
o.oooon
o.ooono
0.00000
2.5243740?
2. 13360400
5.00000400
0.00000
2.52437402
2.13360400
5.00000400
0.00000
1.89819402
2.1336P400
1.40000401
0.00000
1.89819402
2.13360400
1.40000401
0.00000
1.58666402
2.13360400
1 .70000401
0.00000
1.58666402
2.13360400
1. 70000401
0.00000
?. 62476402
2.13360400
0.00000
o.oooon
2.62476402
2.13360400
o.oooon
o.ooonn
2.14452402
2. 13360400
1.10000401
o. oonno
3.79*29402
7.27300401
(,.00000400
o.ooonn
1.92304+02
9.41700401
o.ooono
0.00000
1. 92304402
9.41700401
0.00000
0.00000
1.44638402
7.08300401
0.00000
0.00000
1.44638402
7.08300401
0.00000
0.00000
1.20821402
5.91700401
o.ooono
0.00000
1.20821402
5.91700401
0.00000
0.00000
1.99970402
9.79200401
0.00000
o.ooonn
1.99970402
9.79200401
n.ooonn
0.00000
1 .63376402
8. 00000401
o.ooono
0. 00000
6.34931405
1.35200402
0.00000
1.60000401
5.69006405
1.21000402
0.00000
0.00000
5.69006405
1.21500402
0.00000
0.00000
5.6900640^
1.23000402
0.00000
0.00000
5.69006405
1.21900402
0.00000
0.00000
5.69006405
1.29000402
0.00000
0.00000
5.69006405
1 .29100402
0.00000
0.00000
5.69006405
1.2200040?
0.00000
0.00000
5.69006+05
1.25400402
0.00000
0.00000
5.69006*05
1.26000402
n. ooooo
0.00000
1 .80000401
5.70000400
0.00000
0.00000
1.20000401
3.75000400
0.00000
0.00000
1.20000401
3.90000400
0.00000
0.00000
1.00000401
4.10000400
0.00000
0.00000
1.00000401
3.95000400
0.00000
0.00000
8.00000400
4.95000400
0.00000
0.00000
8.00000400
4.95000400
0.00000
0.00000
1.20000401
3.95000400
0.00000
0.00000
1.20000401
4.45000400
0.00000
0.00000
1.20000401
4.45000400
0.00000
n.oonoo
1.00000400
o.onooo
4.41908404
0.00000
1.00000400
O.onooo
4.56C>17404
0.00000
1.00000400
0.00000
4.56517404
0.00000
1.00000400
0.00000
4.56517404
o.ooono
1.00000400
o.onooo
4.56517404
0.00000
1.00000400
0.00000
4.56517+04
0.00000
i.nnoo0400
o.oonoo
4.56517+04
o.onooo
1.00000400
0.00000
4.56517+04
0.00000
1.00000400
o.onono
4.56517404
o.noono
l.nnooo+no
O.oonoo
4.56517+04
o.onooo
l.ooonn+oo
o.ooonn
2.00000400
o.noono
o.ooonn
0.00000
5.U0000400
o.ooooo
0.00000
o.onooo
7.00000400
o.oooon
0.00000
0.00000
5.00000400
o.ooooo
o.uoooo
0.00000
7.00000400
o.uoooo
o.ooono
o.ooono
5.UOOOO+00
o.ooono
0.00000
o.ooooo
7.00000400
o.ooooo
o.ooooo
o.ooooo
1.00000400
0.00000
o.ooono
o.ooooo
3.onooo400
o.ooooo
0 . U 0 0 0 0
O.cnooo
5.U0000400
i) . o o o o n

-------
                    TABLE C-4.   (Continued)
HORI70NTHLLY  OPPOSED OIL  FIRED BOILERS
1
2
3
4
1
2
3
i«
1
2
3
4
1
2
3
4
1
2
3
0 «
CJ
V£> j
2
3
"
1
?
3
if
1
2
3
4
1
2
3
4
1
2
3
4
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5

6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
2
2
?
?
2
2
2
?
?
2
2
2
2
2
2
2
2
2
2
2

2
?
2
2
2
2
2
?
2
?
2
2
?
2
?
2
2
?
p
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2

2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
31
31
31
31
32
32
32
32
33
33
33
33
34
34
34
34
35
35
35
35

36
36
36
36
37
37
37
37
36
38
38
38
39
39
39
39
40
40
40
40
2.60000-01
2.43fl40+00
9.70000+01
2.47400+02
2.60000-01
2.43A4Q+00
1.26000+02
2.33100+02
2.60000-01
2.43840+00
fl. 50000+01
2.01100+02
2.60000-01
2.43640+00
1.35000+02
2.16700+02
2.60000-01
2.43840+00
ft. 30000+01
2.05400+02

2.60000-01
1.11862+00
1.16000+02
4.21300+02
2.60000-01
1.11862+00
1.06000+02
2.96900+02
2.60000-01
1.11862+00
7.10000+01
2.39000+02
2.60000-01
1.11862+00
1.05000+02
3.54JOO+02
2.60000-01
1.11862+00
1.04000+02
2.61300+02
2.14452+02
2.13360+00
1.10000+01
0.00000
1.59700+02
2.13360+00
2.50000+01
0.00000
1.58666+02
2.13360+00
2.50000+01
o.ooono
1.00498+02
2.13360+00
5. 60000+Ox
0.00000
1.00498+02
2.13360+00
5.60000+01
0.00000

2.55645+02
?. 871*26 + 00
0.00000
0.00000
2.55645+0?
2.871*26 + 00
0.00000
0.00000
2.55*45+02
?.fl7t»2* + 00
0.00000
0.00000
?. 55645+0?
2.«7i»26+0n
0.00000
o. oonoo
?. 54196 + 0?
?./»7<»?f, + on
n.nooon
o. oonoo
1.63376+n?
8.00000+01
o.noooo
o.oooon
1.21673+02
5.95800+01
0.00000
o.ooonn
1.20821+02
5.91700+01
o.ooono
O.OOOOO
7.65935+01
3.75000+01
0.00000
o.ooooo
7.6593-i + Ol
3.75000+01
0.00000
0.00000

4.16753+02
1.00000+02
0.00000
0.00000
4.16753+02
1.00000+02
0.00000
0.00000
4.16753+02
1.00000+0?
ft. 00000+00
o.oooon
4.16753+0?
i.ooono+02
0.00000
0.00000
4.14387+02
9.9i*3on + 01
0.00000
o.ooono
5.69006+05
1.2*400+0?
0.00000
0.00000
5.69006+05
1.26000+0?
0.00000
0.00000
5.69006+05
1.26000+02
0.00000
0.00000
5. 69006+05
1.35000+02
0.00000
0.00000
5.69006+05
1.38000+02
0.00000
0.00000

8.438i»0 + 0">
1.16000+02
0.00000
0.00000
6.43840+05
1.08000+02
o.ooono
1.85600+01
8.43840+05
1.15700+02
0.00000
0.00000
8.438i*0 + 05
1.14100+02
0.00000
0.00000
8.4381*0 + 05
1. 1/>?00 + 02
0 .00000
2.<»2onn+oi
1.20000+01
4.85000+00
O.OOOPO
o.oooon
8.00000+00
4.55000+00
o.ooooo
0.00000
6.00000+00
4.80000+00
0.00000
0.00000
6.00000+00
5.63000+00
0.00000
0.00000
6.00000+00
6.10000+00
0.00000
o.onooo

2.40000+01
3.10000+00
0.00000
0.00000
2.40000+01
1.60000+00
0.00000
0.00000
1.60000+01
3.00000+00
0.00000
0.00000
2.40000+01
2.70000+00
0.00000
0.00000
2.40000+01
2. 40000+00
n. oonoo
n. ooooo
l.onooo+oo
o.nonon
4.56517+04
o.onono
1. 00000+00
0.00000
4.56517+04
o.onooo
1.00000+00
0.00000
4.56517+04
0.00000
1.00000+00
0.00000
4.56517+04
o.onooo
1.00000+00
0.00000
4.56517+04
0.00000

1.00000+00
o.onooo
4.56517+04
o.ooooo
1.00000+00
0.00000
4.56517+04
o.onooo
1.00000+00
0.00000
4.56517+04
o.onooo
l.onooo+oo
o.noooo
4.5*517+04
o.ooono
i.nnoon+oo
o.npoou
4.5f.«Sl7+»14
o . n n o n (i
o.ooono
U. 00000
7.00000+00
o.ooono
o.nnooo
o.uooro
5.00000+00
o.ooono
o.ooooo
0.00000
7.00000+00
o.ooono
o.uoooo
o.uoooo
5. 00000+00
o.ooooo
0.00000
o.ooooo
7.00000+00
o.oooon

0.00000
o.onooo
1.00000+00
0.00000
o.oooon
o.uooon
1.00000+00
o.ooono
o.ooooo
o.uoooo
4.uooon+oo
o.ooono
o.oooon
o . o o o P n
3. 00000+00
o.ooonn
o.upoon
o.nnooo
j.'ioono+oo
n . n n o n n

-------
                   TABLE C-4.  (Continued)
HORIZONTALLY OPPOSED OIL  FIRFO  BOILFTKS
1
2
3
4
1
2
3
<«
1
2
3
<«
1
2
3
4
1
2
5
4
1
2
3
4
1
2
3
i»
1
2
3
H
1
2
3
4
1
?
3
14
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
2
?
2
?
?
2
2
2
?
2
2
2
2
2
2
2
2
9
2
2
?
2
2
2
2
?
2
2
?
?
3
2
2
2
?
2
2
?
7
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
<«1
4]
4]
ooon+oi
0.00000
1.117BO+02
?.«742ft+00
3.60000+01
0.00000
1.09f,06 + 02
2.87426+00
3.4000H+01
0.00000
1.12504+02
2.87426+00
3.20000+01
0.00000
1.44590+02
2.87426+00
2.70000+01
0.00000
2.54196*02
2.87426+00
0.00000
O.OOOPO
2.52022+02
?. 87426+00
0.00000
0.00000
2.54196+02
2.87426+00
0.00000
0.00000
2.5«H96+0?
2.8742f,+00
0.00000
0.00000
?.5<*196 + 0?
?.87
-------
                   TABLE C-4.   (Concluded)
HORIZONTALLY opposro OIL  FIRFD POILEKS
1
2
3
it
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
0
i, 1
"-• 2
3
4
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7

7
7
7
7
2
?
?
2
2
9
2
2
2
?
2
2
2
2
2
2
2
2
2
?

2
?
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2

2
2
2
2
51
51
51
51
52
52
52
52
53
53
53
53
54
54
54
54
55
55
55
55

56
56
56
56
2.60000-01
1.11662+00
7.30000401
2. 21*00+02
2.60000-01
1.11862+00
1. 18000+02
3.31400+02
2.60000.01
1.11862+00
1.10000+02
2.63600+02
2.60000-01
1.11662+00
7.00000+01
1.40400+02
2.60000-01
1.11862+00
1.15000+02
2.60000+02

2.60000-01
1.11862+00
1.06000+02
2.26600+02
?. 55645+02
2.87426+00
o.oonon
0.00000
1.09606+0?
2.87426+00
3.60000+01
0.00000
1.09606+02
2.67426+00
4.00000+01
o.oooon
1.09606+02
2.67426+00
4.70000+01
O.OOPOO
1.60735+02
2.87426+00
0.00000
0.00000

1.60735+02
2.87426+00
0.00000
0.00000
4.16753+02
1.00000+02
8.00000+00
0.00000
1.78613+02
4.26600+01
0.00000
0.00000
1.78613+02
4.28600+01
0.00000
o.oooon
1.76615+02
4.28600+01
8.00000+00
0.00000
2.61957+02
6.28600+01
0.00000
o.ooono

2.61957+0?
6.28600+01
0.00000
0.00000
8.43840+05
1 .19300 + 02
0.00000
1.03000+01
8.43640+05
1.1*000+0?
0.00000
0.00000
8.43840+05
1.19100+0?
0.00000
0.00000
8.43840+05
l.l'tSOO + O?
0.00000
1.98000+01
8.43840+05
1.15000+02
0.00000
1 .50000+01

6.4?840+05
1.16000+02
0.00000
J .91000+01
1.60000+01
3.. 55000 + 00
0.00000
0.00000
2.40000+01
3.40000+00
0.00000
0.00000
2.40000+01
3.53000+00
0.00000
0.00000
1.60000+01
2.80000+00
0.00000
0.00000
2. 40000+01
3.00000+00
0.00000
0.00000

2.40000+01
3.05000+00
0.00000
0.00000
1.00000+00
0.00000
4.56517+04
o.nnooo
1.00000+00
o.onooo
4.56517+04
0.00000
1.00000+00
0.00000
4.56517+04
o.onooo
1. 00000 + 00
0.00000
4.56517+04
0.00000
1.00000+00
0.00000
4.56517+Ot
0.00000

1.00000+00
O.ooono
4.56517+04
o.ooono
O.i'OOno
o.uoooo
4.UOOOO+00
0.00000
0.00000
o.uoooo
5.00000+00
o.oooon
0.00000
0.00000
7.1)0000 + 00
o.nnoon
o.oooon
0.00000
n.uoooo+oo
0.00000
0.00000
o.uoooo
1.00001+00
0.00000

o.onooo
o. uoonn
3.00000+00
o.uoono

-------
                         TABLE C-5.   N0x CONTROL TEST DATA  FROM  SINGLE WALL OIL-FIRED  BOILERS
o
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
11
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
*
1
2
3
4
1
2
3
4
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
3
3
3
3
3
3
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
J
3
3
3
J
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
1
1
1
1
2
2
2
2
3
3
3
3
4
4
4
*
5
5
5
5
6
6
6
6
7
7
7
7
a
a
a
a
9
9
9
9
10
10
10
10
3.60000-01
0.00000
1.21600+02
3.67000+02
3.60000-01
0.00000
1.08300+02
2.38000+02
3.60000-01
0.00000
9.03000+01
2.01000+02
2.10000-01
0.00000
1.16400+02
2.52000+02
2.10000-01
0.00000
9.12000+01
1.60000+02
3.60000-01
0.00000
9.70000+01
2.53000+02
3.60000-01
0.00000
1.27000+02
3.22000+02
3.60000-01
0.00000
8.93000+01
1.85000+02
3.60000-01
0.00000
1.08000+02
2.41000+02
2.10000-01
0.00000
1.00000+02
?.3?nOO+02
?.5999?+02
O.OOPPO
0.00000
o.nonoo
?.64]3?+0?
0.00000
o.ooonn
0.00000
2.5999?+02
o.oonoo
0.00000
0.00000
?. 57715+02
0.00000
0.00000
O.OUOOO
2.58957+02
0.00000
0.00000
0.00000
2.57715+0?
0.00000
0.00000
0.00000
1.59804+02
0.00000
0.00000
0.00000
1.59804+02
0.00000
0.00000
0.00000
1.61357+02
0.00000
o.oooon
o.oooon
1.55560+0?
O.OOOOP
o.ooonn
n.noonn
2.52493+0?
1.01700+02
0.00000
0.00000
2.56468+0?
1.03300+02
0.00000
0.00000
2.52493+0?
1.01700+02
4.00000+00
0.00000
2.50254+0?
1.00800+02
0.00000
0.00000
2.51484+0?
1.01300+02
4.00000+00
o.oooon
2.50254+02
1.00800+02
4.00000+00
o.ooono
1.55174+02
6.25000+01
0.00000
0.00000
1.55174+02
6.25000+01
4.00000+00
0.00000
1.56B46+02
6.31700+01
0.00000
0.00000
1.51010+0?
6.083no+ni
4.00000+OU
o.ooono
4.70265 + 0*.
1.21*00+0?
o.onooo
1.90000+01
4.70265+05
I .08300+02
0.00000
4.20000+01
4.70265+05
1.20400+0?
0.00000
3.20000+01
4.70?65+Q5
1.16400+02
0.00000
2.40000+01
4.70265+05
1 .21600+02
0.00000
4.30000+01
4.70265+05
l.?9300+0?
0.00000
2.10000+01
4.70265+05
1.27000+0?
o.ooono
1 .90000 + 01
4.70265+05
1.19000+02
0.00000
2.90000+01
4.70265+05
1.08000 + 0?.
0.00000
?. 50000+01
4.70265 + 0=,
1 .33300+0?
0.00000
?. 60000+01
1.60000+01
3.90000+00
n.oonoo
0.00000
1. 60000 + 01
1.70000+on
n.ooono
0.00000
1.20000+01
3.7onno+oo
n. ooooo
o.ooono
1.60000+01
3.10000+00
0.00000
0.00000
1.20000+01
3.90000+00
0.00000
o.onooo
1.20000+01
4.90000+00
0.00000
0.00000
1.60000+01
4.60000+00
0.00000
o.ooono
1.20000+01
3.50000+00
o.oooon
0.00000
1. 60000 + 01
1.70000+00
o.ooono
n. ooooo
1 .20000+01
5.4onon+oo
o.oonoo
n. ooooo
1.00000+00
o.onnoo
4.4?44<4 + 04
o.ooono
l.OPOOO+00
0.00000
4.42444+04
0.00000
1.00000+00
0.00000
4.42444+04
o.onooo
1.00000+00
0.00000
4.59592+04
0.00000
l.ooono+no
o.onnoo
4.59592+04
o.ooono
l.nnooo+oo
o.ooono
4.42444+04
0.00000
1.00000+00
o.onono
4.42444+04
o.onooo
1.00000+00
o.onooo
4.42444+04
0.00000
l.onooo+oo
0.00000
4.4?4M4+04
o.oonno
l .nnooo + no
o.nnooo
4.50592+04
o.o. nno
l.dOOOO+00
o.nooon
l.doono+oo
n.uoouo
1 .UOOUO + 00
o.unoon
l.COOOO+00
0.00000
1. 00000 + 00
0.00000
2.00000+00
0 . 0 C 0 U 0
1.00000+00
0.00000
1.00000+00
0.00000
1.00000+00
o.ooono
2.00000+00
o.ooono
1. 00000 + 00
0.00000
2.00000+OP
o.ooono
i.onooo+oo
o.oooon
l.oooon+no
0.00000
i.onoon+oo
0.00000
2.0POOO+00
o.coono
i.onooo+on
o.ooonn
l.onoon+no
o.oponp
o.nnoon
o.nonnn
?.unonn+oo
o.iinonn

-------
                   TABLE C-5.   (Continued)
FRONT WALL OIL  FIRED
1
2
3
*
1
2
3
*»
1
2
3
4
1
2
3
**
1
2
3
0 4
w l
2
3
4
1
2
3
14
1
2
3
*
1
2
3
u
1
?
3
i)
1
1
1
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
11
11
11
11
12
12
12
12
13
13
13
13
It
14
I1*
1*
15
15
15
15
16
16
16
16
17
17
17
17
18
18
18
18
19
19
19
19
20
20
20
20
3.60000-01
0.00000
1.27000+02
2.66000+02
3.60000-01
0.00000
1.10000+02
1.91000*02
3.10000-01
0.00000
1.21700+02
5.60000+02
3.10000-01
0.00000
1.12200*02
<». 53000 + 02
3.10000-01
0.00000
1.00000+02
3.73000+02
3.10000-01
0.00000
9.80000+01
2.93000+02
3.10000-01
O.onooo
1.26000+02
3.61000+02
3.10000-01
0.00000
1.01000+02
2.52000+02
4.10000-01
0.00000
1.36000+02
2.58000+02
t. 10000-01
0.00000
1.06000+02
2. 03000+02
9.P0145+01
o.oooon
o.oonon
o.oooon
1. 00084+0?
0.00000
0.00000
0.00000
2.751413 + 0?
0.00000
0.00000
O.OOPOO
?.75«»1? + 0?
0.00000
0.00000
0.00000
2.77276+02
0.00000
0.00000
0.00000
2.77276+0?
0.00000
0.00000
0.00000
1.66324+0?
o.oooon
0.00000
0.00000
1.6270?+02
0.00000
o.ocnoo
o.ooonn
6.65505+0)
o.oonon
o.onnoo
o.oonon
6.Pfl?«*5 + ftT
O.OPOOO
o.oooon
o.ounon
9.51740+nj
3.83300+01
o.ooono
o.oooon
9.72560+01
3.917PO+01
0.00000
o.noooo
3.15901+02
9.19800+01
0.00000
0.00000
3.15901+02
9.19flOO+01
0.00000
0.00000
3.18014+02
9.25900+01
2.00000+00
0.00000
3.18014+02
9.259PO+01
2.00000+00
o.ooono
1 .90821 + 02
5.55600+01
O.UOOOO
0.00000
1.86562+02
5.43200+Oi
2.00000+00
o.ooonn
7.63n95+01
2.222nO+Ol
o.ooono
n.noonn
7.?0«24«.01
2.09SOI1 + 01
2.noono+no
n.ononu
4.70265+05
1.27000+0?
n. ooooo
1 .40000+01
4.70265+05
1 .10000+02
0.00000
2.00000+01
2.69560+05
1.21700+02
0.00000
5.90000+01
2.69560+05
1.12200+02
0.00000
5.25000+02
2.69560+05
1.29600+02
0.00000
f .30000+01
2.69560+05
1.17600+02
0.00000
9.50000+01
2.69560+05
1.26000+02
0.00000
4.60000+01
2.69560+05
1.21200 + 0?.
0.00000
9.40000+01
2.69560+05
1.36000+0?
o.ooono
0.00000
2.69560+OS
l.?7?()0 + 0?
o.ooono
fl.7(iono + ni
i .2noon+nl
4.60000+00
0.00000
n. ooooo
1.20000+01
2.00000+00
0.00000
n.nonno
1.20000+01
3.90000+00
0.00000
0.00000
1.20000+01
2.40000+00
0.00000
0.00000
1.00000+01
5.00000+00
0.00000
n. ooooo
1.00000+01
3.30000+00
0.00000
0.00000
1 .20000+01
4.50000+00
0.00000
0.00000
1 .00000+01
3.90000+00
0.00000
o.oonoo
i.ooooo+ni
5.80000+00
o.ooono
n. ooooo
1. 00000+01
5.3onon+no
n . o o n o o
o.ooono
i.nnono+oo
o.nnooo
H ^2444+04
0.00000
1.00000+00
o.onono
4.42444+04
o.onooo
1.00000+00
0.00000
4. "1442 + 04
0.00000
1.00000+00
0.00000
4.4J442+04
o.onooo
l.onooo+oo
0.00000
4.41442+04
0.00000
l.onooo+oo
o.onooo
4.41442+04
0.00000
1.00000+00
o.onooo
4.41442+04
o.ooono
1.00000+00
o.nonnn
4 .41442+04
o.oooon
l.UOOOO+OO
o.onooo
4.37924+04
O.nnono
1 .onnno+no
o.nnonn
4 .37«*?-* + 04
o . n o o n n
l.nnoon+oo
o.noonn
1 .00000+00
o . u o o o n
l.OPOOO+OO
o.ooono
l.UOOOO+OO
0.00000
o.ooono
0.00000
1.00000+00
o.oooon
0.00000
0.00000
1.00000+00
0.00000
O.UOOOO
0.00000
1.00000+00
0.00000
o.oooon
0.00000
2.00000+00
o.unono
o.onooo
o.ooono
1.00000+00
o.unooo
o.oooon
O.UOOOO
?. 00000 + 00
n.unonn
o.oooon
o.oooon
i.onooo+on
o.unooo
o . c o o n n
o.nnonn
2,ncuon+nn
o.coonn

-------
                 TABLE C-5.   (Continued)
FRONT WALL OIL  FIRTP ROILFRS
1
2
3
it
1
2
3
4
1
2
3
M
1
2
3
it
1
2
3
4
1
2
3
14
1
2
3
it
1
2
3
4
1
2
3
4
1
f
3
4
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
3
3
3
3
1
3
3
3
3
3
3
,
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
?
3
3
?
3
*
3
5
Tt
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
21
21
21
21
22
22
22
22
23
23
23
23
24
24
24
24
25
25
25
25
26
26
26
26
27
27
27
27
28
28
28
28
29
29
29
29
30
30
30
30
3.10000-01
0.00000
1.15100+02
1.50000+02
3.10000-01
0.00000
1.09600+02
3.70000+02
3.10000-01
0.00000
9.53000+01
2.70000*02
3.10000-01
0.00000
9.25000*01
1.42000*02
3.10000-01
0.00000
1.13000*02
3.53000*02
3.10000-01
0.00000
1.05000*02
2.98000*02
3.10000-01
0.00000
9.67000*01
2.67000*02
3.10000-01
0.00000
9.03000*01
2.29000+02
3.20000-01
0.00000
1.07000+02
1.74000+02
3.20000-01
0.00000
9.10000+01
1. 53000+02
2.04107+02
0.00000
0.00000
o.nonnn
?.90«»3P + 0?
O.OOPOO
0.00000
0.00000
2.79553+02
O.OOOPO
0.00000
o.ooopn
?.7034?+02
0.00000
2.50000+01
o.ooono
1.92406+02
0.00000
0.00000
0.00000
1.97064+02
o.oooon
0.00000
0.00000
1.97064+02
0.00000
0.00000
O.OOPOO
1.97064+02
0.00000
0.00000
0.00000
i.93?3e+n?
0.00000
2.50000+nt
o.onpnn
1.92
-------
             TABLE C-5.   (Continued)
W/ILL OIL
               HOILFRS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
"
1
2
3
*
1
2
3
4
1
2
3
*
1
2
3
4
1
2
3
4
1
2
3
i|
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
5
5
5
5
5
5
5
«>
3
3
?
3
3
j
3
i
3
3
3
31
?
?
3
3
3
3
3
3
3
3
3
3
3
3
5
3
3
3
3
5
3
3
*
3
3
3
3
»
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
31
31
31
31
32
32
32
32
33
33
33
33
34
34
34
34
35
35
35
35
36
36
36
36
37
37
37
37
38
38
38
38
39
39
39
39
40
40
40
40
2.40000-01
?. 43840 + 00
1.09000+02
3.57000+02
2.40000-01
2.43840+00
1.06000+02
3.10600*02
2.40000-01
2.43840*00
1.08000*02
2.70000*02
2.40000-01
2.43840*00
1.18000*02
2.80500*02
2.40000-01
2.43840+00
8.62000*01
2.63000+02
2.40000-01
2.43840+00
7.70000+01
2.11000+02
2.40000-01
2.43840+00
1.15000+02
1.77000+02
2.40000-01
2.43840+00
7.90000+01
1.51200+02
2.40000-01
2.43840+00
1.08000+02
3.10600+02
2.40000-01
2.43840+00
1 .10000+02
?. 97000+02
1.91164+02
o. onnoo
2.70000+01
o.oooon
1.58148+02
0.00000
3.noooo+oi
0.00000
1.16?31+02
0.00000
4.70000+01
0.00000
7.84530+01
0.00000
7.30000+01
0.00000
1.83299+02
0.00000
3.00000+01
o.oooon
1.90026+02
0.00000
1.20000+01
0.00000
1.53387+02
0.00000
3.10000+01
0.00000
8.14545+01
o.oooon
6.30000+01
o.oonoo
1.91164+02
o.oooon
2.ooonn+oi
o.ooono
1.91164*02
O.ounnn
2.ioono+oi
o.ooono
2.t566fl9 + 0?
9.67000+01
O.oooon
0.00000
2.12336+0?
a.oooon+oi
0.00000
0.00000
1. 56089+02
5.88000+01
0.00000
0.00000
1.05363+02
3.97000+01
0.00000
0.00000
2.«*6058 + 02
9.27000+01
4.00000+00
o.ooono
2.55080+02
9.61000+01
4.00000+00
0.00000
2.05963+02
7.76000+01
4.00000+00
0.00000
1.09370+02
4.12000+01
4.00000+00
o.onooo
2.566P9+0?
9.67000+01
o.ooono
o.nnoon
2.566P9+0?
9.67000+01
o.nooon
(1.00000
5.17731+05
1.09000+0?
0.00000
1.40000+01
5.17731+05
1 .08000+0?
n. ooooo
1.40000+01
5.17731+0'5
1.08000+02
0.00000
2. l5000+0i
5.17731+05
1.18000+02
0.00000
1.10000+01
5.17731+05
1.29<»00 + 02
o.onooo
4.50000+01
5.17731+05
1.15000+0?
0.00000
2.50000+01
5.17731*05
1 .15000 + 02
o.ooono
1.80000+01
5.17731+05
1.18500+0?
0.00000
?.25oon+oi
5.17731+05
1.08000+0?
0.00000
2.75000+01
5.17731+05
i.ioono+o?
o.ooono
?.p.<*onn+oi
1 .20000+01
i.88non+no
a.ooooo
o.oonoo
i.2oooo+ni
1.70000+00
o.onooo
0.00000
1 .20000+01
l .75000+00
0.00000
0.00000
1.20000+01
3.35000+00
0.00000
0.00000
8.00000+00
4.98000+00
0.00000
0.00000
8.00000+00
3.00000+00
0.00000
0.00000
8.00000+00
2.95000+00
0.00000
0.00000
8. 00000+00
3.38000+00
0.00000
0.00000
1.20000+01
1. 70000+00
0.00000
n.oonon
1.20000+01
1.98000+00
0.00000
n. oo on o
1.00000+00
o.nnonn
4.56703+04
o.nnonn
1.00000+00
o.ooono
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
o.onooo
1. 00000+00
o.onooo
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
i.onooo+oo
0.00000
4.56703+04
0.00000
1.00000+00
o.ooono
4.56703+04
o.noooo
l.onooo+no
0.00000
4.56703+04
o.nnooo
i.nnooo+oo
o.nnoon
4.56703+04
o.nnonn
1 .ononn + no
o.oooon
4 ,f)670 A*04
n . ono'io
o. ononn
O.l'dOno
5.00000+00
O.UOOOO
0.00000
o.ononn
5.UOOOO+00
O.noOOO
0.00000
0.00000
5.00000+00
0.00000
0.00000
0.00000
5.00000+00
o.ooono
0.00000
0.00000
6.00000+00
O.noono
0.00000
o.ooooo
6.00000+00
o.ooono
0.00000
O.UOOOO
6.00000+00
o.noono
o.uoonn
o.onooo
6.UOUOO+00
o.ooono
o.oooon
0 . n n o n o
s.ooooo+on
o.uoonn
o."oono
0 . Ill) UO 11
•s.nnooo + on
n. iinnnn

-------
                  TABLE C-5.   (Continued)
FROM  WALL OIL  FIRED ROILFRS
1
2
3
4
1
2
3
4
1
2
3
«»
1
2
3
4
1
2
3
o 4
* 1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
6
6
6
6
6
6
6
6
6
6
6
6
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
H
11
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
41
41
41
41
42
42
42
42
43
43
43
43
44
44
44
44
45
45
45
45
46
46
46
46
47
47
47
47
48
48
48
48
49
49
49
49
50
50
50
50
2.40000-01
2.438404-00
7.60000+01
1.840004-02
2.40000-01
2.43840+00
1.09000+02
2.540004-02
2.40000-01
2.43840*00
7.70000*01
1.66000*02
2.40000-01
2.43840*00
1.11000*02
2.50600*02
2.40000-01
2.43840*00
7.80000*01
1.61000*02
2.40000-01
2.43840+00
1.18000*02
2.56400*02
2.40000-01
2.43840*00
8.20000*01
1.83000*02
2.40000-01
1.98120*00
9.60000*01
2.02700*02
2.40000-01
1.98120*00
8.40000*01
1.67400*02
2.40000-01
1.98120*00
6.70000*01
1.30000+02
1.92924+02
0.00000
1.90000+01
0.00000
1.533P7+02
0.00000
3.60000+01
0.0000(1
1.58146+02
0.00000
3.50000+01
0.00000
1.19750+02
0.00000
5.2000n+0i
0.00000
1.13229+02
0.00000
5.20000*01
0.00000
7.29675*01
0.00000
8.70000+01
0.00000
7.84530+01
0.00000
8.50onn+oi
0.00000
2.51298+02
0.00000
3.oooon+oo
0.00000
2.53575+02
0.00000
4.00000+00
0.00000
2.16315+02
0.00000
1.70000+Ot
o.oooon
2.59055+0?
9.76000+01
4.00000+00
0.00000
2.05963+0?
7.76000+01
0.00000
0.00000
2.12336*02
8.00000+01
4.00000+00
o.ooono
1.60853+02
6.06000+01
0.00000
0.00000
1.52083+0?
5.73000+01
4.00000+00
0.00000
9.79500+01
3.69000+01
0.00000
0.00000
1.06941+02
3.97000+01
4.00000+00
0.00000
2.43976+02
9.83000+01
4.00000+00
0.00000
2.46216+02
9.92000+01
4.00000+00
0.00000
2.09970+0?
8.46000+01
4.000PO+00
0.00000
5.17731+05
1.14000+0?
0.00000
2.96000+01
5.17731+05
1.09000+0?
0.00000
2.80000+01
5.17731+05
1.15500+02
0.00000
3.50000+01
5.17731+05
1.11000+02
0.00000
2.87000+01
5.17731+05
1.17000+02
0.00000
4.00000+01
5.17731+05
1.18000+02
0.00000
3.10000+01
5.17731+05
1.23000+02
0.00000
3.72000+01
4.70265+05
1.28000+0?
0.00000
o.ooono
4.70265+05
1.12000+02
0.00000
0.00000
4.70265+05
1.16000+02
0.00000
0.00000
». 00000+00
2.78000+00
0.00000
0.00000
1 .?0000+01
1. 80000+00
0.00000
0.00000
8.00000+00
3.10000+00
0.00000
0.00000
1.20000+01
2.18000+00
0.00000
0.00000
8.00000+00
3.10000+00
0.00000
0.00000
1.20000+01
3.38000+00
0.00000
0.00000
8.00000+00
4.05000+00
0.00000
0.00000
1.20000+01
4.75000+00
0.00000
n. ooooo
1.20000+01
2.29000+00
0.00000
0.00000
1.20000+01
2.98000+00
0.00000
0.00000
1.00000+00
0.00000
4.55703+04
o.onooo
1.00000+00
0.00000
4.56703+04
0.00000
1.00000*00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
o.ooono
l.onooo+oo
o.onooo
4,'»f.7n3 + 04
o.ooonn
o.uooon
0.00000
6.00000+00
0.00000
0.00000
o.ooono
•>.onooo+oo
o.nnouo
o.ooono
0.00000
6.00000+00
o.noooo
0.00000
o.ooono
5.00000+00
0.00000
0.00000
o.oooon
6.00000+00
o.ooono
0.00000
o.uoooo
5.00000+00
o.oooon
o.uoooo
o.coooo
6.00000+00
o.ooono
o.ooooo
o.uoono
6.onooo+oo
o.ooono
o.ooono
0.00000
6.uooon+on
o.ooooo
0.00000
0.00000
6.UOUOO+00
o.ununn

-------
                   TABLE C-5.  (Continued)
FRONT WALL  OIL  FIRED BOILERS
1
2
3
"
1
2
3
U
1
2
3
4
1
2
3
4
1
2
3
£ *
-1 i
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
6
6
6
6
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
3
3
3
3
3
3
3
*
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
?
3
3
3
3
3
j
3
3
1
3
*
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
51
51
51
51
52
52
52
52
53
53
53
53
54
54
54
54
55
55
55
55
56
56
56
56
57
57
57
57
58
58
58
58
59
59
59
59
60
60
60
SO
2.40000-01
1.98120+00
7.90000+01
1.49000+02
2.40000-01
1.98120+00
1.21600+02
3.59800+02
2.40000-01
1.96120+00
1.16300+02
2.32000+02
2.40000-01
1.98120+00
9.00000+01
1.86400+02
2.40000-01
1.98120+00
9.10000+01
1.45300+02
2.40000-01
1.98120+00
1.27000+02
3.16700+02
2.40000-01
1.98120+00
1.08000+02
2.19400+02
2.40000-01
1.98120+00
8.80000+01
1.34000+02
2.40000-01
1.98120+00
1.27000+02
2.59000+02
2.40000-01
1.98120+00
1.10000+02
i.naono+02
1.24510+02
0.00000
3.80000+01
o.ooonn
2.45916+02
o.oooon
0.00000
o.oooon
2.42914+02
0.00000
0.00000
0.00000
2.42914+02
0.00000
2.00000+00
o.onooo
2.45916+02
0.00000
4.00000+00
0.00000
1.71499+0?
0.00000
1.30000+01
0.00000
1.66221+02
0.00000
3.iooon+oi
0.00000
1.681B7+02
0.00000
2.70000+01
o.ooonn
1.1509?+OP
o.oonoo
?. 00000+01
o.oonoo
1.1509?+0?
o.oooon
5.10000+01
O.OOOPO
1.208B4+02
4.87000+01
4.00000+00
o.oooon
2.38771+02
9.62000+01
0.00000
0.00000
2.35774+02
9.50000+01
0.00000
0.00000
2.35774+02
9.50000+01
4.00000+00
0.00000
2.38771+02
9.62000+01
4.00000+00
0.00000
1.66531+02
6.71000+01
0.00000
0.00000
1.61326+02
6.50000+01
0.00000
0.00000
1.63313*0?
6.58000+01
4.00000+00
0.00000
1.11673+0?
4.50000+01
0.00000
0.00000
1.11673+0?
4.50000+01
o.oouno
0. UOOOO
4.70265+05
1.18500+0?
o.noono
0.00000
4.70265+05
1.21600+02
0.00000
6.31000+01
4.70265 + 0«i
1.16300+02
0.00000
3.00000+01
4.70265+05
1.20000+02
0.00000
0.00000
4.70265+05
1.21300+02
0.00000
0.00000
4.70265+05
1.27000+02
0.00000
4.40000+01
4.70265+05
1.08000+0?
0.00000
2.BOOOO+01
4.70265+05
1.17000+0?
0.00000
o.oonoo
4. 70265+05
1.27000+0?
0.00000
3.30000+01
4.70265 + 0-5
1 .10000 + 0?
0.00000
0.00000
fl.oonon+no
3.38000+00
n. ooooo
0.00000
i.6oooo+ni
3.89000+00
0.00000
o.ooono
1. 60000+01
3.09000+00
o.oooon
0.00000
1.20000+01
3.71000+00
0.00000
0.00000
1.20000+01
3.91000+00
0.00000
n. ooooo
1.60000+01
4.63000+00
0.00000
0.00000
1.60000+01
1.72000+00
0.00000
o.ooono
1.20000+01
3.23000+00
0.00000
0.00000
1.20000+01
4.60000+00
0.00000
n.ooono
1 .200UO+01
2. 04000+00
o.oonoo
o.oonnn
1.00000+00
o.onooo
4.56703+04
o.ooono
1.00000+00
0.00000
4.56703+04
o.noooo
1.00000+00
0.00000
4.56703+04
0.00000
1. 00000 + 00
0.00000
4.56703+04
0.00000
1.00000+00
o.onoon
4.56703+04
0.00000
1.00000+00
o.nnooo
4.56703+04
0.00000
1.00000+00
0.00000
4.56703+04
o.noooo
1.00000+00
0.00000
4.567n3+n4
0.00000
1.00000+00
o.oooon
4.56703+04
o.onooo
l.opooo+no
o.nnooo
4.5*703+n4
n . fi n n n o
O.noono
o.noooo
6.UOOOP+00
o.ooonn
o.uooon
0.00000
l.noooo+oo
n.ooono
0.00000
o.ooono
1.00000+00
0. UOOOO
0.00000
O.OPOOO
6.00000+00
0.00000
o.uoono
o.coooo
6.00000+00
0.00000
0. UOOOO
0.00000
5. 00000+00
o.oooon
0. UOOOO
o.onooo
5.UOOOO+00
o.uoono
o.uoono
0. UOOOO
6.00000+00
0. UOOOO
0.00000
o.unoon
5.00000+00
o.ooonn
o.noonn
O.OPOOO
'j.unoon+no
o.t'nonn

-------
                                               TABLE C-5.   (Concluded)
                           FPOWT WALL OIL  FIRED  BOILERS
1  7  3  2  61   2.1*0000-01   1.16093 + 02    1.1«4669+02    i*.70265+05   fl.00000 + 00   1.00000 + 00   O.dOOOO
2  7  3  2  61   1.98120+00   0.00000       t.62000+01    1.23800+02   4.30000+00   0.00000      O.UOOOO
3  7  3  2  61   9.90000 + 01   1.10000 + 01    2.00000 + 00    0.00000       0.00000       <* .Sf.703 + 01*   6.00000 + 00
14  7  3  2  61   1.66000+02   O.OUOOO       0.00000       0.00000       0.00000       0.00000      0.00000

-------
                          TABLE C-6.  N0x CONTROL TEST DATA FROM OPPOSED WALL GAS-FIRED BOILERS
<£>
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
*
1
2
3
4
1
?
3
4
1
2
3
4
1
2
3
11
1
2
3
4
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
? 1
? 1
2 1
2 1
? 1
? 1
? 1
? 1
? 1
2 1
2 1
? 1
2 1
2 1
? 1
2 1
2 1
2 1
2 1
? 1
2 1
2 1
2 1
2 1
? 1
2 1
? 1
2 1
? 1
2 1
2 1
2 1
? 1
2 1
? 1
? 1
? 1
? 1
? 1
? 1
1
1
1
1
2
2
2
2
3
3
3
3
4
4
4
4
5
5
5
5
6
6
6
6
7
7
7
7
a
a
8
a
9
9
9
9
10
10
10
in
0.00000
0.00000
1.12700+02
9.46POP+02
0.00000
0.00000
1.07000+02
7.83000+02
0.00000
0.00000
9.75000+01
5.15000+02
0.00000
0.00000
6.92000+01
3.55000+02
0.00000
0.00000
9.34000+01
3.81000+02
0.00000
0.00000
7.82000+01
2.13000+02
0.00000
0.00000
1.08000+02
2.99000+02
o.ooono
0.00000
9.00000+01
a. 7oooo+oi
0.00000
0.00000
9.26000+01
1.65000+02
0.00000
o.onooo
1.06000+02
2.49onn+o2
?. 99425+0?
o.pooon
0.00000
0.00000
2.99425+0?
0.00000
0.00000
0.00000
2.99425+02
0.00000
0.00000
0.00000
2.96528+02
0.00000
0.00000
O.POOOO
2.99425+02
0.00000
0.00000
o.noooo
2.991*25 + 02
0.00000
0.00000
0.00000
1.35067+02
o.oooon
O.OOOPO
O.OOOPO
1.32273+02
o.noono
n.noooo
o.noono
1 .32?73+0?
o.ooono
o.onnon
O.nnnon
1.32?7.1+o?
n.nnnnn
n . P n o P r>
p . n 0 n n o
6.30729+02
1.04400+02
0.00000
0.00000
6.30729+02
1.04400+02
o.oooon
o.oooon
6.30729+02
1.04400+02
0.00000
o.ooono
6.24672+0?
1.03400+02
6.00000+00
0.00000
6.30729+02
1.04400+02
0.00000
o.ooono
6.30729+02
1.04400+P2
6.00000+00
0.00000
2.84481+02
4.70900+01
0.00000
0.00000
2.78613+PP
4.61200+P1
6.00000+00
o.oooon
2.78613+02
4. 61200+01
o.ononn
n. ooooo
2.7P613+02
4.61200+ni
o.unopn
P .1)000 U
6.92185+05
1.12700+0?
0.00000
8.60000+01
«.9218b+05
1.07000+0?
o.onono
7.40000+01
8.92185+05
1.13800+0?
0.00000
6.70000+01
8.92185+05
1.07000+02
0.00000
1.50000+0?
8.92185+05
1.09000+02
0.00000
8.40000+01
8.92185+05
1. 09500+02
0.00000
1 .43000+02
8.92185+05
1.08000+02
0.00000
6.40000+01
P. 92185+05
1.08000+0?
0.00000
5.40000+01
8.92185+05
1.08000+0?
o.onooo
7.40000+01
R.921fl5+05
1.06000+0?
o.onono
•s.7nono + oi
S. 60000+01
2.6ooon+on
o.oooon
0.00000
3. 60000+01
1.60000+00
0.00000
n. ooooo
3. 60000+01
2.80000+00
n. ooooo
o.ooono
3.00000+01
1.50000+00
0.00000
o.ooono
3.60000+01
1.90000+00
0.00000
O.OOOPO
3.00000+01
2.00000+00
0.00000
0.00000
3.60000+01
1 .70000+00
0.00000
0.00000
3.00000+01
1.70000+00
0.00000
0 . 0 0 0 C> 0
3.60000+01
1.70000+00
o.noooo
n. ooooo
?.6<70PO + Ol
i.3f)oon + pn
n.oonno
n.oonno
l .pnnoo+on
o.nnono
3.92769+01
0 .nnoon
1. 00000 + 00
o.ononn
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.onooo
3.92769+01
0.00000
1.00000+00
O.onooo
3.92769+01
o.ooono
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.onooo
3.92769+01
O.OOOPO
1.00000+00
0.00000
3.9?769+ni
o.onnno
1.00000+00
0.00000
3.92769+01
o.onooo
i.noooo+oo
o.ooono
,S.9?769 + nl
0 . o n n P u
o.noonn
O.DOOOO
1. 00000 + 00
o.oooun
o.nooon
o.uoooo
1. 00000 + 00
o.uoooo
o.ooono
o.ooono
3.0000P+00
o.onoon
o.uoooo
O.OPOOO
2.00000+00
O.OPOOO
0.00000
o.uoooo
3.00000+00
o.uoono
o.nooon
o.onooo
4.UOOOO+00
o.onooo
o.onono
0.00000
i.onooo+oo
o.ooono
o.noooo
o.uoonn
?.onoon+oo
o.cnoon
0.00000
o.onoon
3.UOOPO+00
n . i n o P n
o. nnonn
o.unooo
i.onocn+on
n. nnurn

-------
                   TABLE C-6.   (Continued)
HORI70NTALLY OPPOSED GftS  FI«EO BOILERS
1
2
3
1
2
3
4
1
2
3
u
1
2
3
1
2
3
0 4
tn
0 1
2
3
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
3
3
3
3
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
•
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
11
11
11
11
12
12
12
12
13
13
13
13
14
14
I1*
15
15
15
15
16
16
16
16
17
17
17
17
16
16
18
18
19
19
19
19
20
20
?0
?0
0.00000
0.00000
7.86000+01
5.60000+01
0.00000
0.00000
1.21000+02
2.36000+02
0.00000
0.00000
1.150004-02
1.96000+02
0.00000
0.00000
9.09500+01
1.45000+02
0.00000
0.00000
8.63000+01
1.40000+02
0.00000
0.00000
1.25000+02
1.66000+02
0.00000
0.00000
1.15000+02
1.20000+02
0.00000
0.00000
9.34000+01
9.50000+01
0.00000
0.00000
8.58000+01
7.00000+01
0.00000
0.00000
1.14100+02
5.56nnn+o?
1 .39?0«+02
0.00000
0.00000
0.00000
2.P3383+0?
0.00000
O.OOPOO
n.ooono
2.79036+02
0.00000
0.00000
o.oooon
2.79036+0?
0.00000
o.oooon
o.oooon
?. 79036+0?
o.oooon
0.00000
O.POOOO
1.42933+02
o.oooon
0.00000
0.00000
I.i»2g33+02
0.00000
0.00000
0.00000
1.41691+02
o.ooonn
o.ooooo
o.nonoo
1.42933+0?
o.ooonn
o.oonoo
o.ooonn
i.42r3n+o?
o.oonoo
0 . n n n n o
O.oonnn
2.932R1+P?
4.85400+01
6.00000+00
o.ooonn
5.66154+0?
1.00000+02
0.00000
n. ooooo
5.57322+02
9.84400+01
0.00000
0.00000
5.57322+02
9.84400+01
8.00000+00
0.00000
5.57322+02
9.84400+01
8.00000+00
o.ooono
2.85585+02
5.04400+01
0.00000
o.oooon
2.85585+0?
5.044nO+01
0.00000
0.00000
2.83093+02
5.00000+Ql
8.00000+00
0.00000
2.85585+0?
8.00000+00
O.oooon
2.1403P+0?
9.38300+01
o . n o o o o
o . noonn
R. 92185 + 05
1.10100+0?
o.ooono
7.60000+01
1.29887+06
1.21000+02
0.00000
1.20000+01
1.29887+06
1.15000+02
o.noooo
6.ioono+oi
1.29887+06
1.21300+0?
0.00000
1.30000+01
1.29887+06
1.15000+02
0.00000
2.10000+02
1.29887+06
1.25000+0?
0.00000
1 .50000+01
1 .29887+06
1.15000+02
0.00000
4.30000+01
1 .29887+06
1.24500+02
n. ooooo
1.50000+01
1.29887+06
1.14400+02
o.onooo
5.inono+o?
1 ,5?770+06
1.14100+02
n. ooooo
3.00000+P1
2.10000+00
o.oooco
0.00000
2.40000+01
i». 00000 + 00
o.nnooo
o.oonoo
2.40000+01
3.00POO+00
0.00000
0.00000
2.40000+01
4.00000+00
0.00000
0.00000
2.40000+01
3.00000+00
0.00000
0.00000
2.40000+01
4.50000+00
0.00000
0.00000
2.40000+01
3.00000+00
0.00000
n.oonoo
2.40000+01
4.50000+00
0.00000
0.00000
2.40000+01
2.90000+00
n. ooooo
o.ooono
?.4oono+nl
2.90000+PO
o.onnnn
n . o o n p n
i.nnooo+oo
o.nuono
3.92769+01
o.nnooo
1.00000+00
o.ooono
o.onooo
1.00000+00
o.noooo
3.92769+01
0.00000
i.onooo+oo
0.00000
3.9?769+Ol
O.POOOO
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.onooo
3.92769+01
0.00000
1.00000+00
o.noooo
3.9?769+nl
0.00000
i.onooo+oo
o.ooonn
3. 92769+01
0.00000
1.00000+00
o.ooono
3. "2769 + 01
o.ooonn
i .nnoon+no
o.ooono
0 . n n o n n
o.ooonn
O.UPOOO
4. joooo+on
o.unooo
i.onooo+oo
0.00000
i.onooo+oo
o . o o o o n
1.00000+00
0.00000
1.00000+00
o.oooon
l.OOUOO+00
o.ooooo
?. 00000 + 00
o.ooouo
1.00000+00
o.oooon
?.nnooo+oo
o.uoooo
i.ooooo+on
o.onooo
1.00000+00
0.00000
l.UOOOO+00
o . o n o n o
i.onooo+no
o.oooon
i.oooon+oo
o.nooon
?. 00000+00
o.ooooo
1.00000+00
o.ooooo
2.0POOO+00
o.oooon
i.tinoon + no
o.ononn
l.onoOP+OO
o . I'nonn

-------
                                                   TABLE C-6.   (Continued)
                                HORIZONTALLY  OPPOSED (5«S  FIRED BOILERS
o
1
2
3
4
1
2
3
"
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
U
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
4
4
4
4
4
4
4
4
4
4
4
4
2
2
2
?
2
2
2
?
2
2
2
2
2
2
2
2
2
2
?
2
2
2
2
2
2
?
?
?
p
?
2
2
?
2
2
9
?
?
?
?
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
21
21
21
21
22
22
22
22
23
23
23
23
24
24
2*»
24
25
25
25
25
26
26
26
26
27
27
27
27
28
28
28
28
29
29
29
29
30
30
30
3n
0.00000
0.00000
1.10000+02
5.24000+02
0.00000
0.00000
1.18000+02
3.42000+02
0.00000
0.00000
1.10000+02
2.93000+02
0.00000
o.onooo
1.17000+02
2.46000+02
0.00000
0.00000
1.08000+02
2.05000+02
0.00000
0.00000
7.97000+01
1.04000+02
0.00000
0.00000
7.25000+01
9.10000+01
0.00000
0.00000
1.17000+02
6.75noO+02
0.00000
0.00000
1.08000+02
5.19000+02
0.00000
o.onooo
9.0<4700 + 01
2.86100+02
1.40553+02
o.oooon
o.noooo
o.ooono
1.05259+0?
o.nooon
O.OOPOO
o.pnoon
1.02983+02
0.00000
o.noonn
0.00000
8.26965+01
o.nonoo
0.00000
0.00000
8.26965+01
o.noooo
0.00000
o.ooono
8.26965+01
0.00000
o.ooono
o.oonoo
8,i6f.ifi+ni
o.oooon
0.00000
0.00000
2.6l«»<»l+0?
o.npooo
o.noono
o.oonnn
2.6144140?
o.oooon
o.ononn
o.nnnpn
2.61441+0?
o . n n n n n
o.noonn
0 . mm on
2.10632+0?
9.233nn+oi
0.00000
o.ooonn
1.57793+0?
6.91700+01
0.00000
o.ooono
1.54366+02
6.76700+01
0.00000
o.ooono
1.23944+0?
5.43300+01
o.oooon
o.ooono
1.23944+02
5.4330n+01
0.00000
o.ooono
1.23944+02
5.433nO+01
8.00000+00
0.00000
1.22430+02
5. 36700+01
8.00000+00
0.00000
5.21832+02
1.00000+02
0.00000
o.noooo
5.21832+02
l.ooono+02
n.oooon
n.ooono
5.21832+0?
i .onoon+02
* . noooiuon
o.ononn
1.52770+06
1.10000+02
0.00000
P. 00000+01
1.52770+06
1.18000+02
0.00000
1.40000+01
1 .52770+06
1.10000+02
0.00000
s.ooooo+on
1,52770+0*
1.17000+02
o.onooo
2.00000+01
1.52770+06
1.08000+02
0.00000
1.00000+01
1.52770+06
1.19600+02
0.00000
4.00000+01
1 .52770+06
1.08700+02
o.ooono
o.onooo
6.34931+05
1 .17000 + 02
n.ooono
1.40000+01
6.34931+05
1 .08000 + 02
o.ooono
3.4oonn+oi
6.^4931 + Ofi
i .?o6no + o?
0.00000
i ,4nnnn + oi
2.40000+01
2.10000+00
0.00000
o.oonoo
2.40000+01
3.55000+00
n. ooooo
o.oonoo
2.40000+01
i.esooo+no
0.00000
n. ooooo
2.40000+01
3.35000+00
0.00000
0.00000
2.40000+01
1.75000+00
0.00000
o.ooono
1.600PO+01
3.75000+00
0.00000
o.oonno
i.fooon+oi
i.esnon+no
n. ooooo
0.00000
2.4oonn+ni
3.3nnoo+oo
o.oonoo
n.oonoo
2.40000+01
1.70000+00
0.00000
n.oooon
i .sonnn+ni
3.9nnoo+on
n.oonoo
n . n i n n o
l.ooooo+no
o.onoon
3.92769401
o.onooo
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
o.ooono
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.ooono
3.92769+01
0.00000
i.ooooo+no
0.00000
3.92769+01
0.00000
i.ooooo+no
o.ononn
3.92769+01
0.00000
i.nnoon+oo
o.nnooo
3.9?769+nl
o.onono
i.onono+oo
o.ooono
S.lfin + Ql
o.nnonn
i .noono+oo
o.nnono
3.<'?7f-9 + ill
n .nnopd
I .noooo+oo
o . o n o n n
i.ooono+oo
0.00000
1. 00000 + 00
o.onooo
1.00000+00
o.noonn
1.00000+00
O.OOOPO
1.00000+00
o.ooono
1.00000+00
o.ooooo
1.00000+00
o.ooono
i.onooo+oo
o.onooo
1.00000+00
o.oooon
i.noooo+on
0.00000
2.00000+00
o.ooono
1 .00000 + 00
0.00000
2.00000+00
o.noooo
t. 00000+00
o.ononn
i.opoon+on
o.ooono
1.00000+00
o.ooono
l.onoon+no
o.ooon"
i .ononn+oo
o . u n o d n
?.'inuun»on
n.'innnr:

-------
                  TABLE C-6.   (Continued)
HORIZONTALLY OPPOSED GAS  FIRED  HOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
*»
1
2
3
4
1
2
3
4
1
2
3
•«
1
2
3
4
1
2
3
4
4
4
4
4
„
4
4
*»
4
4
4
*
4
4
4
4
4
4
4
4
4
4
4
*
4
4
4
4
5
5
5
5
5
5
5
5
5
5
5
5
?
2
?
?
2
2
?
?
2
2
2
?
2
2
2
2
2
?
?
2
2
2
2
2
2
2
2
2
2
9
2
2
2
2
?
?
?
?
?
?
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
31
31
31
31
32
32
32
32
33
33
33
33
34
34
34
34
35
35
35
35
36
36
36
36
37
37
37
37
38
38
36
38
39
39
39
39
40
40
40
40
0.00000
0.00000
H. 28700+01
2.70000+02
0.00000
o.onooo
1.13000+02
4.00000+02
0.00000
0.00000
7.55400+01
2.64000+02
0.00000
0.00000
1.27000+02
3.13000+02
0.00000
0.00000
1.11000+02
2.36000+02
0.00000
0.00000
9.37800+01
1.50000+02
0.00000
0.00000
8.52300+01
1.07000+02
0.00000
1.11862+00
1.12000+02
9.80000+02
0.00000
1.11862+00
1.11000+02
9.19000+02
0.00000
1.11862+00
1.06000+02
fl. 40000+02
2.61441+0?
o.nooon
o.oonon
0.00000
2.15176+02
0.00000
o.oooon
o.ooonn
2.12071+0?
0.00000
o.ooono
O.OOOOP
1.41899+02
0.00000
0.00000
0.00000
1.33929+02
0.00000
0.00000
o.ooono
1.37137+02
0.00000
0.00000
0.00000
1.35482+02
0.00000
0.00000
0.00000
2.55645+02
?. 87426 + 00
o.oooon
0.00000
2.55*45+0?
2.87426+00
o.nooop
O.OOPPO
2.55645+0?
?.fl742f.+no
0 . 0 P 0 0 0
o . n n n c o
5.21832+0?
l.oooon+02
6.000011 + 00
o.ooonn
4.29561+0?
8.?3200+01
o.onono
o.ooono
H. 23220+02
8.11000+01
8.00000+00
0.00000
2.83188+02
5.42700+01
o.ooono
0.00000
2.67288+02
5.12200+nl
o.oooon
0.00000
2.73661+02
5.244nO+Ol
6.00000+00
0.00000
2.70475+02
5.18300+01
6.00000+00
o.ooono
4.167*3+02
l.OOOOU+0?
o.ooonn
o.ooono
4.16753+02
i.ooonn+02
0.00000
o.ooono
4.16753+0?
i.noonn+o?
o . o n o n o
c. ooooo
6.34931+05
i.iosno+n?
0.00000
2.50000+01
6.34931+05
1.13000+02
0.00000
2.80000+01
6.34931+05
1.13300+0?
0.00000
3.50000+01
6.34931+05
1.27000+02
0.00000
2.10000+01
6.34931+05
1 .11000 + 02
0.00000
2.40000+01
6.34931+05
1.25000+02
0.00000
1.90000+01
6.34931+05
1.13600+02
0.00000
8.60000+01
8.43840+05
1.12000+0?
o . n o o n o
2.00000+01
8.43840 + 0"*
1.11000+0?
0.00000
0.00000
8. 43840+05
1 .06000+0?
0.00000
?. 00000 + 01
i .eonon+ni
2.20000+00
n.ooooo
n. ooono
1.60000+01
?.6onoo+no
o.noooo
n.ooono
1.60000+01
2.70000+00
0.00000
n.ooooo
2.4ooon+oi
4.9noon+no
0.00000
o.ooono
2.40oon+ni
2.40000+00
0.00000
0.00000
i.eooon+oi
4.60000+00
0.00000
0.00000
i.aoooo+oi
2.80000+00
0.00000
0.00000
2.40000+01
2.40000+00
n.oonno
0.00000
2.40000+01
2.30000+00
0.00000
o.onnoo
?.4ooon+oi
i.ssnno+oo
o.ooopn
0.00000
i.ooooo+nu
o.onono
3.t»?769 + 01
o.nnnoo
i.oooon+oo
o.nnooo
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.onooo
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
o.onooo
1.00000+00
0.00000
3.92769+01
o.onooo
i. onooo+oo
0.00000
3.92769+01
o.onooo
l. onooo+oo
O.OOOPO
4. 00602 + 01
o.onono
1.00000+00
0.00000
4.00602+01
o.onono
1 .00000 + 00
o.oonoo
4.pn60? + (ll
o.ppnon
1 .uooon+on
0 . U 0 0 0 0
2.00000+00
o.noono
1.00000+00
o. or ooo
i.ooooo+on
o.ooonn
1.00000+00
O.OPOOO
2. onooo + oo
o.oooon
1.00000+00
o.ooonn
1.00000+00
O.UPOOO
1.00000+00
0.00000
1.00000+00
o.ononn
1.00000+00
0.00000
?."0000+00
0.00000
1.00000+00
o.nooon
2.00000+00
o.noono
0.00000
o.ooonn
l .nnoon+oo
o.uoono
o.ooono
O.OOOPO
1.00000+00
o.oooun
O.OPOOO
0. '10000
1 .00000 + 00
o.nnopn

-------
                   TABLE C-6.  (Continued)
HORI70NTALLY  OPPOSFD GflS  FIRFD  BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
14
1
2
3
0 «»
Ol
U> j
2
3
4
1
2
3
4
1
2
3
<4
1
2
3
14
1
?
3
•4
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5

5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
5
S
2
?
2
2
2
?
2
3
2
2
2
2
?
2
2
2
2
?
2
2

2
2
2
2
2
?
2
2
2
?
2
2
?
2
2
?
?
?
?
?
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1

1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
41
41
11
41
42
42
42
42
43
43
43
43
44
44
44
44
45
45
45
45

46
46
46
46
47
47
47
47
48
48
48
48
49
49
49
49
50
50
50
50
0.00000
1.11862+00
1.10000402
3.00000*02
0.00000
1.11662+00
7.42500+01
3.81000+02
0.00000
1.11862+00
6.65500+01
2.05000+02
0.00000
1.11862+00
1.05100+02
4.77000+02
0.00000
1.11862+00
1.10000+02
3.00000+02

0.00000
1.11662+00
1.02300+02
1.72000+02
0.00000
1.11862+00
7.33300+01
8.00000+01
0.00000
1.11*62+00
6.62700+01
4.30000+01
0.00000
1.11862+00
1.16200+02
3.57000+02
0.00000
I.llfl62+00
1.07200+02
2.15000+02
1.1105ft+02
?.«7o26+oo
0.00000
o.onnno
?. 55645+0?
2.«7426+On
o.ooonn
0.00000
2.55645+02
2.67426+00
0.00000
0.00000
2.55645+02
2.87426+00
0.00000
0.00000
1.11056+02
2.87426+On
o.ooono
0.00000

1.11056+0?
2.87426+00
2.70000+01
0.00000
1.11056+02
?.«7426+00
?. 70000 + 01
0.00000
1.07330+02
?.fl7426+0n
2.70000+01
0 . f 1 0 0 0 0
l.«2574+02
?.e7i»?6*nn
o.ooonn
o.ooono
1 .«2f)7<* + n2
?.*7«?f,+on
0 . o o n P n
o . n o n n n
i.aioio+o?
«t.343no + ni
o.ooono
o.oooon
4.16753+0?
1.00000+02
8.00000+00
o.ooooo
4.16753+02
i.oooon+02
8.00000+00
0.00000
4.16753+02
1.00000+02
o.oooon
0.00000
1.81010+02
4.34300+01
0.00000
o.oooon

1.81010+02
4.34300+01
o.oooon
o.oooon
1.81010+02
4.343on+0l
8.00000+00
0.00000
1.7504fl+02
4.20000+01
e.oooon+oo
0.00000
2.9769-9 + 0?
7.14300+01
0.00000
o.noooo
2.97699+0?
7.i43nn+ni
o.ooono
n . u o o n o
8.4381*0 + 05
1.10000+02
0.00000
2.00000+01
P. 43840 + 05
1 .11400 + 02
o.onooo
2.00000+01
6.43840+05
1.11400+02
0.00000
1.63000+02
8.43840+05
1.13900+02
0.00000
2.00000+01
6.43840+05
1.10000+02
0.00000
2.00000+01

8.43840+05
1.10800+02
0.00000
2.00000+01
8.43640+05
1.10000+0?
0.00000
2.00000+01
8.43840+05
1 .07700+02
0.00000
0.00000
8.43840+05
1 .16200+0?
0.00000
0.00000
8.43840+05
l.i6?nn+o?
0.000 (HI
d.o do no
2.40000+01
2.10000+00
0.00000
0.00000
1.60000+01
2.35oon+no
o.onooo
o.ooono
1.60000+01
2.35000+00
0.00000
o.oonoo
2.40000+01
2.80000+00
0.00000
0.00000
2.40000+01
2.10000+00
o.ooono
0.00000

2.40000+01
2.20000+00
o.oonoo
0.00000
1.60000+01
?.ionon+oo
0.00000
n. ooooo
1 .60000+01
i.65oon+on
n. ooooo
0.00000
?.«*oooo+ni
3.?onoo+oo
o.oonno
n.oonno
?.<*onnn + nl
^.Ponon+no
n . n n n o n
n .oootio
i.onooo+oo
o.onooo
4.00602+01
0.00000
1.00000+00
o.onoon
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
o.onooo
4.00602+01
o.onooo
1.00000+00
0.00000
4.00602+01
0.00000

1.00000+00
0.00000
4.00602+01
0.00000
1 .00000+00
o.onono
4.00602+nl
o.onooo
1.00000+00
0.00000
4.00602+01
0.00000
i.onooo+oo
0.00000
4.nn6o2+oi
o.ononn
i.onono+on
o . n o o n n
« .pnen^ + ni
0 . n n o n u
o.oooon
o.iinonn
i.uuoon+oo
o.'ioonn
o.ooono
o.ooono
2.UOOOO+00
0.00000
o.ooono
o.oooon
4.00000+00
o.oooon
o.oooon
o.oooon
3.00000+00
0.00000
0.00000
o.oooon
1.00000+00
o.ooouo

o.ooonn
0.00000
7.1)0000 + 00
0.000^0
o.uooon
o.noonn
6.00000+00
0.00000
o.onoon
o.ooono
e.onoon+on
0.00000
o.ooono
o.ononn
l.ooono+on
o . o n o n n
o.nnoon
o . 1 1 n o n o
3. oo 1*004. no
o. 11 noun

-------
                   TABLE  C-6.   (Continued)
HORIZONTALLY OPPOSED GAS  FIRFO BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
i*
1
2
3
0 4
CD
*» 1
2
3

-------
                    TABLE C-6.  (Continued)
HORIZONTALLY OPPOSED GAS  FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
"»
1
2
3
4
1
2
0 3
i 4
in
471 1
2
3
**
1
2
3
4
1
2
3
"
1
2
3
4
1
2
3
14
6
6
6
6
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7

7
7
7
7
7
7
7
7
7
7
7
7
8
8
8
8
8
8
8
8
?
?
?.
2
?
2
?
?
2
2
2
•>_
P
2
?
2
2
2
2
2

2
2
2
2
2
?
?
2
?
?
?
2
?
?
2
2
?
?
?
?
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1

1
1
1
1
1
1
1
1
1
1
1
1
1
1





1
61
61
61
61
62
62
62
62
63
63
63
63
64
64
64
64
65
65
65
65

66
66
66
66
67
67
67
67
68
68
68
68
69
69
69
69
70
70
70
70
0.00000
1.11862+00
9.74800+01
5.70000+01
0.00000
2.43840+00
8.19500+01
3.44000+02
0.00000
2.43840+00
5.96100+01
1.35000+02
0.00000
2.43840+00
6.79400+01
1.93000+02
0.00000
2.43840+00
5.81800+01
1.34000+02

0.00000
2.43840+00
1. 45100+02
1.34000+02
0.00000
2.43840+00
1.09600+02
3.30000+02
0.00000
2.43840+00
7.45600+01
2.10000+02
0.00000
2.43840+00
6.01800+01
1.0'«000 + 02
0.00000
2.43840+00
1.33000+02
1.25000+02
1.09503+02
2.87426+00
2.60000+01
0.00000
2.68065+02
2.13360+00
4.00000+00
0.00000
2.68065+02
2.13360+00
0.00000
0.00000
2.68065+02
2.13360+00
0.00000
0.00000
2.68065+02
2.13360+00
4.00000+00
0.00000

9.0"»590 + 01
2.13360+00
3.80000+01
0.00000
9.0"»590 + 01
?. 13360+00
3.60000+01
0.00000
2.?2jl8+02
2.13360+00
5.00000+00
0.00000
?.?231«+02
?. 13360+00
O.ononn
o.onoon
9.04*90+01
? . 13360 + 00
5.2000n+nj
o . n o n r, n
1.78455+02
4.28200+01
0.00000
0.00000
2.04197+02
1.00000+0?
0.00000
0.00000
2. 04197+02
1.00000+02
4.00000+00
0.00000
2.04197+02
1.00000+02
2. 00000+00
0.00000
2.04197+02
1.00000+02
4.00000+OU
0.00000

6.89276+01
3.37500+01
0.00000
0.00000
6.89278+01
3.37500+01
0.00000
0.00000
1.69338+02
8.29200+01
2.00000+00
n.ooono
1.69338+02
8.29200+01
4.00000+00
0.00000
6.89278+01
3.37500+01
0 .ooonn
o.ooono
8.43840+05
1.05600+0?
0.00000
6.00000+01
5.69006+05
1.09300+02
0.00000
0.00000
5.69006+05
1.19200+02
0.00000
8.70000+01
5.69006+05
1.08700+0?
0.00000
1.75000+02
5.69006+05
1 .16400 + 02
o.ooono
0.00000

5.69006+05
1.45100+02
0.00000
1.30000+01
5.69006+05
1 .09600 + 02
0.00000
0.00000
5. 69006+0-5
1.19300+0?
0.00000
6.00000+01
5.69006+05
1.20400+0?
0.00000
o.onooo
5.69006+05
1.33000+0?
o.noono
O.OOOdO
2.40000+01
1.23000+00
o.oonon
0.00000
1.20000+01
1. 95000+00
n. ooooo
0.00000
8.00000+00
3.65000+00
0.00000
0.00000
1.00000+01
1.85000+00
0.00000
0.00000
8.00000+00
3.20000+00
0.00000
0.00000

1.20000+01
6.95000+00
0.00000
0.00000
1 .20000+01
2.05000+00
0.00000
0.00000
1.00000+01
3.70000+00
0.00000
0.00000
8. 00000 + 00
3.82000+00
0.00000
o.oonoo
1 .20000 + 01
5.*.5onn + po
n. ooooo
0.00000
1.00000+00
o.onooo
4.00602+01
o.ooono
1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000

1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
o.onooo
4.pn6n2+oi
o.onooo
1.00000+00
o.onooo
4.00602+01
0.00000
1. 00000+00
0.00000
4.nof-02 + 01
0.00000
l.onooo+no
o.noono
<4. On (,02 + 01
o . nnonn
o.uoooo
0. Op 000
7.UOOOO+00
o.ooooo
0 . 0 o o o n
o.oooon
7.UOOOO+00
o.uooun
0.00000
0.00000
4.00000+00
o.uoonn
o.uoooo
o.ooooo
4.0POOO+00
0.00000
o.oooon
0.00000
8.00000+00
o.ooooo

0.00000
o.ooono
5.00000+00
o.oooon
O.UOOOO
o.ooono
5.00000+00
o.ooooo
o.oooon
O.UOOOO
8.oooon+on
o. ooonn
o. ooonn
0. OOOnn
4,ononn+oo
o.unono
O.uoonn
(i. no (inn
5. uoouo + iin
n . uijonn

-------
                                                   TABLE C-6.   (Concluded)
                               HORIZONTALLY OPPOSED GflS  FIRED BOILI.HS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
A
8
a
8
8
8
a
8
8
8
8
8
8
8
8
8
2
?
2
2
?
2
?
?
2
2
2
2
2
2
2
2
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
71
71
71
71
72
72
72
72
73
73
73
73
74
7«t
7<»
74
0.00000
2.43840+00
1.0B300+02
9.90000+01
0.00000
2.43840+00
8.25000+01
3.26000+02
0.00000
2.43840+00
8.15300+01
1.86000+02
0.00000
2.43840+00
8.37200+01
2.30000+02
<». 04*90 + 01
2.13360+dO
2. 70000 + 01
o.ooonn
2.68065+02
2.13360+00
0.00000
o.oooon
2.01101+0?
2.13360+00
1.20000+01
0.00000
2.01101+02
2.13360+00
1.00000+01
0.00000
fr. 89278+01
3.37500+01
0.001)00
0.00000
2.0>»197+02
1.00000+02
O.OOOPO
0.00000
1.53155+02
7.50000+01
0.00000
0.00000
1.53155+02
7.50000+01
0.00000
0.00000
S. 69006+05
1 .U4000 + 02
0.00000
0.00000
5.69006 + 0«>
1 .10000 + 02
0.00000
0.00000
5.69006+05
1.08700+02
0.00000
0.00000
5.69006+05
1.11600+02
0.00000
o.ooono
1.20000+01
K.^SOOO+OO
0.00000
0.00000
1.20000+01
2.10000+00
0.00000
0.00000
1.20000+01
1.P5000+00
0.00000
0.00000
1.20000+01
2. 40000+00
0.00000
0.00000
1.00000+00
O.onooo
4.00602+01
o.onono
1. 00000+00
0.00000
4.00602+01
O.onooo
1.00000+00
0.00000
H. 00602+01
0.00000
1.00000+00
0.00000
4.00602+01
o.ooono
o.noooo
o.unooo
7.LOOOO+00
0 . U 0 0 U 0
o.ooooo
o.ooonn
3. 00 000+00
n.nonuo
0.00000
0.00000
7.00000+00
0.00000
o.uoooo
o.unooo
7.00000+00
o.uoouo
o

-------
TABLE C-7.  N0  CONTROL TEST DATA FROM SINGLE WALL GAS-FIRED BOILERS
1
2
3
4
1
2
3
1
2
3
1
2
3
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
1
2
3
it
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1

3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
S
3
3
3
3
3
3
3
j
3
3
i
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
2
2
2
2
3
3
3
3
4
4
4
4
5
5
5
5
6
6
6
6
7
7
7
7
8
8
8
8
9
9
9
10
10
10
10
0.00000
0.00000
1.13900+02
3.B7000+02
0.00000
0.00000
1.05300+02
3.31000+02
0.00000
0.00000
1.01700+02
3.34000+02
0.00000
0.00000
8.67000+01
2.01000+02
0.00000
0.00000
7.86000+01
1.56000+02
0.00000
0.00000
8.74000+01
1.95000+02
0.00000
0.00000
1.11000+02
2.30000+02
0.00000
0.00000
1.05000+02
1.88000+02
0.00000
0.00000
8.67000+01
1.33000+02
0.00000
0.00000
7.89000+01
fl.POOOO+01
2.59992+02
o.oooon
0.00000
0.00000
2.63097+02
o.oonoo
0.00000
o.oooco
2.59992+02
0.00000
0.00000
0.00000
2.59992+02
o.ooono
0.00000
0.00000
2.61027+02
0.00000
0.00000
0.00000
2.61027+02
0.00000
0.00000
0.00000
1.61874+02
0.00000
0.00000
0.00000
1 .57630+0?
0.00000
O.OOOOP
o.nonco
1.58458+0?
0.00000
0.00000
o.oonoo
o.ooonn
o.oonoo
o . o n a n n
2.52399+0?
1.01700+02
0.00000
O.OOOOC
2.55396+02
1.02900+02
o.oooon
o.ooono
2.52399+02
1.01700+02
0.00000
0.00000
2.52399+02
1.01700+02
4.00000+00
o.ooono
2.53408+02
1.02100+02
4.00000+00
0.00000
2.53408+02
1.02100+02
4.0000U+00
o.oooon
1.57193+02
6.33300+01
0.00000
o.ooono
1.53061+02
6.16700+01
0.00000
o.ooono
1.53881+02
6.20000+01
4.00000+00
0.00000
1.57193+n2
6. 33300+01
4.ooonu+nn
n . o o o n ij
4.70265+05
1.13900+0?
n. ooooo
1.40000+01
4.70265+05
1.05300+02
0.00000
8.40000+01
4.70265+05
1.04700+02
0.00000
5.40000+01
4.70265+05
1.15600+02
0.00000
l.SOOOO+Oi
4.70265+05
1.04600+02
0.00000
5.00000+01
4.70265+05
1.16600+02
0.00000
1.60000+01
4.70265+05
LllOOO + 02
n. noooo
1.50000+01
4.70265+05
1.05000+0?
0.00000
1.70000+01
4.70265+05
1.15600+0?
0.00000
1.50000+01
4.7(1265 + 05
1 .05100 + 02
o.onono
i ,?oono+o2
1.60000+01
2.78000+00
0.00000
0.00000
1.60000+01
1.1500P+00
0.00000
0.00000
1.60000+01
1.05000+00
0.00000
0.00000
1.20000+01
3.08000+00
0.00000
0.00000
1.20000+01
1.05000+00
0.00000
0.00000
1.20000+01
3.23000+00
0.00000
0.00000
1. 60000+01
2.35000+00
0.00000
o.oonno
i ,6onon+oi
1.05000+00
o.oonoo
n. ooooo
1. 20000+01
3.08000+00
0.00000
o.oonno
i.2onnn+oi
i .unon + oo
n. ooono
n.oonno
i.onooo+oo
o.ooooo
3.92769+01
o.onooo
1.00000+00
o.onooo
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
o.onooo
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
o.onooo
i.oonoo+no
o.oouno
3.92769+01
0.00000
1.00000+00
o.oooon
3.92769+01
O.onono
l.nnono+on
n. on ono
3.92769+01
0 . o n n n o
1 .00000 + 00
o.onoon
1. UOOOO+OO
o.noooo
1.00000+00
o.ooono
1.00000+00
o.ooono
1.00000+00
0.00000
1.00000+00
o.ooono
1.00000+00
0.00000
2.00000+00
0.00000
1.00000+00
0.00000
2.00000+00
o.ooooo
1. 00000+00
o.ooooo
2.00000+00
o.oooon
1.00000+00
0.00000
1.00000+00
O.f'OOOO
1. UOOOO + OO
o.uoooo
1. UOOOO+OO
o.nooon
1.00000+00
o.noooo
?.uooon+nn
O.t'ooon
1 ,'inoon + on
o . u n o n n
2. 1'oooo + nn
n. u en no

-------
                    TABLE C-7.  (Continued)
FRONT WflLl  GOS  FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
0 3
1 4
cn
°° 1
2
3
<«
1
2
3
4
1
2
3
4
1
2
3
U
1
2
3
it
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
2
2
2
2

2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
2
?
j
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3
3
3
3
3
3
3
*
*
3
i
3
^
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1

1
I
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
11
11
11
11
12
12
12
12
13
13
13
13
14
1"»
14
14
15
15
15
15

16
16
16
16
17
17
17
17
18
18
18
18
19
19
19
19
20
20
20
20
o.oonoo
o.oonoo
1.15000+02
1.16000+02
0.00000
0.00000
1.06000+02
1.08000+02
0.00000
0.00000
9.53000+01
a. loooo+oi
0.00000
0.00000
9.00000+01
6.60000+01
0.00000
0.00000
1.22500+02
<». 97000 + 02

0.00000
0.00000
1.12700+02
4.21000+02
0.00000
o.onooo
1.06900+02
3.76000+02
0.00000
0.00000
9.49000+01
3.11000+02
0.00000
0.00000
1.26000+02
9.00000+01
0.00000
0.00000
9.B4QOO+01
6.?ooon+ni
6. 95275+01
o. notion
0.00000
0.00000
«.95?75+01
0.00000
0.00000
0.00000
8. 95275+01
0.00000
o.ooono
0.00000
8.95275+05
0.00000
0.00000
0.00000
2.58129402
0.00000
0.00000
0.00000

2.58129+02
0.00000
0.00000
0.00000
2.58129+02
0.00000
0.00000
0.00000
2.58129+02
0.00000
0.00000
o.oooon
6.10650+01
0.00000
0.00000
0.00000
6.10650+01
o.noooo
o.onnnn
o.onnno
P. 68774+01
3.50000+01
0.00000
o.oooon
fl. 68774+01
3.50000+01
o.oooon
0.00000
8.68774+01
3.50000+01
2.00000+00
0.00000
8.66774+01
3.50000+01
2.00000+00
0.00000
2.96058+02
9.13600+01
0.00000
0.00000

2.96058+0?
9.13600+01
0.00000
0.00000
2.96058+02
9.13600+01
2.00000+00
0.00000
2.96058+02
9.13600+01
2.00000+00
0.00000
7.0000^+Dl
2.16000+01
0.00000
o.nponn
7.00004+01
2.16000+01
2.00000+00
o . n o o n o
4.70265 + 0*5
1.15000+0?
0.00000
1.30000+01
4.70265+05
1.06000+0?
fl. 00000
1.30000+01
4.70265+05
1.14400+02
0.00000
1.60000+01
4.70265+05
1.06000+02
o.ooono
8. 00000+01
2.54324+05
1.22500+02
0.00000
5.20000+01

2.54324+05
1.12700+02
0.00000
1.77000+02
2.5432i* + 05
1.2B300+0?
0.00000
5.60000+01
2.54324+05
1. 13800 + 02
0.00000
2.90000+02
2.54324+05
1.26000+0?
0.00000
5.2000P+01
2.S4324 + 01*
1.18100+0?
0.00000
2.) nooo+o?
1.20000+01
3.05000+00
0.00000
0.00000
1.20000+01
1.23000+00
0.00000
0.00000
1.00000+01
2.86000+00
0.00000
0.00000
1.00000+01
1.07000+00
0.00000
0.00000
1.20000+01
4.18000+00
0.00000
0.00000

1 .20000+01
2.59000+00
0.00000
0.00000
1.00000+01
5.03000+00
0.00000
0.00000
l.OOOOO+Ol
2.80000+00
0.00000
0.00000
l.ooooo+ni
4.65POn+00
0.00000
o.oonon
l.OOOOO+Ol
3.5nnon+no
0.00000
o . o o o n o
1.00000+00
o.ooono
3.92769+01
0.00000
1.00000+00
0.00000
3. 92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1. 00000+00
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+ni
0.00000

1.00000+00
0.00000
3.92769+01
0.00000
i.onooo+oo
0.00000
3.92769+01
0.00000
1.00000+00
0.00000
3.92769+01
0.00000
1.00000+00
o.onooo
3.92769+01
O.onoon
1.00000+00
o.onooo
3.9P769+01
o . n n n n o
l. onooo+oo
o.Linooo
1. 00000 + 00
o.noooo
1 .00000+00
o.ooooo
1.00000+00
o.uoooo
1.00000+00
0.00000
2.00000+00
o.ooooo
1.00000+00
o.ooono
2.00000+00
o.uoooo
o.ooooo
0.00000
1.00000+00
o.ooooo

o.ooooo
o.ooooo
1.00000+00
o.uooon
o.onooo
o.uoooo
2.00000+00
o.uoouo
o.uoooo
0.00000
?.unooo+oo
o.ooooo
o.ooooo
o.ooooo
1.00000+00
o.onono
o . n P o u n
n.noopn
?. iooon+on
n . ''OOPM

-------
                   TABLE C-7.   (Continued)
FRONT WALL  RAS  FIRED BOILERS
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
4
1
2
3
0 4
in
*> 1
2
3
i»
1
2
3
4
1
2
3
<4
1
2
3
"4
1
2
3
14
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
4
4
4
4
4
4
nunn

-------
                                                 TABLE C-7.   (Continued)
                              FRONT WALL GflS   FIRED ROILFRS
o
8
1
2
3
it
1
2
3
14
1
2
3
4
1
2
3

-------
                   TABLE C-7.  (Concluded)
FRONT WALL  GAS  FIRED BOILERS
1
2
3
i»
1
2
3
4
1
2
3
«»
1
2
3
4
1
2
3
0 4
0>
»- 1
2
3
4
1
2
3
<4
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7
7

7
7
7
7
4
I*
4
i»
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3

3
3
3
3
3
3
3
3














1
1
1
1
1
1

1
1
1
1
1
1
1
1
41
41
HI
«u
42
42
42
42
43
43
43
43
44
44
44
44
45
45
45
45

46
46
46
46
47
47
47
47
0.00000
1.96120+00
1.05000+02
3.14300+02
0.00000
1. 98120+00
6.00000+01
1.09600+02
0.00000
1.98120+00
7.60000+01
1.2o2oO+o2
0.00000
1.98120+00
1.12000+02
2.67100+02
0.00000
1.98120+00
8.00000+01
7.50000+01

0.00000
1.96120+00
9.30000+01
5.59000+01
0.00000
2.43A40+00
7.49400+01
1.15100+02
2.57197+02
0.00000
O.OOOPO
0.00000
2.49953+02
o.onooo
0.00000
0.00000
2.55645+02
0.00000
0.00000
0.00000
1.71P10+02
0.00000
4.00000+00
0.00000
1.70465+02
0.00000
4.00000+00
0.00000

8.51805+01
0.00000
5.00000+01
0.00000
1 .89405+02
o.oonoo
1.20000+01
o.ooono
2.49696+02
1.00600+02
o.oooon
o.oooon
2.42683+02
9.77BOO+01
4.00000+00
0.00000
2.48203+02
1.00000+02
4.00000+00
0.00000
1.66846+02
6.72200+01
0.00000
0.00000
1.65456+02
6.66700+01
4.00000+00
o.oooon

8.27134+01
3.33300+01
2.00000+00
0.00000
2.54355+02
9.583nO+Ol
4.00000+00
0.00000
4.70265+0^
1.05000+02
0.00000
0.00000
4.70265+0"5
1.16800+02
0.00000
6.10000+01
4.70265+05
1.04900+02
0.00000
0*00000
4.70265+05
1.12000+02
0.00000
2.89000+01
4.70265+05
1.06100+02
0.00000
0.00000

4.70265+05
1.11200+02
0.00000
0.00000
5.17731+OS
1.12400+02
0.00000
1.95100+01
1.6QOOO+01
1.13000+00
0.00000
0.00000
1.60000+01
3.30000+00
0.00000
0.00000
1.60000+01
1.06000+00
0.00000
n. ooooo
1.60000+01
2.33000+00
0.00000
o.ooono
1.60000+01
1.33000+00
0.00000
0.00000

1.20000+01
2.33000+00
n. ooooo
0.00000
6. 00000+00
2.55000+00
0.00000
0.00000
i.onooo+uo
o.onooo
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000
l.onooo+oo
o.onooo
4.00602+01
0.00000
1.00000+00
0.00000
4.00602+01
0.00000

1.00000+00
o.onooo
4.00602+01
0.00000
i.onnoo+oo
o.onooo
4.00602+01
o.onooo
i.ooooo+on
o.ooono
l.ooooo+oo
0 . n o o o n
1. 00000 + 00
0.00000
2.00000+00
o.uoooo
1.00000+00
0.00000
2.UOOOO+00
o.oouon
1.00000+00
0.00000
5.00000+00
o.noouo
1.00000+00
0.00000
6.00000+00
o.ooono

i.ooono+oo
0.00000
6.00000+00
O.UOOOO
1.00000+00
0.00000
6.oooon+oo
o.ooonn

-------
                                 APPENDIX D
             NOV EMISSIONS CORRELATION:  ANALYSIS OF VARIANCE
               A

       The correlation of NO  emissions with boiler/burner design and
                            A
operating variables by multiple regression analysis was presented in
Section 4.  The analysis of variance for the regression equations are
given in Tables D-l through D-7 of this appendix.
       The multiple regression analysis was performed in a stepwise
manner.  The contribution of each variable towards explaining the total
variance as it enters the regression equation and  its corresponding
partial F ratio are tabulated  in the Analysis of Variance  (ANOVA) tables.
The variance explained  by the  final regression  equation and  its  F ratio
are also shown therein.  The expression for NO  emissions  which  best
correlates the data is  then given.  Finally,  the correlation coefficients
and the standard error  of the  estimate are  presented.
                                     D-l

-------
      TABLE D-l.  ANALYSIS OF VARIANCE:  TANGENTIAL COAL-FIRED BOILERS

Second Order Multiple Regression Model
Source
Regression
X2
X1X2/X2
X1X2» X1X2
X3X4 2 >X1X2'X1
x /x xx v xx
Residual
Total
Degrees of
Freedom
5
1
1
1
1
1
134
139
Sums of
Squares
1447287.8
1103214.2
207911.3
45190.1
54471.1
36501.1
484385.3
1931673.1
Mean Square
289457.6
1103214.2
207911.3
45190.1
54471.1
36501.1
3614.8

F-Ratio
80.1
305.2
57.5
12.5
15.1
10.1


Regression Equation:

   y = 184.2 + 1.597 (x2) + 1.083 x 10'? (x!)(x2) -1.673 x 10-5 (xl) +

       2.494 x 10-6 (x3)(x4) + 6.536 x 10-14 (X1)2

where

   y  = NOX emissions, ppm dry @ 3% 02
   xi = Heat input per active burner, W
   x2 = Stoichiometry to active burners, percent
   X3 = Surface heat release rate, W/m^
   x  = Furnace Stoichiometry, percent

Correlation coefficient           = 0.866
Variation explained by regression = 74.9%
Standard of error of the estimate = 61 ppm
                                       D-2

-------
     TABLE D-2.   ANALYSIS OF VARIANCE:  OPPOSED WALL COAL-FIRED BOILERS

First Order Multiple Regression Model

Analysis of Variance:
Source
Regression
xl
X2/X1
x3/X!,x2
X4/XJ.X2.X3
x5/x1.x2,x3fx4
x6/Xl,x2,x3,x4,x5
Residual
Total
Degrees of
Freedom
6
1
1
1
1
1
1
46
52
Sums of
Squares
832568.1
583727.5
54378.7
112734.9
22602.5
33071.8
26052.7
175186.4
1007754.8
Mean Square
138761.4
583727.5
54378.7
112734.9
22602.5
33071.8
26052.7
3808.4

i
F-Ratio
36.4
153.3
14.3
29.6
5.9
8.7
6.8


 Regression  Equation:

   y  = 470.5 + 5.378  (xj)  + 4.24 x 10'6 (xj)  + 7.41 (x3) - 5.838 (x4)  -

        6.639 x 101 (x5)  +  2.463 x 101 (x6)

 where

   y  = NOX Emissions, ppm  dry @ 3% 02
   X} = Stoichiometry to  active burners, percent
   X2 = Heat input per active burner, W
   x3 = Number of burners firing
   x4 = Flue gas recirculation
   X5 = Number of division  walls
   X5 = Excess Oxygen

 Correlation coefficient           =  0.91
 Variation explained by regression =  82.6%
 Standard of error of the estimate =  62 ppm
                                        D-3

-------
     TABLE D-3.  ANALYSIS OF VARIANCE:  SINGLE WALL COAL-FIRED BOILERS

Second Order Multiple Regression Model

Analysis of Variance:
Source
Regression
X2X3
X2x4/x2x3
1 C' Xp^o 9*^0* A
X-^/X^X^.X^
X1x2/x2x3,x2x4,x1x5,x1x4
Residual
Total
Degrees of
Freedom
5
1
1
1
1
1
81
86
Sums of
Squares
1149017.8
691878.5
409677.2
26315.2
9948.0
11198.9
304997.5
1454015.3
Mean Square
229803.6
691878.5
409677.2
26315.2
9948.0
11198.9
3765.4

F-Ratio
61.0
183.8
108.8
7.0
2.6
2.9


Regression Equation:

  y  = 139.8 + 4.502 x 10-6 (X1)(x2) + 1.978 x 10-1 (X2)(x3) + 7.573 x 10-8 (x2)(x4)

       - 1.023 x ID-ID (x1)(x4) + 6.948 x 10'5 (x!)(x5)

where

  y  = NOX emissions, ppm dry @ 3% 02
  xj_ = Surface heat release rate, W
  X£ = Stoichiometry to active burners, percent
  X3 = Number of burners firing
  x4 = Heat input per active burners, W
  xg = Furnace excess oxygen, percent

Correlation coefficient           =  0.889
Variation explained by regression = 79.0%
Standard of error of the estimate = 61.7 ppm
                                    D-4

-------
     TABLE D-4.   ANALYSIS OF VARIANCE:  OPPOSED WALL OIL-FIRED BOILERS

Second Order Multiple Regression Model

Analysis of Variance:
Source
Regression
X1X2
2
X3 /X1X2
X X /X X X
2
X5/X1X2'X3 >X1X4
Residual
Total
Degrees of
Freedom
4
1
1
1
1
52
56
Sums of
Squares
289322.0
174375.3
36357.0
68805.5
9784.2
69940.4
359262.4
Mean Square
72330.5
174375.3
36357.0
68805.5
9784.2
1345.0

F-Ratio
53.8
129.6
27.0
51.2
7.3


 Regression  Equation;

   y  = -228 + 1.046 x 10~1 (Xl)(x2) + 7.227 x 10'3 (x3)2 - 1.301 (xi)(x4)

        + 2.392 (x5)

 where

   y  = NOX Emissions, ppm dry @ 3% 03
   xi = Firing rate, percent
   X2 = Number of burners firing
   X3 = Stoichiometry to active burners
   x4 = Number of division walls
   X5 = Furnance Stoichiometry, percent

 Correlation coefficient           =  0.897
 Variation explained by regression = 80.5%
 Standard of error  of the estimate = 37 ppm
                                        D-5

-------
      TABLE D-5.  ANALYSIS OF VARIANCE:  SINGLE WALL OIL-FIRED BOILERS

Second Order Multiple Regression Model

Analysis of Variance:
Source
Regression
X1X2
X1/X1X2
y y /y y „
34 12 1
X4X5/X1X2'X1»X3X4
2
Residual
Total
Degrees of
Freecjom
5
1
1
1
1
1
56
61
Sums of
Squares
290684.1
130627.9
131447.6
9942.0
13118.5
5548.1
134892.4
425576.5
Mean Square
58136.8
130627.9
131447.6
9942.0
13118.5
5548.1
2408.8

F-Ratio
24.1
54.2
54.6
4.1
5.5
2.3


Regression Equation;

  y  = 172.7 + 2.283 x 10'5 (xi)(x2) - 1.913 x 10-3 (

       - 9.406 x 10-7) (x4)(x5) + 3.602 x 10-U (x4)2

where
                                                         + 6.179 x 10'8 (x3)(x4)
  y  = NOX emissions, ppm dry @ 3% 02
  x^ = Volumetric heat release rate, W
  x2 = Stoichiometry to active burners, percent
  X3 = Total furnace Stoichiometry minus Stoichiometry to active burners, percent
  x4 = Heat input per active burners, W
  X5 = Number of burners out of service

Correlation coefficient           =  0.826
Variation explained by regression = 68.3%
Standard of error of the estimate = 49 ppm
                                       D-6

-------
     TABLE D-6.  ANALYSIS OF VARIANCE:  OPPOSED WALL GAS-FIRED BOILERS

Logarithmic Multiple Regression Model

Analysis of Variance;
                         Degrees of      Sums of
        Source            Freedom        Squares   Mean Square    F-Ratio
  Total
 Regression  Equation;

                  1.271      2.496      -2.665     -0.2668      -0.03517
   y  =  4.42   (x       )  (x       )  (x        )  (x         ) (x         )
                 1234            5

 where

   y  =  NOX  emissions,  ppm dry @ 3% 02
   x^ =  Firing rate,  percent
   X2 =  Stoichiometry to  active burner, percent
   X3 =  Furnace stoichiometry, percent
   X4 =  Number of furnace division walls plus one
   X5 =  Flue gas recirculation plus one, percent

 Correlation coefficient            =   0.871
 Variation explained by regression =  75.8%
 Standard of error of the estimate = 107.2 ppm
                                         D-7

-------
      TABLE D-7.  ANALYSIS OF VARIANCE:  SINGLE WALL GAS-FIRED BOILERS

Second Order Multiple Regression Model

Analysis of Variance:
Source
Regression
X1X2
X1x3/x1x2
X3/ xi xp »X1 X3
X2x4/x1x2,x1x3,x3
Residual
Total
Degrees of
Freedom
4
1
1
1
1
37
41
Sums of
Squares
581913.3
499943.0
75062.7
3702.7
3204.9
54846.0
638747.5
Mean Square
145478.3
499943.0
75062.7
3702.7
3204.9
1482.3

F-Ratio
98.1
337.3
50.6
2.5
2.2


Regression Equation:

  y  = 37.2 + 1.448 x 10'5 (xi)(x2) - 1.852 x 10~4 (xi)(x3)

       + 2.089 x IQl (x3) - 6.461 x 10'3 (x2)(x4)

where

  y  = NOX emissions, ppm dry @ 3% 02
  xi = Surface heat release rate, W
  x2 = Stoichiometry to active burners, percent
  x3 = Number of burners out of service
  X4 = Flue gas recirculation, percent

Correlation coefficient           =  0.949
Variation explained by regression = 91.4%
Standard of error of the estimate = 39 ppm
                                    D-8

-------
                                 APPENDIX E
               INPUTS TO COST ANALYSIS CALCULATION ALGORITHM

       Inputs to the cost analysis calculation algorithm described in
Section 6.2 and typical control cases presented in Section 6.3 are listed
in this appendix.  Table E-l is a glossary of terms used in the cost
analysis computer code, while Tables E-2 through E-7 list the inputs for
each of the control cases treated.
                                     E-l

-------
 TABLE E-l.  GLOSSARY OF TERMS USED IN COST ANALYSIS CALCULATION ALGORITHM

AKW    =   Additional Fan Power Requirements, kW
AROY   =   Annual Royalties, $/yr
Bl     =   Debt/Equity Ratio, fraction
CANAL  =   Cost per Analysis, $
CF1    =   Construction Facilities Factor, fraction
CFE1   =   Construction Field Expense Factor, fraction
CGA    =   Construction General & Administrative Expense, fraction
CON1   =   Contractor's Fee, fraction
CRATE  =   Composite Construction Crew Rate, $/h
CSUPV  =   Construction Supervision Factor, fraction
CTN1   =   Construction Contingency Factor, fraction
DESRAT =   Designer's Rate, $/h
DHRS   =   Design Hours, h
DRATE  =   Derate of Boiler, kW
DS1    =   Engineering Design and Supervision Factor, fraction
EGA    =   Engineering and Design G&A, fraction
EHRS   =   Engineering Hours, h
EOHD   =   Engineering and Design Overhead, fraction
EOOS   =   Equipment Out of Service, $
ER     =   Electric Power Rate, $/kWh
ERAT   =   Engineering Rate, $/hr
ESUPV  =   Engineering Supervision Factor, fraction
Fl     =   Federal Tax Rate, fraction
FCOST  =   Fuel Cost, $/106 Btu (1 Btu = 1.055 kJ)
FEER   =   Engineering Fee, fraction
FPEN   =   Fuel Penalty, fraction
HRATE  =   Heat Rate of Boiler, Btu/kWh (1 Btu = 1.055 kJ)
HRINST =   Installation Time, h
HYR    =   Annual Operation Time, h
1C     =   Initial Charges, $
110    =   Initial Investment of Boiler, $
ILAST  =   Computer Code Counter
INI    =   Insurance Factor, fraction
101    =   Interest on Borrowed Money, Original  Investment,  fraction
                                    E-2

-------
                          TABLE F-l.  (Concluded)

II     =   Interest on Borrowed Money, Present Investment, fraction
K      =   Age of Existing Boiler, yr
KW     =   Power Rating of Boiler, kW
Ml     =   Maintenance Factor, fraction
N      =   Remaining Lifetime of Boiler, yr
NANAL  =   Number of Analyses Required
NLOST  =   Total Lifetime of Boiler, yr
NOBASE =   Baseline NO  Emissions, ppm
                      J\
NOCONT =   Controlled N0v Emissions, ppm
                        A
NOP    =   Number of Operators
OHA1   =   Administrative Overhead Operating Labor Factor, fraction
OHP1   =   Power Plant Overhead, fraction
PPR    =   Purchased Power Rate, $/kWh
RE1    =   Replacement Equipment Factor, fraction
RM     =   Raw Materials, $/yr
R01    =   Return to Equity, Original  Investment, fraction
Rl     =   Return to Equity, Present  Investment, fraction
SCI    =   Startup Cost Factor, fraction
SF1    =   Service Facilities Factor,  fraction
SI     =   State Tax Rate, fraction
TM     =   Total Materials (Hardware)  Required,  $
UF1    =   Utilities Facilities Factor, fraction
WAGE   =   Operating Labor Rate, $/h
                                     E-3

-------
     TABLE E-2.  COST INPUTS FOR RETROFIT OFA FOR TANGENTIAL COAL-FIRED BOILER
AKW     =
AROY    =
Bl      =
CANAL   =
CFE1    =
CF1     =
CGA     =
CON1    =
CRATE   =
CSUPV   =
CTN1    =
DESRAT  =
OHRS    =
DRATE   =
OS1     =
EGA     =
EHRS    =
EOHD    =
EOOS    =
ER      =
ERAT    =
ESUPV   =
FCOST   =
PEER    =
FPEN    =
Fl      =
HRATE   =
HRINST  =
.38200000E+03
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE+00
.13000000E+00
.50000000E-01
.25000000E+00
.70000000E-01
.15300000E+02
.10000000E+00
.11000000E+00
.90000000E+01
.60000000E+03
.OOOOOOOOE+00
.OOOOOOOOE+00
.25000000E+00
.24000000E+03
.11000000E+01
.OOOOOOOOE+00
.25000000E-01
.12000000E+02
.10000000E+00
.13000000E+01
.eoooooooE-oi
.OOOOOOOOE+00
,«*8oonoooE+oo
.92000000E+OU
,35300000E + 0«*
HYR
1C
no
ILAST
INI
101
II
K
KW
Ml
N
NANAL
NLOST
NOBASE
NOCONT
NOP
OHA1
OHP1
RE1
RM
R01
Rl
SCI
SF1
SI
PPR
TH
UF1
WAGE
.70000000E+04
.OOOOOOOOE+00
.32600000E+08
           + 0
.50000000E-02
.80000000E-01
.80000000E-01
           + 5
.22500000E+06
.50000000E-01
          +25
.OOOOOOOOE+00
.30000000E+02
.45500000F+03
.31000000E+03
.OOOOOOOOE+00
.10000000E+00
.20000000E+00
.HOOOOOOOE»02
.OOOOOOOOE+00
.12000000E+00
.12000000E+00
.10000000E+00
.50000000E-01
.60000000E-01
.26000000E-01
.31903000E+05
.30000000E-01
.10000000E+02
                                  E-4

-------
     TABLE E-3.  COST INPUTS FOR RETROFIT OFA FOR OPPOSED WALL COAL-FIRED BOILER
AKW     =
AROY    =
Bl      =
CANAL   =
CFE1    =
CF1     =
C6A     =
CON1    =
CRATE   s
CSUPV   =
CTN1    =
DESRAT  =
DHRS    =
DRATE   =
OS1     =
EGA     =
EHRS    =
EOHD    =
EOOS    =
ER      =
ERAT    =
ESUPV   s
FCOST   =
PEER    =
FPEN    =
Fl      =
HRATE   =
HRINST  =
.91800000E+03
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE+00
.13000000E+00
.50000000E-01
.25000000E+00
.70000000E-01
.15300000E+02
.10000000E+00
.11000000E+00
.90000000E+01
,70000000E+03
.OOOOOOOOE+00
.OOOOOOOOE+00
.25000000E+00
.30000000E+03
.11000000E+01
.OOOOOOOOE+00
.25000000E-01
.12000000E+02
.10000000E+00
.13000000E+01
.80000000E-01
.25000000E-02
.H8000000E+00
.92000000E+OU
.56130000E+OU
HYR
1C
ZIO
ILAST
INI
101
II
K
KU
HI
N
NANAL
NLOST
NOBASE
NOCONJ
NOP
OHA1
OHP1
RE1
RM
R01
Rl
SCI
SF1
SI
PPR
TM
UF1
WAGE
.70000000E+04
.OOOOOOOOE+00
.OOOOOOOOE+00
           *0
.50000000E-02
.eoooooooE-oi
.eoooooooE-oi
           *5
.5HOOOOOOE+06
.50000000E-01
          +25
.OOOOOOOOE+00
.30000000E+02
.76500000E+03
.55000000E+03
.OOOOOOOOE+00
.10000000E+00
.20000000E+00
.40000000E-02
.OOOOOOOOE+00
.12000000E+00
.12000000E+00
.10000000E+00
.50000000E-01
.60000000E-01
.26000000E-01
.66073000E+05
.30000000E-01
.10000000F+02
                                 E-5

-------
      TABLE E-4.  COST INPUTS FOR RETROFIT LOW NOV BURNERS FOR OPPOSED WALL
                                           A

                             COAL-FIRED BOILER
AKW     =
AROY    =
Bl      =
CANAL   =
CFE1    =
CF1     =
CGA     =
COM    =
CRATE   =
CSUPV   =
CTN1    =
DESRAT  =
DHRS    =
ORATE   =
DS1     =
EGA     =
EHRS    =
EOHD    =
EOOS    =
ER      =
ERAT    =
ESUPV   =
FCOST   =
PEER    =
FPEN    =
Fl      =
HRATE   =
HRIMST  =
.OOOOOOOOE+00
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE+00
.13000000E+00
.50000000E-01
.25000000E+00
.70000000E-01
.15300000E+02
.10000000E+00
.11000000E+00
.90000000F+01
.40000000E+03
.OOOOOOOOE+00
.OOOOOOOOE+00
.25000000E+00
.15000000E+03
.11000000E+01
.OOOOOOOOE+00
.25000000E-01
.12000000E+02
.iooooooor+00
.13000000E+01
.BOOOOOOOE-01
.OOOOOOOOE+00
.taooooooF+oo
.92000000E + 0**
.15360000E+05
HYR
1C
110
ItAST
INI
101
II
K
KW
Ml
M
NANAL
NLOST
MOBASE
NOCONT
NOP
OHA1
OHP1
RE1
RM
R01
Rl
SCI
SF1
SI
PPR
TM
UF1
WAGE
,70000000E + 0«f
.OOOOOOOOE+00
.OOOOOOOOE+00
           + 0
.50000000E-02
.eoooooooE-oi
.eoooooooE-oi
           + 5
.5<*OOOOOOE + 06
.50000000E-01
          + 25
.OOOOOOOOE+00
.30000000E+02
.78500000F+03
.39000000E+03
.OOOOOOOOE+00
.10000000E+00
.20000000E+00
.HOOOOOOOE-02
.OOOOOOOOE+00
.12000000E+00
.12000000E+00
.10000000F+00
.50000000E-01
.60000000E-01
.26000000E-01
.33600000E+06
.30000000E-01
.10000000E+02
                                  E-6

-------
        TABLE E-5.  COST INPUTS FOR BURNERS OUT OF SERVICE FOR OPPOSED WALL

                             COAL-FIRED BOILER
AKW     =
AROY    =
Bl      =
CANAL   =
CFE1    =
CF1     =
C6A     =
CON1    =
CRATE   =
CSUPV   =
CTN1    =
OESRAT  =
OHRS    =
ORATE   =
DS1     =
EGA     =
EHRS    =
EOHD    =
EOOS    =
ER      =
ERAT    =
ESUPV   =
FCOST   =
FEER    =
FPEN    =
Fl      =
HRATE   =
HRINST  =
.OOOOOOOOE+OO
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE+00
.13000000E400
.50000000E-01
.25000000E400
.70000000E-01
.15300000E402
.10000000E400
.11000000E+00
.90000000E401
.50000000E402
.10800000E406
.OOOOOOOOE+00
.25000000E400
.6^000000E+03
.11000000E+01
.OOOOOOOOE+00
.25000000E-01
.12000000E+02
.lOOOOOOOE+00
.13000000E+01
.80000000E-01
.25000000E-02
.48000000E+00
.92000000E+04
.24000000E+03
HYR
1C
no
ILAST
INI
101
II
K
KU
Ml
N
NANAL
NLOST
NOBASE
NOCONT
NOP
OHA1
OHP1
RE1
RM
R01
Rl
SCI
SF1
SI
PPR
TH
UF1
WAGE
.TOOOOOOOE-t-Oif
.OOOOOOOOE+00
.83700000E+08
           + 0
.50000000E-02
.80000000E-01
.eoooooooE-oi
           45
.54000000E+06
.50000000E-01
.OOOOOOOOE+00
.30000000E402
.78500000E403
.51000000E+03
.OOOOOOOOE+00
.10000000E400
.20000000E+00
.HOOOOOOOE-02
.OOOOOOOOE+00
.12000000E+00
.12000000E+00
.lOOOOOOOE+00
.50000000E-01
.60000000E-01
.26000000E-01
.OOOOOOOOE+00
.30000000E-01
.10000000E+02
                                 E-7

-------
        TABLE E-6.  COST  INPUTS FOR BURNERS OUT OF SERVICE FOR SINGLE WALL

                         OIL- AND GAS-FIRED BOILER
AKW
AROY
Bl
CANAL
CFE1
CF1
CGA
CON1
CRATE
CSUPV
CTN1
DESRAT
DHRS
DRATE
DS1
EGA
EHRS
EOMD
EOOS
ER
ERAT
ESUPV
FCOST
FEER
FPEN
Fl
HRATE
HRINST
.OOOOOOOOE+00
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE+00
.13000000E+00
.50000000E-01
.25000000E+00
.70000000E-01
.15300000E+02
.10000000E+00
.11000000E+00
.90000000E+01
.30000000E+02
.OOOOOOOOE+00
.OOOOOOOOE+00
.25000000E+00
.50000000E+03
.11000000E+01
.OOOOOOOOE+00
.25000000E-01
.12000000E+02
.10000000E+00
,27000000E*01
.eoooooooE-oi
.25000000E-02
.U8000000E+00
.92000000E+OU
.16000000E+03
HYR
1C
110
ILAST
INI
101
II
K
XW
Ml
N
NANAL
NLOST
NOBASE
NOCONT
NOP
OHA1
OHP1
RE1
RM
R01
Rl
SCI
SF1
SI
PPR
TM
UF1
WAGE
.70000000E + 0
-------
           TABLE E-7.  COST INPUTS FOR RETROFIT FGR/OFA.FOR SINGLE WALL

                         OIL- AND GAS-FIRED BOILER
AKW     =
AROY    =
Bl      =
CANAL   =
CFE1    =
CF1     =
C6A     =
CON1    =
CRATE   =
CSUPV   =
CTN1    =
DCSRAT  =
DHRS    =
DRATE   =
DS1     =
EGA     =
EHRS    =
EOHD    =
EOOS    =
ER      -
ERAT    *
ESUPV   *
FCOST   =
PEER    =
FPEN    -
Fl      =
HRATE   s
HRINST  =
,«»5000000E + 03
.OOOOOOOOE+00
.50000000E+00
.OOOOOOOOE-i-00
.13000000E+00
.50000000E-01
.25000000E+00
.70000000E-01
.15300000E+02
.10000000E+00
.11000000E+00
.90000000E+01
.80000000F+03
.OOOOOOOOE400
.OOOOOOOOE+00
.25000000E+00
.29000000E+03
.11000000E+01
.OOOOOOOOE-fOO
.25000000E-01
.12000000E+02
.10000000E+00
.27000000E+01
.80000000E-01
.50000000E-02
.U6000000E+00
.92000000E+04
HYR     =
1C      =
110     s
ILAST   =
INI     =
101     =
II      =
K       =
KU      =
Ml      =
N       =
NANAL   =
NLOST   *
NOBASE  =
NOCONT  =
NOP     s
OHA1    =
OHP1    =
RE1     =
RM      s
R01     s
Rl      s
SCI     s
SF1     =
SI      =
PPR     =
TM      =
UF1     =
WAGE    =
.70000000E+OH
.OOOOOOOOEt-00
.OOOOOOOOE+00
           *0
.50000000E-02
.eoooooooE-oi
.80000000E-01
           *5
.90000000E+05
.50000000E-01
          +25
.OOOOOOOOE+00
.30000000E+02
.35500000E+03
.15500000E+03
.OOOOOOOOE+00
.10000000E+00
.20000000E+00
.HOOOOOOOE-02
.OOOOOOOOE+00
.12000000E+00
.12000000E+00
.10000000E+00
.50000000E-01
.60000000E-01
.26000000E-01
.191fl5000E+06
.30000000F-01
.10000000E+02
                                 E-9

-------
                                APPENDIX F
                            CONVERSION FACTORS
  To  Obtain
From
                         Multiply By
  ng/J
  ng/J NOX (as  N02)
  ng/J NOX (as  N02)
  ng/J NOX (as  N02)
  NOX ppm @ 3%  02 dry
lb/106 Btu
NOX ppm @ 3% 02 dry
NOX ppm @ 3% 02 dry
NOX ppm @ 3% 02 dry
NOV ppm dry
                         430
                           0.510 (natural gas)*
                           0.561 (oil)*
                           0.611 (coal)*
                                17.9
                          20.9 - %
                                      dry
  *These approximate factors used only when data were otherwise insufficient,
Reference:
Maloney, K. L., et al., "Low-Sulfur Western Coal Use in Existing Small and
Intermediate-Si zed" EoTlers," EPA-600/7-78-153a, July 1978.
                                     F-l

-------
                                 APPENDIX G
                           LIST OF ABBREVIATIONS

AH         Air heater
BBF        Biased burner firing
BOOS       Burners out of service
DMEG       Discharge multimedia environmental goals
DS         Discharge severity
EA         Environmental assessment
FD         Forced draft
F6R        Flue gas recirculation
F6T        Flue gas treatment
HC         Hydrocarbon
ID         Induced draft
LEA        Low excess air
LNB        Low NO  burner
                 n
MCR        Maximum continuous  rating
MEG        Multimedia environmental goal
NO         Nitrogen oxides
   A
NSPS       New Source Performance Standard
OFA        Overfire  air
OSC        Off stoichiometric  combustion
PAH  (PNA)  Polynuclear  aromatic hydrocarbon (same as POM below)
POM        Polycyclic organic  matter
RAP        Reduced  (combustion) air preheat
RH        Reheater
SAM         Source  analysis  model
SCR         Selective catalytic reduction
SH         Superheater
                                     G-l

-------
TWOS       Total weighted discharge severity
UHC        Unburned hydrocarbon
WDS        Weighted discharge severity
WI         Water injection
                                    G-2

-------
TECHNICAL REPORT DATA
(Pletue nod Imitruc lions on the revtnt before completing}
"REPORT NO.
EPA-600/7-80-075b
2.
4. TITUE AND SUBTITLE
Environmental Assessment of Utility Boiler
Combustion Modification NOx Controls:
Volume 2. Aooendices
K^lTim , L. R . Water land ,
and E. B. Higginbotham
C.Castaldini, Z.Chiba,
^-PERFORMING ORGANIZATION NAME AND ADDRESS
Acurex/Energy and Environmental Division
485 Clyde Avenue
Mountain View, California
94042
pnTsPONSORtNG AGENCY NAME AND ADDRESS
EPA Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
3. RECIPIENT'S ACCESSION-NO.

B. REPORT DATE
April 1980
B. PERFORMING ORGANIZATION
B. PERFORMING ORGANIZATION
TR-78-105
CODE
REPORT NO.
10. PROGRAM ELEMENT NO.
EHE624A
11. CONTRACT/GRANT NO.
68-02.2160
13. TYPE OF REPORT AND PERIOD COVERED
Final: 3/77-5/78
14. SPONSORING AGENCY CODE
EPA/600/13
IB. SUPPLEMENTARY NOTES IERL_RTp project officer is Joshua S. Bowen, Mail Drop
65, 919/
541-2470.
         The report gives results of an evaluation of combustion modification tech-
niques for coal-, oil-, and gas-fired utility boilers, with respect to NOx control re-
duction effectiveness, operational impact, thermal efficiency impact, capital and
annualized operating costs, and effect on emissions of pollutants other than NOx.
For gas- and oil-fired boilers,  30 to 60% NOx reductions are achievable with the
combined use of staged combustion, flue gas recirculation, and low excess air at an
annualized cost of #0. 50 to #3. OOAW-yr. For retrofit control of existing coal-fired
boilers, low NOx burners and/or staged combustion yields a 30 to  60% NOx reduction
at an annualized cost of $0.40 to $1.20AW-yr. For new sources, modified furnace
design with low NOx burners and/or overfire air can achieve emission levels of 260
to 170 ng/J  (40 to 60% reduction).  Detailed emission tests on a 200 MW coal-fired
boiler showed that changes in trace specie emissions due to combustion modifications
were small compared to the benefit of reduced NOx emissions.
17.
                            KEY WORDS AND DOCUMENT ANALYSIS
                DESCRIPTORS
                    b.IDENTIFIERS/OPEN ENDED TERMS
                                                                    COSATI Field/Group
Air Pollution
Assessments
Combustion Control
Nitrogen Oxides
Boilers
Utilities
Cost Effectiveness
Fossil Fuels
Dust
Aerosols
Trace Elements
Organic Compounds
Air Pollution Control
Stationary Sources
Utility Boilers
Combustion Modification
Particulate
Environmental Assess-
  ment
13B
14B
21B
07B
13A
14A
21D
11G
07D
06A
07C
 j DISTRIBUTION STATEMENT

 Release to Public
 9. SECURITY CLASS (OtisRtport)
 Unclassified
20. SECURITY CLASS (TM*
 Unclassified
                                            21. NO. OF PAGERS
                                                208
                                            22. PRICE
KFA Form 2220-1 (t-73)
                                        6-3

-------