-------
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
-------
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
-------
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
-------
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
-------
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
-------
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
-------
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
-------
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
-------
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
-------
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
-------
A-8
Babcock&Wilcox
-------
A-9
Babcock&Wilcox
-------
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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
-------
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
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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 - ..... ,_
r — x^™'
^ "^
[___ g QT — : •
....
...'.-....
- . - -
•. - . ........
i
..-;..;.:.
6
: ®_^-© 2 :
7 vi/ ft)
.-. -;-•.--:.:-.- : :: •- : ::~-; -
\ . .... , . ,
:': -. :
40 30 20 10 0
% EXCESS AIR
; .
..
PPM
_ : : .
.:-; r:: -.
-
—
1*>0
1 -J V.
-
-
-
-100
:
en
- bu
i n
- IU
0
: ;: i:-,- - .; .. :. . ; ; -~ :. .
CO,
." ": '-••"-: ' : : : :.: :
"• -.: — • • r : r
--.: : ' : " : .:" _:[." : : -
-: :-_..:-.-- L - ; --.L -' .: :-
: r ~ --- - " r;_.--rr:_- . : .— ^:. : .; -- :
• — -._- -.-
_-_____-_.:_ i .:: — ^'^LI,
"1*iO
• «**
4©
®3 ;
1©
..... . .
8© 100 -]
i ......
.;• • .: ..:_;.
— • . ....
:
— 50
2®
>2/ 7
.:.-.:. :....:_•-:-;:..•. : .
- ..... ._
IU
50 75 100
% MCR
•
' '. ~ ' ' '.
PPM
L_ r . ; :: - - .
. .....
- ; ...
.: .;..__ _.""'.
• - - -— - — - --
<^»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_
- i
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-NSPS UNITS: NOX REDUCTIC
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FIGURES IN PARENTHESES: IDLE BURNER
STAGED FIRING SIMULATED BY TAKING T
ROW OUT OF SERVICE.
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\^r~~^7~\ 'TYPICAL FOR SINGLE!
H '/I ' WALL BOILERS; MIGHT"
^*0| \TURBULENTBURNER.]
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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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1-9
-------
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
-------
.
0
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BOILERS WITH HIGH }
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INTERVANE BUR!
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IRBULENT BURNERS. ij
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FIGURE 4 -10
i
: f
•
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
-------